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{{#Wiki_filter:Oconee Nuclear Station UFSAR Appendix 6A. Tables Appendix 6A. Tables
{{#Wiki_filter:Oconee Nuclear Station UFSAR Appendix 6A. Tables Appendix 6A. Tables  


Oconee Nuclear Station             UFSAR Table 6-1 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-1 (Page 1 of 1)
Table 6-1. Deleted per 1995 Update (31 DEC 2000)
(31 DEC 2000)
Table 6-1. Deleted per 1995 Update  


Oconee Nuclear Station             UFSAR Table 6-2 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-2 (Page 1 of 1)
Table 6-2. Deleted per 2000 Update (31 DEC 2000)
(31 DEC 2000)
Table 6-2. Deleted per 2000 Update  


Oconee Nuclear Station                                                         UFSAR Table 6-3 (Page 1 of 2)
Oconee Nuclear Station UFSAR Table 6-3 (Page 1 of 2)
Table 6-3. Quality Control Standards for Engineered Safeguards Systems Summary of Requirements for Core Flooding Tanks CLASSIFICATION:           ASME III, Class C, Paragraph N-2113 and the requirements of ASME VIII, Paragraph UW-2(a) (lethal substances)
(31 DEC 2000)
Inspection Requirements                                                   Acceptance Standard
Table 6-3. Quality Control Standards for Engineered Safeguards Systems Summary of Requirements for Core Flooding Tanks CLASSIFICATION:
: 1. Inspection of raw materials and review of certificates                 ASME III material
ASME III, Class C, Paragraph N-2113 and the requirements of ASME VIII, Paragraph UW-2(a) (lethal substances)
: 2. Hydro test                                                             ASME III
Inspection Requirements Acceptance Standard
: 3. Radiograph                                                             ASME VIII Summary of Requirements for Low Pressure Injection Heat Exchanger CLASSIFICATGION: Shell ASME VIII, Tube ASME III, Class C (lethal)
: 1. Inspection of raw materials and review of certificates ASME III material
Inspection Requirements                                                   Acceptance Standard
: 2. Hydro test ASME III
: 1. Inspection of raw materials and review of material certificates       ASME II, III, VIII
: 3. Radiograph ASME VIII Summary of Requirements for Low Pressure Injection Heat Exchanger CLASSIFICATGION: Shell ASME VIII, Tube ASME III, Class C (lethal)
: 2. Seal weld on tubes-to-tube sheet                                       TEMA-R-7 and additional requirements
Inspection Requirements Acceptance Standard
: 3. Liquid penetrant inspection on tube-to-tube sheet                     ASME III, N-627 and additional requirements
: 1. Inspection of raw materials and review of material certificates ASME II, III, VIII
: 4. Hydro test                                                             ASME III, VIII, TEMA-R
: 2. Seal weld on tubes-to-tube sheet TEMA-R-7 and additional requirements
: 3. Liquid penetrant inspection on tube-to-tube sheet ASME III, N-627 and additional requirements
: 4. Hydro test ASME III, VIII, TEMA-R
: 5. Leak test and seal weld (air)
: 5. Leak test and seal weld (air)
Summary of Requirements for Valves Inspection Requirements                                                   Acceptance Standard Class I and II Valves
Summary of Requirements for Valves Inspection Requirements Acceptance Standard Class I and II Valves
: 1. Radiographic inspection of the body casing                             USAS B31.7
: 1. Radiographic inspection of the body casing USAS B31.7
: 2. Inspection of material and review of material                         USAS B31.7 certificates
: 2. Inspection of material and review of material USAS B31.7 certificates
: 3. Liquids penetrant inspection of the valve body                         USAS B31.7
: 3. Liquids penetrant inspection of the valve body USAS B31.7
: 4. Hydro test of valve assembly                                           USAS B16.5 and additional requirements
: 4. Hydro test of valve assembly USAS B16.5 and additional requirements
: 5. Seat Leakage test                                                     MSS-SP-61 and additional requirements Class III Valves
: 5. Seat Leakage test MSS-SP-61 and additional requirements Class III Valves
: 1. Inspection of material and review of material                         USAS B31.7 certificates
: 1. Inspection of material and review of material USAS B31.7 certificates
: 2. Hydro test of valve assembly                                           USAS B16.5
: 2. Hydro test of valve assembly USAS B16.5
: 3. Seat leakage test                                                     MSS-SP-61 and additional requirements In addition to these inspections listed above, all valve materials must meet the ASTM material specification.
: 3. Seat leakage test MSS-SP-61 and additional requirements In addition to these inspections listed above, all valve materials must meet the ASTM material specification.
Summary of Requirements for Engineered Safeguards Systems Pumps (31 DEC 2000)
Summary of Requirements for Engineered Safeguards Systems Pumps  


Oconee Nuclear Station                                                       UFSAR Table 6-3 (Page 2 of 2)
Oconee Nuclear Station UFSAR Table 6-3 (Page 2 of 2)
Inspection Requirements                                                 Acceptance Standard
(31 DEC 2000)
: 1. Inspection of materials and review of material                       ASTM certificates
Inspection Requirements Acceptance Standard
: 2. Liquid-penetrant inspection of castings                               ASME VIII
: 1. Inspection of materials and review of material ASTM certificates
: 3. Performance test                                                     Hydraulic Institute Standard Additional requirements:
: 2. Liquid-penetrant inspection of castings ASME VIII
: 3. Performance test Hydraulic Institute Standard Additional requirements:
Low Pressure Injection Pumps
Low Pressure Injection Pumps
: 1. Hydrotest casing to 600 psig. Test pressure is held for 30 minutes per inch of thickness with a minimum holding time of 30 minutes. This exceeds the hydrotest requirements of ASME VIII Paragraph UG-99 (> 1.5 x design pressure).
: 1. Hydrotest casing to 600 psig. Test pressure is held for 30 minutes per inch of thickness with a minimum holding time of 30 minutes. This exceeds the hydrotest requirements of ASME VIII Paragraph UG-99 (> 1.5 x design pressure).
Line 63: Line 68:
: 1. Documented quality control records and certified caliper measurements of the entire casting thickness will be furnished.
: 1. Documented quality control records and certified caliper measurements of the entire casting thickness will be furnished.
: 2. Witness performance test will be performed. Acceptance standards are per Hydraulic Institute Standard.
: 2. Witness performance test will be performed. Acceptance standards are per Hydraulic Institute Standard.
: 3. A documented, non-witness, hydro-test will be performed. Acceptance standards are per ASME code.
: 3. A documented, non-witness, hydro-test will be performed. Acceptance standards are per ASME code.  
(31 DEC 2000)


Oconee Nuclear Station                                                     UFSAR Table 6-4 (Page 1 of 2)
Oconee Nuclear Station UFSAR Table 6-4 (Page 1 of 2)
Table 6-4. Engineered Safeguards Piping Design Conditions Temp (F)     Press. (psig)
(31 DEC 2016)
: 1. High Pressure Injection System
Table 6-4. Engineered Safeguards Piping Design Conditions Temp (F)
: a. From the pump discharge to upstream of the check valves           200/150       3,040/3120 inside the secondary shielding.
Press. (psig)
: b. High pressure injection pump.                                     200/150       3,040/3,120
: 1.
: c. From upstream of the check valves to the reactor inlet line.     650           2,500
High Pressure Injection System
: 2. Low Pressure Injection System
: a.
: a. From the borated water storage tank to upstream of the           150          Static borated water storage tank outlet valves.
From the pump discharge to upstream of the check valves inside the secondary shielding.
: b. From upstream of the borated water storage tank outlet valve     200          100 to upstream of the electric motor operated valves in the borated water feed lines. (Unit 2 only, is to the check valves in the borated water feed lines)
200/150 3,040/3120
: c. From upstream of the electric motor operated valves in the       300          200 borated water feed lines to upstream of the valves at the pump inlets. (Unit 2 only, is from the check valves in the borated water feed lines)
: b.
: d.       From upstream of the system inlet valves at the pump inlets to the pump inlet.
High pressure injection pump.
Trains 1A, 1C, 2A, 2C                                         300/250       470/505 Trains 1B, 2B                                               300           370
200/150 3,040/3,120
: e. From the pump outlet to upstream of the throttle valves at the cooler discharge.
: c.
Trains 1A, 1C, 2A, 2C 1                                       300/250       470/515 Trains 1B, 2B                                                 300           370
From upstream of the check valves to the reactor inlet line.
: f. From upstream of the throttle valves at the cooler discharge to upstream of the LPI Header isolation valves.
650 2,500
Trains 1A, 2A                                                 300/250       470/515 Trains 1B, 2B                                                 300           470/505
: 2.
: g. From upstream of the system inlet valves to upstream of the       300          2,500 check valves in the core flooding lines.
Low Pressure Injection System
: h. From upstream of the check valves in the core flooding lines     650          2,500 to the reactor vessel.
: a.
: i. From the Reactor Building emergency sump to upstream of           300          59 the valves in the recirculation lines.
From the borated water storage tank to upstream of the borated water storage tank outlet valves.
: 3. Reactor Building Spray System (31 DEC 2016)
150 Static
: b.
From upstream of the borated water storage tank outlet valve to upstream of the electric motor operated valves in the borated water feed lines. (Unit 2 only, is to the check valves in the borated water feed lines) 200 100
: c.
From upstream of the electric motor operated valves in the borated water feed lines to upstream of the valves at the pump inlets. (Unit 2 only, is from the check valves in the borated water feed lines) 300 200
: d.
From upstream of the system inlet valves at the pump inlets to the pump inlet.
Trains 1A, 1C, 2A, 2C 300/250 470/505 Trains 1B, 2B 300 370
: e.
From the pump outlet to upstream of the throttle valves at the cooler discharge.
Trains 1A, 1C, 2A, 2C 1 300/250 470/515 Trains 1B, 2B 300 370
: f.
From upstream of the throttle valves at the cooler discharge to upstream of the LPI Header isolation valves.
Trains 1A, 2A 300/250 470/515 Trains 1B, 2B 300 470/505
: g.
From upstream of the system inlet valves to upstream of the check valves in the core flooding lines.
300 2,500
: h.
From upstream of the check valves in the core flooding lines to the reactor vessel.
650 2,500
: i.
From the Reactor Building emergency sump to upstream of the valves in the recirculation lines.
300 59
: 3.
Reactor Building Spray System  


Oconee Nuclear Station                                                       UFSAR Table 6-4 (Page 2 of 2)
Oconee Nuclear Station UFSAR Table 6-4 (Page 2 of 2)
Temp (F)           Press. (psig)
(31 DEC 2016)
: a. From downstream of the pump inlet valves to downstream of       250                495 the Reactor Building valves.
Temp (F)
: b. From downstream of the inlet valves through the nozzles2.       250/286             200
Press. (psig)
: 4. Low Pressure Service Water System
: a.
: a. Condenser circulating water crossover to low pressure service   100                50 water pump suction.
From downstream of the pump inlet valves to downstream of the Reactor Building valves.
: b. Pump discharge                                                   100                 100 (OCONEE 3 ONLY)
250 495
: 1. Low Pressure Injection System
: b.
: a. From the borated water storage tank to upstream of the           150                Static borated water storage tank outlet valves.
From downstream of the inlet valves through the nozzles2.
: b. From upstream of the borated water storage tank outlet valve     200                100 to upstream of the check valves in the borated water feed lines.
250/286 200
: c. From upstream of the check valves to upstream of the motor       300                300 operated valves in the borated water feed lines.
: 4.
: d. From upstream of the electric motor operated valves in the       300                388 borated water feed lines to upstream of the valves at the pump inlets.
Low Pressure Service Water System
: e. From upstream of the system inlet valves at the pump inlets to   300/250            470/505 upstream of the LPI Header Isolation valves.
: a.
: f. From upstream of the system inlet valves to upstream of the     300                2,500 check valves in the core flooding lines.
Condenser circulating water crossover to low pressure service water pump suction.
: g. From upstream of the check valves in the core flooding lines     650                2,500 to the reactor vessel.
100 50
: h. From the Reactor Building emergency sump to upstream of         300                59 the valves in the recirculation lines.
: b.
Note:
Pump discharge 100 100 (OCONEE 3 ONLY)
: 1.
Low Pressure Injection System
: a.
From the borated water storage tank to upstream of the borated water storage tank outlet valves.
150 Static
: b.
From upstream of the borated water storage tank outlet valve to upstream of the check valves in the borated water feed lines.
200 100
: c.
From upstream of the check valves to upstream of the motor operated valves in the borated water feed lines.
300 300
: d.
From upstream of the electric motor operated valves in the borated water feed lines to upstream of the valves at the pump inlets.
300 388
: e.
From upstream of the system inlet valves at the pump inlets to upstream of the LPI Header Isolation valves.
300/250 470/505
: f.
From upstream of the system inlet valves to upstream of the check valves in the core flooding lines.
300 2,500
: g.
From upstream of the check valves in the core flooding lines to the reactor vessel.
650 2,500
: h.
From the Reactor Building emergency sump to upstream of the valves in the recirculation lines.
300 59 Note:
: 1. For the C Train Connection to the B Train Cooler, design conditions are 300°F and 370 psig beginning downstream of the cross over valve.
: 1. For the C Train Connection to the B Train Cooler, design conditions are 300°F and 370 psig beginning downstream of the cross over valve.
: 2. A 286 F design temperature is applicable due to the Post-LOCA and Post-MSLB environmental temperature inside containment. All other plant conditions that require integrity of this pipe are enveloped by the 250 F design temperature.
: 2. A 286 F design temperature is applicable due to the Post-LOCA and Post-MSLB environmental temperature inside containment. All other plant conditions that require integrity of this pipe are enveloped by the 250 F design temperature.  
(31 DEC 2016)


Oconee Nuclear Station                                                   UFSAR Table 6-5 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-5 (Page 1 of 1)
Table 6-5. Single Failure Analysis Reactor Building Spray System Component                  Malfunction            Comments
: 1. Reactor Building the Fails to start.          Since each of the two strings of Reactor Building spray pump.                                    Spray System is equally sized, the remaining string will provide heat removal capability at a reduced rate. In combination with the Reactor Building Cooling System, heat removal capability in excess of the requirements will be provided.
: 2. Building isolation    Fails to open.          (Same as above.)
valve.
: 3. Check valve in        Fails to open.          (Same as above.)
suction or discharge line.
(31 DEC 2000)
(31 DEC 2000)
Table 6-5. Single Failure Analysis Reactor Building Spray System Component Malfunction Comments
: 1.
Reactor Building the spray pump.
Fails to start.
Since each of the two strings of Reactor Building Spray System is equally sized, the remaining string will provide heat removal capability at a reduced rate. In combination with the Reactor Building Cooling System, heat removal capability in excess of the requirements will be provided.
: 2.
Building isolation valve.
Fails to open.
(Same as above.)
: 3.
Check valve in suction or discharge line.
Fails to open.
(Same as above.)


Oconee Nuclear Station                                                     UFSAR Table 6-6 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-6 (Page 1 of 1)
Table 6-6. Single Failure Analysis For Reactor Building Cooling System Component                  Malfunction            Comments
: 1. Circulating fan        Fails to operate.      The cooling capacity of the cooling units is reduced; however, 2 of 3 cooling units provide the required cooling.
: 2. Cooler service water Fails to open fully      Valve will normally be partially open. If the outlet valve.                                  valve fails to open fully, the unit will operate (LPSW-18, -21, -24)                            under reduced heat removal capability. The required cooling load will be met by 2 of 3 cooling units.
: 3. Cooler service water  Inadvertently left      The flow through this string will be unavailable inlet valve. (LPSW-    closed.                for cooling. It is unlikely that this condition 16, -19, -22)                                  would occur during an accident since the position and flow are monitored during normal operation. The required cooling load will be met by 2 of 3 cooling units.
: 4. Service water pump    Fails to operate.      The two remaining pumps will provide full low (1A, 1B, 1C).                                  pressure service water flow to all components.
: 5. Service water pump    Fails to operate.      The one remaining pump will provide full low (3A, 3B).                                      pressure service water flow to all components.
(31 DEC 2000)
(31 DEC 2000)
Table 6-6. Single Failure Analysis For Reactor Building Cooling System Component Malfunction Comments
: 1.
Circulating fan Fails to operate.
The cooling capacity of the cooling units is reduced; however, 2 of 3 cooling units provide the required cooling.
: 2.
Cooler service water outlet valve.
(LPSW-18, -21, -24)
Fails to open fully Valve will normally be partially open. If the valve fails to open fully, the unit will operate under reduced heat removal capability. The required cooling load will be met by 2 of 3 cooling units.
: 3.
Cooler service water inlet valve. (LPSW-16, -19, -22)
Inadvertently left closed.
The flow through this string will be unavailable for cooling. It is unlikely that this condition would occur during an accident since the position and flow are monitored during normal operation. The required cooling load will be met by 2 of 3 cooling units.
: 4.
Service water pump (1A, 1B, 1C).
Fails to operate.
The two remaining pumps will provide full low pressure service water flow to all components.
: 5.
Service water pump (3A, 3B).
Fails to operate.
The one remaining pump will provide full low pressure service water flow to all components.


Oconee Nuclear Station                                                                                                           UFSAR Table 6-7 (Page 1 of 7)
Oconee Nuclear Station UFSAR Table 6-7 (Page 1 of 7)
Table 6-7. Reactor Building Penetration Valve Information Inside Penetration Valve Data                                           Outside Penetration Valve Data Valve Position                                                             Valve Position Vlv                                                            Post Indi-                                                               Post    Indi-Pen    Description      Arrg Qty Size     Type Oper     Signal   Norm     Fail     Acc cation Qty  Size        Type    Oper    Signal    Norm     Fail   Acc     cation 1(16)   Pressurizer       1   2   3/4         SH   EMO     ES       OP       AI       CL   YES   1     1/2         SH     AIR     ES         OP     CL       CL     YES Sample 2       OTSG A           8                                                                         1     1/2         SH     AIR     ES         CL     CL       CL     YES Closed Loop Inside Containment Sample 3       Component         3   1   6         CK   -        -        OP       -        CL   NO     1     6           CK     -        -          OP     -        CL     NO Cooling Inlet 4       OTSG B Drain     7                       Closed Loop Inside Containment                   1     4           SH     EMO     ES         OP     AI       CL     YES RB Normal                                                                                   5       1       SH     MAN         -        CL       -      CL     NO 5A                        24                                    None Sump Drain                                                                                  1       2       SH     EMO         ES       OP       AI     CL     YES 1       2       SH     AIR         ES       OP       CL     CL     YES (5)                       (5)                         (5)     (15) 5B      Post Accident    13                                    None                                2    1          SH    SOL        -          CL      CL      CL    YES(5)
(31 DEC 2014)
Liquid Sample 6       RC Letdown       1   2   2           SH   EMO     ES       OP       AI       CL   YES   1     2         SH     AIR       ES         OP     CL       CL     YES (7)                                                                                                                    (1) 7      RC Pump Seal     4   1   3,4         SH   EMO     ES       OP       AI       CL   YES   1     2         SH     AIR       ES         OP     OP       CL     YES Return 8A     Pressurizer       3   1   1,11/2(11) CK   -        -        OP       -        CL   NO     1     1,11/2(11) CK     -          -          OP     -        CL     NO Aux Spray 8B     Loop A Nozzle     3   1   1,11/2(11) CK   -        -        OP       -        CL   NO     1     1,11/2(11) CK     -          -          OP     -        CL     NO Warming 9       HP     Injection 2   1   4           CK   -        -        OP       -        OP   NO None Loop A 10A     RC Pump Seal     3   1   1           CK   -        -        OP       -        CL   NO     1     1,11/2(6)   CK   -          -          OP     -        CL     NO Injection 10B     RC Pump Seal     3   1   1           CK   -        -        OP       -        CL   NO     1     1           CK   -          -          OP     -        CL     NO Injection (31 DEC 2014)
Table 6-7. Reactor Building Penetration Valve Information Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc 1(16)
Pressurizer Sample 1
2 3/4 SH EMO ES OP AI CL YES 1
1/2 SH AIR ES OP CL CL YES 2
OTSG A Sample 8
Closed Loop Inside Containment 1
1/2 SH AIR ES CL CL CL YES 3
Component Cooling Inlet 3
1 6
CK OP CL NO 1
6 CK OP CL NO 4
OTSG B Drain 7
Closed Loop Inside Containment 1
4 SH EMO ES OP AI CL YES 5A RB Normal Sump Drain 24 None 5
1 SH MAN CL CL NO 1
2 SH EMO ES OP AI CL YES 1
2 SH AIR ES OP CL CL YES 5B Post Accident Liquid Sample 13 None 2(5) 1 SH SOL(5)
CL CL(5)
CL(15)
YES(5) 6 RC Letdown 1
2 2
SH EMO ES OP AI CL YES 1
2 SH AIR ES OP CL CL YES 7
RC Pump Seal Return 4
1 3,4(7)
SH EMO ES OP AI CL YES 1
2 SH AIR ES OP OP(1)
CL YES 8A Pressurizer Aux Spray 3
1 1,11/2(11)
CK OP CL NO 1
1,11/2(11)
CK OP CL NO 8B Loop A Nozzle Warming 3
1 1,11/2(11)
CK OP CL NO 1
1,11/2(11)
CK OP CL NO 9
HP Injection Loop A 2
1 4
CK OP OP NO None 10A RC Pump Seal Injection 3
1 1
CK OP CL NO 1
1,11/2(6)
CK OP CL NO 10B RC Pump Seal Injection 3
1 1
CK OP CL NO 1
1 CK OP CL NO  


Oconee Nuclear Station                                                                                                 UFSAR Table 6-7 (Page 2 of 7)
Oconee Nuclear Station UFSAR Table 6-7 (Page 2 of 7)
Inside Penetration Valve Data                                         Outside Penetration Valve Data Valve Position                                                         Valve Position Vlv                                                        Post Indi-                                                           Post  Indi-Pen    Description    Arrg Qty Size Type Oper     Signal     Norm     Fail     Acc cation Qty Size        Type    Oper    Signal    Norm     Fail   Acc   cation 11     Fuel Transfer Tube                                   Special Closure (Flange) 19                                                                                                    None 1   3   SH   EMO       -        CL     AL       CL   YES 1   4   SH   EMO       -        CL     AL       CL   YES 12     Fuel Transfer Tube                                   Special Closure (Flange) 18  1   3   SH   EMO       -        CL     AL       CL   YES                                   None 1   11/2 SH   EMO       -        CL     AL       CL   YES 2   1   SH   EMO       -        CL     AL       CL   YES 13     RB Spray Inlet 2   1   8   CK   -          -        CL     -        OP   NO                                     None 14     RB Spray Inlet 2   1   8   CK   -        -          CL     -        OP   NO                                     None 15     LPI Inlet     2   1   10   CK   -          -        CL     -        OP   NO                                     None 16     LPI Inlet     2   1   10   CK   -          -        CL     -        OP   NO                                     None 17     OTSG B EFW 5                   Closed Loop Inside Containment                                                     None Injection 18     Quench   Tank 4   1   2   SH   EMO       ES       OP     AI       CL   YES   1   2           SH   AIR       ES       OP     CL       CL   YES Vent 19     RB Purge Inlet 4   1   48   SH   EMO       ES       CL     AI       CL   YES   1   48         SH   AIR       ES       CL     CL       CL   YES 20     RB Purge       4   1   48   SH   EMO       ES       CL     AI       CL   YES   1   48         SH   AIR       ES       CL     CL       CL   YES Outlet 21     LPSW to RCP 7                   Closed Loop Inside Containment                     1   10         SH   EMO       ES       OP     AI       CL   YES Coolers 22     LPSW from     7 Closed Loop Inside Containment                     1   10         SH   EMO       ES       OP     AI       CL   YES RCP Coolers 23A     RC Pump Seal   3   1   1   CK   -          -        OP     -        CL   NO     1   1           CK   -          -        OP     -        CL   NO Injection 23B     RC Pump Seal   3   1   1   CK   -          -        OP     -        CL   NO     1   1           CK   -          -        OP     -        CL   NO Injection 24A     RB Hydrogen   10                                                                     1   1/2,3/8(12) SH   SOL       -        CL     CL       CL(2) YES None Analyzer (31 DEC 2014)
(31 DEC 2014)
Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc 11 Fuel Transfer Tube 19 Special Closure (Flange)
None 1
3 SH EMO CL AL CL YES 1
4 SH EMO CL AL CL YES 12 Fuel Transfer Tube 18 Special Closure (Flange)
None 1
3 SH EMO CL AL CL YES 1
11/2 SH EMO CL AL CL YES 2
1 SH EMO CL AL CL YES 13 RB Spray Inlet 2
1 8
CK CL OP NO None 14 RB Spray Inlet 2
1 8
CK CL OP NO None 15 LPI Inlet 2
1 10 CK CL OP NO None 16 LPI Inlet 2
1 10 CK CL OP NO None 17 OTSG B EFW Injection 5
Closed Loop Inside Containment None 18 Quench Tank Vent 4
1 2
SH EMO ES OP AI CL YES 1
2 SH AIR ES OP CL CL YES 19 RB Purge Inlet 4
1 48 SH EMO ES CL AI CL YES 1
48 SH AIR ES CL CL CL YES 20 RB Purge Outlet 4
1 48 SH EMO ES CL AI CL YES 1
48 SH AIR ES CL CL CL YES 21 LPSW to RCP Coolers 7
Closed Loop Inside Containment 1
10 SH EMO ES OP AI CL YES 22 LPSW from RCP Coolers 7
Closed Loop Inside Containment 1
10 SH EMO ES OP AI CL YES 23A RC Pump Seal Injection 3
1 1
CK OP CL NO 1
1 CK OP CL NO 23B RC Pump Seal Injection 3
1 1
CK OP CL NO 1
1 CK OP CL NO 24A RB Hydrogen Analyzer 10 None 1
1/2,3/8(12)
SH SOL CL CL CL(2)
YES  


Oconee Nuclear Station                                                                                               UFSAR Table 6-7 (Page 3 of 7)
Oconee Nuclear Station UFSAR Table 6-7 (Page 3 of 7)
Inside Penetration Valve Data                                       Outside Penetration Valve Data Valve Position                                                         Valve Position Vlv                                                      Post Indi-                                                           Post  Indi-Pen    Description    Arrg Qty Size Type Oper     Signal   Norm     Fail     Acc cation Qty Size        Type    Oper    Signal    Norm     Fail   Acc   cation 24B     RB Hydrogen   10                                                                   1   1/2,3/8(12) SH   SOL       -        CL     CL       CL(2) YES None Analyzer 25     OTSG B 6                   Closed Loop Inside Containment                   1   24         CK   -          -        OP     -        CL   NO Feedwater Line 26     OTSG A Main   5 Closed Loop Inside Containment                                                   None Stream Line 27     OTSG A         6 Closed Loop Inside Containment                   1   24         CK   -          -        OP     -        CL   NO Feedwater Line 28(20) OTSG B Main   5 Closed Loop Inside Containment                                                   None Steam Line 29     Quench Tank   4   1   4   SH   EMO       ES       OP     AI       CL   YES   1   2           SH   AIR       ES       OP     CL       CL   YES Drain 30     LPSW to 5                   Closed Loop Inside Containment                                                   None RBCU 31     LPSW to       5 Closed Loop Inside Containment                                                   None RBCU 32     LPSW to       5 Closed Loop Inside Containment                                                   None RBCU 33     LPSW from     5 Closed Loop Inside Containment                                                   None RBCU 34     LPSW from     5 Closed Loop Inside Containment                                                   None RBCU 35     LPSW from     5 Closed Loop Inside Containment                                                   None RBCU RB Emergency 36                    12                               None                                 1   14         SH   EMO       -        CL     AI       OP   YES Sump Recirc 1   14         SH   EMO         -        CL     AI     OP     YES RB Emergency 37                    15                              None Sump Recirc                                                                          1   1           SH   MAN         -        CL     -      OP     NO (9) 38     Quench Tank   3   1   11/2 CK   -        -        OP     -        CL   NO     1   11/2,2     CK   -          -        OP     -        CL   NO Cooler Inlet 39a(17) Core Flood     16   1   1   SH   MAN       -        CL     -        CL   NO     2   1           SH   MAN       -        CL     -        CL   NO (31 DEC 2014)
(31 DEC 2014)
Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc 24B RB Hydrogen Analyzer 10 None 1
1/2,3/8(12)
SH SOL CL CL CL(2)
YES 25 OTSG B Feedwater Line 6
Closed Loop Inside Containment 1
24 CK OP CL NO 26 OTSG A Main Stream Line 5
Closed Loop Inside Containment None 27 OTSG A Feedwater Line 6
Closed Loop Inside Containment 1
24 CK OP CL NO 28(20)
OTSG B Main Steam Line 5
Closed Loop Inside Containment None 29 Quench Tank Drain 4
1 4
SH EMO ES OP AI CL YES 1
2 SH AIR ES OP CL CL YES 30 LPSW to RBCU 5
Closed Loop Inside Containment None 31 LPSW to RBCU 5
Closed Loop Inside Containment None 32 LPSW to RBCU 5
Closed Loop Inside Containment None 33 LPSW from RBCU 5
Closed Loop Inside Containment None 34 LPSW from RBCU 5
Closed Loop Inside Containment None 35 LPSW from RBCU 5
Closed Loop Inside Containment None 36 RB Emergency Sump Recirc 12 None 1
14 SH EMO CL AI OP YES 37 RB Emergency Sump Recirc 15 None 1
14 SH EMO CL AI OP YES 1
1 SH MAN CL OP NO 38 Quench Tank Cooler Inlet 3
1 11/2 CK OP CL NO 1
11/2,2(9)
CK OP CL NO 39a(17)
Core Flood 16 1
1 SH MAN CL CL NO 2
1 SH MAN CL CL NO  


Oconee Nuclear Station                                                                                                   UFSAR Table 6-7 (Page 4 of 7)
Oconee Nuclear Station UFSAR Table 6-7 (Page 4 of 7)
Inside Penetration Valve Data                                         Outside Penetration Valve Data Valve Position                                                         Valve Position Vlv                                                        Post Indi-                                                             Post  Indi-Pen    Description    Arrg Qty Size Type Oper     Signal     Norm     Fail     Acc cation Qty Size        Type    Oper    Signal  Norm     Fail Acc   cation Tank Vent 39b     HP Nitrogen   20   1   1   CK   -          -        CL     -        CL   NO     1   1/2         SH   MAN         -        CL       -      CL     NO Supply 1   1           CK   -          -        CL       -      CL     NO 1   1           SH   MAN         -        CL       -      CL     NO 40     RB Emergency   14                                                                     1   2           SH   MAN         -        CL       -      CL   NO Sump Drain None                                2   2           CK   -          -        CL       -      OP   NO 2   3/4         SH   MAN         -        CL       -      CL   NO 41     Instrument Air 9   1   3   SH   MAN       -        CL     -        CL   NO     1   3           SH   MAN         -        CL       -      CL   NO Supply 42A     RB Hydrogen   10                               None                                 1   1/2,3/8(12) SH   SOL         -        CL     CL       CL(2) YES Analyzer 42B     RB Hydrogen   10                                                                     1   1/2,3/8(12) SH   SOL         -        CL     CL       CL(2) YES None Analyzer 43     OTSG A Drain   7                   Closed Loop Inside Containment                     1   4           SH   EMO         ES       OP     AI       CL   YES 44     Component     3   1   21/2 CK   -          -        OP     -        CL   NO     1   21/2         CK   -          -        OP     -        CL   NO Cooling to CRD 45A     Leak Rate Test 9   1   1/2 SH   MAN       -        CL     -        CL   NO     1   1/2         SH   MAN         -        CK     -        CL   NO Line 45B     Leak Rate Test 9   1   1/2 SH   MAN       -        CL     -        CL   NO     1   1/2         SH   MAN         -        CL     -        CL   NO Line 45C(17) Leak Rate Test 9   1   1/2 SH   MAN       -        CL     -        CL   NO     1   1/2         SH   MAN         -        CL     -        CL   NO Line 48     Breathing Air 9   1   2   SH   MAN       -        CL     -        CL   NO     1   2           SH   MAN         -        CL     -        CL   NO Supply to RB 49(16) LP Nitrogen   22   1   11/2 CK   -          -        CL     -        CL   NO     2   1           SH   MAN         -        CL     -        CL   NO Supply to RB 50     OTSG A EFW     5 Closed Loop Inside Containment                                                     None Injection 51     LRT Supply     11                     Special Closure (Flange)                       1     8         SH     AIR     -        CL       AI       CL     NO (31 DEC 2014)
(31 DEC 2014)
Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc Tank Vent 39b HP Nitrogen Supply 20 1
1 CK CL CL NO 1
1/2 SH MAN CL CL NO 1
1 CK CL CL NO 1
1 SH MAN CL CL NO 40 RB Emergency Sump Drain 14 None 1
2 SH MAN CL CL NO 2
2 CK CL OP NO 2
3/4 SH MAN CL CL NO 41 Instrument Air Supply 9
1 3
SH MAN CL CL NO 1
3 SH MAN CL CL NO 42A RB Hydrogen Analyzer 10 None 1
1/2,3/8(12)
SH SOL CL CL CL(2)
YES 42B RB Hydrogen Analyzer 10 None 1
1/2,3/8(12)
SH SOL CL CL CL(2)
YES 43 OTSG A Drain 7
Closed Loop Inside Containment 1
4 SH EMO ES OP AI CL YES 44 Component Cooling to CRD 3
1 21/2 CK OP CL NO 1
21/2 CK OP CL NO 45A Leak Rate Test Line 9
1 1/2 SH MAN CL CL NO 1
1/2 SH MAN CK CL NO 45B Leak Rate Test Line 9
1 1/2 SH MAN CL CL NO 1
1/2 SH MAN CL CL NO 45C(17)
Leak Rate Test Line 9
1 1/2 SH MAN CL CL NO 1
1/2 SH MAN CL CL NO 48 Breathing Air Supply to RB 9
1 2
SH MAN CL CL NO 1
2 SH MAN CL CL NO 49(16)
LP Nitrogen Supply to RB 22 1
11/2 CK CL CL NO 2
1 SH MAN CL CL NO 50 OTSG A EFW Injection 5
Closed Loop Inside Containment None 51 LRT Supply 11 Special Closure (Flange) 1 8
SH AIR CL AI CL NO  


Oconee Nuclear Station                                                                                                         UFSAR Table 6-7 (Page 5 of 7)
Oconee Nuclear Station UFSAR Table 6-7 (Page 5 of 7)
Inside Penetration Valve Data                                       Outside Penetration Valve Data Valve Position                                                         Valve Position Vlv                                                              Post Indi-                                                           Post Indi-Pen      Description    Arrg Qty Size         Type Oper     Signal   Norm     Fail     Acc cation Qty Size        Type  Oper    Signal  Norm     Fail Acc cation and Exhaust                                                                                 1     1/2,(10) SH     MAN     -        CL     -        CL   NO 52       HP Injection B 2   1     4         CK   -        -        CL     -        OP   NO                                     None Loop 53A       HP Nitrogen to 20   1     1         CK   -        -        CL     -        CL   NO     1     1/2,     SH     MAN     -        CL       -      CL   NO CFT                                                                                              1(8) 1    1       SH     MAN     -        CL       -      CL   NO 1     1       CK     -        -        CL       -      CL   NO (17) 53B      LP Nitrogen   21   1     11/2       CK   -        -        CL     -        CL   NO     1     2         SH   MAN       -      CL         -      CL NO Supply to RB 54       Component     4   1     8         SH   EMO       ES       OP     AI       CL   YES   1   8           SH     AIR     ES       OP       OP(1)   CL YES Cooling Outlet 55       Demin Water   9   1     4         SH   MAN       -        CL     -        CL   NO     1   4           SH     MAN     -        CL       -      CL NO Supply 56       Spent Fuel     9   1     8         SH     MAN       -    CL     -        CL   NO     1   8           SH     MAN     -        CL       -      CL NO Canal Fill/Drain 57(16)   DHR Return     28   1     12         SH   EMO       -        CL     AI       CL14 YES                                   None Line 1     10         SH   MAN       -        CL     -        CL   NO 14 1     8         SH   EMO       -        CL     AI       CL  YES (17)                                 (13) 58A      Pressurizer   1   2   3/4 1         SH   EMO       ES       OP     AI       CL   YES   1   1/2         SH     AIR     ES       OP       CL     CL YES Sample Line 58B       OTSG B         8                         Closed Loop Inside Containment                   1   1/2         SH     AIR     ES       CL       CL     CL YES Sample 59       Core Flood     17   `2 1           SH   EMO       -        CL     AI       CL   YES   2   1           SH     MAN     -        CL       -      CL NO Tank Sample 60       RB Sample     23   1   2           SH   EMO       ES       OP     AI       CL   YES   1   2           SH     AIR     ES       OP     OP1     CL   YES Line (Outlet)
(31 DEC 2014)
(4)                                                                       (3) 1  2,3          SH   EMO       -        CL     AI       CL   YES   1   1/2, 1       SH     MAN     -        CL     -      CL   NO 61       RB Sample     25   1   2           SH   EMO       ES       OP     AI       CL   YES   1   2           SH     AIR     ES       OP       OP1     CL YES Line (Intlet) 1   2           SH   EMO       -        CL     AI       CL   YES (31 DEC 2014)
Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc and Exhaust 1
1/2,(10)
SH MAN CL CL NO 52 HP Injection B Loop 2
1 4
CK CL OP NO None 53A HP Nitrogen to CFT 20 1
1 CK CL CL NO 1
1/2, 1(8)
SH MAN CL CL NO 1
1 SH MAN CL CL NO 1
1 CK CL CL NO 53B(17)
LP Nitrogen Supply to RB 21 1
11/2 CK CL CL NO 1
2 SH MAN CL CL NO 54 Component Cooling Outlet 4
1 8
SH EMO ES OP AI CL YES 1
8 SH AIR ES OP OP(1)
CL YES 55 Demin Water Supply 9
1 4
SH MAN CL CL NO 1
4 SH MAN CL CL NO 56 Spent Fuel Canal Fill/Drain 9
1 8
SH MAN CL CL NO 1
8 SH MAN CL CL NO 57(16)
DHR Return Line 28 1
12 SH EMO CL AI CL14 YES None 1
10 SH MAN CL CL NO 1
8 SH EMO CL AI CL14 YES 58A(17)
Pressurizer Sample Line 1
2 3/4 1(13)
SH EMO ES OP AI CL YES 1
1/2 SH AIR ES OP CL CL YES 58B OTSG B Sample 8
Closed Loop Inside Containment 1
1/2 SH AIR ES CL CL CL YES 59 Core Flood Tank Sample 17  
`2 1
SH EMO CL AI CL YES 2
1 SH MAN CL CL NO 60 RB Sample Line (Outlet) 23 1
2 SH EMO ES OP AI CL YES 1
2 SH AIR ES OP OP1 CL YES 1
2,3(4)
SH EMO CL AI CL YES 1
1/2, 1(3)
SH MAN CL CL NO 61 RB Sample Line (Intlet) 25 1
2 SH EMO ES OP AI CL YES 1
2 SH AIR ES OP OP1 CL YES 1
2 SH EMO CL AI CL YES  


Oconee Nuclear Station                                                                                                                                           UFSAR Table 6-7 (Page 6 of 7)
Oconee Nuclear Station UFSAR Table 6-7 (Page 6 of 7)
Inside Penetration Valve Data                                                         Outside Penetration Valve Data Valve Position                                                                         Valve Position Vlv                                                                          Post        Indi-                                                                   Post Indi-Pen          Description      Arrg    Qty       Size     Type     Oper     Signal   Norm       Fail     Acc         cation      Qty Size        Type      Oper    Signal    Norm   Fail   Acc cation 62(17)       DHR Return       29       1         12         SH     EMO       -        CL       AI       CL(14)       YES                                           None Line 1         10         SH     MAN       -        CL       -        CL           NO 63           LPSW RBACs       27                                                 None                                               2   6           SH       AIR     ES       OP     CL       CL YES Supply 64           LPSW RBACs       27                                                 None                                               2   6           SH       AIR     ES       OP     CL       CL YES Return REACTOR BUILDING PENETRATION VALVE INFORMATION LEGEND 7 NOTES LEGEND Valve Arrgt - Refer to Figure 6-9.
(31 DEC 2014)
Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc 62(17)
DHR Return Line 29 1
12 SH EMO CL AI CL(14)
YES None 1
10 SH MAN CL CL NO 63 LPSW RBACs Supply 27 None 2
6 SH AIR ES OP CL CL YES 64 LPSW RBACs Return 27 None 2
6 SH AIR ES OP CL CL YES REACTOR BUILDING PENETRATION VALVE INFORMATION LEGEND 7 NOTES LEGEND Valve Arrgt - Refer to Figure 6-9.
Qty - Quantity of comparable penetration valves shown Type - Valve types:
Qty - Quantity of comparable penetration valves shown Type - Valve types:
SH (Shut Off Valve) - gate, globe, ball, plug, butterfly, diaphragm or other type on/off valve with the ability to shut off flow.
SH (Shut Off Valve) - gate, globe, ball, plug, butterfly, diaphragm or other type on/off valve with the ability to shut off flow.
CK (Check Valve) - stop check, swing check, tilting disc check, lift check, or other type of check valve whose function is to prevent flow in the reverse direction.
CK (Check Valve) - stop check, swing check, tilting disc check, lift check, or other type of check valve whose function is to prevent flow in the reverse direction.
Size - Valve size in inches Oper - Valve operator types MAN - manual EMO - electric motor operator AIR - diaphragm operator HYD - hydraulic operator SOL - solenoid Signal - Noted "ES" if the valve receives an Engineered Safeguards signal. Refer to Section 7.3 for further discussion of ES signals.
Size - Valve size in inches Oper - Valve operator types MAN - manual EMO - electric motor operator AIR - diaphragm operator HYD - hydraulic operator SOL - solenoid Signal - Noted "ES" if the valve receives an Engineered Safeguards signal. Refer to Section 7.3 for further discussion of ES signals.
Valve Positions - Norm: position during normal operation, Fail: position without operator motive force, Post Acc: desired post-accident position OP - Open CL - Closed AI - As Is Indication - remove valve position indication (31 DEC 2014)
Valve Positions - Norm: position during normal operation, Fail: position without operator motive force, Post Acc: desired post-accident position OP - Open CL - Closed AI - As Is Indication - remove valve position indication  


Oconee Nuclear Station                                                                                                                                           UFSAR Table 6-7 (Page 7 of 7)
Oconee Nuclear Station UFSAR Table 6-7 (Page 7 of 7)
Inside Penetration Valve Data                                                           Outside Penetration Valve Data Valve Position                                                                           Valve Position Vlv                                                                        Post      Indi-                                                                       Post      Indi-Pen      Description          Arrg    Qty     Size     Type     Oper     Signal     Norm     Fail     Acc       cation    Qty    Size          Type    Oper      Signal  Norm   Fail   Acc       cation Notes:
(31 DEC 2014)
: 1. Penetrations 7, 54, 60, and 61 outboard isolation valves fail open on loss of ES power to their associated solenoid valves provided air is available to open the valves. With ES power energizing the solenoid valves, the isolation valves close with or without supply air.
Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc Notes:
: 2. Although initially closed for Reactor Building isolation, valves associated with penetrations 24 and 42 can be opened for post-accident hydrogen monitoring.
: 1.
: 3. For Penetration 60, the Unit 3 outside, manual penetration valve is 1/2 inch while the Unit 1 and Unit 2 outside, manual penetration valve is 1 inch.z
Penetrations 7, 54, 60, and 61 outboard isolation valves fail open on loss of ES power to their associated solenoid valves provided air is available to open the valves. With ES power energizing the solenoid valves, the isolation valves close with or without supply air.
: 4. For Penetration 60, the Unit 3 inside, non-ES actuated penetration valve is 3 inch while the Unit 1 and Unit 2 inside, non-ES actuated penetration valve is 2 inch.
: 2.
: 5. For Penetration 5b, there are two outside penetration solenoid valves for Units 1 and 2. There are two outside penetration manually operated valves for Unit 3. Only the solenoid valves on Units 1 & 2 fail closed and have remote position indication.
Although initially closed for Reactor Building isolation, valves associated with penetrations 24 and 42 can be opened for post-accident hydrogen monitoring.
: 6. For Penetration 10a, the Unit 2 outside penetration valve is 1.5 inches while the Unit 1 & 3 outside penetration valves are 1 inch.
: 3.
: 7. For Penetration 7, the Unit 2 inside penetration valve is 3 inch while the Unit 1 and Unit 3 inside penetration valves are 4 inch.
For Penetration 60, the Unit 3 outside, manual penetration valve is 1/2 inch while the Unit 1 and Unit 2 outside, manual penetration valve is 1 inch.z
: 8. For Penetration 53a, the Unit 1 outside penetration valve is 1 inch while the Unit 2 and Unit 3 outside penetration valves are 1/2 inch.
: 4.
: 9. For Penetration 38, the Unit 1 outside penetration valve is 1.5 inches while the Unit 2 and Unit 3 outside penetration valves are 2 inches.
For Penetration 60, the Unit 3 inside, non-ES actuated penetration valve is 3 inch while the Unit 1 and Unit 2 inside, non-ES actuated penetration valve is 2 inch.
: 5.
For Penetration 5b, there are two outside penetration solenoid valves for Units 1 and 2. There are two outside penetration manually operated valves for Unit 3. Only the solenoid valves on Units 1 & 2 fail closed and have remote position indication.
: 6.
For Penetration 10a, the Unit 2 outside penetration valve is 1.5 inches while the Unit 1 & 3 outside penetration valves are 1 inch.
: 7.
For Penetration 7, the Unit 2 inside penetration valve is 3 inch while the Unit 1 and Unit 3 inside penetration valves are 4 inch.
: 8.
For Penetration 53a, the Unit 1 outside penetration valve is 1 inch while the Unit 2 and Unit 3 outside penetration valves are 1/2 inch.
: 9.
For Penetration 38, the Unit 1 outside penetration valve is 1.5 inches while the Unit 2 and Unit 3 outside penetration valves are 2 inches.
: 10. For Penetration 51, the Unit 1 outside penetration valve is 1 inch while the Unit 2 and Unit 3 outside penetration valves are 1/2 inch.
: 10. For Penetration 51, the Unit 1 outside penetration valve is 1 inch while the Unit 2 and Unit 3 outside penetration valves are 1/2 inch.
: 11. For Penetration 8a & 8b, the Unit 1 inside and outside penetration valve sizes are 1.5 inches. The Units 2 and 3 inside and outside penetration valve sizes are 1 inch.
: 11. For Penetration 8a & 8b, the Unit 1 inside and outside penetration valve sizes are 1.5 inches. The Units 2 and 3 inside and outside penetration valve sizes are 1 inch.
Line 172: Line 452:
: 18. Deleted per 2005 Update.
: 18. Deleted per 2005 Update.
: 19. Deleted per 2005 Update.
: 19. Deleted per 2005 Update.
: 20. For Penetration 28, the OTSG B Main Steam Line piping exits the Reactor Building to the yard.
: 20. For Penetration 28, the OTSG B Main Steam Line piping exits the Reactor Building to the yard.  
(31 DEC 2014)


Oconee Nuclear Station                                                 UFSAR Table 6-8 (Page 1 of 2)
Oconee Nuclear Station UFSAR Table 6-8 (Page 1 of 2)
Table 6-8. High Pressure Injection System Component Data High Pressure Injection Pump Type                                         Vertical, multistage, centrifugal, mechanical seal Capacity, gal/min                             (See Figure 6-16)
(31 DEC 2005)
Head, ft H20 (at sp. gr. = 1)                 (See Figure 6-16)
Table 6-8. High Pressure Injection System Component Data High Pressure Injection Pump Type Vertical, multistage, centrifugal, mechanical seal Capacity, gal/min (See Figure 6-16)
Motor Horsepower, nameplate hp               600 Pump Material                                 SS wetted parts Design Pressure, psig                         3,040/3,120 Design Temperature, F                         200/150 Letdown Cooler Type                                         Shell and spiral tube Heat Transferred, Btu/hr                     16.0 x 106 Letdown Flow, lb/hr                           3.5 x 104 Letdown Cooler lnlet/Outlet Temperature, F   555/120 Material, shell/tube                         CS/SS Design Pressure, psig                         2,500 Design Temperature, F                         600 Component Cooling Water Flow (ea.), lb/hr     2 x 105 Code                                         ASME Sec. III-C & VIII Reactor Coolant Pump Seal Return Cooler Type                                         Shell and tube Heat Transferred, Btu/hr                     2.2 x 106 Seal Return Flow, lb/hr                       1.25 x 105 Seal Return Temperature Change, F             145 - 127 Material, shell/tube                         SS/SS Design Pressure, psig                         150 Design Temperature, F                         286 (Unit 1), 200 (Units 2&3)
Head, ft H20 (at sp. gr. = 1)
Recirculated Cooling Water Flow (ea.), lb/hr 1.25 x 105 Code                                         ASME Sec. III-C & VIII Letdown Storage Tank Volume, ft3                                   600 Design Pressure, psig                         100 Design Temperature, F                         200 (31 DEC 2005)
(See Figure 6-16)
Motor Horsepower, nameplate hp 600 Pump Material SS wetted parts Design Pressure, psig 3,040/3,120 Design Temperature, F 200/150 Letdown Cooler Type Shell and spiral tube Heat Transferred, Btu/hr 16.0 x 106 Letdown Flow, lb/hr 3.5 x 104 Letdown Cooler lnlet/Outlet Temperature, F 555/120 Material, shell/tube CS/SS Design Pressure, psig 2,500 Design Temperature, F 600 Component Cooling Water Flow (ea.), lb/hr 2 x 105 Code ASME Sec. III-C & VIII Reactor Coolant Pump Seal Return Cooler Type Shell and tube Heat Transferred, Btu/hr 2.2 x 106 Seal Return Flow, lb/hr 1.25 x 105 Seal Return Temperature Change, F 145 - 127 Material, shell/tube SS/SS Design Pressure, psig 150 Design Temperature, F 286 (Unit 1), 200 (Units 2&3)
Recirculated Cooling Water Flow (ea.), lb/hr 1.25 x 105 Code ASME Sec. III-C & VIII Letdown Storage Tank Volume, ft3 600 Design Pressure, psig 100 Design Temperature, F 200  


Oconee Nuclear Station                             UFSAR Table 6-8 (Page 2 of 2)
Oconee Nuclear Station UFSAR Table 6-8 (Page 2 of 2)
Material                     SS Code                         ASME Sec. III-C Purification Demineralizer Type                         Mixed bed, boric acid saturated Material                     SS 3
(31 DEC 2005)
Resin Volume, ft            50 Flow, gal/min               70 Vessel Design Pressure, psig 150 Vessel Design Temperature, F 200 Code                         ASME Sec. III-C Letdown Filter Design Flow Rate, gal/min   80 Material                     SS Design Temperature           200 Design Pressure             150 Code                         ASME Sec. III-C (31 DEC 2005)
Material SS Code ASME Sec. III-C Purification Demineralizer Type Mixed bed, boric acid saturated Material SS Resin Volume, ft3 50 Flow, gal/min 70 Vessel Design Pressure, psig 150 Vessel Design Temperature, F 200 Code ASME Sec. III-C Letdown Filter Design Flow Rate, gal/min 80 Material SS Design Temperature 200 Design Pressure 150 Code ASME Sec. III-C  


Oconee Nuclear Station                                         UFSAR Table 6-9 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-9 (Page 1 of 1)
(31 DEC 2009)
Table 6-9. Low Pressure Injection System Component Data Pump (each)
Table 6-9. Low Pressure Injection System Component Data Pump (each)
Type                                     Single stage, centrifugal Capacity, gpm                             3,000 Head at Rated Capacity, ft H20           350 Motor Horsepower, hp                     400 Material                                 SS (wetted parts)
Type Single stage, centrifugal Capacity, gpm 3,000 Head at Rated Capacity, ft H20 350 Motor Horsepower, hp 400 Material SS (wetted parts)
Design Pressure, psig                     560/580 Design Temperature, F                     300/250 Cooler (each)
Design Pressure, psig 560/580 Design Temperature, F 300/250 Cooler (each)
Type                                     Shell and tube Capacity (at 140 F), Btu/hr               60 x 106 Reactor Coolant Flow, gal/min             6,000 Low Pressure Service Water Flow, gal/min 6,000 Low Pressure Service Water lnlet Temp, F 75 Material, Shell/Tube                     CS/SS Design Pressure, Shell                   150 Design Pressure, Tube                     515(1)/370(2) (470/505 for Unit 3 only)
Type Shell and tube Capacity (at 140 F), Btu/hr 60 x 106 Reactor Coolant Flow, gal/min 6,000 Low Pressure Service Water Flow, gal/min 6,000 Low Pressure Service Water lnlet Temp, F 75 Material, Shell/Tube CS/SS Design Pressure, Shell 150 Design Pressure, Tube 515(1)/370(2) (470/505 for Unit 3 only)
Design Temperature, F                     250(1)/300(2) (300/250 for Unit 3 only)
Design Temperature, F 250(1)/300(2) (300/250 for Unit 3 only)
Code                                     ASME Section III-C, III and VIII Borated Water Storage Tank (each)
Code ASME Section III-C, III and VIII Borated Water Storage Tank (each)
Capacity, gal                             388,000 Material                                 CS/Coated inside Design Pressure                           Vessel Full plus 10 ft Hydro Head Design Temperature, F                     150 Code                                     AWWA D-100 Note:
Capacity, gal 388,000 Material CS/Coated inside Design Pressure Vessel Full plus 10 ft Hydro Head Design Temperature, F 150 Code AWWA D-100 Note:
: 1. A Cooler Units 1 & 2
: 1. A Cooler Units 1 & 2
: 2. B Cooler Units 1 & 2 (31 DEC 2009)
: 2. B Cooler Units 1 & 2  


Oconee Nuclear Station                                             UFSAR Table 6-10 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-10 (Page 1 of 1)
Table 6-10. Core Flooding System Components Data Core Flooding Tanks Number                                     2 Design Pressure, psig                       700 Operating Pressure, psig                   600 Minimum Pressure, psig                     575 Design Temperature, F                       300 Operating Temperature, F                   110 3
(31 DEC 2000)
Total Volume, ft                            1,410 3
Table 6-10. Core Flooding System Components Data Core Flooding Tanks Number 2
Normal Water Volume, ft                    1,040 Minimum Water Volume, ft3                   1,010 Material of Construction                   Carbon steel lined with SS Check Valves Number per Flood Line                       2 Size, in.                                   14 Material                                   316 SS Design Pressure, psig                       2,500 Design Temperature Valve nearest reactor, F                 650 Valve nearest tank, F                     300 Isolation Valves Number per Flood Line                       1 Size, in.                                   14 Material                                   304 SS Design Pressure, psig                       2,500 Design Temperature, F                       300 First Check Reactor to First   Valve to Isolation Isolation Valve to Piping                              Check Valve        Valve              Tank Size, in.                           14                 14                 14 Material                           316 SS             304 SS             304 SS Design Pressure, psig               2,500               2,500             700 Design Temperature, F               650                 300               300 (31 DEC 2000)
Design Pressure, psig 700 Operating Pressure, psig 600 Minimum Pressure, psig 575 Design Temperature, F 300 Operating Temperature, F 110 Total Volume, ft3 1,410 Normal Water Volume, ft3 1,040 Minimum Water Volume, ft3 1,010 Material of Construction Carbon steel lined with SS Check Valves Number per Flood Line 2
Size, in.
14 Material 316 SS Design Pressure, psig 2,500 Design Temperature Valve nearest reactor, F 650 Valve nearest tank, F 300 Isolation Valves Number per Flood Line 1
Size, in.
14 Material 304 SS Design Pressure, psig 2,500 Design Temperature, F 300 Piping Reactor to First Check Valve First Check Valve to Isolation Valve Isolation Valve to Tank Size, in.
14 14 14 Material 316 SS 304 SS 304 SS Design Pressure, psig 2,500 2,500 700 Design Temperature, F 650 300 300  


Oconee Nuclear Station                                               UFSAR Table 6-11 (Page 1 of 2)
Oconee Nuclear Station UFSAR Table 6-11 (Page 1 of 2)
Table 6-11. Single Failure Analysis - Emergency Core Cooling System Component                                    Malfunction          Comments A. High Pressure Injection System
: 1. Suction valve for high pressure    Fails to open.        The parallel valve will supply injection pump from borated water                        the required flow to one storage tank.                                            pump string.
: 2. High pressure injection valve      Fails to open.        The alternate line and the two cross connect lines will provide the total required flow.
: 3. High pressure injection pump      Fails (stops).        Two backup pumps are (operating).                                            available to deliver the flow.
: 4. High pressure injection pump.      Fails to start.      Two backup pumps are available to deliver the flow.
: 5. Seal return line isolation valve. Fails to close on ES  The other isolation valve will signal.              close eliminating this fluid path.
: 6. Letdown cooler isolation valve. Fails to close on ES  The other isolation valve will signal.              close the flow path.
: 7. LDST-RBES return line isolation    Fails to open.        The other isolation valve will valve                                                    provide a LDST-RBES return flow path.
B. Low Pressure Injection System
: 1. Low pressure injection pump.      Fails to start.      Adequate injection is provided by the other pump.
: 2. Low pressure injection isolation  Fails to open.        Other line admits necessary valve.                                                  flow through both injection headers via the passive cross-over line.
: 3. Valve in suction line from the    Fails to open.        Drain line upstream of the Reactor Coolant System                                  first isolation valve opens admitting flow to the emergency sump. The LPI System then operates in the recirculation mode.
: 4. LPI Cooler isolation valve        Fails to open.        Other LPSW train admits (LPSW-4, -5)                                            necessary flow.
: 5. Service water pump - 1A, 1B, 1C    Fails to operate      The two remaining pumps will provide full low pressure service water flow to all components.
(31 DEC 2005)
(31 DEC 2005)
Table 6-11. Single Failure Analysis - Emergency Core Cooling System Component Malfunction Comments A.
High Pressure Injection System
: 1.
Suction valve for high pressure injection pump from borated water storage tank.
Fails to open.
The parallel valve will supply the required flow to one pump string.
: 2.
High pressure injection valve Fails to open.
The alternate line and the two cross connect lines will provide the total required flow.
: 3.
High pressure injection pump (operating).
Fails (stops).
Two backup pumps are available to deliver the flow.
: 4.
High pressure injection pump.
Fails to start.
Two backup pumps are available to deliver the flow.
: 5.
Seal return line isolation valve.
Fails to close on ES signal.
The other isolation valve will close eliminating this fluid path.
: 6.
Letdown cooler isolation valve.
Fails to close on ES signal.
The other isolation valve will close the flow path.
: 7.
LDST-RBES return line isolation valve Fails to open.
The other isolation valve will provide a LDST-RBES return flow path.
B.
Low Pressure Injection System
: 1.
Low pressure injection pump.
Fails to start.
Adequate injection is provided by the other pump.
: 2.
Low pressure injection isolation valve.
Fails to open.
Other line admits necessary flow through both injection headers via the passive cross-over line.
: 3.
Valve in suction line from the Reactor Coolant System Fails to open.
Drain line upstream of the first isolation valve opens admitting flow to the emergency sump. The LPI System then operates in the recirculation mode.
: 4.
LPI Cooler isolation valve (LPSW-4, -5)
Fails to open.
Other LPSW train admits necessary flow.
: 5.
Service water pump - 1A, 1B, 1C Fails to operate The two remaining pumps will provide full low pressure service water flow to all components.


Oconee Nuclear Station                                             UFSAR Table 6-11 (Page 2 of 2)
Oconee Nuclear Station UFSAR Table 6-11 (Page 2 of 2)
Component                                   Malfunction         Comments
(31 DEC 2005)
: 6. Service water pump - 3A, 3B       Fails to operate     The one remaining pump will provide full low pressure service water flow to all components.
Component Malfunction Comments
: 6.
Service water pump - 3A, 3B Fails to operate The one remaining pump will provide full low pressure service water flow to all components.
(RECIRCULATION FROM REACTOR BUILDING EMERGENCY SUMP)
(RECIRCULATION FROM REACTOR BUILDING EMERGENCY SUMP)
: 1. Valve in suction line from         Fails to open.       Other line admits necessary emergency sump.                                        flow.
: 1.
: 2. Valve in suction line from BWST. Fails to close after Check valve prevents flow initiating          into BWST.
Valve in suction line from emergency sump.
recirculation.
Fails to open.
: 3. Low pressure injection pump.       Loss of pump.       Reactor core protection will be maintained by alternate pump and low pressure injection string.
Other line admits necessary flow.
: 4. Valve in post accident boron       Fails to open       Redundant post accident dilution flow path from reactor                        boron dilution path admits outlet to emergency sump.                              necessary flow.
: 2.
C. Core Flooding System
Valve in suction line from BWST.
: 1. Isolation valve in discharge line. Closes during normal If the valve cannot be operation.          manually opened, the reactor must shut down or operations limited as specified in Technical Specifications.
Fails to close after initiating recirculation.
: 2. Tank relief valve.                 Opens during normal Loss of nitrogen pressure and operation.          consequent loss of ability of tank to perform. Reactor must be shut down or operations adjusted to Technical Specification limits and relief valve must be repaired.
Check valve prevents flow into BWST.
: 3. Check valves in charge line.       Excessive leak       It is extremely unlikely that detected during      both check valves would normal reactor      permit excessive leakage.
: 3.
operation.          Leakage would be indicated by core flooding tank pressure and level changes. If leakage becomes progressively worse or is unacceptably high, reactor must be shut down while the check valves are repaired.
Low pressure injection pump.
(31 DEC 2005)
Loss of pump.
Reactor core protection will be maintained by alternate pump and low pressure injection string.
: 4.
Valve in post accident boron dilution flow path from reactor outlet to emergency sump.
Fails to open Redundant post accident boron dilution path admits necessary flow.
C.
Core Flooding System
: 1.
Isolation valve in discharge line.
Closes during normal operation.
If the valve cannot be manually opened, the reactor must shut down or operations limited as specified in Technical Specifications.
: 2.
Tank relief valve.
Opens during normal operation.
Loss of nitrogen pressure and consequent loss of ability of tank to perform. Reactor must be shut down or operations adjusted to Technical Specification limits and relief valve must be repaired.
: 3.
Check valves in charge line.
Excessive leak detected during normal reactor operation.
It is extremely unlikely that both check valves would permit excessive leakage.
Leakage would be indicated by core flooding tank pressure and level changes. If leakage becomes progressively worse or is unacceptably high, reactor must be shut down while the check valves are repaired.  


Oconee Nuclear Station                                                                                         UFSAR Table 6-12 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-12 (Page 1 of 1)
Table 6-12. Oconee Nuclear Station Analysis of Valve Motors Which May Become Submerged Following A LOCA No.           Valve Identification Description                       Evaluation 1CF-1         "A" Core Flood Tank Discharge Valve                   No effect on ECCS capability or containment integrity. Valve is 2CF-1                                                                locked open during operation and is not operated subsequent to a 3CF-1                                                                LOCA. Valve is not a containment isolation valve.
(31 DEC 2000)
1CS-51       Reactor Building Isolation Valve for Quench Tank       No effect on ECCS capability or containment integrity. Valve is 2CS-51        Drain                                                  normally closed. Redundant isolation valve on outside of containment 3CS-51                                                              is not affected.
Table 6-12. Oconee Nuclear Station Analysis of Valve Motors Which May Become Submerged Following A LOCA No.
1HP-1         Reactor Coolant Inlet to "A" Letdown Cooler           No effect on ECCS capability or containment integrity. Letdown 2HP-1                                                                coolers are not used following a LOCA. Valve is not a containment 3HP-1                                                                isolation valve.
Valve Identification Description Evaluation 1CF-1 2CF-1 3CF-1 "A" Core Flood Tank Discharge Valve No effect on ECCS capability or containment integrity. Valve is locked open during operation and is not operated subsequent to a LOCA. Valve is not a containment isolation valve.
1HP-2         Reactor Coolant Inlet to "B" Letdown Cooler           No effect on ECCS capability or containment integrity. Letdown 2HP-2                                                                coolers are not used following a LOCA. Valve is not a containment 3HP-2                                                                isolation valve.
1CS-51 2CS-51 3CS-51 Reactor Building Isolation Valve for Quench Tank Drain No effect on ECCS capability or containment integrity. Valve is normally closed. Redundant isolation valve on outside of containment is not affected.
1HP-31       Reactor Coolant Outlet from "A" Letdown Cooler and     No effect on ECCS capability or containment integrity. Letdown 2HP-31        Reactor Building Isolation Valve                      coolers are not used following a LOCA. Redundant isolation valve on 3HP-31                                                              outside of containment is not affected.
1HP-1 2HP-1 3HP-1 Reactor Coolant Inlet to "A" Letdown Cooler No effect on ECCS capability or containment integrity. Letdown coolers are not used following a LOCA. Valve is not a containment isolation valve.
1HP-41       Reactor Coolant Outlet from "B" Letdown Cooler and     No effect on ECCS capability or containment integrity. Letdown 2HP-41        Reactor Building Isolation Valve                      coolers are not used following a LOCA. Redundant isolation valve on 3HP-41                                                              outside of containment is not affected.
1HP-2 2HP-2 3HP-2 Reactor Coolant Inlet to "B" Letdown Cooler No effect on ECCS capability or containment integrity. Letdown coolers are not used following a LOCA. Valve is not a containment isolation valve.
1CC-1         Component Cooling Water Inlet to "A" Letdown           No effect on ECCS capability or containment integrity. Letdown 2CC-1        Coolers                                                coolers are not used following a LOCA. Valve is not a containment 3CC-1                                                                isolation valve.
1HP-31 2HP-31 3HP-31 Reactor Coolant Outlet from "A" Letdown Cooler and Reactor Building Isolation Valve No effect on ECCS capability or containment integrity. Letdown coolers are not used following a LOCA. Redundant isolation valve on outside of containment is not affected.
1CC-2         Component Cooling Water Inlet to "B" Letdown           No effect on ECCS capability or containment integrity. Letdown 2CC-2        Coolers                                                coolers are not used following a LOCA. Valve is not a containment 3CC-2                                                                isolation valve.
1HP-41 2HP-41 3HP-41 Reactor Coolant Outlet from "B" Letdown Cooler and Reactor Building Isolation Valve No effect on ECCS capability or containment integrity. Letdown coolers are not used following a LOCA. Redundant isolation valve on outside of containment is not affected.
1CC-1 2CC-1 3CC-1 Component Cooling Water Inlet to "A" Letdown Coolers No effect on ECCS capability or containment integrity. Letdown coolers are not used following a LOCA. Valve is not a containment isolation valve.
1CC-2 2CC-2 3CC-2 Component Cooling Water Inlet to "B" Letdown Coolers No effect on ECCS capability or containment integrity. Letdown coolers are not used following a LOCA. Valve is not a containment isolation valve.
Note:
Note:
: 1. Valve is an ES valve and would shut upon ES actuation before becoming submerged.
: 1. Valve is an ES valve and would shut upon ES actuation before becoming submerged.  
 
Oconee Nuclear Station UFSAR Table 6-13 (Page 1 of 1)
(31 DEC 2000)
(31 DEC 2000)
Table 6-13. Equipment Operational During An Accident and Located Outside Containment 4160 Volt Station Auxiliary Switchgear 600 Volt Load Centers 600 Volt and 208 Volt Motor Control Center Batteries Chargers and Inverters Panelboards Low Pressure Injection Pump Motors High Pressure Injection Pump Motors Reactor Building Spray Pump Motors Low Pressure Service Water Pump Motors Cables


Oconee Nuclear Station                                           UFSAR Table 6-13 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-14 (Page 1 of 2)
Table 6-13. Equipment Operational During An Accident and Located Outside Containment 4160 Volt Station Auxiliary Switchgear 600 Volt Load Centers 600 Volt and 208 Volt Motor Control Center Batteries Chargers and Inverters Panelboards Low Pressure Injection Pump Motors High Pressure Injection Pump Motors Reactor Building Spray Pump Motors Low Pressure Service Water Pump Motors Cables (31 DEC 2000)
(31 DEC 2000)
 
Table 6-14. Equipment Operational During an Accident and Located Within the Containment Equipment Accident Environmental Tests Reactor Building Cooling Fans and Motors After preaging a prototype motor for an extrapolated 40 years insulation life and Fan testing it for operation under seismic conditions, the motor and fan assembly was placed in a pressure vessel. Steam is then injected into the chamber to a pressure of 70 to 80 psia and chemicals similar to those used in the spray system are introduced. The pressure cycle is repeated four additional times and then pressure is reduced to the level to be expected following the accident. The motor then is run continuously for a minimum of 7 days in the test chamber.
Oconee Nuclear Station                                                        UFSAR Table 6-14 (Page 1 of 2)
Cables Representative samples of preaged cables are tested under high pressure, temperature and humidity conditions equal to or exceeding those specified for the LOCA. These cables are preaged for forty years of radiation and temperature prior to testing.
Table 6-14. Equipment Operational During an Accident and Located Within the Containment Equipment           Accident Environmental Tests Reactor Building     After preaging a prototype motor for an extrapolated 40 years insulation life and Cooling Fans and    Fan testing it for operation under seismic conditions, the motor and fan assembly Motors              was placed in a pressure vessel. Steam is then injected into the chamber to a pressure of 70 to 80 psia and chemicals similar to those used in the spray system are introduced. The pressure cycle is repeated four additional times and then pressure is reduced to the level to be expected following the accident. The motor then is run continuously for a minimum of 7 days in the test chamber.
Valves A typical production valve and actuator was tested as follows under simulated accident conditions. After preaging heat test and shock and vibration tests, the production valve and actuator was subjected to the following environmental tests:
Cables               Representative samples of preaged cables are tested under high pressure, temperature and humidity conditions equal to or exceeding those specified for the LOCA. These cables are preaged for forty years of radiation and temperature prior to testing.
Valves               A typical production valve and actuator was tested as follows under simulated accident conditions. After preaging heat test and shock and vibration tests, the production valve and actuator was subjected to the following environmental tests:
: 1. Saturated steam at 90 psig for one hour.
: 1. Saturated steam at 90 psig for one hour.
: 2. Boric acid spray for the next two hours at 70 psig followed by a pressure drop to 40 psig with the spray continuing for an additional half hour.
: 2. Boric acid spray for the next two hours at 70 psig followed by a pressure drop to 40 psig with the spray continuing for an additional half hour.
Line 260: Line 604:
: 5. Steam pressure at 10 psig was then maintained for six days yielding a total test time of seven days.
: 5. Steam pressure at 10 psig was then maintained for six days yielding a total test time of seven days.
: 6. Valve operation was conducted at the beginning and the end of each level of pressure in 1, 2, 3, 4, and 5 above.
: 6. Valve operation was conducted at the beginning and the end of each level of pressure in 1, 2, 3, 4, and 5 above.
Electrical           Qualification tests have been performed on one production assembly of each type Penetrations        that is required to function during or following the loss-of-coolant accident to verify its functional capability. The interior end of the penetration assemblies were subjected to the following emergency conditions at 100 percent relative humidity in an autoclave built to duplicate Oconee Reactor Building concrete and nozzle design.
Electrical Penetrations Qualification tests have been performed on one production assembly of each type that is required to function during or following the loss-of-coolant accident to verify its functional capability. The interior end of the penetration assemblies were subjected to the following emergency conditions at 100 percent relative humidity in an autoclave built to duplicate Oconee Reactor Building concrete and nozzle design.
: 1. First fifteen minutes:
: 1. First fifteen minutes:
Pressure of 65 psig at a temperature of 300 °F Rise time for normal operating conditions - less than ten seconds.
Pressure of 65 psig at a temperature of 300 F
° Rise time for normal operating conditions - less than ten seconds.
: 2. Next forty-five minutes:
: 2. Next forty-five minutes:
Pressure of 40 psig at a temperature of 260 °F
Pressure of 40 psig at a temperature of 260 F
°
: 3. Next twenty-three hours:
: 3. Next twenty-three hours:
Pressure of 35 psig at a temperature of 250 °F During the environmental tests, functional capability was demonstrated by applying rated current to conductors in series at 600 volts r.m.s. above ground.
Pressure of 35 psig at a temperature of 250 F
The temperature along the nozzle and in the wire bundles was monitored throughout the test. Leak rate was measured and recorded during the test.
° During the environmental tests, functional capability was demonstrated by applying rated current to conductors in series at 600 volts r.m.s. above ground.
The temperature along the nozzle and in the wire bundles was monitored throughout the test. Leak rate was measured and recorded during the test.  
 
Oconee Nuclear Station UFSAR Table 6-14 (Page 2 of 2)
(31 DEC 2000)
(31 DEC 2000)
 
Equipment Accident Environmental Tests The following tests were performed before and after the autoclave test:
Oconee Nuclear Station                                                      UFSAR Table 6-14 (Page 2 of 2)
Equipment           Accident Environmental Tests The following tests were performed before and after the autoclave test:
: 1. Connector and conductor resistance test. Measured ohmic resistance of each conductor.
: 1. Connector and conductor resistance test. Measured ohmic resistance of each conductor.
: 2. Dielectric withstand tests.
: 2. Dielectric withstand tests.
Line 277: Line 624:
: 4. Insulation resistance. Conductor to ground.
: 4. Insulation resistance. Conductor to ground.
: 5. Leak rate test.
: 5. Leak rate test.
Reactor Coolant     Reactor coolant pressure transmitters required for use within the Reactor Building System Pressure      following an accident have been conservatively tested under conditions simulating Transmitters        the environment expected after the design base 14.1 ft2 LOCA. The results of these tests show that the transmitters are acceptable for the required functions. A three phase test was performed to simulate the post-LOCA Reactor Building environment. The respective phases are given below:
Reactor Coolant System Pressure Transmitters Reactor coolant pressure transmitters required for use within the Reactor Building following an accident have been conservatively tested under conditions simulating the environment expected after the design base 14.1 ft2 LOCA. The results of these tests show that the transmitters are acceptable for the required functions. A three phase test was performed to simulate the post-LOCA Reactor Building environment. The respective phases are given below:
Phase I - Pre-accident test at the Babcock & Wilcox Nuclear Development Center (NDC) to simulate the environmental dose to the transmitters associated with the 40-year plant design lifetime.
Phase I - Pre-accident test at the Babcock & Wilcox Nuclear Development Center (NDC) to simulate the environmental dose to the transmitters associated with the 40-year plant design lifetime.
Phase II - Environmental autoclave test at Franklin Institute Research Laboratory to simulate the Reactor Building pressure and temperature history for a LOCA.
Phase II - Environmental autoclave test at Franklin Institute Research Laboratory to simulate the Reactor Building pressure and temperature history for a LOCA.
Line 284: Line 631:
Phase II consisted of exposing the transmitters in the operating mode to a steam environment in a test autoclave for 24 hours. The units were supplied with a constant input of approximately 2/3 of full range and the resultant output/input ratio was measured for the test duration.
Phase II consisted of exposing the transmitters in the operating mode to a steam environment in a test autoclave for 24 hours. The units were supplied with a constant input of approximately 2/3 of full range and the resultant output/input ratio was measured for the test duration.
Phase III consisted of irradiating the transmitters while the units were in the operating mode in much the same manner as Phase I except that the box was lowered into position beside one fuel element from the reactor. A constant input of approximately 2/3 of full range was maintained throughout the test.
Phase III consisted of irradiating the transmitters while the units were in the operating mode in much the same manner as Phase I except that the box was lowered into position beside one fuel element from the reactor. A constant input of approximately 2/3 of full range was maintained throughout the test.
The resulting output signal inaccuracies for each test phase were analyzed and found to be acceptable.
The resulting output signal inaccuracies for each test phase were analyzed and found to be acceptable.  
(31 DEC 2000)


Oconee Nuclear Station                                                       UFSAR Table 6-15 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-15 (Page 1 of 1)
Table 6-15. Emergency Core Cooling Systems Performance Testing High Pressure        One of two pumps operates continuously. The other pump will be operated Injection Pumps      periodically.
High Pressure        The remotely operated stop valves in each line are opened partially one at a time.
Injection Line      The flow monitors will indicate flow through the lines.
Valves High Pressure        The valves are opened and closed individually and console lights monitored to Injection Pump      indicate valve position.
Suction Valves Low Pressure        Pumps are used in normal service for shutdown cooling. These pumps are tested Injection Pumps      singly for operability by opening the borated water storage tank outlet valves and the bypass valves in the borated water storage tank fill line. This allows water to be pumped from the borated water storage tank through each of the injection lines and back to the tank.
Borated Water        The operational readiness of these valves is established in completing the pump Storage Tank        operational test discussed above. During this test, each valve is tested separately.
Outlet Valves Low Pressure        With pumps shut down and borated water storage tank outlet valves closed, these Injection Valves    valves can be opened and reclosed by operator action.
Sump                With low pressure injection pumps shut down, operation of these valves can be Recirculation        checked.
Suction Valves Check Valves in      With the reactor shut down, the check valves in each core flood line are checked Core Flooding        for operability by closing the isolation valves, reducing the Reactor Coolant Injection            System pressure to provide P slightly above the check valve opening pressure, and opening the isolation valves. Check valve operability is shown by tank pressure and level changes.
(31 DEC 2005)
(31 DEC 2005)
Table 6-15. Emergency Core Cooling Systems Performance Testing High Pressure Injection Pumps One of two pumps operates continuously. The other pump will be operated periodically.
High Pressure Injection Line Valves The remotely operated stop valves in each line are opened partially one at a time.
The flow monitors will indicate flow through the lines.
High Pressure Injection Pump Suction Valves The valves are opened and closed individually and console lights monitored to indicate valve position.
Low Pressure Injection Pumps Pumps are used in normal service for shutdown cooling. These pumps are tested singly for operability by opening the borated water storage tank outlet valves and the bypass valves in the borated water storage tank fill line. This allows water to be pumped from the borated water storage tank through each of the injection lines and back to the tank.
Borated Water Storage Tank Outlet Valves The operational readiness of these valves is established in completing the pump operational test discussed above. During this test, each valve is tested separately.
Low Pressure Injection Valves With pumps shut down and borated water storage tank outlet valves closed, these valves can be opened and reclosed by operator action.
Sump Recirculation Suction Valves With low pressure injection pumps shut down, operation of these valves can be checked.
Check Valves in Core Flooding Injection With the reactor shut down, the check valves in each core flood line are checked for operability by closing the isolation valves, reducing the Reactor Coolant System pressure to provide P slightly above the check valve opening pressure, and opening the isolation valves. Check valve operability is shown by tank pressure and level changes.


