ML17226A146
| ML17226A146 | |
| Person / Time | |
|---|---|
| Site: | River Bend  |
| Issue date: | 07/28/2017 |
| From: | Entergy Operations |
| To: | Office of Nuclear Reactor Regulation, Office of Nuclear Material Safety and Safeguards |
| Shared Package | |
| ML17226A087 | List:
|
| References | |
| RBG-47776, RBF1-17-0089 | |
| Download: ML17226A146 (114) | |
Text
RBS USAR TABLE 9.1-1 TOOLS AND SERVICING EQUIPMENT Revision 16 1 of 1 March 2003 Fuel Servicing Equipment In-Vessel Servicing Equipment
16 5 Channel handling boom Control rod grapple Fuel preparation machines Control rod guide tube grapple New fuel inspection stand Fuel support grapple Channel bolt wrenches Grid guide Channel handling tool Control rod latch tool Fuel pool sipper Control rod guide tube seal Fuel transfer system Incore guide tube seal Channel gauging fixture Blade guides General purpose grapples Fuel bundle sampler Fuel handling platform Blade guide rack with 2 blade Refueling Equipment guides Refueling platform 5
Auxiliary and vessel platform Servicing Aids Portable radiation shield 16
Pool tool accessories Actuating poles Storage Equipment General area underwater lights Local area underwater lights Spent fuel storage racks Drop lights Channel storage racks Underwater TV monitoring Control rod storage racks system Defective fuel storage Underwater vacuum cleaner containers Viewing aids In-vessel racks Light support brackets Defective fuel storage racks Underwater viewing tube New fuel storage racks Reactor Vessel Servicing Under-Reactor Vessel Servicing Equipment Equipment Reactor vessel servicing tools Control rod drive servicing Steam line plugs and tools installation tools CRD hydraulic system tools Shroud head bolt wrenches Water seal cap Head holding pedestals Control rod drive handling Head stud rack equipment Dryer-Separator Strongback Equipment handling platform Head Strongback/Carousel Thermal sleeve installation (incl. stud tensioners) tool Incore flange seal test plug Key bender
RBS USAR (1) NE - Nonessential PE - Passive essential Revision 21 1 of 1 Table 9.1-2 FUEL SERVICING EQUIPMENT Component Identification Essential Classification(1)
Safety Classification Seismic Category
6 Fuel prep machine PE NNS II 6
New fuel inspection stand PE 2
I Channel bolt wrench NE NNS NA Channel handling tool NE NNS NA Fuel pool sipper NE NNS NA Channel gauging fixture NE NNS NA General purpose grapple PE UNC I
10 Jib crane 10
PE 2
I Channel handling boom NE NNS NA
5 Blade guide rack with two blade guides NE NNS NA 5
of 2
August 1987 TABLE 9.1-3 FUEL TRANSFER SYSTEM COMPONENTS Essential Safety Component Classifi-Classifi-Seismic No.
Identification cation (1) cation Category 1
Winch NE NNS NA 2
Hydraulic power NE NNS NA supply 3
Fluid stop NE NNS NA 4
Vent pipe NE NNS NA 5
Cable enclosures NE NNS NA 6
Top horiz. guide NE NNS NA arms 7
Upper pool upender NE NNS NA 8
Trunnion box NE NNS NA 9
Hydraulic cylinder NE NNS NA 10 Upper pool framing NE NNS NA 11 Sheave box cover NE NNS NA 12 Hydraulic cylinder NE NNS NA 13 Fill valve NE NNS NA 14 Sheave box NE NNS NA 15 Sheave pipe NE NNS I
16 Hydraulic cylinder NE NNS NA 17 Manual gate valve NE NNS I
18 Containment isolation PE 2
I 20 Transfer tube NE/PE NNS/2 I
21 Hydraulic power NE NNS NA supply 22 Mid-support NE NNS I
23 Wire rope (cables)
NE NNS NA 24 Carriage NE NNS NA 24A Tilt tube NE NNS NA 24B Follower NE NNS NA 25 Gate valve NE NNS I
26 Bellows NE NNS NA 27 Drain valve NE NNS NA 28 Horizontal guide NE NNS NA arms
(1)NE - Nonessential PE - Passive essential 2 of 2 August 1987 TABLE 9.1-3 (Cont)
FUEL TRANSFER SYSTEM COMPONENTS Essential Safety Component Classifi-Classifi-Seismic No.
Identification cation(1) cation Category 29 Valve support NE NNS I
structure 30 Lower pool framing NE NNS NA 31 Lower pool upender NE NNS NA 32 Pivot arm framing NE NNS NA control system
RBS USAR TABLE 9.1-4 REACTOR VESSEL SERVICING EQUIPMENT 1 of 1 August 1987 Essential Safety Component Classifi-Classifi-Seismic Identification cation(1) cation Category Reactor vessel serv. tools NE NNS NA Steam line plugs NE UNC NA Shroud head bolt wrench NE NNS NA Head holding pedestal PE NNS I
Head stud rack NE NNS NA Dryer and separator PE 2
I(2) strongback Head strongback carousel PE 2
I (1)
NE - Nonessential PE - Passive essential (2)
Dynamic analysis methods for seismic loading are not applicable, as this equipment is supported by the reactor building polar crane. Lifting devices have been designed with a minimum safety factor of 5 and undergo proof testing.
RBS USAR Revision 23 1 of 2 TABLE 9.1-5 DESIGN PARAMETERS OF FUEL POOL COOLING AND PURIFICATION SUBSYSTEMS Cooling Subsystem
- 14 *8A *8 Fuel Building Fuel Storage Pool Max Normal Temp 139.8°F Max Abnormal Temp 1 (Full Core Off Load) 155.6°F Max Abnormal Temp 1 (Temporary Loss of Cooling) 170.0°F 14*
Containment Fuel Storage Pool Max Normal Temp (0.32 cores) 126.9°F Max Abnormal Temp (0.32 cores) 134.6°F (Temporary Loss of Cooling) 170.0°F 8* 8A*
Cooling Water Temperature RPCCW 105°F (maximum)
SSW 95°F (maximum)
Pump Capacity 2 @ 100%
Type Horizontal Centrifugal 2,500 gpm Design Flow 87.6 ft H2O Design Total Head 87.6 ft Shell Side Tube Side Cooler Fluid RPCCW Fuel Pool Water Flow 1,000,000 lb/hr 1,250,000 lb/hr Design Pressure 150 psig 150 psig Normal Heat Load 2,3 17.07 x 10 6 Btu/hr Temp, in 105.0°F 140.0°F Temp, out 122.1°F 126.3°F Abnormal Heat Load 3
28.63 x 10 6 Btu/hr Temp, in 105.0°F 163.3°F Temp, out 133.7°F 140.5°F
- 11 *8A 8A* 11*
RBS USAR Revision 23 2 of 2 TABLE 9.1-5 (cont)
Purification Subsystem Demineralizer Flow 300 gpm Filter Flow 600 gpm (each)
Filter Design Maximum Particle Size 6 microns Pumps Capacity 2 @ 50%
Type Horizontal Centrifugal Design Flow 600 gpm (each)
Design Total Head 260 ft H2O Pool Water Quality Conductivity
= 3 umho/cm @ 25°C Chloride
= 0.5 ppm pH 5.3 to 7.5 @ 25°C Heavy Elements
< 0.1 ppm (Fe, Cu, Hg, Ni)
Total Insolubles
< 1 ppm 1 Design Limits 2 Heat loads shown are for the fuel building fuel storage pool only. These values are the limiting case numbers for the fuel storage pools.
3 These values calculated using SRP 9.1.3 method. Offload rate to the fuel building fuel storage pool is constrained to ensure the temperature design limit is maintained.
KEY:
RPCCW - Reactor Plant Component Cooling Water SSW
- Standby Service Water
RBS USAR Table 9.1-6 FUEL DISCHARGE HEAT LOAD FOR NORMAL OPERATION (24-MONTH REFUELING CYCLE)
Revision 23 1 of 1 14 Discharge Number Number of Fuel Assemblies Decay Time (days) 1 260 400 2
260 365 3
260 150 hours0.00174 days <br />0.0417 hours <br />2.480159e-4 weeks <br />5.7075e-5 months <br /> 14
RBS USAR Revision 15 1 of 2 May 2002 TABLE 9.1-7
- 15 LIGHT LOADS OVER THE SPENT FUEL POOL FUEL BUILDING 15*
Distance (ft)
Kinetic Item Above Pool Surface Total Above Rack Dry Weight (lb)
Energy at Impact (2)
(top of rack)
(ft-lb)
Channel bolt wrench 4
31 15 465 Channel handling tool 11.5(1) 38.5(1) 25 963 Channel gauging fixture 17.8(1) 210 3738 General purpose grapple 3.6(1) 30.6(1) 45 1377 Actuating pole 4
31 61 1891 Drop light 4
31 25 775 Local area underwater light 4
31 35 1085 Viewing aid 27 13 351 Control rod 12(1) 218 2616 Handrail, removable 4
31 122 3782 Underwater TV camera 4
31 50 1550
- 1 Defect. fuel container with fuel assembly 5.4 617(4) 3332 Fuel channel 24(1) 99 2376
- 15 Dummy fuel assembly 5.79(9) 617(4) 3573(3)
Fuel bundle 5.79(9) 580(4) 3358(3)
- 2 Fuel bundle and channel 5.79(9) 664(4) 3752(3)(5)
New Fuel Bundle and Channel(6) 51.7(7) 744 27680 2*
- 10 Miscellaneous Light Loads(8) 36.83
1200(8) 44200(8) 15* 10* 1*
Revision 15 2 of 2 May 2002
- 1 (1)
Distance from center of gravity to top of fuel storage rack and pool surface.