Oconee Nuclear Station             UFSAR Table 6-16 and 6-17 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-16 and 6-17 (Page 1 of 1)
Table 6-16. Deleted Per 1999 Update Table 6-17. Deleted Per 1999 Update (31 DEC 2000)
(31 DEC 2000)
Table 6-16. Deleted Per 1999 Update Table 6-17. Deleted Per 1999 Update  


Oconee Nuclear Station                                                   UFSAR Table 6-18 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-18 (Page 1 of 1)
(31 DEC 2000)
Table 6-18. Inventory of Iodine Isotopes in Reactor Building (at t = o)
Table 6-18. Inventory of Iodine Isotopes in Reactor Building (at t = o)
Isotope                                       Initial Inventory Curies/MWt Iodine 131                                         2.51 x 104 Iodine 132                                         3.81 x 104 Iodine 133                                         5.63 x 104 Iodine 134                                         6.58 x 104 Iodine 135                                         5.10 x 104 (31 DEC 2000)
Isotope Initial Inventory Curies/MWt Iodine 131 2.51 x 104 Iodine 132 3.81 x 104 Iodine 133 5.63 x 104 Iodine 134 6.58 x 104 Iodine 135 5.10 x 104  


Oconee Nuclear Station             UFSAR Table 6-19 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-19 (Page 1 of 1)
Table 6-19. Deleted Per 2015 Update (31 DEC 2015)
(31 DEC 2015)
Table 6-19. Deleted Per 2015 Update  


Oconee Nuclear Station                                           UFSAR Table 6-20 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-20 (Page 1 of 1)
Table 6-20. Parameters for Boron Precipitation Analysis Initial Reactor Core Power                     2568 MWth Decay Heat                                     120% of 1971 ANS LPI Flow Rate                                   402 lbm/sec Core Mixing Mass                               60000 lbm LPI Injection Enthalpy                         123 Btu/lbm Containment Pressure                           25 psia RCS Boron Concentration                         2100 ppm BWST Boron Concentration                       3000 ppm CFT Boron Concentration                         4000 ppm (31 DEC 2000)
(31 DEC 2000)
Table 6-20. Parameters for Boron Precipitation Analysis Initial Reactor Core Power 2568 MWth Decay Heat 120% of 1971 ANS LPI Flow Rate 402 lbm/sec Core Mixing Mass 60000 lbm LPI Injection Enthalpy 123 Btu/lbm Containment Pressure 25 psia RCS Boron Concentration 2100 ppm BWST Boron Concentration 3000 ppm CFT Boron Concentration 4000 ppm  


Oconee Nuclear Station                                           UFSAR Table 6-21 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-21 (Page 1 of 1)
Table 6-21. Summary of Calculated Containment Pressures and Temperatures for LOCA Cases Peak           Peak                    Blowdown Containment    Containment                   Energy Pressure     Temperature Time of Peak      Release Description                (psig)         (°F)   Pressure (sec)   (x106Btu)
(31 DEC 2003)
Hot Leg SG Inlet Cases (14.1 ft2 break size) 100% RTP                   56.95         281.68       14.5           316.23 Reduced Tavg                 55.27         279.57       15.3           312.37 10°F Tcold                 56.62         281.29       13.9           314.59 80% RTP                   56.34         280.94       14.2           313.78 60% RTP                   55.74         280.19       14.2           311.65 Max ECCS case                 56.88         281.45       14.3           315.74 LOOP Case                   56.82         281.54       14.2           315.39 Hot Leg RV Outlet Cases (14.1 ft2 break size) 100% RTP                   56.69         281.40       13.0           316.56 Cold Leg Pump Discharge Case (8.55 ft2 break size) 100% RTP                   52.52         276.00       16.8           313.31 Cold Leg Pump Suction Case (8.55 ft2 break size 100% RTP                   53.50         277.31       23.6           303.47 (31 DEC 2003)
Table 6-21. Summary of Calculated Containment Pressures and Temperatures for LOCA Cases Description Peak Containment Pressure (psig)
Peak Containment Temperature
(°F)
Time of Peak Pressure (sec)
Blowdown Energy Release (x106Btu)
Hot Leg SG Inlet Cases (14.1 ft2 break size) 100% RTP 56.95 281.68 14.5 316.23 Reduced Tavg 55.27 279.57 15.3 312.37 10°F Tcold 56.62 281.29 13.9 314.59 80% RTP 56.34 280.94 14.2 313.78 60% RTP 55.74 280.19 14.2 311.65 Max ECCS case 56.88 281.45 14.3 315.74 LOOP Case 56.82 281.54 14.2 315.39 Hot Leg RV Outlet Cases (14.1 ft2 break size) 100% RTP 56.69 281.40 13.0 316.56 Cold Leg Pump Discharge Case (8.55 ft2 break size) 100% RTP 52.52 276.00 16.8 313.31 Cold Leg Pump Suction Case (8.55 ft2 break size 100% RTP 53.50 277.31 23.6 303.47  


Oconee Nuclear Station                                                                           UFSAR Table 6-22 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-22 (Page 1 of 1)
Table 6-22. Containment Response Analyses Initial Conditions General Information External containment design pressure (psid)                               3.0 Internal containment design pressure (psig)                               59 Containment design temperature (°F)
(31 DEC 2017)
Containment free volume (ft3)                                         1,810,000 Containment design leak rate (/1st day at peak accident pressure)       0.2%
Table 6-22. Containment Response Analyses Initial Conditions General Information External containment design pressure (psid) 3.0 Internal containment design pressure (psig) 59 Containment design temperature (°F)
Large LOCA Short Large LOCA Long-   Steam Line Break Term            Term Initial Conditions Reactor power (MWt @ 102% design overpower)                             2619             2619               2619 Average reactor coolant temperature (°F)                                 581             581                 581 Containment pressure (psig)                                               1.2               0                 1.5 Containment atmosphere temperature (°F)                                   80           variable             170 Containment atmosphere relative humidity (%)                               0             100                   0 Low pressure service water temperature (°F)                             N/A           variable             N/A Borated water temperature (°F)                                           N/A             115                 120 Borated water storage tank level (ft)                                   N/A               46                 N/A 3
Containment free volume (ft3) 1,810,000 Containment design leak rate (/1st day at peak accident pressure) 0.2%
Core flood tank volume (both, ft )                                       1944             1944               1940 (31 DEC 2017)
Large LOCA Short Term Large LOCA Long-Term Steam Line Break Initial Conditions Reactor power (MWt @ 102% design overpower) 2619 2619 2619 Average reactor coolant temperature (°F) 581 581 581 Containment pressure (psig) 1.2 0
1.5 Containment atmosphere temperature (°F) 80 variable 170 Containment atmosphere relative humidity (%)
0 100 0
Low pressure service water temperature (°F)
N/A variable N/A Borated water temperature (°F)
N/A 115 120 Borated water storage tank level (ft)
N/A 46 N/A Core flood tank volume (both, ft3) 1944 1944 1940  


Oconee Nuclear Station                                         UFSAR Table 6-23 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-23 (Page 1 of 1)
Table 6-23. Containment Structural Heat Sink Data Heat Sink           Painted     Unpainted       Unpainted   Unpainted    Total Surface Material        Metal          Metal    Metal Total    Area (ft2)
(31 DEC 2013)
Thickness (ft)  Thickness        Exposed    Mass (lbm)
Table 6-23. Containment Structural Heat Sink Data Heat Sink Painted Material Thickness (ft)
Group        Surface Area (ft2)
Unpainted Metal Thickness Group Unpainted Metal Exposed Surface Area (ft2)
Carbon Steel         0.0208                                                   61,353 Building Cylinder Concrete              3.75                                                   61,353 Building Cylinder Carbon Steel         0.0208                                                   16,230 Building Dome Concrete              3.25                                                   16,230 Building Dome Carbon Steel         0.0208                                                     8890 Building Base Concrete              8.5                                                     8890 Building Base Internal               1.76                                                   66,231 Concrete Internal             0.0316                                                   165,400 Carbon Steel Internal                            1             63,727     300,000         63,727 Carbon Steel Internal                            2             8628     258,000           8628 Stainless Steel Internal                             1             9892       3828             9892 Aluminum Internal                             4               727     23,268           727 Copper (31 DEC 2013)
Unpainted Metal Total Mass (lbm)
Total Surface Area (ft2)
Carbon Steel Building Cylinder 0.0208 61,353 Concrete Building Cylinder 3.75 61,353 Carbon Steel Building Dome 0.0208 16,230 Concrete Building Dome 3.25 16,230 Carbon Steel Building Base 0.0208 8890 Concrete Building Base 8.5 8890 Internal Concrete 1.76 66,231 Internal Carbon Steel 0.0316 165,400 Internal Carbon Steel 1
63,727 300,000 63,727 Internal Stainless Steel 2
8628 258,000 8628 Internal Aluminum 1
9892 3828 9892 Internal Copper 4
727 23,268 727  


Oconee Nuclear Station                                             UFSAR Table 6-24 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-24 (Page 1 of 1)
Table 6-24. Accident Chronology for Limiting Break for Equipment Qualification Event                                                        Time(seconds)
Beginning of ECCS injection                                  6.0 Beginning of CFT injection                                    12.0 Peak containment pressure                                    20 End of blowdown phase                                        26.5 Beginning of RB Spray                                        142 Beginning of RBCU operation                                  302 Peak containment pressure after blowdown                      N/A End of core reflood phase                                    535 Beginning of sump recirculation phase                        4529 End of RB Spray/Beginning of re-circ spray                    4529 End of S/G energy release                                    N/A Depressurization of containment (1/2 of design pressure)      within 2000 seconds (depending on RBCU assumptions)
(31 DEC 2017)
(31 DEC 2017)
Table 6-24. Accident Chronology for Limiting Break for Equipment Qualification Event Time(seconds)
Beginning of ECCS injection 6.0 Beginning of CFT injection 12.0 Peak containment pressure 20 End of blowdown phase 26.5 Beginning of RB Spray 142 Beginning of RBCU operation 302 Peak containment pressure after blowdown N/A End of core reflood phase 535 Beginning of sump recirculation phase 4529 End of RB Spray/Beginning of re-circ spray 4529 End of S/G energy release N/A Depressurization of containment (1/2 of design pressure) within 2000 seconds (depending on RBCU assumptions)


Oconee Nuclear Station                                                                               UFSAR Table 6-25 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-25 (Page 1 of 1)
Table 6-25. Minimum Acceptable Combinations of Containment Heat Removal Equipment Performance Case                                     INPUT ASSUMPTIONS                                                       RESULTS No.          LPI Overall Ht     RBCU    LPSW      Rx Bldg Temp  RBS (inj phase) RBS (recirc phase)      T (1 day)      T (15 days)
(31 DEC 2017)
Transfer Coeff @250F LPI (Btu/hr-ft2-ºF)   (MBtu/hr) (ºF)         (ºF)         (gpm)           (gpm)                 (ºF)           (ºF)
Table 6-25. Minimum Acceptable Combinations of Containment Heat Removal Equipment Performance Case No.
H-2-25           250           105.79   90           130           700             900                 180.8           140.2 (31 DEC 2017)
INPUT ASSUMPTIONS RESULTS LPI Overall Ht Transfer Coeff @250F LPI (Btu/hr-ft2-ºF)
RBCU (MBtu/hr)
LPSW
(ºF)
Rx Bldg Temp
(ºF)
RBS (inj phase)
(gpm)
RBS (recirc phase)
(gpm)
T (1 day)
(ºF)
T (15 days)
(ºF)
H-2-25 250 105.79 90 130 700 900 180.8 140.2  


Oconee Nuclear Station                                                                       UFSAR Table 6-26 (Page 1 of 2)
Oconee Nuclear Station UFSAR Table 6-26 (Page 1 of 2)
Table 6-26. Engineered Safety Feature Assumptions in Containment Response Analyses Passive safety injection system                           Full Capacity     Large LOCA Large LOCA        Steam Line Short-Term Long-Term           Break Number of core flood tanks                                     2               N/A         2                 2 Core flood tank pressure setpoint (psig)                       600             N/A       655               550 Active safety injection systems Number of HPI lines                                             2               N/A         1                 1 Number of HPI pumps                                             3               N/A         2                 2 HPI flow rate (gpm/pump)                                       300             N/A     variable         variable Number of LPI lines                                             2               N/A         1                 1 Number of LPI pumps                                             3               N/A         1                 1 LPI flow rate (gpm/pump)                                       3000             N/A     variable             N/A Containment spray system Number of injection spray lines                                 2               N/A         1                 1 Number of injection spray pumps                                 2               N/A         1                 1 Number of injection spray headers                               2               N/A         1                 1 Injection flow rate (gpm/pump)                             700-1200           N/A       700               700 Number of recirculation spray lines                             2               N/A         1                 N/A Number of recirculation spray pumps                             2               N/A         1                 N/A Number of recirculation spray headers                           2               N/A         1                 N/A Recirculation flow rate (gpm/pump)                             1000             N/A       900               N/A Containment fan cooler system Number of coolers (RBCUs)                                       3               N/A         2                 2 Air side flow rate per RBCU (cfm)                           108,000           N/A       54,000           54,000 (31 DEC 2013)
(31 DEC 2013)
Table 6-26. Engineered Safety Feature Assumptions in Containment Response Analyses Passive safety injection system Full Capacity Large LOCA Short-Term Large LOCA Long-Term Steam Line Break Number of core flood tanks 2
N/A 2
2 Core flood tank pressure setpoint (psig) 600 N/A 655 550 Active safety injection systems Number of HPI lines 2
N/A 1
1 Number of HPI pumps 3
N/A 2
2 HPI flow rate (gpm/pump) 300 N/A variable variable Number of LPI lines 2
N/A 1
1 Number of LPI pumps 3
N/A 1
1 LPI flow rate (gpm/pump) 3000 N/A variable N/A Containment spray system Number of injection spray lines 2
N/A 1
1 Number of injection spray pumps 2
N/A 1
1 Number of injection spray headers 2
N/A 1
1 Injection flow rate (gpm/pump) 700-1200 N/A 700 700 Number of recirculation spray lines 2
N/A 1
N/A Number of recirculation spray pumps 2
N/A 1
N/A Number of recirculation spray headers 2
N/A 1
N/A Recirculation flow rate (gpm/pump) 1000 N/A 900 N/A Containment fan cooler system Number of coolers (RBCUs) 3 N/A 2
2 Air side flow rate per RBCU (cfm) 108,000 N/A 54,000 54,000  


Oconee Nuclear Station                                                                       UFSAR Table 6-26 (Page 2 of 2)
Oconee Nuclear Station UFSAR Table 6-26 (Page 2 of 2)
Heat removal rate at design temperature (millions of Btu/hr)       80           N/A     variable         variable Heat Exchangers                                             Full Capacity Large LOCA Large LOCA       Steam Line Short-Term Long-Term           Break System                                                           LPI           N/A       LPI               N/A Type                                                           U-tube         N/A       U-tube             N/A Number                                                             2           N/A         1                 N/A 2
(31 DEC 2013)
Heat transfer area (ft )                                         3986         N/A       3900               N/A Heat removal rate at design temperature (millions of Btu/hr)       60           N/A     variable             N/A Recirculation side flow rate (gpm)                               6000         N/A       2830               N/A Exterior side flow rate (gpm)                                     6000         N/A       5000               N/A Source of cooling water                                         LPSW           N/A       LPSW               N/A Cooling begins (sec)                                         not calculated     N/A       5467               N/A Deleted row (s) per 2011 update (31 DEC 2013)
Heat removal rate at design temperature (millions of Btu/hr) 80 N/A variable variable Heat Exchangers Full Capacity Large LOCA Short-Term Large LOCA Long-Term Steam Line Break System LPI N/A LPI N/A Type U-tube N/A U-tube N/A Number 2
N/A 1
N/A Heat transfer area (ft2) 3986 N/A 3900 N/A Heat removal rate at design temperature (millions of Btu/hr) 60 N/A variable N/A Recirculation side flow rate (gpm) 6000 N/A 2830 N/A Exterior side flow rate (gpm) 6000 N/A 5000 N/A Source of cooling water LPSW N/A LPSW N/A Cooling begins (sec) not calculated N/A 5467 N/A Deleted row (s) per 2011 update  


Oconee Nuclear Station                                                                             UFSAR Table 6-27 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-27 (Page 1 of 1)
Table 6-27. Summary of Calculated Containment Pressures and Temperatures for Secondary System Pipe Rupture Cases Energy Released to Containment up to Time of Peak        End of Blowdown Break Location         Break Size         Peak Pressure (psig) Peak Temperature (F) Pressure (sec)       (106Btu)
(31 DEC 2008)
Deleted row(s) per 2008 update S/G outlet             12.6               58.85               464                   156                 291 (31 DEC 2008)
Table 6-27. Summary of Calculated Containment Pressures and Temperatures for Secondary System Pipe Rupture Cases Break Location Break Size Peak Pressure (psig)
Peak Temperature (F)
Time of Peak Pressure (sec)
Energy Released to Containment up to End of Blowdown (106Btu)
Deleted row(s) per 2008 update S/G outlet 12.6 58.85 464 156 291  


Oconee Nuclear Station                                             UFSAR Table 6-28 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-28 (Page 1 of 1)
(31 DEC 2000)
Table 6-28. Steam Generator Compartment Pressure Response Flowpath Discharge Coefficients Flow Area (ft2)
Table 6-28. Steam Generator Compartment Pressure Response Flowpath Discharge Coefficients Flow Area (ft2)
Vent Flowpath       West Compartment         East Compartment     Discharge Coefficients Location Top                             528                       417         (Figure 6-46)
Vent Flowpath Location West Compartment East Compartment Discharge Coefficients Top 528 417 (Figure 6-46)
Bottom                         522                       522         0.85 Cross Compartment               116                       116         (Figure 6-47)
Bottom 522 522 0.85 Cross Compartment 116 116 (Figure 6-47)
Cross Compartment               167                       167         0.60 2                          2 Total                         1,333 ft                  1,222 ft (31 DEC 2000)
Cross Compartment 167 167 0.60 Total 1,333 ft2 1,222 ft2


Oconee Nuclear Station                                                                     UFSAR Table 6-29 (Page 1 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 1 of 15)
Table 6-29. Peak Pressure Mass and Energy Release Data Reactor Vessel Side                                 Steam Generator Side Liquid                                            Liquid Gas Mass      Gas        Mass      Liquid          Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow    Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 0.0       3010.01     1184.97   49671.97     582.17   2193.5   3285.7   1185.3   53516.7     582.0         2194.5 0.1       3292.43     1186.06   48890.57     578.04 1181.629   3595.0   1186.3   50971.8     577.1         1197.0 0.2       3514.61     1187.31   47678.99     574.34 1159.982   3628.0   1188.2   46317.2     572.9         1107.1 0.3       3543.37     1188.18   44653.10     572.03 1110.159   3397.0   1190.1   41300.8     572.3         1029.7 0.4       3630.87     1189.37   40559.81     567.41   1049.93   3693.9   1191.7   35278.7     566.8         976.9 0.5       3635.68     1190.27   38647.09     565.67 1034.564   4278.5   1195.5   31515.0     552.9         936.0 0.6       3648.05     1190.44   38356.02     565.55 1035.154   4962.8   1201.0   30910.8     531.2         856.1 0.7       3669.39     1190.34   38597.74     565.83 1038.666   5331.4   1204.5   29974.4     516.3         804.5 0.8       3718.86     1190.34   38499.13     565.82 1039.054   5240.4   1205.9   28512.6     508.7         755.2 0.9       3792.57     1190.46   38007.04     565.60 1035.513   4979.0   1206.5   27982.4     503.2         731.9 1.0       3894.59     1190.67   37243.49     565.28 1032.616   4666.8   1206.5   28170.5     500.4         718.2 1.1       4040.05     1191.05   36056.67     564.56 1024.747   4338.3   1206.1   28843.6     499.1         714.5 1.2       4207.73     1191.60   34568.39     563.29 1013.115   4009.4   1205.6   29806.0     498.8         716.5 1.3       4365.54     1192.20   33138.08     561.69 1000.073   3717.0   1205.0   30817.1     499.0         720.2 1.4       4993.88     1195.85   32492.03     552.24 989.5376   3479.8   1204.6   31694.5     499.3         723.7 1.5       5680.12     1199.71   30794.20     538.92 875.3103   3300.6   1204.3   32345.0     499.5         726.3 1.6       5890.87     1201.23   29217.68     532.83 910.9592   3181.6   1204.1   32666.4     499.7         728.1 1.7       6230.52     1203.24   28865.65     528.18   886.991   3106.0   1204.0   32723.4     499.8         729.0 1.8       6589.77     1206.18   26964.95     519.59 803.0924   3052.9   1203.9   32680.9     499.6         728.4 (31 DEC 2003)
(31 DEC 2003)
Table 6-29. Peak Pressure Mass and Energy Release Data Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 0.0 3010.01 1184.97 49671.97 582.17 2193.5 3285.7 1185.3 53516.7 582.0 2194.5 0.1 3292.43 1186.06 48890.57 578.04 1181.629 3595.0 1186.3 50971.8 577.1 1197.0 0.2 3514.61 1187.31 47678.99 574.34 1159.982 3628.0 1188.2 46317.2 572.9 1107.1 0.3 3543.37 1188.18 44653.10 572.03 1110.159 3397.0 1190.1 41300.8 572.3 1029.7 0.4 3630.87 1189.37 40559.81 567.41 1049.93 3693.9 1191.7 35278.7 566.8 976.9 0.5 3635.68 1190.27 38647.09 565.67 1034.564 4278.5 1195.5 31515.0 552.9 936.0 0.6 3648.05 1190.44 38356.02 565.55 1035.154 4962.8 1201.0 30910.8 531.2 856.1 0.7 3669.39 1190.34 38597.74 565.83 1038.666 5331.4 1204.5 29974.4 516.3 804.5 0.8 3718.86 1190.34 38499.13 565.82 1039.054 5240.4 1205.9 28512.6 508.7 755.2 0.9 3792.57 1190.46 38007.04 565.60 1035.513 4979.0 1206.5 27982.4 503.2 731.9 1.0 3894.59 1190.67 37243.49 565.28 1032.616 4666.8 1206.5 28170.5 500.4 718.2 1.1 4040.05 1191.05 36056.67 564.56 1024.747 4338.3 1206.1 28843.6 499.1 714.5 1.2 4207.73 1191.60 34568.39 563.29 1013.115 4009.4 1205.6 29806.0 498.8 716.5 1.3 4365.54 1192.20 33138.08 561.69 1000.073 3717.0 1205.0 30817.1 499.0 720.2 1.4 4993.88 1195.85 32492.03 552.24 989.5376 3479.8 1204.6 31694.5 499.3 723.7 1.5 5680.12 1199.71 30794.20 538.92 875.3103 3300.6 1204.3 32345.0 499.5 726.3 1.6 5890.87 1201.23 29217.68 532.83 910.9592 3181.6 1204.1 32666.4 499.7 728.1 1.7 6230.52 1203.24 28865.65 528.18 886.991 3106.0 1204.0 32723.4 499.8 729.0 1.8 6589.77 1206.18 26964.95 519.59 803.0924 3052.9 1203.9 32680.9 499.6 728.4  


Oconee Nuclear Station                                                                     UFSAR Table 6-29 (Page 2 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 2 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 1.9       6793.44     1208.29   24854.61   512.88 762.0923   3020.8   1203.9   32600.2     499.2         726.3 2.0       6987.48     1209.57   23543.95   509.93 757.0142   3010.7   1204.0   32499.2     498.5         722.8 2.1       7049.20     1210.37   22700.01   507.46 732.7446   3020.8   1204.1   32356.9     497.7         717.8 2.2       6982.30     1210.71   22352.82   505.43 722.8103   3050.3   1204.4   32131.9     496.6         711.7 2.3       6929.43     1211.04   21991.46   503.58   712.88   3106.2   1204.6   31730.6     495.4         705.0 2.4       6926.97     1211.55   21424.15   501.60 700.4492   3181.4   1204.9   31161.7     494.3         698.2 2.5       6972.51     1212.27   20638.07   499.39 686.8077   3257.5   1205.1   30565.0     493.1         691.1 2.6       7045.78     1213.19   19690.63   496.92 670.8762   3329.2   1205.4   29990.4     491.9         684.3 2.7       7104.95     1214.14   18744.18   494.28 653.8654   3396.4   1205.7   29409.8     490.6         677.1 2.8       7120.03     1214.90   17983.51   491.78 638.7917   3460.7   1206.0   28798.3     489.2         669.3 2.9       7090.58     1215.41   17449.85   489.58 626.4775   3523.6   1206.3   28153.2     487.6         660.6 3.0       7024.28     1215.70   17117.19   487.66 616.2853   3586.2   1206.7   27480.8     486.0         651.3 3.1       6931.13     1215.78   16983.97   486.12 608.9916   3650.1   1207.0   26806.2     484.1         641.6 3.2       6827.70     1215.69   16999.04   484.98 604.6638   3707.1   1207.4   26140.4     482.1         629.7 3.3       6723.07     1215.54   17071.12   484.04 601.1656   3751.8   1207.7   25494.8     480.1         619.2 3.4       6617.46     1215.36   17164.90   483.17 598.1012   3787.5   1208.0   24906.0     478.3         609.5 3.5       6513.70     1215.16   17283.34   482.42 595.6895   3819.2   1208.3   24363.3     476.7         601.6 3.6       6410.98     1214.94   17419.40   481.73 593.6919   3851.2   1208.6   23822.7     475.1         593.5 3.7       6306.66     1214.70   17580.36   481.12 592.0447   3885.2   1208.9   23248.5     473.4         584.7 3.8       6197.66     1214.45   17746.44   480.48 590.5136   3928.3   1209.2   22613.2     471.6         575.1 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 1.9 6793.44 1208.29 24854.61 512.88 762.0923 3020.8 1203.9 32600.2 499.2 726.3 2.0 6987.48 1209.57 23543.95 509.93 757.0142 3010.7 1204.0 32499.2 498.5 722.8 2.1 7049.20 1210.37 22700.01 507.46 732.7446 3020.8 1204.1 32356.9 497.7 717.8 2.2 6982.30 1210.71 22352.82 505.43 722.8103 3050.3 1204.4 32131.9 496.6 711.7 2.3 6929.43 1211.04 21991.46 503.58 712.88 3106.2 1204.6 31730.6 495.4 705.0 2.4 6926.97 1211.55 21424.15 501.60 700.4492 3181.4 1204.9 31161.7 494.3 698.2 2.5 6972.51 1212.27 20638.07 499.39 686.8077 3257.5 1205.1 30565.0 493.1 691.1 2.6 7045.78 1213.19 19690.63 496.92 670.8762 3329.2 1205.4 29990.4 491.9 684.3 2.7 7104.95 1214.14 18744.18 494.28 653.8654 3396.4 1205.7 29409.8 490.6 677.1 2.8 7120.03 1214.90 17983.51 491.78 638.7917 3460.7 1206.0 28798.3 489.2 669.3 2.9 7090.58 1215.41 17449.85 489.58 626.4775 3523.6 1206.3 28153.2 487.6 660.6 3.0 7024.28 1215.70 17117.19 487.66 616.2853 3586.2 1206.7 27480.8 486.0 651.3 3.1 6931.13 1215.78 16983.97 486.12 608.9916 3650.1 1207.0 26806.2 484.1 641.6 3.2 6827.70 1215.69 16999.04 484.98 604.6638 3707.1 1207.4 26140.4 482.1 629.7 3.3 6723.07 1215.54 17071.12 484.04 601.1656 3751.8 1207.7 25494.8 480.1 619.2 3.4 6617.46 1215.36 17164.90 483.17 598.1012 3787.5 1208.0 24906.0 478.3 609.5 3.5 6513.70 1215.16 17283.34 482.42 595.6895 3819.2 1208.3 24363.3 476.7 601.6 3.6 6410.98 1214.94 17419.40 481.73 593.6919 3851.2 1208.6 23822.7 475.1 593.5 3.7 6306.66 1214.70 17580.36 481.12 592.0447 3885.2 1208.9 23248.5 473.4 584.7 3.8 6197.66 1214.45 17746.44 480.48 590.5136 3928.3 1209.2 22613.2 471.6 575.1  


Oconee Nuclear Station                                                                     UFSAR Table 6-29 (Page 3 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 3 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 3.9       6091.36     1214.23   17887.72   479.78 588.2765   3975.1   1209.6   21950.0     469.7         565.2 4.0       5999.57     1214.06   17982.71   479.08 586.2639   4013.3   1209.9   21316.9     467.8         555.6 4.1       5919.56     1213.96   17999.05   478.23 582.8126   4041.9   1210.2   20723.0     465.9         546.1 4.2       5850.31     1213.91   17975.75   477.35 578.8416   4063.8   1210.5   20159.5     464.1         536.9 4.3       5785.93     1213.86   17948.31   476.51 575.8641   4081.9   1210.8   19619.1     462.2         527.8 4.4       5719.81     1213.82   17907.76   475.59 571.6936   4097.2   1211.1   19096.9     460.4         519.1 4.5       5657.05     1213.79   17859.65   474.68 567.8912   4109.7   1211.3   18589.4     458.6         510.5 4.6       5601.93     1213.77   17801.33   473.81 564.1906   4120.8   1211.6   18096.4     456.8         501.9 4.7       5556.08     1213.79   17707.59   472.91 560.3049   4130.3   1211.8   17625.7     455.1         493.9 4.8       5521.32     1213.86   17560.69   471.95 555.8145   4135.5   1212.1   17179.0     453.4         486.0 4.9       5497.49     1213.99   17366.12   470.94 550.9728   4136.0   1212.3   16743.6     451.7         478.2 5.0       5479.21     1214.14   17138.19   469.87 545.6119   4135.3   1212.5   16305.3     450.0         470.1 5.1       5461.59     1214.30   16903.19   468.77 540.1775   4138.0   1212.8   15863.6     448.2         462.2 5.2       5458.31     1214.41   16753.36   468.13 534.9559   4144.7   1213.0   15424.4     446.6         454.6 5.3       5452.41     1214.50   16629.87   467.58   537.133   4154.3   1213.3   14993.1     445.0         447.2 5.4       5418.88     1214.63   16392.82   466.31 527.8124   4167.1   1213.5   14579.1     443.5         440.3 5.5       5377.81     1214.79   16119.89   464.77 520.9561   4179.8   1213.8   14186.3     442.0         433.9 5.6       5331.54     1214.88   15926.04   463.43 514.8933   4187.2   1214.0   13802.8     440.6         427.4 5.7       5270.87     1214.87   15832.54   462.28 510.2204   4191.7   1214.2   13411.3     439.1         420.5 5.8       5202.57     1214.79   15800.48   461.26 506.3772   4199.3   1214.5   12999.4     437.5         413.4 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 3.9 6091.36 1214.23 17887.72 479.78 588.2765 3975.1 1209.6 21950.0 469.7 565.2 4.0 5999.57 1214.06 17982.71 479.08 586.2639 4013.3 1209.9 21316.9 467.8 555.6 4.1 5919.56 1213.96 17999.05 478.23 582.8126 4041.9 1210.2 20723.0 465.9 546.1 4.2 5850.31 1213.91 17975.75 477.35 578.8416 4063.8 1210.5 20159.5 464.1 536.9 4.3 5785.93 1213.86 17948.31 476.51 575.8641 4081.9 1210.8 19619.1 462.2 527.8 4.4 5719.81 1213.82 17907.76 475.59 571.6936 4097.2 1211.1 19096.9 460.4 519.1 4.5 5657.05 1213.79 17859.65 474.68 567.8912 4109.7 1211.3 18589.4 458.6 510.5 4.6 5601.93 1213.77 17801.33 473.81 564.1906 4120.8 1211.6 18096.4 456.8 501.9 4.7 5556.08 1213.79 17707.59 472.91 560.3049 4130.3 1211.8 17625.7 455.1 493.9 4.8 5521.32 1213.86 17560.69 471.95 555.8145 4135.5 1212.1 17179.0 453.4 486.0 4.9 5497.49 1213.99 17366.12 470.94 550.9728 4136.0 1212.3 16743.6 451.7 478.2 5.0 5479.21 1214.14 17138.19 469.87 545.6119 4135.3 1212.5 16305.3 450.0 470.1 5.1 5461.59 1214.30 16903.19 468.77 540.1775 4138.0 1212.8 15863.6 448.2 462.2 5.2 5458.31 1214.41 16753.36 468.13 534.9559 4144.7 1213.0 15424.4 446.6 454.6 5.3 5452.41 1214.50 16629.87 467.58 537.133 4154.3 1213.3 14993.1 445.0 447.2 5.4 5418.88 1214.63 16392.82 466.31 527.8124 4167.1 1213.5 14579.1 443.5 440.3 5.5 5377.81 1214.79 16119.89 464.77 520.9561 4179.8 1213.8 14186.3 442.0 433.9 5.6 5331.54 1214.88 15926.04 463.43 514.8933 4187.2 1214.0 13802.8 440.6 427.4 5.7 5270.87 1214.87 15832.54 462.28 510.2204 4191.7 1214.2 13411.3 439.1 420.5 5.8 5202.57 1214.79 15800.48 461.26 506.3772 4199.3 1214.5 12999.4 437.5 413.4  


Oconee Nuclear Station                                                                     UFSAR Table 6-29 (Page 4 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 4 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 5.9       5136.92     1214.70   15777.82   460.32 502.8705   4214.5   1214.9   12544.7     435.8         406.0 6.0       5084.95     1214.66   15709.59   459.38 499.2031   4227.8   1215.2   12095.1     434.1         398.1 6.1       5058.63     1214.74   15535.22   458.37 494.8307   4233.7   1215.5   11685.9     432.5         391.1 6.2       5061.77     1214.98   15214.89   457.19   488.941   4238.8   1215.8   11282.6     430.9         383.9 6.3       5087.59     1215.37   14763.62   455.79 481.5992   4242.2   1216.2   10887.3     429.3         376.9 6.4       5126.83     1215.87   14229.35   454.24 473.1572   4243.0   1216.5   10506.6     427.7         370.0 6.5       5166.82     1216.43   13671.74   452.60 464.2117   4241.2   1216.8   10139.1     426.1         363.3 6.6       5199.58     1216.96   13143.25   450.96 455.6055   4236.9   1217.0     9782.5     424.5         356.6 6.7       5225.96     1217.46   12655.68   449.39 447.4246   4230.4   1217.3     9435.8     422.9         349.9 6.8       5248.35     1217.96   12194.42   447.88 439.5559   4221.9   1217.6     9097.6     421.3         343.4 6.9       5268.13     1218.45   11744.27   446.39 431.8085   4211.2   1217.9     8767.5     419.7         336.9 7.0       5285.42     1218.94   11299.63   444.91 424.1094   4197.9   1218.1     8446.1     418.1         330.4 7.1       5300.02     1219.44   10861.96   443.41 416.4128   4182.1   1218.4     8134.4     416.5         324.0 7.2       5312.88     1219.96   10430.75   441.92 408.7826   4163.6   1218.7     7835.1     414.9         317.6 7.3       5325.34     1220.51     9998.25   440.43 401.1175   4142.7   1219.0     7549.3     413.3         311.4 7.4       5335.32     1221.08     9568.11   438.92 393.3681   4119.8   1219.2     7275.8     411.7         305.4 7.5       5339.94     1221.65     9151.08   437.39 385.6325   4094.8   1219.5     7015.1     410.1         299.5 7.6       5338.68     1222.21     8748.44   435.83 377.9228   4068.1   1219.7     6768.1     408.5         293.7 7.7       5332.27     1222.75     8363.09   434.27   370.244   4039.8   1219.9     6534.3     406.9         288.1 7.8       5321.04     1223.26     7998.24   432.72 363.0505   4010.1   1220.1     6313.3     405.4         282.8 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 5.9 5136.92 1214.70 15777.82 460.32 502.8705 4214.5 1214.9 12544.7 435.8 406.0 6.0 5084.95 1214.66 15709.59 459.38 499.2031 4227.8 1215.2 12095.1 434.1 398.1 6.1 5058.63 1214.74 15535.22 458.37 494.8307 4233.7 1215.5 11685.9 432.5 391.1 6.2 5061.77 1214.98 15214.89 457.19 488.941 4238.8 1215.8 11282.6 430.9 383.9 6.3 5087.59 1215.37 14763.62 455.79 481.5992 4242.2 1216.2 10887.3 429.3 376.9 6.4 5126.83 1215.87 14229.35 454.24 473.1572 4243.0 1216.5 10506.6 427.7 370.0 6.5 5166.82 1216.43 13671.74 452.60 464.2117 4241.2 1216.8 10139.1 426.1 363.3 6.6 5199.58 1216.96 13143.25 450.96 455.6055 4236.9 1217.0 9782.5 424.5 356.6 6.7 5225.96 1217.46 12655.68 449.39 447.4246 4230.4 1217.3 9435.8 422.9 349.9 6.8 5248.35 1217.96 12194.42 447.88 439.5559 4221.9 1217.6 9097.6 421.3 343.4 6.9 5268.13 1218.45 11744.27 446.39 431.8085 4211.2 1217.9 8767.5 419.7 336.9 7.0 5285.42 1218.94 11299.63 444.91 424.1094 4197.9 1218.1 8446.1 418.1 330.4 7.1 5300.02 1219.44 10861.96 443.41 416.4128 4182.1 1218.4 8134.4 416.5 324.0 7.2 5312.88 1219.96 10430.75 441.92 408.7826 4163.6 1218.7 7835.1 414.9 317.6 7.3 5325.34 1220.51 9998.25 440.43 401.1175 4142.7 1219.0 7549.3 413.3 311.4 7.4 5335.32 1221.08 9568.11 438.92 393.3681 4119.8 1219.2 7275.8 411.7 305.4 7.5 5339.94 1221.65 9151.08 437.39 385.6325 4094.8 1219.5 7015.1 410.1 299.5 7.6 5338.68 1222.21 8748.44 435.83 377.9228 4068.1 1219.7 6768.1 408.5 293.7 7.7 5332.27 1222.75 8363.09 434.27 370.244 4039.8 1219.9 6534.3 406.9 288.1 7.8 5321.04 1223.26 7998.24 432.72 363.0505 4010.1 1220.1 6313.3 405.4 282.8  


Oconee Nuclear Station                                                                     UFSAR Table 6-29 (Page 5 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 5 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 7.9       5303.07     1223.73     7652.23   431.15 355.3909   3979.5   1220.3     6103.5     403.9         277.5 8.0       5280.96     1224.18     7327.65   429.60 348.3742   3949.0   1220.4     5902.4     402.4         272.5 8.1       5255.83     1224.61     7021.56   428.07 341.5477   3919.4   1220.6     5705.6     401.0         267.6 8.2       5222.98     1225.02     6721.74   426.45 334.4929   3888.6   1220.8     5505.3     399.5         262.7 8.3       5178.24     1225.42     6421.44   424.64   326.976   3830.0   1220.8     5307.4     397.5         256.6 8.4       5121.44     1225.79     6125.63   422.63 318.8619   3733.0   1220.5     5167.8     394.9         249.3 8.5       5056.17     1226.14     5837.72   420.50 310.7606   3634.5   1220.1     5061.3     392.4         243.5 8.6       4982.49     1226.47     5555.02   418.23   302.328   3564.0   1220.0     4863.4     390.1         237.0 8.7       4898.50     1226.75     5286.03   415.81 293.5971   3523.9   1220.5     4527.7     387.7         229.0 8.8       4808.09     1226.93     5044.59   413.34 285.3314   3502.3   1221.3     4096.3     385.3         219.9 8.9       4711.35     1227.00     4833.97   410.86   277.262   3479.2   1222.3     3639.8     382.7         210.2 9.0       4606.88     1226.95     4657.63   408.31 269.5202   3436.9   1223.2     3223.6     379.9         200.3 9.1       4500.25     1226.80     4515.59   405.81 262.4702   3367.1   1223.8     2891.7     376.8         190.9 9.2       4393.63     1226.56     4395.57   403.35 255.7832   3271.4   1223.9     2665.5     373.5         182.4 9.3       4285.60     1226.25     4292.05   400.89   249.39   3159.3   1223.5     2537.1     370.1         175.4 9.4       4172.87     1225.85     4206.82   398.35 243.1775   3043.6   1222.8     2464.3     366.8         169.2 9.5       4056.84     1225.37     4138.37   395.77 236.9903   2935.8   1222.0     2423.7     363.8         164.0 9.6       3947.57     1224.86     4087.16   393.33 231.5702   2840.2   1221.2     2389.4     361.1         159.6 9.7       3835.90     1224.30     4041.69   390.82 226.4181   2761.6   1220.7     2326.7     358.6         154.9 9.8       3723.65     1223.79     3970.26   388.15 220.1975   2702.5   1220.5     2239.8     356.6         151.0 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 7.9 5303.07 1223.73 7652.23 431.15 355.3909 3979.5 1220.3 6103.5 403.9 277.5 8.0 5280.96 1224.18 7327.65 429.60 348.3742 3949.0 1220.4 5902.4 402.4 272.5 8.1 5255.83 1224.61 7021.56 428.07 341.5477 3919.4 1220.6 5705.6 401.0 267.6 8.2 5222.98 1225.02 6721.74 426.45 334.4929 3888.6 1220.8 5505.3 399.5 262.7 8.3 5178.24 1225.42 6421.44 424.64 326.976 3830.0 1220.8 5307.4 397.5 256.6 8.4 5121.44 1225.79 6125.63 422.63 318.8619 3733.0 1220.5 5167.8 394.9 249.3 8.5 5056.17 1226.14 5837.72 420.50 310.7606 3634.5 1220.1 5061.3 392.4 243.5 8.6 4982.49 1226.47 5555.02 418.23 302.328 3564.0 1220.0 4863.4 390.1 237.0 8.7 4898.50 1226.75 5286.03 415.81 293.5971 3523.9 1220.5 4527.7 387.7 229.0 8.8 4808.09 1226.93 5044.59 413.34 285.3314 3502.3 1221.3 4096.3 385.3 219.9 8.9 4711.35 1227.00 4833.97 410.86 277.262 3479.2 1222.3 3639.8 382.7 210.2 9.0 4606.88 1226.95 4657.63 408.31 269.5202 3436.9 1223.2 3223.6 379.9 200.3 9.1 4500.25 1226.80 4515.59 405.81 262.4702 3367.1 1223.8 2891.7 376.8 190.9 9.2 4393.63 1226.56 4395.57 403.35 255.7832 3271.4 1223.9 2665.5 373.5 182.4 9.3 4285.60 1226.25 4292.05 400.89 249.39 3159.3 1223.5 2537.1 370.1 175.4 9.4 4172.87 1225.85 4206.82 398.35 243.1775 3043.6 1222.8 2464.3 366.8 169.2 9.5 4056.84 1225.37 4138.37 395.77 236.9903 2935.8 1222.0 2423.7 363.8 164.0 9.6 3947.57 1224.86 4087.16 393.33 231.5702 2840.2 1221.2 2389.4 361.1 159.6 9.7 3835.90 1224.30 4041.69 390.82 226.4181 2761.6 1220.7 2326.7 358.6 154.9 9.8 3723.65 1223.79 3970.26 388.15 220.1975 2702.5 1220.5 2239.8 356.6 151.0  


Oconee Nuclear Station                                                                     UFSAR Table 6-29 (Page 6 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 6 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow      Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (Btu/lbm)       (psi) 9.9       3637.49     1223.53     3852.26   385.81 214.6207   2655.9   1220.6     2113.9     354.7         146.8 10.0       3574.11     1223.47     3707.97   383.83 209.3918   2612.7   1220.9     1954.7     352.7         141.6 10.1       3516.03     1223.39     3588.09   382.03 204.7022   2568.8   1221.1     1814.3     350.7         137.2 10.2       3453.19     1223.16     3511.79   380.28 200.9402   2529.7   1221.5     1663.8     348.9         132.8 10.3       3387.37     1222.85     3449.77   378.51 197.0519   2502.7   1222.4     1463.3     347.3         127.5 10.4       3332.71     1222.68     3368.08   376.89 193.3959   2478.7   1223.5     1269.5     345.8         122.5 10.5       3291.35     1222.70     3256.39   375.45 189.7945   2451.0   1224.3     1115.5     344.4         118.4 10.6       3252.54     1222.80     3126.88   373.98 185.8833   2433.4   1225.5     959.8     343.3         114.4 10.7       3209.24     1222.88     2997.81   372.40 181.8303   2427.7   1227.2     776.2     342.7         110.4 10.8       3159.90     1222.89     2878.73   370.69 177.7135   2414.3   1229.0     598.8     342.1         105.9 10.9       3102.83     1222.81     2767.53   368.80 173.5954   2375.7   1229.9     481.5     340.7         101.7 11.0       3022.52     1222.51     2652.96   366.29 168.4726   2316.7   1229.9     432.5     338.6         98.3 11.1       2921.69     1222.01     2534.35   363.17 162.1219   2258.8   1229.5     408.8     336.6         95.6 11.2       2841.36     1221.68     2419.12   360.53 156.5801   2215.6   1229.5     367.6     335.1         93.0 11.3       2784.73     1221.45     2336.24   358.61 153.2978   2187.5   1230.1     299.6     334.1         90.4 11.4       2721.38     1221.00     2289.86   356.65 150.1807   2167.0   1231.1     219.2     333.3         87.8 11.5       2647.53     1220.47     2225.48   354.32 146.3128   2139.3   1231.8     148.1     332.4         85.3 11.6       2571.92     1219.92     2152.39   351.83 141.5976   2029.6   1226.9     103.5     328.2         82.5 11.7       2488.89     1219.16     2103.44   349.18 138.5105   1909.2   1219.9       86.3     322.5         89.6 11.8       2367.60     1217.94     2038.88   345.28 132.5417   1857.9   1217.9     82.1       320.5         88.9 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 9.9 3637.49 1223.53 3852.26 385.81 214.6207 2655.9 1220.6 2113.9 354.7 146.8 10.0 3574.11 1223.47 3707.97 383.83 209.3918 2612.7 1220.9 1954.7 352.7 141.6 10.1 3516.03 1223.39 3588.09 382.03 204.7022 2568.8 1221.1 1814.3 350.7 137.2 10.2 3453.19 1223.16 3511.79 380.28 200.9402 2529.7 1221.5 1663.8 348.9 132.8 10.3 3387.37 1222.85 3449.77 378.51 197.0519 2502.7 1222.4 1463.3 347.3 127.5 10.4 3332.71 1222.68 3368.08 376.89 193.3959 2478.7 1223.5 1269.5 345.8 122.5 10.5 3291.35 1222.70 3256.39 375.45 189.7945 2451.0 1224.3 1115.5 344.4 118.4 10.6 3252.54 1222.80 3126.88 373.98 185.8833 2433.4 1225.5 959.8 343.3 114.4 10.7 3209.24 1222.88 2997.81 372.40 181.8303 2427.7 1227.2 776.2 342.7 110.4 10.8 3159.90 1222.89 2878.73 370.69 177.7135 2414.3 1229.0 598.8 342.1 105.9 10.9 3102.83 1222.81 2767.53 368.80 173.5954 2375.7 1229.9 481.5 340.7 101.7 11.0 3022.52 1222.51 2652.96 366.29 168.4726 2316.7 1229.9 432.5 338.6 98.3 11.1 2921.69 1222.01 2534.35 363.17 162.1219 2258.8 1229.5 408.8 336.6 95.6 11.2 2841.36 1221.68 2419.12 360.53 156.5801 2215.6 1229.5 367.6 335.1 93.0 11.3 2784.73 1221.45 2336.24 358.61 153.2978 2187.5 1230.1 299.6 334.1 90.4 11.4 2721.38 1221.00 2289.86 356.65 150.1807 2167.0 1231.1 219.2 333.3 87.8 11.5 2647.53 1220.47 2225.48 354.32 146.3128 2139.3 1231.8 148.1 332.4 85.3 11.6 2571.92 1219.92 2152.39 351.83 141.5976 2029.6 1226.9 103.5 328.2 82.5 11.7 2488.89 1219.16 2103.44 349.18 138.5105 1909.2 1219.9 86.3 322.5 89.6 11.8 2367.60 1217.94 2038.88 345.28 132.5417 1857.9 1217.9 82.1 320.5 88.9  


Oconee Nuclear Station                                                                     UFSAR Table 6-29 (Page 7 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 7 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 11.9       2211.88     1216.15     1985.77   340.13   125.396   1811.1   1216.6     74.3     318.8         88.0 12.0       2080.26     1214.41     1975.41   335.77 120.0252   1755.1   1215.1     62.1     316.7         86.8 12.1       1976.69     1212.96     1984.45   332.23 116.7781   1687.3   1213.3     52.1     314.2         85.5 12.2       1861.60     1211.18     2028.49   328.28 112.3925   1621.1   1211.6     45.5     311.7         84.3 12.3       1741.18     1209.23     2069.41   324.04 108.2196   1572.0   1210.3     41.4     309.9         83.4 12.4       1656.14     1207.86     2074.89   320.78 103.8234   1542.5   1209.5     39.3     308.9         83.0 12.5       1638.77     1207.62     2064.24   319.99 104.8238   1522.9   1209.0     39.2     308.2         82.7 12.6       1615.17     1207.37     2011.97   318.74 101.6428   1501.4   1208.4     43.4     307.4         82.4 12.7       1570.89     1206.86     1922.47   316.35 98.20489   1473.8   1207.6     46.0     306.5         82.1 12.8       1552.09     1206.91     1808.22   314.80 96.26216   1432.9   1206.5     41.1     305.1         81.5 12.9       1513.04     1206.70     1663.76   312.22 91.32984   1391.3   1205.4     34.5     303.6         80.6 13.0       1441.60     1205.89     1529.09   308.12 86.44714   1370.8   1204.9     29.9     302.8         80.4 13.1       1359.13     1204.64     1441.25   303.62   81.8531   1341.3   1204.2     27.2     301.8         80.1 13.2       1285.69     1202.69     1399.98   300.88 81.00603   1261.1   1202.2     24.5     299.1         78.9 13.3       1228.48     1200.84     1361.43   299.37 81.01533   1169.0   1201.0     21.8     296.1         77.8 13.4       1194.66     1200.05     1321.72   297.96 80.41002   1112.3   1201.4     21.8     294.3         77.3 13.5       1163.71     1199.33     1295.32   296.58 79.40754   1078.9   1201.6     26.5     293.4         76.9 13.6       1120.23     1198.26     1262.64   294.55   77.6799   1043.2   1201.0     31.8     292.3         77.1 13.7       1082.17     1197.28     1236.92   293.01 77.24097   985.0   1200.0     32.5     290.7         76.3 13.8       1050.36     1196.44     1226.41   292.06 76.99243   925.1   1199.6     32.2     289.0         75.9 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 11.9 2211.88 1216.15 1985.77 340.13 125.396 1811.1 1216.6 74.3 318.8 88.0 12.0 2080.26 1214.41 1975.41 335.77 120.0252 1755.1 1215.1 62.1 316.7 86.8 12.1 1976.69 1212.96 1984.45 332.23 116.7781 1687.3 1213.3 52.1 314.2 85.5 12.2 1861.60 1211.18 2028.49 328.28 112.3925 1621.1 1211.6 45.5 311.7 84.3 12.3 1741.18 1209.23 2069.41 324.04 108.2196 1572.0 1210.3 41.4 309.9 83.4 12.4 1656.14 1207.86 2074.89 320.78 103.8234 1542.5 1209.5 39.3 308.9 83.0 12.5 1638.77 1207.62 2064.24 319.99 104.8238 1522.9 1209.0 39.2 308.2 82.7 12.6 1615.17 1207.37 2011.97 318.74 101.6428 1501.4 1208.4 43.4 307.4 82.4 12.7 1570.89 1206.86 1922.47 316.35 98.20489 1473.8 1207.6 46.0 306.5 82.1 12.8 1552.09 1206.91 1808.22 314.80 96.26216 1432.9 1206.5 41.1 305.1 81.5 12.9 1513.04 1206.70 1663.76 312.22 91.32984 1391.3 1205.4 34.5 303.6 80.6 13.0 1441.60 1205.89 1529.09 308.12 86.44714 1370.8 1204.9 29.9 302.8 80.4 13.1 1359.13 1204.64 1441.25 303.62 81.8531 1341.3 1204.2 27.2 301.8 80.1 13.2 1285.69 1202.69 1399.98 300.88 81.00603 1261.1 1202.2 24.5 299.1 78.9 13.3 1228.48 1200.84 1361.43 299.37 81.01533 1169.0 1201.0 21.8 296.1 77.8 13.4 1194.66 1200.05 1321.72 297.96 80.41002 1112.3 1201.4 21.8 294.3 77.3 13.5 1163.71 1199.33 1295.32 296.58 79.40754 1078.9 1201.6 26.5 293.4 76.9 13.6 1120.23 1198.26 1262.64 294.55 77.6799 1043.2 1201.0 31.8 292.3 77.1 13.7 1082.17 1197.28 1236.92 293.01 77.24097 985.0 1200.0 32.5 290.7 76.3 13.8 1050.36 1196.44 1226.41 292.06 76.99243 925.1 1199.6 32.2 289.0 75.9  


Oconee Nuclear Station                                                                     UFSAR Table 6-29 (Page 8 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 8 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass      Gas      Mass      Liquid Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 13.9       1020.71     1195.68     1219.63   291.20   76.7229   886.0     1199.2     39.4     287.9         75.7 14.0       972.68     1194.51     1198.88   289.84 76.36981   866.2     1198.3     55.0     287.5         75.6 14.1       900.88     1192.79     1158.71   287.89 75.62348   862.1     1197.5     70.2     287.4         75.7 14.2       827.53     1191.10     1109.10   286.04 75.25019   857.7     1197.0     76.0     287.3         75.7 14.3       771.08     1189.85     1064.41   284.73 74.94771   825.2     1196.5     70.2     286.5         75.5 14.4       738.42     1189.16     1044.59   284.05 74.85709   764.6     1195.9     62.2     285.0         75.0 14.5       722.98     1188.85     1059.36   283.76   74.9034   700.9     1195.2     61.0     283.5         74.6 14.6       701.42     1188.44     1056.75   283.32   74.7923   638.2     1194.4     63.0     282.2         74.3 14.7       655.77     1187.63     961.10   282.40 74.49541   567.0     1193.5     62.7     281.0         74.4 14.8       585.34     1186.84     825.49   281.11   74.0854   483.4     1192.9     58.9     279.8         73.6 14.9       506.65     1186.41     727.80   279.85 73.87328   366.5     1192.3     49.7     278.4         73.4 15.0       445.48     1186.14     661.92   279.03   73.8341   210.5     1192.0     33.0     277.2         73.6 15.1       411.78     1185.81     619.64   278.64 73.87054   64.4     1192.0     12.5     276.6         73.5 15.2       385.86     1185.49     592.75   278.37 73.83266     1.1     1190.4       1.0     276.2         73.6 15.3       349.27     1185.30     554.67   278.03 73.74274     0.0     100.0       0.0       10.0         73.6 15.4       319.59     1185.20     507.41   277.77 73.76365     0.0     100.0       0.0       10.0         73.6 15.5       325.76     1185.22     498.53   277.98 73.77338     0.0     100.0       0.0       10.0         73.6 15.6       369.42     1184.78     575.30   278.45 74.58835     0.0     100.0       0.0       10.0         73.5 15.7       346.74     1184.61     584.43   278.21 73.66819     0.0     100.0       0.0       10.0         73.5 15.8       262.52     1184.94     466.55   277.51 73.63993     0.0     100.0       0.0       10.0         73.4 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 13.9 1020.71 1195.68 1219.63 291.20 76.7229 886.0 1199.2 39.4 287.9 75.7 14.0 972.68 1194.51 1198.88 289.84 76.36981 866.2 1198.3 55.0 287.5 75.6 14.1 900.88 1192.79 1158.71 287.89 75.62348 862.1 1197.5 70.2 287.4 75.7 14.2 827.53 1191.10 1109.10 286.04 75.25019 857.7 1197.0 76.0 287.3 75.7 14.3 771.08 1189.85 1064.41 284.73 74.94771 825.2 1196.5 70.2 286.5 75.5 14.4 738.42 1189.16 1044.59 284.05 74.85709 764.6 1195.9 62.2 285.0 75.0 14.5 722.98 1188.85 1059.36 283.76 74.9034 700.9 1195.2 61.0 283.5 74.6 14.6 701.42 1188.44 1056.75 283.32 74.7923 638.2 1194.4 63.0 282.2 74.3 14.7 655.77 1187.63 961.10 282.40 74.49541 567.0 1193.5 62.7 281.0 74.4 14.8 585.34 1186.84 825.49 281.11 74.0854 483.4 1192.9 58.9 279.8 73.6 14.9 506.65 1186.41 727.80 279.85 73.87328 366.5 1192.3 49.7 278.4 73.4 15.0 445.48 1186.14 661.92 279.03 73.8341 210.5 1192.0 33.0 277.2 73.6 15.1 411.78 1185.81 619.64 278.64 73.87054 64.4 1192.0 12.5 276.6 73.5 15.2 385.86 1185.49 592.75 278.37 73.83266 1.1 1190.4 1.0 276.2 73.6 15.3 349.27 1185.30 554.67 278.03 73.74274 0.0 100.0 0.0 10.0 73.6 15.4 319.59 1185.20 507.41 277.77 73.76365 0.0 100.0 0.0 10.0 73.6 15.5 325.76 1185.22 498.53 277.98 73.77338 0.0 100.0 0.0 10.0 73.6 15.6 369.42 1184.78 575.30 278.45 74.58835 0.0 100.0 0.0 10.0 73.5 15.7 346.74 1184.61 584.43 278.21 73.66819 0.0 100.0 0.0 10.0 73.5 15.8 262.52 1184.94 466.55 277.51 73.63993 0.0 100.0 0.0 10.0 73.4  


Oconee Nuclear Station                                                                     UFSAR Table 6-29 (Page 9 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 9 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 15.9       218.42     1184.87     361.49   277.11 73.67149     0.0     100.0       0.0       10.0         73.3 16.0       222.61     1184.76     320.17   277.10   73.7808     0.0     100.0       0.0       10.0         73.3 16.1       256.26     1184.43     361.74   277.35 73.88752     0.0     100.0       0.0       10.0         73.5 16.2       314.87     1184.32     484.15   278.05 74.00542     0.0     100.0       0.0       10.0         73.5 16.3       399.70     1184.46     651.48   278.87   74.611     0.0     100.0       0.0       10.0         73.6 16.4       424.88     1184.86     697.94   278.89   73.8687     0.0     100.0       0.0       10.0         73.6 16.5       386.37     1185.31     628.68   278.39 73.86523     0.0     100.0       0.0       10.0         73.6 16.6       346.12     1185.35     566.91   278.02 73.71196     0.0     100.0       0.0       10.0         73.5 16.7       322.87     1185.29     517.31   277.81 73.76705     0.0     100.0       0.0       10.0         73.1 16.8       333.86     1185.05     522.15   277.92 73.94365   25.1     1184.8       0.1     275.9         73.8 16.9       347.65     1184.83     558.07   278.03 73.91508   35.5     1184.8       0.4     275.3         73.6 17.0       345.70     1184.89     568.38   277.99 73.85989   10.5     1185.0       0.3     275.0         73.5 17.1       350.61     1185.03     570.27   278.08 73.87688     0.0     100.0       0.0       10.0         73.6 17.2       379.62     1184.96     607.60   278.44 74.09661     0.0     100.0       0.0       10.0         73.8 17.3       404.80     1184.94     647.60   278.66 74.03583     0.0     100.0       0.0       10.0         73.7 17.4       435.72     1185.41     687.07   279.23 74.02745     0.0     100.0       0.0       10.0         73.7 17.5       598.94     1187.92     924.39   282.82 75.58422   18.0     1184.9       0.0     300.0         73.7 17.6       720.00     1188.90     1114.95   284.07 74.80801   96.3     1186.4       1.0     277.4         73.9 17.7       680.45     1188.07     1081.59   282.91 74.60171   83.9     1186.8       1.1     276.9         73.4 17.8       651.61     1187.52     1065.14   282.37 74.85718   52.1     1187.6       0.5     274.3         73.8 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 15.9 218.42 1184.87 361.49 277.11 73.67149 0.0 100.0 0.0 10.0 73.3 16.0 222.61 1184.76 320.17 277.10 73.7808 0.0 100.0 0.0 10.0 73.3 16.1 256.26 1184.43 361.74 277.35 73.88752 0.0 100.0 0.0 10.0 73.5 16.2 314.87 1184.32 484.15 278.05 74.00542 0.0 100.0 0.0 10.0 73.5 16.3 399.70 1184.46 651.48 278.87 74.611 0.0 100.0 0.0 10.0 73.6 16.4 424.88 1184.86 697.94 278.89 73.8687 0.0 100.0 0.0 10.0 73.6 16.5 386.37 1185.31 628.68 278.39 73.86523 0.0 100.0 0.0 10.0 73.6 16.6 346.12 1185.35 566.91 278.02 73.71196 0.0 100.0 0.0 10.0 73.5 16.7 322.87 1185.29 517.31 277.81 73.76705 0.0 100.0 0.0 10.0 73.1 16.8 333.86 1185.05 522.15 277.92 73.94365 25.1 1184.8 0.1 275.9 73.8 16.9 347.65 1184.83 558.07 278.03 73.91508 35.5 1184.8 0.4 275.3 73.6 17.0 345.70 1184.89 568.38 277.99 73.85989 10.5 1185.0 0.3 275.0 73.5 17.1 350.61 1185.03 570.27 278.08 73.87688 0.0 100.0 0.0 10.0 73.6 17.2 379.62 1184.96 607.60 278.44 74.09661 0.0 100.0 0.0 10.0 73.8 17.3 404.80 1184.94 647.60 278.66 74.03583 0.0 100.0 0.0 10.0 73.7 17.4 435.72 1185.41 687.07 279.23 74.02745 0.0 100.0 0.0 10.0 73.7 17.5 598.94 1187.92 924.39 282.82 75.58422 18.0 1184.9 0.0 300.0 73.7 17.6 720.00 1188.90 1114.95 284.07 74.80801 96.3 1186.4 1.0 277.4 73.9 17.7 680.45 1188.07 1081.59 282.91 74.60171 83.9 1186.8 1.1 276.9 73.4 17.8 651.61 1187.52 1065.14 282.37 74.85718 52.1 1187.6 0.5 274.3 73.8  


Oconee Nuclear Station                                                                   UFSAR Table 6-29 (Page 10 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 10 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass      Gas      Mass      Liquid Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 17.9       633.42     1187.19     1015.64   282.03 74.48551   59.0     1187.8       0.6     276.1         73.5 18.0       607.27     1186.78     915.49   281.51 74.38813   12.5     1189.0       0.2     282.2         73.6 18.1       587.60     1186.59     852.64   281.15 74.21064     0.0     100.0       0.0       10.0         73.7 18.2       553.74     1186.32     815.45   280.62 74.19325     0.3     1184.5       0.0       10.0         73.8 18.3       478.24     1186.12     732.12   279.57 73.75981     0.4     1183.7       0.0       10.0         73.6 18.4       429.67     1186.05     664.12   278.92 73.93896     2.3     1184.7       0.0     100.0         73.8 18.5       438.00     1185.61     678.40   279.04 74.11103     2.3     1184.8       0.0     100.0         73.2 18.6       457.94     1185.43     719.11   279.32 74.05242     0.0     100.0       0.0       10.0         71.4 18.7       482.49     1185.54     754.55   279.68 74.06602     0.0     100.0       0.0       10.0         71.3 18.8       504.59     1185.59     780.58   279.95 74.33266     0.0     100.0       0.0       10.0         72.4 18.9       503.49     1185.66     768.14   279.87 74.15369   49.5     1186.1       0.0     300.0         74.0 19.0       476.57     1185.79     724.02   279.47 73.98391   135.2     1189.1       0.1     280.0         73.8 19.1       466.39     1185.81     711.54   279.38 74.10407   161.5     1193.2       0.2     273.5         73.7 19.2       495.61     1185.75     756.43   279.88   74.2496   77.7     1195.9       0.1     280.0         73.5 19.3       525.03     1185.73     791.41   280.25 74.28757     1.9     1197.3       0.0     500.0         73.7 19.4       523.68     1185.85     767.50   280.16 74.18356     0.0     100.0       0.0       10.0         73.6 19.5       522.86     1186.05     749.64   280.17 74.31515     3.3     1186.5       0.0       10.0         73.8 19.6       533.74     1185.99     768.04   280.33 74.43989     3.3     1186.5       0.0       10.0         73.6 19.7       502.24     1185.92     730.49   279.85 73.89213     0.0     100.0       0.0       10.0         73.7 19.8       508.56     1186.34     734.64   280.20 74.19047   11.4     1187.3       0.0       10.0         73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 17.9 633.42 1187.19 1015.64 282.03 74.48551 59.0 1187.8 0.6 276.1 73.5 18.0 607.27 1186.78 915.49 281.51 74.38813 12.5 1189.0 0.2 282.2 73.6 18.1 587.60 1186.59 852.64 281.15 74.21064 0.0 100.0 0.0 10.0 73.7 18.2 553.74 1186.32 815.45 280.62 74.19325 0.3 1184.5 0.0 10.0 73.8 18.3 478.24 1186.12 732.12 279.57 73.75981 0.4 1183.7 0.0 10.0 73.6 18.4 429.67 1186.05 664.12 278.92 73.93896 2.3 1184.7 0.0 100.0 73.8 18.5 438.00 1185.61 678.40 279.04 74.11103 2.3 1184.8 0.0 100.0 73.2 18.6 457.94 1185.43 719.11 279.32 74.05242 0.0 100.0 0.0 10.0 71.4 18.7 482.49 1185.54 754.55 279.68 74.06602 0.0 100.0 0.0 10.0 71.3 18.8 504.59 1185.59 780.58 279.95 74.33266 0.0 100.0 0.0 10.0 72.4 18.9 503.49 1185.66 768.14 279.87 74.15369 49.5 1186.1 0.0 300.0 74.0 19.0 476.57 1185.79 724.02 279.47 73.98391 135.2 1189.1 0.1 280.0 73.8 19.1 466.39 1185.81 711.54 279.38 74.10407 161.5 1193.2 0.2 273.5 73.7 19.2 495.61 1185.75 756.43 279.88 74.2496 77.7 1195.9 0.1 280.0 73.5 19.3 525.03 1185.73 791.41 280.25 74.28757 1.9 1197.3 0.0 500.0 73.7 19.4 523.68 1185.85 767.50 280.16 74.18356 0.0 100.0 0.0 10.0 73.6 19.5 522.86 1186.05 749.64 280.17 74.31515 3.3 1186.5 0.0 10.0 73.8 19.6 533.74 1185.99 768.04 280.33 74.43989 3.3 1186.5 0.0 10.0 73.6 19.7 502.24 1185.92 730.49 279.85 73.89213 0.0 100.0 0.0 10.0 73.7 19.8 508.56 1186.34 734.64 280.20 74.19047 11.4 1187.3 0.0 10.0 73.7  


Oconee Nuclear Station                                                                   UFSAR Table 6-29 (Page 11 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 11 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 19.9       616.57     1187.48     917.68   282.36   74.8431   64.5     1192.6       0.0     200.0         73.8 20.0       775.01     1190.10     1383.88   285.64 76.28355   28.5     1195.3       0.0     200.0         73.6 20.5       768.54     1189.90     1293.07   285.24 75.66263     6.5     1198.0       0.0       10.0         72.1 21.0       737.11     1189.18     1175.02   284.21 74.90845   70.9     1196.7       0.0     276.0         69.2 21.5       735.01     1189.12     1277.36   284.25 75.24608   80.3     1196.4       0.0     280.0         73.5 22.0       720.92     1188.88     1432.47   284.08 75.57133     9.4     1194.6       0.0     100.0         73.7 22.5       726.28     1189.06     1447.13   284.21 75.18275   61.9     1195.8       0.0       10.0         72.5 23.0       773.58     1189.98     1180.22   284.93 75.54347   73.5     1197.0       0.0       10.0         73.7 23.5       743.87     1189.42     909.58   284.23 74.70858   12.2     1202.9       0.0       10.0         73.7 24.0       653.24     1187.68     951.56   282.29 74.38791   40.8     1196.2       0.0       10.0         73.4 24.5       622.69     1187.07     1153.75   281.98 74.78619   57.5     1198.2       0.0       10.0         73.7 25.0       591.01     1186.75     1165.02   281.47 74.57095   26.6     1201.6       0.0       10.0         73.7 25.5       517.97     1185.79     1246.63   280.26 74.32353   11.5     1197.8       0.0       10.0         73.7 26.0       470.72     1184.94     1528.44   279.77 74.51925   29.9     1203.0       0.0       10.0         73.7 26.5       438.75     1184.57     1620.52   279.41 74.44828   37.2     1204.4       0.0       10.0         73.7 27.0       395.58     1184.51     1391.44   278.83   74.1436   15.0     1205.2       0.0       10.0         73.6 27.5       354.94     1184.46     1206.39   278.25 74.01461   11.1     1205.5       0.0       10.0         73.7 28.0       323.82     1184.30     1180.52   277.94 73.94646   12.2     1205.8       0.0       10.0         73.7 28.5       292.90     1184.23     1080.88   277.65 73.87787     7.0     1205.2       0.0       10.0         73.7 29.0       264.78     1184.22     925.93   277.40 73.82074     0.4     1197.2       0.0       10.0         73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 19.9 616.57 1187.48 917.68 282.36 74.8431 64.5 1192.6 0.0 200.0 73.8 20.0 775.01 1190.10 1383.88 285.64 76.28355 28.5 1195.3 0.0 200.0 73.6 20.5 768.54 1189.90 1293.07 285.24 75.66263 6.5 1198.0 0.0 10.0 72.1 21.0 737.11 1189.18 1175.02 284.21 74.90845 70.9 1196.7 0.0 276.0 69.2 21.5 735.01 1189.12 1277.36 284.25 75.24608 80.3 1196.4 0.0 280.0 73.5 22.0 720.92 1188.88 1432.47 284.08 75.57133 9.4 1194.6 0.0 100.0 73.7 22.5 726.28 1189.06 1447.13 284.21 75.18275 61.9 1195.8 0.0 10.0 72.5 23.0 773.58 1189.98 1180.22 284.93 75.54347 73.5 1197.0 0.0 10.0 73.7 23.5 743.87 1189.42 909.58 284.23 74.70858 12.2 1202.9 0.0 10.0 73.7 24.0 653.24 1187.68 951.56 282.29 74.38791 40.8 1196.2 0.0 10.0 73.4 24.5 622.69 1187.07 1153.75 281.98 74.78619 57.5 1198.2 0.0 10.0 73.7 25.0 591.01 1186.75 1165.02 281.47 74.57095 26.6 1201.6 0.0 10.0 73.7 25.5 517.97 1185.79 1246.63 280.26 74.32353 11.5 1197.8 0.0 10.0 73.7 26.0 470.72 1184.94 1528.44 279.77 74.51925 29.9 1203.0 0.0 10.0 73.7 26.5 438.75 1184.57 1620.52 279.41 74.44828 37.2 1204.4 0.0 10.0 73.7 27.0 395.58 1184.51 1391.44 278.83 74.1436 15.0 1205.2 0.0 10.0 73.6 27.5 354.94 1184.46 1206.39 278.25 74.01461 11.1 1205.5 0.0 10.0 73.7 28.0 323.82 1184.30 1180.52 277.94 73.94646 12.2 1205.8 0.0 10.0 73.7 28.5 292.90 1184.23 1080.88 277.65 73.87787 7.0 1205.2 0.0 10.0 73.7 29.0 264.78 1184.22 925.93 277.40 73.82074 0.4 1197.2 0.0 10.0 73.7  


Oconee Nuclear Station                                                                   UFSAR Table 6-29 (Page 12 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 12 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 29.5       245.07     1184.19     783.58   277.24 73.79306   0.7     1191.1       0.0       10.0         73.7 30.0       229.02     1184.14     675.89   277.13 73.76751     2.4     1191.5       0.0       10.0         73.7 30.5       213.60     1184.07     602.43   277.03 73.76419     2.1     1191.2       0.0       10.0         73.7 31.0       198.66     1183.96     559.76   276.95 73.75786     0.4     1189.1       0.0       10.0         73.7 31.5       186.45     1183.85     523.38   276.88 73.75477     0.7     1186.9       0.0       10.0         73.7 32.0       177.71     1183.74     519.98   276.84 73.75468   11.1     1197.0       0.0       10.0         73.7 32.5       169.39     1183.59     570.67   276.81 73.75427   28.1     1203.4       0.0       10.0         73.7 33.0       159.81     1183.43     642.99   276.77 73.74869   32.7     1208.1       0.0       10.0         73.7 33.5       151.10     1183.28     707.65   276.75 73.77543   28.2     1206.7       0.0       10.0         73.7 34.0       146.42     1183.16     789.63   276.74 73.76569   13.4     1203.3       0.0       10.0         73.6 34.5       144.36     1183.05     1033.98   276.76 73.78262     0.1     1206.4       0.0       10.0         72.9 35.0       141.69     1182.90     1571.86   276.82 73.81935     6.3     1186.6       0.0       10.0         71.2 35.5       137.42     1182.69     2171.55   276.87 73.89374   41.0     1191.9       0.0     200.0         73.9 36.0       135.44     1182.48     2562.42   276.95 73.96019   53.1     1192.8       0.0     200.0         73.8 36.5       134.63     1182.34     2833.52   277.00 74.03759   24.5     1193.0       0.0       10.0         73.6 37.0       131.47     1182.28     2925.39   276.99 74.02323   27.0     1195.9       0.0       10.0         73.5 37.5       127.70     1182.29     2813.08   276.94 73.99922   22.8     1197.0       0.0       10.0         73.7 38.0       123.37     1182.32     2700.79   276.88   73.9596     2.6     1197.9       0.0       10.0         73.7 38.5       118.40     1182.32     2638.13   276.83 73.92158   11.2     1193.1       0.0       10.0         73.8 39.0       114.06     1182.31     2613.86   276.80 73.92563   16.2     1193.1       0.0       10.0         73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 29.5 245.07 1184.19 783.58 277.24 73.79306 0.7 1191.1 0.0 10.0 73.7 30.0 229.02 1184.14 675.89 277.13 73.76751 2.4 1191.5 0.0 10.0 73.7 30.5 213.60 1184.07 602.43 277.03 73.76419 2.1 1191.2 0.0 10.0 73.7 31.0 198.66 1183.96 559.76 276.95 73.75786 0.4 1189.1 0.0 10.0 73.7 31.5 186.45 1183.85 523.38 276.88 73.75477 0.7 1186.9 0.0 10.0 73.7 32.0 177.71 1183.74 519.98 276.84 73.75468 11.1 1197.0 0.0 10.0 73.7 32.5 169.39 1183.59 570.67 276.81 73.75427 28.1 1203.4 0.0 10.0 73.7 33.0 159.81 1183.43 642.99 276.77 73.74869 32.7 1208.1 0.0 10.0 73.7 33.5 151.10 1183.28 707.65 276.75 73.77543 28.2 1206.7 0.0 10.0 73.7 34.0 146.42 1183.16 789.63 276.74 73.76569 13.4 1203.3 0.0 10.0 73.6 34.5 144.36 1183.05 1033.98 276.76 73.78262 0.1 1206.4 0.0 10.0 72.9 35.0 141.69 1182.90 1571.86 276.82 73.81935 6.3 1186.6 0.0 10.0 71.2 35.5 137.42 1182.69 2171.55 276.87 73.89374 41.0 1191.9 0.0 200.0 73.9 36.0 135.44 1182.48 2562.42 276.95 73.96019 53.1 1192.8 0.0 200.0 73.8 36.5 134.63 1182.34 2833.52 277.00 74.03759 24.5 1193.0 0.0 10.0 73.6 37.0 131.47 1182.28 2925.39 276.99 74.02323 27.0 1195.9 0.0 10.0 73.5 37.5 127.70 1182.29 2813.08 276.94 73.99922 22.8 1197.0 0.0 10.0 73.7 38.0 123.37 1182.32 2700.79 276.88 73.9596 2.6 1197.9 0.0 10.0 73.7 38.5 118.40 1182.32 2638.13 276.83 73.92158 11.2 1193.1 0.0 10.0 73.8 39.0 114.06 1182.31 2613.86 276.80 73.92563 16.2 1193.1 0.0 10.0 73.7  


Oconee Nuclear Station                                                                   UFSAR Table 6-29 (Page 13 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 13 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 39.5       108.28     1182.30     2554.13   276.70 73.88004     7.8     1192.9       0.0       10.0         73.7 40.0       100.17     1182.31     2396.29   276.57 73.70213     3.1     1192.8       0.0       10.0         73.7 40.5       92.79     1182.32     2230.38   276.51 73.70171   1.8     1191.0       0.0       10.0         73.7 41.0       87.72     1182.29     2155.10   276.49 73.70168   7.2     1195.5       0.0       10.0         73.7 41.5       84.54     1182.24     2182.41   276.49 73.70219   13.5     1199.4       0.0       10.0         73.7 42.0       82.74     1182.21     2261.05   276.48 73.70177   14.1     1203.9       0.0       10.0         73.7 42.5       83.64     1182.15     2397.74   276.49 73.70461   15.0     1206.8       0.0       10.0         73.7 43.0       88.05     1181.99     2703.09   276.51 73.70767   16.8     1208.7       0.0       10.0         73.7 43.5       92.99     1181.86     3081.04   276.53 73.71006   18.3     1210.4       0.0       10.0         73.7 44.0       97.06     1181.81     3345.76   276.55   73.713   19.8     1211.8       0.0       10.0         73.7 44.5       100.77     1181.80     3464.22   276.57 73.71436   20.3     1213.0       0.0       10.0         73.7 45.0       102.87     1181.82     3440.50   276.57 73.71311   20.2     1214.0       0.0       10.0         73.7 45.5       102.00     1181.87     3331.83   276.56 73.70994   20.2     1214.8       0.0       10.0         73.7 46.0       98.34     1181.93     3218.84   276.55 73.70684   21.2     1215.5       0.0       10.0         73.7 46.5       94.03     1181.96     3146.64   276.53 73.70648   23.9     1216.1       0.0       10.0         73.7 47.0       92.13     1181.94     3165.32   276.53 73.70738   27.5     1216.5       0.0       10.0         73.7 47.5       94.10     1181.87     3291.14   276.54 73.71215   29.7     1216.9       0.0       10.0         73.7 48.0       96.45     1181.83     3429.04   276.55 73.71077   26.7     1217.1       0.0       10.0         73.7 48.5       94.99     1181.86     3441.09   276.54   73.7085   25.4     1217.3       0.0       10.0         73.7 49.0       90.01     1181.96     3220.39   276.52 73.70547   25.6     1217.5       0.0       10.0         73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 39.5 108.28 1182.30 2554.13 276.70 73.88004 7.8 1192.9 0.0 10.0 73.7 40.0 100.17 1182.31 2396.29 276.57 73.70213 3.1 1192.8 0.0 10.0 73.7 40.5 92.79 1182.32 2230.38 276.51 73.70171 1.8 1191.0 0.0 10.0 73.7 41.0 87.72 1182.29 2155.10 276.49 73.70168 7.2 1195.5 0.0 10.0 73.7 41.5 84.54 1182.24 2182.41 276.49 73.70219 13.5 1199.4 0.0 10.0 73.7 42.0 82.74 1182.21 2261.05 276.48 73.70177 14.1 1203.9 0.0 10.0 73.7 42.5 83.64 1182.15 2397.74 276.49 73.70461 15.0 1206.8 0.0 10.0 73.7 43.0 88.05 1181.99 2703.09 276.51 73.70767 16.8 1208.7 0.0 10.0 73.7 43.5 92.99 1181.86 3081.04 276.53 73.71006 18.3 1210.4 0.0 10.0 73.7 44.0 97.06 1181.81 3345.76 276.55 73.713 19.8 1211.8 0.0 10.0 73.7 44.5 100.77 1181.80 3464.22 276.57 73.71436 20.3 1213.0 0.0 10.0 73.7 45.0 102.87 1181.82 3440.50 276.57 73.71311 20.2 1214.0 0.0 10.0 73.7 45.5 102.00 1181.87 3331.83 276.56 73.70994 20.2 1214.8 0.0 10.0 73.7 46.0 98.34 1181.93 3218.84 276.55 73.70684 21.2 1215.5 0.0 10.0 73.7 46.5 94.03 1181.96 3146.64 276.53 73.70648 23.9 1216.1 0.0 10.0 73.7 47.0 92.13 1181.94 3165.32 276.53 73.70738 27.5 1216.5 0.0 10.0 73.7 47.5 94.10 1181.87 3291.14 276.54 73.71215 29.7 1216.9 0.0 10.0 73.7 48.0 96.45 1181.83 3429.04 276.55 73.71077 26.7 1217.1 0.0 10.0 73.7 48.5 94.99 1181.86 3441.09 276.54 73.7085 25.4 1217.3 0.0 10.0 73.7 49.0 90.01 1181.96 3220.39 276.52 73.70547 25.6 1217.5 0.0 10.0 73.7  


Oconee Nuclear Station                                                                   UFSAR Table 6-29 (Page 14 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 14 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 49.5       79.93     1182.12     2782.82   276.49 73.69555   13.3     1217.6       0.0       10.0         73.7 50.0       65.72     1182.28     2336.62   276.46 73.69418     1.5     1217.7       0.0       10.0         73.7 50.5       51.69     1182.43     1936.11   276.44 73.69373     0.0     100.0       0.0       10.0         73.7 51.0       39.33     1182.59     1511.38   276.42 73.69345     0.0     100.0       0.0       10.0         73.7 51.5       31.34     1182.63     1108.77   276.42 73.69723     0.0     100.0       0.0       10.0         73.6 52.0       26.53     1182.53     784.76   276.41   73.6967     0.0     100.0       0.0       10.0         73.6 52.5       21.48     1182.40     524.23   276.40 73.70061     4.4     1188.1       0.0       10.0         73.7 53.0       17.17     1182.48     320.55   276.40 73.69612     4.7     1188.0       0.0       10.0         73.7 53.5       14.90     1182.73     196.09   276.40 73.69675     9.1     1191.8       0.0       10.0         73.7 54.0       14.21     1182.97     107.19   276.41 73.69689   31.5     1198.0       0.0       10.0         73.7 54.5       14.48     1183.19       44.46   276.42   73.6972   54.1     1204.5       0.0       10.0         73.7 55.0       16.08     1183.41       16.26   276.33 73.69724   62.3     1209.8       0.0       10.0         73.7 55.5       22.12     1183.51       19.64   276.40 73.69837   54.2     1213.2       0.0       10.0         73.7 56.0       30.62     1183.12     130.51   276.41 73.69796   41.6     1215.0       0.0       10.0         73.7 56.5       34.60     1182.53     378.40   276.41 73.69784   25.4     1215.8       0.0       10.0         73.7 57.0       33.66     1182.14     581.39   276.41 73.69814     9.4     1216.4       0.0       10.0         73.7 57.5       32.50     1181.98     662.14   276.41   73.6994     8.6     1217.1       0.0       10.0         73.7 58.0       31.96     1181.85     730.39   276.41 73.69713   13.9     1217.5       0.0       10.0         73.7 58.5       29.60     1181.70     720.18   276.41 73.69666   16.6     1217.9       0.0       10.0         73.7 59.0       23.23     1181.54     549.73   276.40 73.69803   18.5     1218.2       0.0       10.0         73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 49.5 79.93 1182.12 2782.82 276.49 73.69555 13.3 1217.6 0.0 10.0 73.7 50.0 65.72 1182.28 2336.62 276.46 73.69418 1.5 1217.7 0.0 10.0 73.7 50.5 51.69 1182.43 1936.11 276.44 73.69373 0.0 100.0 0.0 10.0 73.7 51.0 39.33 1182.59 1511.38 276.42 73.69345 0.0 100.0 0.0 10.0 73.7 51.5 31.34 1182.63 1108.77 276.42 73.69723 0.0 100.0 0.0 10.0 73.6 52.0 26.53 1182.53 784.76 276.41 73.6967 0.0 100.0 0.0 10.0 73.6 52.5 21.48 1182.40 524.23 276.40 73.70061 4.4 1188.1 0.0 10.0 73.7 53.0 17.17 1182.48 320.55 276.40 73.69612 4.7 1188.0 0.0 10.0 73.7 53.5 14.90 1182.73 196.09 276.40 73.69675 9.1 1191.8 0.0 10.0 73.7 54.0 14.21 1182.97 107.19 276.41 73.69689 31.5 1198.0 0.0 10.0 73.7 54.5 14.48 1183.19 44.46 276.42 73.6972 54.1 1204.5 0.0 10.0 73.7 55.0 16.08 1183.41 16.26 276.33 73.69724 62.3 1209.8 0.0 10.0 73.7 55.5 22.12 1183.51 19.64 276.40 73.69837 54.2 1213.2 0.0 10.0 73.7 56.0 30.62 1183.12 130.51 276.41 73.69796 41.6 1215.0 0.0 10.0 73.7 56.5 34.60 1182.53 378.40 276.41 73.69784 25.4 1215.8 0.0 10.0 73.7 57.0 33.66 1182.14 581.39 276.41 73.69814 9.4 1216.4 0.0 10.0 73.7 57.5 32.50 1181.98 662.14 276.41 73.6994 8.6 1217.1 0.0 10.0 73.7 58.0 31.96 1181.85 730.39 276.41 73.69713 13.9 1217.5 0.0 10.0 73.7 58.5 29.60 1181.70 720.18 276.41 73.69666 16.6 1217.9 0.0 10.0 73.7 59.0 23.23 1181.54 549.73 276.40 73.69803 18.5 1218.2 0.0 10.0 73.7  


Oconee Nuclear Station                                                                   UFSAR Table 6-29 (Page 15 of 15)
Oconee Nuclear Station UFSAR Table 6-29 (Page 15 of 15)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) (Btu/lbm)       (psi) 59.5       16.54     1181.55     318.06   276.40   73.6974   15.3     1218.4       0.0       10.0         73.7 60.0       14.63     1182.30     100.15   276.40 73.69705   10.3     1218.8       0.0       10.0         73.7 61.0       14.80     1182.92       27.07   276.41 73.69739   14.4     1219.2       0.0       10.0         73.7 62.0       14.93     1183.46       3.28   276.49 73.69757   26.0     1219.2       0.0       10.0         73.7 63.0       15.01     1183.93       0.42   276.52 73.69798   29.6     1219.0       0.0       10.0         73.7 64.0       14.08     1184.38       0.07   270.27 73.69649   23.7     1218.9       0.0       10.0         73.7 65.0       11.02     1184.53       0.06   277.31   73.6967   21.6     1219.0       0.0       10.0         73.7 66.0         7.83     1184.36       0.05   284.31 73.69694   22.3     1219.1       0.0       10.0         73.7 67.0         8.98     1184.83       0.03   264.15   73.6979   22.8     1219.2       0.0       10.0         73.7 68.0       13.77     1185.80       0.02   258.06 73.69794   24.3     1219.2       0.0       10.0         73.7 69.0       19.57     1185.76       0.82   276.83   73.6981   26.4     1219.1       0.0       10.0         73.7 70.0       22.80     1184.37       36.64   276.41 73.69612   28.4     1219.1       0.0       10.0         73.7 71.0       21.97     1183.10     150.45   276.40 73.69683   29.5     1219.0       0.0       10.0         73.7 71.68426       20.81     1182.71     265.61   276.40 73.69853   29.8     1219.0       0.0       10.0         73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi) 59.5 16.54 1181.55 318.06 276.40 73.6974 15.3 1218.4 0.0 10.0 73.7 60.0 14.63 1182.30 100.15 276.40 73.69705 10.3 1218.8 0.0 10.0 73.7 61.0 14.80 1182.92 27.07 276.41 73.69739 14.4 1219.2 0.0 10.0 73.7 62.0 14.93 1183.46 3.28 276.49 73.69757 26.0 1219.2 0.0 10.0 73.7 63.0 15.01 1183.93 0.42 276.52 73.69798 29.6 1219.0 0.0 10.0 73.7 64.0 14.08 1184.38 0.07 270.27 73.69649 23.7 1218.9 0.0 10.0 73.7 65.0 11.02 1184.53 0.06 277.31 73.6967 21.6 1219.0 0.0 10.0 73.7 66.0 7.83 1184.36 0.05 284.31 73.69694 22.3 1219.1 0.0 10.0 73.7 67.0 8.98 1184.83 0.03 264.15 73.6979 22.8 1219.2 0.0 10.0 73.7 68.0 13.77 1185.80 0.02 258.06 73.69794 24.3 1219.2 0.0 10.0 73.7 69.0 19.57 1185.76 0.82 276.83 73.6981 26.4 1219.1 0.0 10.0 73.7 70.0 22.80 1184.37 36.64 276.41 73.69612 28.4 1219.1 0.0 10.0 73.7 71.0 21.97 1183.10 150.45 276.40 73.69683 29.5 1219.0 0.0 10.0 73.7 71.68426 20.81 1182.71 265.61 276.40 73.69853 29.8 1219.0 0.0 10.0 73.7  


Oconee Nuclear Station                                                                       UFSAR Table 6-30 (Page 1 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 1 of 40)
Table 6-30. RELAP5 Long-Term Mass and Energy Release Data Reactor Vessel Side                                 Pump Discharge Side Liquid                                            Liquid Gas Mass    Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid                    Spilled Time         Flow  Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy    Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   Btu/lbm)       (psi)       (gpm) 0.0           2.61   1190.80   45034.67   560.04   2294.67   622.72   1195.07   24082.41     538.81     2296.60         0.00 0.5           1.35   1190.73   45002.73   561.03   1141.73   701.17   1195.39   23503.53     536.92       946.56         0.00 1.0           1.97   1189.03   43883.38   561.31   1112.71   821.86   1195.63   22712.44     535.16       946.49         0.00 1.5         14.86   1188.96   41138.78   560.56   1113.47   940.61   1195.69   22178.90     535.45       952.13         0.00 2.0         50.78   1188.48   37445.88   561.23   1121.34   1048.83   1196.19   20838.21     536.12       928.40         0.00 2.5         131.14   1188.16   33748.12   562.75   1143.21   1085.61   1196.58   19040.70     538.38       895.71         0.00 3.0         295.10   1188.29   31133.46   563.51   1137.55   1165.81   1196.70   17346.79     538.67       874.28         0.00 3.5         499.44   1188.67   29332.74   562.72   1127.36   1339.95   1197.43   15457.64     534.17       837.95         0.00 4.0         702.87   1189.19   27711.68   561.28   1120.62   1789.77   1201.47   13673.54     517.80       797.22         0.00 4.5         973.92   1190.10   25969.13   558.99   1104.83   2328.37   1205.61   11416.29     495.80       685.83         0.00 5.0       1308.56   1191.25   23634.97   556.36   1072.47   2574.99   1207.92   9250.46     482.53       620.76         0.00 5.5       1580.32   1191.83   20906.55   556.08   1032.60   2641.20   1209.04   8241.40     475.89       590.78         0.00 6.0       1802.31   1192.39   18632.19   555.19   1003.97   2628.75   1209.53   7834.36     472.11       577.39         0.00 6.5       2004.58   1193.41   17055.64   550.93   979.81   2676.06   1210.49   7089.30     467.57       557.19         7.51 7.0       2142.47   1194.57   15821.38   545.99   951.27   2816.47   1212.28   5780.78     460.58       509.76       15.21 7.5       2201.87   1195.71   14909.52   540.90   924.81   2904.60   1213.70   4810.09     454.21       479.95       23.09 8.0       2201.25   1196.85   14343.35   535.83   901.26   2906.34   1214.35   4396.83     450.43       464.32       31.11 8.5       2432.66   1200.19   14060.63   524.56   844.18   2868.05   1214.66   4167.69     447.20       451.84       39.38 9.0       2754.27   1203.35   13282.68   512.71   792.59   2818.77   1214.99   3900.91     443.34       435.95       47.90 (31 DEC 2003)
(31 DEC 2003)
Table 6-30. RELAP5 Long-Term Mass and Energy Release Data Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 0.0 2.61 1190.80 45034.67 560.04 2294.67 622.72 1195.07 24082.41 538.81 2296.60 0.00 0.5 1.35 1190.73 45002.73 561.03 1141.73 701.17 1195.39 23503.53 536.92 946.56 0.00 1.0 1.97 1189.03 43883.38 561.31 1112.71 821.86 1195.63 22712.44 535.16 946.49 0.00 1.5 14.86 1188.96 41138.78 560.56 1113.47 940.61 1195.69 22178.90 535.45 952.13 0.00 2.0 50.78 1188.48 37445.88 561.23 1121.34 1048.83 1196.19 20838.21 536.12 928.40 0.00 2.5 131.14 1188.16 33748.12 562.75 1143.21 1085.61 1196.58 19040.70 538.38 895.71 0.00 3.0 295.10 1188.29 31133.46 563.51 1137.55 1165.81 1196.70 17346.79 538.67 874.28 0.00 3.5 499.44 1188.67 29332.74 562.72 1127.36 1339.95 1197.43 15457.64 534.17 837.95 0.00 4.0 702.87 1189.19 27711.68 561.28 1120.62 1789.77 1201.47 13673.54 517.80 797.22 0.00 4.5 973.92 1190.10 25969.13 558.99 1104.83 2328.37 1205.61 11416.29 495.80 685.83 0.00 5.0 1308.56 1191.25 23634.97 556.36 1072.47 2574.99 1207.92 9250.46 482.53 620.76 0.00 5.5 1580.32 1191.83 20906.55 556.08 1032.60 2641.20 1209.04 8241.40 475.89 590.78 0.00 6.0 1802.31 1192.39 18632.19 555.19 1003.97 2628.75 1209.53 7834.36 472.11 577.39 0.00 6.5 2004.58 1193.41 17055.64 550.93 979.81 2676.06 1210.49 7089.30 467.57 557.19 7.51 7.0 2142.47 1194.57 15821.38 545.99 951.27 2816.47 1212.28 5780.78 460.58 509.76 15.21 7.5 2201.87 1195.71 14909.52 540.90 924.81 2904.60 1213.70 4810.09 454.21 479.95 23.09 8.0 2201.25 1196.85 14343.35 535.83 901.26 2906.34 1214.35 4396.83 450.43 464.32 31.11 8.5 2432.66 1200.19 14060.63 524.56 844.18 2868.05 1214.66 4167.69 447.20 451.84 39.38 9.0 2754.27 1203.35 13282.68 512.71 792.59 2818.77 1214.99 3900.91 443.34 435.95 47.90  


Oconee Nuclear Station                                                                       UFSAR Table 6-30 (Page 2 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 2 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid                    Spilled Time         Flow  Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy    Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   Btu/lbm)       (psi)       (gpm) 9.5       2871.87   1204.91   12016.15   506.08   753.66   2771.95   1215.55   3502.50     438.36       413.89       56.67 10.0       2910.01   1206.30   10930.33   499.17   715.22   2732.74   1216.38   2996.00     432.48       387.73         65.73 10.5       2893.94   1207.56     9959.00   491.68   672.61   2681.48   1217.16   2516.27     426.21       362.25         75.14 11.0       2866.07   1208.79     9014.42   483.96   632.15   2594.28   1217.52   2178.14     419.90       338.86         84.77 11.5       2839.38   1209.99     8060.30   475.90   588.69   2485.06   1217.59   1934.33     413.70       318.78         94.71 12.0       2659.09   1210.53     7615.43   466.52   551.69   2376.03   1217.67   1697.65     407.37       296.84       104.83 12.5       2069.41   1209.75     8732.67   450.07   490.74   2281.22   1217.91   1430.96     401.09       277.06       115.14 13.0       1475.93   1208.24   10159.54   433.27   422.92   2207.90   1218.48   1111.64     394.91       255.52       125.01 13.5       1223.13   1207.47   10460.70   418.41   371.54   2140.84   1219.30     783.30     388.66       234.91       134.01 14.0       1074.33   1206.66   10258.17   404.44   322.90   2054.75   1220.00     502.83     382.03       213.44       143.03 14.5       959.22   1205.72     9831.20   392.62   285.56   1945.08   1220.32     301.89     374.90       194.07       152.06 15.0       825.84   1204.48     9494.08   382.34   261.44   1814.99   1220.50     154.67     368.23       172.93       161.10 15.5       687.19   1202.93     9221.88   372.02   235.30   1648.52   1219.51     91.58     356.60       155.28       170.15 16.0       582.34   1201.44     8886.18   361.07   214.06   1471.92   1217.77     73.06     349.40       136.72       179.21 16.5       522.33   1200.11     8517.77   347.47   201.93   1310.72   1219.71     25.72     342.61       118.47       188.27 17.0       462.30   1198.49     8201.79   333.03   181.54   1140.02   1232.42     2.62     335.89       101.48       197.34 17.5       388.14   1196.14     8086.54   320.25   154.66   982.25   1247.77     0.09     319.35       88.88       206.40 18.0       334.42   1193.50     8097.22   308.14   132.07   856.27   1250.00     0.11     310.19       79.00       215.45 18.5       300.17   1190.66     8172.03   296.34   111.48   745.49   1246.15     0.13     303.05       75.32       224.50 19.0       249.01   1187.99     7975.41   285.43   93.94   648.70   1239.56     0.21     294.81       72.42       233.54 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 9.5 2871.87 1204.91 12016.15 506.08 753.66 2771.95 1215.55 3502.50 438.36 413.89 56.67 10.0 2910.01 1206.30 10930.33 499.17 715.22 2732.74 1216.38 2996.00 432.48 387.73 65.73 10.5 2893.94 1207.56 9959.00 491.68 672.61 2681.48 1217.16 2516.27 426.21 362.25 75.14 11.0 2866.07 1208.79 9014.42 483.96 632.15 2594.28 1217.52 2178.14 419.90 338.86 84.77 11.5 2839.38 1209.99 8060.30 475.90 588.69 2485.06 1217.59 1934.33 413.70 318.78 94.71 12.0 2659.09 1210.53 7615.43 466.52 551.69 2376.03 1217.67 1697.65 407.37 296.84 104.83 12.5 2069.41 1209.75 8732.67 450.07 490.74 2281.22 1217.91 1430.96 401.09 277.06 115.14 13.0 1475.93 1208.24 10159.54 433.27 422.92 2207.90 1218.48 1111.64 394.91 255.52 125.01 13.5 1223.13 1207.47 10460.70 418.41 371.54 2140.84 1219.30 783.30 388.66 234.91 134.01 14.0 1074.33 1206.66 10258.17 404.44 322.90 2054.75 1220.00 502.83 382.03 213.44 143.03 14.5 959.22 1205.72 9831.20 392.62 285.56 1945.08 1220.32 301.89 374.90 194.07 152.06 15.0 825.84 1204.48 9494.08 382.34 261.44 1814.99 1220.50 154.67 368.23 172.93 161.10 15.5 687.19 1202.93 9221.88 372.02 235.30 1648.52 1219.51 91.58 356.60 155.28 170.15 16.0 582.34 1201.44 8886.18 361.07 214.06 1471.92 1217.77 73.06 349.40 136.72 179.21 16.5 522.33 1200.11 8517.77 347.47 201.93 1310.72 1219.71 25.72 342.61 118.47 188.27 17.0 462.30 1198.49 8201.79 333.03 181.54 1140.02 1232.42 2.62 335.89 101.48 197.34 17.5 388.14 1196.14 8086.54 320.25 154.66 982.25 1247.77 0.09 319.35 88.88 206.40 18.0 334.42 1193.50 8097.22 308.14 132.07 856.27 1250.00 0.11 310.19 79.00 215.45 18.5 300.17 1190.66 8172.03 296.34 111.48 745.49 1246.15 0.13 303.05 75.32 224.50 19.0 249.01 1187.99 7975.41 285.43 93.94 648.70 1239.56 0.21 294.81 72.42 233.54  


Oconee Nuclear Station                                                                       UFSAR Table 6-30 (Page 3 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 3 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid                    Spilled Time         Flow  Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow      Enthalpy    Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   Btu/lbm)       (psi)       (gpm) 19.5       171.69   1185.35     7496.61   273.86   88.14     572.76   1221.23       1.02     285.27       70.02         242.58 20.0       125.51   1181.92     7477.24   258.83   68.46     510.71   1203.59       5.30     281.20       68.44         251.61 20.5         85.76   1178.12     7206.32   234.47   58.72     461.12   1198.73     16.35     279.10       67.69         251.64 21.0         41.52   1172.48     6823.43   209.85   43.15     423.82   1195.20     34.96     277.24       67.20         251.67 21.5         24.30   1169.09     6869.18   199.55   37.14     393.55   1190.35     56.72     275.83       66.92         251.68 22.0         16.74   1167.35     6706.53   193.57   35.06     368.52   1186.88     77.95     274.67       66.61         251.69 22.5         13.23   1166.81     6332.16   191.06   33.87     343.15   1185.05     100.84     273.64       66.33         251.70 23.0         11.13   1166.81     5975.03   190.89   35.99     318.22   1184.14     118.38     272.77       66.03         251.72 23.5         8.81   1166.62     5793.32   188.98   33.97     297.75   1183.51     129.30     272.05       65.84         251.73 24.0         6.98   1166.70     5463.94   188.53   33.11     278.42   1182.96     137.99     271.41       65.63         251.74 24.5         6.18   1167.51     5209.50   188.10   33.87     260.48   1182.47     137.95     270.81       65.37         251.75 25.0         8.81   1172.33     5088.87   192.17   34.44     239.74   1182.10     129.04     270.16       65.16         251.77 25.5         13.66   1177.36     5061.48   191.39   49.33     221.36   1181.90     121.85     269.57       64.91         251.77 26.0         13.92   1179.01     4819.75   183.61   49.14     210.18   1182.30     112.02     269.24       64.80         251.79 26.5         12.38   1178.14     4099.11   191.56   55.62     183.79   1184.18     87.49     268.66       64.46         251.81 27.0         9.08   1178.57     3385.51   196.88   54.40     152.31   1187.39     61.24     267.95       64.29         251.80 27.5         4.62   1182.12     2978.50   191.22   56.41     118.94   1190.83     41.35     267.47       64.12         251.83 28.0         1.67   1186.52     1546.48   190.48   62.83     56.84   1193.16     20.05     267.00       63.94         251.86 28.5         0.00   1173.07     97.41     190.70   61.92       8.18   1191.67       4.20     266.56       63.85         251.86 29.0         0.00   1169.54       0.00     261.52   55.11       0.00   1174.65       0.00     261.50       63.81         251.87 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 19.5 171.69 1185.35 7496.61 273.86 88.14 572.76 1221.23 1.02 285.27 70.02 242.58 20.0 125.51 1181.92 7477.24 258.83 68.46 510.71 1203.59 5.30 281.20 68.44 251.61 20.5 85.76 1178.12 7206.32 234.47 58.72 461.12 1198.73 16.35 279.10 67.69 251.64 21.0 41.52 1172.48 6823.43 209.85 43.15 423.82 1195.20 34.96 277.24 67.20 251.67 21.5 24.30 1169.09 6869.18 199.55 37.14 393.55 1190.35 56.72 275.83 66.92 251.68 22.0 16.74 1167.35 6706.53 193.57 35.06 368.52 1186.88 77.95 274.67 66.61 251.69 22.5 13.23 1166.81 6332.16 191.06 33.87 343.15 1185.05 100.84 273.64 66.33 251.70 23.0 11.13 1166.81 5975.03 190.89 35.99 318.22 1184.14 118.38 272.77 66.03 251.72 23.5 8.81 1166.62 5793.32 188.98 33.97 297.75 1183.51 129.30 272.05 65.84 251.73 24.0 6.98 1166.70 5463.94 188.53 33.11 278.42 1182.96 137.99 271.41 65.63 251.74 24.5 6.18 1167.51 5209.50 188.10 33.87 260.48 1182.47 137.95 270.81 65.37 251.75 25.0 8.81 1172.33 5088.87 192.17 34.44 239.74 1182.10 129.04 270.16 65.16 251.77 25.5 13.66 1177.36 5061.48 191.39 49.33 221.36 1181.90 121.85 269.57 64.91 251.77 26.0 13.92 1179.01 4819.75 183.61 49.14 210.18 1182.30 112.02 269.24 64.80 251.79 26.5 12.38 1178.14 4099.11 191.56 55.62 183.79 1184.18 87.49 268.66 64.46 251.81 27.0 9.08 1178.57 3385.51 196.88 54.40 152.31 1187.39 61.24 267.95 64.29 251.80 27.5 4.62 1182.12 2978.50 191.22 56.41 118.94 1190.83 41.35 267.47 64.12 251.83 28.0 1.67 1186.52 1546.48 190.48 62.83 56.84 1193.16 20.05 267.00 63.94 251.86 28.5 0.00 1173.07 97.41 190.70 61.92 8.18 1191.67 4.20 266.56 63.85 251.86 29.0 0.00 1169.54 0.00 261.52 55.11 0.00 1174.65 0.00 261.50 63.81 251.87  


Oconee Nuclear Station                                                                       UFSAR Table 6-30 (Page 4 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 4 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid                    Spilled Time         Flow  Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy    Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   Btu/lbm)       (psi)       (gpm) 29.5         0.00   1168.90       0.00     261.67   53.33       0.00   1174.36     0.00     261.63       63.35         251.87 30.0         0.00   1169.17       0.00     261.47   54.14       0.00   1174.26     0.00     261.68       63.14         251.87 31           0.00   1167.33       0.00     262.99   49.67       0.00   1173.95     0.00     261.82       62.58         251.89 32           0.00   1168.81       0.00     261.39   52.98     14.15   1207.90     0.04     269.33       62.69         251.87 33           0.00   1172.52       0.00     262.87   60.22     14.24   1207.93     0.04     267.47       63.33         251.85 34           0.00   1169.02       0.00     260.98   53.42       9.28   1202.56     0.02     260.61       62.61         251.87 35           0.00   1170.08       0.00     260.67   55.62     11.91   1199.71     0.02     264.86       62.76         251.86 36         12.25   1202.55     120.64   226.64   56.40     31.16   1216.23     0.04     265.91       62.79         251.86 37         12.81   1201.81     133.73   225.33   62.25     31.38   1219.40     0.05     265.31       62.82         251.86 38         114.71   1187.73     259.64   265.32   63.96     70.37   1251.25     0.03     265.62       63.18         251.82 39         287.46   1190.16     392.15   268.51   64.44     148.11   1233.85     2.85     266.58       62.71         251.80 40         379.29   1189.84     362.22   270.53   64.37     177.09   1205.36     16.57     266.97       62.71         251.80 41         391.99   1187.18     375.78   270.82   65.50     184.09   1191.36     34.19     266.69       62.76         251.78 42         357.15   1185.55     421.36   270.33   63.22     170.81   1187.04     46.01     266.36       62.37         251.81 43         371.22   1186.09     475.78   270.67   67.23     177.56   1184.23     62.23     266.42       62.80         251.78 44         358.14   1185.62     373.60   269.60   63.36     168.68   1183.55     65.23     266.10       62.24         251.80 45         301.98   1183.54     317.79   267.52   62.84     140.01   1184.02     64.73     265.36       62.03         251.81 46         292.95   1183.15     305.97   267.16   62.79     130.70   1182.49     81.70     265.12       61.95         251.81 47         298.85   1183.16     315.79   267.17   62.58     130.47   1181.63     93.87     265.01       61.80         251.82 48         302.29   1183.22     337.72   267.17   62.67     131.96   1181.30     98.58     264.91       61.71         251.81 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 29.5 0.00 1168.90 0.00 261.67 53.33 0.00 1174.36 0.00 261.63 63.35 251.87 30.0 0.00 1169.17 0.00 261.47 54.14 0.00 1174.26 0.00 261.68 63.14 251.87 31 0.00 1167.33 0.00 262.99 49.67 0.00 1173.95 0.00 261.82 62.58 251.89 32 0.00 1168.81 0.00 261.39 52.98 14.15 1207.90 0.04 269.33 62.69 251.87 33 0.00 1172.52 0.00 262.87 60.22 14.24 1207.93 0.04 267.47 63.33 251.85 34 0.00 1169.02 0.00 260.98 53.42 9.28 1202.56 0.02 260.61 62.61 251.87 35 0.00 1170.08 0.00 260.67 55.62 11.91 1199.71 0.02 264.86 62.76 251.86 36 12.25 1202.55 120.64 226.64 56.40 31.16 1216.23 0.04 265.91 62.79 251.86 37 12.81 1201.81 133.73 225.33 62.25 31.38 1219.40 0.05 265.31 62.82 251.86 38 114.71 1187.73 259.64 265.32 63.96 70.37 1251.25 0.03 265.62 63.18 251.82 39 287.46 1190.16 392.15 268.51 64.44 148.11 1233.85 2.85 266.58 62.71 251.80 40 379.29 1189.84 362.22 270.53 64.37 177.09 1205.36 16.57 266.97 62.71 251.80 41 391.99 1187.18 375.78 270.82 65.50 184.09 1191.36 34.19 266.69 62.76 251.78 42 357.15 1185.55 421.36 270.33 63.22 170.81 1187.04 46.01 266.36 62.37 251.81 43 371.22 1186.09 475.78 270.67 67.23 177.56 1184.23 62.23 266.42 62.80 251.78 44 358.14 1185.62 373.60 269.60 63.36 168.68 1183.55 65.23 266.10 62.24 251.80 45 301.98 1183.54 317.79 267.52 62.84 140.01 1184.02 64.73 265.36 62.03 251.81 46 292.95 1183.15 305.97 267.16 62.79 130.70 1182.49 81.70 265.12 61.95 251.81 47 298.85 1183.16 315.79 267.17 62.58 130.47 1181.63 93.87 265.01 61.80 251.82 48 302.29 1183.22 337.72 267.17 62.67 131.96 1181.30 98.58 264.91 61.71 251.81  


Oconee Nuclear Station                                                                       UFSAR Table 6-30 (Page 5 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 5 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid                    Spilled Time         Flow  Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow      Enthalpy    Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   Btu/lbm)       (psi)       (gpm) 49         304.79   1183.28     336.95   267.10   62.59     132.09   1180.90     105.03     264.78       61.60         251.81 50         299.65   1183.10     328.89   266.84   62.38     128.95   1180.52     113.38     264.61       61.47         251.81 51         282.29   1182.63     313.69   266.34   62.12     122.57   1180.41     117.85     264.39       61.34         251.82 52         260.99   1182.20     300.55   265.76   61.72     114.38   1180.57     117.71     264.14       61.17         251.82 53         249.94   1181.97     302.22   265.43   61.58     109.41   1180.67     117.90     263.94       61.04         251.82 54         245.26   1181.81     306.17   265.23   61.48     108.17   1180.58     119.63     263.79       60.92         251.82 55         232.70   1181.79     292.61   264.89   61.24     104.07   1180.70     117.76     263.60       60.78         251.83 56         218.64   1181.80     281.43   264.50   60.99     98.82   1180.94     114.52     263.40       60.63         251.83 57         212.67   1181.80     277.39   264.28   60.85     96.38   1181.04     113.40     263.23       60.50         251.83 58         205.27   1181.90     258.90   264.02   60.70     93.57   1181.17     111.40     263.06       60.37         251.83 59         205.83   1182.09     295.46   264.49   60.46     90.84   1181.39     109.86     262.91       60.23         251.83 60         241.80   1182.13     361.54   265.08   62.43     110.30   1180.18     132.93     263.20       60.43         251.82 61         242.62   1181.86     314.13   264.64   60.52     113.22   1180.08     130.16     263.16       60.12         251.83 62         216.16   1181.77     243.87   263.80   60.43     96.33   1181.28     102.44     262.73       60.06         251.83 63         211.13   1182.03     224.70   263.67   60.31     93.84   1181.45     100.33     262.66       60.01         251.83 64         196.74   1182.09     212.49   263.41   60.20     88.70   1181.63     101.00     262.57       59.96         251.84 65         188.06   1182.12     205.51   263.26   60.15     85.51   1181.76     102.27     262.50       59.93         251.84 66         184.70   1182.18     191.29   263.15   60.05     83.60   1181.90     101.57     262.45       59.89         251.84 67         176.40   1182.12     189.67   262.97   59.98     81.07   1182.14     98.32     262.38       59.85         251.84 68         205.52   1181.96     268.47   263.92   59.93     96.50   1181.12     115.51     262.77       59.82         251.84 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 49 304.79 1183.28 336.95 267.10 62.59 132.09 1180.90 105.03 264.78 61.60 251.81 50 299.65 1183.10 328.89 266.84 62.38 128.95 1180.52 113.38 264.61 61.47 251.81 51 282.29 1182.63 313.69 266.34 62.12 122.57 1180.41 117.85 264.39 61.34 251.82 52 260.99 1182.20 300.55 265.76 61.72 114.38 1180.57 117.71 264.14 61.17 251.82 53 249.94 1181.97 302.22 265.43 61.58 109.41 1180.67 117.90 263.94 61.04 251.82 54 245.26 1181.81 306.17 265.23 61.48 108.17 1180.58 119.63 263.79 60.92 251.82 55 232.70 1181.79 292.61 264.89 61.24 104.07 1180.70 117.76 263.60 60.78 251.83 56 218.64 1181.80 281.43 264.50 60.99 98.82 1180.94 114.52 263.40 60.63 251.83 57 212.67 1181.80 277.39 264.28 60.85 96.38 1181.04 113.40 263.23 60.50 251.83 58 205.27 1181.90 258.90 264.02 60.70 93.57 1181.17 111.40 263.06 60.37 251.83 59 205.83 1182.09 295.46 264.49 60.46 90.84 1181.39 109.86 262.91 60.23 251.83 60 241.80 1182.13 361.54 265.08 62.43 110.30 1180.18 132.93 263.20 60.43 251.82 61 242.62 1181.86 314.13 264.64 60.52 113.22 1180.08 130.16 263.16 60.12 251.83 62 216.16 1181.77 243.87 263.80 60.43 96.33 1181.28 102.44 262.73 60.06 251.83 63 211.13 1182.03 224.70 263.67 60.31 93.84 1181.45 100.33 262.66 60.01 251.83 64 196.74 1182.09 212.49 263.41 60.20 88.70 1181.63 101.00 262.57 59.96 251.84 65 188.06 1182.12 205.51 263.26 60.15 85.51 1181.76 102.27 262.50 59.93 251.84 66 184.70 1182.18 191.29 263.15 60.05 83.60 1181.90 101.57 262.45 59.89 251.84 67 176.40 1182.12 189.67 262.97 59.98 81.07 1182.14 98.32 262.38 59.85 251.84 68 205.52 1181.96 268.47 263.92 59.93 96.50 1181.12 115.51 262.77 59.82 251.84  


Oconee Nuclear Station                                                                       UFSAR Table 6-30 (Page 6 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 6 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid                    Spilled Time         Flow  Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow      Enthalpy    Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   Btu/lbm)       (psi)       (gpm) 69         228.28   1181.58     314.22   264.12   60.56     105.73   1180.77     114.93     262.83       59.86         251.82 70         211.39   1181.50     260.95   263.51   60.05     96.34   1181.79     87.90     262.43       59.76         251.84 71         205.62   1182.15     211.03   263.29   60.03     92.69   1182.19     83.58     262.34       59.74         251.83 72         195.59   1182.56     181.51   263.07   59.89     87.25   1182.01     91.87     262.25       59.69         251.84 73         186.06   1182.68     167.17   262.88   59.81     82.39   1181.86     101.60     262.17       59.66         251.84 74         182.09   1182.72     152.77   262.73   59.73     79.81   1181.80     106.64     262.12       59.62         251.84 75         174.34   1182.42     167.84   262.59   59.67     78.35   1181.84     107.38     262.07       59.59         251.84 76         167.76   1182.02     194.13   262.51   59.66     78.08   1181.88     106.55     262.03       59.55         251.84 77         171.14   1181.79     211.29   262.57   59.62     79.29   1181.86     105.66     262.00       59.52         251.84 78         180.39   1181.60     229.44   262.71   59.74     82.74   1181.66     106.10     262.00       59.51         251.84 79         186.18   1181.59     227.52   262.75   59.70     85.12   1181.56     105.29     261.98       59.47         251.84 80         187.40   1181.76     216.34   262.72   59.65     85.92   1181.56     103.65     261.95       59.44         251.84 81         189.20   1182.09     193.61   262.68   59.61     85.20   1181.72     99.97     261.91       59.39         251.84 82         189.21   1182.36     169.14   262.61   59.52     83.05   1182.06     93.54     261.84       59.36         251.84 83         182.44   1182.30     174.37   262.46   59.48     81.51   1182.24     90.08     261.79       59.32         251.84 84         173.12   1182.11     187.45   262.29   59.40     79.56   1182.26     91.10     261.73       59.28         251.84 85         166.15   1181.96     191.34   262.15   59.35     77.67   1182.18     95.13     261.68       59.25         251.84 86         160.21   1181.90     185.84   262.03   59.28     75.57   1182.12     99.01     261.62       59.21         251.84 87         154.33   1181.85     180.63   261.92   59.22     73.36   1182.13     101.85     261.57       59.17         251.84 88         150.02   1181.84     173.45   261.83   59.17     71.37   1182.12     104.41     261.51       59.14         251.84 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 69 228.28 1181.58 314.22 264.12 60.56 105.73 1180.77 114.93 262.83 59.86 251.82 70 211.39 1181.50 260.95 263.51 60.05 96.34 1181.79 87.90 262.43 59.76 251.84 71 205.62 1182.15 211.03 263.29 60.03 92.69 1182.19 83.58 262.34 59.74 251.83 72 195.59 1182.56 181.51 263.07 59.89 87.25 1182.01 91.87 262.25 59.69 251.84 73 186.06 1182.68 167.17 262.88 59.81 82.39 1181.86 101.60 262.17 59.66 251.84 74 182.09 1182.72 152.77 262.73 59.73 79.81 1181.80 106.64 262.12 59.62 251.84 75 174.34 1182.42 167.84 262.59 59.67 78.35 1181.84 107.38 262.07 59.59 251.84 76 167.76 1182.02 194.13 262.51 59.66 78.08 1181.88 106.55 262.03 59.55 251.84 77 171.14 1181.79 211.29 262.57 59.62 79.29 1181.86 105.66 262.00 59.52 251.84 78 180.39 1181.60 229.44 262.71 59.74 82.74 1181.66 106.10 262.00 59.51 251.84 79 186.18 1181.59 227.52 262.75 59.70 85.12 1181.56 105.29 261.98 59.47 251.84 80 187.40 1181.76 216.34 262.72 59.65 85.92 1181.56 103.65 261.95 59.44 251.84 81 189.20 1182.09 193.61 262.68 59.61 85.20 1181.72 99.97 261.91 59.39 251.84 82 189.21 1182.36 169.14 262.61 59.52 83.05 1182.06 93.54 261.84 59.36 251.84 83 182.44 1182.30 174.37 262.46 59.48 81.51 1182.24 90.08 261.79 59.32 251.84 84 173.12 1182.11 187.45 262.29 59.40 79.56 1182.26 91.10 261.73 59.28 251.84 85 166.15 1181.96 191.34 262.15 59.35 77.67 1182.18 95.13 261.68 59.25 251.84 86 160.21 1181.90 185.84 262.03 59.28 75.57 1182.12 99.01 261.62 59.21 251.84 87 154.33 1181.85 180.63 261.92 59.22 73.36 1182.13 101.85 261.57 59.17 251.84 88 150.02 1181.84 173.45 261.83 59.17 71.37 1182.12 104.41 261.51 59.14 251.84  


Oconee Nuclear Station                                                                       UFSAR Table 6-30 (Page 7 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 7 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid                    Spilled Time         Flow  Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow      Enthalpy    Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   Btu/lbm)       (psi)       (gpm) 89         146.81   1181.87     163.70   261.75   59.12     69.25   1182.01     106.84     261.46       59.10         251.84 90         145.08   1182.03     144.75   261.71   59.08     66.73   1181.81     108.90     261.40       59.06         251.84 91         142.31   1182.13     132.30   261.67   59.06     64.49   1181.63     110.74     261.37       59.05         251.85 92         140.24   1182.31     118.47   261.65   59.05     62.77   1181.49     112.28     261.34       59.03         251.85 93         138.59   1182.51     101.62   261.63   59.03     60.68   1181.37     111.96     261.31       59.02         251.85 94         135.67   1182.75       90.54   261.61   59.01     58.76   1181.30     109.76     261.28       59.00         251.85 95         132.34   1183.11       75.58   261.59   59.00     57.23   1181.30     105.54     261.26       58.99         251.85 96         128.05   1183.34       66.81   261.55   58.98     56.13   1181.38     99.03     261.24       58.97         251.85 97         124.92   1183.63       56.19   261.53   58.97     55.40   1181.51     91.22     261.22       58.96         251.85 98         121.64   1183.88       47.33   261.51   58.96     54.29   1181.62     83.38     261.20       58.95         251.85 99         117.13   1184.02       40.18   261.48   58.94     52.44   1181.65     77.13     261.17       58.93         251.85 100         111.09   1184.10       33.74   261.45   58.92     50.11   1181.58     73.41     261.14       58.92         251.85 101         104.19   1184.15       29.03   261.41   58.91     47.06   1181.40     72.24     261.12       58.90         251.85 102         97.68   1184.23       25.76   261.34   58.91     43.21   1181.17     71.12     261.09       58.89         251.85 103         92.03   1184.39       23.33   261.28   58.89     39.93   1180.96     69.33     261.06       58.87         251.85 104         87.56   1184.59       21.68   261.25   58.87     38.11   1180.82     68.30     261.04       58.86         251.85 105         85.72   1185.08       20.35   261.23   58.87     37.50   1180.80     66.37     261.02       58.85         251.85 106         84.95   1186.62       18.17   261.22   58.86     37.70   1180.95     61.67     261.02       58.84         251.85 107         84.60   1188.89       15.56   261.21   58.86     40.14   1181.38     54.67     261.02       58.83         251.85 108         86.92   1190.59       14.32   261.18   58.84     43.40   1181.91     49.81     261.02       58.84         251.85 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 89 146.81 1181.87 163.70 261.75 59.12 69.25 1182.01 106.84 261.46 59.10 251.84 90 145.08 1182.03 144.75 261.71 59.08 66.73 1181.81 108.90 261.40 59.06 251.84 91 142.31 1182.13 132.30 261.67 59.06 64.49 1181.63 110.74 261.37 59.05 251.85 92 140.24 1182.31 118.47 261.65 59.05 62.77 1181.49 112.28 261.34 59.03 251.85 93 138.59 1182.51 101.62 261.63 59.03 60.68 1181.37 111.96 261.31 59.02 251.85 94 135.67 1182.75 90.54 261.61 59.01 58.76 1181.30 109.76 261.28 59.00 251.85 95 132.34 1183.11 75.58 261.59 59.00 57.23 1181.30 105.54 261.26 58.99 251.85 96 128.05 1183.34 66.81 261.55 58.98 56.13 1181.38 99.03 261.24 58.97 251.85 97 124.92 1183.63 56.19 261.53 58.97 55.40 1181.51 91.22 261.22 58.96 251.85 98 121.64 1183.88 47.33 261.51 58.96 54.29 1181.62 83.38 261.20 58.95 251.85 99 117.13 1184.02 40.18 261.48 58.94 52.44 1181.65 77.13 261.17 58.93 251.85 100 111.09 1184.10 33.74 261.45 58.92 50.11 1181.58 73.41 261.14 58.92 251.85 101 104.19 1184.15 29.03 261.41 58.91 47.06 1181.40 72.24 261.12 58.90 251.85 102 97.68 1184.23 25.76 261.34 58.91 43.21 1181.17 71.12 261.09 58.89 251.85 103 92.03 1184.39 23.33 261.28 58.89 39.93 1180.96 69.33 261.06 58.87 251.85 104 87.56 1184.59 21.68 261.25 58.87 38.11 1180.82 68.30 261.04 58.86 251.85 105 85.72 1185.08 20.35 261.23 58.87 37.50 1180.80 66.37 261.02 58.85 251.85 106 84.95 1186.62 18.17 261.22 58.86 37.70 1180.95 61.67 261.02 58.84 251.85 107 84.60 1188.89 15.56 261.21 58.86 40.14 1181.38 54.67 261.02 58.83 251.85 108 86.92 1190.59 14.32 261.18 58.84 43.40 1181.91 49.81 261.02 58.84 251.85  


Oconee Nuclear Station                                                                       UFSAR Table 6-30 (Page 8 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 8 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid                    Spilled Time         Flow  Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy    Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   Btu/lbm)       (psi)       (gpm) 109         85.56   1191.89       11.98   261.16   58.83     39.54   1181.95     42.35     261.00       58.81         251.85 110         79.56   1193.00       8.41   261.13   58.82     34.12   1181.74     33.81     260.96       58.80         251.85 111         75.29   1193.63       6.58   261.07   58.81     33.16   1181.58     34.06     260.94       58.79         251.85 112         73.24   1194.03       6.34   261.02   58.80     32.67   1181.17     41.18     260.92       58.78         251.85 113         73.47   1193.95       7.97   261.02   58.79     33.24   1180.87     49.57     260.91       58.77         251.85 114         74.47   1193.93       10.91   261.08   58.77     34.71   1180.96     51.47     260.91       58.76         251.85 115         75.20   1194.45       12.40   261.06   58.77     37.11   1181.63     43.45     260.92       58.76         251.85 116         76.21   1195.58       10.62   261.03   58.77     39.94   1183.13     29.36     260.93       58.75         251.85 117         77.94   1196.99       6.96   260.98   58.75     43.21   1185.50     16.82     260.93       58.75         251.85 118         76.80   1198.30       3.77   260.92   58.74     43.01   1186.48     12.18     260.92       58.73         251.85 119         73.04   1198.00       3.72   261.02   58.73     40.91   1185.19     16.21     260.90       58.72         251.85 120         71.80   1192.62       17.04   260.98   58.73     43.25   1181.99     53.40     260.88       58.71         251.85 125         76.74   1192.45       19.02   260.97   58.67     44.71   1181.31     66.34     260.85       58.68         251.85 130         80.32   1193.99       13.63   260.95   58.63     44.73   1183.14     49.67     260.81       58.63         251.85 135         77.98   1198.43       4.59   260.88   58.58     42.47   1189.86     15.96     260.75       58.58         251.85 140         106.76   1198.56       54.64   261.64   58.54     54.59   1188.32     19.19     260.86       58.53         251.85 145         141.38   1190.46     106.37   261.59   58.50     65.70   1182.93     53.92     260.85       58.49         251.85 150         151.29   1183.48     116.84   261.51   58.49     66.58   1181.41     74.15     260.80       58.49         251.85 155         159.11   1182.54     125.19   261.45   58.43     69.29   1181.15     83.06     260.75       58.44         251.85 160         163.67   1182.52     124.93   261.41   58.37     68.87   1180.80     90.80     260.70       58.38         251.85 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 109 85.56 1191.89 11.98 261.16 58.83 39.54 1181.95 42.35 261.00 58.81 251.85 110 79.56 1193.00 8.41 261.13 58.82 34.12 1181.74 33.81 260.96 58.80 251.85 111 75.29 1193.63 6.58 261.07 58.81 33.16 1181.58 34.06 260.94 58.79 251.85 112 73.24 1194.03 6.34 261.02 58.80 32.67 1181.17 41.18 260.92 58.78 251.85 113 73.47 1193.95 7.97 261.02 58.79 33.24 1180.87 49.57 260.91 58.77 251.85 114 74.47 1193.93 10.91 261.08 58.77 34.71 1180.96 51.47 260.91 58.76 251.85 115 75.20 1194.45 12.40 261.06 58.77 37.11 1181.63 43.45 260.92 58.76 251.85 116 76.21 1195.58 10.62 261.03 58.77 39.94 1183.13 29.36 260.93 58.75 251.85 117 77.94 1196.99 6.96 260.98 58.75 43.21 1185.50 16.82 260.93 58.75 251.85 118 76.80 1198.30 3.77 260.92 58.74 43.01 1186.48 12.18 260.92 58.73 251.85 119 73.04 1198.00 3.72 261.02 58.73 40.91 1185.19 16.21 260.90 58.72 251.85 120 71.80 1192.62 17.04 260.98 58.73 43.25 1181.99 53.40 260.88 58.71 251.85 125 76.74 1192.45 19.02 260.97 58.67 44.71 1181.31 66.34 260.85 58.68 251.85 130 80.32 1193.99 13.63 260.95 58.63 44.73 1183.14 49.67 260.81 58.63 251.85 135 77.98 1198.43 4.59 260.88 58.58 42.47 1189.86 15.96 260.75 58.58 251.85 140 106.76 1198.56 54.64 261.64 58.54 54.59 1188.32 19.19 260.86 58.53 251.85 145 141.38 1190.46 106.37 261.59 58.50 65.70 1182.93 53.92 260.85 58.49 251.85 150 151.29 1183.48 116.84 261.51 58.49 66.58 1181.41 74.15 260.80 58.49 251.85 155 159.11 1182.54 125.19 261.45 58.43 69.29 1181.15 83.06 260.75 58.44 251.85 160 163.67 1182.52 124.93 261.41 58.37 68.87 1180.80 90.80 260.70 58.38 251.85  