(2)
Kinetic energy calculated without credit taken for buoyancy and drag for conservation, except for defective fuel container and spent fuel assembly.
(3)
See USAR Section 15.7.4 for fuel assembly fuel handling accident.
Kinetic energy values differ because of rounding-off of factors.
(4)
Credit was taken for buoyancy.
- 2 (5)
Credit was taken for fluid drag forces.
1*
(6)
No credit taken for buoyancy or fluid drag forces.
The top of a fuel channel or new fuel bundle alone, is bounded by the analyzed drop of a new fuel bundle and channel.
- 15 (7)
Distance from top of new fuel bundle to upper tie plate of spent fuel stored in spent fuel racks. For actual energy impact calculation, a value of 37.2 ft is used which is conservative to the height specified (442 in, 36.83 ft) which represents the distance from the bottom of a new fuel bundle to the upper tie plate of fuel stored in the spent fuel rack.
15*
2*
- 10 (8)
Miscellaneous light loads have been generically bounded by evaluation.
Specific weight versus height criteria has been analytically developed to ensure that consequences are bounded by regulatory limits.
10* *15 (9)
Distance from bottom of new fuel bundle to top of spent fuel rack.
RBS USAR Revision 5 1 of 2 August 1992 TABLE 9.1-8 LIGHT LOADS OVER THE UPPER CONTAINMENT POOL Total Distance Distance Kinetic Energy Above Above Dry(2) at Impact(2)
HWL Rack(1)
Weight (top of rack)
Item (ft-in)
(ft-in)
(lb)
(ft-lb)
Channel bolt wrench 16-2 41-9 15 626 Channel gauging fixture 0
15-7 210 3272 General purpose grapple 1-8 27-3 45 1226 Utility manipulator 19-8 45-3 45 2036 Actuating pole 0
15-0 61 915
- 5 Fuel bundle sampler 0
12-0 600 7200 5*
Drop light 4-2 29-9 25 744
- 1 Spent fuel assembly 0
5-10 664 3220 1*
Viewing aids 0
25-7 13 333 Light support bracket 4-2 29-9 110 3273 Channel handling tool 12-2 37-9 25 944 Underwater viewing tube 4-2 29-9 20 595 Fuel support grapple 19-2 44-9 147 6578 Peripheral fuel support plug 20-2 45-9 16 732 Control tube grapple 16-2 41-9 45 1879
RBS USAR Revision 10 2 of 2 April 1998 TABLE 9.1-8 (Cont)
LIGHT LOADS OVER THE UPPER CONTAINMENT POOL
- 1 Total Distance Distance Kinetic Energy Above Above Dry(2) at Impact(2)
HWL Rack(1)
Weight (top of rack)
Item (ft-in)
(ft-in)
(lb)
(ft-lb) 1*
Control rod latch tool 0
21-9 74 1610 Blade guide 0
21-9 180 3915 Grid guide 0
21-9 32 696 Removable handrails 2-2 27-9 122 3386 Magnetic retriever 4-2 29-9 2
60
- 5 Blade guide rack with two blade guides 0
9-11 3/4 400 3992 5*
- 10 Miscellaneous Light Loads (3)
(3) 1200(3)
(3) 10*
(1) All distances are measured from the center of gravity of the dropped object to the top of the rack.
(2) For conservatism, all kinetic energies are calculated without credit taken for buoyancy and drag forces for the distance travelled through water.
The kinetic energies are therefore calculated as if the entire drop occurs through air only.
(Buoyancy effects were considered for the spent fuel assembly.)
- 10 (3) Miscellaneous light loads have been generically bounded by evaluation.
Specific weight versus height criteria has been analytically developed to ensure that consequences are bounded by regulatory limits.
10*
RBS USAR 1 of 2 August 1988 TABLE 9.1-9 LIGHT LOADS OVER THE REACTOR VESSEL CORE (DURING REFUELING, VESSEL HEAD OFF)
- 1 Total Distance Distance (2)
Kinetic Energy Above Above Dry at Impact (2)
HWL Core (1)
Weight (top of rack)
Item (ft-in)
(ft-in)
(lb)
(ft-lb) 1*
General purpose 17-2 71-7 45 3221 grapple Utility manipulator 20-2 74-7 45 3356 grapple Fuel bundle 0
40-10 600 24500 sampler Clam shell retriever 3-0 57-5 25 1435 Peripheral fuel 20-2 74-7 16 1193 support plug Drop light 20-2 74-7 25 1865 Underwater TV 18-8 73-1 25 1827 Viewing aid 0
54-5 13 707
- 1 Spent fuel assembly 0
34-0 664 22576 1*
Fuel support grapple 19-2 73-7 147 10817 Peripheral office 17-2 71-7 45 3221 grapple CRD guide tube seal 20-2 74-7 60 4475 In-core guide tube 0
52-7 56 2945 seal Peripheral orifice 20-2 74-7 130 9696 holder Blade guide 0
52-1 180 9375
Revision 7 2 of 2 January 1995
- 1 Total Distance Distance (2)
Kinetic Energy Above Above Dry at Impact (2)
HWL Core (1)
Weight (top of rack)
Item (ft-in)
(ft-in)
(lb)
(ft-lb) 1*
Fuel bail cleaner 15-0 69-5 100 6917 Grid guide 0
51-5 32 1645 Fuel grapple 9-2 63-7 450 28613 Control rod grapple 19-2 73-7 17 1251 CRD guide tube 19-8 74-1 35 2593 grapple Stud handling tool 17-2 71-7 135 9664 RPV stud 18-2 72-7 500 36292
- 7 Shroud head bolt 18-2 72-7 420 30486 wrench 7*
Steamline plug 13-2 67-7 72 4866 installation tool Local area under-20-2 74-7 35 2610 water light General area light 20-2 74-7 50 3729 Steamline plug 19-2 73-7 375 27594 Head stud rack 18-2 72-7 200 14517 (empty)
Magnetic retriever 5-0 59-5 2
119
- 1 In-vessel 31-2 83-8 405 33882 control rod storage rack (empty) 1*
RBS USAR TABLE 9.1-9 (Cont) 2a of 2 August 1988
- 1 Total Distance Distance (2)
Kinetic Energy Above Above Dry at Impact (2)
HWL Core (1)
Weight (top of rack)
Item (ft-in)
(ft-in)
(lb)
(ft-lb) 1*
In-vessel 0
32-11 623 20506 control rod storage rack (loaded with a control rod)
(1)
All distances are measured from the center of gravity of the dropped object to the top of the core.
(2)
For conservatism, all kinetic energies are calculated without credit taken for buoyancy and drag forces, for the distance traveled through water.
The kinetic energies are therefore calculated as if the entire drop occurs through air only.
(Buoyancy effects were considered for the spent fuel assembly.)