Oconee Nuclear Station                                                                       UFSAR Table 6-30 (Page 9 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 9 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid                    Spilled Time         Flow  Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy    Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   Btu/lbm)       (psi)       (gpm) 165         163.65   1182.12     142.01   261.30   58.86     70.41   1180.88     85.43     260.66       58.48         251.84 170         156.93   1181.96     146.92   261.14   58.30     68.83   1180.92     83.45     260.57       58.29         251.85 175         149.54   1182.01     134.68   261.00   58.27     64.30   1180.75     88.06     260.48       58.25         251.85 180         146.79   1182.10     131.98   260.94   58.19     61.47   1180.38     95.10     260.41       58.19         251.85 185         136.31   1184.21     101.69   260.81   58.14     55.55   1180.44     83.27     260.32       58.14         251.85 190         118.19   1185.09       74.19   260.50   58.09     49.80   1181.02     58.11     260.19       58.08         251.85 195         93.44   1184.22       69.65   260.36   58.01     44.53   1183.00     28.88     260.13       58.01         251.85 200         61.38   1188.49       36.98   260.22   57.96     34.83   1183.95     9.20     259.98       57.95         251.85 205         34.94   1195.83       6.77     260.06   57.90     22.27   1182.35     6.50     259.91       57.90         251.86 210         18.66   1201.86       0.15     259.81   57.86     15.18   1181.60     4.62     259.81       57.86         251.86 215         12.87   1206.61       0.03     257.58   57.81     15.20   1183.23     3.73     259.77       57.81         251.86 220         12.25   1209.83       0.02     256.04   57.76     15.49   1184.96     1.68     259.71       57.76         251.86 225         13.75   1210.42       0.02     257.86   57.71     14.96   1203.17     0.89     259.70       57.71         251.86 230         34.98   1205.70       0.75     259.95   57.67     18.79   1249.57     0.02     260.50       57.67         251.86 235         58.49   1200.67       20.78   259.72   57.57     26.81   1245.36     0.59     259.53       57.61         251.85 240         63.22   1191.11       77.61   259.73   57.57     32.35   1205.38     4.95     259.54       57.57         251.86 245         59.61   1185.05     110.68   259.69   57.52     31.36   1188.44     5.09     259.53       57.53         251.86 250         58.98   1183.14     250.47   260.07   57.46     28.68   1195.90     1.86     259.42       57.48         251.86 255         76.45   1181.50     295.98   260.01   57.65     35.55   1190.11     8.87     259.38       57.44         251.85 260         85.21   1182.24     161.11   259.63   57.41     40.11   1183.19     32.03     259.32       57.38         251.85 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 165 163.65 1182.12 142.01 261.30 58.86 70.41 1180.88 85.43 260.66 58.48 251.84 170 156.93 1181.96 146.92 261.14 58.30 68.83 1180.92 83.45 260.57 58.29 251.85 175 149.54 1182.01 134.68 261.00 58.27 64.30 1180.75 88.06 260.48 58.25 251.85 180 146.79 1182.10 131.98 260.94 58.19 61.47 1180.38 95.10 260.41 58.19 251.85 185 136.31 1184.21 101.69 260.81 58.14 55.55 1180.44 83.27 260.32 58.14 251.85 190 118.19 1185.09 74.19 260.50 58.09 49.80 1181.02 58.11 260.19 58.08 251.85 195 93.44 1184.22 69.65 260.36 58.01 44.53 1183.00 28.88 260.13 58.01 251.85 200 61.38 1188.49 36.98 260.22 57.96 34.83 1183.95 9.20 259.98 57.95 251.85 205 34.94 1195.83 6.77 260.06 57.90 22.27 1182.35 6.50 259.91 57.90 251.86 210 18.66 1201.86 0.15 259.81 57.86 15.18 1181.60 4.62 259.81 57.86 251.86 215 12.87 1206.61 0.03 257.58 57.81 15.20 1183.23 3.73 259.77 57.81 251.86 220 12.25 1209.83 0.02 256.04 57.76 15.49 1184.96 1.68 259.71 57.76 251.86 225 13.75 1210.42 0.02 257.86 57.71 14.96 1203.17 0.89 259.70 57.71 251.86 230 34.98 1205.70 0.75 259.95 57.67 18.79 1249.57 0.02 260.50 57.67 251.86 235 58.49 1200.67 20.78 259.72 57.57 26.81 1245.36 0.59 259.53 57.61 251.85 240 63.22 1191.11 77.61 259.73 57.57 32.35 1205.38 4.95 259.54 57.57 251.86 245 59.61 1185.05 110.68 259.69 57.52 31.36 1188.44 5.09 259.53 57.53 251.86 250 58.98 1183.14 250.47 260.07 57.46 28.68 1195.90 1.86 259.42 57.48 251.86 255 76.45 1181.50 295.98 260.01 57.65 35.55 1190.11 8.87 259.38 57.44 251.85 260 85.21 1182.24 161.11 259.63 57.41 40.11 1183.19 32.03 259.32 57.38 251.85  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 10 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 10 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 265         70.56   1183.17     115.93   259.52   57.35     33.17   1180.38     48.45     259.27       57.36         251.86 270         58.17   1182.98     108.49   259.40   57.31     26.47   1179.67     33.27     259.21       57.29         251.86 275         46.24   1183.17       86.62   259.30   57.24     20.51   1180.49     11.18     259.15       57.24         251.86 280         26.43   1185.23       34.42   259.18   57.19     11.67   1181.14     2.33     259.08       57.19         251.86 285         16.46   1190.90       3.02     259.06   57.15     7.89   1193.57     0.28     259.04       57.14         251.86 290         15.98   1195.10       0.74     258.89   57.10     8.23   1221.46     0.01     259.42       57.09         251.86 295         17.43   1189.80       14.99   258.90   57.05     8.47   1240.39     0.00     253.86       57.04         251.86 300         16.37   1184.34       24.97   258.86   56.99     8.31   1241.14     0.00     253.81       57.00         251.86 305         14.46   1184.34       21.97   258.80   56.96     7.54   1247.83     0.00     253.77       56.96         251.86 310         17.52   1183.79       35.47   258.75   56.92     8.48   1251.49     0.00     253.72       56.92         251.86 315         19.05   1183.48       39.99   258.72   56.88     8.37   1249.76     0.00     253.68       56.88         251.86 320         14.62   1183.70       30.07   258.66   56.83     6.54   1245.51     0.00     253.61       56.83         251.86 325         9.47   1183.70       25.79   258.60   56.79     5.94   1242.48     0.00     253.57       56.79         251.86 330         7.57   1183.88       16.45   258.56   56.76     5.54   1246.80     0.00     253.52       56.75         251.86 335         7.09   1184.10       10.49   258.49   56.71     5.11   1255.87     0.00     253.47       56.71         251.86 340         14.81   1183.32       43.87   258.47   56.67     7.70   1258.51     0.00     253.43       56.67         251.86 345         20.13   1183.07       65.11   258.44   56.63     9.05   1239.76     0.01     253.38       56.62         251.86 350         23.28   1182.59       75.27   258.40   56.59     9.91   1196.69     0.34     258.35       56.58         251.86 355         30.57   1181.98     105.94   258.39   56.55     12.29   1181.00     2.02     258.25       56.54         251.86 360         36.96   1180.30     143.28   258.36   56.51     13.69   1179.20     7.16     258.22       56.50         251.86 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 265 70.56 1183.17 115.93 259.52 57.35 33.17 1180.38 48.45 259.27 57.36 251.86 270 58.17 1182.98 108.49 259.40 57.31 26.47 1179.67 33.27 259.21 57.29 251.86 275 46.24 1183.17 86.62 259.30 57.24 20.51 1180.49 11.18 259.15 57.24 251.86 280 26.43 1185.23 34.42 259.18 57.19 11.67 1181.14 2.33 259.08 57.19 251.86 285 16.46 1190.90 3.02 259.06 57.15 7.89 1193.57 0.28 259.04 57.14 251.86 290 15.98 1195.10 0.74 258.89 57.10 8.23 1221.46 0.01 259.42 57.09 251.86 295 17.43 1189.80 14.99 258.90 57.05 8.47 1240.39 0.00 253.86 57.04 251.86 300 16.37 1184.34 24.97 258.86 56.99 8.31 1241.14 0.00 253.81 57.00 251.86 305 14.46 1184.34 21.97 258.80 56.96 7.54 1247.83 0.00 253.77 56.96 251.86 310 17.52 1183.79 35.47 258.75 56.92 8.48 1251.49 0.00 253.72 56.92 251.86 315 19.05 1183.48 39.99 258.72 56.88 8.37 1249.76 0.00 253.68 56.88 251.86 320 14.62 1183.70 30.07 258.66 56.83 6.54 1245.51 0.00 253.61 56.83 251.86 325 9.47 1183.70 25.79 258.60 56.79 5.94 1242.48 0.00 253.57 56.79 251.86 330 7.57 1183.88 16.45 258.56 56.76 5.54 1246.80 0.00 253.52 56.75 251.86 335 7.09 1184.10 10.49 258.49 56.71 5.11 1255.87 0.00 253.47 56.71 251.86 340 14.81 1183.32 43.87 258.47 56.67 7.70 1258.51 0.00 253.43 56.67 251.86 345 20.13 1183.07 65.11 258.44 56.63 9.05 1239.76 0.01 253.38 56.62 251.86 350 23.28 1182.59 75.27 258.40 56.59 9.91 1196.69 0.34 258.35 56.58 251.86 355 30.57 1181.98 105.94 258.39 56.55 12.29 1181.00 2.02 258.25 56.54 251.86 360 36.96 1180.30 143.28 258.36 56.51 13.69 1179.20 7.16 258.22 56.50 251.86  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 11 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 11 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 365         41.06   1178.74     172.25   258.34   56.48     14.17   1178.68     15.04     258.18       56.46         251.86 370         40.77   1178.35     174.37   258.30   56.43     13.65   1178.45     22.60     258.13       56.42         251.86 375         38.97   1178.34     169.67   258.25   56.39     12.99   1178.34     26.98     258.09       56.37         251.86 380         33.45   1178.37     140.89   258.18   56.34     11.07   1178.26     24.72     258.04       56.33         251.86 385         27.20   1178.63       98.55   258.09   56.30     7.50   1178.18     15.53     258.00       56.29         251.86 390         28.82   1178.66       99.17   258.02   56.26     7.00   1178.43     7.38     257.95       56.25         251.86 395         32.44   1178.47     115.24   258.00   56.22     9.47   1178.40     12.48     257.87       56.21         251.86 400         31.88   1178.37     106.91   257.95   56.18     10.31   1178.23     17.71     257.85       56.17         251.86 405         29.51   1178.32     101.09   257.89   56.13     10.26   1178.28     14.18     257.80       56.13         251.86 410         24.79   1178.47       87.79   257.83   56.09     8.95   1178.26     11.06     257.75       56.08         251.86 415         20.89   1178.63       76.83   257.75   56.05     6.85   1178.22     7.42     257.70       56.04         251.86 420         15.30   1178.65       60.79   257.68   55.99     5.07   1178.43     3.47     257.66       56.00         251.86 425         8.58   1179.04       31.53   257.62   55.94     3.36   1178.84     0.95     257.62       55.95         251.86 430         4.02   1179.46       14.93   257.58   55.90     1.87   1179.23     0.19     257.55       55.91         251.86 435         2.93   1179.87       13.75   257.53   55.87     1.39   1184.60     0.03     257.64       55.87         251.86 440         4.49   1180.02       15.59   257.49   55.78     1.67   1193.87     0.00     252.45       55.83         251.86 445         5.57   1180.39       23.49   257.42   55.79     2.67   1219.61     0.00     252.39       55.78         251.86 450         11.89   1179.28       66.46   257.35   55.75     5.21   1250.75     0.00     252.35       55.75         251.86 455         19.39   1178.21     138.34   257.35   55.71     7.91   1238.88     0.01     252.30       55.71         251.86 460         22.16   1177.81     196.83   257.34   55.67     9.88   1199.92     0.31     257.17       55.67         251.86 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 365 41.06 1178.74 172.25 258.34 56.48 14.17 1178.68 15.04 258.18 56.46 251.86 370 40.77 1178.35 174.37 258.30 56.43 13.65 1178.45 22.60 258.13 56.42 251.86 375 38.97 1178.34 169.67 258.25 56.39 12.99 1178.34 26.98 258.09 56.37 251.86 380 33.45 1178.37 140.89 258.18 56.34 11.07 1178.26 24.72 258.04 56.33 251.86 385 27.20 1178.63 98.55 258.09 56.30 7.50 1178.18 15.53 258.00 56.29 251.86 390 28.82 1178.66 99.17 258.02 56.26 7.00 1178.43 7.38 257.95 56.25 251.86 395 32.44 1178.47 115.24 258.00 56.22 9.47 1178.40 12.48 257.87 56.21 251.86 400 31.88 1178.37 106.91 257.95 56.18 10.31 1178.23 17.71 257.85 56.17 251.86 405 29.51 1178.32 101.09 257.89 56.13 10.26 1178.28 14.18 257.80 56.13 251.86 410 24.79 1178.47 87.79 257.83 56.09 8.95 1178.26 11.06 257.75 56.08 251.86 415 20.89 1178.63 76.83 257.75 56.05 6.85 1178.22 7.42 257.70 56.04 251.86 420 15.30 1178.65 60.79 257.68 55.99 5.07 1178.43 3.47 257.66 56.00 251.86 425 8.58 1179.04 31.53 257.62 55.94 3.36 1178.84 0.95 257.62 55.95 251.86 430 4.02 1179.46 14.93 257.58 55.90 1.87 1179.23 0.19 257.55 55.91 251.86 435 2.93 1179.87 13.75 257.53 55.87 1.39 1184.60 0.03 257.64 55.87 251.86 440 4.49 1180.02 15.59 257.49 55.78 1.67 1193.87 0.00 252.45 55.83 251.86 445 5.57 1180.39 23.49 257.42 55.79 2.67 1219.61 0.00 252.39 55.78 251.86 450 11.89 1179.28 66.46 257.35 55.75 5.21 1250.75 0.00 252.35 55.75 251.86 455 19.39 1178.21 138.34 257.35 55.71 7.91 1238.88 0.01 252.30 55.71 251.86 460 22.16 1177.81 196.83 257.34 55.67 9.88 1199.92 0.31 257.17 55.67 251.86  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 12 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 12 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 465         24.64   1177.94     243.61   257.31   55.65     10.55   1180.22     3.39     257.18       55.62         251.86 470         27.67   1179.91     298.59   257.29   55.60     10.26   1178.20     11.27     257.14       55.58         251.86 475         28.62   1181.51     325.73   257.25   55.54     9.68   1177.91     19.07     257.10       55.54         251.86 480         28.02   1182.12     333.19   257.20   55.50     9.05   1177.81     21.34     257.05       55.50         251.86 485         28.65   1182.16     335.36   257.15   55.47     8.39   1177.78     20.06     257.00       55.46         251.86 490         29.05   1181.28     336.11   257.10   55.43     7.47   1177.80     14.55     256.96       55.42         251.86 495         29.37   1181.87     337.37   257.05   55.38     7.05   1178.10     6.07     256.93       55.37         251.86 500         30.06   1181.96     314.79   257.00   55.34     6.56   1179.58     1.25     256.89       55.33         251.86 505         29.34   1181.65     297.75   256.94   55.30     5.94   1190.02     0.11     256.89       55.29         251.86 510         28.32   1182.08     311.80   256.89   55.26     6.03   1202.14     0.00     251.76       55.25         251.86 515         28.06   1181.89     317.88   256.84   55.22     5.93   1204.84     0.00     251.71       55.21         251.86 520         27.50   1182.20     300.49   256.78   55.17     5.60   1205.03     0.00     251.66       55.17         251.86 525         26.91   1182.39     290.72   256.73   55.11     5.56   1205.12     0.00     251.61       55.13         251.86 530         26.49   1181.89     289.91   256.68   55.09     5.43   1205.28     0.00     251.56       55.08         251.86 535         24.18   1182.01     262.12   256.62   55.05     4.72   1205.46     0.00     251.51       55.04         251.86 540         17.20   1181.75     153.46   256.56   55.00     2.76   1206.62     0.00     251.45       55.00         251.87 545         17.48   1178.41     119.78   256.47   54.96     5.26   1212.00     0.05     256.26       54.96         251.87 550         26.48   1177.45     191.53   256.46   54.92     7.48   1198.97     1.63     256.34       54.92         251.87 555         30.38   1179.49     256.27   256.44   54.88     6.17   1178.09     2.40     256.33       54.87         251.87 560         30.27   1181.52     287.52   256.39   54.84     6.18   1178.98     0.93     256.27       54.83         251.87 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 465 24.64 1177.94 243.61 257.31 55.65 10.55 1180.22 3.39 257.18 55.62 251.86 470 27.67 1179.91 298.59 257.29 55.60 10.26 1178.20 11.27 257.14 55.58 251.86 475 28.62 1181.51 325.73 257.25 55.54 9.68 1177.91 19.07 257.10 55.54 251.86 480 28.02 1182.12 333.19 257.20 55.50 9.05 1177.81 21.34 257.05 55.50 251.86 485 28.65 1182.16 335.36 257.15 55.47 8.39 1177.78 20.06 257.00 55.46 251.86 490 29.05 1181.28 336.11 257.10 55.43 7.47 1177.80 14.55 256.96 55.42 251.86 495 29.37 1181.87 337.37 257.05 55.38 7.05 1178.10 6.07 256.93 55.37 251.86 500 30.06 1181.96 314.79 257.00 55.34 6.56 1179.58 1.25 256.89 55.33 251.86 505 29.34 1181.65 297.75 256.94 55.30 5.94 1190.02 0.11 256.89 55.29 251.86 510 28.32 1182.08 311.80 256.89 55.26 6.03 1202.14 0.00 251.76 55.25 251.86 515 28.06 1181.89 317.88 256.84 55.22 5.93 1204.84 0.00 251.71 55.21 251.86 520 27.50 1182.20 300.49 256.78 55.17 5.60 1205.03 0.00 251.66 55.17 251.86 525 26.91 1182.39 290.72 256.73 55.11 5.56 1205.12 0.00 251.61 55.13 251.86 530 26.49 1181.89 289.91 256.68 55.09 5.43 1205.28 0.00 251.56 55.08 251.86 535 24.18 1182.01 262.12 256.62 55.05 4.72 1205.46 0.00 251.51 55.04 251.86 540 17.20 1181.75 153.46 256.56 55.00 2.76 1206.62 0.00 251.45 55.00 251.87 545 17.48 1178.41 119.78 256.47 54.96 5.26 1212.00 0.05 256.26 54.96 251.87 550 26.48 1177.45 191.53 256.46 54.92 7.48 1198.97 1.63 256.34 54.92 251.87 555 30.38 1179.49 256.27 256.44 54.88 6.17 1178.09 2.40 256.33 54.87 251.87 560 30.27 1181.52 287.52 256.39 54.84 6.18 1178.98 0.93 256.27 54.83 251.87  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 13 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 13 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 565         29.68   1182.10     289.02   256.34   54.80     5.81   1188.63     0.12     256.17       54.79         251.87 570         29.00   1182.49     319.90   256.30   54.76     6.16   1201.20     0.00     251.16       54.75         251.87 575         28.82   1181.95     349.48   256.26   54.72     6.22   1204.55     0.00     251.11       54.71         251.87 580         28.74   1181.58     335.08   256.21   54.67     5.72   1204.78     0.00     251.06       54.67         251.87 585         27.90   1181.53     317.08   256.14   54.63     5.57   1204.95     0.00     251.01       54.62         251.87 590         27.41   1181.83     332.46   256.10   54.59     5.59   1204.91     0.00     250.96       54.58         251.87 595         27.02   1181.85     350.62   256.05   54.55     5.76   1204.89     0.00     250.91       54.54         251.87 600         27.14   1181.99     337.96   256.00   54.51     5.61   1204.90     0.00     250.86       54.50         251.87 605         27.77   1182.06     322.40   255.94   54.46     5.39   1204.93     0.00     250.81       54.46         301.87 610         27.77   1181.46     288.88   255.89   54.42     5.23   1205.08     0.00     250.76       54.42         301.87 615         27.53   1181.16     250.34   255.82   54.38     5.07   1205.32     0.00     250.71       54.37         301.87 620         27.37   1180.31     236.36   255.77   54.34     4.90   1205.47     0.00     250.66       54.33         301.87 625         27.22   1180.09     225.57   255.71   54.30     4.86   1205.47     0.00     250.61       54.29         301.87 630         26.99   1180.08     227.60   255.66   54.26     4.82   1205.47     0.00     250.56       54.25         301.87 635         26.77   1180.58     241.34   255.61   54.21     4.96   1205.40     0.00     250.51       54.21         301.87 640         26.59   1180.51     255.24   255.57   54.17     5.13   1205.37     0.00     250.45       54.16         301.87 645         26.66   1180.38     247.06   255.52   54.13     4.77   1205.40     0.00     250.40       54.12         301.87 650         26.69   1180.58     248.12   255.47   54.09     4.85   1205.32     0.00     250.35       54.08         301.87 655         26.72   1180.03     252.04   255.42   54.05     5.15   1205.32     0.00     250.30       54.04         301.87 660         25.87   1178.97     226.41   255.37   54.01     4.74   1205.45     0.00     250.25       54.00         301.87 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 565 29.68 1182.10 289.02 256.34 54.80 5.81 1188.63 0.12 256.17 54.79 251.87 570 29.00 1182.49 319.90 256.30 54.76 6.16 1201.20 0.00 251.16 54.75 251.87 575 28.82 1181.95 349.48 256.26 54.72 6.22 1204.55 0.00 251.11 54.71 251.87 580 28.74 1181.58 335.08 256.21 54.67 5.72 1204.78 0.00 251.06 54.67 251.87 585 27.90 1181.53 317.08 256.14 54.63 5.57 1204.95 0.00 251.01 54.62 251.87 590 27.41 1181.83 332.46 256.10 54.59 5.59 1204.91 0.00 250.96 54.58 251.87 595 27.02 1181.85 350.62 256.05 54.55 5.76 1204.89 0.00 250.91 54.54 251.87 600 27.14 1181.99 337.96 256.00 54.51 5.61 1204.90 0.00 250.86 54.50 251.87 605 27.77 1182.06 322.40 255.94 54.46 5.39 1204.93 0.00 250.81 54.46 301.87 610 27.77 1181.46 288.88 255.89 54.42 5.23 1205.08 0.00 250.76 54.42 301.87 615 27.53 1181.16 250.34 255.82 54.38 5.07 1205.32 0.00 250.71 54.37 301.87 620 27.37 1180.31 236.36 255.77 54.34 4.90 1205.47 0.00 250.66 54.33 301.87 625 27.22 1180.09 225.57 255.71 54.30 4.86 1205.47 0.00 250.61 54.29 301.87 630 26.99 1180.08 227.60 255.66 54.26 4.82 1205.47 0.00 250.56 54.25 301.87 635 26.77 1180.58 241.34 255.61 54.21 4.96 1205.40 0.00 250.51 54.21 301.87 640 26.59 1180.51 255.24 255.57 54.17 5.13 1205.37 0.00 250.45 54.16 301.87 645 26.66 1180.38 247.06 255.52 54.13 4.77 1205.40 0.00 250.40 54.12 301.87 650 26.69 1180.58 248.12 255.47 54.09 4.85 1205.32 0.00 250.35 54.08 301.87 655 26.72 1180.03 252.04 255.42 54.05 5.15 1205.32 0.00 250.30 54.04 301.87 660 25.87 1178.97 226.41 255.37 54.01 4.74 1205.45 0.00 250.25 54.00 301.87  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 14 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 14 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 665         25.53   1177.48     234.07   255.31   53.96     4.81   1205.27     0.00     250.21       53.96         301.87 670         26.01   1178.19     258.72   255.01   53.92     5.81   1201.25     0.09     255.07       53.92         301.87 675         26.88   1178.10     255.58   254.96   53.88     5.90   1188.49     0.65     255.09       53.87         301.87 680         27.03   1176.99     222.88   255.18   53.84     5.51   1177.89     0.82     255.08       53.83         301.87 685         27.32   1177.77     234.35   255.13   53.79     5.89   1179.08     0.53     254.98       53.79         301.87 690         28.96   1178.60     266.16   255.09   53.75     6.21   1178.94     0.68     254.92       53.75         301.87 695         28.67   1178.30     285.31   255.04   53.71     6.39   1180.46     0.47     254.89       53.71         301.87 700         28.28   1177.69     275.35   254.99   53.67     5.93   1191.03     0.07     254.68       53.67         301.87 705         27.51   1177.10     221.73   254.92   53.63     5.34   1202.99     0.00     249.80       53.62         301.87 710         26.20   1176.76     226.97   254.87   53.59     5.30   1204.57     0.00     249.75       53.58         301.87 715         26.07   1176.68     231.41   254.82   53.55     5.32   1204.70     0.00     249.70       53.54         301.87 720         25.81   1176.68     231.83   254.77   53.50     5.36   1204.69     0.00     249.65       53.50         301.87 725         25.40   1176.71     237.27   254.72   53.46     5.36   1204.67     0.00     249.59       53.46         301.87 730         25.32   1176.70     229.92   254.67   53.42     5.25   1204.74     0.00     249.54       53.42         301.87 735         25.25   1176.68     222.03   254.61   53.38     5.06   1204.75     0.00     249.49       53.37         301.87 740         25.02   1176.65     217.70   254.56   53.34     5.17   1204.76     0.00     249.44       53.33         301.87 745         24.79   1176.65     220.01   254.51   53.29     5.22   1204.87     0.00     249.39       53.29         301.87 750         24.75   1176.63     213.97   254.46   53.25     5.01   1204.80     0.00     249.34       53.25         301.87 755         24.42   1176.63     220.85   254.40   53.21     5.22   1204.76     0.00     249.29       53.21         301.87 760         24.31   1176.56     224.99   254.35   53.17     5.13   1204.87     0.00     249.24       53.17         301.87 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 665 25.53 1177.48 234.07 255.31 53.96 4.81 1205.27 0.00 250.21 53.96 301.87 670 26.01 1178.19 258.72 255.01 53.92 5.81 1201.25 0.09 255.07 53.92 301.87 675 26.88 1178.10 255.58 254.96 53.88 5.90 1188.49 0.65 255.09 53.87 301.87 680 27.03 1176.99 222.88 255.18 53.84 5.51 1177.89 0.82 255.08 53.83 301.87 685 27.32 1177.77 234.35 255.13 53.79 5.89 1179.08 0.53 254.98 53.79 301.87 690 28.96 1178.60 266.16 255.09 53.75 6.21 1178.94 0.68 254.92 53.75 301.87 695 28.67 1178.30 285.31 255.04 53.71 6.39 1180.46 0.47 254.89 53.71 301.87 700 28.28 1177.69 275.35 254.99 53.67 5.93 1191.03 0.07 254.68 53.67 301.87 705 27.51 1177.10 221.73 254.92 53.63 5.34 1202.99 0.00 249.80 53.62 301.87 710 26.20 1176.76 226.97 254.87 53.59 5.30 1204.57 0.00 249.75 53.58 301.87 715 26.07 1176.68 231.41 254.82 53.55 5.32 1204.70 0.00 249.70 53.54 301.87 720 25.81 1176.68 231.83 254.77 53.50 5.36 1204.69 0.00 249.65 53.50 301.87 725 25.40 1176.71 237.27 254.72 53.46 5.36 1204.67 0.00 249.59 53.46 301.87 730 25.32 1176.70 229.92 254.67 53.42 5.25 1204.74 0.00 249.54 53.42 301.87 735 25.25 1176.68 222.03 254.61 53.38 5.06 1204.75 0.00 249.49 53.37 301.87 740 25.02 1176.65 217.70 254.56 53.34 5.17 1204.76 0.00 249.44 53.33 301.87 745 24.79 1176.65 220.01 254.51 53.29 5.22 1204.87 0.00 249.39 53.29 301.87 750 24.75 1176.63 213.97 254.46 53.25 5.01 1204.80 0.00 249.34 53.25 301.87 755 24.42 1176.63 220.85 254.40 53.21 5.22 1204.76 0.00 249.29 53.21 301.87 760 24.31 1176.56 224.99 254.35 53.17 5.13 1204.87 0.00 249.24 53.17 301.87  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 15 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 15 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 765         24.26   1176.52     215.18   254.30   53.13     4.96   1204.83     0.00     249.19       53.12         301.87 770         24.09   1176.51     209.85   254.25   53.09     5.17   1204.80     0.00     249.13       53.08         301.87 775         24.14   1176.53     208.88   254.20   53.04     4.88   1204.89     0.00     249.08       53.04         301.87 780         23.63   1176.59     229.88   254.15   53.00     5.03   1204.74     0.00     249.03       53.00         301.87 785         23.58   1176.58     239.83   254.10   52.96     5.18   1204.74     0.00     248.98       52.96         301.87 790         23.65   1176.55     235.12   254.05   52.92     4.94   1204.78     0.00     248.93       52.92         301.87 795         23.33   1176.54     234.43   254.00   52.88     5.02   1204.74     0.00     248.88       52.87         301.87 800         23.14   1176.52     231.85   253.94   52.84     5.20   1204.80     0.00     248.83       52.83         301.87 805         23.29   1176.48     218.85   253.89   52.80     4.81   1204.83     0.00     248.78       52.79         301.87 810         22.99   1176.78     229.13   253.70   52.75     5.11   1204.73     0.00     248.72       52.75         301.87 815         22.80   1176.78     225.98   253.45   52.71     5.01   1204.83     0.00     248.67       52.71         301.87 820         22.32   1176.52     210.71   252.33   52.67     4.71   1192.86     0.12     253.64       52.67         301.87 825         21.72   1177.67     227.24   249.12   52.63     5.20   1180.62     0.23     253.55       52.62         301.87 830         22.54   1177.92     222.46   246.63   52.59     4.78   1177.85     0.28     253.56       52.58         301.87 835         21.51   1177.71     240.40   242.95   52.54     4.79   1178.20     0.31     253.46       52.54         301.87 840         19.39   1178.97     280.58   235.87   52.50     5.22   1178.16     0.35     253.37       52.50         301.87 845         20.33   1178.39     266.18   229.96   52.47     4.81   1177.39     0.52     253.35       52.46         301.87 850         19.72   1177.20     243.59   230.57   52.41     4.86   1177.31     0.64     253.32       52.42         301.87 855         18.44   1178.05     299.71   226.22   52.37     5.30   1177.45     0.53     253.31       52.37         301.87 860         18.92   1179.02     326.12   214.84   52.34     5.05   1179.15     0.29     253.18       52.33         301.87 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 765 24.26 1176.52 215.18 254.30 53.13 4.96 1204.83 0.00 249.19 53.12 301.87 770 24.09 1176.51 209.85 254.25 53.09 5.17 1204.80 0.00 249.13 53.08 301.87 775 24.14 1176.53 208.88 254.20 53.04 4.88 1204.89 0.00 249.08 53.04 301.87 780 23.63 1176.59 229.88 254.15 53.00 5.03 1204.74 0.00 249.03 53.00 301.87 785 23.58 1176.58 239.83 254.10 52.96 5.18 1204.74 0.00 248.98 52.96 301.87 790 23.65 1176.55 235.12 254.05 52.92 4.94 1204.78 0.00 248.93 52.92 301.87 795 23.33 1176.54 234.43 254.00 52.88 5.02 1204.74 0.00 248.88 52.87 301.87 800 23.14 1176.52 231.85 253.94 52.84 5.20 1204.80 0.00 248.83 52.83 301.87 805 23.29 1176.48 218.85 253.89 52.80 4.81 1204.83 0.00 248.78 52.79 301.87 810 22.99 1176.78 229.13 253.70 52.75 5.11 1204.73 0.00 248.72 52.75 301.87 815 22.80 1176.78 225.98 253.45 52.71 5.01 1204.83 0.00 248.67 52.71 301.87 820 22.32 1176.52 210.71 252.33 52.67 4.71 1192.86 0.12 253.64 52.67 301.87 825 21.72 1177.67 227.24 249.12 52.63 5.20 1180.62 0.23 253.55 52.62 301.87 830 22.54 1177.92 222.46 246.63 52.59 4.78 1177.85 0.28 253.56 52.58 301.87 835 21.51 1177.71 240.40 242.95 52.54 4.79 1178.20 0.31 253.46 52.54 301.87 840 19.39 1178.97 280.58 235.87 52.50 5.22 1178.16 0.35 253.37 52.50 301.87 845 20.33 1178.39 266.18 229.96 52.47 4.81 1177.39 0.52 253.35 52.46 301.87 850 19.72 1177.20 243.59 230.57 52.41 4.86 1177.31 0.64 253.32 52.42 301.87 855 18.44 1178.05 299.71 226.22 52.37 5.30 1177.45 0.53 253.31 52.37 301.87 860 18.92 1179.02 326.12 214.84 52.34 5.05 1179.15 0.29 253.18 52.33 301.87  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 16 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 16 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 865         17.80   1178.83     252.70   216.09   52.29     3.99   1179.33     0.34     253.10       52.29         301.87 870         16.97   1179.99     271.38   218.34   52.24     4.75   1177.27     0.74     253.10       52.25         301.87 875         17.45   1180.78     310.02   210.19   52.21     5.82   1177.34     0.92     253.05       52.21         301.87 880         17.93   1179.19     232.52   217.26   52.16     4.08   1177.10     0.87     253.02       52.16         301.87 885         17.29   1179.86     254.57   215.56   52.17     4.74   1177.10     0.96     252.93       52.13         301.87 890         17.24   1180.18     310.69   205.39   52.08     5.53   1177.37     0.83     252.91       52.08         301.88 895         17.26   1178.74     256.64   212.66   52.03     3.82   1177.25     0.91     252.86       52.04         301.88 900         16.92   1180.56     265.04   213.30   52.00     5.05   1177.03     1.18     252.79       52.00         301.87 905         17.88   1180.52     252.95   206.59   51.97     5.21   1177.15     0.95     252.75       51.96         301.88 910         18.01   1179.30     244.00   209.84   51.94     3.74   1177.14     0.97     252.69       51.93         301.87 915         18.20   1180.43     248.91   212.02   51.90     4.87   1177.18     0.96     252.68       51.90         301.88 920         17.89   1179.43     178.18   222.76   51.87     6.27   1181.07     0.47     252.67       51.87         301.88 925         16.65   1179.34     166.34   223.40   51.83     6.84   1207.64     0.14     252.61       51.83         301.88 930         16.95   1178.97     137.39   223.31   51.80     6.70   1233.76     0.00     247.55       51.80         301.88 935         16.88   1178.70     176.77   227.14   51.77     6.93   1236.87     0.00     247.50       51.77         301.88 940         17.01   1178.26     174.69   228.48   51.73     7.04   1236.49     0.00     247.46       51.73         301.88 945         17.74   1177.65     193.15   237.64   51.70     6.00   1226.72     0.18     252.38       51.70         301.88 950         20.25   1179.17     266.62   232.52   51.67     5.46   1195.25     0.50     252.38       51.67         301.88 955         23.16   1177.96     249.89   239.34   51.61     4.86   1176.95     0.83     252.34       51.63         301.88 960         23.46   1178.00     278.10   240.43   51.60     4.36   1176.89     0.70     252.28       51.60         301.88 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 865 17.80 1178.83 252.70 216.09 52.29 3.99 1179.33 0.34 253.10 52.29 301.87 870 16.97 1179.99 271.38 218.34 52.24 4.75 1177.27 0.74 253.10 52.25 301.87 875 17.45 1180.78 310.02 210.19 52.21 5.82 1177.34 0.92 253.05 52.21 301.87 880 17.93 1179.19 232.52 217.26 52.16 4.08 1177.10 0.87 253.02 52.16 301.87 885 17.29 1179.86 254.57 215.56 52.17 4.74 1177.10 0.96 252.93 52.13 301.87 890 17.24 1180.18 310.69 205.39 52.08 5.53 1177.37 0.83 252.91 52.08 301.88 895 17.26 1178.74 256.64 212.66 52.03 3.82 1177.25 0.91 252.86 52.04 301.88 900 16.92 1180.56 265.04 213.30 52.00 5.05 1177.03 1.18 252.79 52.00 301.87 905 17.88 1180.52 252.95 206.59 51.97 5.21 1177.15 0.95 252.75 51.96 301.88 910 18.01 1179.30 244.00 209.84 51.94 3.74 1177.14 0.97 252.69 51.93 301.87 915 18.20 1180.43 248.91 212.02 51.90 4.87 1177.18 0.96 252.68 51.90 301.88 920 17.89 1179.43 178.18 222.76 51.87 6.27 1181.07 0.47 252.67 51.87 301.88 925 16.65 1179.34 166.34 223.40 51.83 6.84 1207.64 0.14 252.61 51.83 301.88 930 16.95 1178.97 137.39 223.31 51.80 6.70 1233.76 0.00 247.55 51.80 301.88 935 16.88 1178.70 176.77 227.14 51.77 6.93 1236.87 0.00 247.50 51.77 301.88 940 17.01 1178.26 174.69 228.48 51.73 7.04 1236.49 0.00 247.46 51.73 301.88 945 17.74 1177.65 193.15 237.64 51.70 6.00 1226.72 0.18 252.38 51.70 301.88 950 20.25 1179.17 266.62 232.52 51.67 5.46 1195.25 0.50 252.38 51.67 301.88 955 23.16 1177.96 249.89 239.34 51.61 4.86 1176.95 0.83 252.34 51.63 301.88 960 23.46 1178.00 278.10 240.43 51.60 4.36 1176.89 0.70 252.28 51.60 301.88  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 17 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 17 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 965         24.63   1177.51     209.56   239.31   51.57     4.08   1178.42     0.22     252.24       51.56         301.88 970         24.97   1175.87     147.55   252.24   51.53     4.27   1184.28     0.04     252.24       51.53         301.88 975         24.22   1175.78     184.87   252.27   51.50     4.60   1184.47     0.04     251.82       51.50         301.88 980         24.53   1175.75     196.38   252.24   51.47     4.23   1190.20     0.02     251.95       51.47         301.88 985         24.32   1175.77     212.19   252.20   51.44     4.58   1201.71     0.00     247.08       51.43         301.88 990         24.62   1175.77     208.66   252.16   51.40     4.09   1204.52     0.00     247.04       51.40         301.88 995         23.90   1175.83     231.24   252.11   51.37     4.34   1195.99     0.06     252.21       51.37         301.88 1000       23.39   1175.81     251.65   252.08   51.34     4.60   1184.97     0.14     251.92       51.33         301.88 1005       23.31   1175.75     234.44   252.03   51.30     4.37   1184.25     0.08     251.91       51.30         301.88 1010       23.02   1175.95     222.89   251.76   51.27     4.40   1195.80     0.00     246.87       51.27         301.88 1015       23.16   1176.03     246.80   251.63   51.24     4.31   1192.74     0.23     251.79       51.23         301.88 1020       22.90   1175.84     265.86   251.81   51.20     4.78   1180.37     0.42     251.79       51.20         301.88 1025       22.97   1175.79     252.45   251.86   51.17     4.68   1180.14     0.21     251.76       51.17         301.88 1030       23.05   1175.74     226.25   251.82   51.14     4.37   1191.89     0.02     252.25       51.13         301.88 1035       22.50   1175.75     218.13   251.77   51.10     4.53   1202.71     0.00     246.66       51.10         301.88 1040       22.45   1176.29     270.51   251.39   51.06     4.50   1204.33     0.00     246.62       51.07         301.88 1045       22.73   1176.19     269.50   251.35   51.03     4.37   1204.63     0.00     246.58       51.03         301.88 1050       22.53   1175.62     219.91   251.64   51.00     4.06   1204.65     0.00     246.53       51.00         301.88 1055       22.27   1175.59     207.85   251.59   50.97     4.18   1202.38     0.01     246.49       50.97         301.88 1060       21.94   1175.65     231.20   251.56   50.94     4.49   1190.07     0.07     251.53       50.93         301.88 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 965 24.63 1177.51 209.56 239.31 51.57 4.08 1178.42 0.22 252.24 51.56 301.88 970 24.97 1175.87 147.55 252.24 51.53 4.27 1184.28 0.04 252.24 51.53 301.88 975 24.22 1175.78 184.87 252.27 51.50 4.60 1184.47 0.04 251.82 51.50 301.88 980 24.53 1175.75 196.38 252.24 51.47 4.23 1190.20 0.02 251.95 51.47 301.88 985 24.32 1175.77 212.19 252.20 51.44 4.58 1201.71 0.00 247.08 51.43 301.88 990 24.62 1175.77 208.66 252.16 51.40 4.09 1204.52 0.00 247.04 51.40 301.88 995 23.90 1175.83 231.24 252.11 51.37 4.34 1195.99 0.06 252.21 51.37 301.88 1000 23.39 1175.81 251.65 252.08 51.34 4.60 1184.97 0.14 251.92 51.33 301.88 1005 23.31 1175.75 234.44 252.03 51.30 4.37 1184.25 0.08 251.91 51.30 301.88 1010 23.02 1175.95 222.89 251.76 51.27 4.40 1195.80 0.00 246.87 51.27 301.88 1015 23.16 1176.03 246.80 251.63 51.24 4.31 1192.74 0.23 251.79 51.23 301.88 1020 22.90 1175.84 265.86 251.81 51.20 4.78 1180.37 0.42 251.79 51.20 301.88 1025 22.97 1175.79 252.45 251.86 51.17 4.68 1180.14 0.21 251.76 51.17 301.88 1030 23.05 1175.74 226.25 251.82 51.14 4.37 1191.89 0.02 252.25 51.13 301.88 1035 22.50 1175.75 218.13 251.77 51.10 4.53 1202.71 0.00 246.66 51.10 301.88 1040 22.45 1176.29 270.51 251.39 51.06 4.50 1204.33 0.00 246.62 51.07 301.88 1045 22.73 1176.19 269.50 251.35 51.03 4.37 1204.63 0.00 246.58 51.03 301.88 1050 22.53 1175.62 219.91 251.64 51.00 4.06 1204.65 0.00 246.53 51.00 301.88 1055 22.27 1175.59 207.85 251.59 50.97 4.18 1202.38 0.01 246.49 50.97 301.88 1060 21.94 1175.65 231.20 251.56 50.94 4.49 1190.07 0.07 251.53 50.93 301.88  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 18 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 18 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 1065       21.83   1175.66     239.80   251.52   50.90     4.40   1182.25     0.07     251.60       50.90         301.88 1070       21.74   1175.59     216.69   251.47   50.87     4.42   1193.73     0.01     246.36       50.87         301.88 1075       22.23   1175.53     184.92   251.42   50.84     4.05   1203.35     0.00     246.32       50.83         301.88 1080       21.72   1175.56     203.55   251.38   50.80     4.44   1191.70     0.16     251.25       50.80         301.88 1085       21.65   1175.54     224.82   251.34   50.77     4.44   1179.26     0.27     251.26       50.77         301.88 1090       21.68   1175.49     201.62   251.30   50.74     4.32   1177.75     0.17     251.15       50.73         301.88 1095       20.75   1176.03     208.73   243.76   50.70     4.34   1178.26     0.10     250.96       50.70         301.88 1100       21.15   1176.56     234.28   243.60   50.68     4.33   1179.36     0.13     251.23       50.67         301.88 1105       20.75   1176.57     274.99   244.68   50.61     4.84   1179.36     0.15     251.13       50.63         301.88 1110       19.43   1177.52     322.60   233.27   50.60     4.94   1186.80     0.06     251.02       50.60         301.88 1115       19.64   1177.89     294.36   228.42   50.57     4.14   1198.38     0.00     245.98       50.57         301.88 1120       18.01   1177.68     273.20   226.40   50.54     4.06   1188.84     0.28     250.85       50.53         301.88 1125       16.54   1179.09     332.81   213.41   50.50     5.01   1177.77     0.59     250.92       50.50         301.88 1130       17.76   1178.55     283.41   215.83   50.45     3.91   1176.57     0.54     250.86       50.47         301.88 1135       16.13   1177.66     266.68   213.73   50.44     3.98   1176.56     0.64     250.81       50.43         301.88 1140       14.99   1177.93     316.84   202.77   50.40     4.86   1176.71     0.61     250.80       50.40         301.88 1145       14.80   1176.97     237.35   213.26   50.37     4.66   1176.56     0.56     250.70       50.37         301.88 1150       13.70   1177.28     254.22   211.19   50.34     6.32   1178.75     0.58     250.71       50.33         301.88 1155       13.34   1177.99     268.99   199.08   50.30     6.66   1197.44     0.24     250.67       50.30         301.88 1160       13.50   1177.15     209.90   208.50   50.25     4.01   1208.01     0.08     250.46       50.26         301.88 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 1065 21.83 1175.66 239.80 251.52 50.90 4.40 1182.25 0.07 251.60 50.90 301.88 1070 21.74 1175.59 216.69 251.47 50.87 4.42 1193.73 0.01 246.36 50.87 301.88 1075 22.23 1175.53 184.92 251.42 50.84 4.05 1203.35 0.00 246.32 50.83 301.88 1080 21.72 1175.56 203.55 251.38 50.80 4.44 1191.70 0.16 251.25 50.80 301.88 1085 21.65 1175.54 224.82 251.34 50.77 4.44 1179.26 0.27 251.26 50.77 301.88 1090 21.68 1175.49 201.62 251.30 50.74 4.32 1177.75 0.17 251.15 50.73 301.88 1095 20.75 1176.03 208.73 243.76 50.70 4.34 1178.26 0.10 250.96 50.70 301.88 1100 21.15 1176.56 234.28 243.60 50.68 4.33 1179.36 0.13 251.23 50.67 301.88 1105 20.75 1176.57 274.99 244.68 50.61 4.84 1179.36 0.15 251.13 50.63 301.88 1110 19.43 1177.52 322.60 233.27 50.60 4.94 1186.80 0.06 251.02 50.60 301.88 1115 19.64 1177.89 294.36 228.42 50.57 4.14 1198.38 0.00 245.98 50.57 301.88 1120 18.01 1177.68 273.20 226.40 50.54 4.06 1188.84 0.28 250.85 50.53 301.88 1125 16.54 1179.09 332.81 213.41 50.50 5.01 1177.77 0.59 250.92 50.50 301.88 1130 17.76 1178.55 283.41 215.83 50.45 3.91 1176.57 0.54 250.86 50.47 301.88 1135 16.13 1177.66 266.68 213.73 50.44 3.98 1176.56 0.64 250.81 50.43 301.88 1140 14.99 1177.93 316.84 202.77 50.40 4.86 1176.71 0.61 250.80 50.40 301.88 1145 14.80 1176.97 237.35 213.26 50.37 4.66 1176.56 0.56 250.70 50.37 301.88 1150 13.70 1177.28 254.22 211.19 50.34 6.32 1178.75 0.58 250.71 50.33 301.88 1155 13.34 1177.99 268.99 199.08 50.30 6.66 1197.44 0.24 250.67 50.30 301.88 1160 13.50 1177.15 209.90 208.50 50.25 4.01 1208.01 0.08 250.46 50.26 301.88  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 19 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 19 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 1165       14.02   1178.05     254.88   205.99   50.24     4.17   1177.60     0.27     250.55       50.23         301.88 1170       14.37   1178.61     286.20   199.32   50.20     4.74   1177.27     0.37     250.50       50.20         301.88 1175       15.61   1177.42     256.10   209.72   50.18     3.42   1176.60     0.43     250.48       50.17         301.88 1180       16.30   1177.73     280.26   203.37   50.14     4.37   1176.61     0.51     250.44       50.13         301.88 1185       16.18   1177.32     235.82   204.44   49.91     3.76   1176.64     0.41     250.39       50.10         301.88 1190       16.31   1177.06     241.18   214.02   50.06     4.11   1176.55     0.55     250.32       50.07         301.88 1195       16.88   1178.14     308.80   204.13   50.03     5.04   1176.59     0.62     250.31       50.03         301.88 1200       17.66   1178.06     259.68   210.10   49.99     4.41   1176.40     0.66     250.23       50.00         301.88 1210       17.72   1177.84     240.85   215.72   49.94     4.63   1176.38     0.68     250.17       49.93         301.88 1220       17.51   1177.09     235.10   215.37   49.87     4.55   1176.45     0.62     250.08       49.87         301.88 1230       18.72   1176.41     231.44   219.72   49.81     4.31   1176.40     0.59     249.99       49.80         301.88 1240       21.09   1176.21     207.39   233.01   49.74     4.09   1177.28     0.37     249.93       49.73         301.88 1250       23.14   1175.55     202.50   246.80   49.67     4.20   1184.65     0.12     249.94       49.67         301.88 1260       23.98   1174.94     193.33   249.71   49.60     4.40   1191.81     0.03     250.09       49.60         301.88 1270       23.41   1174.80     185.95   249.75   49.54     4.34   1198.41     0.00     244.65       49.53         301.88 1280       22.81   1174.84     211.46   249.67   49.47     4.26   1203.96     0.00     244.56       49.47         301.88 1290       22.16   1174.87     218.76   249.58   49.40     4.26   1204.00     0.00     244.48       49.40         301.88 1300       21.47   1174.88     225.03   249.49   49.34     4.22   1203.81     0.00     244.39       49.33         301.88 1310       21.03   1175.37     244.42   248.91   49.27     4.15   1203.36     0.00     244.30       49.27         301.88 1320       20.14   1176.36     269.26   245.05   49.20     4.26   1203.45     0.00     244.22       49.20         301.88 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 1165 14.02 1178.05 254.88 205.99 50.24 4.17 1177.60 0.27 250.55 50.23 301.88 1170 14.37 1178.61 286.20 199.32 50.20 4.74 1177.27 0.37 250.50 50.20 301.88 1175 15.61 1177.42 256.10 209.72 50.18 3.42 1176.60 0.43 250.48 50.17 301.88 1180 16.30 1177.73 280.26 203.37 50.14 4.37 1176.61 0.51 250.44 50.13 301.88 1185 16.18 1177.32 235.82 204.44 49.91 3.76 1176.64 0.41 250.39 50.10 301.88 1190 16.31 1177.06 241.18 214.02 50.06 4.11 1176.55 0.55 250.32 50.07 301.88 1195 16.88 1178.14 308.80 204.13 50.03 5.04 1176.59 0.62 250.31 50.03 301.88 1200 17.66 1178.06 259.68 210.10 49.99 4.41 1176.40 0.66 250.23 50.00 301.88 1210 17.72 1177.84 240.85 215.72 49.94 4.63 1176.38 0.68 250.17 49.93 301.88 1220 17.51 1177.09 235.10 215.37 49.87 4.55 1176.45 0.62 250.08 49.87 301.88 1230 18.72 1176.41 231.44 219.72 49.81 4.31 1176.40 0.59 249.99 49.80 301.88 1240 21.09 1176.21 207.39 233.01 49.74 4.09 1177.28 0.37 249.93 49.73 301.88 1250 23.14 1175.55 202.50 246.80 49.67 4.20 1184.65 0.12 249.94 49.67 301.88 1260 23.98 1174.94 193.33 249.71 49.60 4.40 1191.81 0.03 250.09 49.60 301.88 1270 23.41 1174.80 185.95 249.75 49.54 4.34 1198.41 0.00 244.65 49.53 301.88 1280 22.81 1174.84 211.46 249.67 49.47 4.26 1203.96 0.00 244.56 49.47 301.88 1290 22.16 1174.87 218.76 249.58 49.40 4.26 1204.00 0.00 244.48 49.40 301.88 1300 21.47 1174.88 225.03 249.49 49.34 4.22 1203.81 0.00 244.39 49.33 301.88 1310 21.03 1175.37 244.42 248.91 49.27 4.15 1203.36 0.00 244.30 49.27 301.88 1320 20.14 1176.36 269.26 245.05 49.20 4.26 1203.45 0.00 244.22 49.20 301.88  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 20 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 20 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 1330       19.25   1177.07     302.52   241.29   49.14     4.13   1203.83     0.00     244.13       49.13         301.88 1340       17.51   1177.87     301.64   228.48   49.06     4.13   1201.34     0.01     248.64       49.07         301.88 1350       15.22   1178.03     299.56   215.78   49.00     4.21   1189.09     0.05     248.88       49.00         301.89 1360       13.85   1176.85     268.95   213.24   48.94     3.84   1178.18     0.06     248.96       48.93         301.89 1370       12.01   1177.05     264.88   200.87   48.86     4.28   1181.28     0.06     248.66       48.87         301.89 1380       10.33   1177.45     267.46   196.56   48.81     4.51   1180.14     0.19     248.65       48.80         301.89 1390       10.13   1176.65     210.18   197.46   48.73     3.92   1176.10     0.31     248.61       48.73         301.89 1400       13.37   1176.88     335.28   194.41   48.65     6.34   1177.45     20.09     248.47       48.67         301.88 1410       16.72   1176.82     355.03   201.37   48.60     6.40   1177.10     24.47     248.45       48.60         301.89 1420       17.47   1176.03     279.69   205.55   48.53     4.81   1175.22     11.82     248.33       48.53         301.89 1430       18.74   1175.81     219.60   201.59   48.47     4.62   1175.42     8.40     248.27       48.46         301.89 1440       20.18   1176.11     184.84   213.17   48.41     4.33   1175.43     7.14     248.14       48.41         301.89 1450       19.34   1175.89     193.95   219.68   48.34     4.64   1175.29     7.45     248.11       48.33         301.89 1460       16.65   1175.97     141.72   232.04   48.27     5.12   1179.23     1.76     248.02       48.27         301.89 1470       14.30   1176.75     188.04   225.87   48.20     6.17   1202.78     0.33     247.93       48.20         301.89 1480       13.06   1176.69     212.12   224.13   48.14     6.01   1224.85     0.00     242.81       48.13         301.89 1490       13.28   1176.35     206.06   225.06   48.07     5.92   1225.40     0.00     242.73       48.07         301.89 1500       19.00   1176.82     335.32   222.56   48.00     6.27   1204.08     0.22     247.64       48.00         301.89 1510       24.99   1176.14     328.41   228.87   47.96     6.10   1180.85     0.72     247.58       47.96         301.89 1520       26.02   1175.15     185.76   246.53   47.93     5.44   1185.14     0.51     247.57       47.92         301.89 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 1330 19.25 1177.07 302.52 241.29 49.14 4.13 1203.83 0.00 244.13 49.13 301.88 1340 17.51 1177.87 301.64 228.48 49.06 4.13 1201.34 0.01 248.64 49.07 301.88 1350 15.22 1178.03 299.56 215.78 49.00 4.21 1189.09 0.05 248.88 49.00 301.89 1360 13.85 1176.85 268.95 213.24 48.94 3.84 1178.18 0.06 248.96 48.93 301.89 1370 12.01 1177.05 264.88 200.87 48.86 4.28 1181.28 0.06 248.66 48.87 301.89 1380 10.33 1177.45 267.46 196.56 48.81 4.51 1180.14 0.19 248.65 48.80 301.89 1390 10.13 1176.65 210.18 197.46 48.73 3.92 1176.10 0.31 248.61 48.73 301.89 1400 13.37 1176.88 335.28 194.41 48.65 6.34 1177.45 20.09 248.47 48.67 301.88 1410 16.72 1176.82 355.03 201.37 48.60 6.40 1177.10 24.47 248.45 48.60 301.89 1420 17.47 1176.03 279.69 205.55 48.53 4.81 1175.22 11.82 248.33 48.53 301.89 1430 18.74 1175.81 219.60 201.59 48.47 4.62 1175.42 8.40 248.27 48.46 301.89 1440 20.18 1176.11 184.84 213.17 48.41 4.33 1175.43 7.14 248.14 48.41 301.89 1450 19.34 1175.89 193.95 219.68 48.34 4.64 1175.29 7.45 248.11 48.33 301.89 1460 16.65 1175.97 141.72 232.04 48.27 5.12 1179.23 1.76 248.02 48.27 301.89 1470 14.30 1176.75 188.04 225.87 48.20 6.17 1202.78 0.33 247.93 48.20 301.89 1480 13.06 1176.69 212.12 224.13 48.14 6.01 1224.85 0.00 242.81 48.13 301.89 1490 13.28 1176.35 206.06 225.06 48.07 5.92 1225.40 0.00 242.73 48.07 301.89 1500 19.00 1176.82 335.32 222.56 48.00 6.27 1204.08 0.22 247.64 48.00 301.89 1510 24.99 1176.14 328.41 228.87 47.96 6.10 1180.85 0.72 247.58 47.96 301.89 1520 26.02 1175.15 185.76 246.53 47.93 5.44 1185.14 0.51 247.57 47.92 301.89  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 21 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 21 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 1530       26.49   1175.75     175.36   247.48   47.88     5.28   1198.68     0.00     242.48       47.88         301.89 1540       26.34   1175.74     199.51   247.53   47.84     5.15   1202.14     0.00     242.42       47.84         301.89 1550       25.25   1175.40     250.22   241.71   47.80     5.24   1201.94     0.00     242.37       47.80         301.89 1560       25.43   1175.75     245.85   241.44   47.76     5.32   1201.89     0.00     242.31       47.76         301.89 1570       25.50   1177.09     206.55   246.32   47.72     5.14   1202.04     0.00     242.26       47.72         301.89 1580       24.59   1178.05     200.98   246.37   47.68     4.99   1202.03     0.00     242.21       47.68         301.89 1590       24.11   1177.08     197.40   247.25   47.64     5.01   1201.98     0.00     242.16       47.64         301.89 1600       22.33   1177.17     232.84   247.20   47.60     5.13   1201.87     0.00     242.10       47.60         301.89 1610       20.28   1177.76     254.97   244.06   47.56     5.24   1201.79     0.00     242.05       47.56         301.89 1620       17.68   1177.26     247.30   231.92   47.53     5.06   1200.06     0.00     242.00       47.52         301.89 1630       13.96   1176.36     262.39   213.34   47.48     4.86   1190.71     0.06     246.79       47.48         301.89 1640       11.02   1176.44     321.56   198.17   47.40     4.98   1179.97     0.35     246.87       47.44         301.89 1650         9.39   1176.63     306.59   193.47   47.41     4.56   1176.27     0.45     246.83       47.40         301.89 1660         7.78   1175.66     237.10   189.19   47.35     4.41   1183.71     0.19     246.85       47.36         301.89 1670         6.12   1175.64     267.73   186.38   47.24     4.36   1201.56     0.03     247.18       47.32         301.89 1680         5.19   1176.46     255.85   187.94   47.28     3.62   1215.01     0.00     241.67       47.28         301.89 1690         6.41   1175.88     239.39   191.14   47.25     3.63   1213.63     0.00     241.62       47.24         301.89 1700         7.59   1176.08     290.02   192.98   47.11     4.02   1210.67     0.00     241.57       47.20         301.89 1710         7.88   1176.07     266.98   195.92   47.16     3.82   1210.99     0.00     241.51       47.16         301.89 1720         9.09   1175.35     249.26   198.13   47.13     4.02   1212.99     0.00     241.45       47.12         301.89 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 1530 26.49 1175.75 175.36 247.48 47.88 5.28 1198.68 0.00 242.48 47.88 301.89 1540 26.34 1175.74 199.51 247.53 47.84 5.15 1202.14 0.00 242.42 47.84 301.89 1550 25.25 1175.40 250.22 241.71 47.80 5.24 1201.94 0.00 242.37 47.80 301.89 1560 25.43 1175.75 245.85 241.44 47.76 5.32 1201.89 0.00 242.31 47.76 301.89 1570 25.50 1177.09 206.55 246.32 47.72 5.14 1202.04 0.00 242.26 47.72 301.89 1580 24.59 1178.05 200.98 246.37 47.68 4.99 1202.03 0.00 242.21 47.68 301.89 1590 24.11 1177.08 197.40 247.25 47.64 5.01 1201.98 0.00 242.16 47.64 301.89 1600 22.33 1177.17 232.84 247.20 47.60 5.13 1201.87 0.00 242.10 47.60 301.89 1610 20.28 1177.76 254.97 244.06 47.56 5.24 1201.79 0.00 242.05 47.56 301.89 1620 17.68 1177.26 247.30 231.92 47.53 5.06 1200.06 0.00 242.00 47.52 301.89 1630 13.96 1176.36 262.39 213.34 47.48 4.86 1190.71 0.06 246.79 47.48 301.89 1640 11.02 1176.44 321.56 198.17 47.40 4.98 1179.97 0.35 246.87 47.44 301.89 1650 9.39 1176.63 306.59 193.47 47.41 4.56 1176.27 0.45 246.83 47.40 301.89 1660 7.78 1175.66 237.10 189.19 47.35 4.41 1183.71 0.19 246.85 47.36 301.89 1670 6.12 1175.64 267.73 186.38 47.24 4.36 1201.56 0.03 247.18 47.32 301.89 1680 5.19 1176.46 255.85 187.94 47.28 3.62 1215.01 0.00 241.67 47.28 301.89 1690 6.41 1175.88 239.39 191.14 47.25 3.63 1213.63 0.00 241.62 47.24 301.89 1700 7.59 1176.08 290.02 192.98 47.11 4.02 1210.67 0.00 241.57 47.20 301.89 1710 7.88 1176.07 266.98 195.92 47.16 3.82 1210.99 0.00 241.51 47.16 301.89 1720 9.09 1175.35 249.26 198.13 47.13 4.02 1212.99 0.00 241.45 47.12 301.89  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 22 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 22 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 1730         9.61   1175.52     275.56   199.15   47.05     4.39   1212.27     0.00     241.40       47.08         301.89 1740         9.98   1175.72     249.71   204.12   47.04     4.40   1211.30     0.00     241.35       47.04         301.89 1750       11.00   1177.76     270.22   208.78   47.00     4.31   1203.13     0.80     246.24       47.00         301.89 1760       21.34   1176.20     356.99   214.03   46.98     5.01   1183.15     2.13     246.23       46.95         301.89 1770       24.77   1174.79     240.94   216.75   46.92     5.12   1176.04     1.38     246.22       46.92         301.89 1780       17.12   1174.84       98.05   213.69   46.88     5.13   1190.72     0.06     246.18       46.88         301.89 1790       16.22   1174.80     116.91   228.22   46.84     6.10   1204.39     0.00     241.08       46.84         301.89 1800       17.25   1174.23     127.18   243.23   46.80     6.28   1207.93     0.00     241.02       46.80         301.89 1810       17.50   1174.08     141.14   245.99   46.76     6.22   1207.68     0.00     240.97       46.76         301.89 1820       16.84   1174.39     161.10   245.97   46.72     6.10   1207.41     0.00     240.92       46.72         301.89 1830       15.45   1174.72     204.02   241.42   46.68     6.01   1207.04     0.00     240.86       46.68         301.89 1840       14.44   1175.16     274.64   228.25   46.70     5.46   1200.52     0.01     240.81       46.64         301.89 1850       15.13   1175.41     289.94   225.31   46.58     4.76   1186.36     0.04     245.58       46.60         301.89 1860       15.53   1175.41     225.40   232.52   46.56     4.72   1182.65     0.05     245.57       46.56         301.89 1870       14.74   1175.39     215.79   226.43   46.52     4.67   1184.99     0.04     245.49       46.52         301.89 1880       15.10   1175.49     241.89   223.04   46.48     4.10   1183.17     0.03     245.44       46.48         301.89 1890       15.33   1175.40     263.41   217.54   46.45     3.42   1186.32     0.02     245.79       46.44         301.89 1900       13.46   1175.00     275.44   208.62   46.41     3.96   1195.75     0.01     240.47       46.40         301.89 1910       13.27   1175.31     278.26   210.65   46.33     4.46   1190.70     0.05     245.41       46.36         301.89 1920       14.26   1175.39     272.39   210.74   46.32     4.12   1182.76     0.06     245.43       46.32         301.89 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 1730 9.61 1175.52 275.56 199.15 47.05 4.39 1212.27 0.00 241.40 47.08 301.89 1740 9.98 1175.72 249.71 204.12 47.04 4.40 1211.30 0.00 241.35 47.04 301.89 1750 11.00 1177.76 270.22 208.78 47.00 4.31 1203.13 0.80 246.24 47.00 301.89 1760 21.34 1176.20 356.99 214.03 46.98 5.01 1183.15 2.13 246.23 46.95 301.89 1770 24.77 1174.79 240.94 216.75 46.92 5.12 1176.04 1.38 246.22 46.92 301.89 1780 17.12 1174.84 98.05 213.69 46.88 5.13 1190.72 0.06 246.18 46.88 301.89 1790 16.22 1174.80 116.91 228.22 46.84 6.10 1204.39 0.00 241.08 46.84 301.89 1800 17.25 1174.23 127.18 243.23 46.80 6.28 1207.93 0.00 241.02 46.80 301.89 1810 17.50 1174.08 141.14 245.99 46.76 6.22 1207.68 0.00 240.97 46.76 301.89 1820 16.84 1174.39 161.10 245.97 46.72 6.10 1207.41 0.00 240.92 46.72 301.89 1830 15.45 1174.72 204.02 241.42 46.68 6.01 1207.04 0.00 240.86 46.68 301.89 1840 14.44 1175.16 274.64 228.25 46.70 5.46 1200.52 0.01 240.81 46.64 301.89 1850 15.13 1175.41 289.94 225.31 46.58 4.76 1186.36 0.04 245.58 46.60 301.89 1860 15.53 1175.41 225.40 232.52 46.56 4.72 1182.65 0.05 245.57 46.56 301.89 1870 14.74 1175.39 215.79 226.43 46.52 4.67 1184.99 0.04 245.49 46.52 301.89 1880 15.10 1175.49 241.89 223.04 46.48 4.10 1183.17 0.03 245.44 46.48 301.89 1890 15.33 1175.40 263.41 217.54 46.45 3.42 1186.32 0.02 245.79 46.44 301.89 1900 13.46 1175.00 275.44 208.62 46.41 3.96 1195.75 0.01 240.47 46.40 301.89 1910 13.27 1175.31 278.26 210.65 46.33 4.46 1190.70 0.05 245.41 46.36 301.89 1920 14.26 1175.39 272.39 210.74 46.32 4.12 1182.76 0.06 245.43 46.32 301.89  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 23 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 23 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 1930       14.31   1175.81     249.44   205.85   46.28     4.02   1182.61     0.02     245.33       46.28         301.89 1940       14.21   1176.77     246.04   203.64   46.24     3.81   1184.61     0.01     244.97       46.24         301.89 1950       14.93   1177.36     223.18   209.53   46.20     2.89   1190.19     0.00     240.21       46.19         301.89 1960       15.10   1178.01     240.46   209.78   46.16     2.42   1197.24     0.00     240.15       46.16         301.89 1970       14.28   1178.43     257.28   205.60   46.13     3.13   1199.86     0.00     240.09       46.12         301.89 1980       13.36   1177.80     264.47   200.20   46.09     3.40   1201.40     0.00     240.03       46.08         301.90 1990       12.99   1176.04     257.97   198.59   45.91     2.69   1205.61     0.00     239.98       46.04         301.90 2000       12.92   1174.94     254.80   203.30   46.00     2.51   1205.71     0.00     239.92       46.00         301.90 2010       12.75   1174.22     245.29   206.08   45.97     2.53   1200.04     0.00     239.88       45.97         301.90 2020       11.55   1173.98     257.56   198.31   45.95     2.63   1200.30     0.00     239.84       45.94         301.90 2030       10.08   1174.43     292.00   191.62   45.86     2.54   1203.35     0.00     239.80       45.91         301.90 2040       10.09   1174.63     235.62   195.59   45.88     2.07   1203.49     0.00     239.76       45.88         301.90 2050       10.03   1175.88     241.87   195.99   45.86     2.85   1202.80     0.00     239.72       45.85         301.90 2060         9.86   1177.89     293.14   191.70   45.79     3.07   1201.26     0.00     239.68       45.82         301.90 2070         9.78   1179.03     261.28   191.51   45.79     2.56   1200.54     0.00     239.64       45.79         301.90 2080       10.01   1178.70     214.97   194.45   45.76     2.73   1199.97     0.00     239.59       45.76         301.90 2090       10.58   1177.97     268.62   193.91   45.72     2.74   1200.03     0.00     239.55       45.73         301.90 2100       11.03   1178.51     288.25   195.35   45.71     2.91   1199.45     0.02     244.64       45.70         301.90 2110       12.18   1178.52     238.53   201.04   45.63     2.96   1192.60     0.02     244.40       45.67         301.90 2120       13.02   1178.10     206.77   205.20   45.64     2.95   1194.38     0.01     243.49       45.64         301.90 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 1930 14.31 1175.81 249.44 205.85 46.28 4.02 1182.61 0.02 245.33 46.28 301.89 1940 14.21 1176.77 246.04 203.64 46.24 3.81 1184.61 0.01 244.97 46.24 301.89 1950 14.93 1177.36 223.18 209.53 46.20 2.89 1190.19 0.00 240.21 46.19 301.89 1960 15.10 1178.01 240.46 209.78 46.16 2.42 1197.24 0.00 240.15 46.16 301.89 1970 14.28 1178.43 257.28 205.60 46.13 3.13 1199.86 0.00 240.09 46.12 301.89 1980 13.36 1177.80 264.47 200.20 46.09 3.40 1201.40 0.00 240.03 46.08 301.90 1990 12.99 1176.04 257.97 198.59 45.91 2.69 1205.61 0.00 239.98 46.04 301.90 2000 12.92 1174.94 254.80 203.30 46.00 2.51 1205.71 0.00 239.92 46.00 301.90 2010 12.75 1174.22 245.29 206.08 45.97 2.53 1200.04 0.00 239.88 45.97 301.90 2020 11.55 1173.98 257.56 198.31 45.95 2.63 1200.30 0.00 239.84 45.94 301.90 2030 10.08 1174.43 292.00 191.62 45.86 2.54 1203.35 0.00 239.80 45.91 301.90 2040 10.09 1174.63 235.62 195.59 45.88 2.07 1203.49 0.00 239.76 45.88 301.90 2050 10.03 1175.88 241.87 195.99 45.86 2.85 1202.80 0.00 239.72 45.85 301.90 2060 9.86 1177.89 293.14 191.70 45.79 3.07 1201.26 0.00 239.68 45.82 301.90 2070 9.78 1179.03 261.28 191.51 45.79 2.56 1200.54 0.00 239.64 45.79 301.90 2080 10.01 1178.70 214.97 194.45 45.76 2.73 1199.97 0.00 239.59 45.76 301.90 2090 10.58 1177.97 268.62 193.91 45.72 2.74 1200.03 0.00 239.55 45.73 301.90 2100 11.03 1178.51 288.25 195.35 45.71 2.91 1199.45 0.02 244.64 45.70 301.90 2110 12.18 1178.52 238.53 201.04 45.63 2.96 1192.60 0.02 244.40 45.67 301.90 2120 13.02 1178.10 206.77 205.20 45.64 2.95 1194.38 0.01 243.49 45.64 301.90  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 24 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 24 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 2130       13.30   1178.00     204.62   203.40   45.61     3.39   1191.05     0.02     244.14       45.61         301.90 2140       14.27   1178.18     235.21   203.05   45.58     3.30   1188.69     0.01     239.34       45.58         301.90 2150       14.87   1177.50     229.89   206.74   45.55     2.59   1194.16     0.00     239.30       45.55         301.90 2160       14.37   1177.31     230.56   206.44   45.52     2.61   1196.63     0.00     239.26       45.52         301.90 2170       13.85   1177.59     254.91   205.77   45.49     3.45   1197.19     0.00     239.22       45.49         301.90 2180       14.12   1177.95     262.08   209.85   45.44     3.12   1197.23     0.00     239.18       45.46         301.90 2190       13.81   1179.09     255.27   207.35   45.43     2.43   1199.91     0.00     239.13       45.43         301.90 2200       14.07   1177.70     214.48   208.84   45.40     2.37   1195.09     0.00     239.09       45.40         301.90 2210       13.43   1176.81     187.24   212.76   45.37     2.76   1198.58     0.00     239.05       45.37         301.90 2220       13.32   1177.65     242.68   210.36   45.34     2.50   1201.72     0.00     239.01       45.34         301.90 2230       13.82   1178.41     282.79   208.21   45.31     2.34   1196.71     0.00     238.97       45.31         301.90 2240       13.14   1178.98     268.70   207.36   45.26     3.09   1198.51     0.00     238.93       45.28         301.90 2250       13.53   1178.46     261.03   209.29   45.26     2.76   1202.82     0.00     238.88       45.25         301.90 2260       13.32   1178.04     274.96   202.13   45.22     2.67   1199.81     0.00     238.84       45.22         301.90 2270       13.28   1177.08     269.13   200.05   45.19     2.99   1194.71     0.00     238.80       45.19         301.90 2280       13.33   1176.87     250.29   201.40   45.16     2.62   1192.34     0.00     238.76       45.16         301.90 2290       13.31   1176.55     236.84   202.66   45.13     2.36   1198.39     0.00     238.72       45.13         301.90 2300       13.13   1176.26     228.27   202.59   45.10     2.20   1203.37     0.00     238.67       45.10         301.90 2310       12.83   1176.65     232.93   200.49   45.07     2.56   1193.79     0.00     238.63       45.07         301.90 2320       13.65   1177.12     250.72   200.33   45.03     2.25   1190.38     0.00     238.59       45.04         301.90 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 2130 13.30 1178.00 204.62 203.40 45.61 3.39 1191.05 0.02 244.14 45.61 301.90 2140 14.27 1178.18 235.21 203.05 45.58 3.30 1188.69 0.01 239.34 45.58 301.90 2150 14.87 1177.50 229.89 206.74 45.55 2.59 1194.16 0.00 239.30 45.55 301.90 2160 14.37 1177.31 230.56 206.44 45.52 2.61 1196.63 0.00 239.26 45.52 301.90 2170 13.85 1177.59 254.91 205.77 45.49 3.45 1197.19 0.00 239.22 45.49 301.90 2180 14.12 1177.95 262.08 209.85 45.44 3.12 1197.23 0.00 239.18 45.46 301.90 2190 13.81 1179.09 255.27 207.35 45.43 2.43 1199.91 0.00 239.13 45.43 301.90 2200 14.07 1177.70 214.48 208.84 45.40 2.37 1195.09 0.00 239.09 45.40 301.90 2210 13.43 1176.81 187.24 212.76 45.37 2.76 1198.58 0.00 239.05 45.37 301.90 2220 13.32 1177.65 242.68 210.36 45.34 2.50 1201.72 0.00 239.01 45.34 301.90 2230 13.82 1178.41 282.79 208.21 45.31 2.34 1196.71 0.00 238.97 45.31 301.90 2240 13.14 1178.98 268.70 207.36 45.26 3.09 1198.51 0.00 238.93 45.28 301.90 2250 13.53 1178.46 261.03 209.29 45.26 2.76 1202.82 0.00 238.88 45.25 301.90 2260 13.32 1178.04 274.96 202.13 45.22 2.67 1199.81 0.00 238.84 45.22 301.90 2270 13.28 1177.08 269.13 200.05 45.19 2.99 1194.71 0.00 238.80 45.19 301.90 2280 13.33 1176.87 250.29 201.40 45.16 2.62 1192.34 0.00 238.76 45.16 301.90 2290 13.31 1176.55 236.84 202.66 45.13 2.36 1198.39 0.00 238.72 45.13 301.90 2300 13.13 1176.26 228.27 202.59 45.10 2.20 1203.37 0.00 238.67 45.10 301.90 2310 12.83 1176.65 232.93 200.49 45.07 2.56 1193.79 0.00 238.63 45.07 301.90 2320 13.65 1177.12 250.72 200.33 45.03 2.25 1190.38 0.00 238.59 45.04 301.90  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 25 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 25 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 2330       13.36   1178.13     253.86   198.64   45.01     2.28   1198.25     0.00     238.55       45.01         301.90 2340       11.86   1178.02     243.56   202.12   44.98     3.20   1201.87     0.00     238.51       44.98         301.90 2350       12.58   1177.50     249.14   206.92   45.24     2.72   1202.30     0.00     238.46       44.95         301.90 2360       13.07   1177.71     257.10   204.79   44.92     2.12   1200.34     0.00     238.42       44.92         301.90 2370       12.57   1177.12     243.77   202.99   44.89     2.35   1193.70     0.01     238.38       44.89         301.90 2380       13.04   1177.21     233.84   203.63   44.86     2.67   1194.61     0.00     238.34       44.86         301.90 2390       13.07   1178.08     275.37   199.92   44.83     2.08   1198.56     0.00     238.29       44.83         301.90 2400       12.37   1177.64     282.07   195.14   44.80     2.41   1201.80     0.00     238.25       44.80         301.90 2410       12.32   1177.33     269.60   196.07   44.74     2.68   1201.89     0.00     238.21       44.77         301.90 2420       12.20   1177.24     254.49   198.27   44.74     1.93   1198.91     0.00     238.17       44.74         301.90 2430       11.72   1176.69     221.21   196.59   44.71     2.23   1194.68     0.00     238.13       44.71         301.90 2440       12.69   1177.22     252.21   196.43   44.68     1.99   1193.15     0.00     238.08       44.68         301.90 2450       12.51   1177.78     265.72   193.28   44.65     2.36   1199.83     0.00     238.04       44.65         301.90 2460       12.65   1178.19     254.90   194.74   44.63     2.47   1197.10     0.00     238.00       44.62         301.90 2470       12.85   1178.38     251.42   196.83   44.59     2.11   1194.65     0.00     237.96       44.59         301.90 2480       12.48   1178.28     235.33   200.14   44.53     2.40   1196.66     0.00     237.91       44.56         301.90 2490       12.49   1177.67     235.09   201.13   44.53     2.05   1197.94     0.00     237.87       44.53         301.90 2500       12.50   1177.55     232.66   200.30   44.50     2.24   1194.70     0.00     237.83       44.50         301.90 2510       12.63   1178.05     241.38   201.11   44.47     2.20   1193.51     0.00     237.79       44.47         301.90 2520       12.50   1177.46     253.89   198.59   44.42     2.32   1193.52     0.00     237.74       44.44         301.90 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 2330 13.36 1178.13 253.86 198.64 45.01 2.28 1198.25 0.00 238.55 45.01 301.90 2340 11.86 1178.02 243.56 202.12 44.98 3.20 1201.87 0.00 238.51 44.98 301.90 2350 12.58 1177.50 249.14 206.92 45.24 2.72 1202.30 0.00 238.46 44.95 301.90 2360 13.07 1177.71 257.10 204.79 44.92 2.12 1200.34 0.00 238.42 44.92 301.90 2370 12.57 1177.12 243.77 202.99 44.89 2.35 1193.70 0.01 238.38 44.89 301.90 2380 13.04 1177.21 233.84 203.63 44.86 2.67 1194.61 0.00 238.34 44.86 301.90 2390 13.07 1178.08 275.37 199.92 44.83 2.08 1198.56 0.00 238.29 44.83 301.90 2400 12.37 1177.64 282.07 195.14 44.80 2.41 1201.80 0.00 238.25 44.80 301.90 2410 12.32 1177.33 269.60 196.07 44.74 2.68 1201.89 0.00 238.21 44.77 301.90 2420 12.20 1177.24 254.49 198.27 44.74 1.93 1198.91 0.00 238.17 44.74 301.90 2430 11.72 1176.69 221.21 196.59 44.71 2.23 1194.68 0.00 238.13 44.71 301.90 2440 12.69 1177.22 252.21 196.43 44.68 1.99 1193.15 0.00 238.08 44.68 301.90 2450 12.51 1177.78 265.72 193.28 44.65 2.36 1199.83 0.00 238.04 44.65 301.90 2460 12.65 1178.19 254.90 194.74 44.63 2.47 1197.10 0.00 238.00 44.62 301.90 2470 12.85 1178.38 251.42 196.83 44.59 2.11 1194.65 0.00 237.96 44.59 301.90 2480 12.48 1178.28 235.33 200.14 44.53 2.40 1196.66 0.00 237.91 44.56 301.90 2490 12.49 1177.67 235.09 201.13 44.53 2.05 1197.94 0.00 237.87 44.53 301.90 2500 12.50 1177.55 232.66 200.30 44.50 2.24 1194.70 0.00 237.83 44.50 301.90 2510 12.63 1178.05 241.38 201.11 44.47 2.20 1193.51 0.00 237.79 44.47 301.90 2520 12.50 1177.46 253.89 198.59 44.42 2.32 1193.52 0.00 237.74 44.44 301.90  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 26 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 26 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 2530       12.36   1177.08     256.25   196.96   44.39     2.90   1195.30     0.00     237.70       44.41         301.90 2540       12.42   1176.77     276.94   194.54   44.37     2.37   1198.47     0.00     237.66       44.38         301.90 2550       13.02   1176.60     270.95   194.95   44.36     2.10   1200.07     0.00     237.62       44.35         301.90 2560       12.83   1176.32     239.93   195.60   44.32     2.76   1202.47     0.00     237.57       44.32         301.90 2570       12.63   1176.57     260.29   194.28   44.30     2.35   1199.10     0.00     237.53       44.29         301.90 2580       13.01   1176.58     262.47   194.97   44.26     2.07   1195.19     0.00     237.49       44.26         301.90 2590       12.49   1176.20     241.81   193.09   44.24     2.80   1199.10     0.00     237.45       44.23         301.90 2600       11.90   1176.68     263.70   192.76   44.20     2.62   1199.78     0.00     237.40       44.20         301.90 2610       11.92   1177.05     256.18   193.58   44.17     2.66   1198.93     0.00     237.36       44.17         301.90 2620       11.74   1176.89     254.17   193.50   44.12     2.58   1196.77     0.00     237.32       44.14         301.90 2630       11.57   1176.38     257.59   196.02   44.10     2.36   1197.02     0.00     237.28       44.11         301.90 2640       11.49   1176.99     233.90   196.75   44.08     2.34   1201.14     0.00     237.23       44.08         301.90 2650       11.75   1177.26     223.96   195.71   44.05     2.11   1201.55     0.00     237.19       44.05         301.90 2660       12.17   1177.16     238.23   192.24   44.02     2.47   1201.57     0.00     237.15       44.02         301.90 2670       12.37   1177.10     249.44   192.82   43.99     2.21   1200.03     0.00     237.10       43.99         301.90 2680       12.45   1177.07     242.01   195.94   43.96     2.18   1200.83     0.00     237.06       43.96         301.90 2690       12.55   1177.10     253.23   193.86   43.93     2.62   1202.68     0.00     237.02       43.93         301.90 2700       11.92   1176.98     266.46   190.97   43.90     2.49   1200.44     0.00     236.97       43.90         301.90 2710       11.78   1176.70     248.67   191.94   43.86     2.66   1198.77     0.00     236.93       43.87         301.90 2720       11.79   1176.34     263.58   192.28   43.82     2.56   1198.63     0.00     236.89       43.84         301.90 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 2530 12.36 1177.08 256.25 196.96 44.39 2.90 1195.30 0.00 237.70 44.41 301.90 2540 12.42 1176.77 276.94 194.54 44.37 2.37 1198.47 0.00 237.66 44.38 301.90 2550 13.02 1176.60 270.95 194.95 44.36 2.10 1200.07 0.00 237.62 44.35 301.90 2560 12.83 1176.32 239.93 195.60 44.32 2.76 1202.47 0.00 237.57 44.32 301.90 2570 12.63 1176.57 260.29 194.28 44.30 2.35 1199.10 0.00 237.53 44.29 301.90 2580 13.01 1176.58 262.47 194.97 44.26 2.07 1195.19 0.00 237.49 44.26 301.90 2590 12.49 1176.20 241.81 193.09 44.24 2.80 1199.10 0.00 237.45 44.23 301.90 2600 11.90 1176.68 263.70 192.76 44.20 2.62 1199.78 0.00 237.40 44.20 301.90 2610 11.92 1177.05 256.18 193.58 44.17 2.66 1198.93 0.00 237.36 44.17 301.90 2620 11.74 1176.89 254.17 193.50 44.12 2.58 1196.77 0.00 237.32 44.14 301.90 2630 11.57 1176.38 257.59 196.02 44.10 2.36 1197.02 0.00 237.28 44.11 301.90 2640 11.49 1176.99 233.90 196.75 44.08 2.34 1201.14 0.00 237.23 44.08 301.90 2650 11.75 1177.26 223.96 195.71 44.05 2.11 1201.55 0.00 237.19 44.05 301.90 2660 12.17 1177.16 238.23 192.24 44.02 2.47 1201.57 0.00 237.15 44.02 301.90 2670 12.37 1177.10 249.44 192.82 43.99 2.21 1200.03 0.00 237.10 43.99 301.90 2680 12.45 1177.07 242.01 195.94 43.96 2.18 1200.83 0.00 237.06 43.96 301.90 2690 12.55 1177.10 253.23 193.86 43.93 2.62 1202.68 0.00 237.02 43.93 301.90 2700 11.92 1176.98 266.46 190.97 43.90 2.49 1200.44 0.00 236.97 43.90 301.90 2710 11.78 1176.70 248.67 191.94 43.86 2.66 1198.77 0.00 236.93 43.87 301.90 2720 11.79 1176.34 263.58 192.28 43.82 2.56 1198.63 0.00 236.89 43.84 301.90  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 27 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 27 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 2730       12.10   1175.81     268.62   192.53   43.82     2.37   1198.77     0.00     236.84       43.81         301.90 2740       12.14   1175.67     245.70   191.94   43.78     2.82   1200.23     0.00     236.80       43.78         301.90 2750       12.50   1176.39     287.69   192.08   43.76     2.21   1202.02     0.00     236.76       43.75         301.90 2760       12.47   1176.72     290.53   194.33   43.66     1.71   1204.48     0.00     236.72       43.72         301.90 2770       11.48   1176.15     242.01   198.55   43.69     2.05   1202.19     0.00     236.67       43.69         301.90 2780       11.35   1175.76     240.22   199.20   43.66     1.66   1200.45     0.00     236.63       43.66         301.90 2790       11.56   1175.37     265.35   194.94   43.60     1.76   1199.10     0.00     236.59       43.63         301.90 2800       12.02   1174.67     261.00   194.16   43.58     2.51   1200.63     0.00     236.54       43.60         301.90 2810       11.42   1175.70     270.84   192.43   43.56     2.38   1201.49     0.00     236.50       43.57         301.90 2820       11.30   1176.67     264.28   191.41   43.55     2.59   1198.99     0.00     236.46       43.54         301.90 2830       11.65   1177.26     263.93   191.62   43.52     2.50   1195.94     0.00     236.41       43.51         301.90 2840       11.49   1177.21     261.57   192.70   43.48     2.43   1196.19     0.00     236.37       43.48         301.90 2850       12.04   1177.02     258.58   194.77   43.45     2.38   1196.77     0.00     236.33       43.45         301.90 2860       12.31   1176.92     271.84   191.11   43.42     2.01   1198.09     0.00     236.28       43.42         301.90 2870       11.55   1176.27     241.87   189.90   42.95     2.57   1202.40     0.00     236.24       43.39         301.90 2880       11.20   1177.21     238.23   196.05   43.36     2.66   1201.80     0.00     236.20       43.36         301.90 2890       12.36   1177.88     251.71   195.46   43.33     2.17   1200.89     0.00     236.15       43.33         301.90 2900       12.87   1177.12     267.37   191.13   43.30     1.98   1201.10     0.00     236.11       43.30         301.90 2910       11.76   1176.44     248.01   191.13   43.27     2.23   1201.34     0.00     236.07       43.27         301.90 2920       12.12   1177.06     240.84   193.95   43.24     2.28   1198.69     0.00     236.02       43.24         301.90 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 2730 12.10 1175.81 268.62 192.53 43.82 2.37 1198.77 0.00 236.84 43.81 301.90 2740 12.14 1175.67 245.70 191.94 43.78 2.82 1200.23 0.00 236.80 43.78 301.90 2750 12.50 1176.39 287.69 192.08 43.76 2.21 1202.02 0.00 236.76 43.75 301.90 2760 12.47 1176.72 290.53 194.33 43.66 1.71 1204.48 0.00 236.72 43.72 301.90 2770 11.48 1176.15 242.01 198.55 43.69 2.05 1202.19 0.00 236.67 43.69 301.90 2780 11.35 1175.76 240.22 199.20 43.66 1.66 1200.45 0.00 236.63 43.66 301.90 2790 11.56 1175.37 265.35 194.94 43.60 1.76 1199.10 0.00 236.59 43.63 301.90 2800 12.02 1174.67 261.00 194.16 43.58 2.51 1200.63 0.00 236.54 43.60 301.90 2810 11.42 1175.70 270.84 192.43 43.56 2.38 1201.49 0.00 236.50 43.57 301.90 2820 11.30 1176.67 264.28 191.41 43.55 2.59 1198.99 0.00 236.46 43.54 301.90 2830 11.65 1177.26 263.93 191.62 43.52 2.50 1195.94 0.00 236.41 43.51 301.90 2840 11.49 1177.21 261.57 192.70 43.48 2.43 1196.19 0.00 236.37 43.48 301.90 2850 12.04 1177.02 258.58 194.77 43.45 2.38 1196.77 0.00 236.33 43.45 301.90 2860 12.31 1176.92 271.84 191.11 43.42 2.01 1198.09 0.00 236.28 43.42 301.90 2870 11.55 1176.27 241.87 189.90 42.95 2.57 1202.40 0.00 236.24 43.39 301.90 2880 11.20 1177.21 238.23 196.05 43.36 2.66 1201.80 0.00 236.20 43.36 301.90 2890 12.36 1177.88 251.71 195.46 43.33 2.17 1200.89 0.00 236.15 43.33 301.90 2900 12.87 1177.12 267.37 191.13 43.30 1.98 1201.10 0.00 236.11 43.30 301.90 2910 11.76 1176.44 248.01 191.13 43.27 2.23 1201.34 0.00 236.07 43.27 301.90 2920 12.12 1177.06 240.84 193.95 43.24 2.28 1198.69 0.00 236.02 43.24 301.90  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 28 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 28 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 2930       11.36   1176.82     231.17   190.99   43.21     2.33   1199.43     0.00     235.98       43.21         301.90 2940       10.44   1176.89     220.55   193.30   43.18     2.55   1202.91     0.00     235.94       43.18         301.91 2950       10.96   1176.79     210.61   198.58   43.15     2.17   1202.53     0.00     235.89       43.15         301.91 2960       10.72   1176.04     223.22   195.07   43.12     2.22   1200.24     0.00     235.85       43.12         301.90 2970       11.24   1175.52     296.82   192.76   43.09     2.08   1198.37     0.00     235.81       43.09         301.90 2980       11.56   1174.62     272.49   191.73   43.06     2.22   1196.87     0.00     235.76       43.06         301.90 2990         9.97   1175.47     240.42   189.17   43.03     2.80   1199.91     0.00     235.72       43.03         301.90 3000       10.14   1175.85     276.97   190.89   42.99     2.39   1201.57     0.00     235.68       43.00         301.91 3010       10.85   1174.77     266.93   192.80   42.95     2.43   1199.28     0.00     235.60       42.95         301.91 3020       10.78   1173.96     266.06   192.12   42.91     2.48   1196.46     0.00     235.53       42.90         301.91 3030       11.91   1174.53     280.03   189.86   42.85     2.13   1196.89     0.00     235.45       42.85         301.91 3040       11.60   1175.13     245.12   188.77   42.80     2.09   1200.95     0.00     235.38       42.80         301.91 3050       11.44   1175.69     246.09   192.54   42.75     2.23   1199.19     0.00     235.31       42.75         301.91 3060       11.98   1175.67     265.08   189.70   42.70     2.19   1199.65     0.00     235.24       42.70         301.91 3070       12.01   1174.81     245.72   189.16   42.65     1.81   1201.45     0.00     235.16       42.65         301.91 3080       11.90   1175.41     233.14   191.81   42.60     1.84   1198.47     0.00     235.09       42.60         301.91 3090       11.89   1175.40     249.55   189.99   42.56     2.20   1199.12     0.00     235.02       42.55         301.91 3100       12.42   1174.95     274.15   189.16   42.50     2.30   1201.26     0.00     234.94       42.50         301.91 3110       11.31   1175.87     250.18   187.79   42.45     2.38   1199.56     0.00     234.87       42.45         301.91 3120         9.81   1175.20     226.87   188.25   42.40     2.22   1198.76     0.00     234.80       42.40         301.91 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 2930 11.36 1176.82 231.17 190.99 43.21 2.33 1199.43 0.00 235.98 43.21 301.90 2940 10.44 1176.89 220.55 193.30 43.18 2.55 1202.91 0.00 235.94 43.18 301.91 2950 10.96 1176.79 210.61 198.58 43.15 2.17 1202.53 0.00 235.89 43.15 301.91 2960 10.72 1176.04 223.22 195.07 43.12 2.22 1200.24 0.00 235.85 43.12 301.90 2970 11.24 1175.52 296.82 192.76 43.09 2.08 1198.37 0.00 235.81 43.09 301.90 2980 11.56 1174.62 272.49 191.73 43.06 2.22 1196.87 0.00 235.76 43.06 301.90 2990 9.97 1175.47 240.42 189.17 43.03 2.80 1199.91 0.00 235.72 43.03 301.90 3000 10.14 1175.85 276.97 190.89 42.99 2.39 1201.57 0.00 235.68 43.00 301.91 3010 10.85 1174.77 266.93 192.80 42.95 2.43 1199.28 0.00 235.60 42.95 301.91 3020 10.78 1173.96 266.06 192.12 42.91 2.48 1196.46 0.00 235.53 42.90 301.91 3030 11.91 1174.53 280.03 189.86 42.85 2.13 1196.89 0.00 235.45 42.85 301.91 3040 11.60 1175.13 245.12 188.77 42.80 2.09 1200.95 0.00 235.38 42.80 301.91 3050 11.44 1175.69 246.09 192.54 42.75 2.23 1199.19 0.00 235.31 42.75 301.91 3060 11.98 1175.67 265.08 189.70 42.70 2.19 1199.65 0.00 235.24 42.70 301.91 3070 12.01 1174.81 245.72 189.16 42.65 1.81 1201.45 0.00 235.16 42.65 301.91 3080 11.90 1175.41 233.14 191.81 42.60 1.84 1198.47 0.00 235.09 42.60 301.91 3090 11.89 1175.40 249.55 189.99 42.56 2.20 1199.12 0.00 235.02 42.55 301.91 3100 12.42 1174.95 274.15 189.16 42.50 2.30 1201.26 0.00 234.94 42.50 301.91 3110 11.31 1175.87 250.18 187.79 42.45 2.38 1199.56 0.00 234.87 42.45 301.91 3120 9.81 1175.20 226.87 188.25 42.40 2.22 1198.76 0.00 234.80 42.40 301.91  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 29 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 29 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 3130       10.76   1173.55     252.44   191.54   42.35     2.18   1196.63     0.00     234.72       42.35         301.91 3140       10.61   1173.91     231.81   192.09   42.31     2.43   1198.10     0.00     234.65       42.30         301.91 3150       10.67   1175.36     243.62   190.04   42.25     2.06   1201.22     0.00     234.57       42.25         301.91 3160       11.37   1175.07     252.60   188.47   42.19     2.12   1199.26     0.00     234.50       42.20         301.91 3170         9.44   1174.08     237.32   184.24   42.13     2.50   1201.13     0.00     234.43       42.15         301.91 3180       10.16   1174.22     278.28   186.96   42.11     2.00   1199.73     0.00     234.36       42.10         301.91 3190       11.88   1174.80     281.80   188.48   42.05     2.04   1194.80     0.00     234.28       42.05         301.91 3200       10.94   1174.60     259.80   186.33   42.01     2.72   1198.03     0.00     234.21       42.00         301.91 3210       11.29   1174.51     270.78   189.28   41.96     2.31   1197.94     0.00     234.13       41.95         301.91 3220       11.79   1175.02     272.52   186.86   41.88     1.96   1196.61     0.00     234.06       41.90         301.91 3230       11.18   1174.45     247.16   184.92   41.83     2.58   1199.79     0.00     233.98       41.85         301.91 3240       11.76   1174.89     255.00   189.21   41.81     2.15   1199.01     0.00     233.91       41.80         301.91 3250       12.15   1175.34     258.45   185.20   41.74     1.79   1198.39     0.00     233.84       41.75         301.91 3260       10.98   1174.26     232.62   182.65   41.67     2.49   1201.26     0.00     233.76       41.70         301.91 3270       10.09   1174.60     229.02   189.72   41.65     2.84   1201.43     0.00     233.69       41.65         301.91 3280       11.21   1175.25     259.39   190.17   41.60     2.27   1199.10     0.00     233.61       41.60         301.91 3290       11.05   1174.29     237.82   186.57   41.55     2.10   1199.82     0.00     233.54       41.55         301.91 3300         9.52   1173.82     223.23   190.19   41.51     2.37   1202.43     0.00     233.46       41.50         301.91 3310       10.85   1174.76     262.36   194.21   41.45     2.18   1199.64     0.00     233.39       41.45         301.91 3320       11.71   1174.76     278.39   188.92   41.40     2.04   1198.48     0.00     233.31       41.40         301.91 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 3130 10.76 1173.55 252.44 191.54 42.35 2.18 1196.63 0.00 234.72 42.35 301.91 3140 10.61 1173.91 231.81 192.09 42.31 2.43 1198.10 0.00 234.65 42.30 301.91 3150 10.67 1175.36 243.62 190.04 42.25 2.06 1201.22 0.00 234.57 42.25 301.91 3160 11.37 1175.07 252.60 188.47 42.19 2.12 1199.26 0.00 234.50 42.20 301.91 3170 9.44 1174.08 237.32 184.24 42.13 2.50 1201.13 0.00 234.43 42.15 301.91 3180 10.16 1174.22 278.28 186.96 42.11 2.00 1199.73 0.00 234.36 42.10 301.91 3190 11.88 1174.80 281.80 188.48 42.05 2.04 1194.80 0.00 234.28 42.05 301.91 3200 10.94 1174.60 259.80 186.33 42.01 2.72 1198.03 0.00 234.21 42.00 301.91 3210 11.29 1174.51 270.78 189.28 41.96 2.31 1197.94 0.00 234.13 41.95 301.91 3220 11.79 1175.02 272.52 186.86 41.88 1.96 1196.61 0.00 234.06 41.90 301.91 3230 11.18 1174.45 247.16 184.92 41.83 2.58 1199.79 0.00 233.98 41.85 301.91 3240 11.76 1174.89 255.00 189.21 41.81 2.15 1199.01 0.00 233.91 41.80 301.91 3250 12.15 1175.34 258.45 185.20 41.74 1.79 1198.39 0.00 233.84 41.75 301.91 3260 10.98 1174.26 232.62 182.65 41.67 2.49 1201.26 0.00 233.76 41.70 301.91 3270 10.09 1174.60 229.02 189.72 41.65 2.84 1201.43 0.00 233.69 41.65 301.91 3280 11.21 1175.25 259.39 190.17 41.60 2.27 1199.10 0.00 233.61 41.60 301.91 3290 11.05 1174.29 237.82 186.57 41.55 2.10 1199.82 0.00 233.54 41.55 301.91 3300 9.52 1173.82 223.23 190.19 41.51 2.37 1202.43 0.00 233.46 41.50 301.91 3310 10.85 1174.76 262.36 194.21 41.45 2.18 1199.64 0.00 233.39 41.45 301.91 3320 11.71 1174.76 278.39 188.92 41.40 2.04 1198.48 0.00 233.31 41.40 301.91  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 30 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 30 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 3330       11.45   1173.77     283.97   184.57   41.35     2.00   1200.66     0.00     233.24       41.35         301.91 3340       10.98   1173.70     253.54   186.97   41.23     2.39   1200.86     0.00     233.16       41.30         301.91 3350       10.40   1173.84     238.19   192.40   41.25     2.49   1200.87     0.00     233.09       41.25         301.91 3360       11.72   1173.56     280.22   192.54   41.20     2.38   1199.29     0.00     233.01       41.20         301.91 3370       12.35   1174.15     309.63   188.37   41.15     2.24   1199.26     0.00     232.93       41.15         301.91 3380       10.98   1173.75     271.47   187.54   41.10     2.06   1201.13     0.00     232.86       41.10         301.91 3390       11.35   1172.80     257.33   192.04   41.01     2.03   1197.94     0.00     232.78       41.05         301.91 3400       11.89   1173.28     284.53   187.19   41.00     2.04   1197.32     0.00     232.71       41.00         301.91 3410       10.48   1173.17     253.59   182.37   40.95     2.38   1200.25     0.00     232.63       40.95         301.91 3420         9.87   1172.69     225.14   189.86   40.90     2.45   1200.19     0.00     232.56       40.90         301.91 3430       11.02   1173.17     250.89   190.08   40.85     2.22   1196.80     0.00     232.48       40.85         301.91 3440       11.53   1173.16     273.45   183.56   40.80     2.04   1195.69     0.00     232.40       40.80         301.91 3450       10.31   1172.61     251.21   184.09   40.75     2.23   1200.09     0.00     232.33       40.75         301.91 3460         9.87   1173.07     230.68   190.11   40.70     2.26   1201.45     0.00     232.25       40.70         301.91 3470       11.17   1173.39     247.89   189.20   40.65     2.06   1199.01     0.00     232.18       40.65         301.91 3480       10.27   1173.42     238.36   185.45   40.60     2.24   1199.52     0.00     232.10       40.60         301.91 3490         9.49   1173.67     233.68   188.23   40.55     2.11   1201.82     0.00     232.02       40.55         301.91 3500       11.04   1173.69     263.30   188.84   40.49     2.05   1197.76     0.00     231.95       40.50         301.91 3510       10.55   1173.12     258.89   185.97   40.43     2.04   1197.49     0.00     231.87       40.45         301.91 3520       10.51   1172.61     258.87   186.41   40.40     2.05   1198.80     0.00     231.80       40.40         301.91 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 3330 11.45 1173.77 283.97 184.57 41.35 2.00 1200.66 0.00 233.24 41.35 301.91 3340 10.98 1173.70 253.54 186.97 41.23 2.39 1200.86 0.00 233.16 41.30 301.91 3350 10.40 1173.84 238.19 192.40 41.25 2.49 1200.87 0.00 233.09 41.25 301.91 3360 11.72 1173.56 280.22 192.54 41.20 2.38 1199.29 0.00 233.01 41.20 301.91 3370 12.35 1174.15 309.63 188.37 41.15 2.24 1199.26 0.00 232.93 41.15 301.91 3380 10.98 1173.75 271.47 187.54 41.10 2.06 1201.13 0.00 232.86 41.10 301.91 3390 11.35 1172.80 257.33 192.04 41.01 2.03 1197.94 0.00 232.78 41.05 301.91 3400 11.89 1173.28 284.53 187.19 41.00 2.04 1197.32 0.00 232.71 41.00 301.91 3410 10.48 1173.17 253.59 182.37 40.95 2.38 1200.25 0.00 232.63 40.95 301.91 3420 9.87 1172.69 225.14 189.86 40.90 2.45 1200.19 0.00 232.56 40.90 301.91 3430 11.02 1173.17 250.89 190.08 40.85 2.22 1196.80 0.00 232.48 40.85 301.91 3440 11.53 1173.16 273.45 183.56 40.80 2.04 1195.69 0.00 232.40 40.80 301.91 3450 10.31 1172.61 251.21 184.09 40.75 2.23 1200.09 0.00 232.33 40.75 301.91 3460 9.87 1173.07 230.68 190.11 40.70 2.26 1201.45 0.00 232.25 40.70 301.91 3470 11.17 1173.39 247.89 189.20 40.65 2.06 1199.01 0.00 232.18 40.65 301.91 3480 10.27 1173.42 238.36 185.45 40.60 2.24 1199.52 0.00 232.10 40.60 301.91 3490 9.49 1173.67 233.68 188.23 40.55 2.11 1201.82 0.00 232.02 40.55 301.91 3500 11.04 1173.69 263.30 188.84 40.49 2.05 1197.76 0.00 231.95 40.50 301.91 3510 10.55 1173.12 258.89 185.97 40.43 2.04 1197.49 0.00 231.87 40.45 301.91 3520 10.51 1172.61 258.87 186.41 40.40 2.05 1198.80 0.00 231.80 40.40 301.91  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 31 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 31 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 3530       11.16   1172.76     279.20   184.26   40.35     2.19   1197.73     0.00     231.72       40.35         301.91 3540         9.47   1172.40     243.04   183.41   40.31     2.14   1200.30     0.00     231.64       40.30         301.91 3550         9.56   1172.24     225.68   188.63   40.25     1.91   1202.55     0.00     231.56       40.25         301.91 3560       10.95   1172.36     254.66   187.57   40.21     2.00   1199.87     0.00     231.49       40.20         301.91 3570         9.27   1172.45     229.46   182.82   40.15     2.26   1199.84     0.00     231.41       40.15         301.92 3580         9.86   1172.80     230.74   188.24   40.10     1.85   1202.37     0.00     231.33       40.10         301.91 3590       11.01   1172.95     258.78   189.85   40.04     2.02   1198.04     0.00     231.26       40.05         301.91 3600         8.87   1173.06     244.76   184.16   40.00     2.34   1198.71     0.00     231.18       40.00         301.92 3610         9.66   1172.73     267.47   188.44   39.93     1.76   1202.65     0.00     231.10       39.95         301.91 3620       10.89   1172.39     266.96   190.79   39.89     1.99   1200.09     0.00     231.02       39.90         301.91 3630         8.89   1172.53     250.00   185.78   39.82     2.44   1200.71     0.00     230.95       39.85         301.91 3640         9.60   1172.69     277.46   186.87   39.80     1.78   1201.49     0.00     230.87       39.80         301.92 3650       10.61   1172.42     259.62   187.01   39.76     2.03   1199.20     0.00     230.79       39.75         301.92 3660         8.63   1172.37     245.75   184.84   39.69     2.45   1201.23     0.00     230.72       39.70         301.92 3670         9.58   1172.57     272.09   187.39   39.66     1.69   1200.90     0.00     230.64       39.65         301.92 3680       10.56   1172.26     257.78   186.84   39.61     2.01   1198.09     0.00     230.56       39.60         301.92 3690         8.52   1172.17     243.60   185.49   39.56     2.51   1201.14     0.00     230.48       39.55         301.92 3700         9.29   1172.47     269.74   186.50   39.51     1.78   1199.23     0.00     230.41       39.50         301.92 3710       10.62   1172.17     279.28   183.99   39.45     1.72   1193.49     0.00     230.33       39.45         301.92 3720         9.70   1171.83     253.68   182.34   39.41     2.43   1198.44     0.00     230.25       39.40         301.92 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 3530 11.16 1172.76 279.20 184.26 40.35 2.19 1197.73 0.00 231.72 40.35 301.91 3540 9.47 1172.40 243.04 183.41 40.31 2.14 1200.30 0.00 231.64 40.30 301.91 3550 9.56 1172.24 225.68 188.63 40.25 1.91 1202.55 0.00 231.56 40.25 301.91 3560 10.95 1172.36 254.66 187.57 40.21 2.00 1199.87 0.00 231.49 40.20 301.91 3570 9.27 1172.45 229.46 182.82 40.15 2.26 1199.84 0.00 231.41 40.15 301.92 3580 9.86 1172.80 230.74 188.24 40.10 1.85 1202.37 0.00 231.33 40.10 301.91 3590 11.01 1172.95 258.78 189.85 40.04 2.02 1198.04 0.00 231.26 40.05 301.91 3600 8.87 1173.06 244.76 184.16 40.00 2.34 1198.71 0.00 231.18 40.00 301.92 3610 9.66 1172.73 267.47 188.44 39.93 1.76 1202.65 0.00 231.10 39.95 301.91 3620 10.89 1172.39 266.96 190.79 39.89 1.99 1200.09 0.00 231.02 39.90 301.91 3630 8.89 1172.53 250.00 185.78 39.82 2.44 1200.71 0.00 230.95 39.85 301.91 3640 9.60 1172.69 277.46 186.87 39.80 1.78 1201.49 0.00 230.87 39.80 301.92 3650 10.61 1172.42 259.62 187.01 39.76 2.03 1199.20 0.00 230.79 39.75 301.92 3660 8.63 1172.37 245.75 184.84 39.69 2.45 1201.23 0.00 230.72 39.70 301.92 3670 9.58 1172.57 272.09 187.39 39.66 1.69 1200.90 0.00 230.64 39.65 301.92 3680 10.56 1172.26 257.78 186.84 39.61 2.01 1198.09 0.00 230.56 39.60 301.92 3690 8.52 1172.17 243.60 185.49 39.56 2.51 1201.14 0.00 230.48 39.55 301.92 3700 9.29 1172.47 269.74 186.50 39.51 1.78 1199.23 0.00 230.41 39.50 301.92 3710 10.62 1172.17 279.28 183.99 39.45 1.72 1193.49 0.00 230.33 39.45 301.92 3720 9.70 1171.83 253.68 182.34 39.41 2.43 1198.44 0.00 230.25 39.40 301.92  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 32 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 32 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 3730         8.49   1171.85     242.06   183.93   39.36     2.65   1201.59     0.00     230.17       39.35         301.92 3740         9.35   1171.80     269.87   185.29   39.31     1.96   1199.08     0.00     230.09       39.30         301.92 3750       10.22   1171.70     263.03   184.42   39.25     2.21   1197.26     0.00     230.02       39.25         301.92 3760       10.74   1172.05     261.15   186.25   39.21     1.92   1196.64     0.00     229.94       39.20         301.92 3770       10.79   1172.45     248.31   186.01   39.14     1.76   1197.44     0.00     229.86       39.15         301.92 3780         8.65   1172.62     233.27   184.47   39.10     2.45   1202.15     0.00     229.78       39.10         301.92 3790         9.43   1172.48     271.43   184.97   39.04     1.73   1198.62     0.00     229.70       39.05         301.92 3800       10.57   1172.00     275.24   182.16   38.96     1.61   1193.60     0.00     229.62       39.00         301.92 3810         9.56   1171.51     253.48   182.76   38.95     2.32   1200.18     0.00     229.54       38.95         301.92 3820         8.21   1171.63     245.66   185.51   38.91     2.50   1203.09     0.00     229.46       38.90         301.92 3830         9.47   1172.09     263.98   186.24   38.85     1.76   1199.94     0.00     229.39       38.85         301.92 3840       10.17   1171.87     249.10   183.42   38.80     1.93   1198.00     0.00     229.31       38.80         301.92 3850         7.95   1171.64     232.95   182.63   38.72     2.45   1201.86     0.00     229.23       38.75         301.92 3860         9.05   1171.98     269.68   184.88   38.69     1.80   1198.24     0.00     229.15       38.70         301.92 3870       10.19   1171.68     283.63   182.05   38.65     1.65   1194.28     0.00     229.07       38.65         301.92 3880         9.07   1171.29     257.36   180.86   38.60     2.37   1199.05     0.00     228.99       38.60         301.92 3890         8.28   1171.48     238.84   184.94   38.53     2.60   1201.44     0.00     228.91       38.55         301.92 3900         9.73   1171.90     258.76   185.13   38.50     1.82   1198.38     0.00     228.83       38.50         301.92 3910       10.26   1171.61     249.68   183.10   38.43     1.95   1196.49     0.00     228.75       38.45         301.92 3920         8.19   1171.33     239.06   184.13   38.39     2.51   1201.56     0.00     228.67       38.40         301.92 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 3730 8.49 1171.85 242.06 183.93 39.36 2.65 1201.59 0.00 230.17 39.35 301.92 3740 9.35 1171.80 269.87 185.29 39.31 1.96 1199.08 0.00 230.09 39.30 301.92 3750 10.22 1171.70 263.03 184.42 39.25 2.21 1197.26 0.00 230.02 39.25 301.92 3760 10.74 1172.05 261.15 186.25 39.21 1.92 1196.64 0.00 229.94 39.20 301.92 3770 10.79 1172.45 248.31 186.01 39.14 1.76 1197.44 0.00 229.86 39.15 301.92 3780 8.65 1172.62 233.27 184.47 39.10 2.45 1202.15 0.00 229.78 39.10 301.92 3790 9.43 1172.48 271.43 184.97 39.04 1.73 1198.62 0.00 229.70 39.05 301.92 3800 10.57 1172.00 275.24 182.16 38.96 1.61 1193.60 0.00 229.62 39.00 301.92 3810 9.56 1171.51 253.48 182.76 38.95 2.32 1200.18 0.00 229.54 38.95 301.92 3820 8.21 1171.63 245.66 185.51 38.91 2.50 1203.09 0.00 229.46 38.90 301.92 3830 9.47 1172.09 263.98 186.24 38.85 1.76 1199.94 0.00 229.39 38.85 301.92 3840 10.17 1171.87 249.10 183.42 38.80 1.93 1198.00 0.00 229.31 38.80 301.92 3850 7.95 1171.64 232.95 182.63 38.72 2.45 1201.86 0.00 229.23 38.75 301.92 3860 9.05 1171.98 269.68 184.88 38.69 1.80 1198.24 0.00 229.15 38.70 301.92 3870 10.19 1171.68 283.63 182.05 38.65 1.65 1194.28 0.00 229.07 38.65 301.92 3880 9.07 1171.29 257.36 180.86 38.60 2.37 1199.05 0.00 228.99 38.60 301.92 3890 8.28 1171.48 238.84 184.94 38.53 2.60 1201.44 0.00 228.91 38.55 301.92 3900 9.73 1171.90 258.76 185.13 38.50 1.82 1198.38 0.00 228.83 38.50 301.92 3910 10.26 1171.61 249.68 183.10 38.43 1.95 1196.49 0.00 228.75 38.45 301.92 3920 8.19 1171.33 239.06 184.13 38.39 2.51 1201.56 0.00 228.67 38.40 301.92  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 33 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 33 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 3930         9.26   1171.75     267.74   184.79   38.33     1.71   1198.80     0.00     228.59       38.35         301.92 3940       10.34   1171.57     274.24   182.10   38.28     1.52   1193.40     0.00     228.51       38.30         301.92 3950         9.31   1171.18     249.18   180.42   38.25     2.36   1199.07     0.00     228.43       38.25         301.92 3960         8.41   1171.22     236.40   184.16   38.21     2.61   1201.60     0.00     228.35       38.20         301.92 3970         9.49   1171.60     262.67   185.68   38.16     1.82   1199.09     0.00     228.27       38.15         301.92 3980       10.19   1171.41     254.87   183.44   38.10     1.98   1197.48     0.00     228.19       38.10         301.92 3990         8.31   1171.13     233.62   182.92   38.06     2.48   1200.93     0.00     228.11       38.05         301.92 4000         9.27   1171.57     265.68   185.35   38.01     1.60   1199.94     0.00     228.03       38.00         301.92 4010         9.95   1171.42     261.01   184.42   37.98     1.95   1197.56     0.00     228.00       37.98         301.92 4020         7.83   1171.15     231.08   181.53   37.96     2.45   1200.64     0.00     227.96       37.96         301.92 4030         8.32   1171.46     262.98   182.16   37.95     1.66   1199.92     0.00     227.93       37.94         301.92 4040         9.58   1171.38     279.54   181.17   37.93     1.71   1194.91     0.00     227.90       37.92         301.92 4050         9.63   1171.29     243.89   180.34   37.90     1.96   1196.73     0.00     227.87       37.90         301.92 4060         9.22   1171.41     250.01   179.99   37.86     2.12   1198.53     0.00     227.84       37.88         301.92 4070         7.81   1171.39     245.93   178.64   37.86     2.41   1199.85     0.00     227.80       37.86         301.92 4080         8.57   1171.10     232.45   182.74   37.84     1.94   1201.65     0.00     227.77       37.84         301.92 4090         9.49   1171.31     270.79   182.32   37.83     2.00   1196.98     0.00     227.74       37.82         301.92 4100         7.93   1171.58     259.83   177.64   37.80     2.53   1197.61     0.00     227.70       37.80         301.92 4110         7.80   1171.16     245.77   179.51   37.79     2.12   1201.20     0.00     227.67       37.78         301.92 4120         8.83   1171.19     278.95   181.37   37.76     1.92   1197.70     0.00     227.64       37.76         301.92 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 3930 9.26 1171.75 267.74 184.79 38.33 1.71 1198.80 0.00 228.59 38.35 301.92 3940 10.34 1171.57 274.24 182.10 38.28 1.52 1193.40 0.00 228.51 38.30 301.92 3950 9.31 1171.18 249.18 180.42 38.25 2.36 1199.07 0.00 228.43 38.25 301.92 3960 8.41 1171.22 236.40 184.16 38.21 2.61 1201.60 0.00 228.35 38.20 301.92 3970 9.49 1171.60 262.67 185.68 38.16 1.82 1199.09 0.00 228.27 38.15 301.92 3980 10.19 1171.41 254.87 183.44 38.10 1.98 1197.48 0.00 228.19 38.10 301.92 3990 8.31 1171.13 233.62 182.92 38.06 2.48 1200.93 0.00 228.11 38.05 301.92 4000 9.27 1171.57 265.68 185.35 38.01 1.60 1199.94 0.00 228.03 38.00 301.92 4010 9.95 1171.42 261.01 184.42 37.98 1.95 1197.56 0.00 228.00 37.98 301.92 4020 7.83 1171.15 231.08 181.53 37.96 2.45 1200.64 0.00 227.96 37.96 301.92 4030 8.32 1171.46 262.98 182.16 37.95 1.66 1199.92 0.00 227.93 37.94 301.92 4040 9.58 1171.38 279.54 181.17 37.93 1.71 1194.91 0.00 227.90 37.92 301.92 4050 9.63 1171.29 243.89 180.34 37.90 1.96 1196.73 0.00 227.87 37.90 301.92 4060 9.22 1171.41 250.01 179.99 37.86 2.12 1198.53 0.00 227.84 37.88 301.92 4070 7.81 1171.39 245.93 178.64 37.86 2.41 1199.85 0.00 227.80 37.86 301.92 4080 8.57 1171.10 232.45 182.74 37.84 1.94 1201.65 0.00 227.77 37.84 301.92 4090 9.49 1171.31 270.79 182.32 37.83 2.00 1196.98 0.00 227.74 37.82 301.92 4100 7.93 1171.58 259.83 177.64 37.80 2.53 1197.61 0.00 227.70 37.80 301.92 4110 7.80 1171.16 245.77 179.51 37.79 2.12 1201.20 0.00 227.67 37.78 301.92 4120 8.83 1171.19 278.95 181.37 37.76 1.92 1197.70 0.00 227.64 37.76 301.92  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 34 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 34 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 4130         9.40   1171.32     294.00   180.76   37.74     2.14   1197.71     0.00     227.61       37.74         301.92 4140         8.84   1171.05     259.29   181.26   37.72     2.35   1200.85     0.00     227.58       37.72         301.92 4150         7.81   1170.92     236.50   182.66   37.70     2.24   1201.08     0.00     227.54       37.70         301.92 4160         8.71   1171.34     269.84   180.62   37.68     2.01   1197.83     0.00     227.51       37.68         301.92 4170         9.78   1171.49     288.14   177.12   37.66     1.99   1195.90     0.00     227.48       37.66         301.92 4180         8.84   1171.25     251.75   177.17   37.63     2.27   1199.09     0.00     227.45       37.64         301.92 4190         7.64   1171.02     225.48   180.25   37.62     2.51   1200.45     0.00     227.41       37.62         301.92 4200         8.56   1171.15     259.92   181.14   37.61     1.79   1197.77     0.00     227.38       37.60         301.92 4210         8.83   1171.04     260.28   180.29   37.58     1.98   1198.06     0.00     227.35       37.58         301.92 4220         7.68   1170.80     231.08   180.48   37.56     2.53   1200.87     0.00     227.32       37.56         301.92 4230         8.64   1171.13     260.93   181.44   37.51     1.72   1197.92     0.00     227.28       37.54         301.92 4240         8.86   1171.02     262.73   181.09   37.49     1.93   1197.24     0.00     227.26       37.52         301.92 4250         7.42   1170.73     231.38   180.81   37.50     2.65   1200.46     0.00     227.22       37.50         301.92 4260         8.01   1171.01     262.96   182.08   37.48     1.96   1198.33     0.00     227.19       37.48         301.92 4270         8.72   1170.94     285.16   181.24   37.46     1.56   1194.49     0.00     227.16       37.46         301.92 4280         8.44   1170.61     247.85   181.18   37.45     2.27   1198.63     0.00     227.12       37.44         301.92 4290         7.80   1170.67     228.28   181.93   37.42     2.59   1200.44     0.00     227.09       37.42         301.92 4300         8.35   1170.99     247.21   181.42   37.40     1.80   1199.75     0.00     227.06       37.40         301.92 4310         8.52   1170.99     252.46   180.96   37.37     1.94   1199.63     0.00     227.02       37.38         301.92 4320         7.62   1170.79     234.23   180.11   37.33     2.62   1200.60     0.00     226.99       37.36         301.92 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 4130 9.40 1171.32 294.00 180.76 37.74 2.14 1197.71 0.00 227.61 37.74 301.92 4140 8.84 1171.05 259.29 181.26 37.72 2.35 1200.85 0.00 227.58 37.72 301.92 4150 7.81 1170.92 236.50 182.66 37.70 2.24 1201.08 0.00 227.54 37.70 301.92 4160 8.71 1171.34 269.84 180.62 37.68 2.01 1197.83 0.00 227.51 37.68 301.92 4170 9.78 1171.49 288.14 177.12 37.66 1.99 1195.90 0.00 227.48 37.66 301.92 4180 8.84 1171.25 251.75 177.17 37.63 2.27 1199.09 0.00 227.45 37.64 301.92 4190 7.64 1171.02 225.48 180.25 37.62 2.51 1200.45 0.00 227.41 37.62 301.92 4200 8.56 1171.15 259.92 181.14 37.61 1.79 1197.77 0.00 227.38 37.60 301.92 4210 8.83 1171.04 260.28 180.29 37.58 1.98 1198.06 0.00 227.35 37.58 301.92 4220 7.68 1170.80 231.08 180.48 37.56 2.53 1200.87 0.00 227.32 37.56 301.92 4230 8.64 1171.13 260.93 181.44 37.51 1.72 1197.92 0.00 227.28 37.54 301.92 4240 8.86 1171.02 262.73 181.09 37.49 1.93 1197.24 0.00 227.26 37.52 301.92 4250 7.42 1170.73 231.38 180.81 37.50 2.65 1200.46 0.00 227.22 37.50 301.92 4260 8.01 1171.01 262.96 182.08 37.48 1.96 1198.33 0.00 227.19 37.48 301.92 4270 8.72 1170.94 285.16 181.24 37.46 1.56 1194.49 0.00 227.16 37.46 301.92 4280 8.44 1170.61 247.85 181.18 37.45 2.27 1198.63 0.00 227.12 37.44 301.92 4290 7.80 1170.67 228.28 181.93 37.42 2.59 1200.44 0.00 227.09 37.42 301.92 4300 8.35 1170.99 247.21 181.42 37.40 1.80 1199.75 0.00 227.06 37.40 301.92 4310 8.52 1170.99 252.46 180.96 37.37 1.94 1199.63 0.00 227.02 37.38 301.92 4320 7.62 1170.79 234.23 180.11 37.33 2.62 1200.60 0.00 226.99 37.36 301.92  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 35 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 35 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 4330         8.43   1170.95     249.61   182.54   37.33     1.97   1200.64     0.00     226.96       37.34         301.92 4340         8.73   1171.02     269.58   182.15   37.29     1.85   1197.56     0.00     226.93       37.32         301.92 4350         8.42   1170.71     275.62   179.86   37.30     2.30   1197.67     0.00     226.89       37.30         301.92 4360         7.78   1170.69     267.45   179.40   37.28     2.41   1199.53     0.00     226.86       37.28         301.92 4370         7.85   1170.66     252.31   179.68   37.26     2.07   1200.66     0.00     226.83       37.26         301.92 4380         8.70   1170.86     276.49   179.26   37.23     1.93   1198.14     0.00     226.80       37.24         301.92 4390         8.21   1171.02     268.59   178.83   37.22     2.26   1197.91     0.00     226.76       37.22         301.92 4400         8.19   1170.81     265.48   178.96   37.21     2.13   1199.06     0.00     226.73       37.20         301.92 4410         8.20   1170.76     256.66   179.61   37.18     2.17   1199.36     0.00     226.70       37.18         301.93 4420         9.08   1170.85     238.18   182.57   37.16     2.01   1199.14     0.00     226.67       37.16         301.93 4430         9.68   1170.75     219.16   183.90   37.14     2.18   1199.48     0.00     226.63       37.14         301.93 4440         9.09   1170.61     183.19   187.03   37.09     2.63   1200.84     0.00     226.60       37.12         301.93 4450       10.95   1171.02     203.00   187.54   37.11     1.77   1197.62     0.00     226.57       37.10         301.92 4460       11.53   1170.84     188.86   187.19   37.06     1.77   1197.09     0.00     226.54       37.08         301.93 4470       10.30   1170.51     149.90   192.53   37.07     2.48   1200.49     0.00     226.50       37.06         301.92 4480       11.30   1170.70     166.68   194.43   37.04     1.90   1199.90     0.00     226.47       37.04         301.92 4490       11.98   1170.96     206.84   189.31   37.02     1.94   1197.44     0.00     226.44       37.02         301.92 4500       11.31   1171.09     209.05   186.73   37.00     2.35   1198.85     0.00     226.40       37.00         301.93 4510       11.75   1171.37     213.42   185.15   36.98     2.06   1200.17     0.00     226.37       36.98         301.93 4520       11.15   1171.45     199.03   182.99   36.96     2.19   1200.78     0.00     226.34       36.96         301.93 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 4330 8.43 1170.95 249.61 182.54 37.33 1.97 1200.64 0.00 226.96 37.34 301.92 4340 8.73 1171.02 269.58 182.15 37.29 1.85 1197.56 0.00 226.93 37.32 301.92 4350 8.42 1170.71 275.62 179.86 37.30 2.30 1197.67 0.00 226.89 37.30 301.92 4360 7.78 1170.69 267.45 179.40 37.28 2.41 1199.53 0.00 226.86 37.28 301.92 4370 7.85 1170.66 252.31 179.68 37.26 2.07 1200.66 0.00 226.83 37.26 301.92 4380 8.70 1170.86 276.49 179.26 37.23 1.93 1198.14 0.00 226.80 37.24 301.92 4390 8.21 1171.02 268.59 178.83 37.22 2.26 1197.91 0.00 226.76 37.22 301.92 4400 8.19 1170.81 265.48 178.96 37.21 2.13 1199.06 0.00 226.73 37.20 301.92 4410 8.20 1170.76 256.66 179.61 37.18 2.17 1199.36 0.00 226.70 37.18 301.93 4420 9.08 1170.85 238.18 182.57 37.16 2.01 1199.14 0.00 226.67 37.16 301.93 4430 9.68 1170.75 219.16 183.90 37.14 2.18 1199.48 0.00 226.63 37.14 301.93 4440 9.09 1170.61 183.19 187.03 37.09 2.63 1200.84 0.00 226.60 37.12 301.93 4450 10.95 1171.02 203.00 187.54 37.11 1.77 1197.62 0.00 226.57 37.10 301.92 4460 11.53 1170.84 188.86 187.19 37.06 1.77 1197.09 0.00 226.54 37.08 301.93 4470 10.30 1170.51 149.90 192.53 37.07 2.48 1200.49 0.00 226.50 37.06 301.92 4480 11.30 1170.70 166.68 194.43 37.04 1.90 1199.90 0.00 226.47 37.04 301.92 4490 11.98 1170.96 206.84 189.31 37.02 1.94 1197.44 0.00 226.44 37.02 301.92 4500 11.31 1171.09 209.05 186.73 37.00 2.35 1198.85 0.00 226.40 37.00 301.93 4510 11.75 1171.37 213.42 185.15 36.98 2.06 1200.17 0.00 226.37 36.98 301.93 4520 11.15 1171.45 199.03 182.99 36.96 2.19 1200.78 0.00 226.34 36.96 301.93  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 36 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 36 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 4530       11.20   1171.08     178.13   186.70   36.94     1.62   1199.63     0.00     226.31       36.94         301.93 4540       11.64   1171.08     161.19   191.30   36.92     1.69   1200.28     0.00     226.27       36.92         301.93 4550       10.37   1171.17     151.73   191.07   36.88     2.67   1201.38     0.00     226.24       36.90         301.92 4560       10.79   1171.34     173.37   193.32   36.88     2.43   1200.64     0.00     226.20       36.88         301.93 4570       10.97   1171.65     194.79   195.90   36.86     1.76   1200.82     0.00     226.17       36.86         301.93 4580       10.96   1171.31     200.58   201.77   36.84     1.98   1201.21     0.00     226.14       36.84         301.93 4590       11.05   1171.47     177.91   203.20   36.82     2.58   1200.99     0.00     226.11       36.82         301.93 4600       10.51   1172.67     170.85   197.66   36.80     2.54   1200.77     0.00     226.07       36.80         301.93 4610       10.78   1173.10     187.47   196.40   36.78     2.28   1200.15     0.00     226.04       36.78         301.93 4620       11.62   1172.95     226.93   191.94   36.76     2.02   1197.61     0.00     226.01       36.76         301.93 4630       11.50   1172.03     205.17   191.31   36.74     2.23   1198.60     0.00     225.97       36.74         301.93 4640       10.31   1171.54     170.63   189.53   36.72     2.57   1200.30     0.00     225.94       36.72         301.93 4650       11.19   1171.65     193.55   189.14   36.70     1.64   1197.90     0.00     225.91       36.70         301.93 4660       11.65   1170.83     179.24   192.84   36.68     1.59   1198.06     0.00     225.88       36.68         301.93 4670       10.55   1170.33     152.38   193.82   36.65     2.60   1200.44     0.00     225.84       36.66         301.93 4680       10.34   1171.21     155.21   194.04   36.64     2.53   1200.68     0.00     225.81       36.64         301.93 4690       11.01   1172.55     189.43   192.97   36.62     1.97   1199.58     0.00     225.77       36.62         301.93 4700       11.96   1172.31     206.45   192.35   36.60     1.68   1197.70     0.00     225.74       36.60         301.93 4710       11.04   1172.09     192.96   190.64   36.58     2.20   1199.62     0.00     225.71       36.58         301.93 4720         8.36   1171.58     141.13   186.65   36.56     1.90   1201.74     0.00     225.68       36.56         301.93 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 4530 11.20 1171.08 178.13 186.70 36.94 1.62 1199.63 0.00 226.31 36.94 301.93 4540 11.64 1171.08 161.19 191.30 36.92 1.69 1200.28 0.00 226.27 36.92 301.93 4550 10.37 1171.17 151.73 191.07 36.88 2.67 1201.38 0.00 226.24 36.90 301.92 4560 10.79 1171.34 173.37 193.32 36.88 2.43 1200.64 0.00 226.20 36.88 301.93 4570 10.97 1171.65 194.79 195.90 36.86 1.76 1200.82 0.00 226.17 36.86 301.93 4580 10.96 1171.31 200.58 201.77 36.84 1.98 1201.21 0.00 226.14 36.84 301.93 4590 11.05 1171.47 177.91 203.20 36.82 2.58 1200.99 0.00 226.11 36.82 301.93 4600 10.51 1172.67 170.85 197.66 36.80 2.54 1200.77 0.00 226.07 36.80 301.93 4610 10.78 1173.10 187.47 196.40 36.78 2.28 1200.15 0.00 226.04 36.78 301.93 4620 11.62 1172.95 226.93 191.94 36.76 2.02 1197.61 0.00 226.01 36.76 301.93 4630 11.50 1172.03 205.17 191.31 36.74 2.23 1198.60 0.00 225.97 36.74 301.93 4640 10.31 1171.54 170.63 189.53 36.72 2.57 1200.30 0.00 225.94 36.72 301.93 4650 11.19 1171.65 193.55 189.14 36.70 1.64 1197.90 0.00 225.91 36.70 301.93 4660 11.65 1170.83 179.24 192.84 36.68 1.59 1198.06 0.00 225.88 36.68 301.93 4670 10.55 1170.33 152.38 193.82 36.65 2.60 1200.44 0.00 225.84 36.66 301.93 4680 10.34 1171.21 155.21 194.04 36.64 2.53 1200.68 0.00 225.81 36.64 301.93 4690 11.01 1172.55 189.43 192.97 36.62 1.97 1199.58 0.00 225.77 36.62 301.93 4700 11.96 1172.31 206.45 192.35 36.60 1.68 1197.70 0.00 225.74 36.60 301.93 4710 11.04 1172.09 192.96 190.64 36.58 2.20 1199.62 0.00 225.71 36.58 301.93 4720 8.36 1171.58 141.13 186.65 36.56 1.90 1201.74 0.00 225.68 36.56 301.93  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 37 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 37 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 4730         7.88   1169.89     149.45   193.70   36.54     1.75   1205.09     0.00     225.64       36.54         301.93 4740       10.20   1169.97     196.81   199.19   36.52     2.07   1203.34     0.00     225.61       36.52         301.93 4750       12.21   1170.61     213.27   192.22   36.50     1.93   1198.06     0.00     225.58       36.50         301.93 4760       11.78   1170.83     205.44   184.99   36.48     2.27   1197.56     0.00     225.54       36.48         301.93 4770       12.33   1170.70     173.88   188.62   36.39     1.56   1196.97     0.00     225.51       36.46         301.93 4780       12.95   1170.99     155.65   194.43   36.45     1.57   1197.99     0.00     225.48       36.44         301.93 4790       11.51   1171.13     130.54   198.92   36.41     2.46   1200.27     0.00     225.44       36.42         301.93 4800       11.31   1171.13     142.54   201.12   36.40     2.42   1200.97     0.00     225.41       36.40         301.93 4810       12.07   1171.12     164.12   200.56   36.38     2.06   1200.60     0.00     225.38       36.38         301.93 4820       12.76   1171.64     184.21   200.05   36.36     2.00   1199.69     0.00     225.34       36.36         301.93 4830       12.12   1171.61     167.15   201.13   36.34     2.48   1200.21     0.00     225.31       36.34         301.93 4840       11.29   1170.67     154.12   202.44   36.32     2.57   1201.25     0.00     225.28       36.32         301.93 4850       11.51   1170.75     168.96   204.22   36.30     2.36   1201.23     0.00     225.24       36.30         301.93 4860       12.62   1171.65     200.72   203.69   36.28     2.03   1200.84     0.00     225.21       36.28         301.93 4870       12.30   1171.85     196.58   202.07   36.26     2.26   1200.88     0.00     225.17       36.26         301.93 4880       11.02   1171.47     160.80   203.24   36.24     2.61   1200.99     0.00     225.14       36.24         301.93 4890       10.97   1171.48     153.73   206.70   36.22     2.60   1200.96     0.00     225.11       36.22         301.93 4900       11.71   1171.59     171.45   206.11   36.20     2.07   1200.23     0.00     225.07       36.20         301.93 4910       12.14   1172.28     241.08   193.92   36.18     1.96   1200.19     0.00     225.04       36.18         301.93 4920       12.09   1172.20     259.43   186.75   36.16     1.90   1200.09     0.00     225.01       36.16         301.93 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 4730 7.88 1169.89 149.45 193.70 36.54 1.75 1205.09 0.00 225.64 36.54 301.93 4740 10.20 1169.97 196.81 199.19 36.52 2.07 1203.34 0.00 225.61 36.52 301.93 4750 12.21 1170.61 213.27 192.22 36.50 1.93 1198.06 0.00 225.58 36.50 301.93 4760 11.78 1170.83 205.44 184.99 36.48 2.27 1197.56 0.00 225.54 36.48 301.93 4770 12.33 1170.70 173.88 188.62 36.39 1.56 1196.97 0.00 225.51 36.46 301.93 4780 12.95 1170.99 155.65 194.43 36.45 1.57 1197.99 0.00 225.48 36.44 301.93 4790 11.51 1171.13 130.54 198.92 36.41 2.46 1200.27 0.00 225.44 36.42 301.93 4800 11.31 1171.13 142.54 201.12 36.40 2.42 1200.97 0.00 225.41 36.40 301.93 4810 12.07 1171.12 164.12 200.56 36.38 2.06 1200.60 0.00 225.38 36.38 301.93 4820 12.76 1171.64 184.21 200.05 36.36 2.00 1199.69 0.00 225.34 36.36 301.93 4830 12.12 1171.61 167.15 201.13 36.34 2.48 1200.21 0.00 225.31 36.34 301.93 4840 11.29 1170.67 154.12 202.44 36.32 2.57 1201.25 0.00 225.28 36.32 301.93 4850 11.51 1170.75 168.96 204.22 36.30 2.36 1201.23 0.00 225.24 36.30 301.93 4860 12.62 1171.65 200.72 203.69 36.28 2.03 1200.84 0.00 225.21 36.28 301.93 4870 12.30 1171.85 196.58 202.07 36.26 2.26 1200.88 0.00 225.17 36.26 301.93 4880 11.02 1171.47 160.80 203.24 36.24 2.61 1200.99 0.00 225.14 36.24 301.93 4890 10.97 1171.48 153.73 206.70 36.22 2.60 1200.96 0.00 225.11 36.22 301.93 4900 11.71 1171.59 171.45 206.11 36.20 2.07 1200.23 0.00 225.07 36.20 301.93 4910 12.14 1172.28 241.08 193.92 36.18 1.96 1200.19 0.00 225.04 36.18 301.93 4920 12.09 1172.20 259.43 186.75 36.16 1.90 1200.09 0.00 225.01 36.16 301.93  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 38 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 38 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 4930       11.78   1170.56     177.50   187.97   36.14     2.00   1201.03     0.00     224.98       36.14         301.93 4940       11.07   1170.22     131.88   194.56   36.12     2.57   1201.30     0.00     224.94       36.12         301.93 4950       10.44   1170.87     146.73   197.05   36.08     2.55   1200.62     0.00     224.91       36.10         301.93 4960         9.28   1170.35     168.33   193.04   36.09     2.56   1200.66     0.00     224.87       36.08         301.93 4970       10.49   1170.20     194.53   193.47   36.07     1.78   1199.38     0.00     224.84       36.06         301.93 4980       11.78   1171.05     219.17   191.43   36.03     1.71   1196.08     0.00     224.81       36.04         301.93 4990       11.55   1171.41     237.87   186.73   36.02     2.35   1197.99     0.00     224.78       36.02         301.93 5000       11.19   1170.78     212.91   185.92   36.00     2.50   1200.24     0.00     224.74       36.00         301.93 5010       11.55   1171.29     189.32   181.28   36.00     1.93   1199.96     0.00     224.74       36.00         301.93 5020       11.52   1171.51     169.65   183.67   35.99     1.82   1201.35     0.00     224.74       36.00         301.93 5030       11.46   1170.93     145.48   193.38   36.01     1.80   1200.60     0.00     224.74       36.00         301.93 5040       11.46   1170.45     166.49   190.35   36.02     1.68   1197.49     0.00     224.74       36.00         301.93 5050       10.59   1170.00     192.87   185.94   36.00     2.36   1199.12     0.00     224.74       36.00         301.93 5060       11.61   1171.96     218.48   184.14   36.00     2.18   1199.63     0.00     224.74       36.00         301.93 5070       11.24   1172.88     194.70   183.39   36.00     2.26   1200.01     0.00     224.74       36.00         301.93 5080       11.71   1171.18     147.68   189.98   35.99     1.38   1199.77     0.00     224.74       36.00         301.93 5090       12.03   1170.10     138.18   193.57   36.00     1.23   1197.64     0.00     224.74       36.00         301.93 5100       10.14   1169.74     143.77   189.99   35.98     2.30   1199.77     0.00     224.74       36.00         301.93 5110       10.68   1170.81     188.41   190.05   36.00     1.96   1200.69     0.00     224.74       36.00         301.93 5120         9.20   1170.84     164.15   195.10   36.00     1.76   1198.68     0.00     224.74       36.00         301.93 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 4930 11.78 1170.56 177.50 187.97 36.14 2.00 1201.03 0.00 224.98 36.14 301.93 4940 11.07 1170.22 131.88 194.56 36.12 2.57 1201.30 0.00 224.94 36.12 301.93 4950 10.44 1170.87 146.73 197.05 36.08 2.55 1200.62 0.00 224.91 36.10 301.93 4960 9.28 1170.35 168.33 193.04 36.09 2.56 1200.66 0.00 224.87 36.08 301.93 4970 10.49 1170.20 194.53 193.47 36.07 1.78 1199.38 0.00 224.84 36.06 301.93 4980 11.78 1171.05 219.17 191.43 36.03 1.71 1196.08 0.00 224.81 36.04 301.93 4990 11.55 1171.41 237.87 186.73 36.02 2.35 1197.99 0.00 224.78 36.02 301.93 5000 11.19 1170.78 212.91 185.92 36.00 2.50 1200.24 0.00 224.74 36.00 301.93 5010 11.55 1171.29 189.32 181.28 36.00 1.93 1199.96 0.00 224.74 36.00 301.93 5020 11.52 1171.51 169.65 183.67 35.99 1.82 1201.35 0.00 224.74 36.00 301.93 5030 11.46 1170.93 145.48 193.38 36.01 1.80 1200.60 0.00 224.74 36.00 301.93 5040 11.46 1170.45 166.49 190.35 36.02 1.68 1197.49 0.00 224.74 36.00 301.93 5050 10.59 1170.00 192.87 185.94 36.00 2.36 1199.12 0.00 224.74 36.00 301.93 5060 11.61 1171.96 218.48 184.14 36.00 2.18 1199.63 0.00 224.74 36.00 301.93 5070 11.24 1172.88 194.70 183.39 36.00 2.26 1200.01 0.00 224.74 36.00 301.93 5080 11.71 1171.18 147.68 189.98 35.99 1.38 1199.77 0.00 224.74 36.00 301.93 5090 12.03 1170.10 138.18 193.57 36.00 1.23 1197.64 0.00 224.74 36.00 301.93 5100 10.14 1169.74 143.77 189.99 35.98 2.30 1199.77 0.00 224.74 36.00 301.93 5110 10.68 1170.81 188.41 190.05 36.00 1.96 1200.69 0.00 224.74 36.00 301.93 5120 9.20 1170.84 164.15 195.10 36.00 1.76 1198.68 0.00 224.74 36.00 301.93  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 39 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 39 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 5130       13.53   1169.80     252.02   204.92   36.01     2.21   1197.54     0.00     224.74       36.00         301.93 5140       15.88   1169.76     261.95   200.50   36.00     2.63   1196.93     0.00     224.74       36.00         301.93 5150       13.46   1169.68     103.37   187.50   36.00     2.53   1195.41     0.00     224.74       36.00         301.93 5160       16.09   1170.32       95.15   188.75   35.98     1.66   1194.54     0.00     224.74       36.00         301.93 5170       16.14   1171.89     125.64   191.39   36.00     1.95   1196.84     0.00     224.74       36.00         301.93 5180       14.95   1173.17     145.74   191.47   36.00     2.56   1198.26     0.00     224.74       36.00         301.93 5190       15.00   1174.01     174.95   190.73   36.00     2.10   1198.94     0.00     224.74       36.00         301.93 5200       14.62   1174.12     172.55   191.32   36.00     2.36   1199.30     0.00     224.74       36.00         301.93 5210       14.50   1174.05     169.77   189.21   36.00     1.95   1199.56     0.00     224.74       36.00         301.93 5220       15.67   1173.70     171.43   194.64   36.01     1.34   1201.72     0.00     224.74       36.00         301.93 5230       15.48   1172.72     184.42   194.20   35.99     1.90   1201.36     0.00     224.74       36.00         301.93 5240       14.99   1173.54     233.19   186.76   36.00     2.28   1198.78     0.00     224.74       36.00         301.93 5250       14.92   1174.05     212.67   182.95   36.00     1.68   1197.46     0.00     224.74       36.00         301.93 5260       14.44   1172.88     145.09   188.87   36.00     1.89   1200.03     0.00     224.74       36.00         301.93 5270       14.40   1172.38     138.45   196.72   35.99     2.15   1200.55     0.00     224.74       36.00         301.93 5280       14.20   1173.00     170.10   190.18   36.00     1.79   1198.82     0.00     224.74       36.00         301.93 5290       12.57   1172.25     182.66   188.98   36.00     2.35   1199.72     0.00     224.74       36.00         301.93 5300       11.66   1171.87     180.78   184.95   36.00     2.56   1199.57     0.00     224.74       36.00         301.93 5310       11.66   1172.21     127.89   190.13   36.00     1.22   1198.03     0.00     224.74       36.00         301.93 5320       13.07   1169.96     185.42   212.05   35.98     1.34   1196.44     0.01     224.74       36.00         301.93 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 5130 13.53 1169.80 252.02 204.92 36.01 2.21 1197.54 0.00 224.74 36.00 301.93 5140 15.88 1169.76 261.95 200.50 36.00 2.63 1196.93 0.00 224.74 36.00 301.93 5150 13.46 1169.68 103.37 187.50 36.00 2.53 1195.41 0.00 224.74 36.00 301.93 5160 16.09 1170.32 95.15 188.75 35.98 1.66 1194.54 0.00 224.74 36.00 301.93 5170 16.14 1171.89 125.64 191.39 36.00 1.95 1196.84 0.00 224.74 36.00 301.93 5180 14.95 1173.17 145.74 191.47 36.00 2.56 1198.26 0.00 224.74 36.00 301.93 5190 15.00 1174.01 174.95 190.73 36.00 2.10 1198.94 0.00 224.74 36.00 301.93 5200 14.62 1174.12 172.55 191.32 36.00 2.36 1199.30 0.00 224.74 36.00 301.93 5210 14.50 1174.05 169.77 189.21 36.00 1.95 1199.56 0.00 224.74 36.00 301.93 5220 15.67 1173.70 171.43 194.64 36.01 1.34 1201.72 0.00 224.74 36.00 301.93 5230 15.48 1172.72 184.42 194.20 35.99 1.90 1201.36 0.00 224.74 36.00 301.93 5240 14.99 1173.54 233.19 186.76 36.00 2.28 1198.78 0.00 224.74 36.00 301.93 5250 14.92 1174.05 212.67 182.95 36.00 1.68 1197.46 0.00 224.74 36.00 301.93 5260 14.44 1172.88 145.09 188.87 36.00 1.89 1200.03 0.00 224.74 36.00 301.93 5270 14.40 1172.38 138.45 196.72 35.99 2.15 1200.55 0.00 224.74 36.00 301.93 5280 14.20 1173.00 170.10 190.18 36.00 1.79 1198.82 0.00 224.74 36.00 301.93 5290 12.57 1172.25 182.66 188.98 36.00 2.35 1199.72 0.00 224.74 36.00 301.93 5300 11.66 1171.87 180.78 184.95 36.00 2.56 1199.57 0.00 224.74 36.00 301.93 5310 11.66 1172.21 127.89 190.13 36.00 1.22 1198.03 0.00 224.74 36.00 301.93 5320 13.07 1169.96 185.42 212.05 35.98 1.34 1196.44 0.01 224.74 36.00 301.93  


Oconee Nuclear Station                                                                     UFSAR Table 6-30 (Page 40 of 40)
Oconee Nuclear Station UFSAR Table 6-30 (Page 40 of 40)
Reactor Vessel Side                               Pump Discharge Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass    Liquid                    Spilled Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure    HPI Flow (seconds)   (lbm/sec) (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec) Btu/lbm)       (psi)       (gpm) 5330       16.16   1168.56     177.12   215.15   35.96     2.60   1189.95     0.01     230.08       36.00         301.93 5340       16.29   1169.11     101.32   198.85   36.00     2.44   1189.32     0.00     224.74       36.00         301.93 5350       15.15   1170.34     158.45   180.98   36.00     2.09   1197.23     0.00     224.74       36.00         301.93 5360       14.68   1171.32     147.86   178.48   36.00     2.13   1199.31     0.00     224.74       36.00         301.93 5370       14.76   1171.98     117.27   186.78   36.00     1.66   1199.23     0.00     224.74       36.00         301.93 5380       15.86   1172.83     158.02   192.27   36.00     1.70   1196.44     0.00     224.74       36.00         301.93 5390       15.44   1173.84     201.41   190.11   36.00     2.35   1196.62     0.00     224.74       36.00         301.93 5400       13.60   1174.34     195.33   186.41   36.00     2.55   1198.57     0.00     224.74       36.00         301.93 5410       13.68   1173.84     181.14   183.49   36.00     1.92   1199.56     0.00     224.74       36.00         301.93 5420       15.41   1172.81     149.62   190.78   35.98     1.17   1201.90     0.00     224.74       36.00         301.93 5430       14.90   1173.15     154.24   194.17   35.99     2.03   1200.15     0.00     224.74       36.00         301.93 5440       13.31   1174.10     194.49   187.81   36.00     2.62   1199.03     0.00     224.74       36.00         301.93 5450       13.25   1175.02     215.33   182.62   36.00     2.30   1199.91     0.00     224.74       36.00         301.93 5460       14.59   1173.67     166.76   186.09   36.00     1.45   1199.67     0.00     224.74       36.00         301.93 5466.85       15.50   1171.05       70.54   218.83   36.00     0.58   1198.07     0.00     224.74       36.00         301.93 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Pump Discharge Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy Btu/lbm)
Pressure (psi)
Spilled HPI Flow (gpm) 5330 16.16 1168.56 177.12 215.15 35.96 2.60 1189.95 0.01 230.08 36.00 301.93 5340 16.29 1169.11 101.32 198.85 36.00 2.44 1189.32 0.00 224.74 36.00 301.93 5350 15.15 1170.34 158.45 180.98 36.00 2.09 1197.23 0.00 224.74 36.00 301.93 5360 14.68 1171.32 147.86 178.48 36.00 2.13 1199.31 0.00 224.74 36.00 301.93 5370 14.76 1171.98 117.27 186.78 36.00 1.66 1199.23 0.00 224.74 36.00 301.93 5380 15.86 1172.83 158.02 192.27 36.00 1.70 1196.44 0.00 224.74 36.00 301.93 5390 15.44 1173.84 201.41 190.11 36.00 2.35 1196.62 0.00 224.74 36.00 301.93 5400 13.60 1174.34 195.33 186.41 36.00 2.55 1198.57 0.00 224.74 36.00 301.93 5410 13.68 1173.84 181.14 183.49 36.00 1.92 1199.56 0.00 224.74 36.00 301.93 5420 15.41 1172.81 149.62 190.78 35.98 1.17 1201.90 0.00 224.74 36.00 301.93 5430 14.90 1173.15 154.24 194.17 35.99 2.03 1200.15 0.00 224.74 36.00 301.93 5440 13.31 1174.10 194.49 187.81 36.00 2.62 1199.03 0.00 224.74 36.00 301.93 5450 13.25 1175.02 215.33 182.62 36.00 2.30 1199.91 0.00 224.74 36.00 301.93 5460 14.59 1173.67 166.76 186.09 36.00 1.45 1199.67 0.00 224.74 36.00 301.93 5466.85 15.50 1171.05 70.54 218.83 36.00 0.58 1198.07 0.00 224.74 36.00 301.93  


Oconee Nuclear Station                                                           UFSAR Table 6-31 (Page 1 of 2)
Oconee Nuclear Station UFSAR Table 6-31 (Page 1 of 2)
Table 6-31. BFLOW/FATHOMS Long-Term Mass and Energy Releases Time               Time      Steam Flow        Steam Enthalpy Bk liq flow    Liquid Enthalpy (sec)           (Days)       (lbm/sec)           (Btu/lbm)   (lbm/sec)       (Btu/lbm) 4561                           25.24               1163.93     358.19           170.13 4811                           24.63               1164.56     350.28           169.97 7211                           19.56               1166.13     356.92           162.03 10012                           18.25               1165.98     359.64           154.52 24012                           15.16               1163.50     371.60           128.60 36013                           13.98               1161.70     373.59           117.93 49415                           13.25               1160.26     374.87           110.18 72815                           12.07               1158.49     376.61           102.09 87216             1.01         11.71               1157.80     377.19             98.73 2.1           9.86               1155.60     379.67             89.18 3.1           8.41               1154.24     381.39             85.79 4.0           7.41               1153.41     382.54             84.13 5.1           6.55               1152.74     383.52             82.85 6.1           5.91               1152.25     384.26             81.81 7.0           5.36               1152.62     384.96             80.19 8.1           4.75               1153.15     386.07             74.55 9.0           4.45               1152.58     386.39             74.21 10.0           4.16               1152.16     386.69             73.98 11.1           3.91               1151.83     386.95             73.81 12.0           3.71               1151.57     387.16             73.69 13.0           3.51               1151.33     386.91             73.59 14.1           3.34               1151.13     387.10             73.49 (31 DEC 2017)
(31 DEC 2017)
Table 6-31. BFLOW/FATHOMS Long-Term Mass and Energy Releases Time (sec)
Time (Days)
Steam Flow (lbm/sec)
Steam Enthalpy (Btu/lbm)
Bk liq flow (lbm/sec)
Liquid Enthalpy (Btu/lbm) 4561 25.24 1163.93 358.19 170.13 4811 24.63 1164.56 350.28 169.97 7211 19.56 1166.13 356.92 162.03 10012 18.25 1165.98 359.64 154.52 24012 15.16 1163.50 371.60 128.60 36013 13.98 1161.70 373.59 117.93 49415 13.25 1160.26 374.87 110.18 72815 12.07 1158.49 376.61 102.09 87216 1.01 11.71 1157.80 377.19 98.73 2.1 9.86 1155.60 379.67 89.18 3.1 8.41 1154.24 381.39 85.79 4.0 7.41 1153.41 382.54 84.13 5.1 6.55 1152.74 383.52 82.85 6.1 5.91 1152.25 384.26 81.81 7.0 5.36 1152.62 384.96 80.19 8.1 4.75 1153.15 386.07 74.55 9.0 4.45 1152.58 386.39 74.21 10.0 4.16 1152.16 386.69 73.98 11.1 3.91 1151.83 386.95 73.81 12.0 3.71 1151.57 387.16 73.69 13.0 3.51 1151.33 386.91 73.59 14.1 3.34 1151.13 387.10 73.49  


Oconee Nuclear Station                                             UFSAR Table 6-31 (Page 2 of 2)
Oconee Nuclear Station UFSAR Table 6-31 (Page 2 of 2)
Time               Time  Steam Flow Steam Enthalpy Bk liq flow    Liquid Enthalpy (sec)             (Days) (lbm/sec)   (Btu/lbm)   (lbm/sec)       (Btu/lbm) 15.0     3.19       1150.96     387.69           73.44 16.1     3.04       1150.79     387.84           73.38 17.1     2.91       1150.65     387.97           73.32 18.0     2.80       1150.53     386.18           73.29 19.1     2.69       1150.42     384.25           73.27 20.1     2.58       1150.31     388.32           73.18 21.0     2.49       1150.22     388.41           73.14 22.1     2.40       1150.13     388.51           73.11 23.0     2.32       1150.05     388.59           73.08 24.0     2.23       1149.98     388.67           73.05 25.1     2.16       1149.88     388.75           73.01 26.0     2.09       1149.79     388.82           72.98 27.1     2.02       1149.69     388.89           72.94 28.1     1.96       1149.60     384.45           72.96 29.0     1.90       1149.53     389.02           72.88 30.1     1.84       1149.45     389.08           72.85 31.1     1.78       1149.38     389.14           72.82 32.0     1.73       1149.31     389.19           72.80 33.1     1.68       1149.24     387.48           72.79 34.0     1.63       1149.18     389.29           72.75 35.0     1.57       1149.11     389.35           72.72 38 (31 DEC 2017)
(31 DEC 2017)
Time (sec)
Time (Days)
Steam Flow (lbm/sec)
Steam Enthalpy (Btu/lbm)
Bk liq flow (lbm/sec)
Liquid Enthalpy (Btu/lbm) 15.0 3.19 1150.96 387.69 73.44 16.1 3.04 1150.79 387.84 73.38 17.1 2.91 1150.65 387.97 73.32 18.0 2.80 1150.53 386.18 73.29 19.1 2.69 1150.42 384.25 73.27 20.1 2.58 1150.31 388.32 73.18 21.0 2.49 1150.22 388.41 73.14 22.1 2.40 1150.13 388.51 73.11 23.0 2.32 1150.05 388.59 73.08 24.0 2.23 1149.98 388.67 73.05 25.1 2.16 1149.88 388.75 73.01 26.0 2.09 1149.79 388.82 72.98 27.1 2.02 1149.69 388.89 72.94 28.1 1.96 1149.60 384.45 72.96 29.0 1.90 1149.53 389.02 72.88 30.1 1.84 1149.45 389.08 72.85 31.1 1.78 1149.38 389.14 72.82 32.0 1.73 1149.31 389.19 72.80 33.1 1.68 1149.24 387.48 72.79 34.0 1.63 1149.18 389.29 72.75 35.0 1.57 1149.11 389.35 72.72 38  


Oconee Nuclear Station                                                                               UFSAR Table 6-32 (Page 1 of 5)
Oconee Nuclear Station UFSAR Table 6-32 (Page 1 of 5)
Table 6-32. Steam Line Break Mass and Energy Releases for Double-Ended Guillotine Break Time       Flow      Enthalpy  Pressure  Time      Flow    Enthalpy    Pressure    Time    Flow      Enthalpy      Pressure (sec)   (lbm/sec)   (Btu/lbm)   (psia)   (sec)   (lbm/sec)   (Btu/lbm)     (psia)   (sec) (lbm/sec)   (Btu/lbm)       (psia) 0.0       0.0       1261.9   944.1     2.1     6737.0     1270.7     834.7       4.2   3029.1       1275.1       784.7 0.1     16210.7       1262.9   933.9     2.2     6687.0     1270.8     833.4       4.3   2947.1       1275.2       783.2 0.2     11175.3       1265.2   909.5     2.3     6646.9     1271.0     831.8       4.4   2893.7       1275.3       781.8 0.3     9092.1       1266.6   895.2     2.4     6618.9     1271.1     830.0       4.5   2885.6       1275.3       780.2 0.4     8239.2       1267.5   884.4     2.5     6586.4     1271.4     827.3       4.6   2878.4       1275.3       778.4 0.5     8007.2       1268.1   876.9     2.6     6495.0     1271.6     824.4       4.7   2871.9       1275.4       776.1 0.6     8083.4       1268.6   871.5     2.7     6341.9     1271.9     821.6       4.8   2866.1       1275.6       773.8 0.7     8133.4       1268.9   867.3     2.8     6147.2     1272.0     818.8       4.9   2860.2       1275.8       771.5 0.8     8100.8       1269.1   863.6     2.9     5915.9     1272.2     816.1       5.0   2894.2       1276.0       769.4 0.9     7998.8       1269.3   860.4     3.0     5645.9     1272.4     813.3       5.5   2795.1       1276.6       759.4 1.0     7858.0       1269.6   856.9     3.1     5354.2     1272.6     810.7       6.0   2728.0       1277.4       743.2 1.1     7705.4       1269.9   853.0     3.2     5038.2     1272.7     808.3       6.5   2687.9       1277.7       724.7 1.2     7556.9       1270.2   849.0     3.3     4673.2     1272.9     806.1       7.0   2616.5       1277.3       712.3 1.3     7420.6       1270.5   845.3     3.4     4219.5     1273.1     803.7       7.5   2557.0       1277.7       693.3 1.4     7297.7       1270.7   842.3     3.5     3923.4     1273.3     801.4       8.0   2473.2       1277.6       674.9 1.5     7188.1       1270.7   840.0     3.6     3711.9     1273.6     798.6       8.5   2422.2       1277.4       658.9 1.6     7089.9       1270.7   838.1     3.7     3539.0     1273.9     795.7       9.0   2364.1       1276.5       649.7 1.7     7005.0       1270.6   837.4     3.8     3391.3     1274.1     793.2       9.5   2351.6       1275.2       644.6 1.8     6929.4       1270.6   837.0     3.9     3278.9     1274.4     790.9     10.0   2322.4       1273.9       639.7 1.9     6859.9       1270.5   836.4     4.0     3196.1     1274.6     788.7     10.5   2309.3       1272.6       635.2 2.0     6795.3       1270.6   835.7     4.1     3117.8     1274.9     786.5     11.0   2289.4       1271.4       630.2 (31 DEC 2003)
(31 DEC 2003)
Table 6-32. Steam Line Break Mass and Energy Releases for Double-Ended Guillotine Break Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia) 0.0 0.0 1261.9 944.1 2.1 6737.0 1270.7 834.7 4.2 3029.1 1275.1 784.7 0.1 16210.7 1262.9 933.9 2.2 6687.0 1270.8 833.4 4.3 2947.1 1275.2 783.2 0.2 11175.3 1265.2 909.5 2.3 6646.9 1271.0 831.8 4.4 2893.7 1275.3 781.8 0.3 9092.1 1266.6 895.2 2.4 6618.9 1271.1 830.0 4.5 2885.6 1275.3 780.2 0.4 8239.2 1267.5 884.4 2.5 6586.4 1271.4 827.3 4.6 2878.4 1275.3 778.4 0.5 8007.2 1268.1 876.9 2.6 6495.0 1271.6 824.4 4.7 2871.9 1275.4 776.1 0.6 8083.4 1268.6 871.5 2.7 6341.9 1271.9 821.6 4.8 2866.1 1275.6 773.8 0.7 8133.4 1268.9 867.3 2.8 6147.2 1272.0 818.8 4.9 2860.2 1275.8 771.5 0.8 8100.8 1269.1 863.6 2.9 5915.9 1272.2 816.1 5.0 2894.2 1276.0 769.4 0.9 7998.8 1269.3 860.4 3.0 5645.9 1272.4 813.3 5.5 2795.1 1276.6 759.4 1.0 7858.0 1269.6 856.9 3.1 5354.2 1272.6 810.7 6.0 2728.0 1277.4 743.2 1.1 7705.4 1269.9 853.0 3.2 5038.2 1272.7 808.3 6.5 2687.9 1277.7 724.7 1.2 7556.9 1270.2 849.0 3.3 4673.2 1272.9 806.1 7.0 2616.5 1277.3 712.3 1.3 7420.6 1270.5 845.3 3.4 4219.5 1273.1 803.7 7.5 2557.0 1277.7 693.3 1.4 7297.7 1270.7 842.3 3.5 3923.4 1273.3 801.4 8.0 2473.2 1277.6 674.9 1.5 7188.1 1270.7 840.0 3.6 3711.9 1273.6 798.6 8.5 2422.2 1277.4 658.9 1.6 7089.9 1270.7 838.1 3.7 3539.0 1273.9 795.7 9.0 2364.1 1276.5 649.7 1.7 7005.0 1270.6 837.4 3.8 3391.3 1274.1 793.2 9.5 2351.6 1275.2 644.6 1.8 6929.4 1270.6 837.0 3.9 3278.9 1274.4 790.9 10.0 2322.4 1273.9 639.7 1.9 6859.9 1270.5 836.4 4.0 3196.1 1274.6 788.7 10.5 2309.3 1272.6 635.2 2.0 6795.3 1270.6 835.7 4.1 3117.8 1274.9 786.5 11.0 2289.4 1271.4 630.2  


Oconee Nuclear Station                                                                   UFSAR Table 6-32 (Page 2 of 5)
Oconee Nuclear Station UFSAR Table 6-32 (Page 2 of 5)
Time     Flow      Enthalpy  Pressure Time    Flow  Enthalpy  Pressure Time    Flow      Enthalpy      Pressure (sec) (lbm/sec)     (Btu/lbm) (psia) (sec) (lbm/sec) (Btu/lbm) (psia) (sec) (lbm/sec)   (Btu/lbm)       (psia) 11.5     2263.4       1270.4   623.9   22.5   2165.9   1252.6   569.4   33.5   1832.3       1244.4       495.4 12.0     2234.8       1269.8   616.0   23.0   2109.0   1248.9   574.6   34.0   1824.5       1244.1       493.4 12.5     2199.7       1269.3   609.2   23.5   2098.7   1247.4   575.6   34.5   1817.9       1243.8       491.3 13.0     2176.4       1268.9   602.6   24.0   2088.9   1247.0   572.6   35.0   1809.5       1243.4       489.2 13.5     2131.2       1269.1   591.1   24.5   2077.7   1246.8   567.0   35.5   1801.6       1242.9       487.1 14.0     2088.8       1269.3   579.4   25.0   2063.4   1246.7   560.7   36.0   1792.4       1242.4       484.8 14.5     2035.1       1269.3   569.9   25.5   2049.0   1246.6   554.6   36.5   1782.9       1241.9       482.3 15.0     2026.8       1268.6   568.5   26.0   2030.4   1246.4   548.5   37.0   1773.0       1241.5       479.7 15.5     2040.1       1267.4   571.8   26.5   2008.4   1246.3   542.8   37.5   1762.5       1241.1       477.0 16.0     2054.8       1266.1   575.8   27.0   1990.3   1246.2   537.7   38.0   1751.8       1240.7       474.1 16.5     2069.9       1265.0   579.6   27.5   1971.6   1246.1   532.8   38.5   1740.8       1240.4       471.1 17.0     2091.3       1263.9   582.9   28.0   1956.4   1245.9   528.3   39.0   1729.9       1240.1       468.2 17.5     2091.6       1263.1   583.0   28.5   1940.4   1245.8   524.3   39.5   1718.4       1239.8       465.1 18.0     2090.9       1262.7   580.1   29.0   1926.8   1245.6   520.6   40.0   1707.5       1239.5       462.1 18.5     2097.9       1262.1   577.6   29.5   1913.8   1245.5   517.5   40.5   1695.8       1239.3       458.9 19.0     2083.5       1261.5   575.2   30.0   1901.5   1245.3   514.3   41.0   1685.6       1239.1       455.9 19.5     2067.7       1260.8   574.1   30.5   1889.7   1245.2   511.0   41.5   1674.8       1238.9       453.0 20.0     2053.4       1260.2   573.3   31.0   1878.2   1245.2   507.9   42.0   1664.8       1238.8       449.9 20.5     2052.9       1259.4   572.2   31.5   1867.4   1245.1   504.8   42.5   1653.9       1238.6       447.1 21.0     2060.6       1258.6   569.7   32.0   1856.7   1245.0   502.1   43.0   1644.1       1238.4       444.6 21.5     2081.0       1257.6   566.8   32.5   1848.0   1244.8   499.8   43.5   1634.8       1238.3       442.1 22.0     2066.0       1256.3   565.5   33.0   1839.3   1244.6   497.6   44.0   1625.9       1238.1       440.1 (31 DEC 2003)
(31 DEC 2003)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia) 11.5 2263.4 1270.4 623.9 22.5 2165.9 1252.6 569.4 33.5 1832.3 1244.4 495.4 12.0 2234.8 1269.8 616.0 23.0 2109.0 1248.9 574.6 34.0 1824.5 1244.1 493.4 12.5 2199.7 1269.3 609.2 23.5 2098.7 1247.4 575.6 34.5 1817.9 1243.8 491.3 13.0 2176.4 1268.9 602.6 24.0 2088.9 1247.0 572.6 35.0 1809.5 1243.4 489.2 13.5 2131.2 1269.1 591.1 24.5 2077.7 1246.8 567.0 35.5 1801.6 1242.9 487.1 14.0 2088.8 1269.3 579.4 25.0 2063.4 1246.7 560.7 36.0 1792.4 1242.4 484.8 14.5 2035.1 1269.3 569.9 25.5 2049.0 1246.6 554.6 36.5 1782.9 1241.9 482.3 15.0 2026.8 1268.6 568.5 26.0 2030.4 1246.4 548.5 37.0 1773.0 1241.5 479.7 15.5 2040.1 1267.4 571.8 26.5 2008.4 1246.3 542.8 37.5 1762.5 1241.1 477.0 16.0 2054.8 1266.1 575.8 27.0 1990.3 1246.2 537.7 38.0 1751.8 1240.7 474.1 16.5 2069.9 1265.0 579.6 27.5 1971.6 1246.1 532.8 38.5 1740.8 1240.4 471.1 17.0 2091.3 1263.9 582.9 28.0 1956.4 1245.9 528.3 39.0 1729.9 1240.1 468.2 17.5 2091.6 1263.1 583.0 28.5 1940.4 1245.8 524.3 39.5 1718.4 1239.8 465.1 18.0 2090.9 1262.7 580.1 29.0 1926.8 1245.6 520.6 40.0 1707.5 1239.5 462.1 18.5 2097.9 1262.1 577.6 29.5 1913.8 1245.5 517.5 40.5 1695.8 1239.3 458.9 19.0 2083.5 1261.5 575.2 30.0 1901.5 1245.3 514.3 41.0 1685.6 1239.1 455.9 19.5 2067.7 1260.8 574.1 30.5 1889.7 1245.2 511.0 41.5 1674.8 1238.9 453.0 20.0 2053.4 1260.2 573.3 31.0 1878.2 1245.2 507.9 42.0 1664.8 1238.8 449.9 20.5 2052.9 1259.4 572.2 31.5 1867.4 1245.1 504.8 42.5 1653.9 1238.6 447.1 21.0 2060.6 1258.6 569.7 32.0 1856.7 1245.0 502.1 43.0 1644.1 1238.4 444.6 21.5 2081.0 1257.6 566.8 32.5 1848.0 1244.8 499.8 43.5 1634.8 1238.3 442.1 22.0 2066.0 1256.3 565.5 33.0 1839.3 1244.6 497.6 44.0 1625.9 1238.1 440.1  


Oconee Nuclear Station                                                                   UFSAR Table 6-32 (Page 3 of 5)
Oconee Nuclear Station UFSAR Table 6-32 (Page 3 of 5)
Time     Flow      Enthalpy  Pressure Time    Flow  Enthalpy  Pressure Time    Flow      Enthalpy      Pressure (sec) (lbm/sec)     (Btu/lbm) (psia) (sec) (lbm/sec) (Btu/lbm) (psia) (sec) (lbm/sec)   (Btu/lbm)       (psia) 44.5     1617.3       1238.0   437.7   56.0   1445.1   1235.1   391.5   79.0   1235.5       1231.0       338.7 45.0     1609.4       1237.8   436.3   57.0   1432.4   1234.9   388.9   80.0   1227.6       1230.9       336.5 45.5     1602.7       1237.6   434.3   59.0   1412.0   1234.4   384.5   81.0   1219.2       1230.8       334.4 46.0     1595.5       1237.4   432.5   60.0   1403.8   1234.1   382.9   82.0   1210.9       1230.6       332.3 46.5     1589.0       1237.3   430.4   61.0   1396.1   1233.8   380.9   83.0   1203.1       1230.5       330.4 47.0     1582.0       1237.0   429.0   62.0   1387.7   1233.5   378.9   85.0   1188.4       1230.4       326.3 47.5     1575.5       1236.9   426.8   63.0   1378.7   1233.3   376.2   86.0   1181.2       1230.3       324.3 48.0     1568.3       1236.7   424.8   64.0   1369.2   1233.1   373.3   87.0   1173.5       1230.2       322.3 48.5     1561.9       1236.5   423.3   65.0   1358.7   1233.1   370.6   88.0   1165.9       1230.0       320.4 49.0     1554.6       1236.3   421.3   66.0   1348.7   1233.0   368.0   89.0   1158.6       1229.7       318.7 49.5     1547.4       1236.1   419.5   67.0   1338.3   1233.0   364.4   90.0   1150.9       1229.4       316.6 50.0     1540.0       1236.0   417.6   68.0   1326.6   1232.9   361.2   91.0   1142.4       1229.1       314.2 50.5     1532.4       1235.9   414.8   69.0   1317.5   1232.8   359.4   92.0   1133.3       1228.8       312.2 51.0     1524.4       1235.8   412.4   70.0   1309.8   1232.5   357.5   93.0   1123.3       1228.5       309.1 51.5     1515.7       1235.7   410.4   71.0   1302.9   1232.2   356.0   94.0   1112.9       1228.2       306.6 52.0     1507.3       1235.6   408.2   72.0   1294.8   1232.1   353.7   95.0   1102.1       1227.8       303.7 52.5     1499.5       1235.5   406.3   73.0   1285.4   1232.0   351.4   96.0   1090.8       1227.5       301.1 53.0     1491.6       1235.4   404.2   74.0   1275.8   1231.9   348.9   97.0   1078.3       1226.9       297.8 53.5     1483.5       1235.3   401.9   75.0   1266.3   1231.7   346.5   98.0   1064.5       1226.4       294.4 54.0     1475.3       1235.2   400.1   76.0   1257.7   1231.6   344.4   99.0   1051.0       1226.0       291.0 54.5     1466.7       1235.2   397.8   77.0   1250.1   1231.4   342.4   100.0   1039.2       1226.0       287.9 55.0     1459.7       1235.1   396.0   78.0   1242.9   1231.2   340.8   101.0   1028.7       1226.6       283.8 (31 DEC 2003)
(31 DEC 2003)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia) 44.5 1617.3 1238.0 437.7 56.0 1445.1 1235.1 391.5 79.0 1235.5 1231.0 338.7 45.0 1609.4 1237.8 436.3 57.0 1432.4 1234.9 388.9 80.0 1227.6 1230.9 336.5 45.5 1602.7 1237.6 434.3 59.0 1412.0 1234.4 384.5 81.0 1219.2 1230.8 334.4 46.0 1595.5 1237.4 432.5 60.0 1403.8 1234.1 382.9 82.0 1210.9 1230.6 332.3 46.5 1589.0 1237.3 430.4 61.0 1396.1 1233.8 380.9 83.0 1203.1 1230.5 330.4 47.0 1582.0 1237.0 429.0 62.0 1387.7 1233.5 378.9 85.0 1188.4 1230.4 326.3 47.5 1575.5 1236.9 426.8 63.0 1378.7 1233.3 376.2 86.0 1181.2 1230.3 324.3 48.0 1568.3 1236.7 424.8 64.0 1369.2 1233.1 373.3 87.0 1173.5 1230.2 322.3 48.5 1561.9 1236.5 423.3 65.0 1358.7 1233.1 370.6 88.0 1165.9 1230.0 320.4 49.0 1554.6 1236.3 421.3 66.0 1348.7 1233.0 368.0 89.0 1158.6 1229.7 318.7 49.5 1547.4 1236.1 419.5 67.0 1338.3 1233.0 364.4 90.0 1150.9 1229.4 316.6 50.0 1540.0 1236.0 417.6 68.0 1326.6 1232.9 361.2 91.0 1142.4 1229.1 314.2 50.5 1532.4 1235.9 414.8 69.0 1317.5 1232.8 359.4 92.0 1133.3 1228.8 312.2 51.0 1524.4 1235.8 412.4 70.0 1309.8 1232.5 357.5 93.0 1123.3 1228.5 309.1 51.5 1515.7 1235.7 410.4 71.0 1302.9 1232.2 356.0 94.0 1112.9 1228.2 306.6 52.0 1507.3 1235.6 408.2 72.0 1294.8 1232.1 353.7 95.0 1102.1 1227.8 303.7 52.5 1499.5 1235.5 406.3 73.0 1285.4 1232.0 351.4 96.0 1090.8 1227.5 301.1 53.0 1491.6 1235.4 404.2 74.0 1275.8 1231.9 348.9 97.0 1078.3 1226.9 297.8 53.5 1483.5 1235.3 401.9 75.0 1266.3 1231.7 346.5 98.0 1064.5 1226.4 294.4 54.0 1475.3 1235.2 400.1 76.0 1257.7 1231.6 344.4 99.0 1051.0 1226.0 291.0 54.5 1466.7 1235.2 397.8 77.0 1250.1 1231.4 342.4 100.0 1039.2 1226.0 287.9 55.0 1459.7 1235.1 396.0 78.0 1242.9 1231.2 340.8 101.0 1028.7 1226.6 283.8  


Oconee Nuclear Station                                                                   UFSAR Table 6-32 (Page 4 of 5)
Oconee Nuclear Station UFSAR Table 6-32 (Page 4 of 5)
Time     Flow      Enthalpy  Pressure Time    Flow    Enthalpy  Pressure Time    Flow      Enthalpy      Pressure (sec) (lbm/sec)     (Btu/lbm) (psia) (sec) (lbm/sec) (Btu/lbm) (psia) (sec) (lbm/sec)   (Btu/lbm)       (psia) 102.0   1019.3       1227.2   280.9   124.0   895.0     1220.9   252.5   146.0   709.1       1222.7       206.6 103.0   1009.5       1227.8   277.7   125.0   886.7     1220.4   250.6   147.0   681.2       1223.4       202.9 104.0   1000.0       1228.1   274.9   126.0   878.0     1220.3   248.4   148.0   714.2       1223.9       198.7 105.0     991.5       1227.9   273.2   127.0   871.4     1220.5   246.6   149.0   689.0       1223.9       194.5 106.0     984.6       1227.3   272.3   128.0   867.7     1220.8   244.9   150.0   662.3       1224.0       190.2 107.0     977.9       1226.5   271.5   129.0   863.1     1221.0   243.1   151.0   640.4       1224.1       184.7 108.0     971.1       1225.7   270.4   130.0   855.0     1221.1   240.7   152.0   623.1       1224.1       178.6 109.0     964.3       1224.9   268.8   131.0   846.8     1220.9   238.7   153.0   607.7       1224.3       172.1 110.0     958.3       1224.5   267.1   132.0   838.0     1220.3   236.7   154.0   591.5       1225.0       164.6 111.0     951.9       1224.3   264.9   133.0   828.7     1219.8   234.1   155.0   571.4       1226.1       156.5 112.0     945.5       1224.3   262.8   134.0   819.0     1219.5   231.4   156.0   545.0       1227.4       147.4 113.0     938.6       1224.0   260.9   135.0   811.1     1219.6   229.1   157.0   511.4       1228.8       138.1 114.0     930.6       1223.7   259.2   136.0   804.5     1220.0   227.0   158.0   471.5       1230.1       128.1 115.0     924.6       1223.3   257.6   137.0   799.3     1220.4   225.5   159.0   429.0       1231.2       118.0 116.0     918.2       1223.4   256.2   138.0   795.6     1220.6   224.3   160.0   387.2       1232.2       107.8 117.0     911.6       1223.7   255.1   139.0   793.9     1220.4   223.6   161.0   346.1       1233.3         97.2 118.0     909.1       1224.0   254.7   140.0   781.4     1220.6   222.1   162.0   305.5       1234.5         86.1 119.0     910.5       1224.0   254.8   141.0   773.9     1220.5   220.3   163.0   275.5       1235.4         77.5 120.0     911.9       1223.6   255.3   142.0   765.9     1220.5   218.2   164.0   249.6       1236.1         70.5 121.0     911.2       1223.0   255.7   143.0   755.4     1220.6   215.4   165.0   224.6       1236.7         64.0 122.0     908.2       1222.4   255.3   144.0   743.9     1221.1   212.5   166.0   201.9       1237.5         57.6 123.0     902.3       1221.7   254.1   145.0   731.9     1221.9   209.5   167.0   195.1       1238.1         55.1 (31 DEC 2003)
(31 DEC 2003)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia) 102.0 1019.3 1227.2 280.9 124.0 895.0 1220.9 252.5 146.0 709.1 1222.7 206.6 103.0 1009.5 1227.8 277.7 125.0 886.7 1220.4 250.6 147.0 681.2 1223.4 202.9 104.0 1000.0 1228.1 274.9 126.0 878.0 1220.3 248.4 148.0 714.2 1223.9 198.7 105.0 991.5 1227.9 273.2 127.0 871.4 1220.5 246.6 149.0 689.0 1223.9 194.5 106.0 984.6 1227.3 272.3 128.0 867.7 1220.8 244.9 150.0 662.3 1224.0 190.2 107.0 977.9 1226.5 271.5 129.0 863.1 1221.0 243.1 151.0 640.4 1224.1 184.7 108.0 971.1 1225.7 270.4 130.0 855.0 1221.1 240.7 152.0 623.1 1224.1 178.6 109.0 964.3 1224.9 268.8 131.0 846.8 1220.9 238.7 153.0 607.7 1224.3 172.1 110.0 958.3 1224.5 267.1 132.0 838.0 1220.3 236.7 154.0 591.5 1225.0 164.6 111.0 951.9 1224.3 264.9 133.0 828.7 1219.8 234.1 155.0 571.4 1226.1 156.5 112.0 945.5 1224.3 262.8 134.0 819.0 1219.5 231.4 156.0 545.0 1227.4 147.4 113.0 938.6 1224.0 260.9 135.0 811.1 1219.6 229.1 157.0 511.4 1228.8 138.1 114.0 930.6 1223.7 259.2 136.0 804.5 1220.0 227.0 158.0 471.5 1230.1 128.1 115.0 924.6 1223.3 257.6 137.0 799.3 1220.4 225.5 159.0 429.0 1231.2 118.0 116.0 918.2 1223.4 256.2 138.0 795.6 1220.6 224.3 160.0 387.2 1232.2 107.8 117.0 911.6 1223.7 255.1 139.0 793.9 1220.4 223.6 161.0 346.1 1233.3 97.2 118.0 909.1 1224.0 254.7 140.0 781.4 1220.6 222.1 162.0 305.5 1234.5 86.1 119.0 910.5 1224.0 254.8 141.0 773.9 1220.5 220.3 163.0 275.5 1235.4 77.5 120.0 911.9 1223.6 255.3 142.0 765.9 1220.5 218.2 164.0 249.6 1236.1 70.5 121.0 911.2 1223.0 255.7 143.0 755.4 1220.6 215.4 165.0 224.6 1236.7 64.0 122.0 908.2 1222.4 255.3 144.0 743.9 1221.1 212.5 166.0 201.9 1237.5 57.6 123.0 902.3 1221.7 254.1 145.0 731.9 1221.9 209.5 167.0 195.1 1238.1 55.1  


Oconee Nuclear Station                                                                   UFSAR Table 6-32 (Page 5 of 5)
Oconee Nuclear Station UFSAR Table 6-32 (Page 5 of 5)
Time     Flow        Enthalpy  Pressure Time    Flow    Enthalpy  Pressure Time    Flow      Enthalpy      Pressure (sec) (lbm/sec)     (Btu/lbm) (psia) (sec) (lbm/sec) (Btu/lbm) (psia) (sec) (lbm/sec)   (Btu/lbm)       (psia) 168.0   173.0         1239.5   49.5   177.0   55.7     1243.3   27.4   186.0   37.9       1245.2         27.8 169.0   151.3         1241.0   44.1   178.0   53.3     1243.3   27.6   187.0   37.0       1245.2         27.6 170.0   174.4         1240.9   49.1   179.0   51.4     1243.7   27.4   188.0   32.6       1245.2         27.5 171.0   154.1         1241.7   45.2   180.0   46.8     1244.3   27.3   190.0   32.4       1245.2         27.9 172.0   137.3         1242.3   40.9   181.0   43.0     1244.8   27.5   192.0   26.8       1245.3         27.6 173.0   122.7         1242.6   37.5   182.0   45.0     1245.1   27.7   194.0   28.3       1246.0         28.1 174.0   112.1         1242.8   34.7   183.0   43.6     1245.3   27.5   196.0   22.1       1246.9         27.8 175.0     98.5         1243.1   31.4   184.0   39.1     1245.3   27.3   198.0   25.0       1246.8         28.3 176.0     87.7         1243.3   28.6   185.0   35.3     1245.2   27.7   200.0   17.7       1246.5         27.9 (31 DEC 2003)
(31 DEC 2003)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia)
Time (sec)
Flow (lbm/sec)
Enthalpy (Btu/lbm)
Pressure (psia) 168.0 173.0 1239.5 49.5 177.0 55.7 1243.3 27.4 186.0 37.9 1245.2 27.8 169.0 151.3 1241.0 44.1 178.0 53.3 1243.3 27.6 187.0 37.0 1245.2 27.6 170.0 174.4 1240.9 49.1 179.0 51.4 1243.7 27.4 188.0 32.6 1245.2 27.5 171.0 154.1 1241.7 45.2 180.0 46.8 1244.3 27.3 190.0 32.4 1245.2 27.9 172.0 137.3 1242.3 40.9 181.0 43.0 1244.8 27.5 192.0 26.8 1245.3 27.6 173.0 122.7 1242.6 37.5 182.0 45.0 1245.1 27.7 194.0 28.3 1246.0 28.1 174.0 112.1 1242.8 34.7 183.0 43.6 1245.3 27.5 196.0 22.1 1246.9 27.8 175.0 98.5 1243.1 31.4 184.0 39.1 1245.3 27.3 198.0 25.0 1246.8 28.3 176.0 87.7 1243.3 28.6 185.0 35.3 1245.2 27.7 200.0 17.7 1246.5 27.9  


Oconee Nuclear Station                                                     UFSAR Table 6-33 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-33 (Page 1 of 1)
(31 DEC 2005)
Table 6-33. NPSH Available and Required for LPI and BS Pumps (Limiting Flow Case)
Table 6-33. NPSH Available and Required for LPI and BS Pumps (Limiting Flow Case)
Flow                       NPSHr                   NPSHa BS                     1110 gpm                     15.0 ft                 21.33 ft LPI                   3840 gpm                     16.5 ft                 18.09 ft Note:
Flow NPSHr NPSHa BS 1110 gpm 15.0 ft 21.33 ft LPI 3840 gpm 16.5 ft 18.09 ft Note:
The above information is currently being revised as part of the Reactor Building Emergency Sump Screen replacement project and will be replaced with updated valves at the completion of that effort.
The above information is currently being revised as part of the Reactor Building Emergency Sump Screen replacement project and will be replaced with updated valves at the completion of that effort.  
(31 DEC 2005)


Oconee Nuclear Station             UFSAR Table 6-34 (Page 1 of 1)
Oconee Nuclear Station UFSAR Table 6-34 (Page 1 of 1)
Table 6-34. Deleted Per 2008 Update (31 DEC 2008)
(31 DEC 2008)
Table 6-34. Deleted Per 2008 Update  


Oconee Nuclear Station                                                                     UFSAR Table 6-35 (Page 1 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 1 of 18)
Table 6-35. ROTSG Peak Pressure Mass and Energy Release Data Reactor Vessel Side                                 Steam Generator Side Liquid                                            Liquid Gas Mass      Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)     (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 0.0       2952.54     1185.14   50071.66   586.96   2194.9   3246.74   1185.47   53239.03     586.22       2195.9 0.1       3252.01     1186.21   49158.25   582.61   1184.1   3591.04   1186.39   50260.68     580.74       1187.2 0.2       3480.73     1187.49   47758.00   578.56   1155.1   3667.39   1188.29   44940.82     575.74       1078.4 0.3       3491.71     1188.37   44815.42   576.24   1108.5   3528.65   1190.47   39264.74     574.99       1010.7 0.4       3572.82     1189.50   40849.95   571.75   1049.1   3814.95   1192.29   33527.03     569.28       962.7 0.5       3582.23     1190.37   38848.06   569.99   1033.8   4077.28   1194.93   30429.58     558.98       923.0 0.6       3603.98     1190.57   38417.86   569.85   1032.2   4555.21   1200.03   30843.14     537.92       849.1 0.7       3631.00     1190.50   38565.54   570.09   1034.6   4940.88   1203.72   31095.94     521.43       807.9 0.8       3681.98     1190.50   38455.83   570.10   1035.7   4877.74   1204.80   29888.32     515.67       776.7 0.9       3757.54     1190.61   37989.32   569.90   1031.9   4689.83   1205.30   29486.80     511.62       754.1 1.0       3857.08     1190.78   37278.62   569.65   1029.8   4451.19   1205.38   29643.73     509.03       742.1 1.1       3998.17     1191.12   36168.17   569.06   1022.8   4192.05   1205.19   30189.31     507.64       736.7 1.2       4164.63     1191.64   34711.18   567.89   1012.0   3936.15   1204.89   30906.12     506.99       735.4 1.3       4325.52     1192.23   33257.31   566.34     999.0   3706.45   1204.57   31632.17     506.74       735.9 1.4       4885.59     1195.32   32760.04   558.32     988.0   3515.74   1204.30   32257.22     506.65       736.9 1.5       5584.34     1199.42   30882.26   544.85     873.7   3370.40   1204.10   32701.09     506.54       737.3 1.6       5860.66     1201.32   29087.52   537.20     912.6   3273.78   1203.98   32895.95     506.36       737.1 1.7       6167.30     1203.04   28953.62   533.36     884.2   3214.41   1203.93   32897.65     506.07       736.0 1.8       6527.57     1205.91   27179.85   525.07     806.8   3178.33   1203.95   32817.10     505.55       733.3 (31 DEC 2003)
(31 DEC 2003)
Table 6-35. ROTSG Peak Pressure Mass and Energy Release Data Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 0.0 2952.54 1185.14 50071.66 586.96 2194.9 3246.74 1185.47 53239.03 586.22 2195.9 0.1 3252.01 1186.21 49158.25 582.61 1184.1 3591.04 1186.39 50260.68 580.74 1187.2 0.2 3480.73 1187.49 47758.00 578.56 1155.1 3667.39 1188.29 44940.82 575.74 1078.4 0.3 3491.71 1188.37 44815.42 576.24 1108.5 3528.65 1190.47 39264.74 574.99 1010.7 0.4 3572.82 1189.50 40849.95 571.75 1049.1 3814.95 1192.29 33527.03 569.28 962.7 0.5 3582.23 1190.37 38848.06 569.99 1033.8 4077.28 1194.93 30429.58 558.98 923.0 0.6 3603.98 1190.57 38417.86 569.85 1032.2 4555.21 1200.03 30843.14 537.92 849.1 0.7 3631.00 1190.50 38565.54 570.09 1034.6 4940.88 1203.72 31095.94 521.43 807.9 0.8 3681.98 1190.50 38455.83 570.10 1035.7 4877.74 1204.80 29888.32 515.67 776.7 0.9 3757.54 1190.61 37989.32 569.90 1031.9 4689.83 1205.30 29486.80 511.62 754.1 1.0 3857.08 1190.78 37278.62 569.65 1029.8 4451.19 1205.38 29643.73 509.03 742.1 1.1 3998.17 1191.12 36168.17 569.06 1022.8 4192.05 1205.19 30189.31 507.64 736.7 1.2 4164.63 1191.64 34711.18 567.89 1012.0 3936.15 1204.89 30906.12 506.99 735.4 1.3 4325.52 1192.23 33257.31 566.34 999.0 3706.45 1204.57 31632.17 506.74 735.9 1.4 4885.59 1195.32 32760.04 558.32 988.0 3515.74 1204.30 32257.22 506.65 736.9 1.5 5584.34 1199.42 30882.26 544.85 873.7 3370.40 1204.10 32701.09 506.54 737.3 1.6 5860.66 1201.32 29087.52 537.20 912.6 3273.78 1203.98 32895.95 506.36 737.1 1.7 6167.30 1203.04 28953.62 533.36 884.2 3214.41 1203.93 32897.65 506.07 736.0 1.8 6527.57 1205.91 27179.85 525.07 806.8 3178.33 1203.95 32817.10 505.55 733.3  


Oconee Nuclear Station                                                                     UFSAR Table 6-35 (Page 2 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 2 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 1.9       6729.14     1208.08   25068.96   517.96   766.6   3163.92   1204.06   32678.24     504.79       729.2 2.0       6928.72     1209.35   23784.28   515.08   758.2   3172.02   1204.22   32466.24     503.84       723.8 2.1       7030.19     1210.21   22869.40   512.77   733.3   3207.95   1204.43   32106.56     502.78       717.6 2.2       6979.55     1210.67   22385.05   510.46   724.0   3265.28   1204.66   31601.79     501.67       711.2 2.3       6907.46     1210.93   22100.22   508.65   713.2   3329.78   1204.92   31039.75     500.48       704.3 2.4       6861.16     1211.26   21717.82   506.83   703.7   3397.75   1205.19   30450.86     499.22       696.9 2.5       6859.45     1211.75   21169.86   504.92   692.3   3468.03   1205.48   29853.11     497.92       689.3 2.6       6897.89     1212.43   20433.47   502.80   679.2   3538.34   1205.78   29265.49     496.63       681.9 2.7       6946.79     1213.25   19584.63   500.40   663.8   3606.07   1206.08   28677.95     495.32       674.5 2.8       6972.43     1214.01   18804.56   497.95   648.7   3670.47   1206.40   28063.32     493.89       666.5 2.9       6965.69     1214.59   18207.22   495.77   636.2   3733.35   1206.74   27429.91     492.32       657.7 3.0       6929.04     1214.96   17795.66   493.90   625.8   3792.59   1207.12   26777.52     490.47       647.6 3.1       6864.79     1215.14   17567.74   492.36   617.9   3842.57   1207.49   26105.76     488.42       636.0 3.2       6784.36     1215.15   17506.03   491.21   612.8   3877.66   1207.82   25467.85     486.44       625.4 3.3       6698.04     1215.06   17543.30   490.34   609.6   3895.99   1208.09   24920.13     484.63       616.2 3.4       6605.71     1214.92   17611.35   489.54   606.6   3926.78   1208.38   24355.35     482.94       607.4 3.5       6506.09     1214.76   17695.64   488.72   603.7   3983.00   1208.74   23690.59     481.19       597.9 3.6       6399.97     1214.56   17815.95   487.95   601.1   4041.44   1209.13   23004.56     479.38       588.2 3.7       6291.48     1214.31   17985.53   487.32   599.3   4091.37   1209.50   22330.49     477.50       578.4 3.8       6189.08     1214.05   18192.78   486.90   598.9   4132.22   1209.86   21676.24     475.58       568.2 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 1.9 6729.14 1208.08 25068.96 517.96 766.6 3163.92 1204.06 32678.24 504.79 729.2 2.0 6928.72 1209.35 23784.28 515.08 758.2 3172.02 1204.22 32466.24 503.84 723.8 2.1 7030.19 1210.21 22869.40 512.77 733.3 3207.95 1204.43 32106.56 502.78 717.6 2.2 6979.55 1210.67 22385.05 510.46 724.0 3265.28 1204.66 31601.79 501.67 711.2 2.3 6907.46 1210.93 22100.22 508.65 713.2 3329.78 1204.92 31039.75 500.48 704.3 2.4 6861.16 1211.26 21717.82 506.83 703.7 3397.75 1205.19 30450.86 499.22 696.9 2.5 6859.45 1211.75 21169.86 504.92 692.3 3468.03 1205.48 29853.11 497.92 689.3 2.6 6897.89 1212.43 20433.47 502.80 679.2 3538.34 1205.78 29265.49 496.63 681.9 2.7 6946.79 1213.25 19584.63 500.40 663.8 3606.07 1206.08 28677.95 495.32 674.5 2.8 6972.43 1214.01 18804.56 497.95 648.7 3670.47 1206.40 28063.32 493.89 666.5 2.9 6965.69 1214.59 18207.22 495.77 636.2 3733.35 1206.74 27429.91 492.32 657.7 3.0 6929.04 1214.96 17795.66 493.90 625.8 3792.59 1207.12 26777.52 490.47 647.6 3.1 6864.79 1215.14 17567.74 492.36 617.9 3842.57 1207.49 26105.76 488.42 636.0 3.2 6784.36 1215.15 17506.03 491.21 612.8 3877.66 1207.82 25467.85 486.44 625.4 3.3 6698.04 1215.06 17543.30 490.34 609.6 3895.99 1208.09 24920.13 484.63 616.2 3.4 6605.71 1214.92 17611.35 489.54 606.6 3926.78 1208.38 24355.35 482.94 607.4 3.5 6506.09 1214.76 17695.64 488.72 603.7 3983.00 1208.74 23690.59 481.19 597.9 3.6 6399.97 1214.56 17815.95 487.95 601.1 4041.44 1209.13 23004.56 479.38 588.2 3.7 6291.48 1214.31 17985.53 487.32 599.3 4091.37 1209.50 22330.49 477.50 578.4 3.8 6189.08 1214.05 18192.78 486.90 598.9 4132.22 1209.86 21676.24 475.58 568.2  


Oconee Nuclear Station                                                                     UFSAR Table 6-35 (Page 3 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 3 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 3.9       6093.43     1213.81   18364.62   486.43   598.2   4166.94   1210.20   21051.50     473.67       558.5 4.0       6002.18     1213.65   18455.89   485.75   595.6   4197.72   1210.53   20464.28     471.84       549.2 4.1       5911.43     1213.51   18513.10   484.94   592.6   4223.01   1210.84   19912.58     470.07       540.3 4.2       5816.88     1213.37   18590.20   484.14   589.5   4242.05   1211.12   19393.09     468.34       531.6 4.3       5723.32     1213.20   18694.91   483.44   587.5   4255.78   1211.39   18902.81     466.64       523.3 4.4       5636.97     1213.05   18782.69   482.76   585.1   4265.65   1211.64   18437.72     464.97       515.2 4.5       5564.71     1212.95   18826.56   482.08   582.7   4272.74   1211.89   17995.82     463.35       507.6 4.6       5509.04     1212.91   18804.40   481.36   579.8   4277.21   1212.11   17578.40     461.79       499.9 4.7       5462.44     1212.92   18716.22   480.50   575.8   4278.83   1212.31   17196.05     460.31       493.2 4.8       5420.41     1212.96   18600.10   479.59   571.6   4275.28   1212.50   16828.26     458.83       486.3 4.9       5384.66     1213.01   18470.19   478.68   567.3   4271.12   1212.70   16445.34     457.27       479.1 5.0       5355.41     1213.09   18322.90   477.77   563.1   4271.49   1212.92   16042.20     455.68       471.8 5.1       5331.29     1213.19   18153.43   476.84   558.7   4276.89   1213.18   15619.78     454.08       464.4 5.2       5313.06     1213.31   17958.80   475.89   554.0   4287.63   1213.45   15191.15     452.52       457.0 5.3       5301.69     1213.46   17733.09   474.89   549.1   4300.49   1213.72   14774.33     451.03       450.1 5.4       5294.20     1213.64   17480.21   473.84   543.8   4312.15   1213.98   14377.30     449.60       443.4 5.5       5286.91     1213.82   17214.45   472.74   538.2   4322.38   1214.24   13995.30     448.20       437.0 5.6       5275.98     1214.00   16947.60   471.59   532.5   4331.98   1214.49   13619.61     446.82       430.6 5.7       5251.41     1214.14   16715.41   470.39   526.7   4341.53   1214.74   13244.54     445.44       424.3 5.8       5209.31     1214.20   16562.60   469.26   521.7   4351.99   1215.01   12866.73     444.06       417.9 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 3.9 6093.43 1213.81 18364.62 486.43 598.2 4166.94 1210.20 21051.50 473.67 558.5 4.0 6002.18 1213.65 18455.89 485.75 595.6 4197.72 1210.53 20464.28 471.84 549.2 4.1 5911.43 1213.51 18513.10 484.94 592.6 4223.01 1210.84 19912.58 470.07 540.3 4.2 5816.88 1213.37 18590.20 484.14 589.5 4242.05 1211.12 19393.09 468.34 531.6 4.3 5723.32 1213.20 18694.91 483.44 587.5 4255.78 1211.39 18902.81 466.64 523.3 4.4 5636.97 1213.05 18782.69 482.76 585.1 4265.65 1211.64 18437.72 464.97 515.2 4.5 5564.71 1212.95 18826.56 482.08 582.7 4272.74 1211.89 17995.82 463.35 507.6 4.6 5509.04 1212.91 18804.40 481.36 579.8 4277.21 1212.11 17578.40 461.79 499.9 4.7 5462.44 1212.92 18716.22 480.50 575.8 4278.83 1212.31 17196.05 460.31 493.2 4.8 5420.41 1212.96 18600.10 479.59 571.6 4275.28 1212.50 16828.26 458.83 486.3 4.9 5384.66 1213.01 18470.19 478.68 567.3 4271.12 1212.70 16445.34 457.27 479.1 5.0 5355.41 1213.09 18322.90 477.77 563.1 4271.49 1212.92 16042.20 455.68 471.8 5.1 5331.29 1213.19 18153.43 476.84 558.7 4276.89 1213.18 15619.78 454.08 464.4 5.2 5313.06 1213.31 17958.80 475.89 554.0 4287.63 1213.45 15191.15 452.52 457.0 5.3 5301.69 1213.46 17733.09 474.89 549.1 4300.49 1213.72 14774.33 451.03 450.1 5.4 5294.20 1213.64 17480.21 473.84 543.8 4312.15 1213.98 14377.30 449.60 443.4 5.5 5286.91 1213.82 17214.45 472.74 538.2 4322.38 1214.24 13995.30 448.20 437.0 5.6 5275.98 1214.00 16947.60 471.59 532.5 4331.98 1214.49 13619.61 446.82 430.6 5.7 5251.41 1214.14 16715.41 470.39 526.7 4341.53 1214.74 13244.54 445.44 424.3 5.8 5209.31 1214.20 16562.60 469.26 521.7 4351.99 1215.01 12866.73 444.06 417.9  


Oconee Nuclear Station                                                                     UFSAR Table 6-35 (Page 4 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 4 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 5.9       5158.60     1214.20   16472.15   468.24   517.5   4364.10   1215.30   12483.40     442.68       411.5 6.0       5106.65     1214.18   16399.34   467.29   513.6   4377.46   1215.62   12092.86     441.28       405.1 6.1       5058.53     1214.18   16312.48   466.33   509.7   4391.25   1215.96   11695.23     439.85       398.5 6.2       5021.41     1214.22   16171.40   465.30   505.4   4405.59   1216.32   11292.11     438.40       391.8 6.3       5008.39     1214.37   15923.55   464.18   500.1   4420.27   1216.70   10885.50     436.94       385.1 6.4       5028.54     1214.69   15526.34   462.92   493.6   4434.26   1217.10   10478.32     435.47       378.3 6.5       5073.99     1215.17   14990.52   461.44   485.4   4446.69   1217.50   10073.97     433.98       371.4 6.6       5131.58     1215.76   14374.32   459.81   476.3   4457.04   1217.91   9674.69     432.48       364.6 6.7       5192.27     1216.42   13736.12   458.12   466.8   4465.40   1218.32   9281.44     430.98       357.7 6.8       5249.12     1217.09   13113.67   456.44   457.3   4472.38   1218.73   8892.40     429.48       350.9 6.9       5296.99     1217.74   12529.17   454.80   448.2   4478.43   1219.16   8504.16     427.96       344.0 7.0       5332.93     1218.34   11994.73   453.20   439.6   4482.85   1219.62   8117.96     426.43       337.0 7.1       5356.00     1218.89   11511.85   451.64   431.4   4484.09   1220.10   7740.85     424.88       330.1 7.2       5366.87     1219.38   11074.62   450.09   423.4   4480.96   1220.57   7380.27     423.32       323.2 7.3       5367.60     1219.82   10674.91   448.55   415.8   4472.86   1221.03   7040.36     421.75       316.5 7.4       5360.53     1220.23   10304.23   447.02   408.4   4459.67   1221.46   6723.53     420.19       309.9 7.5       5347.24     1220.62     9952.78   445.47   401.1   4441.79   1221.87   6430.98     418.65       303.6 7.6       5329.40     1221.01     9610.96   443.89   393.9   4420.44   1222.25   6159.93     417.13       297.6 7.7       5309.32     1221.40     9272.87   442.29   386.5   4397.48   1222.62   5903.92     415.65       291.8 7.8       5289.64     1221.80     8939.86   440.72   379.4   4374.99   1222.97   5655.91     414.21       286.1 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 5.9 5158.60 1214.20 16472.15 468.24 517.5 4364.10 1215.30 12483.40 442.68 411.5 6.0 5106.65 1214.18 16399.34 467.29 513.6 4377.46 1215.62 12092.86 441.28 405.1 6.1 5058.53 1214.18 16312.48 466.33 509.7 4391.25 1215.96 11695.23 439.85 398.5 6.2 5021.41 1214.22 16171.40 465.30 505.4 4405.59 1216.32 11292.11 438.40 391.8 6.3 5008.39 1214.37 15923.55 464.18 500.1 4420.27 1216.70 10885.50 436.94 385.1 6.4 5028.54 1214.69 15526.34 462.92 493.6 4434.26 1217.10 10478.32 435.47 378.3 6.5 5073.99 1215.17 14990.52 461.44 485.4 4446.69 1217.50 10073.97 433.98 371.4 6.6 5131.58 1215.76 14374.32 459.81 476.3 4457.04 1217.91 9674.69 432.48 364.6 6.7 5192.27 1216.42 13736.12 458.12 466.8 4465.40 1218.32 9281.44 430.98 357.7 6.8 5249.12 1217.09 13113.67 456.44 457.3 4472.38 1218.73 8892.40 429.48 350.9 6.9 5296.99 1217.74 12529.17 454.80 448.2 4478.43 1219.16 8504.16 427.96 344.0 7.0 5332.93 1218.34 11994.73 453.20 439.6 4482.85 1219.62 8117.96 426.43 337.0 7.1 5356.00 1218.89 11511.85 451.64 431.4 4484.09 1220.10 7740.85 424.88 330.1 7.2 5366.87 1219.38 11074.62 450.09 423.4 4480.96 1220.57 7380.27 423.32 323.2 7.3 5367.60 1219.82 10674.91 448.55 415.8 4472.86 1221.03 7040.36 421.75 316.5 7.4 5360.53 1220.23 10304.23 447.02 408.4 4459.67 1221.46 6723.53 420.19 309.9 7.5 5347.24 1220.62 9952.78 445.47 401.1 4441.79 1221.87 6430.98 418.65 303.6 7.6 5329.40 1221.01 9610.96 443.89 393.9 4420.44 1222.25 6159.93 417.13 297.6 7.7 5309.32 1221.40 9272.87 442.29 386.5 4397.48 1222.62 5903.92 415.65 291.8 7.8 5289.64 1221.80 8939.86 440.72 379.4 4374.99 1222.97 5655.91 414.21 286.1  


Oconee Nuclear Station                                                                     UFSAR Table 6-35 (Page 5 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 5 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 7.9       5268.74     1222.20     8605.68   439.13   372.0   4354.75   1223.35   5409.71     412.83       280.6 8.0       5248.62     1222.62     8268.98   437.54   364.9   4337.88   1223.77   5160.27     411.50       275.1 8.1       5230.61     1223.05     7936.95   436.00   357.8   4324.49   1224.26   4904.01     410.20       269.7 8.2       5210.71     1223.48     7610.42   434.47   350.8   4314.28   1224.82   4639.68     408.94       264.2 8.3       5185.50     1223.90     7290.51   432.88   343.7   4306.97   1225.45   4368.42     407.72       258.6 8.4       5149.89     1224.29     6981.38   431.16   336.3   4301.07   1226.14   4090.33     406.52       253.0 8.5       5100.61     1224.64     6679.60   429.25   328.6   4294.15   1226.91   3802.16     405.28       247.1 8.6       5041.01     1224.99     6373.97   427.14   320.3   4284.88   1227.80   3496.22     403.95       240.7 8.7       4978.61     1225.36     6064.05   424.95   311.6   4274.21   1228.88   3160.36     402.53       233.6 8.8       4918.44     1225.77     5753.83   422.78   303.5   4264.47   1230.27   2780.89     401.03       225.7 8.9       4859.23     1226.22     5444.20   420.61   295.1   4251.25   1231.89   2383.49     399.48       216.8 9.0       4794.44     1226.62     5150.07   418.40   286.7   4228.88   1233.57   2005.01     397.92       208.0 9.1       4717.10     1226.84     4907.84   416.13   278.8   4188.11   1235.11   1676.80     396.21       199.4 9.2       4624.94     1226.89     4713.82   413.76   271.5   4112.29   1236.10   1442.54     394.02       191.3 9.3       4525.57     1226.87     4533.67   411.27   263.9   3998.83   1236.25   1317.06     391.19       183.9 9.4       4422.59     1226.80     4361.82   408.70   256.4   3861.17   1235.62   1286.28     387.94       177.7 9.5       4315.34     1226.64     4203.04   406.06   249.0   3715.11   1234.44   1319.44     384.55       172.6 9.6       4208.39     1226.45     4054.94   403.42   241.8   3573.79   1233.01   1380.84     381.29       168.3 9.7       4104.11     1226.25     3915.19   400.81   235.0   3445.38   1231.61   1443.70     378.29       164.5 9.8       4002.98     1226.03     3788.12   398.26   228.3   3332.54   1230.37   1493.29     375.59       161.1 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 7.9 5268.74 1222.20 8605.68 439.13 372.0 4354.75 1223.35 5409.71 412.83 280.6 8.0 5248.62 1222.62 8268.98 437.54 364.9 4337.88 1223.77 5160.27 411.50 275.1 8.1 5230.61 1223.05 7936.95 436.00 357.8 4324.49 1224.26 4904.01 410.20 269.7 8.2 5210.71 1223.48 7610.42 434.47 350.8 4314.28 1224.82 4639.68 408.94 264.2 8.3 5185.50 1223.90 7290.51 432.88 343.7 4306.97 1225.45 4368.42 407.72 258.6 8.4 5149.89 1224.29 6981.38 431.16 336.3 4301.07 1226.14 4090.33 406.52 253.0 8.5 5100.61 1224.64 6679.60 429.25 328.6 4294.15 1226.91 3802.16 405.28 247.1 8.6 5041.01 1224.99 6373.97 427.14 320.3 4284.88 1227.80 3496.22 403.95 240.7 8.7 4978.61 1225.36 6064.05 424.95 311.6 4274.21 1228.88 3160.36 402.53 233.6 8.8 4918.44 1225.77 5753.83 422.78 303.5 4264.47 1230.27 2780.89 401.03 225.7 8.9 4859.23 1226.22 5444.20 420.61 295.1 4251.25 1231.89 2383.49 399.48 216.8 9.0 4794.44 1226.62 5150.07 418.40 286.7 4228.88 1233.57 2005.01 397.92 208.0 9.1 4717.10 1226.84 4907.84 416.13 278.8 4188.11 1235.11 1676.80 396.21 199.4 9.2 4624.94 1226.89 4713.82 413.76 271.5 4112.29 1236.10 1442.54 394.02 191.3 9.3 4525.57 1226.87 4533.67 411.27 263.9 3998.83 1236.25 1317.06 391.19 183.9 9.4 4422.59 1226.80 4361.82 408.70 256.4 3861.17 1235.62 1286.28 387.94 177.7 9.5 4315.34 1226.64 4203.04 406.06 249.0 3715.11 1234.44 1319.44 384.55 172.6 9.6 4208.39 1226.45 4054.94 403.42 241.8 3573.79 1233.01 1380.84 381.29 168.3 9.7 4104.11 1226.25 3915.19 400.81 235.0 3445.38 1231.61 1443.70 378.29 164.5 9.8 4002.98 1226.03 3788.12 398.26 228.3 3332.54 1230.37 1493.29 375.59 161.1  


Oconee Nuclear Station                                                                     UFSAR Table 6-35 (Page 6 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 6 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 9.9       3908.74     1225.76     3686.30   395.90   222.8   3235.32   1229.36   1523.70     373.18       157.8 10.0       3801.62     1225.32     3605.12   393.31   217.0   3153.27   1228.60   1532.33     371.06       154.7 10.1       3687.34     1224.80     3519.22   385.59   210.5   3071.49   1227.93   1523.21     363.94       151.6 10.2       3598.56     1224.52     3405.70   383.18   205.0   2967.43   1226.83   1549.42     361.12       147.2 10.3       3531.04     1224.44     3275.64   381.14   199.7   2870.76   1225.59   1600.47     358.61       144.8 10.4       3452.24     1224.25     3152.52   378.85   194.4   2817.51   1225.22   1574.44     357.04       142.2 10.5       3373.12     1224.02     3041.46   376.54   188.9   2800.35   1225.91   1439.72     356.10       138.8 10.6       3318.92     1223.97     2937.43   374.82   185.2   2805.61   1227.46   1230.88     355.62       134.6 10.7       3269.83     1223.96     2833.32   373.22   181.2   2817.97   1229.48     997.89     355.40       130.1 10.8       3218.68     1223.93     2728.20   371.54   177.3   2819.66   1231.40     793.71     355.12       125.7 10.9       3169.92     1223.96     2615.11   369.88   173.3   2801.31   1232.76     646.69     354.42       121.7 11.0       3125.78     1224.06     2493.59   368.29   169.4   2769.07   1233.57     549.41     353.39       118.3 11.1       3082.71     1224.18     2371.39   366.71   165.5   2733.85   1234.12     477.96     352.30       115.4 11.2       3033.10     1224.22     2253.22   364.98   161.5   2701.95   1234.66     411.81     351.34       112.6 11.3       2978.77     1224.19     2143.80   363.14   157.3   2674.46   1235.34     340.97     350.52       109.9 11.4       2917.64     1224.00     2054.52   361.15   153.5   2655.81   1236.24     261.71     349.97       107.4 11.5       2828.28     1223.26     2024.93   358.55   149.4   2634.93   1237.07     183.28     349.40       105.1 11.6       2701.04     1221.73     2072.60   355.13   145.6   2591.18   1237.36     132.54     348.04       102.0 11.7       2555.45     1219.84     2134.30   351.21   141.0   2532.07   1237.23     110.37     346.19       99.0 11.8       2436.12     1218.47     2116.77   347.68   136.2   2469.99   1237.01     96.33     344.28       96.2 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 9.9 3908.74 1225.76 3686.30 395.90 222.8 3235.32 1229.36 1523.70 373.18 157.8 10.0 3801.62 1225.32 3605.12 393.31 217.0 3153.27 1228.60 1532.33 371.06 154.7 10.1 3687.34 1224.80 3519.22 385.59 210.5 3071.49 1227.93 1523.21 363.94 151.6 10.2 3598.56 1224.52 3405.70 383.18 205.0 2967.43 1226.83 1549.42 361.12 147.2 10.3 3531.04 1224.44 3275.64 381.14 199.7 2870.76 1225.59 1600.47 358.61 144.8 10.4 3452.24 1224.25 3152.52 378.85 194.4 2817.51 1225.22 1574.44 357.04 142.2 10.5 3373.12 1224.02 3041.46 376.54 188.9 2800.35 1225.91 1439.72 356.10 138.8 10.6 3318.92 1223.97 2937.43 374.82 185.2 2805.61 1227.46 1230.88 355.62 134.6 10.7 3269.83 1223.96 2833.32 373.22 181.2 2817.97 1229.48 997.89 355.40 130.1 10.8 3218.68 1223.93 2728.20 371.54 177.3 2819.66 1231.40 793.71 355.12 125.7 10.9 3169.92 1223.96 2615.11 369.88 173.3 2801.31 1232.76 646.69 354.42 121.7 11.0 3125.78 1224.06 2493.59 368.29 169.4 2769.07 1233.57 549.41 353.39 118.3 11.1 3082.71 1224.18 2371.39 366.71 165.5 2733.85 1234.12 477.96 352.30 115.4 11.2 3033.10 1224.22 2253.22 364.98 161.5 2701.95 1234.66 411.81 351.34 112.6 11.3 2978.77 1224.19 2143.80 363.14 157.3 2674.46 1235.34 340.97 350.52 109.9 11.4 2917.64 1224.00 2054.52 361.15 153.5 2655.81 1236.24 261.71 349.97 107.4 11.5 2828.28 1223.26 2024.93 358.55 149.4 2634.93 1237.07 183.28 349.40 105.1 11.6 2701.04 1221.73 2072.60 355.13 145.6 2591.18 1237.36 132.54 348.04 102.0 11.7 2555.45 1219.84 2134.30 351.21 141.0 2532.07 1237.23 110.37 346.19 99.0 11.8 2436.12 1218.47 2116.77 347.68 136.2 2469.99 1237.01 96.33 344.28 96.2  


Oconee Nuclear Station                                                                     UFSAR Table 6-35 (Page 7 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 7 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 11.9       2362.55     1218.10     1983.73   344.92   131.5   2387.35   1236.41     96.19     341.42       93.1 12.0       2299.06     1217.99     1823.81   342.21   125.6   2290.04   1235.13     128.95     337.94       88.7 12.1       2231.38     1217.45     1749.89   339.65   122.2   2214.12   1233.88     164.33     335.58       87.4 12.2       2156.97     1216.50     1740.04   337.15   119.1   2164.22   1233.34     169.13     333.89       85.3 12.3       2086.06     1215.54     1733.57   334.74   116.9   2115.02   1232.75     136.58     332.50       83.6 12.4       2000.08     1214.39     1719.46   331.65   113.3   1983.88   1227.32     85.18     328.13       89.1 12.5       1888.23     1212.76     1721.13   327.54   108.5   1842.30   1221.08     68.73     320.75       87.8 12.6       1790.06     1211.21     1731.31   323.87   104.3   1770.92   1219.50     84.20     318.18       87.0 12.7       1699.34     1209.85     1697.05   320.14   100.3   1696.64   1218.10     88.07     315.82       85.9 12.8       1635.43     1208.94     1652.94   317.23   96.5   1625.43   1218.07     69.02     313.51       84.1 12.9       1604.09     1208.60     1605.97   315.61   94.4   1597.64   1219.20     56.24     312.47       84.1 13.0       1562.55     1208.19     1524.04   313.36   91.8   1562.54   1218.43     60.74     311.14       83.7 13.1       1506.14     1207.46     1456.85   310.43   87.3   1478.04   1216.79     57.02     308.37       82.2 13.2       1426.02     1206.05     1435.39   306.58   83.5   1382.20   1215.66     50.38     304.67       80.9 13.3       1341.05     1204.34     1439.95   302.58   80.5   1271.34   1213.67     49.85     300.87       79.4 13.4       1284.05     1202.63     1427.75   300.78   77.8   1148.56   1212.05     44.11     296.93       77.9 13.5       1245.77     1201.26     1370.61   299.99   81.8   1055.04   1211.63     39.42     293.67       76.9 13.6       1219.57     1200.67     1313.42   298.86   80.6     992.54   1211.09     40.57     291.74       76.6 13.7       1176.63     1199.67     1294.43   297.08   79.7     921.42   1209.96     41.28     289.68       76.0 13.8       1109.17     1197.98     1281.82   294.30   77.6     847.66   1209.21     40.34     287.58       75.4 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 11.9 2362.55 1218.10 1983.73 344.92 131.5 2387.35 1236.41 96.19 341.42 93.1 12.0 2299.06 1217.99 1823.81 342.21 125.6 2290.04 1235.13 128.95 337.94 88.7 12.1 2231.38 1217.45 1749.89 339.65 122.2 2214.12 1233.88 164.33 335.58 87.4 12.2 2156.97 1216.50 1740.04 337.15 119.1 2164.22 1233.34 169.13 333.89 85.3 12.3 2086.06 1215.54 1733.57 334.74 116.9 2115.02 1232.75 136.58 332.50 83.6 12.4 2000.08 1214.39 1719.46 331.65 113.3 1983.88 1227.32 85.18 328.13 89.1 12.5 1888.23 1212.76 1721.13 327.54 108.5 1842.30 1221.08 68.73 320.75 87.8 12.6 1790.06 1211.21 1731.31 323.87 104.3 1770.92 1219.50 84.20 318.18 87.0 12.7 1699.34 1209.85 1697.05 320.14 100.3 1696.64 1218.10 88.07 315.82 85.9 12.8 1635.43 1208.94 1652.94 317.23 96.5 1625.43 1218.07 69.02 313.51 84.1 12.9 1604.09 1208.60 1605.97 315.61 94.4 1597.64 1219.20 56.24 312.47 84.1 13.0 1562.55 1208.19 1524.04 313.36 91.8 1562.54 1218.43 60.74 311.14 83.7 13.1 1506.14 1207.46 1456.85 310.43 87.3 1478.04 1216.79 57.02 308.37 82.2 13.2 1426.02 1206.05 1435.39 306.58 83.5 1382.20 1215.66 50.38 304.67 80.9 13.3 1341.05 1204.34 1439.95 302.58 80.5 1271.34 1213.67 49.85 300.87 79.4 13.4 1284.05 1202.63 1427.75 300.78 77.8 1148.56 1212.05 44.11 296.93 77.9 13.5 1245.77 1201.26 1370.61 299.99 81.8 1055.04 1211.63 39.42 293.67 76.9 13.6 1219.57 1200.67 1313.42 298.86 80.6 992.54 1211.09 40.57 291.74 76.6 13.7 1176.63 1199.67 1294.43 297.08 79.7 921.42 1209.96 41.28 289.68 76.0 13.8 1109.17 1197.98 1281.82 294.30 77.6 847.66 1209.21 40.34 287.58 75.4  


Oconee Nuclear Station                                                                     UFSAR Table 6-35 (Page 8 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 8 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow    Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 13.9       1036.37     1196.13     1258.32   291.69   76.8     783.40   1208.74     40.25       285.91       75.1 14.0       958.19     1194.18     1229.61   289.47   76.2     706.24   1207.53     42.45       284.02       74.6 14.1       872.95     1192.17     1177.32   287.22   75.5     615.42   1205.51     47.28       282.05       74.4 14.2       788.89     1190.28     1097.60   285.16   75.0     520.17   1203.40     51.66       280.37       74.2 14.3       718.62     1188.80     999.35   283.60   74.7     398.36   1202.09     48.53       278.82       73.8 14.4       656.81     1187.68     894.77   282.35   74.4     246.09   1201.97     35.16       277.43       73.6 14.5       600.47     1186.91     814.76   281.31   74.2     128.05   1201.52     20.20       276.64       73.6 14.6       552.32     1186.50     769.06   280.53   74.1     124.91   1198.52     19.51       276.67       73.8 14.7       506.53     1186.20     731.54   279.86   74.0     106.18   1197.65     18.85       276.60       73.6 14.8       466.33     1185.95     689.70   279.30   74.0     25.93   1197.03     6.47       276.43       73.6 14.9       424.01     1185.72     643.05   278.80   73.8       0.00   1178.28     0.12       284.00       73.7 15.0       375.60     1185.54     584.78   278.30   73.8     0.00   1178.14     0.00       271.42       73.5 15.1       337.56     1185.36     529.24   277.94   73.8       0.00   1178.24     0.00       271.43       73.6 15.2       317.03     1185.18     492.40   277.74   73.8       0.00   1178.09     0.00       271.49       73.4 15.3       305.80     1184.98     477.44   277.63   73.8       0.00   1178.09     0.00       271.52       73.4 15.4       281.06     1184.75     461.91   277.46   73.7       0.00   1178.04     0.00       271.59       73.3 15.5       236.22     1184.58     411.74   277.23   73.7       0.00   1177.90     0.00       271.73       73.1 15.6       190.97     1184.41     336.17   276.98   73.7       0.00   1177.81     0.00       271.85       72.9 15.7       159.07     1184.23     273.40   276.77   73.7       0.00   1177.80     0.00       271.87       72.8 15.8       145.83     1184.09     237.46   276.71   73.7       0.00   1177.78     0.00       271.89       72.8 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 13.9 1036.37 1196.13 1258.32 291.69 76.8 783.40 1208.74 40.25 285.91 75.1 14.0 958.19 1194.18 1229.61 289.47 76.2 706.24 1207.53 42.45 284.02 74.6 14.1 872.95 1192.17 1177.32 287.22 75.5 615.42 1205.51 47.28 282.05 74.4 14.2 788.89 1190.28 1097.60 285.16 75.0 520.17 1203.40 51.66 280.37 74.2 14.3 718.62 1188.80 999.35 283.60 74.7 398.36 1202.09 48.53 278.82 73.8 14.4 656.81 1187.68 894.77 282.35 74.4 246.09 1201.97 35.16 277.43 73.6 14.5 600.47 1186.91 814.76 281.31 74.2 128.05 1201.52 20.20 276.64 73.6 14.6 552.32 1186.50 769.06 280.53 74.1 124.91 1198.52 19.51 276.67 73.8 14.7 506.53 1186.20 731.54 279.86 74.0 106.18 1197.65 18.85 276.60 73.6 14.8 466.33 1185.95 689.70 279.30 74.0 25.93 1197.03 6.47 276.43 73.6 14.9 424.01 1185.72 643.05 278.80 73.8 0.00 1178.28 0.12 284.00 73.7 15.0 375.60 1185.54 584.78 278.30 73.8 0.00 1178.14 0.00 271.42 73.5 15.1 337.56 1185.36 529.24 277.94 73.8 0.00 1178.24 0.00 271.43 73.6 15.2 317.03 1185.18 492.40 277.74 73.8 0.00 1178.09 0.00 271.49 73.4 15.3 305.80 1184.98 477.44 277.63 73.8 0.00 1178.09 0.00 271.52 73.4 15.4 281.06 1184.75 461.91 277.46 73.7 0.00 1178.04 0.00 271.59 73.3 15.5 236.22 1184.58 411.74 277.23 73.7 0.00 1177.90 0.00 271.73 73.1 15.6 190.97 1184.41 336.17 276.98 73.7 0.00 1177.81 0.00 271.85 72.9 15.7 159.07 1184.23 273.40 276.77 73.7 0.00 1177.80 0.00 271.87 72.8 15.8 145.83 1184.09 237.46 276.71 73.7 0.00 1177.78 0.00 271.89 72.8  


Oconee Nuclear Station                                                                     UFSAR Table 6-35 (Page 9 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 9 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow    Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 15.9       162.79     1184.08     234.57   276.80   73.8       0.00   1177.83     0.00       271.87       72.9 16.0       204.82     1183.92     287.14   277.05   73.9       0.00   1178.21     0.00       271.48       73.6 16.1       263.22     1183.94     395.96   277.64   73.9       0.00   1178.06     0.00       271.58       73.3 16.2       353.08     1184.07     577.52   278.45   74.5       0.00   1177.94     0.00       271.69       73.1 16.3       364.98     1184.35     642.89   278.36   73.7       0.00   1177.56     0.00       272.04       72.5 16.4       300.17     1184.95     529.82   277.74   73.7       0.00   1177.06     0.00       272.62       71.5 16.5       302.18     1185.10     470.69   277.74   73.9     111.37   1197.18     0.18       277.14       74.1 16.6       346.51     1184.78     526.70   278.13   74.0     132.52   1198.18     0.22       277.78       73.4 16.7       377.87     1184.68     605.16   278.38   74.0     21.16   1203.47     0.05       280.00       73.2 16.8       388.91     1184.93     629.58   278.46   74.0       0.00   1178.09     0.00       271.51       73.4 16.9       404.55     1185.15     643.68   278.67   74.0       0.00   1178.13     0.00       271.53       73.5 17.0       426.13     1185.16     670.75   278.91   74.1       0.00   1178.10     0.00       271.59       73.4 17.1       423.44     1185.24     669.67   278.82   74.0       0.00   1178.20     0.00       271.49       73.6 17.2       414.13     1185.43     651.39   278.72   74.0       0.00   1178.21     0.00       271.48       73.6 17.3       419.35     1185.35     656.09   278.80   74.1       0.00   1178.01     0.00       271.53       73.3 17.4       422.88     1185.38     662.39   278.86   73.9       0.00   1177.81     0.00       271.83       72.9 17.5       463.43     1185.55     718.56   279.57   74.3       0.00   1177.77     0.00       271.92       72.8 17.6       533.97     1185.84     823.64   280.52   74.6       0.00   1178.08     0.00       271.65       73.3 17.7       513.09     1186.16     791.87   280.13   73.8       6.58   1187.22     0.00       272.09       72.2 17.8       450.98     1186.10     693.63   279.12   73.9     106.67   1198.85     0.00       272.62       74.5 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 15.9 162.79 1184.08 234.57 276.80 73.8 0.00 1177.83 0.00 271.87 72.9 16.0 204.82 1183.92 287.14 277.05 73.9 0.00 1178.21 0.00 271.48 73.6 16.1 263.22 1183.94 395.96 277.64 73.9 0.00 1178.06 0.00 271.58 73.3 16.2 353.08 1184.07 577.52 278.45 74.5 0.00 1177.94 0.00 271.69 73.1 16.3 364.98 1184.35 642.89 278.36 73.7 0.00 1177.56 0.00 272.04 72.5 16.4 300.17 1184.95 529.82 277.74 73.7 0.00 1177.06 0.00 272.62 71.5 16.5 302.18 1185.10 470.69 277.74 73.9 111.37 1197.18 0.18 277.14 74.1 16.6 346.51 1184.78 526.70 278.13 74.0 132.52 1198.18 0.22 277.78 73.4 16.7 377.87 1184.68 605.16 278.38 74.0 21.16 1203.47 0.05 280.00 73.2 16.8 388.91 1184.93 629.58 278.46 74.0 0.00 1178.09 0.00 271.51 73.4 16.9 404.55 1185.15 643.68 278.67 74.0 0.00 1178.13 0.00 271.53 73.5 17.0 426.13 1185.16 670.75 278.91 74.1 0.00 1178.10 0.00 271.59 73.4 17.1 423.44 1185.24 669.67 278.82 74.0 0.00 1178.20 0.00 271.49 73.6 17.2 414.13 1185.43 651.39 278.72 74.0 0.00 1178.21 0.00 271.48 73.6 17.3 419.35 1185.35 656.09 278.80 74.1 0.00 1178.01 0.00 271.53 73.3 17.4 422.88 1185.38 662.39 278.86 73.9 0.00 1177.81 0.00 271.83 72.9 17.5 463.43 1185.55 718.56 279.57 74.3 0.00 1177.77 0.00 271.92 72.8 17.6 533.97 1185.84 823.64 280.52 74.6 0.00 1178.08 0.00 271.65 73.3 17.7 513.09 1186.16 791.87 280.13 73.8 6.58 1187.22 0.00 272.09 72.2 17.8 450.98 1186.10 693.63 279.12 73.9 106.67 1198.85 0.00 272.62 74.5  


Oconee Nuclear Station                                                                   UFSAR Table 6-35 (Page 10 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 10 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow    Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 17.9       478.30     1186.17     730.24   279.88   74.0     110.32   1200.25     0.00       271.27       73.5 18.0       573.32     1186.80     877.21   281.40   75.3     10.23   1206.49     0.00       271.40       73.7 18.1       587.98     1186.84     889.92   281.30   74.1     62.46   1208.55     0.00       271.41       73.8 18.2       531.31     1186.47     779.51   280.27   74.0     94.26   1210.86     0.00       271.75       73.6 18.3       536.99     1186.32     791.79   280.43   74.9     31.80   1215.40     0.00       271.42       73.5 18.4       525.84     1186.22     792.74   280.25   73.9     15.26   1195.91     0.00       271.48       73.6 18.5       483.93     1186.08     736.24   279.57   74.0     82.90   1210.27     0.00       271.91       73.9 18.6       514.15     1186.25     780.92   280.32   74.1     70.67   1213.79     0.00       271.28       73.5 18.7       617.22     1187.39     950.24   282.25   75.1       3.04   1219.95     0.00       271.49       73.4 18.8       667.82     1187.83     1102.16   282.78   74.9       0.00   1178.30     0.00       271.48       73.7 18.9       645.51     1187.42     1141.82   282.31   74.7       0.00   1178.22     0.00       271.48       73.6 19.0       628.92     1187.12     1126.53   282.04   74.6       4.03   1186.52     0.00       271.72       73.1 19.1       622.35     1187.00     1097.76   281.92   74.6     26.97   1193.74     0.00       271.80       74.0 19.2       627.60     1187.10     1089.15   282.03   74.6     22.94   1195.01     0.00       271.96       72.5 19.3       634.07     1187.20     1089.87   282.13   74.8       0.00   1176.90     0.00       272.77       71.2 19.4       628.25     1187.10     1061.93   281.98   74.7       0.00   1176.11     0.00       273.36       69.7 19.5       615.30     1186.87     1021.49   281.73   74.5       0.00   1175.67     0.00       273.59       68.8 19.6       615.67     1186.88     1017.16   281.75   74.6       0.00   1175.75     0.00       273.56       68.9 19.7       622.13     1187.00     1031.23   281.91   74.5       0.00   1176.61     0.00       273.12       70.5 19.8       641.78     1187.36     1071.28   282.31   75.0     131.44   1201.24     0.01       266.67       74.1 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 17.9 478.30 1186.17 730.24 279.88 74.0 110.32 1200.25 0.00 271.27 73.5 18.0 573.32 1186.80 877.21 281.40 75.3 10.23 1206.49 0.00 271.40 73.7 18.1 587.98 1186.84 889.92 281.30 74.1 62.46 1208.55 0.00 271.41 73.8 18.2 531.31 1186.47 779.51 280.27 74.0 94.26 1210.86 0.00 271.75 73.6 18.3 536.99 1186.32 791.79 280.43 74.9 31.80 1215.40 0.00 271.42 73.5 18.4 525.84 1186.22 792.74 280.25 73.9 15.26 1195.91 0.00 271.48 73.6 18.5 483.93 1186.08 736.24 279.57 74.0 82.90 1210.27 0.00 271.91 73.9 18.6 514.15 1186.25 780.92 280.32 74.1 70.67 1213.79 0.00 271.28 73.5 18.7 617.22 1187.39 950.24 282.25 75.1 3.04 1219.95 0.00 271.49 73.4 18.8 667.82 1187.83 1102.16 282.78 74.9 0.00 1178.30 0.00 271.48 73.7 18.9 645.51 1187.42 1141.82 282.31 74.7 0.00 1178.22 0.00 271.48 73.6 19.0 628.92 1187.12 1126.53 282.04 74.6 4.03 1186.52 0.00 271.72 73.1 19.1 622.35 1187.00 1097.76 281.92 74.6 26.97 1193.74 0.00 271.80 74.0 19.2 627.60 1187.10 1089.15 282.03 74.6 22.94 1195.01 0.00 271.96 72.5 19.3 634.07 1187.20 1089.87 282.13 74.8 0.00 1176.90 0.00 272.77 71.2 19.4 628.25 1187.10 1061.93 281.98 74.7 0.00 1176.11 0.00 273.36 69.7 19.5 615.30 1186.87 1021.49 281.73 74.5 0.00 1175.67 0.00 273.59 68.8 19.6 615.67 1186.88 1017.16 281.75 74.6 0.00 1175.75 0.00 273.56 68.9 19.7 622.13 1187.00 1031.23 281.91 74.5 0.00 1176.61 0.00 273.12 70.5 19.8 641.78 1187.36 1071.28 282.31 75.0 131.44 1201.24 0.01 266.67 74.1  


Oconee Nuclear Station                                                                   UFSAR Table 6-35 (Page 11 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 11 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow    Enthalpy      Flow  Enthalpy  Pressure    Flow  Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 19.9       660.65     1187.68     1105.49   282.65   74.7     297.04   1208.90     0.03       280.00       73.9 20.0       693.38     1188.33     1156.25   283.34   74.9     99.94   1213.59     0.01       272.33       73.6 20.5       670.39     1187.93     1106.57   282.89   74.9     29.06   1212.19     0.00       271.41       73.6 21.0       627.19     1187.19     1024.96   282.00   75.2       2.35   1214.04     0.00       271.42       73.5 21.5       622.60     1187.31     942.12   282.04   74.2       6.47   1192.30     0.00       271.41       73.6 22.0       686.28     1188.48     987.12   283.37   75.0     17.12   1198.12     0.00       271.40       73.6 22.5       750.89     1189.44     1103.70   284.44   75.1     19.11   1206.91     0.00       271.34       73.6 23.0       685.30     1188.72     852.21   283.60   74.5       8.32   1214.00     0.00       271.44       73.5 23.5       615.57     1187.41     753.03   281.84   74.2     47.88   1208.63     0.00       271.54       73.6 24.0       637.82     1187.44     1130.65   282.45   75.3     59.58   1208.17     0.00       271.45       73.7 24.5       634.17     1187.47     1069.06   282.31   74.6     14.91   1206.76     0.00       271.43       73.7 25.0       574.77     1186.80     887.07   280.95   74.2       4.34   1203.16     0.00       271.41       73.6 25.5       537.79     1185.98     1117.72   280.56   74.5       5.24   1197.52     0.00       271.43       73.7 26.0       511.36     1185.64     1195.69   280.22   74.4       7.49   1198.95     0.00       271.41       73.7 26.5       458.63     1185.30     1158.46   279.44   74.2     12.45   1207.33     0.00       271.43       73.7 27.0       411.02     1184.92     1179.36   278.87   74.2     13.00   1213.62     0.00       271.40       73.7 27.5       372.88     1184.54     1296.24   278.46   74.1     12.37   1221.75     0.00       271.45       73.7 28.0       344.56     1184.22     1409.40   278.22   74.1       9.15   1221.44     0.00       271.41       73.7 28.5       317.63     1184.07     1368.75   277.94   74.0       2.74   1206.24     0.00       271.42       73.7 29.0       291.03     1184.01     1290.63   277.67   74.0       4.29   1207.32     0.00       271.39       73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 19.9 660.65 1187.68 1105.49 282.65 74.7 297.04 1208.90 0.03 280.00 73.9 20.0 693.38 1188.33 1156.25 283.34 74.9 99.94 1213.59 0.01 272.33 73.6 20.5 670.39 1187.93 1106.57 282.89 74.9 29.06 1212.19 0.00 271.41 73.6 21.0 627.19 1187.19 1024.96 282.00 75.2 2.35 1214.04 0.00 271.42 73.5 21.5 622.60 1187.31 942.12 282.04 74.2 6.47 1192.30 0.00 271.41 73.6 22.0 686.28 1188.48 987.12 283.37 75.0 17.12 1198.12 0.00 271.40 73.6 22.5 750.89 1189.44 1103.70 284.44 75.1 19.11 1206.91 0.00 271.34 73.6 23.0 685.30 1188.72 852.21 283.60 74.5 8.32 1214.00 0.00 271.44 73.5 23.5 615.57 1187.41 753.03 281.84 74.2 47.88 1208.63 0.00 271.54 73.6 24.0 637.82 1187.44 1130.65 282.45 75.3 59.58 1208.17 0.00 271.45 73.7 24.5 634.17 1187.47 1069.06 282.31 74.6 14.91 1206.76 0.00 271.43 73.7 25.0 574.77 1186.80 887.07 280.95 74.2 4.34 1203.16 0.00 271.41 73.6 25.5 537.79 1185.98 1117.72 280.56 74.5 5.24 1197.52 0.00 271.43 73.7 26.0 511.36 1185.64 1195.69 280.22 74.4 7.49 1198.95 0.00 271.41 73.7 26.5 458.63 1185.30 1158.46 279.44 74.2 12.45 1207.33 0.00 271.43 73.7 27.0 411.02 1184.92 1179.36 278.87 74.2 13.00 1213.62 0.00 271.40 73.7 27.5 372.88 1184.54 1296.24 278.46 74.1 12.37 1221.75 0.00 271.45 73.7 28.0 344.56 1184.22 1409.40 278.22 74.1 9.15 1221.44 0.00 271.41 73.7 28.5 317.63 1184.07 1368.75 277.94 74.0 2.74 1206.24 0.00 271.42 73.7 29.0 291.03 1184.01 1290.63 277.67 74.0 4.29 1207.32 0.00 271.39 73.7  