1*
RBS USAR TABLE 9.2-1 NORMAL SERVICE WATER SYSTEM MAJOR COMPONENT DESIGN DATA Total Operating Design Data Quantity Heat Load for Each Operating/
(Btu/hr Component Description Available x 10
- 6)
(gpm)
Revision 16 1 of 3 March 2003 Normal Service Water Pumps 2/3 31,500 (1)
(approx)
14 12 TPCCW Heat Exchangers 2/3 26.28 9,250 Turbine Building Air-Condi-2/3 38.70 4,000 tioning Water Chillers
9 RHR Heat Exchangers 0/4 0.00 (2) 5,800 (5) 9
RPCCW Heat Exchangers 2/3 48.65 5,000
10 SPC Heat Exchangers 1/1 60 (6) 2,500 10
16 15 7 Drywell Unit Coolers 5/6 13.4 334 7 15 16
3 Control Building Air-Condi-2/4 5.70 630 tioning Water Chillers 3
Lube Oil Coolers 1/2 0.14 1,200 Hydrogen Coolers 4/4 23.44 916 Alternator Cooler 1/1 0.42 240 Standby Diesel Generator 0/2 0.00 (2) 700 Jacket Water Coolers
2 HPCS Diesel Generator 0/1 0.00 (2) 800 Jacket Water Cooler 2 12
Turbine EHC Coolers 1/2 0.14 50 Fuel/Radwaste Building 2/3 12.90 1,200 Chilled Water Chillers 14
Steam Bypass Hydraulic 1/2 0.00 40 Power Units
NORMAL SERVICE WATER SYSTEM MAJOR COMPONENT DESIGN DATA Total Operating Design Data Quantity Heat Load for Each Operating/
(Btu/hr Component Description Available x 10
- 6)
(gpm)
Revision 16 2 of 3 March 2003 Auxiliary Building Unit Coolers
16 14 RWCU Pump and Heat 1/1 0.187 50 Exchanger Room Unit Cooler
12 RPCCW Pump and Heat 1/1 0.318 100 Exchanger Area Unit Cooler El 114' Area Unit Cooler 1/1 0.293 90 HPCS Pump Room Unit Cooler 1/1 0.722 185 Switchgear, LPCS Pump, and 1/1 0.928 235 RHR Pump A Area Unit Cooler Switchgear Room and Electric 1/1 0.486 150 Terminal Boxes Unit Cooler Main Steam Pipe Tunnel, 1/1 0.405 120 North End, Unit Cooler RHR Heat Exchanger, RHR 1/1 0.692 210 Pumps B and C, and RCIC Pump Area Unit Cooler El 95'-9" HPCS Hatch and 1/1 0.118 37 Elevator Area Unit Cooler Upper Auxiliary Building 2/1 1.012 410 Levels Unit Coolers 12 16
Annulus Ventilation 2/2 0.0002 9
Radiation Monitors RHR Heat Exchanger 2/2 0.00 (3) 9 Radiation Monitors 14
NORMAL SERVICE WATER SYSTEM MAJOR COMPONENT DESIGN DATA Total Operating Design Data Quantity Heat Load for Each Operating/
(Btu/hr Component Description Available x 10
- 6)
(gpm)
Revision 14 3 of 3 September 2001
14 Steam Jet Air Ejector 1/2 0.78 131 Intercoolers Turbine Building Sample 1/1 0.22 60 Room Chiller Condensing Unit 14 6 Normal Service Water 7/8 164/444 (4) 9,000 Plate/Frame Heat Exchangers 6
(1)
This number represents 50 percent capacity at 211 ft total head (2)
Does not operate during normal plant operation.
(3)
Does not have a heat load until RHR heat exchangers operate.
14 6 (4)
Normal heat load is 164 Btu/hr x 10 6, while design peak heat load is 444 Btu/hr x 10 6.
6 14
12 9 9 12
10 (6) This number represents design heat load when providing Alternate Decay Heat Removal. Heat load during normal plant operation is negligible.
10
RBS USAR 1 of 1 August 1987 TABLE 9.2-2 REACTOR PLANT COMPONENT COOLING WATER SYSTEM COMPONENT DESCRIPTION RPCCW Pumps (1CCP - P1A, P1B, P1C)
Quantity 3
Type Horizontal, centrifugal Capacity, each, gpm (%)
3,000 (50)
TDH, ft 177 Driver, hp 200 RPCCW Heat Exchangers (1CCP - E1A, E1B, E1C)
Quantity 3
Type TEMA - CEN Duty, each, Btu/hr 25.0 x 106 Shell Side:
Fluid Demineralized cooling water No. of passes 1
Flow rate, gpm 2,337 (50% capacity)
Temperature in/out, °F 126°/105 Tube Side:
Fluid Service water No. of passes 1
Flow rate, gpm 5,022 (50% capacity)
Temperature in/out, °F 95/105 RPCCW Surge Tank (1CCP - TK1)
Capacity, gal 2,300 Design pressure, psig 150 Design temperature, °F 150
RBS USAR TABLE 9.2-3 REACTOR PLANT COMPONENT COOLING WATER SYSTEM MAJOR COMPONENT DESIGN DATA (1) One fuel pool heat exchanger in operation at any one time.
(2)
Supplied with RPCCW following a LOCA if adequate RPCCW pressure is available.
(3) Supplied with SSW following a LOCA if adequate RPCCW pressure is not available.
Revision 14 1 of 1 September 2001 Description Quantity Operation Design Data/Each Component (gpm)
Total Heat Exchange Rate
@ 105 oF Inlet Temp.
(10 Btu/h) 14 Fuel pool heat exchangers (1) 14 (1SFC*E1A, E1B) 2 Normal/
Accident (2,3) 2,000 16.62/24.68 Control rod drive pump lube oil cooler (1C11-PC001A, PC001B) 2 Normal (2) 15 0.05 RHR pump seal coolers (1ETZ*PC002A, PC002B) 2 Normal/
Accident (2,3) 20 0.20 8
Reactor water cleanup pumps seal coolers (1G33-PC001A,PC001B) 2 Normal/
Abnormal (2) 25 0.36 8
Reactor water cleanup non-regenerative HX (1G33-EB002A, EB002B) 2 Normal 627 14.0 Drywell equipment drain sump cooler (1DER-E1) 1 Normal 45 1.01 Reactor plant sample station (1G33-PNLZ020) 1 Normal 25 0.01 Reactor recirculation pump seal, bearing and winding coolers (1G33*PC001A, PC001B) 2 Normal 252 2.5
RBS USAR Revision 14 1 of 1 September 2001 TABLE 9.2-4 DECAY HEAT RATES DUE TO FISSION PRODUCTS AND HEAVY ELEMENTS FOLLOWING A DBA 14 Time (min/hr/days)
Time (sec)
Combined Decay Heat Rate (x 10 6 Btu/hr) 10 1 x 10 1
522.35 50 5 x 10 1
364.61 100 1 x 10 2
353.63 200 2 x 10 2
309.40 500 sec 5 x 10 2
260.81 1000 sec 1 x 10 3
222.28 30.0 min 1.8 x 10 3
188.77 1 hr 3.6 x 10 3
153.77 1.5 hr 5.4 x 10 3
134.60 2.0 7.2 x 10 3
123.54 2.5 9.0 x 10 3
116.17 3.0 1.08 x 10 4
110.97 4.0 1.44 x 10 4
102.69 5.0 1.80 x 10 4
97.05 6.0 2.16 x 10 4
93.01 8.0 2.88 x 10 4
87.65 10.0 3.60 x 10 4
82.29 12.0 4.32 x 10 4
78.04 16.0 5.76 x 10 4
72.33 20.0 7.20 x 10 4
68.16 24.0 8.64 x 10 4
64.56 2 days 1.73 x 10 5
52.73 3
2.59 x 10 5
46.07 4
3.46 x 10 5
41.62 5
4.32 x 10 5
38.31 6
5.18 x 10 5
35.91 7
6.05 x 10 5