Oconee Nuclear Station                                                                   UFSAR Table 6-35 (Page 12 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 12 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 29.5       262.84     1183.99     1173.69   277.42   73.9     2.42   1208.45     0.00       271.37       73.7 30.0       239.91     1183.99     1028.93   277.24   73.8     0.17   1208.16     0.00       271.42       73.7 30.5       222.83     1183.93     933.73   277.12   73.8     0.30   1186.83     0.00       271.40       73.7 31.0       206.51     1183.84     852.42   277.02   73.8     1.01   1188.83     0.00       271.39       73.7 31.5       196.63     1183.76     776.21   276.96   73.8     4.08   1201.34     0.00       271.39       73.7 32.0       190.70     1183.69     775.96   276.93   73.8     13.68   1223.72     0.00       271.42       73.7 32.5       179.66     1183.56     854.17   276.88   73.8     19.86   1235.99     0.00       271.40       73.7 33.0       162.66     1183.39     903.59   276.81   73.8     14.99   1240.65     0.00       271.40       73.7 33.5       148.17     1183.26     783.13   276.74   73.7     6.54   1231.93     0.00       271.40       73.7 34.0       141.77     1183.20     623.80   276.71   73.7     3.27   1203.22     0.00       271.33       73.6 34.5       145.56     1183.16     679.51   276.74   73.8     4.76   1210.38     0.00       271.41       73.7 35.0       148.67     1183.06     1109.38   276.79   73.8     2.59   1216.08     0.00       271.40       73.8 35.5       143.83     1182.84     1858.91   276.87   73.8     16.90   1208.62     0.00       271.55       73.4 36.0       137.78     1182.56     2537.08   276.93   73.9     23.19   1208.76     0.00       271.46       73.8 36.5       132.72     1182.38     2826.84   276.96   74.0     12.90   1214.29     0.00       271.42       73.7 37.0       129.98     1182.29     2876.72   276.97   74.0     9.91   1219.01     0.00       271.40       73.7 37.5       128.23     1182.24     2964.72   276.99   74.0     8.40   1208.43     0.00       271.49       73.8 38.0       127.47     1182.17     3154.39   277.03   74.1     8.06   1204.87     0.00       271.40       73.7 38.5       126.26     1182.12     3340.97   277.06   74.1     6.62   1217.32     0.00       271.41       73.7 39.0       123.70     1182.09     3378.19   277.04   74.1     9.45   1230.39     0.00       271.40       73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 29.5 262.84 1183.99 1173.69 277.42 73.9 2.42 1208.45 0.00 271.37 73.7 30.0 239.91 1183.99 1028.93 277.24 73.8 0.17 1208.16 0.00 271.42 73.7 30.5 222.83 1183.93 933.73 277.12 73.8 0.30 1186.83 0.00 271.40 73.7 31.0 206.51 1183.84 852.42 277.02 73.8 1.01 1188.83 0.00 271.39 73.7 31.5 196.63 1183.76 776.21 276.96 73.8 4.08 1201.34 0.00 271.39 73.7 32.0 190.70 1183.69 775.96 276.93 73.8 13.68 1223.72 0.00 271.42 73.7 32.5 179.66 1183.56 854.17 276.88 73.8 19.86 1235.99 0.00 271.40 73.7 33.0 162.66 1183.39 903.59 276.81 73.8 14.99 1240.65 0.00 271.40 73.7 33.5 148.17 1183.26 783.13 276.74 73.7 6.54 1231.93 0.00 271.40 73.7 34.0 141.77 1183.20 623.80 276.71 73.7 3.27 1203.22 0.00 271.33 73.6 34.5 145.56 1183.16 679.51 276.74 73.8 4.76 1210.38 0.00 271.41 73.7 35.0 148.67 1183.06 1109.38 276.79 73.8 2.59 1216.08 0.00 271.40 73.8 35.5 143.83 1182.84 1858.91 276.87 73.8 16.90 1208.62 0.00 271.55 73.4 36.0 137.78 1182.56 2537.08 276.93 73.9 23.19 1208.76 0.00 271.46 73.8 36.5 132.72 1182.38 2826.84 276.96 74.0 12.90 1214.29 0.00 271.42 73.7 37.0 129.98 1182.29 2876.72 276.97 74.0 9.91 1219.01 0.00 271.40 73.7 37.5 128.23 1182.24 2964.72 276.99 74.0 8.40 1208.43 0.00 271.49 73.8 38.0 127.47 1182.17 3154.39 277.03 74.1 8.06 1204.87 0.00 271.40 73.7 38.5 126.26 1182.12 3340.97 277.06 74.1 6.62 1217.32 0.00 271.41 73.7 39.0 123.70 1182.09 3378.19 277.04 74.1 9.45 1230.39 0.00 271.40 73.7  


Oconee Nuclear Station                                                                   UFSAR Table 6-35 (Page 13 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 13 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow    Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 39.5       119.88     1182.10     3245.16   276.97   74.1     13.37   1239.57     0.00       271.40       73.7 40.0       115.99     1182.13     3085.22   276.91   74.0     17.92   1244.92     0.00       271.41       73.7 40.5       113.36     1182.14     3022.42   276.89   74.0     17.58   1246.55     0.00       271.41       73.7 41.0       111.45     1182.12     3045.18   276.88   74.0     18.08   1247.27     0.00       271.41       73.7 41.5       108.87     1182.10     3107.73   276.87   74.0     18.19   1247.50     0.00       271.38       73.7 42.0       105.23     1182.09     3179.22   276.85   74.0     18.37   1247.68     0.00       271.42       73.7 42.5       100.54     1182.08     3197.31   276.81   74.0     18.19   1247.58     0.00       271.41       73.7 43.0       95.27     1182.06     3102.78   276.71   73.9     17.86   1247.60     0.00       271.42       73.7 43.5       89.48     1182.07     2936.29   276.57   73.7     16.11   1247.82     0.00       271.41       73.7 44.0       81.96     1182.14     2729.48   276.49   73.7     6.77   1246.77     0.00       271.40       73.7 44.5       73.11     1182.20     2494.15   276.47   73.7     1.37   1242.27     0.00       271.39       73.7 45.0       63.95     1182.27     2241.93   276.46   73.7     0.01   1232.88     0.00       271.40       73.7 45.5       55.22     1182.38     1956.43   276.44   73.7     0.00   1178.26     0.00       271.40       73.7 46.0       47.90     1182.48     1663.32   276.43   73.7     0.00   1190.48     0.00       271.40       73.7 46.5       42.12     1182.55     1402.24   276.42   73.7     0.00   1190.48     0.00       271.40       73.7 47.0       38.02     1182.57     1176.52   276.42   73.7     0.00   1178.26     0.00       271.40       73.7 47.5       35.43     1182.54     984.30   276.42   73.7     0.00   1178.26     0.00       271.40       73.7 48.0       33.13     1182.46     796.83   276.41   73.7     0.00   1178.27     0.00       271.40       73.7 48.5       27.86     1182.33     576.53   276.41   73.7     0.00   1178.26     0.00       271.40       73.7 49.0       20.12     1182.33     360.50   276.40   73.7     0.00   1178.26     0.00       271.40       73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 39.5 119.88 1182.10 3245.16 276.97 74.1 13.37 1239.57 0.00 271.40 73.7 40.0 115.99 1182.13 3085.22 276.91 74.0 17.92 1244.92 0.00 271.41 73.7 40.5 113.36 1182.14 3022.42 276.89 74.0 17.58 1246.55 0.00 271.41 73.7 41.0 111.45 1182.12 3045.18 276.88 74.0 18.08 1247.27 0.00 271.41 73.7 41.5 108.87 1182.10 3107.73 276.87 74.0 18.19 1247.50 0.00 271.38 73.7 42.0 105.23 1182.09 3179.22 276.85 74.0 18.37 1247.68 0.00 271.42 73.7 42.5 100.54 1182.08 3197.31 276.81 74.0 18.19 1247.58 0.00 271.41 73.7 43.0 95.27 1182.06 3102.78 276.71 73.9 17.86 1247.60 0.00 271.42 73.7 43.5 89.48 1182.07 2936.29 276.57 73.7 16.11 1247.82 0.00 271.41 73.7 44.0 81.96 1182.14 2729.48 276.49 73.7 6.77 1246.77 0.00 271.40 73.7 44.5 73.11 1182.20 2494.15 276.47 73.7 1.37 1242.27 0.00 271.39 73.7 45.0 63.95 1182.27 2241.93 276.46 73.7 0.01 1232.88 0.00 271.40 73.7 45.5 55.22 1182.38 1956.43 276.44 73.7 0.00 1178.26 0.00 271.40 73.7 46.0 47.90 1182.48 1663.32 276.43 73.7 0.00 1190.48 0.00 271.40 73.7 46.5 42.12 1182.55 1402.24 276.42 73.7 0.00 1190.48 0.00 271.40 73.7 47.0 38.02 1182.57 1176.52 276.42 73.7 0.00 1178.26 0.00 271.40 73.7 47.5 35.43 1182.54 984.30 276.42 73.7 0.00 1178.26 0.00 271.40 73.7 48.0 33.13 1182.46 796.83 276.41 73.7 0.00 1178.27 0.00 271.40 73.7 48.5 27.86 1182.33 576.53 276.41 73.7 0.00 1178.26 0.00 271.40 73.7 49.0 20.12 1182.33 360.50 276.40 73.7 0.00 1178.26 0.00 271.40 73.7  


Oconee Nuclear Station                                                                   UFSAR Table 6-35 (Page 14 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 14 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 49.5       15.66     1182.63     205.44   276.40   73.7     2.83   1199.98     0.00       271.40       73.7 50.0       14.31     1182.88     109.99   276.40   73.7     10.68   1224.31     0.00       271.41       73.7 50.5       13.18     1183.07       50.45   276.42   73.7     16.67   1242.89     0.00       271.40       73.7 51.0       12.51     1183.25       19.05   276.40   73.7     18.05   1252.86     0.00       271.40       73.7 51.5       12.21     1183.43       6.73   276.36   73.7     19.22   1253.45     0.00       271.41       73.7 52.0       11.87     1183.61       2.34   276.42   73.7     18.79   1252.25     0.00       271.41       73.7 52.5       11.56     1183.83       0.85   276.80   73.7     18.10   1251.16     0.00       271.40       73.7 53.0       10.61     1184.05       0.31   275.97   73.7     19.19   1250.40     0.00       271.41       73.7 53.5         8.27     1184.17       0.11   268.52   73.7     20.75   1249.60     0.00       271.41       73.7 54.0         7.05     1184.30       0.04   282.05   73.7     25.68   1248.39     0.00       271.41       73.7 54.5         7.30     1184.63       0.02   294.12   73.7     31.30   1246.59     0.00       271.42       73.7 55.0         7.41     1185.11       0.01   271.39   73.7     33.32   1244.62     0.00       271.42       73.7 55.5         9.39     1185.63       0.01   271.40   73.7     31.63   1243.25     0.00       271.42       73.7 56.0       12.10     1185.99       0.01   250.00   73.7     25.44   1242.73     0.00       271.41       73.7 56.5       13.96     1186.32       0.01   307.69   73.7     22.89   1243.26     0.00       271.41       73.7 57.0       14.70     1186.66       0.01   307.69   73.7     24.77   1243.80     0.00       271.41       73.7 57.5       14.90     1186.69       0.03   264.71   73.7     25.35   1243.97     0.00       271.41       73.7 58.0       14.52     1186.24       0.09   271.74   73.7     25.52   1244.02     0.00       271.41       73.7 58.5       13.35     1185.60       0.16   280.49   73.7     25.61   1244.01     0.00       271.41       73.7 59.0       15.18     1185.26       0.22   277.27   73.7     25.57   1244.01     0.00       271.41       73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 49.5 15.66 1182.63 205.44 276.40 73.7 2.83 1199.98 0.00 271.40 73.7 50.0 14.31 1182.88 109.99 276.40 73.7 10.68 1224.31 0.00 271.41 73.7 50.5 13.18 1183.07 50.45 276.42 73.7 16.67 1242.89 0.00 271.40 73.7 51.0 12.51 1183.25 19.05 276.40 73.7 18.05 1252.86 0.00 271.40 73.7 51.5 12.21 1183.43 6.73 276.36 73.7 19.22 1253.45 0.00 271.41 73.7 52.0 11.87 1183.61 2.34 276.42 73.7 18.79 1252.25 0.00 271.41 73.7 52.5 11.56 1183.83 0.85 276.80 73.7 18.10 1251.16 0.00 271.40 73.7 53.0 10.61 1184.05 0.31 275.97 73.7 19.19 1250.40 0.00 271.41 73.7 53.5 8.27 1184.17 0.11 268.52 73.7 20.75 1249.60 0.00 271.41 73.7 54.0 7.05 1184.30 0.04 282.05 73.7 25.68 1248.39 0.00 271.41 73.7 54.5 7.30 1184.63 0.02 294.12 73.7 31.30 1246.59 0.00 271.42 73.7 55.0 7.41 1185.11 0.01 271.39 73.7 33.32 1244.62 0.00 271.42 73.7 55.5 9.39 1185.63 0.01 271.40 73.7 31.63 1243.25 0.00 271.42 73.7 56.0 12.10 1185.99 0.01 250.00 73.7 25.44 1242.73 0.00 271.41 73.7 56.5 13.96 1186.32 0.01 307.69 73.7 22.89 1243.26 0.00 271.41 73.7 57.0 14.70 1186.66 0.01 307.69 73.7 24.77 1243.80 0.00 271.41 73.7 57.5 14.90 1186.69 0.03 264.71 73.7 25.35 1243.97 0.00 271.41 73.7 58.0 14.52 1186.24 0.09 271.74 73.7 25.52 1244.02 0.00 271.41 73.7 58.5 13.35 1185.60 0.16 280.49 73.7 25.61 1244.01 0.00 271.41 73.7 59.0 15.18 1185.26 0.22 277.27 73.7 25.57 1244.01 0.00 271.41 73.7  


Oconee Nuclear Station                                                                   UFSAR Table 6-35 (Page 15 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 15 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 59.5       19.13     1185.31       0.23   273.50   73.7     25.64   1244.02     0.00       271.41       73.7 60.0       25.72     1184.02       99.31   276.41   73.7     25.82   1243.98     0.00       271.41       73.7 61.0       30.04     1182.83     427.22   276.41   73.7     26.16   1243.96     0.00       271.41       73.7 62.0       31.92     1182.15     831.35   276.41   73.7     27.06   1243.80     0.00       271.41       73.7 63.0       30.90     1182.08     1148.93   276.41   73.7     27.87   1243.49     0.00       271.41       73.7 64.0       30.37     1182.05     1655.04   276.43   73.7     28.48   1243.22     0.00       271.42       73.7 65.0       32.75     1182.00     2211.42   276.44   73.7     29.14   1242.96     0.00       271.42       73.7 66.0       37.71     1181.93     2669.84   276.46   73.7     29.89   1242.70     0.00       271.42       73.7 67.0       43.89     1181.88     3053.06   276.47   73.7     26.48   1242.64     0.00       271.42       73.7 68.0       46.17     1181.94     3056.26   276.46   73.7     24.54   1243.47     0.00       271.42       73.7 69.0       44.31     1182.08     2662.50   276.45   73.7     25.42   1244.21     0.00       271.41       73.7 70.0       42.25     1182.21     2283.35   276.44   73.7     24.27   1244.49     0.00       271.41       73.7 71.0       39.46     1182.33     1940.20   276.43   73.7     24.15   1244.81     0.00       271.41       73.7 72.0       36.35     1182.40     1619.69   276.42   73.7     24.19   1245.02     0.00       271.41       73.7 73.0       34.16     1182.41     1433.50   276.42   73.7     23.40   1245.13     0.00       271.41       73.7 74.0       32.39     1182.37     1420.85   276.42   73.7     15.34   1243.79     0.00       271.38       73.7 75.0       29.01     1182.34     1379.54   276.41   73.7     14.94   1246.29     0.00       271.41       73.7 76.0       25.21     1182.27     1133.99   276.41   73.7     21.09   1248.61     0.00       271.41       73.7 77.0       20.49     1182.07     768.40   276.41   73.7     13.71   1248.25     0.00       271.40       73.7 78.0       13.07     1182.03     327.82   276.40   73.7     8.49   1249.98     0.00       271.40       73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 59.5 19.13 1185.31 0.23 273.50 73.7 25.64 1244.02 0.00 271.41 73.7 60.0 25.72 1184.02 99.31 276.41 73.7 25.82 1243.98 0.00 271.41 73.7 61.0 30.04 1182.83 427.22 276.41 73.7 26.16 1243.96 0.00 271.41 73.7 62.0 31.92 1182.15 831.35 276.41 73.7 27.06 1243.80 0.00 271.41 73.7 63.0 30.90 1182.08 1148.93 276.41 73.7 27.87 1243.49 0.00 271.41 73.7 64.0 30.37 1182.05 1655.04 276.43 73.7 28.48 1243.22 0.00 271.42 73.7 65.0 32.75 1182.00 2211.42 276.44 73.7 29.14 1242.96 0.00 271.42 73.7 66.0 37.71 1181.93 2669.84 276.46 73.7 29.89 1242.70 0.00 271.42 73.7 67.0 43.89 1181.88 3053.06 276.47 73.7 26.48 1242.64 0.00 271.42 73.7 68.0 46.17 1181.94 3056.26 276.46 73.7 24.54 1243.47 0.00 271.42 73.7 69.0 44.31 1182.08 2662.50 276.45 73.7 25.42 1244.21 0.00 271.41 73.7 70.0 42.25 1182.21 2283.35 276.44 73.7 24.27 1244.49 0.00 271.41 73.7 71.0 39.46 1182.33 1940.20 276.43 73.7 24.15 1244.81 0.00 271.41 73.7 72.0 36.35 1182.40 1619.69 276.42 73.7 24.19 1245.02 0.00 271.41 73.7 73.0 34.16 1182.41 1433.50 276.42 73.7 23.40 1245.13 0.00 271.41 73.7 74.0 32.39 1182.37 1420.85 276.42 73.7 15.34 1243.79 0.00 271.38 73.7 75.0 29.01 1182.34 1379.54 276.41 73.7 14.94 1246.29 0.00 271.41 73.7 76.0 25.21 1182.27 1133.99 276.41 73.7 21.09 1248.61 0.00 271.41 73.7 77.0 20.49 1182.07 768.40 276.41 73.7 13.71 1248.25 0.00 271.40 73.7 78.0 13.07 1182.03 327.82 276.40 73.7 8.49 1249.98 0.00 271.40 73.7  


Oconee Nuclear Station                                                                   UFSAR Table 6-35 (Page 16 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 16 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 79.0         6.98     1182.44       52.21   276.41   73.7     7.54   1252.99     0.00       271.40       73.7 80.0         7.00     1183.19       4.79   276.36   73.7     10.24   1257.64     0.00       271.40       73.7 81.0       13.08     1183.97       0.48   275.68   73.7     28.12   1253.17     0.00       271.42       73.7 82.0       16.95     1184.69       0.08   281.44   73.7     38.06   1248.07     0.00       271.43       73.7 83.0       16.93     1185.64       0.02   275.00   73.7     32.77   1243.86     0.00       271.42       73.7 84.0       15.74     1186.35       0.00   271.40   73.7     29.90   1243.17     0.00       271.42       73.7 85.0       12.49     1186.69       0.00   271.40   73.7     29.73   1243.22     0.00       271.42       73.7 86.0         9.03     1186.89       0.00   271.39   73.7     30.38   1243.21     0.00       271.42       73.7 87.0         7.06     1187.06       0.00   271.39   73.7     31.34   1243.04     0.00       271.42       73.7 88.0         7.32     1187.16       0.00   271.39   73.7     31.83   1242.80     0.00       271.42       73.7 89.0         8.50     1187.17       0.00   271.39   73.7     33.49   1242.50     0.00       271.42       73.7 90.0         9.96     1187.12       0.00   271.40   73.7     25.08   1242.66     0.00       271.40       73.7 91.0         9.49     1186.28       0.10   279.19   73.7     11.93   1244.52     0.00       271.41       73.7 92.0         6.89     1184.72       0.13   276.00   73.7     6.03   1238.16     0.00       271.40       73.7 93.0         5.98     1184.21       0.04   271.43   73.7     4.40   1229.30     0.00       271.39       73.7 94.0       11.56     1184.14       29.04   276.43   73.7     14.76   1250.61     0.00       271.41       73.7 95.0       20.35     1182.98     457.00   276.41   73.7     23.87   1252.59     0.00       271.41       73.7 96.0       24.11     1182.12     1181.10   276.42   73.7     22.32   1250.36     0.00       271.41       73.7 97.0       26.24     1182.04     1662.26   276.43   73.7     11.46   1247.09     0.00       271.39       73.7 98.0       30.59     1182.00     2074.41   276.44   73.7     2.40   1210.96     0.00       271.41       73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 79.0 6.98 1182.44 52.21 276.41 73.7 7.54 1252.99 0.00 271.40 73.7 80.0 7.00 1183.19 4.79 276.36 73.7 10.24 1257.64 0.00 271.40 73.7 81.0 13.08 1183.97 0.48 275.68 73.7 28.12 1253.17 0.00 271.42 73.7 82.0 16.95 1184.69 0.08 281.44 73.7 38.06 1248.07 0.00 271.43 73.7 83.0 16.93 1185.64 0.02 275.00 73.7 32.77 1243.86 0.00 271.42 73.7 84.0 15.74 1186.35 0.00 271.40 73.7 29.90 1243.17 0.00 271.42 73.7 85.0 12.49 1186.69 0.00 271.40 73.7 29.73 1243.22 0.00 271.42 73.7 86.0 9.03 1186.89 0.00 271.39 73.7 30.38 1243.21 0.00 271.42 73.7 87.0 7.06 1187.06 0.00 271.39 73.7 31.34 1243.04 0.00 271.42 73.7 88.0 7.32 1187.16 0.00 271.39 73.7 31.83 1242.80 0.00 271.42 73.7 89.0 8.50 1187.17 0.00 271.39 73.7 33.49 1242.50 0.00 271.42 73.7 90.0 9.96 1187.12 0.00 271.40 73.7 25.08 1242.66 0.00 271.40 73.7 91.0 9.49 1186.28 0.10 279.19 73.7 11.93 1244.52 0.00 271.41 73.7 92.0 6.89 1184.72 0.13 276.00 73.7 6.03 1238.16 0.00 271.40 73.7 93.0 5.98 1184.21 0.04 271.43 73.7 4.40 1229.30 0.00 271.39 73.7 94.0 11.56 1184.14 29.04 276.43 73.7 14.76 1250.61 0.00 271.41 73.7 95.0 20.35 1182.98 457.00 276.41 73.7 23.87 1252.59 0.00 271.41 73.7 96.0 24.11 1182.12 1181.10 276.42 73.7 22.32 1250.36 0.00 271.41 73.7 97.0 26.24 1182.04 1662.26 276.43 73.7 11.46 1247.09 0.00 271.39 73.7 98.0 30.59 1182.00 2074.41 276.44 73.7 2.40 1210.96 0.00 271.41 73.7  


Oconee Nuclear Station                                                                   UFSAR Table 6-35 (Page 17 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 17 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 99.0       33.02     1182.01     2352.03   276.44   73.7     2.51   1199.28     0.00       271.41       73.7 100.0       34.11     1182.08     2242.85   276.44   73.7     3.16   1199.39     0.00       271.39       73.7 101.0       41.00     1182.01     2530.23   276.45   73.7     2.13   1199.49     0.00       271.41       73.7 102.0       43.05     1182.07     2549.61   276.45   73.7     1.54   1195.93     0.00       271.40       73.7 103.0       40.88     1182.19     2217.35   276.44   73.7     3.94   1201.74     0.00       271.40       73.7 104.0       42.66     1182.17     2200.29   276.44   73.7     8.60   1226.53     0.00       271.40       73.7 105.0       42.50     1182.22     2064.81   276.43   73.7     7.67   1236.21     0.00       271.40       73.7 106.0       39.63     1182.30     1863.45   276.43   73.7     10.23   1248.74     0.00       271.40       73.7 107.0       35.08     1182.36     1655.03   276.42   73.7     19.95   1251.28     0.00       271.41       73.7 108.0       31.95     1182.34     1542.39   276.42   73.7     22.72   1251.14     0.00       271.41       73.7 109.0       30.93     1182.29     1489.64   276.42   73.7     26.43   1248.84     0.00       271.42       73.7 110.0       31.95     1182.24     1542.24   276.42   73.7     29.30   1246.86     0.00       271.42       73.7 111.0       34.72     1182.19     1710.75   276.43   73.7     29.98   1245.53     0.00       271.42       73.7 112.0       38.13     1182.15     1939.91   276.43   73.7     29.70   1244.89     0.00       271.42       73.7 113.0       41.41     1182.12     2170.53   276.44   73.7     29.36   1244.79     0.00       271.41       73.7 114.0       45.61     1182.06     2419.51   276.45   73.7     30.54   1244.69     0.00       271.42       73.7 115.0       47.92     1182.05     2583.92   276.45   73.7     20.10   1243.91     0.00       271.40       73.7 116.0       41.84     1182.20     2215.63   276.44   73.7     10.62   1236.42     0.00       271.40       73.7 117.0       31.86     1182.38     1646.20   276.42   73.7     8.76   1237.16     0.00       271.41       73.7 118.0       21.12     1182.35     1068.09   276.41   73.7     3.06   1247.95     0.00       271.40       73.7 (31 DEC 2003)
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 99.0 33.02 1182.01 2352.03 276.44 73.7 2.51 1199.28 0.00 271.41 73.7 100.0 34.11 1182.08 2242.85 276.44 73.7 3.16 1199.39 0.00 271.39 73.7 101.0 41.00 1182.01 2530.23 276.45 73.7 2.13 1199.49 0.00 271.41 73.7 102.0 43.05 1182.07 2549.61 276.45 73.7 1.54 1195.93 0.00 271.40 73.7 103.0 40.88 1182.19 2217.35 276.44 73.7 3.94 1201.74 0.00 271.40 73.7 104.0 42.66 1182.17 2200.29 276.44 73.7 8.60 1226.53 0.00 271.40 73.7 105.0 42.50 1182.22 2064.81 276.43 73.7 7.67 1236.21 0.00 271.40 73.7 106.0 39.63 1182.30 1863.45 276.43 73.7 10.23 1248.74 0.00 271.40 73.7 107.0 35.08 1182.36 1655.03 276.42 73.7 19.95 1251.28 0.00 271.41 73.7 108.0 31.95 1182.34 1542.39 276.42 73.7 22.72 1251.14 0.00 271.41 73.7 109.0 30.93 1182.29 1489.64 276.42 73.7 26.43 1248.84 0.00 271.42 73.7 110.0 31.95 1182.24 1542.24 276.42 73.7 29.30 1246.86 0.00 271.42 73.7 111.0 34.72 1182.19 1710.75 276.43 73.7 29.98 1245.53 0.00 271.42 73.7 112.0 38.13 1182.15 1939.91 276.43 73.7 29.70 1244.89 0.00 271.42 73.7 113.0 41.41 1182.12 2170.53 276.44 73.7 29.36 1244.79 0.00 271.41 73.7 114.0 45.61 1182.06 2419.51 276.45 73.7 30.54 1244.69 0.00 271.42 73.7 115.0 47.92 1182.05 2583.92 276.45 73.7 20.10 1243.91 0.00 271.40 73.7 116.0 41.84 1182.20 2215.63 276.44 73.7 10.62 1236.42 0.00 271.40 73.7 117.0 31.86 1182.38 1646.20 276.42 73.7 8.76 1237.16 0.00 271.41 73.7 118.0 21.12 1182.35 1068.09 276.41 73.7 3.06 1247.95 0.00 271.40 73.7  


Oconee Nuclear Station                                                                   UFSAR Table 6-35 (Page 18 of 18)
Oconee Nuclear Station UFSAR Table 6-35 (Page 18 of 18)
Reactor Vessel Side                               Steam Generator Side Liquid                                            Liquid Gas Mass        Gas        Mass    Liquid            Gas Mass    Gas        Mass      Liquid Time         Flow      Enthalpy      Flow  Enthalpy  Pressure  Flow    Enthalpy      Flow    Enthalpy      Pressure (seconds)   (lbm/sec)   (Btu/lbm)   (lbm/sec) (Btu/lbm)   (psi) (lbm/sec) (Btu/lbm) (lbm/sec)   (lbm/sec)       (psi) 119.0         7.80     1182.31     382.58   276.41   73.7     1.84   1196.98     0.00       271.40       73.7 120.0         1.89     1182.72       58.32   276.40   73.7     20.89   1228.71     0.00       271.42       73.7 121.0         2.77     1182.88       9.00   276.35   73.7     38.09   1231.78     0.00       271.42       73.7 (31 DEC 2003)}}
(31 DEC 2003)
Reactor Vessel Side Steam Generator Side Time (seconds)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (Btu/lbm)
Pressure (psi)
Gas Mass Flow (lbm/sec)
Gas Enthalpy (Btu/lbm)
Liquid Mass Flow (lbm/sec)
Liquid Enthalpy (lbm/sec)
Pressure (psi) 119.0 7.80 1182.31 382.58 276.41 73.7 1.84 1196.98 0.00 271.40 73.7 120.0 1.89 1182.72 58.32 276.40 73.7 20.89 1228.71 0.00 271.42 73.7 121.0 2.77 1182.88 9.00 276.35 73.7 38.09 1231.78 0.00 271.42 73.7}}

Latest revision as of 20:12, 10 December 2024

8 to Updated Final Safety Analysis Report, Chapter 6, Appendix 6A, Tables
ML20189A084
Person / Time
Site: Oconee  
Issue date: 06/29/2020
From:
Duke Energy Carolinas
To:
Office of Nuclear Reactor Regulation
Shared Package
ML20189A066 List:
References
RA-20-0136
Download: ML20189A084 (122)


Text

Oconee Nuclear Station UFSAR Appendix 6A. Tables Appendix 6A. Tables

Oconee Nuclear Station UFSAR Table 6-1 (Page 1 of 1)

(31 DEC 2000)

Table 6-1. Deleted per 1995 Update

Oconee Nuclear Station UFSAR Table 6-2 (Page 1 of 1)

(31 DEC 2000)

Table 6-2. Deleted per 2000 Update

Oconee Nuclear Station UFSAR Table 6-3 (Page 1 of 2)

(31 DEC 2000)

Table 6-3. Quality Control Standards for Engineered Safeguards Systems Summary of Requirements for Core Flooding Tanks CLASSIFICATION:

ASME III, Class C, Paragraph N-2113 and the requirements of ASME VIII, Paragraph UW-2(a) (lethal substances)

Inspection Requirements Acceptance Standard

1. Inspection of raw materials and review of certificates ASME III material
2. Hydro test ASME III
3. Radiograph ASME VIII Summary of Requirements for Low Pressure Injection Heat Exchanger CLASSIFICATGION: Shell ASME VIII, Tube ASME III, Class C (lethal)

Inspection Requirements Acceptance Standard

1. Inspection of raw materials and review of material certificates ASME II, III, VIII
2. Seal weld on tubes-to-tube sheet TEMA-R-7 and additional requirements
3. Liquid penetrant inspection on tube-to-tube sheet ASME III, N-627 and additional requirements
4. Hydro test ASME III, VIII, TEMA-R
5. Leak test and seal weld (air)

Summary of Requirements for Valves Inspection Requirements Acceptance Standard Class I and II Valves

1. Radiographic inspection of the body casing USAS B31.7
2. Inspection of material and review of material USAS B31.7 certificates
3. Liquids penetrant inspection of the valve body USAS B31.7
4. Hydro test of valve assembly USAS B16.5 and additional requirements
5. Seat Leakage test MSS-SP-61 and additional requirements Class III Valves
1. Inspection of material and review of material USAS B31.7 certificates
2. Hydro test of valve assembly USAS B16.5
3. Seat leakage test MSS-SP-61 and additional requirements In addition to these inspections listed above, all valve materials must meet the ASTM material specification.

Summary of Requirements for Engineered Safeguards Systems Pumps

Oconee Nuclear Station UFSAR Table 6-3 (Page 2 of 2)

(31 DEC 2000)

Inspection Requirements Acceptance Standard

1. Inspection of materials and review of material ASTM certificates
2. Liquid-penetrant inspection of castings ASME VIII
3. Performance test Hydraulic Institute Standard Additional requirements:

Low Pressure Injection Pumps

1. Hydrotest casing to 600 psig. Test pressure is held for 30 minutes per inch of thickness with a minimum holding time of 30 minutes. This exceeds the hydrotest requirements of ASME VIII Paragraph UG-99 (> 1.5 x design pressure).

Reactor Building Spray Pumps

1. Hydrotest casing to 1,200 psig. Test pressure is held for 30 minutes per inch of thickness with a minimum holding time of 30 minutes. This exceeds the hydrotest requirements of ASME VIII Paragraph UG-99 (> 1.5 x design pressure).

High Pressure Injection Pumps

1. Ultrasonic examination of pump barrel.
2. Hydrotest nozzle head and pump barrel to 4,575 psig. Test pressure is held for 30 minutes per inch of thickness with a minimum holding time of 30 minutes. This exceeds the hydrotest requirements of ASME VIII Paragraph UG-99 (> 1.5 x design pressure of 3,050 psig).

Low Pressure Service Water Pumps

1. Documented quality control records and certified caliper measurements of the entire casting thickness will be furnished.
2. Witness performance test will be performed. Acceptance standards are per Hydraulic Institute Standard.
3. A documented, non-witness, hydro-test will be performed. Acceptance standards are per ASME code.

Oconee Nuclear Station UFSAR Table 6-4 (Page 1 of 2)

(31 DEC 2016)

Table 6-4. Engineered Safeguards Piping Design Conditions Temp (F)

Press. (psig)

1.

High Pressure Injection System

a.

From the pump discharge to upstream of the check valves inside the secondary shielding.

200/150 3,040/3120

b.

High pressure injection pump.

200/150 3,040/3,120

c.

From upstream of the check valves to the reactor inlet line.

650 2,500

2.

Low Pressure Injection System

a.

From the borated water storage tank to upstream of the borated water storage tank outlet valves.

150 Static

b.

From upstream of the borated water storage tank outlet valve to upstream of the electric motor operated valves in the borated water feed lines. (Unit 2 only, is to the check valves in the borated water feed lines) 200 100

c.

From upstream of the electric motor operated valves in the borated water feed lines to upstream of the valves at the pump inlets. (Unit 2 only, is from the check valves in the borated water feed lines) 300 200

d.

From upstream of the system inlet valves at the pump inlets to the pump inlet.

Trains 1A, 1C, 2A, 2C 300/250 470/505 Trains 1B, 2B 300 370

e.

From the pump outlet to upstream of the throttle valves at the cooler discharge.

Trains 1A, 1C, 2A, 2C 1 300/250 470/515 Trains 1B, 2B 300 370

f.

From upstream of the throttle valves at the cooler discharge to upstream of the LPI Header isolation valves.

Trains 1A, 2A 300/250 470/515 Trains 1B, 2B 300 470/505

g.

From upstream of the system inlet valves to upstream of the check valves in the core flooding lines.

300 2,500

h.

From upstream of the check valves in the core flooding lines to the reactor vessel.

650 2,500

i.

From the Reactor Building emergency sump to upstream of the valves in the recirculation lines.

300 59

3.

Reactor Building Spray System

Oconee Nuclear Station UFSAR Table 6-4 (Page 2 of 2)

(31 DEC 2016)

Temp (F)

Press. (psig)

a.

From downstream of the pump inlet valves to downstream of the Reactor Building valves.

250 495

b.

From downstream of the inlet valves through the nozzles2.

250/286 200

4.

Low Pressure Service Water System

a.

Condenser circulating water crossover to low pressure service water pump suction.

100 50

b.

Pump discharge 100 100 (OCONEE 3 ONLY)

1.

Low Pressure Injection System

a.

From the borated water storage tank to upstream of the borated water storage tank outlet valves.

150 Static

b.

From upstream of the borated water storage tank outlet valve to upstream of the check valves in the borated water feed lines.

200 100

c.

From upstream of the check valves to upstream of the motor operated valves in the borated water feed lines.

300 300

d.

From upstream of the electric motor operated valves in the borated water feed lines to upstream of the valves at the pump inlets.

300 388

e.

From upstream of the system inlet valves at the pump inlets to upstream of the LPI Header Isolation valves.

300/250 470/505

f.

From upstream of the system inlet valves to upstream of the check valves in the core flooding lines.

300 2,500

g.

From upstream of the check valves in the core flooding lines to the reactor vessel.

650 2,500

h.

From the Reactor Building emergency sump to upstream of the valves in the recirculation lines.

300 59 Note:

1. For the C Train Connection to the B Train Cooler, design conditions are 300°F and 370 psig beginning downstream of the cross over valve.
2. A 286 F design temperature is applicable due to the Post-LOCA and Post-MSLB environmental temperature inside containment. All other plant conditions that require integrity of this pipe are enveloped by the 250 F design temperature.

Oconee Nuclear Station UFSAR Table 6-5 (Page 1 of 1)

(31 DEC 2000)

Table 6-5. Single Failure Analysis Reactor Building Spray System Component Malfunction Comments

1.

Reactor Building the spray pump.

Fails to start.

Since each of the two strings of Reactor Building Spray System is equally sized, the remaining string will provide heat removal capability at a reduced rate. In combination with the Reactor Building Cooling System, heat removal capability in excess of the requirements will be provided.

2.

Building isolation valve.

Fails to open.

(Same as above.)

3.

Check valve in suction or discharge line.

Fails to open.

(Same as above.)

Oconee Nuclear Station UFSAR Table 6-6 (Page 1 of 1)

(31 DEC 2000)

Table 6-6. Single Failure Analysis For Reactor Building Cooling System Component Malfunction Comments

1.

Circulating fan Fails to operate.

The cooling capacity of the cooling units is reduced; however, 2 of 3 cooling units provide the required cooling.

2.

Cooler service water outlet valve.

(LPSW-18, -21, -24)

Fails to open fully Valve will normally be partially open. If the valve fails to open fully, the unit will operate under reduced heat removal capability. The required cooling load will be met by 2 of 3 cooling units.

3.

Cooler service water inlet valve. (LPSW-16, -19, -22)

Inadvertently left closed.

The flow through this string will be unavailable for cooling. It is unlikely that this condition would occur during an accident since the position and flow are monitored during normal operation. The required cooling load will be met by 2 of 3 cooling units.

4.

Service water pump (1A, 1B, 1C).

Fails to operate.

The two remaining pumps will provide full low pressure service water flow to all components.

5.

Service water pump (3A, 3B).

Fails to operate.

The one remaining pump will provide full low pressure service water flow to all components.

Oconee Nuclear Station UFSAR Table 6-7 (Page 1 of 7)

(31 DEC 2014)

Table 6-7. Reactor Building Penetration Valve Information Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc 1(16)

Pressurizer Sample 1

2 3/4 SH EMO ES OP AI CL YES 1

1/2 SH AIR ES OP CL CL YES 2

OTSG A Sample 8

Closed Loop Inside Containment 1

1/2 SH AIR ES CL CL CL YES 3

Component Cooling Inlet 3

1 6

CK OP CL NO 1

6 CK OP CL NO 4

OTSG B Drain 7

Closed Loop Inside Containment 1

4 SH EMO ES OP AI CL YES 5A RB Normal Sump Drain 24 None 5

1 SH MAN CL CL NO 1

2 SH EMO ES OP AI CL YES 1

2 SH AIR ES OP CL CL YES 5B Post Accident Liquid Sample 13 None 2(5) 1 SH SOL(5)

CL CL(5)

CL(15)

YES(5) 6 RC Letdown 1

2 2

SH EMO ES OP AI CL YES 1

2 SH AIR ES OP CL CL YES 7

RC Pump Seal Return 4

1 3,4(7)

SH EMO ES OP AI CL YES 1

2 SH AIR ES OP OP(1)

CL YES 8A Pressurizer Aux Spray 3

1 1,11/2(11)

CK OP CL NO 1

1,11/2(11)

CK OP CL NO 8B Loop A Nozzle Warming 3

1 1,11/2(11)

CK OP CL NO 1

1,11/2(11)

CK OP CL NO 9

HP Injection Loop A 2

1 4

CK OP OP NO None 10A RC Pump Seal Injection 3

1 1

CK OP CL NO 1

1,11/2(6)

CK OP CL NO 10B RC Pump Seal Injection 3

1 1

CK OP CL NO 1

1 CK OP CL NO

Oconee Nuclear Station UFSAR Table 6-7 (Page 2 of 7)

(31 DEC 2014)

Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc 11 Fuel Transfer Tube 19 Special Closure (Flange)

None 1

3 SH EMO CL AL CL YES 1

4 SH EMO CL AL CL YES 12 Fuel Transfer Tube 18 Special Closure (Flange)

None 1

3 SH EMO CL AL CL YES 1

11/2 SH EMO CL AL CL YES 2

1 SH EMO CL AL CL YES 13 RB Spray Inlet 2

1 8

CK CL OP NO None 14 RB Spray Inlet 2

1 8

CK CL OP NO None 15 LPI Inlet 2

1 10 CK CL OP NO None 16 LPI Inlet 2

1 10 CK CL OP NO None 17 OTSG B EFW Injection 5

Closed Loop Inside Containment None 18 Quench Tank Vent 4

1 2

SH EMO ES OP AI CL YES 1

2 SH AIR ES OP CL CL YES 19 RB Purge Inlet 4

1 48 SH EMO ES CL AI CL YES 1

48 SH AIR ES CL CL CL YES 20 RB Purge Outlet 4

1 48 SH EMO ES CL AI CL YES 1

48 SH AIR ES CL CL CL YES 21 LPSW to RCP Coolers 7

Closed Loop Inside Containment 1

10 SH EMO ES OP AI CL YES 22 LPSW from RCP Coolers 7

Closed Loop Inside Containment 1

10 SH EMO ES OP AI CL YES 23A RC Pump Seal Injection 3

1 1

CK OP CL NO 1

1 CK OP CL NO 23B RC Pump Seal Injection 3

1 1

CK OP CL NO 1

1 CK OP CL NO 24A RB Hydrogen Analyzer 10 None 1

1/2,3/8(12)

SH SOL CL CL CL(2)

YES

Oconee Nuclear Station UFSAR Table 6-7 (Page 3 of 7)

(31 DEC 2014)

Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc 24B RB Hydrogen Analyzer 10 None 1

1/2,3/8(12)

SH SOL CL CL CL(2)

YES 25 OTSG B Feedwater Line 6

Closed Loop Inside Containment 1

24 CK OP CL NO 26 OTSG A Main Stream Line 5

Closed Loop Inside Containment None 27 OTSG A Feedwater Line 6

Closed Loop Inside Containment 1

24 CK OP CL NO 28(20)

OTSG B Main Steam Line 5

Closed Loop Inside Containment None 29 Quench Tank Drain 4

1 4

SH EMO ES OP AI CL YES 1

2 SH AIR ES OP CL CL YES 30 LPSW to RBCU 5

Closed Loop Inside Containment None 31 LPSW to RBCU 5

Closed Loop Inside Containment None 32 LPSW to RBCU 5

Closed Loop Inside Containment None 33 LPSW from RBCU 5

Closed Loop Inside Containment None 34 LPSW from RBCU 5

Closed Loop Inside Containment None 35 LPSW from RBCU 5

Closed Loop Inside Containment None 36 RB Emergency Sump Recirc 12 None 1

14 SH EMO CL AI OP YES 37 RB Emergency Sump Recirc 15 None 1

14 SH EMO CL AI OP YES 1

1 SH MAN CL OP NO 38 Quench Tank Cooler Inlet 3

1 11/2 CK OP CL NO 1

11/2,2(9)

CK OP CL NO 39a(17)

Core Flood 16 1

1 SH MAN CL CL NO 2

1 SH MAN CL CL NO

Oconee Nuclear Station UFSAR Table 6-7 (Page 4 of 7)

(31 DEC 2014)

Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc Tank Vent 39b HP Nitrogen Supply 20 1

1 CK CL CL NO 1

1/2 SH MAN CL CL NO 1

1 CK CL CL NO 1

1 SH MAN CL CL NO 40 RB Emergency Sump Drain 14 None 1

2 SH MAN CL CL NO 2

2 CK CL OP NO 2

3/4 SH MAN CL CL NO 41 Instrument Air Supply 9

1 3

SH MAN CL CL NO 1

3 SH MAN CL CL NO 42A RB Hydrogen Analyzer 10 None 1

1/2,3/8(12)

SH SOL CL CL CL(2)

YES 42B RB Hydrogen Analyzer 10 None 1

1/2,3/8(12)

SH SOL CL CL CL(2)

YES 43 OTSG A Drain 7

Closed Loop Inside Containment 1

4 SH EMO ES OP AI CL YES 44 Component Cooling to CRD 3

1 21/2 CK OP CL NO 1

21/2 CK OP CL NO 45A Leak Rate Test Line 9

1 1/2 SH MAN CL CL NO 1

1/2 SH MAN CK CL NO 45B Leak Rate Test Line 9

1 1/2 SH MAN CL CL NO 1

1/2 SH MAN CL CL NO 45C(17)

Leak Rate Test Line 9

1 1/2 SH MAN CL CL NO 1

1/2 SH MAN CL CL NO 48 Breathing Air Supply to RB 9

1 2

SH MAN CL CL NO 1

2 SH MAN CL CL NO 49(16)

LP Nitrogen Supply to RB 22 1

11/2 CK CL CL NO 2

1 SH MAN CL CL NO 50 OTSG A EFW Injection 5

Closed Loop Inside Containment None 51 LRT Supply 11 Special Closure (Flange) 1 8

SH AIR CL AI CL NO

Oconee Nuclear Station UFSAR Table 6-7 (Page 5 of 7)

(31 DEC 2014)

Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc and Exhaust 1

1/2,(10)

SH MAN CL CL NO 52 HP Injection B Loop 2

1 4

CK CL OP NO None 53A HP Nitrogen to CFT 20 1

1 CK CL CL NO 1

1/2, 1(8)

SH MAN CL CL NO 1

1 SH MAN CL CL NO 1

1 CK CL CL NO 53B(17)

LP Nitrogen Supply to RB 21 1

11/2 CK CL CL NO 1

2 SH MAN CL CL NO 54 Component Cooling Outlet 4

1 8

SH EMO ES OP AI CL YES 1

8 SH AIR ES OP OP(1)

CL YES 55 Demin Water Supply 9

1 4

SH MAN CL CL NO 1

4 SH MAN CL CL NO 56 Spent Fuel Canal Fill/Drain 9

1 8

SH MAN CL CL NO 1

8 SH MAN CL CL NO 57(16)

DHR Return Line 28 1

12 SH EMO CL AI CL14 YES None 1

10 SH MAN CL CL NO 1

8 SH EMO CL AI CL14 YES 58A(17)

Pressurizer Sample Line 1

2 3/4 1(13)

SH EMO ES OP AI CL YES 1

1/2 SH AIR ES OP CL CL YES 58B OTSG B Sample 8

Closed Loop Inside Containment 1

1/2 SH AIR ES CL CL CL YES 59 Core Flood Tank Sample 17

`2 1

SH EMO CL AI CL YES 2

1 SH MAN CL CL NO 60 RB Sample Line (Outlet) 23 1

2 SH EMO ES OP AI CL YES 1

2 SH AIR ES OP OP1 CL YES 1

2,3(4)

SH EMO CL AI CL YES 1

1/2, 1(3)

SH MAN CL CL NO 61 RB Sample Line (Intlet) 25 1

2 SH EMO ES OP AI CL YES 1

2 SH AIR ES OP OP1 CL YES 1

2 SH EMO CL AI CL YES

Oconee Nuclear Station UFSAR Table 6-7 (Page 6 of 7)

(31 DEC 2014)

Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc 62(17)

DHR Return Line 29 1

12 SH EMO CL AI CL(14)

YES None 1

10 SH MAN CL CL NO 63 LPSW RBACs Supply 27 None 2

6 SH AIR ES OP CL CL YES 64 LPSW RBACs Return 27 None 2

6 SH AIR ES OP CL CL YES REACTOR BUILDING PENETRATION VALVE INFORMATION LEGEND 7 NOTES LEGEND Valve Arrgt - Refer to Figure 6-9.

Qty - Quantity of comparable penetration valves shown Type - Valve types:

SH (Shut Off Valve) - gate, globe, ball, plug, butterfly, diaphragm or other type on/off valve with the ability to shut off flow.

CK (Check Valve) - stop check, swing check, tilting disc check, lift check, or other type of check valve whose function is to prevent flow in the reverse direction.

Size - Valve size in inches Oper - Valve operator types MAN - manual EMO - electric motor operator AIR - diaphragm operator HYD - hydraulic operator SOL - solenoid Signal - Noted "ES" if the valve receives an Engineered Safeguards signal. Refer to Section 7.3 for further discussion of ES signals.

Valve Positions - Norm: position during normal operation, Fail: position without operator motive force, Post Acc: desired post-accident position OP - Open CL - Closed AI - As Is Indication - remove valve position indication

Oconee Nuclear Station UFSAR Table 6-7 (Page 7 of 7)

(31 DEC 2014)

Pen Description Vlv Arrg Inside Penetration Valve Data Outside Penetration Valve Data Qty Size Type Oper Signal Valve Position Indi-cation Qty Size Type Oper Signal Valve Position Indi-cation Norm Fail Post Acc Norm Fail Post Acc Notes:

1.

Penetrations 7, 54, 60, and 61 outboard isolation valves fail open on loss of ES power to their associated solenoid valves provided air is available to open the valves. With ES power energizing the solenoid valves, the isolation valves close with or without supply air.

2.

Although initially closed for Reactor Building isolation, valves associated with penetrations 24 and 42 can be opened for post-accident hydrogen monitoring.

3.

For Penetration 60, the Unit 3 outside, manual penetration valve is 1/2 inch while the Unit 1 and Unit 2 outside, manual penetration valve is 1 inch.z

4.

For Penetration 60, the Unit 3 inside, non-ES actuated penetration valve is 3 inch while the Unit 1 and Unit 2 inside, non-ES actuated penetration valve is 2 inch.

5.

For Penetration 5b, there are two outside penetration solenoid valves for Units 1 and 2. There are two outside penetration manually operated valves for Unit 3. Only the solenoid valves on Units 1 & 2 fail closed and have remote position indication.

6.

For Penetration 10a, the Unit 2 outside penetration valve is 1.5 inches while the Unit 1 & 3 outside penetration valves are 1 inch.

7.

For Penetration 7, the Unit 2 inside penetration valve is 3 inch while the Unit 1 and Unit 3 inside penetration valves are 4 inch.

8.

For Penetration 53a, the Unit 1 outside penetration valve is 1 inch while the Unit 2 and Unit 3 outside penetration valves are 1/2 inch.

9.

For Penetration 38, the Unit 1 outside penetration valve is 1.5 inches while the Unit 2 and Unit 3 outside penetration valves are 2 inches.

10. For Penetration 51, the Unit 1 outside penetration valve is 1 inch while the Unit 2 and Unit 3 outside penetration valves are 1/2 inch.
11. For Penetration 8a & 8b, the Unit 1 inside and outside penetration valve sizes are 1.5 inches. The Units 2 and 3 inside and outside penetration valve sizes are 1 inch.
12. For Penetration 24 & 42, the Unit 1 and 3 outside penetration valve sizes are 1/2 inch while the Unit 2 outside penetration valve sizes are 3/8 inch.
13. For Penetration 58a, the two Unit 2 inside penetration valve sizes are 1 inch while the two Unit 3 inside penetration valve sizes are 3/4 inch and 1 inch.
14. Although initially closed for Reactor Building isolation, valves associated with penetrations 57 and 62 (DHR Drop Line) can be opened for post-accident boron dilution.
15. Although initially closed for Reactor Building isolation, valves associated with penetration 5b may be opened post-accident for post accident liquid samples (PALS).
16. Penetration number applies to Unit 1 only.
17. Penetration number applies to Unit 2 and Unit 3 only.
18. Deleted per 2005 Update.
19. Deleted per 2005 Update.
20. For Penetration 28, the OTSG B Main Steam Line piping exits the Reactor Building to the yard.

Oconee Nuclear Station UFSAR Table 6-8 (Page 1 of 2)

(31 DEC 2005)

Table 6-8. High Pressure Injection System Component Data High Pressure Injection Pump Type Vertical, multistage, centrifugal, mechanical seal Capacity, gal/min (See Figure 6-16)

Head, ft H20 (at sp. gr. = 1)

(See Figure 6-16)

Motor Horsepower, nameplate hp 600 Pump Material SS wetted parts Design Pressure, psig 3,040/3,120 Design Temperature, F 200/150 Letdown Cooler Type Shell and spiral tube Heat Transferred, Btu/hr 16.0 x 106 Letdown Flow, lb/hr 3.5 x 104 Letdown Cooler lnlet/Outlet Temperature, F 555/120 Material, shell/tube CS/SS Design Pressure, psig 2,500 Design Temperature, F 600 Component Cooling Water Flow (ea.), lb/hr 2 x 105 Code ASME Sec. III-C & VIII Reactor Coolant Pump Seal Return Cooler Type Shell and tube Heat Transferred, Btu/hr 2.2 x 106 Seal Return Flow, lb/hr 1.25 x 105 Seal Return Temperature Change, F 145 - 127 Material, shell/tube SS/SS Design Pressure, psig 150 Design Temperature, F 286 (Unit 1), 200 (Units 2&3)

Recirculated Cooling Water Flow (ea.), lb/hr 1.25 x 105 Code ASME Sec. III-C & VIII Letdown Storage Tank Volume, ft3 600 Design Pressure, psig 100 Design Temperature, F 200

Oconee Nuclear Station UFSAR Table 6-8 (Page 2 of 2)

(31 DEC 2005)

Material SS Code ASME Sec. III-C Purification Demineralizer Type Mixed bed, boric acid saturated Material SS Resin Volume, ft3 50 Flow, gal/min 70 Vessel Design Pressure, psig 150 Vessel Design Temperature, F 200 Code ASME Sec. III-C Letdown Filter Design Flow Rate, gal/min 80 Material SS Design Temperature 200 Design Pressure 150 Code ASME Sec. III-C

Oconee Nuclear Station UFSAR Table 6-9 (Page 1 of 1)

(31 DEC 2009)

Table 6-9. Low Pressure Injection System Component Data Pump (each)

Type Single stage, centrifugal Capacity, gpm 3,000 Head at Rated Capacity, ft H20 350 Motor Horsepower, hp 400 Material SS (wetted parts)

Design Pressure, psig 560/580 Design Temperature, F 300/250 Cooler (each)

Type Shell and tube Capacity (at 140 F), Btu/hr 60 x 106 Reactor Coolant Flow, gal/min 6,000 Low Pressure Service Water Flow, gal/min 6,000 Low Pressure Service Water lnlet Temp, F 75 Material, Shell/Tube CS/SS Design Pressure, Shell 150 Design Pressure, Tube 515(1)/370(2) (470/505 for Unit 3 only)

Design Temperature, F 250(1)/300(2) (300/250 for Unit 3 only)

Code ASME Section III-C, III and VIII Borated Water Storage Tank (each)

Capacity, gal 388,000 Material CS/Coated inside Design Pressure Vessel Full plus 10 ft Hydro Head Design Temperature, F 150 Code AWWA D-100 Note:

1. A Cooler Units 1 & 2
2. B Cooler Units 1 & 2

Oconee Nuclear Station UFSAR Table 6-10 (Page 1 of 1)

(31 DEC 2000)

Table 6-10. Core Flooding System Components Data Core Flooding Tanks Number 2

Design Pressure, psig 700 Operating Pressure, psig 600 Minimum Pressure, psig 575 Design Temperature, F 300 Operating Temperature, F 110 Total Volume, ft3 1,410 Normal Water Volume, ft3 1,040 Minimum Water Volume, ft3 1,010 Material of Construction Carbon steel lined with SS Check Valves Number per Flood Line 2

Size, in.

14 Material 316 SS Design Pressure, psig 2,500 Design Temperature Valve nearest reactor, F 650 Valve nearest tank, F 300 Isolation Valves Number per Flood Line 1

Size, in.

14 Material 304 SS Design Pressure, psig 2,500 Design Temperature, F 300 Piping Reactor to First Check Valve First Check Valve to Isolation Valve Isolation Valve to Tank Size, in.

14 14 14 Material 316 SS 304 SS 304 SS Design Pressure, psig 2,500 2,500 700 Design Temperature, F 650 300 300

Oconee Nuclear Station UFSAR Table 6-11 (Page 1 of 2)

(31 DEC 2005)

Table 6-11. Single Failure Analysis - Emergency Core Cooling System Component Malfunction Comments A.

High Pressure Injection System

1.

Suction valve for high pressure injection pump from borated water storage tank.

Fails to open.

The parallel valve will supply the required flow to one pump string.

2.

High pressure injection valve Fails to open.

The alternate line and the two cross connect lines will provide the total required flow.

3.

High pressure injection pump (operating).

Fails (stops).

Two backup pumps are available to deliver the flow.

4.

High pressure injection pump.

Fails to start.

Two backup pumps are available to deliver the flow.

5.

Seal return line isolation valve.

Fails to close on ES signal.

The other isolation valve will close eliminating this fluid path.

6.

Letdown cooler isolation valve.

Fails to close on ES signal.

The other isolation valve will close the flow path.

7.

LDST-RBES return line isolation valve Fails to open.

The other isolation valve will provide a LDST-RBES return flow path.

B.

Low Pressure Injection System

1.

Low pressure injection pump.

Fails to start.

Adequate injection is provided by the other pump.

2.

Low pressure injection isolation valve.

Fails to open.

Other line admits necessary flow through both injection headers via the passive cross-over line.

3.

Valve in suction line from the Reactor Coolant System Fails to open.

Drain line upstream of the first isolation valve opens admitting flow to the emergency sump. The LPI System then operates in the recirculation mode.

4.

LPI Cooler isolation valve (LPSW-4, -5)

Fails to open.

Other LPSW train admits necessary flow.

5.

Service water pump - 1A, 1B, 1C Fails to operate The two remaining pumps will provide full low pressure service water flow to all components.

Oconee Nuclear Station UFSAR Table 6-11 (Page 2 of 2)

(31 DEC 2005)

Component Malfunction Comments

6.

Service water pump - 3A, 3B Fails to operate The one remaining pump will provide full low pressure service water flow to all components.

(RECIRCULATION FROM REACTOR BUILDING EMERGENCY SUMP)

1.

Valve in suction line from emergency sump.

Fails to open.

Other line admits necessary flow.

2.

Valve in suction line from BWST.

Fails to close after initiating recirculation.

Check valve prevents flow into BWST.

3.

Low pressure injection pump.

Loss of pump.

Reactor core protection will be maintained by alternate pump and low pressure injection string.

4.

Valve in post accident boron dilution flow path from reactor outlet to emergency sump.

Fails to open Redundant post accident boron dilution path admits necessary flow.

C.

Core Flooding System

1.

Isolation valve in discharge line.

Closes during normal operation.

If the valve cannot be manually opened, the reactor must shut down or operations limited as specified in Technical Specifications.

2.

Tank relief valve.

Opens during normal operation.

Loss of nitrogen pressure and consequent loss of ability of tank to perform. Reactor must be shut down or operations adjusted to Technical Specification limits and relief valve must be repaired.

3.

Check valves in charge line.

Excessive leak detected during normal reactor operation.

It is extremely unlikely that both check valves would permit excessive leakage.

Leakage would be indicated by core flooding tank pressure and level changes. If leakage becomes progressively worse or is unacceptably high, reactor must be shut down while the check valves are repaired.

Oconee Nuclear Station UFSAR Table 6-12 (Page 1 of 1)

(31 DEC 2000)

Table 6-12. Oconee Nuclear Station Analysis of Valve Motors Which May Become Submerged Following A LOCA No.

Valve Identification Description Evaluation 1CF-1 2CF-1 3CF-1 "A" Core Flood Tank Discharge Valve No effect on ECCS capability or containment integrity. Valve is locked open during operation and is not operated subsequent to a LOCA. Valve is not a containment isolation valve.

1CS-51 2CS-51 3CS-51 Reactor Building Isolation Valve for Quench Tank Drain No effect on ECCS capability or containment integrity. Valve is normally closed. Redundant isolation valve on outside of containment is not affected.

1HP-1 2HP-1 3HP-1 Reactor Coolant Inlet to "A" Letdown Cooler No effect on ECCS capability or containment integrity. Letdown coolers are not used following a LOCA. Valve is not a containment isolation valve.

1HP-2 2HP-2 3HP-2 Reactor Coolant Inlet to "B" Letdown Cooler No effect on ECCS capability or containment integrity. Letdown coolers are not used following a LOCA. Valve is not a containment isolation valve.

1HP-31 2HP-31 3HP-31 Reactor Coolant Outlet from "A" Letdown Cooler and Reactor Building Isolation Valve No effect on ECCS capability or containment integrity. Letdown coolers are not used following a LOCA. Redundant isolation valve on outside of containment is not affected.

1HP-41 2HP-41 3HP-41 Reactor Coolant Outlet from "B" Letdown Cooler and Reactor Building Isolation Valve No effect on ECCS capability or containment integrity. Letdown coolers are not used following a LOCA. Redundant isolation valve on outside of containment is not affected.

1CC-1 2CC-1 3CC-1 Component Cooling Water Inlet to "A" Letdown Coolers No effect on ECCS capability or containment integrity. Letdown coolers are not used following a LOCA. Valve is not a containment isolation valve.

1CC-2 2CC-2 3CC-2 Component Cooling Water Inlet to "B" Letdown Coolers No effect on ECCS capability or containment integrity. Letdown coolers are not used following a LOCA. Valve is not a containment isolation valve.

Note:

1. Valve is an ES valve and would shut upon ES actuation before becoming submerged.

Oconee Nuclear Station UFSAR Table 6-13 (Page 1 of 1)

(31 DEC 2000)

Table 6-13. Equipment Operational During An Accident and Located Outside Containment 4160 Volt Station Auxiliary Switchgear 600 Volt Load Centers 600 Volt and 208 Volt Motor Control Center Batteries Chargers and Inverters Panelboards Low Pressure Injection Pump Motors High Pressure Injection Pump Motors Reactor Building Spray Pump Motors Low Pressure Service Water Pump Motors Cables

Oconee Nuclear Station UFSAR Table 6-14 (Page 1 of 2)

(31 DEC 2000)

Table 6-14. Equipment Operational During an Accident and Located Within the Containment Equipment Accident Environmental Tests Reactor Building Cooling Fans and Motors After preaging a prototype motor for an extrapolated 40 years insulation life and Fan testing it for operation under seismic conditions, the motor and fan assembly was placed in a pressure vessel. Steam is then injected into the chamber to a pressure of 70 to 80 psia and chemicals similar to those used in the spray system are introduced. The pressure cycle is repeated four additional times and then pressure is reduced to the level to be expected following the accident. The motor then is run continuously for a minimum of 7 days in the test chamber.

Cables Representative samples of preaged cables are tested under high pressure, temperature and humidity conditions equal to or exceeding those specified for the LOCA. These cables are preaged for forty years of radiation and temperature prior to testing.

Valves A typical production valve and actuator was tested as follows under simulated accident conditions. After preaging heat test and shock and vibration tests, the production valve and actuator was subjected to the following environmental tests:

1. Saturated steam at 90 psig for one hour.
2. Boric acid spray for the next two hours at 70 psig followed by a pressure drop to 40 psig with the spray continuing for an additional half hour.
3. Steam pressure was maintained at 40 psig for a period of 11/2 hours followed by a pressure dropoff of 20 psig.
4. Steam pressure was maintained at 20 psig for the remaining nineteen hours of the first day followed by a pressure decrease to 10 psig.
5. Steam pressure at 10 psig was then maintained for six days yielding a total test time of seven days.
6. Valve operation was conducted at the beginning and the end of each level of pressure in 1, 2, 3, 4, and 5 above.

Electrical Penetrations Qualification tests have been performed on one production assembly of each type that is required to function during or following the loss-of-coolant accident to verify its functional capability. The interior end of the penetration assemblies were subjected to the following emergency conditions at 100 percent relative humidity in an autoclave built to duplicate Oconee Reactor Building concrete and nozzle design.

1. First fifteen minutes:

Pressure of 65 psig at a temperature of 300 F

° Rise time for normal operating conditions - less than ten seconds.

2. Next forty-five minutes:

Pressure of 40 psig at a temperature of 260 F

°

3. Next twenty-three hours:

Pressure of 35 psig at a temperature of 250 F

° During the environmental tests, functional capability was demonstrated by applying rated current to conductors in series at 600 volts r.m.s. above ground.

The temperature along the nozzle and in the wire bundles was monitored throughout the test. Leak rate was measured and recorded during the test.

Oconee Nuclear Station UFSAR Table 6-14 (Page 2 of 2)

(31 DEC 2000)

Equipment Accident Environmental Tests The following tests were performed before and after the autoclave test:

1. Connector and conductor resistance test. Measured ohmic resistance of each conductor.
2. Dielectric withstand tests.
3. Conductor to ground and conductor to conductor.
4. Insulation resistance. Conductor to ground.
5. Leak rate test.

Reactor Coolant System Pressure Transmitters Reactor coolant pressure transmitters required for use within the Reactor Building following an accident have been conservatively tested under conditions simulating the environment expected after the design base 14.1 ft2 LOCA. The results of these tests show that the transmitters are acceptable for the required functions. A three phase test was performed to simulate the post-LOCA Reactor Building environment. The respective phases are given below:

Phase I - Pre-accident test at the Babcock & Wilcox Nuclear Development Center (NDC) to simulate the environmental dose to the transmitters associated with the 40-year plant design lifetime.

Phase II - Environmental autoclave test at Franklin Institute Research Laboratory to simulate the Reactor Building pressure and temperature history for a LOCA.

Phase III - Post-accident test at NDC to simulate the maximum expected dose to the transmitters after an LOCA.

Phase I consisted of irradiating the transmitters while the units were in a nonoperating mode. The transmitters were placed in a sealed aluminum box with two dosimeters attachment to each transmitter and positioned over two reactor fuel elements in the NDC storage pool.

Phase II consisted of exposing the transmitters in the operating mode to a steam environment in a test autoclave for 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />. The units were supplied with a constant input of approximately 2/3 of full range and the resultant output/input ratio was measured for the test duration.

Phase III consisted of irradiating the transmitters while the units were in the operating mode in much the same manner as Phase I except that the box was lowered into position beside one fuel element from the reactor. A constant input of approximately 2/3 of full range was maintained throughout the test.

The resulting output signal inaccuracies for each test phase were analyzed and found to be acceptable.

Oconee Nuclear Station UFSAR Table 6-15 (Page 1 of 1)

(31 DEC 2005)

Table 6-15. Emergency Core Cooling Systems Performance Testing High Pressure Injection Pumps One of two pumps operates continuously. The other pump will be operated periodically.

High Pressure Injection Line Valves The remotely operated stop valves in each line are opened partially one at a time.

The flow monitors will indicate flow through the lines.

High Pressure Injection Pump Suction Valves The valves are opened and closed individually and console lights monitored to indicate valve position.

Low Pressure Injection Pumps Pumps are used in normal service for shutdown cooling. These pumps are tested singly for operability by opening the borated water storage tank outlet valves and the bypass valves in the borated water storage tank fill line. This allows water to be pumped from the borated water storage tank through each of the injection lines and back to the tank.

Borated Water Storage Tank Outlet Valves The operational readiness of these valves is established in completing the pump operational test discussed above. During this test, each valve is tested separately.

Low Pressure Injection Valves With pumps shut down and borated water storage tank outlet valves closed, these valves can be opened and reclosed by operator action.

Sump Recirculation Suction Valves With low pressure injection pumps shut down, operation of these valves can be checked.

Check Valves in Core Flooding Injection With the reactor shut down, the check valves in each core flood line are checked for operability by closing the isolation valves, reducing the Reactor Coolant System pressure to provide P slightly above the check valve opening pressure, and opening the isolation valves. Check valve operability is shown by tank pressure and level changes.

Oconee Nuclear Station UFSAR Table 6-16 and 6-17 (Page 1 of 1)

(31 DEC 2000)

Table 6-16. Deleted Per 1999 Update Table 6-17. Deleted Per 1999 Update

Oconee Nuclear Station UFSAR Table 6-18 (Page 1 of 1)

(31 DEC 2000)

Table 6-18. Inventory of Iodine Isotopes in Reactor Building (at t = o)

Isotope Initial Inventory Curies/MWt Iodine 131 2.51 x 104 Iodine 132 3.81 x 104 Iodine 133 5.63 x 104 Iodine 134 6.58 x 104 Iodine 135 5.10 x 104

Oconee Nuclear Station UFSAR Table 6-19 (Page 1 of 1)

(31 DEC 2015)

Table 6-19. Deleted Per 2015 Update

Oconee Nuclear Station UFSAR Table 6-20 (Page 1 of 1)

(31 DEC 2000)

Table 6-20. Parameters for Boron Precipitation Analysis Initial Reactor Core Power 2568 MWth Decay Heat 120% of 1971 ANS LPI Flow Rate 402 lbm/sec Core Mixing Mass 60000 lbm LPI Injection Enthalpy 123 Btu/lbm Containment Pressure 25 psia RCS Boron Concentration 2100 ppm BWST Boron Concentration 3000 ppm CFT Boron Concentration 4000 ppm

Oconee Nuclear Station UFSAR Table 6-21 (Page 1 of 1)

(31 DEC 2003)

Table 6-21. Summary of Calculated Containment Pressures and Temperatures for LOCA Cases Description Peak Containment Pressure (psig)

Peak Containment Temperature

(°F)

Time of Peak Pressure (sec)

Blowdown Energy Release (x106Btu)

Hot Leg SG Inlet Cases (14.1 ft2 break size) 100% RTP 56.95 281.68 14.5 316.23 Reduced Tavg 55.27 279.57 15.3 312.37 10°F Tcold 56.62 281.29 13.9 314.59 80% RTP 56.34 280.94 14.2 313.78 60% RTP 55.74 280.19 14.2 311.65 Max ECCS case 56.88 281.45 14.3 315.74 LOOP Case 56.82 281.54 14.2 315.39 Hot Leg RV Outlet Cases (14.1 ft2 break size) 100% RTP 56.69 281.40 13.0 316.56 Cold Leg Pump Discharge Case (8.55 ft2 break size) 100% RTP 52.52 276.00 16.8 313.31 Cold Leg Pump Suction Case (8.55 ft2 break size 100% RTP 53.50 277.31 23.6 303.47

Oconee Nuclear Station UFSAR Table 6-22 (Page 1 of 1)

(31 DEC 2017)

Table 6-22. Containment Response Analyses Initial Conditions General Information External containment design pressure (psid) 3.0 Internal containment design pressure (psig) 59 Containment design temperature (°F)

Containment free volume (ft3) 1,810,000 Containment design leak rate (/1st day at peak accident pressure) 0.2%

Large LOCA Short Term Large LOCA Long-Term Steam Line Break Initial Conditions Reactor power (MWt @ 102% design overpower) 2619 2619 2619 Average reactor coolant temperature (°F) 581 581 581 Containment pressure (psig) 1.2 0

1.5 Containment atmosphere temperature (°F) 80 variable 170 Containment atmosphere relative humidity (%)

0 100 0

Low pressure service water temperature (°F)

N/A variable N/A Borated water temperature (°F)

N/A 115 120 Borated water storage tank level (ft)

N/A 46 N/A Core flood tank volume (both, ft3) 1944 1944 1940

Oconee Nuclear Station UFSAR Table 6-23 (Page 1 of 1)

(31 DEC 2013)

Table 6-23. Containment Structural Heat Sink Data Heat Sink Painted Material Thickness (ft)

Unpainted Metal Thickness Group Unpainted Metal Exposed Surface Area (ft2)

Unpainted Metal Total Mass (lbm)

Total Surface Area (ft2)

Carbon Steel Building Cylinder 0.0208 61,353 Concrete Building Cylinder 3.75 61,353 Carbon Steel Building Dome 0.0208 16,230 Concrete Building Dome 3.25 16,230 Carbon Steel Building Base 0.0208 8890 Concrete Building Base 8.5 8890 Internal Concrete 1.76 66,231 Internal Carbon Steel 0.0316 165,400 Internal Carbon Steel 1

63,727 300,000 63,727 Internal Stainless Steel 2

8628 258,000 8628 Internal Aluminum 1

9892 3828 9892 Internal Copper 4

727 23,268 727

Oconee Nuclear Station UFSAR Table 6-24 (Page 1 of 1)

(31 DEC 2017)

Table 6-24. Accident Chronology for Limiting Break for Equipment Qualification Event Time(seconds)

Beginning of ECCS injection 6.0 Beginning of CFT injection 12.0 Peak containment pressure 20 End of blowdown phase 26.5 Beginning of RB Spray 142 Beginning of RBCU operation 302 Peak containment pressure after blowdown N/A End of core reflood phase 535 Beginning of sump recirculation phase 4529 End of RB Spray/Beginning of re-circ spray 4529 End of S/G energy release N/A Depressurization of containment (1/2 of design pressure) within 2000 seconds (depending on RBCU assumptions)

Oconee Nuclear Station UFSAR Table 6-25 (Page 1 of 1)

(31 DEC 2017)

Table 6-25. Minimum Acceptable Combinations of Containment Heat Removal Equipment Performance Case No.

INPUT ASSUMPTIONS RESULTS LPI Overall Ht Transfer Coeff @250F LPI (Btu/hr-ft2-ºF)

RBCU (MBtu/hr)

LPSW

(ºF)

Rx Bldg Temp

(ºF)

RBS (inj phase)

(gpm)

RBS (recirc phase)

(gpm)

T (1 day)

(ºF)

T (15 days)

(ºF)

H-2-25 250 105.79 90 130 700 900 180.8 140.2

Oconee Nuclear Station UFSAR Table 6-26 (Page 1 of 2)

(31 DEC 2013)

Table 6-26. Engineered Safety Feature Assumptions in Containment Response Analyses Passive safety injection system Full Capacity Large LOCA Short-Term Large LOCA Long-Term Steam Line Break Number of core flood tanks 2

N/A 2

2 Core flood tank pressure setpoint (psig) 600 N/A 655 550 Active safety injection systems Number of HPI lines 2

N/A 1

1 Number of HPI pumps 3

N/A 2

2 HPI flow rate (gpm/pump) 300 N/A variable variable Number of LPI lines 2

N/A 1

1 Number of LPI pumps 3

N/A 1

1 LPI flow rate (gpm/pump) 3000 N/A variable N/A Containment spray system Number of injection spray lines 2

N/A 1

1 Number of injection spray pumps 2

N/A 1

1 Number of injection spray headers 2

N/A 1

1 Injection flow rate (gpm/pump) 700-1200 N/A 700 700 Number of recirculation spray lines 2

N/A 1

N/A Number of recirculation spray pumps 2

N/A 1

N/A Number of recirculation spray headers 2

N/A 1

N/A Recirculation flow rate (gpm/pump) 1000 N/A 900 N/A Containment fan cooler system Number of coolers (RBCUs) 3 N/A 2

2 Air side flow rate per RBCU (cfm) 108,000 N/A 54,000 54,000

Oconee Nuclear Station UFSAR Table 6-26 (Page 2 of 2)

(31 DEC 2013)

Heat removal rate at design temperature (millions of Btu/hr) 80 N/A variable variable Heat Exchangers Full Capacity Large LOCA Short-Term Large LOCA Long-Term Steam Line Break System LPI N/A LPI N/A Type U-tube N/A U-tube N/A Number 2

N/A 1

N/A Heat transfer area (ft2) 3986 N/A 3900 N/A Heat removal rate at design temperature (millions of Btu/hr) 60 N/A variable N/A Recirculation side flow rate (gpm) 6000 N/A 2830 N/A Exterior side flow rate (gpm) 6000 N/A 5000 N/A Source of cooling water LPSW N/A LPSW N/A Cooling begins (sec) not calculated N/A 5467 N/A Deleted row (s) per 2011 update

Oconee Nuclear Station UFSAR Table 6-27 (Page 1 of 1)

(31 DEC 2008)

Table 6-27. Summary of Calculated Containment Pressures and Temperatures for Secondary System Pipe Rupture Cases Break Location Break Size Peak Pressure (psig)

Peak Temperature (F)

Time of Peak Pressure (sec)

Energy Released to Containment up to End of Blowdown (106Btu)

Deleted row(s) per 2008 update S/G outlet 12.6 58.85 464 156 291

Oconee Nuclear Station UFSAR Table 6-28 (Page 1 of 1)

(31 DEC 2000)

Table 6-28. Steam Generator Compartment Pressure Response Flowpath Discharge Coefficients Flow Area (ft2)

Vent Flowpath Location West Compartment East Compartment Discharge Coefficients Top 528 417 (Figure 6-46)

Bottom 522 522 0.85 Cross Compartment 116 116 (Figure 6-47)

Cross Compartment 167 167 0.60 Total 1,333 ft2 1,222 ft2

Oconee Nuclear Station UFSAR Table 6-29 (Page 1 of 15)

(31 DEC 2003)

Table 6-29. Peak Pressure Mass and Energy Release Data Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 0.0 3010.01 1184.97 49671.97 582.17 2193.5 3285.7 1185.3 53516.7 582.0 2194.5 0.1 3292.43 1186.06 48890.57 578.04 1181.629 3595.0 1186.3 50971.8 577.1 1197.0 0.2 3514.61 1187.31 47678.99 574.34 1159.982 3628.0 1188.2 46317.2 572.9 1107.1 0.3 3543.37 1188.18 44653.10 572.03 1110.159 3397.0 1190.1 41300.8 572.3 1029.7 0.4 3630.87 1189.37 40559.81 567.41 1049.93 3693.9 1191.7 35278.7 566.8 976.9 0.5 3635.68 1190.27 38647.09 565.67 1034.564 4278.5 1195.5 31515.0 552.9 936.0 0.6 3648.05 1190.44 38356.02 565.55 1035.154 4962.8 1201.0 30910.8 531.2 856.1 0.7 3669.39 1190.34 38597.74 565.83 1038.666 5331.4 1204.5 29974.4 516.3 804.5 0.8 3718.86 1190.34 38499.13 565.82 1039.054 5240.4 1205.9 28512.6 508.7 755.2 0.9 3792.57 1190.46 38007.04 565.60 1035.513 4979.0 1206.5 27982.4 503.2 731.9 1.0 3894.59 1190.67 37243.49 565.28 1032.616 4666.8 1206.5 28170.5 500.4 718.2 1.1 4040.05 1191.05 36056.67 564.56 1024.747 4338.3 1206.1 28843.6 499.1 714.5 1.2 4207.73 1191.60 34568.39 563.29 1013.115 4009.4 1205.6 29806.0 498.8 716.5 1.3 4365.54 1192.20 33138.08 561.69 1000.073 3717.0 1205.0 30817.1 499.0 720.2 1.4 4993.88 1195.85 32492.03 552.24 989.5376 3479.8 1204.6 31694.5 499.3 723.7 1.5 5680.12 1199.71 30794.20 538.92 875.3103 3300.6 1204.3 32345.0 499.5 726.3 1.6 5890.87 1201.23 29217.68 532.83 910.9592 3181.6 1204.1 32666.4 499.7 728.1 1.7 6230.52 1203.24 28865.65 528.18 886.991 3106.0 1204.0 32723.4 499.8 729.0 1.8 6589.77 1206.18 26964.95 519.59 803.0924 3052.9 1203.9 32680.9 499.6 728.4

Oconee Nuclear Station UFSAR Table 6-29 (Page 2 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 1.9 6793.44 1208.29 24854.61 512.88 762.0923 3020.8 1203.9 32600.2 499.2 726.3 2.0 6987.48 1209.57 23543.95 509.93 757.0142 3010.7 1204.0 32499.2 498.5 722.8 2.1 7049.20 1210.37 22700.01 507.46 732.7446 3020.8 1204.1 32356.9 497.7 717.8 2.2 6982.30 1210.71 22352.82 505.43 722.8103 3050.3 1204.4 32131.9 496.6 711.7 2.3 6929.43 1211.04 21991.46 503.58 712.88 3106.2 1204.6 31730.6 495.4 705.0 2.4 6926.97 1211.55 21424.15 501.60 700.4492 3181.4 1204.9 31161.7 494.3 698.2 2.5 6972.51 1212.27 20638.07 499.39 686.8077 3257.5 1205.1 30565.0 493.1 691.1 2.6 7045.78 1213.19 19690.63 496.92 670.8762 3329.2 1205.4 29990.4 491.9 684.3 2.7 7104.95 1214.14 18744.18 494.28 653.8654 3396.4 1205.7 29409.8 490.6 677.1 2.8 7120.03 1214.90 17983.51 491.78 638.7917 3460.7 1206.0 28798.3 489.2 669.3 2.9 7090.58 1215.41 17449.85 489.58 626.4775 3523.6 1206.3 28153.2 487.6 660.6 3.0 7024.28 1215.70 17117.19 487.66 616.2853 3586.2 1206.7 27480.8 486.0 651.3 3.1 6931.13 1215.78 16983.97 486.12 608.9916 3650.1 1207.0 26806.2 484.1 641.6 3.2 6827.70 1215.69 16999.04 484.98 604.6638 3707.1 1207.4 26140.4 482.1 629.7 3.3 6723.07 1215.54 17071.12 484.04 601.1656 3751.8 1207.7 25494.8 480.1 619.2 3.4 6617.46 1215.36 17164.90 483.17 598.1012 3787.5 1208.0 24906.0 478.3 609.5 3.5 6513.70 1215.16 17283.34 482.42 595.6895 3819.2 1208.3 24363.3 476.7 601.6 3.6 6410.98 1214.94 17419.40 481.73 593.6919 3851.2 1208.6 23822.7 475.1 593.5 3.7 6306.66 1214.70 17580.36 481.12 592.0447 3885.2 1208.9 23248.5 473.4 584.7 3.8 6197.66 1214.45 17746.44 480.48 590.5136 3928.3 1209.2 22613.2 471.6 575.1

Oconee Nuclear Station UFSAR Table 6-29 (Page 3 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 3.9 6091.36 1214.23 17887.72 479.78 588.2765 3975.1 1209.6 21950.0 469.7 565.2 4.0 5999.57 1214.06 17982.71 479.08 586.2639 4013.3 1209.9 21316.9 467.8 555.6 4.1 5919.56 1213.96 17999.05 478.23 582.8126 4041.9 1210.2 20723.0 465.9 546.1 4.2 5850.31 1213.91 17975.75 477.35 578.8416 4063.8 1210.5 20159.5 464.1 536.9 4.3 5785.93 1213.86 17948.31 476.51 575.8641 4081.9 1210.8 19619.1 462.2 527.8 4.4 5719.81 1213.82 17907.76 475.59 571.6936 4097.2 1211.1 19096.9 460.4 519.1 4.5 5657.05 1213.79 17859.65 474.68 567.8912 4109.7 1211.3 18589.4 458.6 510.5 4.6 5601.93 1213.77 17801.33 473.81 564.1906 4120.8 1211.6 18096.4 456.8 501.9 4.7 5556.08 1213.79 17707.59 472.91 560.3049 4130.3 1211.8 17625.7 455.1 493.9 4.8 5521.32 1213.86 17560.69 471.95 555.8145 4135.5 1212.1 17179.0 453.4 486.0 4.9 5497.49 1213.99 17366.12 470.94 550.9728 4136.0 1212.3 16743.6 451.7 478.2 5.0 5479.21 1214.14 17138.19 469.87 545.6119 4135.3 1212.5 16305.3 450.0 470.1 5.1 5461.59 1214.30 16903.19 468.77 540.1775 4138.0 1212.8 15863.6 448.2 462.2 5.2 5458.31 1214.41 16753.36 468.13 534.9559 4144.7 1213.0 15424.4 446.6 454.6 5.3 5452.41 1214.50 16629.87 467.58 537.133 4154.3 1213.3 14993.1 445.0 447.2 5.4 5418.88 1214.63 16392.82 466.31 527.8124 4167.1 1213.5 14579.1 443.5 440.3 5.5 5377.81 1214.79 16119.89 464.77 520.9561 4179.8 1213.8 14186.3 442.0 433.9 5.6 5331.54 1214.88 15926.04 463.43 514.8933 4187.2 1214.0 13802.8 440.6 427.4 5.7 5270.87 1214.87 15832.54 462.28 510.2204 4191.7 1214.2 13411.3 439.1 420.5 5.8 5202.57 1214.79 15800.48 461.26 506.3772 4199.3 1214.5 12999.4 437.5 413.4

Oconee Nuclear Station UFSAR Table 6-29 (Page 4 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 5.9 5136.92 1214.70 15777.82 460.32 502.8705 4214.5 1214.9 12544.7 435.8 406.0 6.0 5084.95 1214.66 15709.59 459.38 499.2031 4227.8 1215.2 12095.1 434.1 398.1 6.1 5058.63 1214.74 15535.22 458.37 494.8307 4233.7 1215.5 11685.9 432.5 391.1 6.2 5061.77 1214.98 15214.89 457.19 488.941 4238.8 1215.8 11282.6 430.9 383.9 6.3 5087.59 1215.37 14763.62 455.79 481.5992 4242.2 1216.2 10887.3 429.3 376.9 6.4 5126.83 1215.87 14229.35 454.24 473.1572 4243.0 1216.5 10506.6 427.7 370.0 6.5 5166.82 1216.43 13671.74 452.60 464.2117 4241.2 1216.8 10139.1 426.1 363.3 6.6 5199.58 1216.96 13143.25 450.96 455.6055 4236.9 1217.0 9782.5 424.5 356.6 6.7 5225.96 1217.46 12655.68 449.39 447.4246 4230.4 1217.3 9435.8 422.9 349.9 6.8 5248.35 1217.96 12194.42 447.88 439.5559 4221.9 1217.6 9097.6 421.3 343.4 6.9 5268.13 1218.45 11744.27 446.39 431.8085 4211.2 1217.9 8767.5 419.7 336.9 7.0 5285.42 1218.94 11299.63 444.91 424.1094 4197.9 1218.1 8446.1 418.1 330.4 7.1 5300.02 1219.44 10861.96 443.41 416.4128 4182.1 1218.4 8134.4 416.5 324.0 7.2 5312.88 1219.96 10430.75 441.92 408.7826 4163.6 1218.7 7835.1 414.9 317.6 7.3 5325.34 1220.51 9998.25 440.43 401.1175 4142.7 1219.0 7549.3 413.3 311.4 7.4 5335.32 1221.08 9568.11 438.92 393.3681 4119.8 1219.2 7275.8 411.7 305.4 7.5 5339.94 1221.65 9151.08 437.39 385.6325 4094.8 1219.5 7015.1 410.1 299.5 7.6 5338.68 1222.21 8748.44 435.83 377.9228 4068.1 1219.7 6768.1 408.5 293.7 7.7 5332.27 1222.75 8363.09 434.27 370.244 4039.8 1219.9 6534.3 406.9 288.1 7.8 5321.04 1223.26 7998.24 432.72 363.0505 4010.1 1220.1 6313.3 405.4 282.8

Oconee Nuclear Station UFSAR Table 6-29 (Page 5 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 7.9 5303.07 1223.73 7652.23 431.15 355.3909 3979.5 1220.3 6103.5 403.9 277.5 8.0 5280.96 1224.18 7327.65 429.60 348.3742 3949.0 1220.4 5902.4 402.4 272.5 8.1 5255.83 1224.61 7021.56 428.07 341.5477 3919.4 1220.6 5705.6 401.0 267.6 8.2 5222.98 1225.02 6721.74 426.45 334.4929 3888.6 1220.8 5505.3 399.5 262.7 8.3 5178.24 1225.42 6421.44 424.64 326.976 3830.0 1220.8 5307.4 397.5 256.6 8.4 5121.44 1225.79 6125.63 422.63 318.8619 3733.0 1220.5 5167.8 394.9 249.3 8.5 5056.17 1226.14 5837.72 420.50 310.7606 3634.5 1220.1 5061.3 392.4 243.5 8.6 4982.49 1226.47 5555.02 418.23 302.328 3564.0 1220.0 4863.4 390.1 237.0 8.7 4898.50 1226.75 5286.03 415.81 293.5971 3523.9 1220.5 4527.7 387.7 229.0 8.8 4808.09 1226.93 5044.59 413.34 285.3314 3502.3 1221.3 4096.3 385.3 219.9 8.9 4711.35 1227.00 4833.97 410.86 277.262 3479.2 1222.3 3639.8 382.7 210.2 9.0 4606.88 1226.95 4657.63 408.31 269.5202 3436.9 1223.2 3223.6 379.9 200.3 9.1 4500.25 1226.80 4515.59 405.81 262.4702 3367.1 1223.8 2891.7 376.8 190.9 9.2 4393.63 1226.56 4395.57 403.35 255.7832 3271.4 1223.9 2665.5 373.5 182.4 9.3 4285.60 1226.25 4292.05 400.89 249.39 3159.3 1223.5 2537.1 370.1 175.4 9.4 4172.87 1225.85 4206.82 398.35 243.1775 3043.6 1222.8 2464.3 366.8 169.2 9.5 4056.84 1225.37 4138.37 395.77 236.9903 2935.8 1222.0 2423.7 363.8 164.0 9.6 3947.57 1224.86 4087.16 393.33 231.5702 2840.2 1221.2 2389.4 361.1 159.6 9.7 3835.90 1224.30 4041.69 390.82 226.4181 2761.6 1220.7 2326.7 358.6 154.9 9.8 3723.65 1223.79 3970.26 388.15 220.1975 2702.5 1220.5 2239.8 356.6 151.0