33.56 8
6.91 x 10 5
31.93 9
7.78 x 10 5
30.30 10 8.64 x 10 5
28.98 15 1.29 x 10 6
24.78 20 1.73 x 10 6
21.70 25 2.16 x 10 6
19.83 30 2.59 x 10 6
18.18 14
RBS USAR Revision 24 1 of 1 TABLE 9.2-5 14 DECAY HEAT REJECTION* AND CONTAINMENT UNIT COOLER HEAT LOAD TO STANDBY SERVICE WATER FOLLOWING A LARGE BREAK OF A MAIN STEAM LINE DBA-MSL 12 12 (HEAT Removal Rates: Btu/Hr)
Time After Shutdown Time(sec)
RHR HVR Total Pump Adjustment Adjusted Total Integral Heat load (BTU) 0.00 hr 0.00E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 0.000E+00 10.00 min 6.00E+02 0.000E+00 0.000E+00 0.000E+00 1.071E+07
-1.071E+07 1.79E+06 0.50 hr 1.80E+03 7.960E+07
-7.809E+04 7.952E+07 1.132E+07 6.819E+07 5.56E+06 1
hr 3.60E+03 9.114E+07
-1.996E+04 9.112E+07 8.142E+06 8.297E+07 9.63E+06 1.5 hr 5.40E+03 9.460E+07
-1.076E+04 9.459E+07 8.142E+06 8.645E+07 1.37E+07 2
hr 7.20E+03 9.799E+07 6.315E+03 9.799E+07 8.142E+06 8.985E+07 1.78E+07 2.5 hr 9.00E+03 1.011E+08 1.150E+04 1.011E+08 8.142E+06 9.294E+07 2.18E+07 3
hr 1.08E+04 1.033E+08 2.653E+04 1.034E+08 8.142E+06 9.522E+07 2.59E+07 4
hr 1.44E+04 1.061E+08 4.983E+04 1.061E+08 8.142E+06 9.799E+07 3.41E+07 5
hr 1.80E+04 1.070E+08 6.911E+04 1.071E+08 8.142E+06 9.895E+07 4.22E+07 6
hr 2.16E+04 1.070E+08 8.672E+04 1.071E+08 8.142E+06 9.892E+07 5.03E+07 8
hr 2.88E+04 1.054E+08 1.045E+05 1.055E+08 8.142E+06 9.732E+07 6.66E+07 10 hr 3.60E+04 1.019E+08 1.000E+05 1.020E+08 8.142E+06 9.383E+07 8.29E+07 12 hr 4.32E+04 9.774E+07 1.329E+05 9.787E+07 8.142E+06 8.973E+07 9.92E+07 16 hr 5.76E+04 9.116E+07 1.310E+05 9.129E+07 8.142E+06 8.315E+07 1.32E+08 20 hr 7.20E+04 8.572E+07 1.564E+05 8.587E+07 8.142E+06 7.773E+07 1.64E+08 24 hr 8.64E+04 8.088E+07 1.353E+05 8.102E+07 8.142E+06 7.288E+07 1.97E+08 2
d 1.73E+05 6.581E+07 1.055E+05 6.592E+07 8.142E+06 5.777E+07 3.92E+08 3
d 2.59E+05 5.749E+07 9.215E+04 5.759E+07 8.142E+06 4.944E+07 5.88E+08 4
d 3.46E+05 5.195E+07 8.327E+04 5.204E+07 8.142E+06 4.389E+07 7.83E+08 5
d 4.32E+05 4.780E+07 7.662E+04 4.788E+07 8.142E+06 3.974E+07 9.79E+08 6
d 5.18E+05 4.480E+07 7.181E+04 4.487E+07 8.142E+06 3.673E+07 1.17E+09 7
d 6.05E+05 4.187E+07 6.711E+04 4.194E+07 8.142E+06 3.379E+07 1.37E+09 8
d 6.91E+05 3.984E+07 6.385E+04 3.990E+07 8.142E+06 3.176E+07 1.56E+09 9
d 7.78E+05 3.780E+07 6.059E+04 3.787E+07 8.142E+06 2.972E+07 1.76E+09 10 d
8.64E+05 3.617E+07 5.798E+04 3.623E+07 8.142E+06 2.809E+07 1.96E+09 15 d
1.30E+06 3.091E+07 4.954E+04 3.096E+07 8.142E+06 2.282E+07 2.93E+09 20 d
1.73E+06 2.709E+07 4.342E+04 2.714E+07 8.142E+06 1.899E+07 3.91E+09 25 d
2.16E+06 2.474E+07 3.966E+04 2.478E+07 8.142E+06 1.664E+07 4.89E+09 30 d
2.59E+06 2.268E+07 3.636E+04 2.272E+07 8.142E+06 1.458E+07 5.86E+09 14
RBS USAR TABLE 9.2-6 14 PLANT AUXILIARIES HEAT LOAD (BTU/hr)
INPUT TO STANDBY SERVICE WATER FOLLOWING A DBA Revision 25 1 of 1 12 12 Component 0 - 30 min 30 min - 1 hr 1 hr - 2 hr 2 hr - Day 1 Day 1-Day 10 Day 10 - Day 30 SDG Jacket Wtr Cooler A 1.203E+07 1.203E+07 1.203E+07 1.203E+07 1.203E+07 1.203E+07 HPCS DG Jacket Cooler 8.580E+06 8.580E+06 8.580E+06 8.580E+06 8.580E+06 8.580E+06 Control Room Chillers 2.803E+06 2.803E+06 2.803E+06 2.803E+06 2.803E+06 2.803E+06 Fuel Pool Coolers 0.000E+00 0
0 2.392E+07*
1.465E+07*
1.297E+07*
16 Aux Building Unit Coolers HVR-UC2 8.789E+04 8.789E+04 8.789E+04 8.789E+04 8.789E+04 8.789E+04 HVR-UC3 1.708E+05 1.708E+05 1.708E+05 1.708E+05 1.708E+05 1.708E+05 HVR-UC5 5.396E+05 5.396E+05 5.396E+05 5.396E+05 5.396E+05 5.396E+05 HVR-UC6 6.108E+05 4.073E+05 4.073E+05 4.073E+05 4.073E+05 4.073E+05 HVR-UC7 2.948E+05 2.948E+05 2.948E+05 2.948E+05 2.948E+05 2.948E+05 HVR-UC8 2.424E+05 2.424E+05 2.424E+05 2.424E+05 2.424E+05 2.424E+05 HVR-UC11A 16 5.576E+05 5.576E+05 5.576E+05 5.576E+05 5.576E+05 5.576E+05 RHR Pump Cooler A 0.000E+00 0.000E+00 0.000E+00 5.360E+04 5.360E+04 5.360E+04 PVLCS Air Compressor 1.200E+05 1.200E+05 1.200E+05 1.200E+05 1.200E+05 1.200E+05 14 RMS-RE15A 1.118E+05 1.118E+05 1.118E+05 1.118E+05 1.118E+05 1.118E+05 RMS-RE11A 2.000E+02 2.000E+02 2.000E+02 2.000E+02 2.000E+02 2.000E+02 NOTE: These heat rates assume a coincident loss of offsite power.
- Fuel Pool Loads decrease from the value shown through the remaining time period shown.
RBS USAR Revision 25 1 of 1 TABLE 9.2-7 PLANT AUXILIARIES HEAT INPUT TO STANDBY SERVICE WATER Time Time (sec)
SPC Heat Rejection Rate (Btu/hr) x 10 7
Other Auxiliaries Heat (Btu/hr) x 10 7
Integrated Heat (Btu) 16 14 12 0.0 hr 0.0 2.640 0.0 0.5 1.8 x 10 3
2.620 1.320 x 10 7
1.0 3.6 x 10 3
2.620 2.630 x 10 7
1.5 5.4 x 10 3
2.620 3.940 x 10 7
2.0 7.2 x 10 3
2.392 2.620 5.249 x 10 7
2.5 9.0 x 10 3
2.363 2.625 7.750E+07 3.0 1.08 x 10 4
2.334 2.625 1.024E+08 4.0 1.44 x 10 4
2.277 2.625 1.517E+08 5.0 1.80 x 10 4
2.219 2.625 2.004E+08 6.0 2.16 x 10 4
2.162 2.625 2.486E+08 8.0 2.88 x 10 4
2.047 2.625 3.431E+08 10.0 3.60 x 10 4
1.931 2.625 4.354E+08 12.0 4.32 x 10 4
1.816 2.625 5.254E+08 16.0 5.76 x 10 4
1.586 2.625 6.984E+08 20.0 7.20 x 10 4
1.469 2.625 8.645E+08 24.0 8.64 x 10 4
1.465 2.625 1.028E+09 2 days 1.73 x 10 5
1.449 2.625 2.007E+09 3
2.59 x 10 5
1.426 2.625 2.982E+09 4
3.46 x 10 5
1.405 2.625 3.952E+09 5
4.32 x 10 5
1.385 2.625 4.917E+09 6
5.18 x 10 5
1.366 2.625 5.877E+09 7
6.05 x 10 5
1.347 2.625 6.832E+09 8
6.91 x 10 5
1.330 2.625 7.784E+09 9
7.76 x 10 5
1.313 2.625 8.731E+09 10 8.64 x 10 5
1.297 2.625 9.674E+09 15 1.30 x 10 6
1.225 2.625 1.434E+10 20 1.73 x 10 6
1.165 2.625 1.892E+10 25 2.16 x 10 6
1.114 2.625 2.343E+10 30 2.59 x 10 6
1.070 2.625 2.789E+10 12 14 16
RIVER BEND STATION UPDATED SAFETY ANALYSIS REPORT CONTAINMENT UNIT COOLER HEAT REJECTION TO STANDBY SERVICE WATER FOLLOWING A LARGE RECIRCULATION LINE BREAK TABLE 9.2-8 REVISION 14 SEPTEMBER 2001 THIS TABLE HAS BEEN DELETED
RBS USAR Revision 24 1 of 1 TABLE 9.2-9 HEAT REJECTED BY OPERATING PUMPS FOLLOWING DBA Time Time (sec)
Heat Rejection Rate (Btu/hr) x 10 6
Integrated Heat (Btu) 14 12 0.0 hr 10.850 0.000 14 0.5 1.8 x 10 3
8.354 5.427 x 10 6
1.0 3.6 x 10 3
8.354 9.604 x 10 6
1.5 5.4 x 10 3
8.354 1.378 x 10 7
2.0 7.2 x 10 3
8.354 1.796 x 10 7
2.5 9.0 x 10 3
8.682 2.230 x 10 7
3.0 1.08 x 10 4
8.682 2.664 x 10 7
4.0 1.44 x 10 4
8.682 3.352 x 10 7
5.0 1.80 x 10 4
8.681 4.400 x 10 7
6.0 2.16 x 10 4
8.681 5.268 x 10 7
8.0 2.88 x 10 4
8.681 7.005 x 10 7
10.0 3.60 x 10 4
8.681 8.741 x 10 7
12.0 4.32 x 10 4
8.681 1.048 x 10 8
16.0 5.76 x 10 4
8.680 1.395 x 10 8
20.0 7.20 x 10 4
8.680 1.742 x 10 8
24.0 8.64 x 10 4
8.679 2.089 x 10 8
2 days 1.73 x 10 5
8.676 4.172 x 10 8
3 2.59 x 10 5
8.673 6.254 x 10 8
4 3.46 x 10 5
8.671 8.335 x 10 8
5 4.32 x 10 5
8.668 1.042 x 10 9
6 5.18 x 10 5
8.665 1.25 x 10 9
7 6.05 x 10 5
8.662 1.458 x 10 9
8 6.91 x 10 5
8.659 1.665 x 10 9
9 7.76 x 10 5
8.656 1.873 x 10 9
10 8.64 x 10 5
8.653 1.081 x 10 9
15 1.30 x 10 6
8.468 3.104 x 10 9
20 1.73 x 10 6
8.456 4.119 x 10 9
25 2.16 x 10 6
8.445 5.133 x 10 9
30 2.59 x 10 6
8.433 6.146 x 10 9
12
RBS USAR Revision 25 1 of 1 TABLE 9.2-10 TOTAL INTEGRATED HEAT INPUT TO STANDBY SERVICE WATER FROM RHR HEAT EXCHANGERS, CONTAINMENT UNIT COOLER, PUMPS, SPC, AND PLANT AUXILIARIES Total Integrated Heat (Btu)
Time Time (sec)
RHR Heat Exchangers and Containment Unit Cooler Pumps SPC and Plant Auxiliaries Total Integrated Heat 16 14 12 6 0.0 0.0 0.0 0.0 0.0 0.0 0.5 hr 1.8 x 10 3
8.687 x 10 6
5.427 x 10 6
1.320E+07 2.731E+07 1.0 3.6 x 10 3
4.648 x 10 7
9.604 x 10 6
2.630E+07 8.238E+07 2.0 7.2 x 10 3
1.329 x 10 8
1.796 x 10 7
5.249E+07 2.034E+08 24.0 8.64 x 10 4
2.059 x 10 9
2.089 x 10 8
1.028E+09 3.296E+09 5 days 4.32 x 10 5
7.037 x 10 9
1.042 x 10 9
4.917E+09 1.300E+10 10 8.64 x 10 5
1.102 x 10 10 2.081 x 10 9
9.674E+09 2.277E+10 30 2.59 x 10 6
2.059 x 10 10 6.146 x 10 9
2.789E+10 5.463E+10 6 12 14 16
RBS USAR TABLE 9.2-11 STANDBY COOLING TOWER PERFORMANCE FOLLOWING A LARGE BREAK OF A MAIN STEAM LINE (DBA-MSL)
Revision 25 1 of 1 16 14 12 Time Time (sec)
Total SSW Heat Load (Btu/hr)
SSW Flow (gpm)
Cold Water Temp (
oF)
Hot Water Temp (
oF) 0.5 hr 1.80E+03 1.027E+08 13210 88.51 104.15 1 hr 3.60E+03 1.175E+08 13210 89.55 107.43 2 hr 7.20E+03 1.487E+08 15370 91.91 111.36 3 hr 1.08E+04 1.535E+08 15368 92.10 112.18 4 hr 1.44E+04 1.557E+08 15365 92.17 112.54 5 hr 1.80E+04 1.561E+08 15363 92.18 112.60 6 hr 2.16E+04 1.555E+08 15361 92.16 112.50 8 hr 2.88E+04 1.527E+08 15356 92.07 112.06 10 hr 3.60E+04 1.481E+08 15351 91.88 111.27 12 hr 4.32E+04 1.428E+08 15346 91.67 110.37 16 hr 5.76E+04 1.339E+08 15337 91.31 108.86 20 hr 7.20E+04 1.273E+08 15328 91.04 107.74 24 hr 8.64E+04 1.225E+08 15318 90.84 106.91 2 d 1.73E+05 1.072E+08 15262 88.27 102.39 3 d 2.59E+05 9.947E+07 15205 87.88 101.03 4 d 3.46E+05 9.349E+07 15149 87.56 99.97 5 d 4.32E+05 8.897E+07 15092 87.32 99.17 6 d 5.18E+05 8.564E+07 15036 87.14 98.59 7 d 6.05E+05 8.248E+07 14979 86.97 98.04 8 d 6.91E+05 8.018E+07 14923 86.83 97.64 9 d 7.78E+05 7.796E+07 14867 86.71 97.25 10 d 8.64E+05 7.613E+07 14810 86.59 96.93 15 d 1.30E+06 6.986E+07 12046 85.32 96.98 20 d 1.73E+06 6.539E+07 11834 85.02 96.13 25 d 2.16E+06 6.249E+07 11634 84.80 95.60 30 d 2.59E+06 5.997E+07 11441 84.66 95.19 12 14 16
RBS USAR Revision 25 1 of 1 TABLE 9.2-12 AVAILABLE SCT BASIN VOLUME FOLLOWING DBA WITH EVAPORATION, DRIFT AND PVLCS COMPRESSOR LEAKAGE (MAXIMUM EVAPORATION CASE)
Time Available Basin Mass
[lbm]
Available Basin Volume
[gal]
0 hr 5.338E+07 6.415E+06 0.5 hr 5.334E+07 6.410E+06 1 hr 5.327E+07 6.402E+06 2 hr 5.314E+07 6.386E+06 3 hr 5.300E+07 6.369E+06 4 hr 5.285E+07 6.351E+06 5 hr 5.271E+07 6.334E+06 6 hr 5.256E+07 6.316E+06 8 hr 5.228E+07 6.282E+06 10 hr 5.201E+07 6.250E+06 12 hr 5.175E+07 6.220E+06 16 hr 5.128E+07 6.163E+06 20 hr 5.084E+07 6.110E+06 24 hr 5.044E+07 6.062E+06 2 d 4.810E+07 5.780E+06 3 d 4.606E+07 5.535E+06 4 d 4.408E+07 5.297E+06 5 d 4.216E+07 5.066E+06 6 d 4.028E+07 4.840E+06 7 d 3.850E+07 4.626E+06 8 d 3.679E+07 4.422E+06 9 d 3.508E+07 4.216E+06 10 d 3.343E+07 4.018E+06 15 d 2.534E+07 3.045E+06 20 d 1.772E+07 2.129E+06 25 d 1.037E+07 1.247E+06 30 d 3.272E+06 3.932E+05
RBS USAR (1) Loop A only is assumed to operate following DBA.
- 8A *8 8* 8A*
Revision 22 1 of 1 TABLE 9.2-13 STANDBY SERVICE WATER SYSTEM SAFEGUARD EQUIPMENT STATUS FOLLOWING A DBA
- 9 Component(1) 0-20 min 20 min-1 hr 1 hr-24 hr 24 hr-30 day 9*
RHR Pump A Operating Operating Operating Operating RHR Heat Exch A Off Operating Operating Operating HPCS Pump Operating Operating Operating Operating LPCS Pump Operating Off Off Off SSW Pump A Operating Operating Operating Operating SSW Pump C Operating Operating Operating Operating
- 8A *8 SCT Fans A-E Off Off Operating Operating SCT Fans L-P Off Off Operating Operating 8* 8A*
SDG A Operating Operating Operating Operating HPCS DG Operating Operating Operating Operating
NOTES:
NSW - Normal Service Water RPCCW - Reactor Plant Component Cooling Water HPCS - High Pressure Core Spray RHR - Residual Heat Removal A/C - Air-Conditioning CST - Condensate Storage Tank (for makeup only)
- SSW serves these coolers only if RPCCW discharge pressure is low.