Oconee Nuclear Station UFSAR Table 6-29 (Page 6 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 9.9 3637.49 1223.53 3852.26 385.81 214.6207 2655.9 1220.6 2113.9 354.7 146.8 10.0 3574.11 1223.47 3707.97 383.83 209.3918 2612.7 1220.9 1954.7 352.7 141.6 10.1 3516.03 1223.39 3588.09 382.03 204.7022 2568.8 1221.1 1814.3 350.7 137.2 10.2 3453.19 1223.16 3511.79 380.28 200.9402 2529.7 1221.5 1663.8 348.9 132.8 10.3 3387.37 1222.85 3449.77 378.51 197.0519 2502.7 1222.4 1463.3 347.3 127.5 10.4 3332.71 1222.68 3368.08 376.89 193.3959 2478.7 1223.5 1269.5 345.8 122.5 10.5 3291.35 1222.70 3256.39 375.45 189.7945 2451.0 1224.3 1115.5 344.4 118.4 10.6 3252.54 1222.80 3126.88 373.98 185.8833 2433.4 1225.5 959.8 343.3 114.4 10.7 3209.24 1222.88 2997.81 372.40 181.8303 2427.7 1227.2 776.2 342.7 110.4 10.8 3159.90 1222.89 2878.73 370.69 177.7135 2414.3 1229.0 598.8 342.1 105.9 10.9 3102.83 1222.81 2767.53 368.80 173.5954 2375.7 1229.9 481.5 340.7 101.7 11.0 3022.52 1222.51 2652.96 366.29 168.4726 2316.7 1229.9 432.5 338.6 98.3 11.1 2921.69 1222.01 2534.35 363.17 162.1219 2258.8 1229.5 408.8 336.6 95.6 11.2 2841.36 1221.68 2419.12 360.53 156.5801 2215.6 1229.5 367.6 335.1 93.0 11.3 2784.73 1221.45 2336.24 358.61 153.2978 2187.5 1230.1 299.6 334.1 90.4 11.4 2721.38 1221.00 2289.86 356.65 150.1807 2167.0 1231.1 219.2 333.3 87.8 11.5 2647.53 1220.47 2225.48 354.32 146.3128 2139.3 1231.8 148.1 332.4 85.3 11.6 2571.92 1219.92 2152.39 351.83 141.5976 2029.6 1226.9 103.5 328.2 82.5 11.7 2488.89 1219.16 2103.44 349.18 138.5105 1909.2 1219.9 86.3 322.5 89.6 11.8 2367.60 1217.94 2038.88 345.28 132.5417 1857.9 1217.9 82.1 320.5 88.9

Oconee Nuclear Station UFSAR Table 6-29 (Page 7 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 11.9 2211.88 1216.15 1985.77 340.13 125.396 1811.1 1216.6 74.3 318.8 88.0 12.0 2080.26 1214.41 1975.41 335.77 120.0252 1755.1 1215.1 62.1 316.7 86.8 12.1 1976.69 1212.96 1984.45 332.23 116.7781 1687.3 1213.3 52.1 314.2 85.5 12.2 1861.60 1211.18 2028.49 328.28 112.3925 1621.1 1211.6 45.5 311.7 84.3 12.3 1741.18 1209.23 2069.41 324.04 108.2196 1572.0 1210.3 41.4 309.9 83.4 12.4 1656.14 1207.86 2074.89 320.78 103.8234 1542.5 1209.5 39.3 308.9 83.0 12.5 1638.77 1207.62 2064.24 319.99 104.8238 1522.9 1209.0 39.2 308.2 82.7 12.6 1615.17 1207.37 2011.97 318.74 101.6428 1501.4 1208.4 43.4 307.4 82.4 12.7 1570.89 1206.86 1922.47 316.35 98.20489 1473.8 1207.6 46.0 306.5 82.1 12.8 1552.09 1206.91 1808.22 314.80 96.26216 1432.9 1206.5 41.1 305.1 81.5 12.9 1513.04 1206.70 1663.76 312.22 91.32984 1391.3 1205.4 34.5 303.6 80.6 13.0 1441.60 1205.89 1529.09 308.12 86.44714 1370.8 1204.9 29.9 302.8 80.4 13.1 1359.13 1204.64 1441.25 303.62 81.8531 1341.3 1204.2 27.2 301.8 80.1 13.2 1285.69 1202.69 1399.98 300.88 81.00603 1261.1 1202.2 24.5 299.1 78.9 13.3 1228.48 1200.84 1361.43 299.37 81.01533 1169.0 1201.0 21.8 296.1 77.8 13.4 1194.66 1200.05 1321.72 297.96 80.41002 1112.3 1201.4 21.8 294.3 77.3 13.5 1163.71 1199.33 1295.32 296.58 79.40754 1078.9 1201.6 26.5 293.4 76.9 13.6 1120.23 1198.26 1262.64 294.55 77.6799 1043.2 1201.0 31.8 292.3 77.1 13.7 1082.17 1197.28 1236.92 293.01 77.24097 985.0 1200.0 32.5 290.7 76.3 13.8 1050.36 1196.44 1226.41 292.06 76.99243 925.1 1199.6 32.2 289.0 75.9

Oconee Nuclear Station UFSAR Table 6-29 (Page 8 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 13.9 1020.71 1195.68 1219.63 291.20 76.7229 886.0 1199.2 39.4 287.9 75.7 14.0 972.68 1194.51 1198.88 289.84 76.36981 866.2 1198.3 55.0 287.5 75.6 14.1 900.88 1192.79 1158.71 287.89 75.62348 862.1 1197.5 70.2 287.4 75.7 14.2 827.53 1191.10 1109.10 286.04 75.25019 857.7 1197.0 76.0 287.3 75.7 14.3 771.08 1189.85 1064.41 284.73 74.94771 825.2 1196.5 70.2 286.5 75.5 14.4 738.42 1189.16 1044.59 284.05 74.85709 764.6 1195.9 62.2 285.0 75.0 14.5 722.98 1188.85 1059.36 283.76 74.9034 700.9 1195.2 61.0 283.5 74.6 14.6 701.42 1188.44 1056.75 283.32 74.7923 638.2 1194.4 63.0 282.2 74.3 14.7 655.77 1187.63 961.10 282.40 74.49541 567.0 1193.5 62.7 281.0 74.4 14.8 585.34 1186.84 825.49 281.11 74.0854 483.4 1192.9 58.9 279.8 73.6 14.9 506.65 1186.41 727.80 279.85 73.87328 366.5 1192.3 49.7 278.4 73.4 15.0 445.48 1186.14 661.92 279.03 73.8341 210.5 1192.0 33.0 277.2 73.6 15.1 411.78 1185.81 619.64 278.64 73.87054 64.4 1192.0 12.5 276.6 73.5 15.2 385.86 1185.49 592.75 278.37 73.83266 1.1 1190.4 1.0 276.2 73.6 15.3 349.27 1185.30 554.67 278.03 73.74274 0.0 100.0 0.0 10.0 73.6 15.4 319.59 1185.20 507.41 277.77 73.76365 0.0 100.0 0.0 10.0 73.6 15.5 325.76 1185.22 498.53 277.98 73.77338 0.0 100.0 0.0 10.0 73.6 15.6 369.42 1184.78 575.30 278.45 74.58835 0.0 100.0 0.0 10.0 73.5 15.7 346.74 1184.61 584.43 278.21 73.66819 0.0 100.0 0.0 10.0 73.5 15.8 262.52 1184.94 466.55 277.51 73.63993 0.0 100.0 0.0 10.0 73.4

Oconee Nuclear Station UFSAR Table 6-29 (Page 9 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 15.9 218.42 1184.87 361.49 277.11 73.67149 0.0 100.0 0.0 10.0 73.3 16.0 222.61 1184.76 320.17 277.10 73.7808 0.0 100.0 0.0 10.0 73.3 16.1 256.26 1184.43 361.74 277.35 73.88752 0.0 100.0 0.0 10.0 73.5 16.2 314.87 1184.32 484.15 278.05 74.00542 0.0 100.0 0.0 10.0 73.5 16.3 399.70 1184.46 651.48 278.87 74.611 0.0 100.0 0.0 10.0 73.6 16.4 424.88 1184.86 697.94 278.89 73.8687 0.0 100.0 0.0 10.0 73.6 16.5 386.37 1185.31 628.68 278.39 73.86523 0.0 100.0 0.0 10.0 73.6 16.6 346.12 1185.35 566.91 278.02 73.71196 0.0 100.0 0.0 10.0 73.5 16.7 322.87 1185.29 517.31 277.81 73.76705 0.0 100.0 0.0 10.0 73.1 16.8 333.86 1185.05 522.15 277.92 73.94365 25.1 1184.8 0.1 275.9 73.8 16.9 347.65 1184.83 558.07 278.03 73.91508 35.5 1184.8 0.4 275.3 73.6 17.0 345.70 1184.89 568.38 277.99 73.85989 10.5 1185.0 0.3 275.0 73.5 17.1 350.61 1185.03 570.27 278.08 73.87688 0.0 100.0 0.0 10.0 73.6 17.2 379.62 1184.96 607.60 278.44 74.09661 0.0 100.0 0.0 10.0 73.8 17.3 404.80 1184.94 647.60 278.66 74.03583 0.0 100.0 0.0 10.0 73.7 17.4 435.72 1185.41 687.07 279.23 74.02745 0.0 100.0 0.0 10.0 73.7 17.5 598.94 1187.92 924.39 282.82 75.58422 18.0 1184.9 0.0 300.0 73.7 17.6 720.00 1188.90 1114.95 284.07 74.80801 96.3 1186.4 1.0 277.4 73.9 17.7 680.45 1188.07 1081.59 282.91 74.60171 83.9 1186.8 1.1 276.9 73.4 17.8 651.61 1187.52 1065.14 282.37 74.85718 52.1 1187.6 0.5 274.3 73.8

Oconee Nuclear Station UFSAR Table 6-29 (Page 10 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 17.9 633.42 1187.19 1015.64 282.03 74.48551 59.0 1187.8 0.6 276.1 73.5 18.0 607.27 1186.78 915.49 281.51 74.38813 12.5 1189.0 0.2 282.2 73.6 18.1 587.60 1186.59 852.64 281.15 74.21064 0.0 100.0 0.0 10.0 73.7 18.2 553.74 1186.32 815.45 280.62 74.19325 0.3 1184.5 0.0 10.0 73.8 18.3 478.24 1186.12 732.12 279.57 73.75981 0.4 1183.7 0.0 10.0 73.6 18.4 429.67 1186.05 664.12 278.92 73.93896 2.3 1184.7 0.0 100.0 73.8 18.5 438.00 1185.61 678.40 279.04 74.11103 2.3 1184.8 0.0 100.0 73.2 18.6 457.94 1185.43 719.11 279.32 74.05242 0.0 100.0 0.0 10.0 71.4 18.7 482.49 1185.54 754.55 279.68 74.06602 0.0 100.0 0.0 10.0 71.3 18.8 504.59 1185.59 780.58 279.95 74.33266 0.0 100.0 0.0 10.0 72.4 18.9 503.49 1185.66 768.14 279.87 74.15369 49.5 1186.1 0.0 300.0 74.0 19.0 476.57 1185.79 724.02 279.47 73.98391 135.2 1189.1 0.1 280.0 73.8 19.1 466.39 1185.81 711.54 279.38 74.10407 161.5 1193.2 0.2 273.5 73.7 19.2 495.61 1185.75 756.43 279.88 74.2496 77.7 1195.9 0.1 280.0 73.5 19.3 525.03 1185.73 791.41 280.25 74.28757 1.9 1197.3 0.0 500.0 73.7 19.4 523.68 1185.85 767.50 280.16 74.18356 0.0 100.0 0.0 10.0 73.6 19.5 522.86 1186.05 749.64 280.17 74.31515 3.3 1186.5 0.0 10.0 73.8 19.6 533.74 1185.99 768.04 280.33 74.43989 3.3 1186.5 0.0 10.0 73.6 19.7 502.24 1185.92 730.49 279.85 73.89213 0.0 100.0 0.0 10.0 73.7 19.8 508.56 1186.34 734.64 280.20 74.19047 11.4 1187.3 0.0 10.0 73.7

Oconee Nuclear Station UFSAR Table 6-29 (Page 11 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 19.9 616.57 1187.48 917.68 282.36 74.8431 64.5 1192.6 0.0 200.0 73.8 20.0 775.01 1190.10 1383.88 285.64 76.28355 28.5 1195.3 0.0 200.0 73.6 20.5 768.54 1189.90 1293.07 285.24 75.66263 6.5 1198.0 0.0 10.0 72.1 21.0 737.11 1189.18 1175.02 284.21 74.90845 70.9 1196.7 0.0 276.0 69.2 21.5 735.01 1189.12 1277.36 284.25 75.24608 80.3 1196.4 0.0 280.0 73.5 22.0 720.92 1188.88 1432.47 284.08 75.57133 9.4 1194.6 0.0 100.0 73.7 22.5 726.28 1189.06 1447.13 284.21 75.18275 61.9 1195.8 0.0 10.0 72.5 23.0 773.58 1189.98 1180.22 284.93 75.54347 73.5 1197.0 0.0 10.0 73.7 23.5 743.87 1189.42 909.58 284.23 74.70858 12.2 1202.9 0.0 10.0 73.7 24.0 653.24 1187.68 951.56 282.29 74.38791 40.8 1196.2 0.0 10.0 73.4 24.5 622.69 1187.07 1153.75 281.98 74.78619 57.5 1198.2 0.0 10.0 73.7 25.0 591.01 1186.75 1165.02 281.47 74.57095 26.6 1201.6 0.0 10.0 73.7 25.5 517.97 1185.79 1246.63 280.26 74.32353 11.5 1197.8 0.0 10.0 73.7 26.0 470.72 1184.94 1528.44 279.77 74.51925 29.9 1203.0 0.0 10.0 73.7 26.5 438.75 1184.57 1620.52 279.41 74.44828 37.2 1204.4 0.0 10.0 73.7 27.0 395.58 1184.51 1391.44 278.83 74.1436 15.0 1205.2 0.0 10.0 73.6 27.5 354.94 1184.46 1206.39 278.25 74.01461 11.1 1205.5 0.0 10.0 73.7 28.0 323.82 1184.30 1180.52 277.94 73.94646 12.2 1205.8 0.0 10.0 73.7 28.5 292.90 1184.23 1080.88 277.65 73.87787 7.0 1205.2 0.0 10.0 73.7 29.0 264.78 1184.22 925.93 277.40 73.82074 0.4 1197.2 0.0 10.0 73.7

Oconee Nuclear Station UFSAR Table 6-29 (Page 12 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 29.5 245.07 1184.19 783.58 277.24 73.79306 0.7 1191.1 0.0 10.0 73.7 30.0 229.02 1184.14 675.89 277.13 73.76751 2.4 1191.5 0.0 10.0 73.7 30.5 213.60 1184.07 602.43 277.03 73.76419 2.1 1191.2 0.0 10.0 73.7 31.0 198.66 1183.96 559.76 276.95 73.75786 0.4 1189.1 0.0 10.0 73.7 31.5 186.45 1183.85 523.38 276.88 73.75477 0.7 1186.9 0.0 10.0 73.7 32.0 177.71 1183.74 519.98 276.84 73.75468 11.1 1197.0 0.0 10.0 73.7 32.5 169.39 1183.59 570.67 276.81 73.75427 28.1 1203.4 0.0 10.0 73.7 33.0 159.81 1183.43 642.99 276.77 73.74869 32.7 1208.1 0.0 10.0 73.7 33.5 151.10 1183.28 707.65 276.75 73.77543 28.2 1206.7 0.0 10.0 73.7 34.0 146.42 1183.16 789.63 276.74 73.76569 13.4 1203.3 0.0 10.0 73.6 34.5 144.36 1183.05 1033.98 276.76 73.78262 0.1 1206.4 0.0 10.0 72.9 35.0 141.69 1182.90 1571.86 276.82 73.81935 6.3 1186.6 0.0 10.0 71.2 35.5 137.42 1182.69 2171.55 276.87 73.89374 41.0 1191.9 0.0 200.0 73.9 36.0 135.44 1182.48 2562.42 276.95 73.96019 53.1 1192.8 0.0 200.0 73.8 36.5 134.63 1182.34 2833.52 277.00 74.03759 24.5 1193.0 0.0 10.0 73.6 37.0 131.47 1182.28 2925.39 276.99 74.02323 27.0 1195.9 0.0 10.0 73.5 37.5 127.70 1182.29 2813.08 276.94 73.99922 22.8 1197.0 0.0 10.0 73.7 38.0 123.37 1182.32 2700.79 276.88 73.9596 2.6 1197.9 0.0 10.0 73.7 38.5 118.40 1182.32 2638.13 276.83 73.92158 11.2 1193.1 0.0 10.0 73.8 39.0 114.06 1182.31 2613.86 276.80 73.92563 16.2 1193.1 0.0 10.0 73.7

Oconee Nuclear Station UFSAR Table 6-29 (Page 13 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 39.5 108.28 1182.30 2554.13 276.70 73.88004 7.8 1192.9 0.0 10.0 73.7 40.0 100.17 1182.31 2396.29 276.57 73.70213 3.1 1192.8 0.0 10.0 73.7 40.5 92.79 1182.32 2230.38 276.51 73.70171 1.8 1191.0 0.0 10.0 73.7 41.0 87.72 1182.29 2155.10 276.49 73.70168 7.2 1195.5 0.0 10.0 73.7 41.5 84.54 1182.24 2182.41 276.49 73.70219 13.5 1199.4 0.0 10.0 73.7 42.0 82.74 1182.21 2261.05 276.48 73.70177 14.1 1203.9 0.0 10.0 73.7 42.5 83.64 1182.15 2397.74 276.49 73.70461 15.0 1206.8 0.0 10.0 73.7 43.0 88.05 1181.99 2703.09 276.51 73.70767 16.8 1208.7 0.0 10.0 73.7 43.5 92.99 1181.86 3081.04 276.53 73.71006 18.3 1210.4 0.0 10.0 73.7 44.0 97.06 1181.81 3345.76 276.55 73.713 19.8 1211.8 0.0 10.0 73.7 44.5 100.77 1181.80 3464.22 276.57 73.71436 20.3 1213.0 0.0 10.0 73.7 45.0 102.87 1181.82 3440.50 276.57 73.71311 20.2 1214.0 0.0 10.0 73.7 45.5 102.00 1181.87 3331.83 276.56 73.70994 20.2 1214.8 0.0 10.0 73.7 46.0 98.34 1181.93 3218.84 276.55 73.70684 21.2 1215.5 0.0 10.0 73.7 46.5 94.03 1181.96 3146.64 276.53 73.70648 23.9 1216.1 0.0 10.0 73.7 47.0 92.13 1181.94 3165.32 276.53 73.70738 27.5 1216.5 0.0 10.0 73.7 47.5 94.10 1181.87 3291.14 276.54 73.71215 29.7 1216.9 0.0 10.0 73.7 48.0 96.45 1181.83 3429.04 276.55 73.71077 26.7 1217.1 0.0 10.0 73.7 48.5 94.99 1181.86 3441.09 276.54 73.7085 25.4 1217.3 0.0 10.0 73.7 49.0 90.01 1181.96 3220.39 276.52 73.70547 25.6 1217.5 0.0 10.0 73.7

Oconee Nuclear Station UFSAR Table 6-29 (Page 14 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 49.5 79.93 1182.12 2782.82 276.49 73.69555 13.3 1217.6 0.0 10.0 73.7 50.0 65.72 1182.28 2336.62 276.46 73.69418 1.5 1217.7 0.0 10.0 73.7 50.5 51.69 1182.43 1936.11 276.44 73.69373 0.0 100.0 0.0 10.0 73.7 51.0 39.33 1182.59 1511.38 276.42 73.69345 0.0 100.0 0.0 10.0 73.7 51.5 31.34 1182.63 1108.77 276.42 73.69723 0.0 100.0 0.0 10.0 73.6 52.0 26.53 1182.53 784.76 276.41 73.6967 0.0 100.0 0.0 10.0 73.6 52.5 21.48 1182.40 524.23 276.40 73.70061 4.4 1188.1 0.0 10.0 73.7 53.0 17.17 1182.48 320.55 276.40 73.69612 4.7 1188.0 0.0 10.0 73.7 53.5 14.90 1182.73 196.09 276.40 73.69675 9.1 1191.8 0.0 10.0 73.7 54.0 14.21 1182.97 107.19 276.41 73.69689 31.5 1198.0 0.0 10.0 73.7 54.5 14.48 1183.19 44.46 276.42 73.6972 54.1 1204.5 0.0 10.0 73.7 55.0 16.08 1183.41 16.26 276.33 73.69724 62.3 1209.8 0.0 10.0 73.7 55.5 22.12 1183.51 19.64 276.40 73.69837 54.2 1213.2 0.0 10.0 73.7 56.0 30.62 1183.12 130.51 276.41 73.69796 41.6 1215.0 0.0 10.0 73.7 56.5 34.60 1182.53 378.40 276.41 73.69784 25.4 1215.8 0.0 10.0 73.7 57.0 33.66 1182.14 581.39 276.41 73.69814 9.4 1216.4 0.0 10.0 73.7 57.5 32.50 1181.98 662.14 276.41 73.6994 8.6 1217.1 0.0 10.0 73.7 58.0 31.96 1181.85 730.39 276.41 73.69713 13.9 1217.5 0.0 10.0 73.7 58.5 29.60 1181.70 720.18 276.41 73.69666 16.6 1217.9 0.0 10.0 73.7 59.0 23.23 1181.54 549.73 276.40 73.69803 18.5 1218.2 0.0 10.0 73.7

Oconee Nuclear Station UFSAR Table 6-29 (Page 15 of 15)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi) 59.5 16.54 1181.55 318.06 276.40 73.6974 15.3 1218.4 0.0 10.0 73.7 60.0 14.63 1182.30 100.15 276.40 73.69705 10.3 1218.8 0.0 10.0 73.7 61.0 14.80 1182.92 27.07 276.41 73.69739 14.4 1219.2 0.0 10.0 73.7 62.0 14.93 1183.46 3.28 276.49 73.69757 26.0 1219.2 0.0 10.0 73.7 63.0 15.01 1183.93 0.42 276.52 73.69798 29.6 1219.0 0.0 10.0 73.7 64.0 14.08 1184.38 0.07 270.27 73.69649 23.7 1218.9 0.0 10.0 73.7 65.0 11.02 1184.53 0.06 277.31 73.6967 21.6 1219.0 0.0 10.0 73.7 66.0 7.83 1184.36 0.05 284.31 73.69694 22.3 1219.1 0.0 10.0 73.7 67.0 8.98 1184.83 0.03 264.15 73.6979 22.8 1219.2 0.0 10.0 73.7 68.0 13.77 1185.80 0.02 258.06 73.69794 24.3 1219.2 0.0 10.0 73.7 69.0 19.57 1185.76 0.82 276.83 73.6981 26.4 1219.1 0.0 10.0 73.7 70.0 22.80 1184.37 36.64 276.41 73.69612 28.4 1219.1 0.0 10.0 73.7 71.0 21.97 1183.10 150.45 276.40 73.69683 29.5 1219.0 0.0 10.0 73.7 71.68426 20.81 1182.71 265.61 276.40 73.69853 29.8 1219.0 0.0 10.0 73.7

Oconee Nuclear Station UFSAR Table 6-30 (Page 1 of 40)

(31 DEC 2003)

Table 6-30. RELAP5 Long-Term Mass and Energy Release Data Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 0.0 2.61 1190.80 45034.67 560.04 2294.67 622.72 1195.07 24082.41 538.81 2296.60 0.00 0.5 1.35 1190.73 45002.73 561.03 1141.73 701.17 1195.39 23503.53 536.92 946.56 0.00 1.0 1.97 1189.03 43883.38 561.31 1112.71 821.86 1195.63 22712.44 535.16 946.49 0.00 1.5 14.86 1188.96 41138.78 560.56 1113.47 940.61 1195.69 22178.90 535.45 952.13 0.00 2.0 50.78 1188.48 37445.88 561.23 1121.34 1048.83 1196.19 20838.21 536.12 928.40 0.00 2.5 131.14 1188.16 33748.12 562.75 1143.21 1085.61 1196.58 19040.70 538.38 895.71 0.00 3.0 295.10 1188.29 31133.46 563.51 1137.55 1165.81 1196.70 17346.79 538.67 874.28 0.00 3.5 499.44 1188.67 29332.74 562.72 1127.36 1339.95 1197.43 15457.64 534.17 837.95 0.00 4.0 702.87 1189.19 27711.68 561.28 1120.62 1789.77 1201.47 13673.54 517.80 797.22 0.00 4.5 973.92 1190.10 25969.13 558.99 1104.83 2328.37 1205.61 11416.29 495.80 685.83 0.00 5.0 1308.56 1191.25 23634.97 556.36 1072.47 2574.99 1207.92 9250.46 482.53 620.76 0.00 5.5 1580.32 1191.83 20906.55 556.08 1032.60 2641.20 1209.04 8241.40 475.89 590.78 0.00 6.0 1802.31 1192.39 18632.19 555.19 1003.97 2628.75 1209.53 7834.36 472.11 577.39 0.00 6.5 2004.58 1193.41 17055.64 550.93 979.81 2676.06 1210.49 7089.30 467.57 557.19 7.51 7.0 2142.47 1194.57 15821.38 545.99 951.27 2816.47 1212.28 5780.78 460.58 509.76 15.21 7.5 2201.87 1195.71 14909.52 540.90 924.81 2904.60 1213.70 4810.09 454.21 479.95 23.09 8.0 2201.25 1196.85 14343.35 535.83 901.26 2906.34 1214.35 4396.83 450.43 464.32 31.11 8.5 2432.66 1200.19 14060.63 524.56 844.18 2868.05 1214.66 4167.69 447.20 451.84 39.38 9.0 2754.27 1203.35 13282.68 512.71 792.59 2818.77 1214.99 3900.91 443.34 435.95 47.90

Oconee Nuclear Station UFSAR Table 6-30 (Page 2 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 9.5 2871.87 1204.91 12016.15 506.08 753.66 2771.95 1215.55 3502.50 438.36 413.89 56.67 10.0 2910.01 1206.30 10930.33 499.17 715.22 2732.74 1216.38 2996.00 432.48 387.73 65.73 10.5 2893.94 1207.56 9959.00 491.68 672.61 2681.48 1217.16 2516.27 426.21 362.25 75.14 11.0 2866.07 1208.79 9014.42 483.96 632.15 2594.28 1217.52 2178.14 419.90 338.86 84.77 11.5 2839.38 1209.99 8060.30 475.90 588.69 2485.06 1217.59 1934.33 413.70 318.78 94.71 12.0 2659.09 1210.53 7615.43 466.52 551.69 2376.03 1217.67 1697.65 407.37 296.84 104.83 12.5 2069.41 1209.75 8732.67 450.07 490.74 2281.22 1217.91 1430.96 401.09 277.06 115.14 13.0 1475.93 1208.24 10159.54 433.27 422.92 2207.90 1218.48 1111.64 394.91 255.52 125.01 13.5 1223.13 1207.47 10460.70 418.41 371.54 2140.84 1219.30 783.30 388.66 234.91 134.01 14.0 1074.33 1206.66 10258.17 404.44 322.90 2054.75 1220.00 502.83 382.03 213.44 143.03 14.5 959.22 1205.72 9831.20 392.62 285.56 1945.08 1220.32 301.89 374.90 194.07 152.06 15.0 825.84 1204.48 9494.08 382.34 261.44 1814.99 1220.50 154.67 368.23 172.93 161.10 15.5 687.19 1202.93 9221.88 372.02 235.30 1648.52 1219.51 91.58 356.60 155.28 170.15 16.0 582.34 1201.44 8886.18 361.07 214.06 1471.92 1217.77 73.06 349.40 136.72 179.21 16.5 522.33 1200.11 8517.77 347.47 201.93 1310.72 1219.71 25.72 342.61 118.47 188.27 17.0 462.30 1198.49 8201.79 333.03 181.54 1140.02 1232.42 2.62 335.89 101.48 197.34 17.5 388.14 1196.14 8086.54 320.25 154.66 982.25 1247.77 0.09 319.35 88.88 206.40 18.0 334.42 1193.50 8097.22 308.14 132.07 856.27 1250.00 0.11 310.19 79.00 215.45 18.5 300.17 1190.66 8172.03 296.34 111.48 745.49 1246.15 0.13 303.05 75.32 224.50 19.0 249.01 1187.99 7975.41 285.43 93.94 648.70 1239.56 0.21 294.81 72.42 233.54

Oconee Nuclear Station UFSAR Table 6-30 (Page 3 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 19.5 171.69 1185.35 7496.61 273.86 88.14 572.76 1221.23 1.02 285.27 70.02 242.58 20.0 125.51 1181.92 7477.24 258.83 68.46 510.71 1203.59 5.30 281.20 68.44 251.61 20.5 85.76 1178.12 7206.32 234.47 58.72 461.12 1198.73 16.35 279.10 67.69 251.64 21.0 41.52 1172.48 6823.43 209.85 43.15 423.82 1195.20 34.96 277.24 67.20 251.67 21.5 24.30 1169.09 6869.18 199.55 37.14 393.55 1190.35 56.72 275.83 66.92 251.68 22.0 16.74 1167.35 6706.53 193.57 35.06 368.52 1186.88 77.95 274.67 66.61 251.69 22.5 13.23 1166.81 6332.16 191.06 33.87 343.15 1185.05 100.84 273.64 66.33 251.70 23.0 11.13 1166.81 5975.03 190.89 35.99 318.22 1184.14 118.38 272.77 66.03 251.72 23.5 8.81 1166.62 5793.32 188.98 33.97 297.75 1183.51 129.30 272.05 65.84 251.73 24.0 6.98 1166.70 5463.94 188.53 33.11 278.42 1182.96 137.99 271.41 65.63 251.74 24.5 6.18 1167.51 5209.50 188.10 33.87 260.48 1182.47 137.95 270.81 65.37 251.75 25.0 8.81 1172.33 5088.87 192.17 34.44 239.74 1182.10 129.04 270.16 65.16 251.77 25.5 13.66 1177.36 5061.48 191.39 49.33 221.36 1181.90 121.85 269.57 64.91 251.77 26.0 13.92 1179.01 4819.75 183.61 49.14 210.18 1182.30 112.02 269.24 64.80 251.79 26.5 12.38 1178.14 4099.11 191.56 55.62 183.79 1184.18 87.49 268.66 64.46 251.81 27.0 9.08 1178.57 3385.51 196.88 54.40 152.31 1187.39 61.24 267.95 64.29 251.80 27.5 4.62 1182.12 2978.50 191.22 56.41 118.94 1190.83 41.35 267.47 64.12 251.83 28.0 1.67 1186.52 1546.48 190.48 62.83 56.84 1193.16 20.05 267.00 63.94 251.86 28.5 0.00 1173.07 97.41 190.70 61.92 8.18 1191.67 4.20 266.56 63.85 251.86 29.0 0.00 1169.54 0.00 261.52 55.11 0.00 1174.65 0.00 261.50 63.81 251.87

Oconee Nuclear Station UFSAR Table 6-30 (Page 4 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 29.5 0.00 1168.90 0.00 261.67 53.33 0.00 1174.36 0.00 261.63 63.35 251.87 30.0 0.00 1169.17 0.00 261.47 54.14 0.00 1174.26 0.00 261.68 63.14 251.87 31 0.00 1167.33 0.00 262.99 49.67 0.00 1173.95 0.00 261.82 62.58 251.89 32 0.00 1168.81 0.00 261.39 52.98 14.15 1207.90 0.04 269.33 62.69 251.87 33 0.00 1172.52 0.00 262.87 60.22 14.24 1207.93 0.04 267.47 63.33 251.85 34 0.00 1169.02 0.00 260.98 53.42 9.28 1202.56 0.02 260.61 62.61 251.87 35 0.00 1170.08 0.00 260.67 55.62 11.91 1199.71 0.02 264.86 62.76 251.86 36 12.25 1202.55 120.64 226.64 56.40 31.16 1216.23 0.04 265.91 62.79 251.86 37 12.81 1201.81 133.73 225.33 62.25 31.38 1219.40 0.05 265.31 62.82 251.86 38 114.71 1187.73 259.64 265.32 63.96 70.37 1251.25 0.03 265.62 63.18 251.82 39 287.46 1190.16 392.15 268.51 64.44 148.11 1233.85 2.85 266.58 62.71 251.80 40 379.29 1189.84 362.22 270.53 64.37 177.09 1205.36 16.57 266.97 62.71 251.80 41 391.99 1187.18 375.78 270.82 65.50 184.09 1191.36 34.19 266.69 62.76 251.78 42 357.15 1185.55 421.36 270.33 63.22 170.81 1187.04 46.01 266.36 62.37 251.81 43 371.22 1186.09 475.78 270.67 67.23 177.56 1184.23 62.23 266.42 62.80 251.78 44 358.14 1185.62 373.60 269.60 63.36 168.68 1183.55 65.23 266.10 62.24 251.80 45 301.98 1183.54 317.79 267.52 62.84 140.01 1184.02 64.73 265.36 62.03 251.81 46 292.95 1183.15 305.97 267.16 62.79 130.70 1182.49 81.70 265.12 61.95 251.81 47 298.85 1183.16 315.79 267.17 62.58 130.47 1181.63 93.87 265.01 61.80 251.82 48 302.29 1183.22 337.72 267.17 62.67 131.96 1181.30 98.58 264.91 61.71 251.81

Oconee Nuclear Station UFSAR Table 6-30 (Page 5 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 49 304.79 1183.28 336.95 267.10 62.59 132.09 1180.90 105.03 264.78 61.60 251.81 50 299.65 1183.10 328.89 266.84 62.38 128.95 1180.52 113.38 264.61 61.47 251.81 51 282.29 1182.63 313.69 266.34 62.12 122.57 1180.41 117.85 264.39 61.34 251.82 52 260.99 1182.20 300.55 265.76 61.72 114.38 1180.57 117.71 264.14 61.17 251.82 53 249.94 1181.97 302.22 265.43 61.58 109.41 1180.67 117.90 263.94 61.04 251.82 54 245.26 1181.81 306.17 265.23 61.48 108.17 1180.58 119.63 263.79 60.92 251.82 55 232.70 1181.79 292.61 264.89 61.24 104.07 1180.70 117.76 263.60 60.78 251.83 56 218.64 1181.80 281.43 264.50 60.99 98.82 1180.94 114.52 263.40 60.63 251.83 57 212.67 1181.80 277.39 264.28 60.85 96.38 1181.04 113.40 263.23 60.50 251.83 58 205.27 1181.90 258.90 264.02 60.70 93.57 1181.17 111.40 263.06 60.37 251.83 59 205.83 1182.09 295.46 264.49 60.46 90.84 1181.39 109.86 262.91 60.23 251.83 60 241.80 1182.13 361.54 265.08 62.43 110.30 1180.18 132.93 263.20 60.43 251.82 61 242.62 1181.86 314.13 264.64 60.52 113.22 1180.08 130.16 263.16 60.12 251.83 62 216.16 1181.77 243.87 263.80 60.43 96.33 1181.28 102.44 262.73 60.06 251.83 63 211.13 1182.03 224.70 263.67 60.31 93.84 1181.45 100.33 262.66 60.01 251.83 64 196.74 1182.09 212.49 263.41 60.20 88.70 1181.63 101.00 262.57 59.96 251.84 65 188.06 1182.12 205.51 263.26 60.15 85.51 1181.76 102.27 262.50 59.93 251.84 66 184.70 1182.18 191.29 263.15 60.05 83.60 1181.90 101.57 262.45 59.89 251.84 67 176.40 1182.12 189.67 262.97 59.98 81.07 1182.14 98.32 262.38 59.85 251.84 68 205.52 1181.96 268.47 263.92 59.93 96.50 1181.12 115.51 262.77 59.82 251.84

Oconee Nuclear Station UFSAR Table 6-30 (Page 6 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 69 228.28 1181.58 314.22 264.12 60.56 105.73 1180.77 114.93 262.83 59.86 251.82 70 211.39 1181.50 260.95 263.51 60.05 96.34 1181.79 87.90 262.43 59.76 251.84 71 205.62 1182.15 211.03 263.29 60.03 92.69 1182.19 83.58 262.34 59.74 251.83 72 195.59 1182.56 181.51 263.07 59.89 87.25 1182.01 91.87 262.25 59.69 251.84 73 186.06 1182.68 167.17 262.88 59.81 82.39 1181.86 101.60 262.17 59.66 251.84 74 182.09 1182.72 152.77 262.73 59.73 79.81 1181.80 106.64 262.12 59.62 251.84 75 174.34 1182.42 167.84 262.59 59.67 78.35 1181.84 107.38 262.07 59.59 251.84 76 167.76 1182.02 194.13 262.51 59.66 78.08 1181.88 106.55 262.03 59.55 251.84 77 171.14 1181.79 211.29 262.57 59.62 79.29 1181.86 105.66 262.00 59.52 251.84 78 180.39 1181.60 229.44 262.71 59.74 82.74 1181.66 106.10 262.00 59.51 251.84 79 186.18 1181.59 227.52 262.75 59.70 85.12 1181.56 105.29 261.98 59.47 251.84 80 187.40 1181.76 216.34 262.72 59.65 85.92 1181.56 103.65 261.95 59.44 251.84 81 189.20 1182.09 193.61 262.68 59.61 85.20 1181.72 99.97 261.91 59.39 251.84 82 189.21 1182.36 169.14 262.61 59.52 83.05 1182.06 93.54 261.84 59.36 251.84 83 182.44 1182.30 174.37 262.46 59.48 81.51 1182.24 90.08 261.79 59.32 251.84 84 173.12 1182.11 187.45 262.29 59.40 79.56 1182.26 91.10 261.73 59.28 251.84 85 166.15 1181.96 191.34 262.15 59.35 77.67 1182.18 95.13 261.68 59.25 251.84 86 160.21 1181.90 185.84 262.03 59.28 75.57 1182.12 99.01 261.62 59.21 251.84 87 154.33 1181.85 180.63 261.92 59.22 73.36 1182.13 101.85 261.57 59.17 251.84 88 150.02 1181.84 173.45 261.83 59.17 71.37 1182.12 104.41 261.51 59.14 251.84

Oconee Nuclear Station UFSAR Table 6-30 (Page 7 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 89 146.81 1181.87 163.70 261.75 59.12 69.25 1182.01 106.84 261.46 59.10 251.84 90 145.08 1182.03 144.75 261.71 59.08 66.73 1181.81 108.90 261.40 59.06 251.84 91 142.31 1182.13 132.30 261.67 59.06 64.49 1181.63 110.74 261.37 59.05 251.85 92 140.24 1182.31 118.47 261.65 59.05 62.77 1181.49 112.28 261.34 59.03 251.85 93 138.59 1182.51 101.62 261.63 59.03 60.68 1181.37 111.96 261.31 59.02 251.85 94 135.67 1182.75 90.54 261.61 59.01 58.76 1181.30 109.76 261.28 59.00 251.85 95 132.34 1183.11 75.58 261.59 59.00 57.23 1181.30 105.54 261.26 58.99 251.85 96 128.05 1183.34 66.81 261.55 58.98 56.13 1181.38 99.03 261.24 58.97 251.85 97 124.92 1183.63 56.19 261.53 58.97 55.40 1181.51 91.22 261.22 58.96 251.85 98 121.64 1183.88 47.33 261.51 58.96 54.29 1181.62 83.38 261.20 58.95 251.85 99 117.13 1184.02 40.18 261.48 58.94 52.44 1181.65 77.13 261.17 58.93 251.85 100 111.09 1184.10 33.74 261.45 58.92 50.11 1181.58 73.41 261.14 58.92 251.85 101 104.19 1184.15 29.03 261.41 58.91 47.06 1181.40 72.24 261.12 58.90 251.85 102 97.68 1184.23 25.76 261.34 58.91 43.21 1181.17 71.12 261.09 58.89 251.85 103 92.03 1184.39 23.33 261.28 58.89 39.93 1180.96 69.33 261.06 58.87 251.85 104 87.56 1184.59 21.68 261.25 58.87 38.11 1180.82 68.30 261.04 58.86 251.85 105 85.72 1185.08 20.35 261.23 58.87 37.50 1180.80 66.37 261.02 58.85 251.85 106 84.95 1186.62 18.17 261.22 58.86 37.70 1180.95 61.67 261.02 58.84 251.85 107 84.60 1188.89 15.56 261.21 58.86 40.14 1181.38 54.67 261.02 58.83 251.85 108 86.92 1190.59 14.32 261.18 58.84 43.40 1181.91 49.81 261.02 58.84 251.85

Oconee Nuclear Station UFSAR Table 6-30 (Page 8 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 109 85.56 1191.89 11.98 261.16 58.83 39.54 1181.95 42.35 261.00 58.81 251.85 110 79.56 1193.00 8.41 261.13 58.82 34.12 1181.74 33.81 260.96 58.80 251.85 111 75.29 1193.63 6.58 261.07 58.81 33.16 1181.58 34.06 260.94 58.79 251.85 112 73.24 1194.03 6.34 261.02 58.80 32.67 1181.17 41.18 260.92 58.78 251.85 113 73.47 1193.95 7.97 261.02 58.79 33.24 1180.87 49.57 260.91 58.77 251.85 114 74.47 1193.93 10.91 261.08 58.77 34.71 1180.96 51.47 260.91 58.76 251.85 115 75.20 1194.45 12.40 261.06 58.77 37.11 1181.63 43.45 260.92 58.76 251.85 116 76.21 1195.58 10.62 261.03 58.77 39.94 1183.13 29.36 260.93 58.75 251.85 117 77.94 1196.99 6.96 260.98 58.75 43.21 1185.50 16.82 260.93 58.75 251.85 118 76.80 1198.30 3.77 260.92 58.74 43.01 1186.48 12.18 260.92 58.73 251.85 119 73.04 1198.00 3.72 261.02 58.73 40.91 1185.19 16.21 260.90 58.72 251.85 120 71.80 1192.62 17.04 260.98 58.73 43.25 1181.99 53.40 260.88 58.71 251.85 125 76.74 1192.45 19.02 260.97 58.67 44.71 1181.31 66.34 260.85 58.68 251.85 130 80.32 1193.99 13.63 260.95 58.63 44.73 1183.14 49.67 260.81 58.63 251.85 135 77.98 1198.43 4.59 260.88 58.58 42.47 1189.86 15.96 260.75 58.58 251.85 140 106.76 1198.56 54.64 261.64 58.54 54.59 1188.32 19.19 260.86 58.53 251.85 145 141.38 1190.46 106.37 261.59 58.50 65.70 1182.93 53.92 260.85 58.49 251.85 150 151.29 1183.48 116.84 261.51 58.49 66.58 1181.41 74.15 260.80 58.49 251.85 155 159.11 1182.54 125.19 261.45 58.43 69.29 1181.15 83.06 260.75 58.44 251.85 160 163.67 1182.52 124.93 261.41 58.37 68.87 1180.80 90.80 260.70 58.38 251.85

Oconee Nuclear Station UFSAR Table 6-30 (Page 9 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 165 163.65 1182.12 142.01 261.30 58.86 70.41 1180.88 85.43 260.66 58.48 251.84 170 156.93 1181.96 146.92 261.14 58.30 68.83 1180.92 83.45 260.57 58.29 251.85 175 149.54 1182.01 134.68 261.00 58.27 64.30 1180.75 88.06 260.48 58.25 251.85 180 146.79 1182.10 131.98 260.94 58.19 61.47 1180.38 95.10 260.41 58.19 251.85 185 136.31 1184.21 101.69 260.81 58.14 55.55 1180.44 83.27 260.32 58.14 251.85 190 118.19 1185.09 74.19 260.50 58.09 49.80 1181.02 58.11 260.19 58.08 251.85 195 93.44 1184.22 69.65 260.36 58.01 44.53 1183.00 28.88 260.13 58.01 251.85 200 61.38 1188.49 36.98 260.22 57.96 34.83 1183.95 9.20 259.98 57.95 251.85 205 34.94 1195.83 6.77 260.06 57.90 22.27 1182.35 6.50 259.91 57.90 251.86 210 18.66 1201.86 0.15 259.81 57.86 15.18 1181.60 4.62 259.81 57.86 251.86 215 12.87 1206.61 0.03 257.58 57.81 15.20 1183.23 3.73 259.77 57.81 251.86 220 12.25 1209.83 0.02 256.04 57.76 15.49 1184.96 1.68 259.71 57.76 251.86 225 13.75 1210.42 0.02 257.86 57.71 14.96 1203.17 0.89 259.70 57.71 251.86 230 34.98 1205.70 0.75 259.95 57.67 18.79 1249.57 0.02 260.50 57.67 251.86 235 58.49 1200.67 20.78 259.72 57.57 26.81 1245.36 0.59 259.53 57.61 251.85 240 63.22 1191.11 77.61 259.73 57.57 32.35 1205.38 4.95 259.54 57.57 251.86 245 59.61 1185.05 110.68 259.69 57.52 31.36 1188.44 5.09 259.53 57.53 251.86 250 58.98 1183.14 250.47 260.07 57.46 28.68 1195.90 1.86 259.42 57.48 251.86 255 76.45 1181.50 295.98 260.01 57.65 35.55 1190.11 8.87 259.38 57.44 251.85 260 85.21 1182.24 161.11 259.63 57.41 40.11 1183.19 32.03 259.32 57.38 251.85

Oconee Nuclear Station UFSAR Table 6-30 (Page 10 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 265 70.56 1183.17 115.93 259.52 57.35 33.17 1180.38 48.45 259.27 57.36 251.86 270 58.17 1182.98 108.49 259.40 57.31 26.47 1179.67 33.27 259.21 57.29 251.86 275 46.24 1183.17 86.62 259.30 57.24 20.51 1180.49 11.18 259.15 57.24 251.86 280 26.43 1185.23 34.42 259.18 57.19 11.67 1181.14 2.33 259.08 57.19 251.86 285 16.46 1190.90 3.02 259.06 57.15 7.89 1193.57 0.28 259.04 57.14 251.86 290 15.98 1195.10 0.74 258.89 57.10 8.23 1221.46 0.01 259.42 57.09 251.86 295 17.43 1189.80 14.99 258.90 57.05 8.47 1240.39 0.00 253.86 57.04 251.86 300 16.37 1184.34 24.97 258.86 56.99 8.31 1241.14 0.00 253.81 57.00 251.86 305 14.46 1184.34 21.97 258.80 56.96 7.54 1247.83 0.00 253.77 56.96 251.86 310 17.52 1183.79 35.47 258.75 56.92 8.48 1251.49 0.00 253.72 56.92 251.86 315 19.05 1183.48 39.99 258.72 56.88 8.37 1249.76 0.00 253.68 56.88 251.86 320 14.62 1183.70 30.07 258.66 56.83 6.54 1245.51 0.00 253.61 56.83 251.86 325 9.47 1183.70 25.79 258.60 56.79 5.94 1242.48 0.00 253.57 56.79 251.86 330 7.57 1183.88 16.45 258.56 56.76 5.54 1246.80 0.00 253.52 56.75 251.86 335 7.09 1184.10 10.49 258.49 56.71 5.11 1255.87 0.00 253.47 56.71 251.86 340 14.81 1183.32 43.87 258.47 56.67 7.70 1258.51 0.00 253.43 56.67 251.86 345 20.13 1183.07 65.11 258.44 56.63 9.05 1239.76 0.01 253.38 56.62 251.86 350 23.28 1182.59 75.27 258.40 56.59 9.91 1196.69 0.34 258.35 56.58 251.86 355 30.57 1181.98 105.94 258.39 56.55 12.29 1181.00 2.02 258.25 56.54 251.86 360 36.96 1180.30 143.28 258.36 56.51 13.69 1179.20 7.16 258.22 56.50 251.86

Oconee Nuclear Station UFSAR Table 6-30 (Page 11 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 365 41.06 1178.74 172.25 258.34 56.48 14.17 1178.68 15.04 258.18 56.46 251.86 370 40.77 1178.35 174.37 258.30 56.43 13.65 1178.45 22.60 258.13 56.42 251.86 375 38.97 1178.34 169.67 258.25 56.39 12.99 1178.34 26.98 258.09 56.37 251.86 380 33.45 1178.37 140.89 258.18 56.34 11.07 1178.26 24.72 258.04 56.33 251.86 385 27.20 1178.63 98.55 258.09 56.30 7.50 1178.18 15.53 258.00 56.29 251.86 390 28.82 1178.66 99.17 258.02 56.26 7.00 1178.43 7.38 257.95 56.25 251.86 395 32.44 1178.47 115.24 258.00 56.22 9.47 1178.40 12.48 257.87 56.21 251.86 400 31.88 1178.37 106.91 257.95 56.18 10.31 1178.23 17.71 257.85 56.17 251.86 405 29.51 1178.32 101.09 257.89 56.13 10.26 1178.28 14.18 257.80 56.13 251.86 410 24.79 1178.47 87.79 257.83 56.09 8.95 1178.26 11.06 257.75 56.08 251.86 415 20.89 1178.63 76.83 257.75 56.05 6.85 1178.22 7.42 257.70 56.04 251.86 420 15.30 1178.65 60.79 257.68 55.99 5.07 1178.43 3.47 257.66 56.00 251.86 425 8.58 1179.04 31.53 257.62 55.94 3.36 1178.84 0.95 257.62 55.95 251.86 430 4.02 1179.46 14.93 257.58 55.90 1.87 1179.23 0.19 257.55 55.91 251.86 435 2.93 1179.87 13.75 257.53 55.87 1.39 1184.60 0.03 257.64 55.87 251.86 440 4.49 1180.02 15.59 257.49 55.78 1.67 1193.87 0.00 252.45 55.83 251.86 445 5.57 1180.39 23.49 257.42 55.79 2.67 1219.61 0.00 252.39 55.78 251.86 450 11.89 1179.28 66.46 257.35 55.75 5.21 1250.75 0.00 252.35 55.75 251.86 455 19.39 1178.21 138.34 257.35 55.71 7.91 1238.88 0.01 252.30 55.71 251.86 460 22.16 1177.81 196.83 257.34 55.67 9.88 1199.92 0.31 257.17 55.67 251.86

Oconee Nuclear Station UFSAR Table 6-30 (Page 12 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 465 24.64 1177.94 243.61 257.31 55.65 10.55 1180.22 3.39 257.18 55.62 251.86 470 27.67 1179.91 298.59 257.29 55.60 10.26 1178.20 11.27 257.14 55.58 251.86 475 28.62 1181.51 325.73 257.25 55.54 9.68 1177.91 19.07 257.10 55.54 251.86 480 28.02 1182.12 333.19 257.20 55.50 9.05 1177.81 21.34 257.05 55.50 251.86 485 28.65 1182.16 335.36 257.15 55.47 8.39 1177.78 20.06 257.00 55.46 251.86 490 29.05 1181.28 336.11 257.10 55.43 7.47 1177.80 14.55 256.96 55.42 251.86 495 29.37 1181.87 337.37 257.05 55.38 7.05 1178.10 6.07 256.93 55.37 251.86 500 30.06 1181.96 314.79 257.00 55.34 6.56 1179.58 1.25 256.89 55.33 251.86 505 29.34 1181.65 297.75 256.94 55.30 5.94 1190.02 0.11 256.89 55.29 251.86 510 28.32 1182.08 311.80 256.89 55.26 6.03 1202.14 0.00 251.76 55.25 251.86 515 28.06 1181.89 317.88 256.84 55.22 5.93 1204.84 0.00 251.71 55.21 251.86 520 27.50 1182.20 300.49 256.78 55.17 5.60 1205.03 0.00 251.66 55.17 251.86 525 26.91 1182.39 290.72 256.73 55.11 5.56 1205.12 0.00 251.61 55.13 251.86 530 26.49 1181.89 289.91 256.68 55.09 5.43 1205.28 0.00 251.56 55.08 251.86 535 24.18 1182.01 262.12 256.62 55.05 4.72 1205.46 0.00 251.51 55.04 251.86 540 17.20 1181.75 153.46 256.56 55.00 2.76 1206.62 0.00 251.45 55.00 251.87 545 17.48 1178.41 119.78 256.47 54.96 5.26 1212.00 0.05 256.26 54.96 251.87 550 26.48 1177.45 191.53 256.46 54.92 7.48 1198.97 1.63 256.34 54.92 251.87 555 30.38 1179.49 256.27 256.44 54.88 6.17 1178.09 2.40 256.33 54.87 251.87 560 30.27 1181.52 287.52 256.39 54.84 6.18 1178.98 0.93 256.27 54.83 251.87

Oconee Nuclear Station UFSAR Table 6-30 (Page 13 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 565 29.68 1182.10 289.02 256.34 54.80 5.81 1188.63 0.12 256.17 54.79 251.87 570 29.00 1182.49 319.90 256.30 54.76 6.16 1201.20 0.00 251.16 54.75 251.87 575 28.82 1181.95 349.48 256.26 54.72 6.22 1204.55 0.00 251.11 54.71 251.87 580 28.74 1181.58 335.08 256.21 54.67 5.72 1204.78 0.00 251.06 54.67 251.87 585 27.90 1181.53 317.08 256.14 54.63 5.57 1204.95 0.00 251.01 54.62 251.87 590 27.41 1181.83 332.46 256.10 54.59 5.59 1204.91 0.00 250.96 54.58 251.87 595 27.02 1181.85 350.62 256.05 54.55 5.76 1204.89 0.00 250.91 54.54 251.87 600 27.14 1181.99 337.96 256.00 54.51 5.61 1204.90 0.00 250.86 54.50 251.87 605 27.77 1182.06 322.40 255.94 54.46 5.39 1204.93 0.00 250.81 54.46 301.87 610 27.77 1181.46 288.88 255.89 54.42 5.23 1205.08 0.00 250.76 54.42 301.87 615 27.53 1181.16 250.34 255.82 54.38 5.07 1205.32 0.00 250.71 54.37 301.87 620 27.37 1180.31 236.36 255.77 54.34 4.90 1205.47 0.00 250.66 54.33 301.87 625 27.22 1180.09 225.57 255.71 54.30 4.86 1205.47 0.00 250.61 54.29 301.87 630 26.99 1180.08 227.60 255.66 54.26 4.82 1205.47 0.00 250.56 54.25 301.87 635 26.77 1180.58 241.34 255.61 54.21 4.96 1205.40 0.00 250.51 54.21 301.87 640 26.59 1180.51 255.24 255.57 54.17 5.13 1205.37 0.00 250.45 54.16 301.87 645 26.66 1180.38 247.06 255.52 54.13 4.77 1205.40 0.00 250.40 54.12 301.87 650 26.69 1180.58 248.12 255.47 54.09 4.85 1205.32 0.00 250.35 54.08 301.87 655 26.72 1180.03 252.04 255.42 54.05 5.15 1205.32 0.00 250.30 54.04 301.87 660 25.87 1178.97 226.41 255.37 54.01 4.74 1205.45 0.00 250.25 54.00 301.87

Oconee Nuclear Station UFSAR Table 6-30 (Page 14 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 665 25.53 1177.48 234.07 255.31 53.96 4.81 1205.27 0.00 250.21 53.96 301.87 670 26.01 1178.19 258.72 255.01 53.92 5.81 1201.25 0.09 255.07 53.92 301.87 675 26.88 1178.10 255.58 254.96 53.88 5.90 1188.49 0.65 255.09 53.87 301.87 680 27.03 1176.99 222.88 255.18 53.84 5.51 1177.89 0.82 255.08 53.83 301.87 685 27.32 1177.77 234.35 255.13 53.79 5.89 1179.08 0.53 254.98 53.79 301.87 690 28.96 1178.60 266.16 255.09 53.75 6.21 1178.94 0.68 254.92 53.75 301.87 695 28.67 1178.30 285.31 255.04 53.71 6.39 1180.46 0.47 254.89 53.71 301.87 700 28.28 1177.69 275.35 254.99 53.67 5.93 1191.03 0.07 254.68 53.67 301.87 705 27.51 1177.10 221.73 254.92 53.63 5.34 1202.99 0.00 249.80 53.62 301.87 710 26.20 1176.76 226.97 254.87 53.59 5.30 1204.57 0.00 249.75 53.58 301.87 715 26.07 1176.68 231.41 254.82 53.55 5.32 1204.70 0.00 249.70 53.54 301.87 720 25.81 1176.68 231.83 254.77 53.50 5.36 1204.69 0.00 249.65 53.50 301.87 725 25.40 1176.71 237.27 254.72 53.46 5.36 1204.67 0.00 249.59 53.46 301.87 730 25.32 1176.70 229.92 254.67 53.42 5.25 1204.74 0.00 249.54 53.42 301.87 735 25.25 1176.68 222.03 254.61 53.38 5.06 1204.75 0.00 249.49 53.37 301.87 740 25.02 1176.65 217.70 254.56 53.34 5.17 1204.76 0.00 249.44 53.33 301.87 745 24.79 1176.65 220.01 254.51 53.29 5.22 1204.87 0.00 249.39 53.29 301.87 750 24.75 1176.63 213.97 254.46 53.25 5.01 1204.80 0.00 249.34 53.25 301.87 755 24.42 1176.63 220.85 254.40 53.21 5.22 1204.76 0.00 249.29 53.21 301.87 760 24.31 1176.56 224.99 254.35 53.17 5.13 1204.87 0.00 249.24 53.17 301.87

Oconee Nuclear Station UFSAR Table 6-30 (Page 15 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 765 24.26 1176.52 215.18 254.30 53.13 4.96 1204.83 0.00 249.19 53.12 301.87 770 24.09 1176.51 209.85 254.25 53.09 5.17 1204.80 0.00 249.13 53.08 301.87 775 24.14 1176.53 208.88 254.20 53.04 4.88 1204.89 0.00 249.08 53.04 301.87 780 23.63 1176.59 229.88 254.15 53.00 5.03 1204.74 0.00 249.03 53.00 301.87 785 23.58 1176.58 239.83 254.10 52.96 5.18 1204.74 0.00 248.98 52.96 301.87 790 23.65 1176.55 235.12 254.05 52.92 4.94 1204.78 0.00 248.93 52.92 301.87 795 23.33 1176.54 234.43 254.00 52.88 5.02 1204.74 0.00 248.88 52.87 301.87 800 23.14 1176.52 231.85 253.94 52.84 5.20 1204.80 0.00 248.83 52.83 301.87 805 23.29 1176.48 218.85 253.89 52.80 4.81 1204.83 0.00 248.78 52.79 301.87 810 22.99 1176.78 229.13 253.70 52.75 5.11 1204.73 0.00 248.72 52.75 301.87 815 22.80 1176.78 225.98 253.45 52.71 5.01 1204.83 0.00 248.67 52.71 301.87 820 22.32 1176.52 210.71 252.33 52.67 4.71 1192.86 0.12 253.64 52.67 301.87 825 21.72 1177.67 227.24 249.12 52.63 5.20 1180.62 0.23 253.55 52.62 301.87 830 22.54 1177.92 222.46 246.63 52.59 4.78 1177.85 0.28 253.56 52.58 301.87 835 21.51 1177.71 240.40 242.95 52.54 4.79 1178.20 0.31 253.46 52.54 301.87 840 19.39 1178.97 280.58 235.87 52.50 5.22 1178.16 0.35 253.37 52.50 301.87 845 20.33 1178.39 266.18 229.96 52.47 4.81 1177.39 0.52 253.35 52.46 301.87 850 19.72 1177.20 243.59 230.57 52.41 4.86 1177.31 0.64 253.32 52.42 301.87 855 18.44 1178.05 299.71 226.22 52.37 5.30 1177.45 0.53 253.31 52.37 301.87 860 18.92 1179.02 326.12 214.84 52.34 5.05 1179.15 0.29 253.18 52.33 301.87

Oconee Nuclear Station UFSAR Table 6-30 (Page 16 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 865 17.80 1178.83 252.70 216.09 52.29 3.99 1179.33 0.34 253.10 52.29 301.87 870 16.97 1179.99 271.38 218.34 52.24 4.75 1177.27 0.74 253.10 52.25 301.87 875 17.45 1180.78 310.02 210.19 52.21 5.82 1177.34 0.92 253.05 52.21 301.87 880 17.93 1179.19 232.52 217.26 52.16 4.08 1177.10 0.87 253.02 52.16 301.87 885 17.29 1179.86 254.57 215.56 52.17 4.74 1177.10 0.96 252.93 52.13 301.87 890 17.24 1180.18 310.69 205.39 52.08 5.53 1177.37 0.83 252.91 52.08 301.88 895 17.26 1178.74 256.64 212.66 52.03 3.82 1177.25 0.91 252.86 52.04 301.88 900 16.92 1180.56 265.04 213.30 52.00 5.05 1177.03 1.18 252.79 52.00 301.87 905 17.88 1180.52 252.95 206.59 51.97 5.21 1177.15 0.95 252.75 51.96 301.88 910 18.01 1179.30 244.00 209.84 51.94 3.74 1177.14 0.97 252.69 51.93 301.87 915 18.20 1180.43 248.91 212.02 51.90 4.87 1177.18 0.96 252.68 51.90 301.88 920 17.89 1179.43 178.18 222.76 51.87 6.27 1181.07 0.47 252.67 51.87 301.88 925 16.65 1179.34 166.34 223.40 51.83 6.84 1207.64 0.14 252.61 51.83 301.88 930 16.95 1178.97 137.39 223.31 51.80 6.70 1233.76 0.00 247.55 51.80 301.88 935 16.88 1178.70 176.77 227.14 51.77 6.93 1236.87 0.00 247.50 51.77 301.88 940 17.01 1178.26 174.69 228.48 51.73 7.04 1236.49 0.00 247.46 51.73 301.88 945 17.74 1177.65 193.15 237.64 51.70 6.00 1226.72 0.18 252.38 51.70 301.88 950 20.25 1179.17 266.62 232.52 51.67 5.46 1195.25 0.50 252.38 51.67 301.88 955 23.16 1177.96 249.89 239.34 51.61 4.86 1176.95 0.83 252.34 51.63 301.88 960 23.46 1178.00 278.10 240.43 51.60 4.36 1176.89 0.70 252.28 51.60 301.88

Oconee Nuclear Station UFSAR Table 6-30 (Page 17 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 965 24.63 1177.51 209.56 239.31 51.57 4.08 1178.42 0.22 252.24 51.56 301.88 970 24.97 1175.87 147.55 252.24 51.53 4.27 1184.28 0.04 252.24 51.53 301.88 975 24.22 1175.78 184.87 252.27 51.50 4.60 1184.47 0.04 251.82 51.50 301.88 980 24.53 1175.75 196.38 252.24 51.47 4.23 1190.20 0.02 251.95 51.47 301.88 985 24.32 1175.77 212.19 252.20 51.44 4.58 1201.71 0.00 247.08 51.43 301.88 990 24.62 1175.77 208.66 252.16 51.40 4.09 1204.52 0.00 247.04 51.40 301.88 995 23.90 1175.83 231.24 252.11 51.37 4.34 1195.99 0.06 252.21 51.37 301.88 1000 23.39 1175.81 251.65 252.08 51.34 4.60 1184.97 0.14 251.92 51.33 301.88 1005 23.31 1175.75 234.44 252.03 51.30 4.37 1184.25 0.08 251.91 51.30 301.88 1010 23.02 1175.95 222.89 251.76 51.27 4.40 1195.80 0.00 246.87 51.27 301.88 1015 23.16 1176.03 246.80 251.63 51.24 4.31 1192.74 0.23 251.79 51.23 301.88 1020 22.90 1175.84 265.86 251.81 51.20 4.78 1180.37 0.42 251.79 51.20 301.88 1025 22.97 1175.79 252.45 251.86 51.17 4.68 1180.14 0.21 251.76 51.17 301.88 1030 23.05 1175.74 226.25 251.82 51.14 4.37 1191.89 0.02 252.25 51.13 301.88 1035 22.50 1175.75 218.13 251.77 51.10 4.53 1202.71 0.00 246.66 51.10 301.88 1040 22.45 1176.29 270.51 251.39 51.06 4.50 1204.33 0.00 246.62 51.07 301.88 1045 22.73 1176.19 269.50 251.35 51.03 4.37 1204.63 0.00 246.58 51.03 301.88 1050 22.53 1175.62 219.91 251.64 51.00 4.06 1204.65 0.00 246.53 51.00 301.88 1055 22.27 1175.59 207.85 251.59 50.97 4.18 1202.38 0.01 246.49 50.97 301.88 1060 21.94 1175.65 231.20 251.56 50.94 4.49 1190.07 0.07 251.53 50.93 301.88

Oconee Nuclear Station UFSAR Table 6-30 (Page 18 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 1065 21.83 1175.66 239.80 251.52 50.90 4.40 1182.25 0.07 251.60 50.90 301.88 1070 21.74 1175.59 216.69 251.47 50.87 4.42 1193.73 0.01 246.36 50.87 301.88 1075 22.23 1175.53 184.92 251.42 50.84 4.05 1203.35 0.00 246.32 50.83 301.88 1080 21.72 1175.56 203.55 251.38 50.80 4.44 1191.70 0.16 251.25 50.80 301.88 1085 21.65 1175.54 224.82 251.34 50.77 4.44 1179.26 0.27 251.26 50.77 301.88 1090 21.68 1175.49 201.62 251.30 50.74 4.32 1177.75 0.17 251.15 50.73 301.88 1095 20.75 1176.03 208.73 243.76 50.70 4.34 1178.26 0.10 250.96 50.70 301.88 1100 21.15 1176.56 234.28 243.60 50.68 4.33 1179.36 0.13 251.23 50.67 301.88 1105 20.75 1176.57 274.99 244.68 50.61 4.84 1179.36 0.15 251.13 50.63 301.88 1110 19.43 1177.52 322.60 233.27 50.60 4.94 1186.80 0.06 251.02 50.60 301.88 1115 19.64 1177.89 294.36 228.42 50.57 4.14 1198.38 0.00 245.98 50.57 301.88 1120 18.01 1177.68 273.20 226.40 50.54 4.06 1188.84 0.28 250.85 50.53 301.88 1125 16.54 1179.09 332.81 213.41 50.50 5.01 1177.77 0.59 250.92 50.50 301.88 1130 17.76 1178.55 283.41 215.83 50.45 3.91 1176.57 0.54 250.86 50.47 301.88 1135 16.13 1177.66 266.68 213.73 50.44 3.98 1176.56 0.64 250.81 50.43 301.88 1140 14.99 1177.93 316.84 202.77 50.40 4.86 1176.71 0.61 250.80 50.40 301.88 1145 14.80 1176.97 237.35 213.26 50.37 4.66 1176.56 0.56 250.70 50.37 301.88 1150 13.70 1177.28 254.22 211.19 50.34 6.32 1178.75 0.58 250.71 50.33 301.88 1155 13.34 1177.99 268.99 199.08 50.30 6.66 1197.44 0.24 250.67 50.30 301.88 1160 13.50 1177.15 209.90 208.50 50.25 4.01 1208.01 0.08 250.46 50.26 301.88

Oconee Nuclear Station UFSAR Table 6-30 (Page 19 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 1165 14.02 1178.05 254.88 205.99 50.24 4.17 1177.60 0.27 250.55 50.23 301.88 1170 14.37 1178.61 286.20 199.32 50.20 4.74 1177.27 0.37 250.50 50.20 301.88 1175 15.61 1177.42 256.10 209.72 50.18 3.42 1176.60 0.43 250.48 50.17 301.88 1180 16.30 1177.73 280.26 203.37 50.14 4.37 1176.61 0.51 250.44 50.13 301.88 1185 16.18 1177.32 235.82 204.44 49.91 3.76 1176.64 0.41 250.39 50.10 301.88 1190 16.31 1177.06 241.18 214.02 50.06 4.11 1176.55 0.55 250.32 50.07 301.88 1195 16.88 1178.14 308.80 204.13 50.03 5.04 1176.59 0.62 250.31 50.03 301.88 1200 17.66 1178.06 259.68 210.10 49.99 4.41 1176.40 0.66 250.23 50.00 301.88 1210 17.72 1177.84 240.85 215.72 49.94 4.63 1176.38 0.68 250.17 49.93 301.88 1220 17.51 1177.09 235.10 215.37 49.87 4.55 1176.45 0.62 250.08 49.87 301.88 1230 18.72 1176.41 231.44 219.72 49.81 4.31 1176.40 0.59 249.99 49.80 301.88 1240 21.09 1176.21 207.39 233.01 49.74 4.09 1177.28 0.37 249.93 49.73 301.88 1250 23.14 1175.55 202.50 246.80 49.67 4.20 1184.65 0.12 249.94 49.67 301.88 1260 23.98 1174.94 193.33 249.71 49.60 4.40 1191.81 0.03 250.09 49.60 301.88 1270 23.41 1174.80 185.95 249.75 49.54 4.34 1198.41 0.00 244.65 49.53 301.88 1280 22.81 1174.84 211.46 249.67 49.47 4.26 1203.96 0.00 244.56 49.47 301.88 1290 22.16 1174.87 218.76 249.58 49.40 4.26 1204.00 0.00 244.48 49.40 301.88 1300 21.47 1174.88 225.03 249.49 49.34 4.22 1203.81 0.00 244.39 49.33 301.88 1310 21.03 1175.37 244.42 248.91 49.27 4.15 1203.36 0.00 244.30 49.27 301.88 1320 20.14 1176.36 269.26 245.05 49.20 4.26 1203.45 0.00 244.22 49.20 301.88

Oconee Nuclear Station UFSAR Table 6-30 (Page 20 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 1330 19.25 1177.07 302.52 241.29 49.14 4.13 1203.83 0.00 244.13 49.13 301.88 1340 17.51 1177.87 301.64 228.48 49.06 4.13 1201.34 0.01 248.64 49.07 301.88 1350 15.22 1178.03 299.56 215.78 49.00 4.21 1189.09 0.05 248.88 49.00 301.89 1360 13.85 1176.85 268.95 213.24 48.94 3.84 1178.18 0.06 248.96 48.93 301.89 1370 12.01 1177.05 264.88 200.87 48.86 4.28 1181.28 0.06 248.66 48.87 301.89 1380 10.33 1177.45 267.46 196.56 48.81 4.51 1180.14 0.19 248.65 48.80 301.89 1390 10.13 1176.65 210.18 197.46 48.73 3.92 1176.10 0.31 248.61 48.73 301.89 1400 13.37 1176.88 335.28 194.41 48.65 6.34 1177.45 20.09 248.47 48.67 301.88 1410 16.72 1176.82 355.03 201.37 48.60 6.40 1177.10 24.47 248.45 48.60 301.89 1420 17.47 1176.03 279.69 205.55 48.53 4.81 1175.22 11.82 248.33 48.53 301.89 1430 18.74 1175.81 219.60 201.59 48.47 4.62 1175.42 8.40 248.27 48.46 301.89 1440 20.18 1176.11 184.84 213.17 48.41 4.33 1175.43 7.14 248.14 48.41 301.89 1450 19.34 1175.89 193.95 219.68 48.34 4.64 1175.29 7.45 248.11 48.33 301.89 1460 16.65 1175.97 141.72 232.04 48.27 5.12 1179.23 1.76 248.02 48.27 301.89 1470 14.30 1176.75 188.04 225.87 48.20 6.17 1202.78 0.33 247.93 48.20 301.89 1480 13.06 1176.69 212.12 224.13 48.14 6.01 1224.85 0.00 242.81 48.13 301.89 1490 13.28 1176.35 206.06 225.06 48.07 5.92 1225.40 0.00 242.73 48.07 301.89 1500 19.00 1176.82 335.32 222.56 48.00 6.27 1204.08 0.22 247.64 48.00 301.89 1510 24.99 1176.14 328.41 228.87 47.96 6.10 1180.85 0.72 247.58 47.96 301.89 1520 26.02 1175.15 185.76 246.53 47.93 5.44 1185.14 0.51 247.57 47.92 301.89

Oconee Nuclear Station UFSAR Table 6-30 (Page 21 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 1530 26.49 1175.75 175.36 247.48 47.88 5.28 1198.68 0.00 242.48 47.88 301.89 1540 26.34 1175.74 199.51 247.53 47.84 5.15 1202.14 0.00 242.42 47.84 301.89 1550 25.25 1175.40 250.22 241.71 47.80 5.24 1201.94 0.00 242.37 47.80 301.89 1560 25.43 1175.75 245.85 241.44 47.76 5.32 1201.89 0.00 242.31 47.76 301.89 1570 25.50 1177.09 206.55 246.32 47.72 5.14 1202.04 0.00 242.26 47.72 301.89 1580 24.59 1178.05 200.98 246.37 47.68 4.99 1202.03 0.00 242.21 47.68 301.89 1590 24.11 1177.08 197.40 247.25 47.64 5.01 1201.98 0.00 242.16 47.64 301.89 1600 22.33 1177.17 232.84 247.20 47.60 5.13 1201.87 0.00 242.10 47.60 301.89 1610 20.28 1177.76 254.97 244.06 47.56 5.24 1201.79 0.00 242.05 47.56 301.89 1620 17.68 1177.26 247.30 231.92 47.53 5.06 1200.06 0.00 242.00 47.52 301.89 1630 13.96 1176.36 262.39 213.34 47.48 4.86 1190.71 0.06 246.79 47.48 301.89 1640 11.02 1176.44 321.56 198.17 47.40 4.98 1179.97 0.35 246.87 47.44 301.89 1650 9.39 1176.63 306.59 193.47 47.41 4.56 1176.27 0.45 246.83 47.40 301.89 1660 7.78 1175.66 237.10 189.19 47.35 4.41 1183.71 0.19 246.85 47.36 301.89 1670 6.12 1175.64 267.73 186.38 47.24 4.36 1201.56 0.03 247.18 47.32 301.89 1680 5.19 1176.46 255.85 187.94 47.28 3.62 1215.01 0.00 241.67 47.28 301.89 1690 6.41 1175.88 239.39 191.14 47.25 3.63 1213.63 0.00 241.62 47.24 301.89 1700 7.59 1176.08 290.02 192.98 47.11 4.02 1210.67 0.00 241.57 47.20 301.89 1710 7.88 1176.07 266.98 195.92 47.16 3.82 1210.99 0.00 241.51 47.16 301.89 1720 9.09 1175.35 249.26 198.13 47.13 4.02 1212.99 0.00 241.45 47.12 301.89

Oconee Nuclear Station UFSAR Table 6-30 (Page 22 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 1730 9.61 1175.52 275.56 199.15 47.05 4.39 1212.27 0.00 241.40 47.08 301.89 1740 9.98 1175.72 249.71 204.12 47.04 4.40 1211.30 0.00 241.35 47.04 301.89 1750 11.00 1177.76 270.22 208.78 47.00 4.31 1203.13 0.80 246.24 47.00 301.89 1760 21.34 1176.20 356.99 214.03 46.98 5.01 1183.15 2.13 246.23 46.95 301.89 1770 24.77 1174.79 240.94 216.75 46.92 5.12 1176.04 1.38 246.22 46.92 301.89 1780 17.12 1174.84 98.05 213.69 46.88 5.13 1190.72 0.06 246.18 46.88 301.89 1790 16.22 1174.80 116.91 228.22 46.84 6.10 1204.39 0.00 241.08 46.84 301.89 1800 17.25 1174.23 127.18 243.23 46.80 6.28 1207.93 0.00 241.02 46.80 301.89 1810 17.50 1174.08 141.14 245.99 46.76 6.22 1207.68 0.00 240.97 46.76 301.89 1820 16.84 1174.39 161.10 245.97 46.72 6.10 1207.41 0.00 240.92 46.72 301.89 1830 15.45 1174.72 204.02 241.42 46.68 6.01 1207.04 0.00 240.86 46.68 301.89 1840 14.44 1175.16 274.64 228.25 46.70 5.46 1200.52 0.01 240.81 46.64 301.89 1850 15.13 1175.41 289.94 225.31 46.58 4.76 1186.36 0.04 245.58 46.60 301.89 1860 15.53 1175.41 225.40 232.52 46.56 4.72 1182.65 0.05 245.57 46.56 301.89 1870 14.74 1175.39 215.79 226.43 46.52 4.67 1184.99 0.04 245.49 46.52 301.89 1880 15.10 1175.49 241.89 223.04 46.48 4.10 1183.17 0.03 245.44 46.48 301.89 1890 15.33 1175.40 263.41 217.54 46.45 3.42 1186.32 0.02 245.79 46.44 301.89 1900 13.46 1175.00 275.44 208.62 46.41 3.96 1195.75 0.01 240.47 46.40 301.89 1910 13.27 1175.31 278.26 210.65 46.33 4.46 1190.70 0.05 245.41 46.36 301.89 1920 14.26 1175.39 272.39 210.74 46.32 4.12 1182.76 0.06 245.43 46.32 301.89

Oconee Nuclear Station UFSAR Table 6-30 (Page 23 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 1930 14.31 1175.81 249.44 205.85 46.28 4.02 1182.61 0.02 245.33 46.28 301.89 1940 14.21 1176.77 246.04 203.64 46.24 3.81 1184.61 0.01 244.97 46.24 301.89 1950 14.93 1177.36 223.18 209.53 46.20 2.89 1190.19 0.00 240.21 46.19 301.89 1960 15.10 1178.01 240.46 209.78 46.16 2.42 1197.24 0.00 240.15 46.16 301.89 1970 14.28 1178.43 257.28 205.60 46.13 3.13 1199.86 0.00 240.09 46.12 301.89 1980 13.36 1177.80 264.47 200.20 46.09 3.40 1201.40 0.00 240.03 46.08 301.90 1990 12.99 1176.04 257.97 198.59 45.91 2.69 1205.61 0.00 239.98 46.04 301.90 2000 12.92 1174.94 254.80 203.30 46.00 2.51 1205.71 0.00 239.92 46.00 301.90 2010 12.75 1174.22 245.29 206.08 45.97 2.53 1200.04 0.00 239.88 45.97 301.90 2020 11.55 1173.98 257.56 198.31 45.95 2.63 1200.30 0.00 239.84 45.94 301.90 2030 10.08 1174.43 292.00 191.62 45.86 2.54 1203.35 0.00 239.80 45.91 301.90 2040 10.09 1174.63 235.62 195.59 45.88 2.07 1203.49 0.00 239.76 45.88 301.90 2050 10.03 1175.88 241.87 195.99 45.86 2.85 1202.80 0.00 239.72 45.85 301.90 2060 9.86 1177.89 293.14 191.70 45.79 3.07 1201.26 0.00 239.68 45.82 301.90 2070 9.78 1179.03 261.28 191.51 45.79 2.56 1200.54 0.00 239.64 45.79 301.90 2080 10.01 1178.70 214.97 194.45 45.76 2.73 1199.97 0.00 239.59 45.76 301.90 2090 10.58 1177.97 268.62 193.91 45.72 2.74 1200.03 0.00 239.55 45.73 301.90 2100 11.03 1178.51 288.25 195.35 45.71 2.91 1199.45 0.02 244.64 45.70 301.90 2110 12.18 1178.52 238.53 201.04 45.63 2.96 1192.60 0.02 244.40 45.67 301.90 2120 13.02 1178.10 206.77 205.20 45.64 2.95 1194.38 0.01 243.49 45.64 301.90

Oconee Nuclear Station UFSAR Table 6-30 (Page 24 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 2130 13.30 1178.00 204.62 203.40 45.61 3.39 1191.05 0.02 244.14 45.61 301.90 2140 14.27 1178.18 235.21 203.05 45.58 3.30 1188.69 0.01 239.34 45.58 301.90 2150 14.87 1177.50 229.89 206.74 45.55 2.59 1194.16 0.00 239.30 45.55 301.90 2160 14.37 1177.31 230.56 206.44 45.52 2.61 1196.63 0.00 239.26 45.52 301.90 2170 13.85 1177.59 254.91 205.77 45.49 3.45 1197.19 0.00 239.22 45.49 301.90 2180 14.12 1177.95 262.08 209.85 45.44 3.12 1197.23 0.00 239.18 45.46 301.90 2190 13.81 1179.09 255.27 207.35 45.43 2.43 1199.91 0.00 239.13 45.43 301.90 2200 14.07 1177.70 214.48 208.84 45.40 2.37 1195.09 0.00 239.09 45.40 301.90 2210 13.43 1176.81 187.24 212.76 45.37 2.76 1198.58 0.00 239.05 45.37 301.90 2220 13.32 1177.65 242.68 210.36 45.34 2.50 1201.72 0.00 239.01 45.34 301.90 2230 13.82 1178.41 282.79 208.21 45.31 2.34 1196.71 0.00 238.97 45.31 301.90 2240 13.14 1178.98 268.70 207.36 45.26 3.09 1198.51 0.00 238.93 45.28 301.90 2250 13.53 1178.46 261.03 209.29 45.26 2.76 1202.82 0.00 238.88 45.25 301.90 2260 13.32 1178.04 274.96 202.13 45.22 2.67 1199.81 0.00 238.84 45.22 301.90 2270 13.28 1177.08 269.13 200.05 45.19 2.99 1194.71 0.00 238.80 45.19 301.90 2280 13.33 1176.87 250.29 201.40 45.16 2.62 1192.34 0.00 238.76 45.16 301.90 2290 13.31 1176.55 236.84 202.66 45.13 2.36 1198.39 0.00 238.72 45.13 301.90 2300 13.13 1176.26 228.27 202.59 45.10 2.20 1203.37 0.00 238.67 45.10 301.90 2310 12.83 1176.65 232.93 200.49 45.07 2.56 1193.79 0.00 238.63 45.07 301.90 2320 13.65 1177.12 250.72 200.33 45.03 2.25 1190.38 0.00 238.59 45.04 301.90

Oconee Nuclear Station UFSAR Table 6-30 (Page 25 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 2330 13.36 1178.13 253.86 198.64 45.01 2.28 1198.25 0.00 238.55 45.01 301.90 2340 11.86 1178.02 243.56 202.12 44.98 3.20 1201.87 0.00 238.51 44.98 301.90 2350 12.58 1177.50 249.14 206.92 45.24 2.72 1202.30 0.00 238.46 44.95 301.90 2360 13.07 1177.71 257.10 204.79 44.92 2.12 1200.34 0.00 238.42 44.92 301.90 2370 12.57 1177.12 243.77 202.99 44.89 2.35 1193.70 0.01 238.38 44.89 301.90 2380 13.04 1177.21 233.84 203.63 44.86 2.67 1194.61 0.00 238.34 44.86 301.90 2390 13.07 1178.08 275.37 199.92 44.83 2.08 1198.56 0.00 238.29 44.83 301.90 2400 12.37 1177.64 282.07 195.14 44.80 2.41 1201.80 0.00 238.25 44.80 301.90 2410 12.32 1177.33 269.60 196.07 44.74 2.68 1201.89 0.00 238.21 44.77 301.90 2420 12.20 1177.24 254.49 198.27 44.74 1.93 1198.91 0.00 238.17 44.74 301.90 2430 11.72 1176.69 221.21 196.59 44.71 2.23 1194.68 0.00 238.13 44.71 301.90 2440 12.69 1177.22 252.21 196.43 44.68 1.99 1193.15 0.00 238.08 44.68 301.90 2450 12.51 1177.78 265.72 193.28 44.65 2.36 1199.83 0.00 238.04 44.65 301.90 2460 12.65 1178.19 254.90 194.74 44.63 2.47 1197.10 0.00 238.00 44.62 301.90 2470 12.85 1178.38 251.42 196.83 44.59 2.11 1194.65 0.00 237.96 44.59 301.90 2480 12.48 1178.28 235.33 200.14 44.53 2.40 1196.66 0.00 237.91 44.56 301.90 2490 12.49 1177.67 235.09 201.13 44.53 2.05 1197.94 0.00 237.87 44.53 301.90 2500 12.50 1177.55 232.66 200.30 44.50 2.24 1194.70 0.00 237.83 44.50 301.90 2510 12.63 1178.05 241.38 201.11 44.47 2.20 1193.51 0.00 237.79 44.47 301.90 2520 12.50 1177.46 253.89 198.59 44.42 2.32 1193.52 0.00 237.74 44.44 301.90

Oconee Nuclear Station UFSAR Table 6-30 (Page 26 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 2530 12.36 1177.08 256.25 196.96 44.39 2.90 1195.30 0.00 237.70 44.41 301.90 2540 12.42 1176.77 276.94 194.54 44.37 2.37 1198.47 0.00 237.66 44.38 301.90 2550 13.02 1176.60 270.95 194.95 44.36 2.10 1200.07 0.00 237.62 44.35 301.90 2560 12.83 1176.32 239.93 195.60 44.32 2.76 1202.47 0.00 237.57 44.32 301.90 2570 12.63 1176.57 260.29 194.28 44.30 2.35 1199.10 0.00 237.53 44.29 301.90 2580 13.01 1176.58 262.47 194.97 44.26 2.07 1195.19 0.00 237.49 44.26 301.90 2590 12.49 1176.20 241.81 193.09 44.24 2.80 1199.10 0.00 237.45 44.23 301.90 2600 11.90 1176.68 263.70 192.76 44.20 2.62 1199.78 0.00 237.40 44.20 301.90 2610 11.92 1177.05 256.18 193.58 44.17 2.66 1198.93 0.00 237.36 44.17 301.90 2620 11.74 1176.89 254.17 193.50 44.12 2.58 1196.77 0.00 237.32 44.14 301.90 2630 11.57 1176.38 257.59 196.02 44.10 2.36 1197.02 0.00 237.28 44.11 301.90 2640 11.49 1176.99 233.90 196.75 44.08 2.34 1201.14 0.00 237.23 44.08 301.90 2650 11.75 1177.26 223.96 195.71 44.05 2.11 1201.55 0.00 237.19 44.05 301.90 2660 12.17 1177.16 238.23 192.24 44.02 2.47 1201.57 0.00 237.15 44.02 301.90 2670 12.37 1177.10 249.44 192.82 43.99 2.21 1200.03 0.00 237.10 43.99 301.90 2680 12.45 1177.07 242.01 195.94 43.96 2.18 1200.83 0.00 237.06 43.96 301.90 2690 12.55 1177.10 253.23 193.86 43.93 2.62 1202.68 0.00 237.02 43.93 301.90 2700 11.92 1176.98 266.46 190.97 43.90 2.49 1200.44 0.00 236.97 43.90 301.90 2710 11.78 1176.70 248.67 191.94 43.86 2.66 1198.77 0.00 236.93 43.87 301.90 2720 11.79 1176.34 263.58 192.28 43.82 2.56 1198.63 0.00 236.89 43.84 301.90

Oconee Nuclear Station UFSAR Table 6-30 (Page 27 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 2730 12.10 1175.81 268.62 192.53 43.82 2.37 1198.77 0.00 236.84 43.81 301.90 2740 12.14 1175.67 245.70 191.94 43.78 2.82 1200.23 0.00 236.80 43.78 301.90 2750 12.50 1176.39 287.69 192.08 43.76 2.21 1202.02 0.00 236.76 43.75 301.90 2760 12.47 1176.72 290.53 194.33 43.66 1.71 1204.48 0.00 236.72 43.72 301.90 2770 11.48 1176.15 242.01 198.55 43.69 2.05 1202.19 0.00 236.67 43.69 301.90 2780 11.35 1175.76 240.22 199.20 43.66 1.66 1200.45 0.00 236.63 43.66 301.90 2790 11.56 1175.37 265.35 194.94 43.60 1.76 1199.10 0.00 236.59 43.63 301.90 2800 12.02 1174.67 261.00 194.16 43.58 2.51 1200.63 0.00 236.54 43.60 301.90 2810 11.42 1175.70 270.84 192.43 43.56 2.38 1201.49 0.00 236.50 43.57 301.90 2820 11.30 1176.67 264.28 191.41 43.55 2.59 1198.99 0.00 236.46 43.54 301.90 2830 11.65 1177.26 263.93 191.62 43.52 2.50 1195.94 0.00 236.41 43.51 301.90 2840 11.49 1177.21 261.57 192.70 43.48 2.43 1196.19 0.00 236.37 43.48 301.90 2850 12.04 1177.02 258.58 194.77 43.45 2.38 1196.77 0.00 236.33 43.45 301.90 2860 12.31 1176.92 271.84 191.11 43.42 2.01 1198.09 0.00 236.28 43.42 301.90 2870 11.55 1176.27 241.87 189.90 42.95 2.57 1202.40 0.00 236.24 43.39 301.90 2880 11.20 1177.21 238.23 196.05 43.36 2.66 1201.80 0.00 236.20 43.36 301.90 2890 12.36 1177.88 251.71 195.46 43.33 2.17 1200.89 0.00 236.15 43.33 301.90 2900 12.87 1177.12 267.37 191.13 43.30 1.98 1201.10 0.00 236.11 43.30 301.90 2910 11.76 1176.44 248.01 191.13 43.27 2.23 1201.34 0.00 236.07 43.27 301.90 2920 12.12 1177.06 240.84 193.95 43.24 2.28 1198.69 0.00 236.02 43.24 301.90