1 of 1 August 1987 TABLE 9.2-14 ESSENTIAL COMPONENTS SERVED BY STANDBY SERVICE WATER SYSTEM Component Location Component's Normal Component (Building)
Cooling Supply Standby Diesel Generator 1A Diesel Generator NSW Standby Diesel Generator 1B Diesel Generator NSW HPCS Diesel Diesel Generator NSW Generator Control Building A/C Chiller A Control NSW Control Building A/C Chiller B Control NSW RHR Heat Exchangers A & C Auxiliary NSW RHR Heat Exchangers B & D Auxiliary NSW Fuel Pool Makeup Fuel CST Fuel Pool Cooling*
Fuel RPCCW Unit Cooler Coils Containment Chilled Water Unit Cooler Coils Auxiliary NSW Penetration Valve Leakage Control Compressor Auxiliary NSW RHR Pump Seal Coolers*
Auxiliary RPCCW
RBS USAR Revision 14 1 of 2 September 2001 TABLE 9.2-15 STANDBY SERVICE WATER SYSTEM MAJOR COMPONENT DESIGN DATA Design Data for Each Component Description Quantity (gpm)
Standby Service Water Pumps 4
7,690(1)
- 12 *14 Standby Diesel Generator Jacket Water Coolers 2
700
- 2 High-Pressure Core Spray Diesel Generator Jacket Water Cooler 1
800 2* *3 Control Building Air-Conditioning Water Chillers 4
630 3*
- 9 *8A *8 Residual Heat Removal Heat Exchangers 4
5,800(3) 8* 8A* *9 Containment Unit Coolers 2
540 Auxiliary Building Unit Coolers RWCU Pump and Heat Exchanger Room Unit Cooler 1
50 RPCCW Pumps and Heat Exchanger Room and CRD Transfer and Work Areas Unit Cooler 1
100 El 95'-9" Area Unit Cooler 1
90 HPCS Pump Room Unit Cooler 1
185 12*
RCIC Pump Room, LPCS Pump Room, and RHR Pump A and Heat Exchangers A and C Room Unit Cooler 1
235 14*
(1)
This number represents 50-percent capacity at 170 ft total head.
(2)
This nonessential equipment can be supplied by SSW if available.
- 9 (3)
The SSW flow to the RHR Heat Exchangers will be throttled to 3,000 gpm when the SCT Basin water level drops to an elevation of 90 ft following a LOP-LOCA.
9* *8A *8 8* 8A*
Revision 12 2 of 2 December 1999 TABLE 9.2-15 (Cont)
Design Data for Each Component Description Quantity (gpm)
Normal Switchgear and Electric Terminal Box Area Unit Cooler 1
150
- 1 Main Steam Pipe Tunnel, North End Unit Cooler 1
120 1*
RHR Pump B and Heat Exchangers B and D Room and RHR Pump C Room Unit Cooler 1
210 Elevation 114' HPCS Hatch and Elevator Area Unit Cooler 1
37
- 12 Upper Auxiliary Building Level Unit Coolers 2
410 12*
RHR Pump Seal Coolers 2
15 Fuel Pool Heat Exchangers 2
2,000 Penetration Valve Leakage Control Compressor 2
65 Drywell Unit Coolers(2) 6 334 Reactor Plant Component Cooling Heat Exchangers(2) 3 5,000 Annulus Ventilation Radiation Monitors 2
5 RHR Heat Exchanger Radiation Monitors 2
9
RBS USAR Revision 8A 1 of 1 October 1996 TABLE 9.2-16 STANDBY SERVICE WATER SYSTEM SINGLE PASSIVE FAILURE CRITERION ANALYSIS Single Passive Failure Consequence Failure of UHS This is not a credible cooling tower.
failure due to the design requirements for the tower.
Failure of plant make-Adequate UHS water inventory up water system makeup is provided to make up for line to storage basin.
drift and evaporative losses over a 30-day period.
Failure of HPCS diesel Header can be isolated by generator jacket cool-motor-operated valves.
er or area unit cooler Plant cooldown can be accom-service water headers.
plished using RHR pumps.
Failure of a cooling This is not a credible tower basin.
failure due to the design requirements for the basin.
Failure of the SSW The standby service water sys-pressure boundary for tem redundancy and intercon-any single loop due to nection provide availability pipe rupture, heat to perform the required cooling exchanger tubing rup-function.
ture, or pipe fitting (elbow toe, reducer, etc) rupture.
Failure of any manual The standby service water sys-valve, i.e., valve tem redundancy and intercon-fails opened or closed, nection provide availability contrary to its normal to perform the required cooling position.
function.
- 8A *8 8* 8A*
RBS USAR Revision 17 1 of 1 TABLE 9.2-17 LIST OF COOLERS SERVICED BY TURBINE PLANT COMPONENT COOLING WATER SYSTEM Component Coolers Quantity Generator Stator Coolers (including one spare) 2
8 8
Condensate Pump Motor and Thrust Bearing Coolers 3
Heater Drain Pump Lube Oil and Motor Bearing Coolers (including two spares) 4
12 Air Removal Pump Coolers (used during plant startup) 2 Reactor Feed Pump Lube Oil and Motor Bearing Coolers 3
Off Gas Glycol Condensers 3
- Waste Evaporator Overhead Condenser 1
- Regenerant Evaporator Overhead Condenser 1
- Waste Evaporator Distillate Cooler 1
Regenerant Evaporator Distillate Cooler 1
Off Gas Vault Refrigerant Condenser 2
Auxiliary Boiler Recirculation Pump Gland Cooler 2
- Waste Evaporator Vent Gas Cooler 1
Regenerant Evaporator Vent Gas Cooler 1
Isolated Phase Bus Duct Cooler 4
Auxiliary Boiler Sample Cooler 1
Turb. Bldg. Sample Coolers 6
Reactor Feed Pump Gear Increaser Lube Oil Coolers 3
Reactor Feed Pump Seal Water Heat Exchangers 3
- Instrument Air Comp. Water Jackets and Intercoolers 3
- Intrument Air After Coolers 3
Turb. Plant Sampling Fdwtr Corrosion Monitor Sample Cooler 1
Turb. Plant Sampling Refrigerating Units 1
13 Sample Precoolers (SST-PNL205B/ 206B/ 207B) 3 13
Reactor Feed Pump Seals 6
These components are not used during Normal Operation.
- These components are not connected.
12
RBS USAR Revision 12 1 of 2 December 1999 TABLE 9.2-18 DESIGN DATA FOR VENTILATION CHILLED WATER SYSTEM System Equipment and Design Data Turbine Building Subsystem Radwaste Building Subsystem
- 1. Centrifugal Liquid Chillers Equipment Mark No.
1HVN-CHL1A,B&C 1HVN-CHL2A,B&C Three 50-percent centrifugal liquid chillers for each building 12 Capacity 1250 tons 400 tons Entering chilled water temperature 72°F 65°F Leaving chilled water temperature 57°F 50°F Maximum chilled water capacity 2000 gpm 640 gpm Condenser cooling water requirements 3625 gpm 1200 gpm
- 2. Chilled Condenser Cooling Water Pumps Equipment Mark No.
1SWP-P4A,B&C 1SWP-P5A,B&C Three 50-percent pumps for each building Capacity 4000 gpm 1200 gpm Total head 31 ft 30 ft 12
- 2. Chilled Water Recirculation Pumps Equipment Mark No.
1HVN-P1A&B 1HVN-P4A&B Two 100-percent pumps for each building Capacity 3750 gpm 1550 gpm Total head 231 ft 115 ft
RBS USAR 2 of 2 August 1987 TABLE 9.2-18 (Cont)
System Equipment and Design Data Turbine Building Subsystem Radwaste Building Subsystem
- 4. Secondary Pumps Equipment Mark No.
1HVN-P2A&B Two 100-percent pumps for the fuel building Capacity 400 gpm Total head 161 ft
- 5. Compression Tank Equipment Mark No.
1HVN-TK1 1HVN-TK2 One 100-percent compression tank for each building Working capacity 665 gal 230 gal Design pressure 150 psig 150 psig
RBS USAR Revision 12 1 of 1 December 1999 TABLE 9.2-19 DESIGN DATA FOR THE CONTROL BUILDING CHILLED WATER SYSTEM Equipment Design Data 12 3 1 Centrifugal liquid chillers (Equipment Mark No.
1HVK*CHL1A, B, C, and D)
Capacity: 189 ton (100%)
Entering chilled water temperature: 67.5°F Leaving chilled water temperature: 52.5°F Chilled water capacity: 330 gpm/chiller Condenser cooling water requirements: 630 gpm/loop 12 Condenser cooling water pumps (Equipment Mark No.
1SWP*P3A, B, C and D)
Capacity: 630 gpm (100%)
Total head: 34 ft 1
Chilled water recirculation pumps (Equipment Mark No.
1HVK*P1A, B, C and D)
Capacity: 330 gpm (100%)
Total head: 145 ft 3
Compression tank (Equipment Mark No.