Oconee Nuclear Station UFSAR Table 6-30 (Page 28 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 2930 11.36 1176.82 231.17 190.99 43.21 2.33 1199.43 0.00 235.98 43.21 301.90 2940 10.44 1176.89 220.55 193.30 43.18 2.55 1202.91 0.00 235.94 43.18 301.91 2950 10.96 1176.79 210.61 198.58 43.15 2.17 1202.53 0.00 235.89 43.15 301.91 2960 10.72 1176.04 223.22 195.07 43.12 2.22 1200.24 0.00 235.85 43.12 301.90 2970 11.24 1175.52 296.82 192.76 43.09 2.08 1198.37 0.00 235.81 43.09 301.90 2980 11.56 1174.62 272.49 191.73 43.06 2.22 1196.87 0.00 235.76 43.06 301.90 2990 9.97 1175.47 240.42 189.17 43.03 2.80 1199.91 0.00 235.72 43.03 301.90 3000 10.14 1175.85 276.97 190.89 42.99 2.39 1201.57 0.00 235.68 43.00 301.91 3010 10.85 1174.77 266.93 192.80 42.95 2.43 1199.28 0.00 235.60 42.95 301.91 3020 10.78 1173.96 266.06 192.12 42.91 2.48 1196.46 0.00 235.53 42.90 301.91 3030 11.91 1174.53 280.03 189.86 42.85 2.13 1196.89 0.00 235.45 42.85 301.91 3040 11.60 1175.13 245.12 188.77 42.80 2.09 1200.95 0.00 235.38 42.80 301.91 3050 11.44 1175.69 246.09 192.54 42.75 2.23 1199.19 0.00 235.31 42.75 301.91 3060 11.98 1175.67 265.08 189.70 42.70 2.19 1199.65 0.00 235.24 42.70 301.91 3070 12.01 1174.81 245.72 189.16 42.65 1.81 1201.45 0.00 235.16 42.65 301.91 3080 11.90 1175.41 233.14 191.81 42.60 1.84 1198.47 0.00 235.09 42.60 301.91 3090 11.89 1175.40 249.55 189.99 42.56 2.20 1199.12 0.00 235.02 42.55 301.91 3100 12.42 1174.95 274.15 189.16 42.50 2.30 1201.26 0.00 234.94 42.50 301.91 3110 11.31 1175.87 250.18 187.79 42.45 2.38 1199.56 0.00 234.87 42.45 301.91 3120 9.81 1175.20 226.87 188.25 42.40 2.22 1198.76 0.00 234.80 42.40 301.91

Oconee Nuclear Station UFSAR Table 6-30 (Page 29 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 3130 10.76 1173.55 252.44 191.54 42.35 2.18 1196.63 0.00 234.72 42.35 301.91 3140 10.61 1173.91 231.81 192.09 42.31 2.43 1198.10 0.00 234.65 42.30 301.91 3150 10.67 1175.36 243.62 190.04 42.25 2.06 1201.22 0.00 234.57 42.25 301.91 3160 11.37 1175.07 252.60 188.47 42.19 2.12 1199.26 0.00 234.50 42.20 301.91 3170 9.44 1174.08 237.32 184.24 42.13 2.50 1201.13 0.00 234.43 42.15 301.91 3180 10.16 1174.22 278.28 186.96 42.11 2.00 1199.73 0.00 234.36 42.10 301.91 3190 11.88 1174.80 281.80 188.48 42.05 2.04 1194.80 0.00 234.28 42.05 301.91 3200 10.94 1174.60 259.80 186.33 42.01 2.72 1198.03 0.00 234.21 42.00 301.91 3210 11.29 1174.51 270.78 189.28 41.96 2.31 1197.94 0.00 234.13 41.95 301.91 3220 11.79 1175.02 272.52 186.86 41.88 1.96 1196.61 0.00 234.06 41.90 301.91 3230 11.18 1174.45 247.16 184.92 41.83 2.58 1199.79 0.00 233.98 41.85 301.91 3240 11.76 1174.89 255.00 189.21 41.81 2.15 1199.01 0.00 233.91 41.80 301.91 3250 12.15 1175.34 258.45 185.20 41.74 1.79 1198.39 0.00 233.84 41.75 301.91 3260 10.98 1174.26 232.62 182.65 41.67 2.49 1201.26 0.00 233.76 41.70 301.91 3270 10.09 1174.60 229.02 189.72 41.65 2.84 1201.43 0.00 233.69 41.65 301.91 3280 11.21 1175.25 259.39 190.17 41.60 2.27 1199.10 0.00 233.61 41.60 301.91 3290 11.05 1174.29 237.82 186.57 41.55 2.10 1199.82 0.00 233.54 41.55 301.91 3300 9.52 1173.82 223.23 190.19 41.51 2.37 1202.43 0.00 233.46 41.50 301.91 3310 10.85 1174.76 262.36 194.21 41.45 2.18 1199.64 0.00 233.39 41.45 301.91 3320 11.71 1174.76 278.39 188.92 41.40 2.04 1198.48 0.00 233.31 41.40 301.91

Oconee Nuclear Station UFSAR Table 6-30 (Page 30 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 3330 11.45 1173.77 283.97 184.57 41.35 2.00 1200.66 0.00 233.24 41.35 301.91 3340 10.98 1173.70 253.54 186.97 41.23 2.39 1200.86 0.00 233.16 41.30 301.91 3350 10.40 1173.84 238.19 192.40 41.25 2.49 1200.87 0.00 233.09 41.25 301.91 3360 11.72 1173.56 280.22 192.54 41.20 2.38 1199.29 0.00 233.01 41.20 301.91 3370 12.35 1174.15 309.63 188.37 41.15 2.24 1199.26 0.00 232.93 41.15 301.91 3380 10.98 1173.75 271.47 187.54 41.10 2.06 1201.13 0.00 232.86 41.10 301.91 3390 11.35 1172.80 257.33 192.04 41.01 2.03 1197.94 0.00 232.78 41.05 301.91 3400 11.89 1173.28 284.53 187.19 41.00 2.04 1197.32 0.00 232.71 41.00 301.91 3410 10.48 1173.17 253.59 182.37 40.95 2.38 1200.25 0.00 232.63 40.95 301.91 3420 9.87 1172.69 225.14 189.86 40.90 2.45 1200.19 0.00 232.56 40.90 301.91 3430 11.02 1173.17 250.89 190.08 40.85 2.22 1196.80 0.00 232.48 40.85 301.91 3440 11.53 1173.16 273.45 183.56 40.80 2.04 1195.69 0.00 232.40 40.80 301.91 3450 10.31 1172.61 251.21 184.09 40.75 2.23 1200.09 0.00 232.33 40.75 301.91 3460 9.87 1173.07 230.68 190.11 40.70 2.26 1201.45 0.00 232.25 40.70 301.91 3470 11.17 1173.39 247.89 189.20 40.65 2.06 1199.01 0.00 232.18 40.65 301.91 3480 10.27 1173.42 238.36 185.45 40.60 2.24 1199.52 0.00 232.10 40.60 301.91 3490 9.49 1173.67 233.68 188.23 40.55 2.11 1201.82 0.00 232.02 40.55 301.91 3500 11.04 1173.69 263.30 188.84 40.49 2.05 1197.76 0.00 231.95 40.50 301.91 3510 10.55 1173.12 258.89 185.97 40.43 2.04 1197.49 0.00 231.87 40.45 301.91 3520 10.51 1172.61 258.87 186.41 40.40 2.05 1198.80 0.00 231.80 40.40 301.91

Oconee Nuclear Station UFSAR Table 6-30 (Page 31 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 3530 11.16 1172.76 279.20 184.26 40.35 2.19 1197.73 0.00 231.72 40.35 301.91 3540 9.47 1172.40 243.04 183.41 40.31 2.14 1200.30 0.00 231.64 40.30 301.91 3550 9.56 1172.24 225.68 188.63 40.25 1.91 1202.55 0.00 231.56 40.25 301.91 3560 10.95 1172.36 254.66 187.57 40.21 2.00 1199.87 0.00 231.49 40.20 301.91 3570 9.27 1172.45 229.46 182.82 40.15 2.26 1199.84 0.00 231.41 40.15 301.92 3580 9.86 1172.80 230.74 188.24 40.10 1.85 1202.37 0.00 231.33 40.10 301.91 3590 11.01 1172.95 258.78 189.85 40.04 2.02 1198.04 0.00 231.26 40.05 301.91 3600 8.87 1173.06 244.76 184.16 40.00 2.34 1198.71 0.00 231.18 40.00 301.92 3610 9.66 1172.73 267.47 188.44 39.93 1.76 1202.65 0.00 231.10 39.95 301.91 3620 10.89 1172.39 266.96 190.79 39.89 1.99 1200.09 0.00 231.02 39.90 301.91 3630 8.89 1172.53 250.00 185.78 39.82 2.44 1200.71 0.00 230.95 39.85 301.91 3640 9.60 1172.69 277.46 186.87 39.80 1.78 1201.49 0.00 230.87 39.80 301.92 3650 10.61 1172.42 259.62 187.01 39.76 2.03 1199.20 0.00 230.79 39.75 301.92 3660 8.63 1172.37 245.75 184.84 39.69 2.45 1201.23 0.00 230.72 39.70 301.92 3670 9.58 1172.57 272.09 187.39 39.66 1.69 1200.90 0.00 230.64 39.65 301.92 3680 10.56 1172.26 257.78 186.84 39.61 2.01 1198.09 0.00 230.56 39.60 301.92 3690 8.52 1172.17 243.60 185.49 39.56 2.51 1201.14 0.00 230.48 39.55 301.92 3700 9.29 1172.47 269.74 186.50 39.51 1.78 1199.23 0.00 230.41 39.50 301.92 3710 10.62 1172.17 279.28 183.99 39.45 1.72 1193.49 0.00 230.33 39.45 301.92 3720 9.70 1171.83 253.68 182.34 39.41 2.43 1198.44 0.00 230.25 39.40 301.92

Oconee Nuclear Station UFSAR Table 6-30 (Page 32 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 3730 8.49 1171.85 242.06 183.93 39.36 2.65 1201.59 0.00 230.17 39.35 301.92 3740 9.35 1171.80 269.87 185.29 39.31 1.96 1199.08 0.00 230.09 39.30 301.92 3750 10.22 1171.70 263.03 184.42 39.25 2.21 1197.26 0.00 230.02 39.25 301.92 3760 10.74 1172.05 261.15 186.25 39.21 1.92 1196.64 0.00 229.94 39.20 301.92 3770 10.79 1172.45 248.31 186.01 39.14 1.76 1197.44 0.00 229.86 39.15 301.92 3780 8.65 1172.62 233.27 184.47 39.10 2.45 1202.15 0.00 229.78 39.10 301.92 3790 9.43 1172.48 271.43 184.97 39.04 1.73 1198.62 0.00 229.70 39.05 301.92 3800 10.57 1172.00 275.24 182.16 38.96 1.61 1193.60 0.00 229.62 39.00 301.92 3810 9.56 1171.51 253.48 182.76 38.95 2.32 1200.18 0.00 229.54 38.95 301.92 3820 8.21 1171.63 245.66 185.51 38.91 2.50 1203.09 0.00 229.46 38.90 301.92 3830 9.47 1172.09 263.98 186.24 38.85 1.76 1199.94 0.00 229.39 38.85 301.92 3840 10.17 1171.87 249.10 183.42 38.80 1.93 1198.00 0.00 229.31 38.80 301.92 3850 7.95 1171.64 232.95 182.63 38.72 2.45 1201.86 0.00 229.23 38.75 301.92 3860 9.05 1171.98 269.68 184.88 38.69 1.80 1198.24 0.00 229.15 38.70 301.92 3870 10.19 1171.68 283.63 182.05 38.65 1.65 1194.28 0.00 229.07 38.65 301.92 3880 9.07 1171.29 257.36 180.86 38.60 2.37 1199.05 0.00 228.99 38.60 301.92 3890 8.28 1171.48 238.84 184.94 38.53 2.60 1201.44 0.00 228.91 38.55 301.92 3900 9.73 1171.90 258.76 185.13 38.50 1.82 1198.38 0.00 228.83 38.50 301.92 3910 10.26 1171.61 249.68 183.10 38.43 1.95 1196.49 0.00 228.75 38.45 301.92 3920 8.19 1171.33 239.06 184.13 38.39 2.51 1201.56 0.00 228.67 38.40 301.92

Oconee Nuclear Station UFSAR Table 6-30 (Page 33 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 3930 9.26 1171.75 267.74 184.79 38.33 1.71 1198.80 0.00 228.59 38.35 301.92 3940 10.34 1171.57 274.24 182.10 38.28 1.52 1193.40 0.00 228.51 38.30 301.92 3950 9.31 1171.18 249.18 180.42 38.25 2.36 1199.07 0.00 228.43 38.25 301.92 3960 8.41 1171.22 236.40 184.16 38.21 2.61 1201.60 0.00 228.35 38.20 301.92 3970 9.49 1171.60 262.67 185.68 38.16 1.82 1199.09 0.00 228.27 38.15 301.92 3980 10.19 1171.41 254.87 183.44 38.10 1.98 1197.48 0.00 228.19 38.10 301.92 3990 8.31 1171.13 233.62 182.92 38.06 2.48 1200.93 0.00 228.11 38.05 301.92 4000 9.27 1171.57 265.68 185.35 38.01 1.60 1199.94 0.00 228.03 38.00 301.92 4010 9.95 1171.42 261.01 184.42 37.98 1.95 1197.56 0.00 228.00 37.98 301.92 4020 7.83 1171.15 231.08 181.53 37.96 2.45 1200.64 0.00 227.96 37.96 301.92 4030 8.32 1171.46 262.98 182.16 37.95 1.66 1199.92 0.00 227.93 37.94 301.92 4040 9.58 1171.38 279.54 181.17 37.93 1.71 1194.91 0.00 227.90 37.92 301.92 4050 9.63 1171.29 243.89 180.34 37.90 1.96 1196.73 0.00 227.87 37.90 301.92 4060 9.22 1171.41 250.01 179.99 37.86 2.12 1198.53 0.00 227.84 37.88 301.92 4070 7.81 1171.39 245.93 178.64 37.86 2.41 1199.85 0.00 227.80 37.86 301.92 4080 8.57 1171.10 232.45 182.74 37.84 1.94 1201.65 0.00 227.77 37.84 301.92 4090 9.49 1171.31 270.79 182.32 37.83 2.00 1196.98 0.00 227.74 37.82 301.92 4100 7.93 1171.58 259.83 177.64 37.80 2.53 1197.61 0.00 227.70 37.80 301.92 4110 7.80 1171.16 245.77 179.51 37.79 2.12 1201.20 0.00 227.67 37.78 301.92 4120 8.83 1171.19 278.95 181.37 37.76 1.92 1197.70 0.00 227.64 37.76 301.92

Oconee Nuclear Station UFSAR Table 6-30 (Page 34 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 4130 9.40 1171.32 294.00 180.76 37.74 2.14 1197.71 0.00 227.61 37.74 301.92 4140 8.84 1171.05 259.29 181.26 37.72 2.35 1200.85 0.00 227.58 37.72 301.92 4150 7.81 1170.92 236.50 182.66 37.70 2.24 1201.08 0.00 227.54 37.70 301.92 4160 8.71 1171.34 269.84 180.62 37.68 2.01 1197.83 0.00 227.51 37.68 301.92 4170 9.78 1171.49 288.14 177.12 37.66 1.99 1195.90 0.00 227.48 37.66 301.92 4180 8.84 1171.25 251.75 177.17 37.63 2.27 1199.09 0.00 227.45 37.64 301.92 4190 7.64 1171.02 225.48 180.25 37.62 2.51 1200.45 0.00 227.41 37.62 301.92 4200 8.56 1171.15 259.92 181.14 37.61 1.79 1197.77 0.00 227.38 37.60 301.92 4210 8.83 1171.04 260.28 180.29 37.58 1.98 1198.06 0.00 227.35 37.58 301.92 4220 7.68 1170.80 231.08 180.48 37.56 2.53 1200.87 0.00 227.32 37.56 301.92 4230 8.64 1171.13 260.93 181.44 37.51 1.72 1197.92 0.00 227.28 37.54 301.92 4240 8.86 1171.02 262.73 181.09 37.49 1.93 1197.24 0.00 227.26 37.52 301.92 4250 7.42 1170.73 231.38 180.81 37.50 2.65 1200.46 0.00 227.22 37.50 301.92 4260 8.01 1171.01 262.96 182.08 37.48 1.96 1198.33 0.00 227.19 37.48 301.92 4270 8.72 1170.94 285.16 181.24 37.46 1.56 1194.49 0.00 227.16 37.46 301.92 4280 8.44 1170.61 247.85 181.18 37.45 2.27 1198.63 0.00 227.12 37.44 301.92 4290 7.80 1170.67 228.28 181.93 37.42 2.59 1200.44 0.00 227.09 37.42 301.92 4300 8.35 1170.99 247.21 181.42 37.40 1.80 1199.75 0.00 227.06 37.40 301.92 4310 8.52 1170.99 252.46 180.96 37.37 1.94 1199.63 0.00 227.02 37.38 301.92 4320 7.62 1170.79 234.23 180.11 37.33 2.62 1200.60 0.00 226.99 37.36 301.92

Oconee Nuclear Station UFSAR Table 6-30 (Page 35 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 4330 8.43 1170.95 249.61 182.54 37.33 1.97 1200.64 0.00 226.96 37.34 301.92 4340 8.73 1171.02 269.58 182.15 37.29 1.85 1197.56 0.00 226.93 37.32 301.92 4350 8.42 1170.71 275.62 179.86 37.30 2.30 1197.67 0.00 226.89 37.30 301.92 4360 7.78 1170.69 267.45 179.40 37.28 2.41 1199.53 0.00 226.86 37.28 301.92 4370 7.85 1170.66 252.31 179.68 37.26 2.07 1200.66 0.00 226.83 37.26 301.92 4380 8.70 1170.86 276.49 179.26 37.23 1.93 1198.14 0.00 226.80 37.24 301.92 4390 8.21 1171.02 268.59 178.83 37.22 2.26 1197.91 0.00 226.76 37.22 301.92 4400 8.19 1170.81 265.48 178.96 37.21 2.13 1199.06 0.00 226.73 37.20 301.92 4410 8.20 1170.76 256.66 179.61 37.18 2.17 1199.36 0.00 226.70 37.18 301.93 4420 9.08 1170.85 238.18 182.57 37.16 2.01 1199.14 0.00 226.67 37.16 301.93 4430 9.68 1170.75 219.16 183.90 37.14 2.18 1199.48 0.00 226.63 37.14 301.93 4440 9.09 1170.61 183.19 187.03 37.09 2.63 1200.84 0.00 226.60 37.12 301.93 4450 10.95 1171.02 203.00 187.54 37.11 1.77 1197.62 0.00 226.57 37.10 301.92 4460 11.53 1170.84 188.86 187.19 37.06 1.77 1197.09 0.00 226.54 37.08 301.93 4470 10.30 1170.51 149.90 192.53 37.07 2.48 1200.49 0.00 226.50 37.06 301.92 4480 11.30 1170.70 166.68 194.43 37.04 1.90 1199.90 0.00 226.47 37.04 301.92 4490 11.98 1170.96 206.84 189.31 37.02 1.94 1197.44 0.00 226.44 37.02 301.92 4500 11.31 1171.09 209.05 186.73 37.00 2.35 1198.85 0.00 226.40 37.00 301.93 4510 11.75 1171.37 213.42 185.15 36.98 2.06 1200.17 0.00 226.37 36.98 301.93 4520 11.15 1171.45 199.03 182.99 36.96 2.19 1200.78 0.00 226.34 36.96 301.93

Oconee Nuclear Station UFSAR Table 6-30 (Page 36 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 4530 11.20 1171.08 178.13 186.70 36.94 1.62 1199.63 0.00 226.31 36.94 301.93 4540 11.64 1171.08 161.19 191.30 36.92 1.69 1200.28 0.00 226.27 36.92 301.93 4550 10.37 1171.17 151.73 191.07 36.88 2.67 1201.38 0.00 226.24 36.90 301.92 4560 10.79 1171.34 173.37 193.32 36.88 2.43 1200.64 0.00 226.20 36.88 301.93 4570 10.97 1171.65 194.79 195.90 36.86 1.76 1200.82 0.00 226.17 36.86 301.93 4580 10.96 1171.31 200.58 201.77 36.84 1.98 1201.21 0.00 226.14 36.84 301.93 4590 11.05 1171.47 177.91 203.20 36.82 2.58 1200.99 0.00 226.11 36.82 301.93 4600 10.51 1172.67 170.85 197.66 36.80 2.54 1200.77 0.00 226.07 36.80 301.93 4610 10.78 1173.10 187.47 196.40 36.78 2.28 1200.15 0.00 226.04 36.78 301.93 4620 11.62 1172.95 226.93 191.94 36.76 2.02 1197.61 0.00 226.01 36.76 301.93 4630 11.50 1172.03 205.17 191.31 36.74 2.23 1198.60 0.00 225.97 36.74 301.93 4640 10.31 1171.54 170.63 189.53 36.72 2.57 1200.30 0.00 225.94 36.72 301.93 4650 11.19 1171.65 193.55 189.14 36.70 1.64 1197.90 0.00 225.91 36.70 301.93 4660 11.65 1170.83 179.24 192.84 36.68 1.59 1198.06 0.00 225.88 36.68 301.93 4670 10.55 1170.33 152.38 193.82 36.65 2.60 1200.44 0.00 225.84 36.66 301.93 4680 10.34 1171.21 155.21 194.04 36.64 2.53 1200.68 0.00 225.81 36.64 301.93 4690 11.01 1172.55 189.43 192.97 36.62 1.97 1199.58 0.00 225.77 36.62 301.93 4700 11.96 1172.31 206.45 192.35 36.60 1.68 1197.70 0.00 225.74 36.60 301.93 4710 11.04 1172.09 192.96 190.64 36.58 2.20 1199.62 0.00 225.71 36.58 301.93 4720 8.36 1171.58 141.13 186.65 36.56 1.90 1201.74 0.00 225.68 36.56 301.93

Oconee Nuclear Station UFSAR Table 6-30 (Page 37 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 4730 7.88 1169.89 149.45 193.70 36.54 1.75 1205.09 0.00 225.64 36.54 301.93 4740 10.20 1169.97 196.81 199.19 36.52 2.07 1203.34 0.00 225.61 36.52 301.93 4750 12.21 1170.61 213.27 192.22 36.50 1.93 1198.06 0.00 225.58 36.50 301.93 4760 11.78 1170.83 205.44 184.99 36.48 2.27 1197.56 0.00 225.54 36.48 301.93 4770 12.33 1170.70 173.88 188.62 36.39 1.56 1196.97 0.00 225.51 36.46 301.93 4780 12.95 1170.99 155.65 194.43 36.45 1.57 1197.99 0.00 225.48 36.44 301.93 4790 11.51 1171.13 130.54 198.92 36.41 2.46 1200.27 0.00 225.44 36.42 301.93 4800 11.31 1171.13 142.54 201.12 36.40 2.42 1200.97 0.00 225.41 36.40 301.93 4810 12.07 1171.12 164.12 200.56 36.38 2.06 1200.60 0.00 225.38 36.38 301.93 4820 12.76 1171.64 184.21 200.05 36.36 2.00 1199.69 0.00 225.34 36.36 301.93 4830 12.12 1171.61 167.15 201.13 36.34 2.48 1200.21 0.00 225.31 36.34 301.93 4840 11.29 1170.67 154.12 202.44 36.32 2.57 1201.25 0.00 225.28 36.32 301.93 4850 11.51 1170.75 168.96 204.22 36.30 2.36 1201.23 0.00 225.24 36.30 301.93 4860 12.62 1171.65 200.72 203.69 36.28 2.03 1200.84 0.00 225.21 36.28 301.93 4870 12.30 1171.85 196.58 202.07 36.26 2.26 1200.88 0.00 225.17 36.26 301.93 4880 11.02 1171.47 160.80 203.24 36.24 2.61 1200.99 0.00 225.14 36.24 301.93 4890 10.97 1171.48 153.73 206.70 36.22 2.60 1200.96 0.00 225.11 36.22 301.93 4900 11.71 1171.59 171.45 206.11 36.20 2.07 1200.23 0.00 225.07 36.20 301.93 4910 12.14 1172.28 241.08 193.92 36.18 1.96 1200.19 0.00 225.04 36.18 301.93 4920 12.09 1172.20 259.43 186.75 36.16 1.90 1200.09 0.00 225.01 36.16 301.93

Oconee Nuclear Station UFSAR Table 6-30 (Page 38 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 4930 11.78 1170.56 177.50 187.97 36.14 2.00 1201.03 0.00 224.98 36.14 301.93 4940 11.07 1170.22 131.88 194.56 36.12 2.57 1201.30 0.00 224.94 36.12 301.93 4950 10.44 1170.87 146.73 197.05 36.08 2.55 1200.62 0.00 224.91 36.10 301.93 4960 9.28 1170.35 168.33 193.04 36.09 2.56 1200.66 0.00 224.87 36.08 301.93 4970 10.49 1170.20 194.53 193.47 36.07 1.78 1199.38 0.00 224.84 36.06 301.93 4980 11.78 1171.05 219.17 191.43 36.03 1.71 1196.08 0.00 224.81 36.04 301.93 4990 11.55 1171.41 237.87 186.73 36.02 2.35 1197.99 0.00 224.78 36.02 301.93 5000 11.19 1170.78 212.91 185.92 36.00 2.50 1200.24 0.00 224.74 36.00 301.93 5010 11.55 1171.29 189.32 181.28 36.00 1.93 1199.96 0.00 224.74 36.00 301.93 5020 11.52 1171.51 169.65 183.67 35.99 1.82 1201.35 0.00 224.74 36.00 301.93 5030 11.46 1170.93 145.48 193.38 36.01 1.80 1200.60 0.00 224.74 36.00 301.93 5040 11.46 1170.45 166.49 190.35 36.02 1.68 1197.49 0.00 224.74 36.00 301.93 5050 10.59 1170.00 192.87 185.94 36.00 2.36 1199.12 0.00 224.74 36.00 301.93 5060 11.61 1171.96 218.48 184.14 36.00 2.18 1199.63 0.00 224.74 36.00 301.93 5070 11.24 1172.88 194.70 183.39 36.00 2.26 1200.01 0.00 224.74 36.00 301.93 5080 11.71 1171.18 147.68 189.98 35.99 1.38 1199.77 0.00 224.74 36.00 301.93 5090 12.03 1170.10 138.18 193.57 36.00 1.23 1197.64 0.00 224.74 36.00 301.93 5100 10.14 1169.74 143.77 189.99 35.98 2.30 1199.77 0.00 224.74 36.00 301.93 5110 10.68 1170.81 188.41 190.05 36.00 1.96 1200.69 0.00 224.74 36.00 301.93 5120 9.20 1170.84 164.15 195.10 36.00 1.76 1198.68 0.00 224.74 36.00 301.93

Oconee Nuclear Station UFSAR Table 6-30 (Page 39 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 5130 13.53 1169.80 252.02 204.92 36.01 2.21 1197.54 0.00 224.74 36.00 301.93 5140 15.88 1169.76 261.95 200.50 36.00 2.63 1196.93 0.00 224.74 36.00 301.93 5150 13.46 1169.68 103.37 187.50 36.00 2.53 1195.41 0.00 224.74 36.00 301.93 5160 16.09 1170.32 95.15 188.75 35.98 1.66 1194.54 0.00 224.74 36.00 301.93 5170 16.14 1171.89 125.64 191.39 36.00 1.95 1196.84 0.00 224.74 36.00 301.93 5180 14.95 1173.17 145.74 191.47 36.00 2.56 1198.26 0.00 224.74 36.00 301.93 5190 15.00 1174.01 174.95 190.73 36.00 2.10 1198.94 0.00 224.74 36.00 301.93 5200 14.62 1174.12 172.55 191.32 36.00 2.36 1199.30 0.00 224.74 36.00 301.93 5210 14.50 1174.05 169.77 189.21 36.00 1.95 1199.56 0.00 224.74 36.00 301.93 5220 15.67 1173.70 171.43 194.64 36.01 1.34 1201.72 0.00 224.74 36.00 301.93 5230 15.48 1172.72 184.42 194.20 35.99 1.90 1201.36 0.00 224.74 36.00 301.93 5240 14.99 1173.54 233.19 186.76 36.00 2.28 1198.78 0.00 224.74 36.00 301.93 5250 14.92 1174.05 212.67 182.95 36.00 1.68 1197.46 0.00 224.74 36.00 301.93 5260 14.44 1172.88 145.09 188.87 36.00 1.89 1200.03 0.00 224.74 36.00 301.93 5270 14.40 1172.38 138.45 196.72 35.99 2.15 1200.55 0.00 224.74 36.00 301.93 5280 14.20 1173.00 170.10 190.18 36.00 1.79 1198.82 0.00 224.74 36.00 301.93 5290 12.57 1172.25 182.66 188.98 36.00 2.35 1199.72 0.00 224.74 36.00 301.93 5300 11.66 1171.87 180.78 184.95 36.00 2.56 1199.57 0.00 224.74 36.00 301.93 5310 11.66 1172.21 127.89 190.13 36.00 1.22 1198.03 0.00 224.74 36.00 301.93 5320 13.07 1169.96 185.42 212.05 35.98 1.34 1196.44 0.01 224.74 36.00 301.93

Oconee Nuclear Station UFSAR Table 6-30 (Page 40 of 40)

(31 DEC 2003)

Reactor Vessel Side Pump Discharge Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy Btu/lbm)

Pressure (psi)

Spilled HPI Flow (gpm) 5330 16.16 1168.56 177.12 215.15 35.96 2.60 1189.95 0.01 230.08 36.00 301.93 5340 16.29 1169.11 101.32 198.85 36.00 2.44 1189.32 0.00 224.74 36.00 301.93 5350 15.15 1170.34 158.45 180.98 36.00 2.09 1197.23 0.00 224.74 36.00 301.93 5360 14.68 1171.32 147.86 178.48 36.00 2.13 1199.31 0.00 224.74 36.00 301.93 5370 14.76 1171.98 117.27 186.78 36.00 1.66 1199.23 0.00 224.74 36.00 301.93 5380 15.86 1172.83 158.02 192.27 36.00 1.70 1196.44 0.00 224.74 36.00 301.93 5390 15.44 1173.84 201.41 190.11 36.00 2.35 1196.62 0.00 224.74 36.00 301.93 5400 13.60 1174.34 195.33 186.41 36.00 2.55 1198.57 0.00 224.74 36.00 301.93 5410 13.68 1173.84 181.14 183.49 36.00 1.92 1199.56 0.00 224.74 36.00 301.93 5420 15.41 1172.81 149.62 190.78 35.98 1.17 1201.90 0.00 224.74 36.00 301.93 5430 14.90 1173.15 154.24 194.17 35.99 2.03 1200.15 0.00 224.74 36.00 301.93 5440 13.31 1174.10 194.49 187.81 36.00 2.62 1199.03 0.00 224.74 36.00 301.93 5450 13.25 1175.02 215.33 182.62 36.00 2.30 1199.91 0.00 224.74 36.00 301.93 5460 14.59 1173.67 166.76 186.09 36.00 1.45 1199.67 0.00 224.74 36.00 301.93 5466.85 15.50 1171.05 70.54 218.83 36.00 0.58 1198.07 0.00 224.74 36.00 301.93

Oconee Nuclear Station UFSAR Table 6-31 (Page 1 of 2)

(31 DEC 2017)

Table 6-31. BFLOW/FATHOMS Long-Term Mass and Energy Releases Time (sec)

Time (Days)

Steam Flow (lbm/sec)

Steam Enthalpy (Btu/lbm)

Bk liq flow (lbm/sec)

Liquid Enthalpy (Btu/lbm) 4561 25.24 1163.93 358.19 170.13 4811 24.63 1164.56 350.28 169.97 7211 19.56 1166.13 356.92 162.03 10012 18.25 1165.98 359.64 154.52 24012 15.16 1163.50 371.60 128.60 36013 13.98 1161.70 373.59 117.93 49415 13.25 1160.26 374.87 110.18 72815 12.07 1158.49 376.61 102.09 87216 1.01 11.71 1157.80 377.19 98.73 2.1 9.86 1155.60 379.67 89.18 3.1 8.41 1154.24 381.39 85.79 4.0 7.41 1153.41 382.54 84.13 5.1 6.55 1152.74 383.52 82.85 6.1 5.91 1152.25 384.26 81.81 7.0 5.36 1152.62 384.96 80.19 8.1 4.75 1153.15 386.07 74.55 9.0 4.45 1152.58 386.39 74.21 10.0 4.16 1152.16 386.69 73.98 11.1 3.91 1151.83 386.95 73.81 12.0 3.71 1151.57 387.16 73.69 13.0 3.51 1151.33 386.91 73.59 14.1 3.34 1151.13 387.10 73.49

Oconee Nuclear Station UFSAR Table 6-31 (Page 2 of 2)

(31 DEC 2017)

Time (sec)

Time (Days)

Steam Flow (lbm/sec)

Steam Enthalpy (Btu/lbm)

Bk liq flow (lbm/sec)

Liquid Enthalpy (Btu/lbm) 15.0 3.19 1150.96 387.69 73.44 16.1 3.04 1150.79 387.84 73.38 17.1 2.91 1150.65 387.97 73.32 18.0 2.80 1150.53 386.18 73.29 19.1 2.69 1150.42 384.25 73.27 20.1 2.58 1150.31 388.32 73.18 21.0 2.49 1150.22 388.41 73.14 22.1 2.40 1150.13 388.51 73.11 23.0 2.32 1150.05 388.59 73.08 24.0 2.23 1149.98 388.67 73.05 25.1 2.16 1149.88 388.75 73.01 26.0 2.09 1149.79 388.82 72.98 27.1 2.02 1149.69 388.89 72.94 28.1 1.96 1149.60 384.45 72.96 29.0 1.90 1149.53 389.02 72.88 30.1 1.84 1149.45 389.08 72.85 31.1 1.78 1149.38 389.14 72.82 32.0 1.73 1149.31 389.19 72.80 33.1 1.68 1149.24 387.48 72.79 34.0 1.63 1149.18 389.29 72.75 35.0 1.57 1149.11 389.35 72.72 38

Oconee Nuclear Station UFSAR Table 6-32 (Page 1 of 5)

(31 DEC 2003)

Table 6-32. Steam Line Break Mass and Energy Releases for Double-Ended Guillotine Break Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia) 0.0 0.0 1261.9 944.1 2.1 6737.0 1270.7 834.7 4.2 3029.1 1275.1 784.7 0.1 16210.7 1262.9 933.9 2.2 6687.0 1270.8 833.4 4.3 2947.1 1275.2 783.2 0.2 11175.3 1265.2 909.5 2.3 6646.9 1271.0 831.8 4.4 2893.7 1275.3 781.8 0.3 9092.1 1266.6 895.2 2.4 6618.9 1271.1 830.0 4.5 2885.6 1275.3 780.2 0.4 8239.2 1267.5 884.4 2.5 6586.4 1271.4 827.3 4.6 2878.4 1275.3 778.4 0.5 8007.2 1268.1 876.9 2.6 6495.0 1271.6 824.4 4.7 2871.9 1275.4 776.1 0.6 8083.4 1268.6 871.5 2.7 6341.9 1271.9 821.6 4.8 2866.1 1275.6 773.8 0.7 8133.4 1268.9 867.3 2.8 6147.2 1272.0 818.8 4.9 2860.2 1275.8 771.5 0.8 8100.8 1269.1 863.6 2.9 5915.9 1272.2 816.1 5.0 2894.2 1276.0 769.4 0.9 7998.8 1269.3 860.4 3.0 5645.9 1272.4 813.3 5.5 2795.1 1276.6 759.4 1.0 7858.0 1269.6 856.9 3.1 5354.2 1272.6 810.7 6.0 2728.0 1277.4 743.2 1.1 7705.4 1269.9 853.0 3.2 5038.2 1272.7 808.3 6.5 2687.9 1277.7 724.7 1.2 7556.9 1270.2 849.0 3.3 4673.2 1272.9 806.1 7.0 2616.5 1277.3 712.3 1.3 7420.6 1270.5 845.3 3.4 4219.5 1273.1 803.7 7.5 2557.0 1277.7 693.3 1.4 7297.7 1270.7 842.3 3.5 3923.4 1273.3 801.4 8.0 2473.2 1277.6 674.9 1.5 7188.1 1270.7 840.0 3.6 3711.9 1273.6 798.6 8.5 2422.2 1277.4 658.9 1.6 7089.9 1270.7 838.1 3.7 3539.0 1273.9 795.7 9.0 2364.1 1276.5 649.7 1.7 7005.0 1270.6 837.4 3.8 3391.3 1274.1 793.2 9.5 2351.6 1275.2 644.6 1.8 6929.4 1270.6 837.0 3.9 3278.9 1274.4 790.9 10.0 2322.4 1273.9 639.7 1.9 6859.9 1270.5 836.4 4.0 3196.1 1274.6 788.7 10.5 2309.3 1272.6 635.2 2.0 6795.3 1270.6 835.7 4.1 3117.8 1274.9 786.5 11.0 2289.4 1271.4 630.2

Oconee Nuclear Station UFSAR Table 6-32 (Page 2 of 5)

(31 DEC 2003)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia) 11.5 2263.4 1270.4 623.9 22.5 2165.9 1252.6 569.4 33.5 1832.3 1244.4 495.4 12.0 2234.8 1269.8 616.0 23.0 2109.0 1248.9 574.6 34.0 1824.5 1244.1 493.4 12.5 2199.7 1269.3 609.2 23.5 2098.7 1247.4 575.6 34.5 1817.9 1243.8 491.3 13.0 2176.4 1268.9 602.6 24.0 2088.9 1247.0 572.6 35.0 1809.5 1243.4 489.2 13.5 2131.2 1269.1 591.1 24.5 2077.7 1246.8 567.0 35.5 1801.6 1242.9 487.1 14.0 2088.8 1269.3 579.4 25.0 2063.4 1246.7 560.7 36.0 1792.4 1242.4 484.8 14.5 2035.1 1269.3 569.9 25.5 2049.0 1246.6 554.6 36.5 1782.9 1241.9 482.3 15.0 2026.8 1268.6 568.5 26.0 2030.4 1246.4 548.5 37.0 1773.0 1241.5 479.7 15.5 2040.1 1267.4 571.8 26.5 2008.4 1246.3 542.8 37.5 1762.5 1241.1 477.0 16.0 2054.8 1266.1 575.8 27.0 1990.3 1246.2 537.7 38.0 1751.8 1240.7 474.1 16.5 2069.9 1265.0 579.6 27.5 1971.6 1246.1 532.8 38.5 1740.8 1240.4 471.1 17.0 2091.3 1263.9 582.9 28.0 1956.4 1245.9 528.3 39.0 1729.9 1240.1 468.2 17.5 2091.6 1263.1 583.0 28.5 1940.4 1245.8 524.3 39.5 1718.4 1239.8 465.1 18.0 2090.9 1262.7 580.1 29.0 1926.8 1245.6 520.6 40.0 1707.5 1239.5 462.1 18.5 2097.9 1262.1 577.6 29.5 1913.8 1245.5 517.5 40.5 1695.8 1239.3 458.9 19.0 2083.5 1261.5 575.2 30.0 1901.5 1245.3 514.3 41.0 1685.6 1239.1 455.9 19.5 2067.7 1260.8 574.1 30.5 1889.7 1245.2 511.0 41.5 1674.8 1238.9 453.0 20.0 2053.4 1260.2 573.3 31.0 1878.2 1245.2 507.9 42.0 1664.8 1238.8 449.9 20.5 2052.9 1259.4 572.2 31.5 1867.4 1245.1 504.8 42.5 1653.9 1238.6 447.1 21.0 2060.6 1258.6 569.7 32.0 1856.7 1245.0 502.1 43.0 1644.1 1238.4 444.6 21.5 2081.0 1257.6 566.8 32.5 1848.0 1244.8 499.8 43.5 1634.8 1238.3 442.1 22.0 2066.0 1256.3 565.5 33.0 1839.3 1244.6 497.6 44.0 1625.9 1238.1 440.1

Oconee Nuclear Station UFSAR Table 6-32 (Page 3 of 5)

(31 DEC 2003)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia) 44.5 1617.3 1238.0 437.7 56.0 1445.1 1235.1 391.5 79.0 1235.5 1231.0 338.7 45.0 1609.4 1237.8 436.3 57.0 1432.4 1234.9 388.9 80.0 1227.6 1230.9 336.5 45.5 1602.7 1237.6 434.3 59.0 1412.0 1234.4 384.5 81.0 1219.2 1230.8 334.4 46.0 1595.5 1237.4 432.5 60.0 1403.8 1234.1 382.9 82.0 1210.9 1230.6 332.3 46.5 1589.0 1237.3 430.4 61.0 1396.1 1233.8 380.9 83.0 1203.1 1230.5 330.4 47.0 1582.0 1237.0 429.0 62.0 1387.7 1233.5 378.9 85.0 1188.4 1230.4 326.3 47.5 1575.5 1236.9 426.8 63.0 1378.7 1233.3 376.2 86.0 1181.2 1230.3 324.3 48.0 1568.3 1236.7 424.8 64.0 1369.2 1233.1 373.3 87.0 1173.5 1230.2 322.3 48.5 1561.9 1236.5 423.3 65.0 1358.7 1233.1 370.6 88.0 1165.9 1230.0 320.4 49.0 1554.6 1236.3 421.3 66.0 1348.7 1233.0 368.0 89.0 1158.6 1229.7 318.7 49.5 1547.4 1236.1 419.5 67.0 1338.3 1233.0 364.4 90.0 1150.9 1229.4 316.6 50.0 1540.0 1236.0 417.6 68.0 1326.6 1232.9 361.2 91.0 1142.4 1229.1 314.2 50.5 1532.4 1235.9 414.8 69.0 1317.5 1232.8 359.4 92.0 1133.3 1228.8 312.2 51.0 1524.4 1235.8 412.4 70.0 1309.8 1232.5 357.5 93.0 1123.3 1228.5 309.1 51.5 1515.7 1235.7 410.4 71.0 1302.9 1232.2 356.0 94.0 1112.9 1228.2 306.6 52.0 1507.3 1235.6 408.2 72.0 1294.8 1232.1 353.7 95.0 1102.1 1227.8 303.7 52.5 1499.5 1235.5 406.3 73.0 1285.4 1232.0 351.4 96.0 1090.8 1227.5 301.1 53.0 1491.6 1235.4 404.2 74.0 1275.8 1231.9 348.9 97.0 1078.3 1226.9 297.8 53.5 1483.5 1235.3 401.9 75.0 1266.3 1231.7 346.5 98.0 1064.5 1226.4 294.4 54.0 1475.3 1235.2 400.1 76.0 1257.7 1231.6 344.4 99.0 1051.0 1226.0 291.0 54.5 1466.7 1235.2 397.8 77.0 1250.1 1231.4 342.4 100.0 1039.2 1226.0 287.9 55.0 1459.7 1235.1 396.0 78.0 1242.9 1231.2 340.8 101.0 1028.7 1226.6 283.8

Oconee Nuclear Station UFSAR Table 6-32 (Page 4 of 5)

(31 DEC 2003)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia) 102.0 1019.3 1227.2 280.9 124.0 895.0 1220.9 252.5 146.0 709.1 1222.7 206.6 103.0 1009.5 1227.8 277.7 125.0 886.7 1220.4 250.6 147.0 681.2 1223.4 202.9 104.0 1000.0 1228.1 274.9 126.0 878.0 1220.3 248.4 148.0 714.2 1223.9 198.7 105.0 991.5 1227.9 273.2 127.0 871.4 1220.5 246.6 149.0 689.0 1223.9 194.5 106.0 984.6 1227.3 272.3 128.0 867.7 1220.8 244.9 150.0 662.3 1224.0 190.2 107.0 977.9 1226.5 271.5 129.0 863.1 1221.0 243.1 151.0 640.4 1224.1 184.7 108.0 971.1 1225.7 270.4 130.0 855.0 1221.1 240.7 152.0 623.1 1224.1 178.6 109.0 964.3 1224.9 268.8 131.0 846.8 1220.9 238.7 153.0 607.7 1224.3 172.1 110.0 958.3 1224.5 267.1 132.0 838.0 1220.3 236.7 154.0 591.5 1225.0 164.6 111.0 951.9 1224.3 264.9 133.0 828.7 1219.8 234.1 155.0 571.4 1226.1 156.5 112.0 945.5 1224.3 262.8 134.0 819.0 1219.5 231.4 156.0 545.0 1227.4 147.4 113.0 938.6 1224.0 260.9 135.0 811.1 1219.6 229.1 157.0 511.4 1228.8 138.1 114.0 930.6 1223.7 259.2 136.0 804.5 1220.0 227.0 158.0 471.5 1230.1 128.1 115.0 924.6 1223.3 257.6 137.0 799.3 1220.4 225.5 159.0 429.0 1231.2 118.0 116.0 918.2 1223.4 256.2 138.0 795.6 1220.6 224.3 160.0 387.2 1232.2 107.8 117.0 911.6 1223.7 255.1 139.0 793.9 1220.4 223.6 161.0 346.1 1233.3 97.2 118.0 909.1 1224.0 254.7 140.0 781.4 1220.6 222.1 162.0 305.5 1234.5 86.1 119.0 910.5 1224.0 254.8 141.0 773.9 1220.5 220.3 163.0 275.5 1235.4 77.5 120.0 911.9 1223.6 255.3 142.0 765.9 1220.5 218.2 164.0 249.6 1236.1 70.5 121.0 911.2 1223.0 255.7 143.0 755.4 1220.6 215.4 165.0 224.6 1236.7 64.0 122.0 908.2 1222.4 255.3 144.0 743.9 1221.1 212.5 166.0 201.9 1237.5 57.6 123.0 902.3 1221.7 254.1 145.0 731.9 1221.9 209.5 167.0 195.1 1238.1 55.1

Oconee Nuclear Station UFSAR Table 6-32 (Page 5 of 5)

(31 DEC 2003)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia)

Time (sec)

Flow (lbm/sec)

Enthalpy (Btu/lbm)

Pressure (psia) 168.0 173.0 1239.5 49.5 177.0 55.7 1243.3 27.4 186.0 37.9 1245.2 27.8 169.0 151.3 1241.0 44.1 178.0 53.3 1243.3 27.6 187.0 37.0 1245.2 27.6 170.0 174.4 1240.9 49.1 179.0 51.4 1243.7 27.4 188.0 32.6 1245.2 27.5 171.0 154.1 1241.7 45.2 180.0 46.8 1244.3 27.3 190.0 32.4 1245.2 27.9 172.0 137.3 1242.3 40.9 181.0 43.0 1244.8 27.5 192.0 26.8 1245.3 27.6 173.0 122.7 1242.6 37.5 182.0 45.0 1245.1 27.7 194.0 28.3 1246.0 28.1 174.0 112.1 1242.8 34.7 183.0 43.6 1245.3 27.5 196.0 22.1 1246.9 27.8 175.0 98.5 1243.1 31.4 184.0 39.1 1245.3 27.3 198.0 25.0 1246.8 28.3 176.0 87.7 1243.3 28.6 185.0 35.3 1245.2 27.7 200.0 17.7 1246.5 27.9

Oconee Nuclear Station UFSAR Table 6-33 (Page 1 of 1)

(31 DEC 2005)

Table 6-33. NPSH Available and Required for LPI and BS Pumps (Limiting Flow Case)

Flow NPSHr NPSHa BS 1110 gpm 15.0 ft 21.33 ft LPI 3840 gpm 16.5 ft 18.09 ft Note:

The above information is currently being revised as part of the Reactor Building Emergency Sump Screen replacement project and will be replaced with updated valves at the completion of that effort.

Oconee Nuclear Station UFSAR Table 6-34 (Page 1 of 1)

(31 DEC 2008)

Table 6-34. Deleted Per 2008 Update

Oconee Nuclear Station UFSAR Table 6-35 (Page 1 of 18)

(31 DEC 2003)

Table 6-35. ROTSG Peak Pressure Mass and Energy Release Data Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 0.0 2952.54 1185.14 50071.66 586.96 2194.9 3246.74 1185.47 53239.03 586.22 2195.9 0.1 3252.01 1186.21 49158.25 582.61 1184.1 3591.04 1186.39 50260.68 580.74 1187.2 0.2 3480.73 1187.49 47758.00 578.56 1155.1 3667.39 1188.29 44940.82 575.74 1078.4 0.3 3491.71 1188.37 44815.42 576.24 1108.5 3528.65 1190.47 39264.74 574.99 1010.7 0.4 3572.82 1189.50 40849.95 571.75 1049.1 3814.95 1192.29 33527.03 569.28 962.7 0.5 3582.23 1190.37 38848.06 569.99 1033.8 4077.28 1194.93 30429.58 558.98 923.0 0.6 3603.98 1190.57 38417.86 569.85 1032.2 4555.21 1200.03 30843.14 537.92 849.1 0.7 3631.00 1190.50 38565.54 570.09 1034.6 4940.88 1203.72 31095.94 521.43 807.9 0.8 3681.98 1190.50 38455.83 570.10 1035.7 4877.74 1204.80 29888.32 515.67 776.7 0.9 3757.54 1190.61 37989.32 569.90 1031.9 4689.83 1205.30 29486.80 511.62 754.1 1.0 3857.08 1190.78 37278.62 569.65 1029.8 4451.19 1205.38 29643.73 509.03 742.1 1.1 3998.17 1191.12 36168.17 569.06 1022.8 4192.05 1205.19 30189.31 507.64 736.7 1.2 4164.63 1191.64 34711.18 567.89 1012.0 3936.15 1204.89 30906.12 506.99 735.4 1.3 4325.52 1192.23 33257.31 566.34 999.0 3706.45 1204.57 31632.17 506.74 735.9 1.4 4885.59 1195.32 32760.04 558.32 988.0 3515.74 1204.30 32257.22 506.65 736.9 1.5 5584.34 1199.42 30882.26 544.85 873.7 3370.40 1204.10 32701.09 506.54 737.3 1.6 5860.66 1201.32 29087.52 537.20 912.6 3273.78 1203.98 32895.95 506.36 737.1 1.7 6167.30 1203.04 28953.62 533.36 884.2 3214.41 1203.93 32897.65 506.07 736.0 1.8 6527.57 1205.91 27179.85 525.07 806.8 3178.33 1203.95 32817.10 505.55 733.3

Oconee Nuclear Station UFSAR Table 6-35 (Page 2 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 1.9 6729.14 1208.08 25068.96 517.96 766.6 3163.92 1204.06 32678.24 504.79 729.2 2.0 6928.72 1209.35 23784.28 515.08 758.2 3172.02 1204.22 32466.24 503.84 723.8 2.1 7030.19 1210.21 22869.40 512.77 733.3 3207.95 1204.43 32106.56 502.78 717.6 2.2 6979.55 1210.67 22385.05 510.46 724.0 3265.28 1204.66 31601.79 501.67 711.2 2.3 6907.46 1210.93 22100.22 508.65 713.2 3329.78 1204.92 31039.75 500.48 704.3 2.4 6861.16 1211.26 21717.82 506.83 703.7 3397.75 1205.19 30450.86 499.22 696.9 2.5 6859.45 1211.75 21169.86 504.92 692.3 3468.03 1205.48 29853.11 497.92 689.3 2.6 6897.89 1212.43 20433.47 502.80 679.2 3538.34 1205.78 29265.49 496.63 681.9 2.7 6946.79 1213.25 19584.63 500.40 663.8 3606.07 1206.08 28677.95 495.32 674.5 2.8 6972.43 1214.01 18804.56 497.95 648.7 3670.47 1206.40 28063.32 493.89 666.5 2.9 6965.69 1214.59 18207.22 495.77 636.2 3733.35 1206.74 27429.91 492.32 657.7 3.0 6929.04 1214.96 17795.66 493.90 625.8 3792.59 1207.12 26777.52 490.47 647.6 3.1 6864.79 1215.14 17567.74 492.36 617.9 3842.57 1207.49 26105.76 488.42 636.0 3.2 6784.36 1215.15 17506.03 491.21 612.8 3877.66 1207.82 25467.85 486.44 625.4 3.3 6698.04 1215.06 17543.30 490.34 609.6 3895.99 1208.09 24920.13 484.63 616.2 3.4 6605.71 1214.92 17611.35 489.54 606.6 3926.78 1208.38 24355.35 482.94 607.4 3.5 6506.09 1214.76 17695.64 488.72 603.7 3983.00 1208.74 23690.59 481.19 597.9 3.6 6399.97 1214.56 17815.95 487.95 601.1 4041.44 1209.13 23004.56 479.38 588.2 3.7 6291.48 1214.31 17985.53 487.32 599.3 4091.37 1209.50 22330.49 477.50 578.4 3.8 6189.08 1214.05 18192.78 486.90 598.9 4132.22 1209.86 21676.24 475.58 568.2

Oconee Nuclear Station UFSAR Table 6-35 (Page 3 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 3.9 6093.43 1213.81 18364.62 486.43 598.2 4166.94 1210.20 21051.50 473.67 558.5 4.0 6002.18 1213.65 18455.89 485.75 595.6 4197.72 1210.53 20464.28 471.84 549.2 4.1 5911.43 1213.51 18513.10 484.94 592.6 4223.01 1210.84 19912.58 470.07 540.3 4.2 5816.88 1213.37 18590.20 484.14 589.5 4242.05 1211.12 19393.09 468.34 531.6 4.3 5723.32 1213.20 18694.91 483.44 587.5 4255.78 1211.39 18902.81 466.64 523.3 4.4 5636.97 1213.05 18782.69 482.76 585.1 4265.65 1211.64 18437.72 464.97 515.2 4.5 5564.71 1212.95 18826.56 482.08 582.7 4272.74 1211.89 17995.82 463.35 507.6 4.6 5509.04 1212.91 18804.40 481.36 579.8 4277.21 1212.11 17578.40 461.79 499.9 4.7 5462.44 1212.92 18716.22 480.50 575.8 4278.83 1212.31 17196.05 460.31 493.2 4.8 5420.41 1212.96 18600.10 479.59 571.6 4275.28 1212.50 16828.26 458.83 486.3 4.9 5384.66 1213.01 18470.19 478.68 567.3 4271.12 1212.70 16445.34 457.27 479.1 5.0 5355.41 1213.09 18322.90 477.77 563.1 4271.49 1212.92 16042.20 455.68 471.8 5.1 5331.29 1213.19 18153.43 476.84 558.7 4276.89 1213.18 15619.78 454.08 464.4 5.2 5313.06 1213.31 17958.80 475.89 554.0 4287.63 1213.45 15191.15 452.52 457.0 5.3 5301.69 1213.46 17733.09 474.89 549.1 4300.49 1213.72 14774.33 451.03 450.1 5.4 5294.20 1213.64 17480.21 473.84 543.8 4312.15 1213.98 14377.30 449.60 443.4 5.5 5286.91 1213.82 17214.45 472.74 538.2 4322.38 1214.24 13995.30 448.20 437.0 5.6 5275.98 1214.00 16947.60 471.59 532.5 4331.98 1214.49 13619.61 446.82 430.6 5.7 5251.41 1214.14 16715.41 470.39 526.7 4341.53 1214.74 13244.54 445.44 424.3 5.8 5209.31 1214.20 16562.60 469.26 521.7 4351.99 1215.01 12866.73 444.06 417.9

Oconee Nuclear Station UFSAR Table 6-35 (Page 4 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 5.9 5158.60 1214.20 16472.15 468.24 517.5 4364.10 1215.30 12483.40 442.68 411.5 6.0 5106.65 1214.18 16399.34 467.29 513.6 4377.46 1215.62 12092.86 441.28 405.1 6.1 5058.53 1214.18 16312.48 466.33 509.7 4391.25 1215.96 11695.23 439.85 398.5 6.2 5021.41 1214.22 16171.40 465.30 505.4 4405.59 1216.32 11292.11 438.40 391.8 6.3 5008.39 1214.37 15923.55 464.18 500.1 4420.27 1216.70 10885.50 436.94 385.1 6.4 5028.54 1214.69 15526.34 462.92 493.6 4434.26 1217.10 10478.32 435.47 378.3 6.5 5073.99 1215.17 14990.52 461.44 485.4 4446.69 1217.50 10073.97 433.98 371.4 6.6 5131.58 1215.76 14374.32 459.81 476.3 4457.04 1217.91 9674.69 432.48 364.6 6.7 5192.27 1216.42 13736.12 458.12 466.8 4465.40 1218.32 9281.44 430.98 357.7 6.8 5249.12 1217.09 13113.67 456.44 457.3 4472.38 1218.73 8892.40 429.48 350.9 6.9 5296.99 1217.74 12529.17 454.80 448.2 4478.43 1219.16 8504.16 427.96 344.0 7.0 5332.93 1218.34 11994.73 453.20 439.6 4482.85 1219.62 8117.96 426.43 337.0 7.1 5356.00 1218.89 11511.85 451.64 431.4 4484.09 1220.10 7740.85 424.88 330.1 7.2 5366.87 1219.38 11074.62 450.09 423.4 4480.96 1220.57 7380.27 423.32 323.2 7.3 5367.60 1219.82 10674.91 448.55 415.8 4472.86 1221.03 7040.36 421.75 316.5 7.4 5360.53 1220.23 10304.23 447.02 408.4 4459.67 1221.46 6723.53 420.19 309.9 7.5 5347.24 1220.62 9952.78 445.47 401.1 4441.79 1221.87 6430.98 418.65 303.6 7.6 5329.40 1221.01 9610.96 443.89 393.9 4420.44 1222.25 6159.93 417.13 297.6 7.7 5309.32 1221.40 9272.87 442.29 386.5 4397.48 1222.62 5903.92 415.65 291.8 7.8 5289.64 1221.80 8939.86 440.72 379.4 4374.99 1222.97 5655.91 414.21 286.1

Oconee Nuclear Station UFSAR Table 6-35 (Page 5 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 7.9 5268.74 1222.20 8605.68 439.13 372.0 4354.75 1223.35 5409.71 412.83 280.6 8.0 5248.62 1222.62 8268.98 437.54 364.9 4337.88 1223.77 5160.27 411.50 275.1 8.1 5230.61 1223.05 7936.95 436.00 357.8 4324.49 1224.26 4904.01 410.20 269.7 8.2 5210.71 1223.48 7610.42 434.47 350.8 4314.28 1224.82 4639.68 408.94 264.2 8.3 5185.50 1223.90 7290.51 432.88 343.7 4306.97 1225.45 4368.42 407.72 258.6 8.4 5149.89 1224.29 6981.38 431.16 336.3 4301.07 1226.14 4090.33 406.52 253.0 8.5 5100.61 1224.64 6679.60 429.25 328.6 4294.15 1226.91 3802.16 405.28 247.1 8.6 5041.01 1224.99 6373.97 427.14 320.3 4284.88 1227.80 3496.22 403.95 240.7 8.7 4978.61 1225.36 6064.05 424.95 311.6 4274.21 1228.88 3160.36 402.53 233.6 8.8 4918.44 1225.77 5753.83 422.78 303.5 4264.47 1230.27 2780.89 401.03 225.7 8.9 4859.23 1226.22 5444.20 420.61 295.1 4251.25 1231.89 2383.49 399.48 216.8 9.0 4794.44 1226.62 5150.07 418.40 286.7 4228.88 1233.57 2005.01 397.92 208.0 9.1 4717.10 1226.84 4907.84 416.13 278.8 4188.11 1235.11 1676.80 396.21 199.4 9.2 4624.94 1226.89 4713.82 413.76 271.5 4112.29 1236.10 1442.54 394.02 191.3 9.3 4525.57 1226.87 4533.67 411.27 263.9 3998.83 1236.25 1317.06 391.19 183.9 9.4 4422.59 1226.80 4361.82 408.70 256.4 3861.17 1235.62 1286.28 387.94 177.7 9.5 4315.34 1226.64 4203.04 406.06 249.0 3715.11 1234.44 1319.44 384.55 172.6 9.6 4208.39 1226.45 4054.94 403.42 241.8 3573.79 1233.01 1380.84 381.29 168.3 9.7 4104.11 1226.25 3915.19 400.81 235.0 3445.38 1231.61 1443.70 378.29 164.5 9.8 4002.98 1226.03 3788.12 398.26 228.3 3332.54 1230.37 1493.29 375.59 161.1

Oconee Nuclear Station UFSAR Table 6-35 (Page 6 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 9.9 3908.74 1225.76 3686.30 395.90 222.8 3235.32 1229.36 1523.70 373.18 157.8 10.0 3801.62 1225.32 3605.12 393.31 217.0 3153.27 1228.60 1532.33 371.06 154.7 10.1 3687.34 1224.80 3519.22 385.59 210.5 3071.49 1227.93 1523.21 363.94 151.6 10.2 3598.56 1224.52 3405.70 383.18 205.0 2967.43 1226.83 1549.42 361.12 147.2 10.3 3531.04 1224.44 3275.64 381.14 199.7 2870.76 1225.59 1600.47 358.61 144.8 10.4 3452.24 1224.25 3152.52 378.85 194.4 2817.51 1225.22 1574.44 357.04 142.2 10.5 3373.12 1224.02 3041.46 376.54 188.9 2800.35 1225.91 1439.72 356.10 138.8 10.6 3318.92 1223.97 2937.43 374.82 185.2 2805.61 1227.46 1230.88 355.62 134.6 10.7 3269.83 1223.96 2833.32 373.22 181.2 2817.97 1229.48 997.89 355.40 130.1 10.8 3218.68 1223.93 2728.20 371.54 177.3 2819.66 1231.40 793.71 355.12 125.7 10.9 3169.92 1223.96 2615.11 369.88 173.3 2801.31 1232.76 646.69 354.42 121.7 11.0 3125.78 1224.06 2493.59 368.29 169.4 2769.07 1233.57 549.41 353.39 118.3 11.1 3082.71 1224.18 2371.39 366.71 165.5 2733.85 1234.12 477.96 352.30 115.4 11.2 3033.10 1224.22 2253.22 364.98 161.5 2701.95 1234.66 411.81 351.34 112.6 11.3 2978.77 1224.19 2143.80 363.14 157.3 2674.46 1235.34 340.97 350.52 109.9 11.4 2917.64 1224.00 2054.52 361.15 153.5 2655.81 1236.24 261.71 349.97 107.4 11.5 2828.28 1223.26 2024.93 358.55 149.4 2634.93 1237.07 183.28 349.40 105.1 11.6 2701.04 1221.73 2072.60 355.13 145.6 2591.18 1237.36 132.54 348.04 102.0 11.7 2555.45 1219.84 2134.30 351.21 141.0 2532.07 1237.23 110.37 346.19 99.0 11.8 2436.12 1218.47 2116.77 347.68 136.2 2469.99 1237.01 96.33 344.28 96.2

Oconee Nuclear Station UFSAR Table 6-35 (Page 7 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 11.9 2362.55 1218.10 1983.73 344.92 131.5 2387.35 1236.41 96.19 341.42 93.1 12.0 2299.06 1217.99 1823.81 342.21 125.6 2290.04 1235.13 128.95 337.94 88.7 12.1 2231.38 1217.45 1749.89 339.65 122.2 2214.12 1233.88 164.33 335.58 87.4 12.2 2156.97 1216.50 1740.04 337.15 119.1 2164.22 1233.34 169.13 333.89 85.3 12.3 2086.06 1215.54 1733.57 334.74 116.9 2115.02 1232.75 136.58 332.50 83.6 12.4 2000.08 1214.39 1719.46 331.65 113.3 1983.88 1227.32 85.18 328.13 89.1 12.5 1888.23 1212.76 1721.13 327.54 108.5 1842.30 1221.08 68.73 320.75 87.8 12.6 1790.06 1211.21 1731.31 323.87 104.3 1770.92 1219.50 84.20 318.18 87.0 12.7 1699.34 1209.85 1697.05 320.14 100.3 1696.64 1218.10 88.07 315.82 85.9 12.8 1635.43 1208.94 1652.94 317.23 96.5 1625.43 1218.07 69.02 313.51 84.1 12.9 1604.09 1208.60 1605.97 315.61 94.4 1597.64 1219.20 56.24 312.47 84.1 13.0 1562.55 1208.19 1524.04 313.36 91.8 1562.54 1218.43 60.74 311.14 83.7 13.1 1506.14 1207.46 1456.85 310.43 87.3 1478.04 1216.79 57.02 308.37 82.2 13.2 1426.02 1206.05 1435.39 306.58 83.5 1382.20 1215.66 50.38 304.67 80.9 13.3 1341.05 1204.34 1439.95 302.58 80.5 1271.34 1213.67 49.85 300.87 79.4 13.4 1284.05 1202.63 1427.75 300.78 77.8 1148.56 1212.05 44.11 296.93 77.9 13.5 1245.77 1201.26 1370.61 299.99 81.8 1055.04 1211.63 39.42 293.67 76.9 13.6 1219.57 1200.67 1313.42 298.86 80.6 992.54 1211.09 40.57 291.74 76.6 13.7 1176.63 1199.67 1294.43 297.08 79.7 921.42 1209.96 41.28 289.68 76.0 13.8 1109.17 1197.98 1281.82 294.30 77.6 847.66 1209.21 40.34 287.58 75.4

Oconee Nuclear Station UFSAR Table 6-35 (Page 8 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 13.9 1036.37 1196.13 1258.32 291.69 76.8 783.40 1208.74 40.25 285.91 75.1 14.0 958.19 1194.18 1229.61 289.47 76.2 706.24 1207.53 42.45 284.02 74.6 14.1 872.95 1192.17 1177.32 287.22 75.5 615.42 1205.51 47.28 282.05 74.4 14.2 788.89 1190.28 1097.60 285.16 75.0 520.17 1203.40 51.66 280.37 74.2 14.3 718.62 1188.80 999.35 283.60 74.7 398.36 1202.09 48.53 278.82 73.8 14.4 656.81 1187.68 894.77 282.35 74.4 246.09 1201.97 35.16 277.43 73.6 14.5 600.47 1186.91 814.76 281.31 74.2 128.05 1201.52 20.20 276.64 73.6 14.6 552.32 1186.50 769.06 280.53 74.1 124.91 1198.52 19.51 276.67 73.8 14.7 506.53 1186.20 731.54 279.86 74.0 106.18 1197.65 18.85 276.60 73.6 14.8 466.33 1185.95 689.70 279.30 74.0 25.93 1197.03 6.47 276.43 73.6 14.9 424.01 1185.72 643.05 278.80 73.8 0.00 1178.28 0.12 284.00 73.7 15.0 375.60 1185.54 584.78 278.30 73.8 0.00 1178.14 0.00 271.42 73.5 15.1 337.56 1185.36 529.24 277.94 73.8 0.00 1178.24 0.00 271.43 73.6 15.2 317.03 1185.18 492.40 277.74 73.8 0.00 1178.09 0.00 271.49 73.4 15.3 305.80 1184.98 477.44 277.63 73.8 0.00 1178.09 0.00 271.52 73.4 15.4 281.06 1184.75 461.91 277.46 73.7 0.00 1178.04 0.00 271.59 73.3 15.5 236.22 1184.58 411.74 277.23 73.7 0.00 1177.90 0.00 271.73 73.1 15.6 190.97 1184.41 336.17 276.98 73.7 0.00 1177.81 0.00 271.85 72.9 15.7 159.07 1184.23 273.40 276.77 73.7 0.00 1177.80 0.00 271.87 72.8 15.8 145.83 1184.09 237.46 276.71 73.7 0.00 1177.78 0.00 271.89 72.8

Oconee Nuclear Station UFSAR Table 6-35 (Page 9 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 15.9 162.79 1184.08 234.57 276.80 73.8 0.00 1177.83 0.00 271.87 72.9 16.0 204.82 1183.92 287.14 277.05 73.9 0.00 1178.21 0.00 271.48 73.6 16.1 263.22 1183.94 395.96 277.64 73.9 0.00 1178.06 0.00 271.58 73.3 16.2 353.08 1184.07 577.52 278.45 74.5 0.00 1177.94 0.00 271.69 73.1 16.3 364.98 1184.35 642.89 278.36 73.7 0.00 1177.56 0.00 272.04 72.5 16.4 300.17 1184.95 529.82 277.74 73.7 0.00 1177.06 0.00 272.62 71.5 16.5 302.18 1185.10 470.69 277.74 73.9 111.37 1197.18 0.18 277.14 74.1 16.6 346.51 1184.78 526.70 278.13 74.0 132.52 1198.18 0.22 277.78 73.4 16.7 377.87 1184.68 605.16 278.38 74.0 21.16 1203.47 0.05 280.00 73.2 16.8 388.91 1184.93 629.58 278.46 74.0 0.00 1178.09 0.00 271.51 73.4 16.9 404.55 1185.15 643.68 278.67 74.0 0.00 1178.13 0.00 271.53 73.5 17.0 426.13 1185.16 670.75 278.91 74.1 0.00 1178.10 0.00 271.59 73.4 17.1 423.44 1185.24 669.67 278.82 74.0 0.00 1178.20 0.00 271.49 73.6 17.2 414.13 1185.43 651.39 278.72 74.0 0.00 1178.21 0.00 271.48 73.6 17.3 419.35 1185.35 656.09 278.80 74.1 0.00 1178.01 0.00 271.53 73.3 17.4 422.88 1185.38 662.39 278.86 73.9 0.00 1177.81 0.00 271.83 72.9 17.5 463.43 1185.55 718.56 279.57 74.3 0.00 1177.77 0.00 271.92 72.8 17.6 533.97 1185.84 823.64 280.52 74.6 0.00 1178.08 0.00 271.65 73.3 17.7 513.09 1186.16 791.87 280.13 73.8 6.58 1187.22 0.00 272.09 72.2 17.8 450.98 1186.10 693.63 279.12 73.9 106.67 1198.85 0.00 272.62 74.5

Oconee Nuclear Station UFSAR Table 6-35 (Page 10 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 17.9 478.30 1186.17 730.24 279.88 74.0 110.32 1200.25 0.00 271.27 73.5 18.0 573.32 1186.80 877.21 281.40 75.3 10.23 1206.49 0.00 271.40 73.7 18.1 587.98 1186.84 889.92 281.30 74.1 62.46 1208.55 0.00 271.41 73.8 18.2 531.31 1186.47 779.51 280.27 74.0 94.26 1210.86 0.00 271.75 73.6 18.3 536.99 1186.32 791.79 280.43 74.9 31.80 1215.40 0.00 271.42 73.5 18.4 525.84 1186.22 792.74 280.25 73.9 15.26 1195.91 0.00 271.48 73.6 18.5 483.93 1186.08 736.24 279.57 74.0 82.90 1210.27 0.00 271.91 73.9 18.6 514.15 1186.25 780.92 280.32 74.1 70.67 1213.79 0.00 271.28 73.5 18.7 617.22 1187.39 950.24 282.25 75.1 3.04 1219.95 0.00 271.49 73.4 18.8 667.82 1187.83 1102.16 282.78 74.9 0.00 1178.30 0.00 271.48 73.7 18.9 645.51 1187.42 1141.82 282.31 74.7 0.00 1178.22 0.00 271.48 73.6 19.0 628.92 1187.12 1126.53 282.04 74.6 4.03 1186.52 0.00 271.72 73.1 19.1 622.35 1187.00 1097.76 281.92 74.6 26.97 1193.74 0.00 271.80 74.0 19.2 627.60 1187.10 1089.15 282.03 74.6 22.94 1195.01 0.00 271.96 72.5 19.3 634.07 1187.20 1089.87 282.13 74.8 0.00 1176.90 0.00 272.77 71.2 19.4 628.25 1187.10 1061.93 281.98 74.7 0.00 1176.11 0.00 273.36 69.7 19.5 615.30 1186.87 1021.49 281.73 74.5 0.00 1175.67 0.00 273.59 68.8 19.6 615.67 1186.88 1017.16 281.75 74.6 0.00 1175.75 0.00 273.56 68.9 19.7 622.13 1187.00 1031.23 281.91 74.5 0.00 1176.61 0.00 273.12 70.5 19.8 641.78 1187.36 1071.28 282.31 75.0 131.44 1201.24 0.01 266.67 74.1

Oconee Nuclear Station UFSAR Table 6-35 (Page 11 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 19.9 660.65 1187.68 1105.49 282.65 74.7 297.04 1208.90 0.03 280.00 73.9 20.0 693.38 1188.33 1156.25 283.34 74.9 99.94 1213.59 0.01 272.33 73.6 20.5 670.39 1187.93 1106.57 282.89 74.9 29.06 1212.19 0.00 271.41 73.6 21.0 627.19 1187.19 1024.96 282.00 75.2 2.35 1214.04 0.00 271.42 73.5 21.5 622.60 1187.31 942.12 282.04 74.2 6.47 1192.30 0.00 271.41 73.6 22.0 686.28 1188.48 987.12 283.37 75.0 17.12 1198.12 0.00 271.40 73.6 22.5 750.89 1189.44 1103.70 284.44 75.1 19.11 1206.91 0.00 271.34 73.6 23.0 685.30 1188.72 852.21 283.60 74.5 8.32 1214.00 0.00 271.44 73.5 23.5 615.57 1187.41 753.03 281.84 74.2 47.88 1208.63 0.00 271.54 73.6 24.0 637.82 1187.44 1130.65 282.45 75.3 59.58 1208.17 0.00 271.45 73.7 24.5 634.17 1187.47 1069.06 282.31 74.6 14.91 1206.76 0.00 271.43 73.7 25.0 574.77 1186.80 887.07 280.95 74.2 4.34 1203.16 0.00 271.41 73.6 25.5 537.79 1185.98 1117.72 280.56 74.5 5.24 1197.52 0.00 271.43 73.7 26.0 511.36 1185.64 1195.69 280.22 74.4 7.49 1198.95 0.00 271.41 73.7 26.5 458.63 1185.30 1158.46 279.44 74.2 12.45 1207.33 0.00 271.43 73.7 27.0 411.02 1184.92 1179.36 278.87 74.2 13.00 1213.62 0.00 271.40 73.7 27.5 372.88 1184.54 1296.24 278.46 74.1 12.37 1221.75 0.00 271.45 73.7 28.0 344.56 1184.22 1409.40 278.22 74.1 9.15 1221.44 0.00 271.41 73.7 28.5 317.63 1184.07 1368.75 277.94 74.0 2.74 1206.24 0.00 271.42 73.7 29.0 291.03 1184.01 1290.63 277.67 74.0 4.29 1207.32 0.00 271.39 73.7

Oconee Nuclear Station UFSAR Table 6-35 (Page 12 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 29.5 262.84 1183.99 1173.69 277.42 73.9 2.42 1208.45 0.00 271.37 73.7 30.0 239.91 1183.99 1028.93 277.24 73.8 0.17 1208.16 0.00 271.42 73.7 30.5 222.83 1183.93 933.73 277.12 73.8 0.30 1186.83 0.00 271.40 73.7 31.0 206.51 1183.84 852.42 277.02 73.8 1.01 1188.83 0.00 271.39 73.7 31.5 196.63 1183.76 776.21 276.96 73.8 4.08 1201.34 0.00 271.39 73.7 32.0 190.70 1183.69 775.96 276.93 73.8 13.68 1223.72 0.00 271.42 73.7 32.5 179.66 1183.56 854.17 276.88 73.8 19.86 1235.99 0.00 271.40 73.7 33.0 162.66 1183.39 903.59 276.81 73.8 14.99 1240.65 0.00 271.40 73.7 33.5 148.17 1183.26 783.13 276.74 73.7 6.54 1231.93 0.00 271.40 73.7 34.0 141.77 1183.20 623.80 276.71 73.7 3.27 1203.22 0.00 271.33 73.6 34.5 145.56 1183.16 679.51 276.74 73.8 4.76 1210.38 0.00 271.41 73.7 35.0 148.67 1183.06 1109.38 276.79 73.8 2.59 1216.08 0.00 271.40 73.8 35.5 143.83 1182.84 1858.91 276.87 73.8 16.90 1208.62 0.00 271.55 73.4 36.0 137.78 1182.56 2537.08 276.93 73.9 23.19 1208.76 0.00 271.46 73.8 36.5 132.72 1182.38 2826.84 276.96 74.0 12.90 1214.29 0.00 271.42 73.7 37.0 129.98 1182.29 2876.72 276.97 74.0 9.91 1219.01 0.00 271.40 73.7 37.5 128.23 1182.24 2964.72 276.99 74.0 8.40 1208.43 0.00 271.49 73.8 38.0 127.47 1182.17 3154.39 277.03 74.1 8.06 1204.87 0.00 271.40 73.7 38.5 126.26 1182.12 3340.97 277.06 74.1 6.62 1217.32 0.00 271.41 73.7 39.0 123.70 1182.09 3378.19 277.04 74.1 9.45 1230.39 0.00 271.40 73.7

Oconee Nuclear Station UFSAR Table 6-35 (Page 13 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 39.5 119.88 1182.10 3245.16 276.97 74.1 13.37 1239.57 0.00 271.40 73.7 40.0 115.99 1182.13 3085.22 276.91 74.0 17.92 1244.92 0.00 271.41 73.7 40.5 113.36 1182.14 3022.42 276.89 74.0 17.58 1246.55 0.00 271.41 73.7 41.0 111.45 1182.12 3045.18 276.88 74.0 18.08 1247.27 0.00 271.41 73.7 41.5 108.87 1182.10 3107.73 276.87 74.0 18.19 1247.50 0.00 271.38 73.7 42.0 105.23 1182.09 3179.22 276.85 74.0 18.37 1247.68 0.00 271.42 73.7 42.5 100.54 1182.08 3197.31 276.81 74.0 18.19 1247.58 0.00 271.41 73.7 43.0 95.27 1182.06 3102.78 276.71 73.9 17.86 1247.60 0.00 271.42 73.7 43.5 89.48 1182.07 2936.29 276.57 73.7 16.11 1247.82 0.00 271.41 73.7 44.0 81.96 1182.14 2729.48 276.49 73.7 6.77 1246.77 0.00 271.40 73.7 44.5 73.11 1182.20 2494.15 276.47 73.7 1.37 1242.27 0.00 271.39 73.7 45.0 63.95 1182.27 2241.93 276.46 73.7 0.01 1232.88 0.00 271.40 73.7 45.5 55.22 1182.38 1956.43 276.44 73.7 0.00 1178.26 0.00 271.40 73.7 46.0 47.90 1182.48 1663.32 276.43 73.7 0.00 1190.48 0.00 271.40 73.7 46.5 42.12 1182.55 1402.24 276.42 73.7 0.00 1190.48 0.00 271.40 73.7 47.0 38.02 1182.57 1176.52 276.42 73.7 0.00 1178.26 0.00 271.40 73.7 47.5 35.43 1182.54 984.30 276.42 73.7 0.00 1178.26 0.00 271.40 73.7 48.0 33.13 1182.46 796.83 276.41 73.7 0.00 1178.27 0.00 271.40 73.7 48.5 27.86 1182.33 576.53 276.41 73.7 0.00 1178.26 0.00 271.40 73.7 49.0 20.12 1182.33 360.50 276.40 73.7 0.00 1178.26 0.00 271.40 73.7

Oconee Nuclear Station UFSAR Table 6-35 (Page 14 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 49.5 15.66 1182.63 205.44 276.40 73.7 2.83 1199.98 0.00 271.40 73.7 50.0 14.31 1182.88 109.99 276.40 73.7 10.68 1224.31 0.00 271.41 73.7 50.5 13.18 1183.07 50.45 276.42 73.7 16.67 1242.89 0.00 271.40 73.7 51.0 12.51 1183.25 19.05 276.40 73.7 18.05 1252.86 0.00 271.40 73.7 51.5 12.21 1183.43 6.73 276.36 73.7 19.22 1253.45 0.00 271.41 73.7 52.0 11.87 1183.61 2.34 276.42 73.7 18.79 1252.25 0.00 271.41 73.7 52.5 11.56 1183.83 0.85 276.80 73.7 18.10 1251.16 0.00 271.40 73.7 53.0 10.61 1184.05 0.31 275.97 73.7 19.19 1250.40 0.00 271.41 73.7 53.5 8.27 1184.17 0.11 268.52 73.7 20.75 1249.60 0.00 271.41 73.7 54.0 7.05 1184.30 0.04 282.05 73.7 25.68 1248.39 0.00 271.41 73.7 54.5 7.30 1184.63 0.02 294.12 73.7 31.30 1246.59 0.00 271.42 73.7 55.0 7.41 1185.11 0.01 271.39 73.7 33.32 1244.62 0.00 271.42 73.7 55.5 9.39 1185.63 0.01 271.40 73.7 31.63 1243.25 0.00 271.42 73.7 56.0 12.10 1185.99 0.01 250.00 73.7 25.44 1242.73 0.00 271.41 73.7 56.5 13.96 1186.32 0.01 307.69 73.7 22.89 1243.26 0.00 271.41 73.7 57.0 14.70 1186.66 0.01 307.69 73.7 24.77 1243.80 0.00 271.41 73.7 57.5 14.90 1186.69 0.03 264.71 73.7 25.35 1243.97 0.00 271.41 73.7 58.0 14.52 1186.24 0.09 271.74 73.7 25.52 1244.02 0.00 271.41 73.7 58.5 13.35 1185.60 0.16 280.49 73.7 25.61 1244.01 0.00 271.41 73.7 59.0 15.18 1185.26 0.22 277.27 73.7 25.57 1244.01 0.00 271.41 73.7

Oconee Nuclear Station UFSAR Table 6-35 (Page 15 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 59.5 19.13 1185.31 0.23 273.50 73.7 25.64 1244.02 0.00 271.41 73.7 60.0 25.72 1184.02 99.31 276.41 73.7 25.82 1243.98 0.00 271.41 73.7 61.0 30.04 1182.83 427.22 276.41 73.7 26.16 1243.96 0.00 271.41 73.7 62.0 31.92 1182.15 831.35 276.41 73.7 27.06 1243.80 0.00 271.41 73.7 63.0 30.90 1182.08 1148.93 276.41 73.7 27.87 1243.49 0.00 271.41 73.7 64.0 30.37 1182.05 1655.04 276.43 73.7 28.48 1243.22 0.00 271.42 73.7 65.0 32.75 1182.00 2211.42 276.44 73.7 29.14 1242.96 0.00 271.42 73.7 66.0 37.71 1181.93 2669.84 276.46 73.7 29.89 1242.70 0.00 271.42 73.7 67.0 43.89 1181.88 3053.06 276.47 73.7 26.48 1242.64 0.00 271.42 73.7 68.0 46.17 1181.94 3056.26 276.46 73.7 24.54 1243.47 0.00 271.42 73.7 69.0 44.31 1182.08 2662.50 276.45 73.7 25.42 1244.21 0.00 271.41 73.7 70.0 42.25 1182.21 2283.35 276.44 73.7 24.27 1244.49 0.00 271.41 73.7 71.0 39.46 1182.33 1940.20 276.43 73.7 24.15 1244.81 0.00 271.41 73.7 72.0 36.35 1182.40 1619.69 276.42 73.7 24.19 1245.02 0.00 271.41 73.7 73.0 34.16 1182.41 1433.50 276.42 73.7 23.40 1245.13 0.00 271.41 73.7 74.0 32.39 1182.37 1420.85 276.42 73.7 15.34 1243.79 0.00 271.38 73.7 75.0 29.01 1182.34 1379.54 276.41 73.7 14.94 1246.29 0.00 271.41 73.7 76.0 25.21 1182.27 1133.99 276.41 73.7 21.09 1248.61 0.00 271.41 73.7 77.0 20.49 1182.07 768.40 276.41 73.7 13.71 1248.25 0.00 271.40 73.7 78.0 13.07 1182.03 327.82 276.40 73.7 8.49 1249.98 0.00 271.40 73.7

Oconee Nuclear Station UFSAR Table 6-35 (Page 16 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 79.0 6.98 1182.44 52.21 276.41 73.7 7.54 1252.99 0.00 271.40 73.7 80.0 7.00 1183.19 4.79 276.36 73.7 10.24 1257.64 0.00 271.40 73.7 81.0 13.08 1183.97 0.48 275.68 73.7 28.12 1253.17 0.00 271.42 73.7 82.0 16.95 1184.69 0.08 281.44 73.7 38.06 1248.07 0.00 271.43 73.7 83.0 16.93 1185.64 0.02 275.00 73.7 32.77 1243.86 0.00 271.42 73.7 84.0 15.74 1186.35 0.00 271.40 73.7 29.90 1243.17 0.00 271.42 73.7 85.0 12.49 1186.69 0.00 271.40 73.7 29.73 1243.22 0.00 271.42 73.7 86.0 9.03 1186.89 0.00 271.39 73.7 30.38 1243.21 0.00 271.42 73.7 87.0 7.06 1187.06 0.00 271.39 73.7 31.34 1243.04 0.00 271.42 73.7 88.0 7.32 1187.16 0.00 271.39 73.7 31.83 1242.80 0.00 271.42 73.7 89.0 8.50 1187.17 0.00 271.39 73.7 33.49 1242.50 0.00 271.42 73.7 90.0 9.96 1187.12 0.00 271.40 73.7 25.08 1242.66 0.00 271.40 73.7 91.0 9.49 1186.28 0.10 279.19 73.7 11.93 1244.52 0.00 271.41 73.7 92.0 6.89 1184.72 0.13 276.00 73.7 6.03 1238.16 0.00 271.40 73.7 93.0 5.98 1184.21 0.04 271.43 73.7 4.40 1229.30 0.00 271.39 73.7 94.0 11.56 1184.14 29.04 276.43 73.7 14.76 1250.61 0.00 271.41 73.7 95.0 20.35 1182.98 457.00 276.41 73.7 23.87 1252.59 0.00 271.41 73.7 96.0 24.11 1182.12 1181.10 276.42 73.7 22.32 1250.36 0.00 271.41 73.7 97.0 26.24 1182.04 1662.26 276.43 73.7 11.46 1247.09 0.00 271.39 73.7 98.0 30.59 1182.00 2074.41 276.44 73.7 2.40 1210.96 0.00 271.41 73.7

Oconee Nuclear Station UFSAR Table 6-35 (Page 17 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 99.0 33.02 1182.01 2352.03 276.44 73.7 2.51 1199.28 0.00 271.41 73.7 100.0 34.11 1182.08 2242.85 276.44 73.7 3.16 1199.39 0.00 271.39 73.7 101.0 41.00 1182.01 2530.23 276.45 73.7 2.13 1199.49 0.00 271.41 73.7 102.0 43.05 1182.07 2549.61 276.45 73.7 1.54 1195.93 0.00 271.40 73.7 103.0 40.88 1182.19 2217.35 276.44 73.7 3.94 1201.74 0.00 271.40 73.7 104.0 42.66 1182.17 2200.29 276.44 73.7 8.60 1226.53 0.00 271.40 73.7 105.0 42.50 1182.22 2064.81 276.43 73.7 7.67 1236.21 0.00 271.40 73.7 106.0 39.63 1182.30 1863.45 276.43 73.7 10.23 1248.74 0.00 271.40 73.7 107.0 35.08 1182.36 1655.03 276.42 73.7 19.95 1251.28 0.00 271.41 73.7 108.0 31.95 1182.34 1542.39 276.42 73.7 22.72 1251.14 0.00 271.41 73.7 109.0 30.93 1182.29 1489.64 276.42 73.7 26.43 1248.84 0.00 271.42 73.7 110.0 31.95 1182.24 1542.24 276.42 73.7 29.30 1246.86 0.00 271.42 73.7 111.0 34.72 1182.19 1710.75 276.43 73.7 29.98 1245.53 0.00 271.42 73.7 112.0 38.13 1182.15 1939.91 276.43 73.7 29.70 1244.89 0.00 271.42 73.7 113.0 41.41 1182.12 2170.53 276.44 73.7 29.36 1244.79 0.00 271.41 73.7 114.0 45.61 1182.06 2419.51 276.45 73.7 30.54 1244.69 0.00 271.42 73.7 115.0 47.92 1182.05 2583.92 276.45 73.7 20.10 1243.91 0.00 271.40 73.7 116.0 41.84 1182.20 2215.63 276.44 73.7 10.62 1236.42 0.00 271.40 73.7 117.0 31.86 1182.38 1646.20 276.42 73.7 8.76 1237.16 0.00 271.41 73.7 118.0 21.12 1182.35 1068.09 276.41 73.7 3.06 1247.95 0.00 271.40 73.7

Oconee Nuclear Station UFSAR Table 6-35 (Page 18 of 18)

(31 DEC 2003)

Reactor Vessel Side Steam Generator Side Time (seconds)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (Btu/lbm)

Pressure (psi)

Gas Mass Flow (lbm/sec)

Gas Enthalpy (Btu/lbm)

Liquid Mass Flow (lbm/sec)

Liquid Enthalpy (lbm/sec)

Pressure (psi) 119.0 7.80 1182.31 382.58 276.41 73.7 1.84 1196.98 0.00 271.40 73.7 120.0 1.89 1182.72 58.32 276.40 73.7 20.89 1228.71 0.00 271.42 73.7 121.0 2.77 1182.88 9.00 276.35 73.7 38.09 1231.78 0.00 271.42 73.7