1HVK*TK1A and B)
Working capacity: 125 gal Design pressure: 150 psig
RBS USAR Revision 14 1 of 1 September 2001 6
TABLE 9.2-20 SERVICE WATER COOLING SYSTEM MAJOR COMPONENT DESIGN DATA 14 Description of Component Quantity Operating/
Available Total Operating 10 6 BTU/HR Design GPM for Each Component 14 Service Water Cooling Pumps (1) 2/3 31,500 Service Water Cooling System Flushable Filters 7/8 9,000 Service Water Cooling System Cooling Tower 1/1 444 63,000 NOTES:
(1) Approximate flow at 211 ft. developed head 6
RBS USAR TABLE 9.3-1 PROCESS SAMPLING SYSTEM Measured Description Sample Station Location Purpose Parameter Revision 16 1 of 8 March 2003 Reactor Steam Supply System Reactor Water 1G33-PNL Z020, Recirculation Pump Reactor Water CE & CP 1SSR-PNL 121 Discharge (Grab Sample Quality at the Sample Panel)
Main Steam 1SST-PNL 80 Main Steam Line (Grab Carryover/
CE Sample at the Sample Moisture Panel)
Standby Liquid Control System NA Borated Water Storage Borate Borate Tank (Local Grab Sample)
Concentration Concentration Reactor Water Cleanup System Filter/Demineralizer Influent 1G33-PNL Z020 Inlet Line (Grab Sample Reactor Water CE At the Sample Panel)
Quality Filter/Demineralizer Effluent 1G33-PNL Z020 &
Outlet Line (Grab Sample Filter CE & CP 1SRR-PNL 121 at the Sample Panel)
Efficiency Fuel Pool Cooling and Cleanup System
16 Purification Pump 1SSR-PNL 120 Discharge (Grab Sample Fuel Pool CE at the Sample Panel)
Water Quality Filter Effluent 1SSR-PNL 120 Outlet Line (Grab Sample Filter CE at the Sample Panel)
Efficiency Demineralizer Effluent 1SSR-PNL 120 Outlet Line (Grab Sample Demineralizer CE At the Sample Panel)
Efficiency 16
Measured Description Sample Station Location Purpose Parameter Revision 16 2 of 8 March 2003 Reactor Plant Component Cooling Water Cooling Water Sample 1SST-PNL 80 Outlet of Each Major Monitor Heat CE Heat Exchanger (Grab Exchanger Tube Sample at the Sample Leaks Panel)
Turbine Plant Component Cooling Water Cooling Water Sample 1SST-PNL 80 Outlet of Each Major Monitor Heat CE Heat Exchanger (Grab Exchanger Tube Sample at the Sample Leaks Panel)
Residual Heat Removal System Heat Exchanger Outlet 1SST-PNL 80 Outlet of Each Heat Water Quality CE Exchanger (Grab Sample at the Sample Panel)
Control Rod Drive System CRD Supply 1G33-PNL Z020 &
Inlet Line (Grab Sample Water Quality CE & CP 1SRR-PNL 121 at the Sample Panel)
Radwaste System
16 Waste Collector Tank 1SSW-PNL 130 Effluent (Grab Sample Process Data CE at the Sample Panel)
Demineralizer 1SSW-PNL 130 Effluent (Grab Sample Demineralizer CE at the Sample Panel)
Efficiency Filtrate Pump 1SSW-PNL 130 Effluent (Grab Sample Process Data CE at the Sample Panel) 16
Measured Description Sample Station Location Purpose Parameter Revision 16 3 of 8 March 2003
16 Demineralizer 1SSW-PNL 130 Influent (Grab Sample Process Data CE at the Sample Panel)
Demineralizer NA Acid Influent (Local Acid Concentration pH,CE Grab Sample)
Demineralizer NA Caustic Influent (Local Caustic pH,CE Grab Sample)
Concentration Recovery Sample Tank 1SSW-PNL 130 Effluent (Grab Sample Water Quality CE at the Sample Panel)
Floor Drain Collector Tank 1SSW-PNL 130 Effluent (Grab Sample Process Data CE at the Sample Panel)
Discharge Control 1SSW-PNL 130 Final Discharge (Grab Water Quality CE Sample at the Sample Panel)
Monitor Station RAD Liquid Activity Releases (Continuous)
Radwaste Filter 1SSW-PNL 130 Effluent (Grab Sample Filter CE at the Sample Panel)
Efficiency Regenerant Waste Tank 1SSW-PNL 130 Effluent (Grab Sample Process Data CE at the Sample Panel)
Regenerant Evaporator Bottoms 1SSW-PNL 130 Effluent (Grab Process Data CE Sample at the Sample Panel) 16
Phase Separator Tank NA Pump Discharge Process Data CE (Local Grab Sample)
Measured Description Sample Station Location Purpose Parameter Revision 16 4 of 8 March 2003
16 Waste Evaporator Bottoms 1SSW-PNL 130 Effluent (Grab Sample Process Data CE at the Sample Panel)
Waste Evaporator Distillate Cooler NA Effluent (Local Grab Process Data CE Sample)
Regenerant Evaporator Distillate NA Effluent (Local Grab Process Data CE Cooler Sample)
Radwaste Demineralizer Waste 1SSW-PNL 130 Effluent (Grab Sample Process Data CE Header At the Sample Panel)
TABLE 9.3-1 (Cont) 16
Water Treating System Cation Exchanger Unit 1SST-PNL 78 Influent (Grab Sample Process Data CE at the Sample Panel)
Cation Exchanger Unit 1SST-PNL 78 Effluent (Grab Sample Demineralizer CE at the Sample Panel)
Efficiency Anion Exchanger Unit 1SST-PNL 78 Influent (Grab Sample Process Data CE at the Sample Panel)
Anion Exchanger Unit 1SST-PNL 78 Effluent (Grab Sample Demineralizer CE,Si at the Sample Panel)
Efficiency Mixed-Bed Exchanger Unit 1SST-PNL 78 Influent (Grab Sample Process Data CE at the Sample Panel)
Mixed-Bed Exchanger Unit 1SST-PNL 78 Effluent (Grab Sample Demineralizer CE,Si at the Sample Panel)
Efficiency Dilute Acid NA Effluent (Local Grab Acid Concentration pH Sample)
Measured Description Sample Station Location Purpose Parameter 5 of 8 August 1988 Dilute Caustic NA Effluent (Local Grab Caustic pH Sample)
Concentration Wastewater NA Effluent (Local Grab Process Data CE Sample)
Condensate Demineralizer System Demineralizer (Train) 1SST-PNL 72 Influent Header (Grab Process Data CP,TU,O-,CE Sample at the Sample Panel)
Demineralizer (Train) 1SST-PNL 72 Effluent Header (Grab Demineralizer CP,TU,O-,CE Sample at the Sample Efficiency Panel)
Resin Hold Tank 1SST-PNL 72 Effluent (Grab Sample Process Data CE at the Sample Panel)
Demineralizers (10) 1SST-PNL 72 Effluent (Grab Sample Process Data CE,CP at the Sample Panel)
Ultrasonic Resin Cleaner NA Effluent (Local Grab Process Data CE Sample)
Resin Mix Tank 1SST-PNL 72 Effluent (Grab Sample Process Data CE at the Sample Panel)
Cation Regeneration Tank 1SST-PNL 72 Effluent (Grab Sample Process Data CE at the Sample Panel)
Anion Regeneration Tank 1SST-PNL 72 Effluent (Grab Sample Process Data CE at the Sample Panel)
Recovered Acid Tank NA Effluent (Local Grab Acid Concentration pH,CE Sample)
Dilute Acid NA Effluent (Local Grab Acid Concentration pH,CE Sample)
Measured Description Sample Station Location Purpose Parameter 6 of 8 August 1988 Recovered Caustic Tank NA Effluent (Local Grab Caustic pH,CE Sample)
Concentration Dilute Caustic NA Effluent (Local Grab Caustic pH,CE Sample)
Concentration Recovered Water Sump NA Pump Discharge (Local Process Data pH,CE Grab Sample)
Condensate Makeup and Drawoff System
1 Condensate ISSR-PNL 120 Pump Discharge (Grab Condensate CE Sample at the Sample Quality Panel) 1
Makeup Water System Demineralizer Water 1SST-PNL 80 Transfer Line (Grab Demineralizer CE Sample at the Sample Water Quality Panel)
Wastewater Treatment System Waste Neutralizing Tank NA Effluent (Local Grab Process Data CE Sample)
Condensate System Condensate 1SST-PNL 80 Condensate Pump Condensate Quality CE Discharge (Grab Sample and Condenser Tube at the Sample Panel)
Leaks Condenser NA Hotwell (Local Sample Condenser Tube CE Probe and Monitor)
Leaks Heater Drains 1SST-PNL 80 Third Point Heater Water Quality and CP,TU,O-Drains (Grab Sample
- Concentration at the Sample Panel)
Measured Description Sample Station Location Purpose Parameter Revision 13 7 of 8 September 2000 Reactor Feedwater System Feedwater 1SST-PNL 80 and After Last Heater (Grab Feedwater Quality CE,pH,O-,
1BZ1-PNL Z001 Sample at the Sample and Check Corrosion TU,CP
13 SST-PNL207**
Panel) 13
Circulating Water System Effluent NA Blowdown Line (Local Monitor Station CE,RAD Online Monitor)
Liquid Activity Releases Auxiliary Steam System Auxiliary Boiler 1SST-PNL 78 Steam Outlet (Grab Water Quality CE Sample at the Sample Panel)
Feedwater 1SST-PNL 78 Feedpump Discharge Water Quality CE,O-(Grab Sample at the Sample Panel)
Auxiliary Boiler NA Blowdown (Local Water Quality CE Conductivity Element)
Sealing Steam System Sealing Steam Evaporator 1SST-PNL 80 Evaporator Effluent Steam Quality CE (Grab Sample at the Sample Panel)
9
- Note: 1BZ1-PNLZ001 does not measure turbidity 9
13
- SST-PNL207 is for corrosion products sample collection 13
Measured Description Sample Station Location Purpose Parameter 8 of 8 August 1988 Radwaste Steam Supply Radwaste Steam Reboiler 1SST-PNL 80 Reboiler Discharge Steam Quality CE (Radwaste Auxiliary Steam)
(Grab Sample at the Sample Panel)
Containment Sumps Equipment Drain Sumps N/A Equipment Drain Sump Water Quality As Required Pump Discharge (Local Grab Sample)
Floor Drain Sumps N/A Floor Drain Sump Pump Water Quality As Required Discharge (Local Grab Sample)
Key to Sample Stations:
Key to Measured Parameters:
1G33-PNL Z020 - Reactor Plant Sample Station CE - Conductivity 1SSR-PNL 121 - Reactor Plant Corrosion Product Monitor pH - pH 1SSR-PNL 120 - Fuel Building Sample Station TU - Turbidity 1SST-PNL 72 - Condensate Demineralizer Area Sample Station O2 - Dissolved Oxygen 1SST-PNL 78 - Water Treatment Building Station Si - Silica 1SST-PNL 80 - Turbine Building Sample Station CP - Corrosion Products 1SSW-PNL 1 - Radwaste Building Sample Station RAD-Radiation (See Section 11.5 for 1B21-PNL Z001 - Feedwater System Corrosion Product Monitor monitors that specifically measure radiation levels of radioactive samples)
RBS USAR TABLE 9.3-1a EQUIPMENT AND FLOOR DRAINAGE SYSTEMS COMPONENT CAPACITIES 1 of 1 August 1987 Pump Sump Mark Sump Pump Data Nominal Sump Capacity Number Pump 1 Pump 2 Capacity (gal) (gpm, each) 1DFT-TK1A 1DFT-P1A 1DFT-P1D 650 50 1DFT-TK1B 1DFT-P1B 1DFT-P1E 830 50 1DFT-TK1C 1DFT-P1C 1DFT-P1F 710 50 1DFT-TK2A 1DFT-P2A 1DFT-P2C 710 50 1DFT-TK2B 1DFT-P2B 1DFT-P2D 770 50 1DFT-TK3 1DFT-P3A 1DFT-P3B 590 50 1DET-TK1A 1DET-P1A 1DET-P1D 710 50 1DET-TK1B 1DET-P1B 1DET-P1E 710 50 1DET-TK1C 1DET-P1C 1DET-P1F 830 50 1DFT-TK7 1DFT-P7A 1DFT-P7B 950 50 1DFM-TK4 1DFM-P4A 1DFM-P4B 710 50 1DFM-TK7 1DFM-P7 None 400 50 1DFM-TK8 1DFM-P8 None 400 50 1DFM-TK9 1DFM-P9 None 400 50 1DFM-TK11 1DFM-P11 None 370 50 1DFM-TK1 1DFM-P1 None 260 50 1DFM-TK2 1DFM-P2 None 260 50 1DFM-TK3 1DFM-P3 None 260 50 1DFM-TK5 1DFM-P5A 1DFM-P5B 340 50 1DFM-TK6 1DFM-P6A 1DFM-P6B 490 50 1DFW-TK1A 1DFW-P1A 1DFW-P1C 710 50 1DFW-TK1B 1DFW-P1B 1DFW-P1D 710 50 1DFW-TK2 1DFW-P2A 1DFW-P2B 950 50 1DFA-TK4 1DFA-P4A 1DFA-P4B 710 50 1DER-TK1 1DER-P1A 1DER-P1B 950 50 1DER-TK2 1DER-P2A 1DER-P2B 770 50 1DER-TK3 1DER-P3A 1DER-P3B 770 50 1DFR-TK1 1DFR-P1A 1DFR-P1B 830 50 1DFR-TK2 1DFR-P2A 1DFR-P2B 590 50 1DFR-TK3A 1DFR-P3A 1DFR-P3G 530 50 1DFR-TK3B 1DFR-P3B 1DFR-P3H 590 50 1DFR-TK3C 1DFR-P3C 1DFR-P3J 530 50 1DFR-TK3D 1DFR-P3D 1DFR-P3K 530 50 1DFR-TK3E 1DFR-P3E 1DFR-P3L 530 50 1DFR-TK3F 1DFR-P3F 1DFR-P3M 530 50 1DFR-TK5A 1DFR-P5A 1DFR-P5D 650 50 1DFR-TK5B 1DFR-P5B 1DFR-P5E 650 50 1DFR-TK5C 1DFR-P5C 1DFR-P5F 650 50 1DFR-TK6 1DFR-P6A 1DFR-P6B 350 50
RBS USAR TABLE 9.3-2 STANDBY LIQUID CONTROL SYSTEM OPERATING PRESSURE/TEMPERATURE CONDITIONS SLCS Modes(1)
Standby Mode(1)
Circulation Test Injection Test(2) Operating Mode(1)¸ Revision 15 1 of 2 May 2002 Pressure Temp Pressure Temp Pressure Temp Pressure Temp Piping (psig)(3)
(°F)
(psig)(3)
(°F)
(psig)(3)
(°F)
(psig)(3)
(°F)
- 12 Pump Makeup 70/100 Test Tank 70/100 Test Tank 70/100 Storage 70/110 Suction Water (4)
Static (4)
Static (4)
Tank (4)
Pressure Head(5)
Head(5)
Static Head
- 15 Pump Dis-Makeup 70/100 0/1250 70/100 70 Plus 70/100 (70 Plus 70/110 charge to Water Reactor Reactor Explosive Pressure Static Static Valve Inlet Head Head) To 1,250 12*
Explosive Reactor 70/100 Reactor 70/100
<70 Plus 70/100
(<70 Plus 70/110 Valve Outlet Static Static Reactor Reactor to but not Head To Head To Static Static Including 1,180(6) 1,180(6)
Head Head) To First Iso-
<1,250 lation Check Valve First Iso-Reactor 70/565 Reactor 70/565 Reactor 125(2)
Reactor 70/560 lation Static (7)
Static (7)
Static Static (7)
Check Valve Head To Head Head(2)
Head To to the 1,180(6) 1,180(6)
Reactor 15*
RBS USAR Revision 15 2 of 2 May 2002 TABLE 9.3-2 (Cont)
Notes to Table 9.3-2:
(1)The pump flow rate is zero (pump not operating) during the standby mode and at rated capacity during the test and operating modes.
(2)Reactor to be at 0 psig and 125°F before changing from the standby mode to the injection test mode.
(3)Pressures tabulated represent pressure at the points identified below. To obtain pressure at intermediate points in the system, the pressures tabulated must be adjusted for elevation difference and pressure drop between such intermediate points and the pressure points identified below:
Piping Pressure Point Pump suction Pump suction flange inlet Pump discharge to ex-Pump discharge flange plosive valve inlet outlet Explosive valve outlet to but not including first isolation check valve Explosive valve outlet First isolation check valve to the reactor Reactor sparger outlet (4)During chemical mixing, the liquid in the storage tank is at a temperature of 150°F maximum.
(5)Pump suction piping is subject to demineralized water supply pressure during flushing and filling of the piping and during any testing where suction is taken directly from the demineralized water supply line rather than a test tank.
- 15 (6)Maximum reactor operating pressure is 1,180 psig at reactor standby liquid control sparger outlet.
(7)565°F represents maximum sustained operating temperature.
15*
RBS USAR TABLE 9.3-3 Revision 10 1 of 1 April 1998 PVLCS PROCESS LINE INFORMATION THIS TABLE HAS BEEN DELETED
- Based on manufacturer's requirements.
- 3
- See Section 9.3.1.1.2 for clarification for Category 2
actuators on Category 1 valves/dampers.
3*
Revision 3 1 of 1 August 1990 TABLE 9.3-4
- 3 SAFETY-RELATED EQUIPMENT SUPPLIED BY INSTRUMENT AIR SYSTEM**
3*
Maximum Allowable Particle Size*
Description (microns)
Air-operated ventilation 175 shutoff valves Testable check for inboard 175 and outboard containment isolation valves Air-operated ventilation 155 shutoff dampers Drywell penetration 40 isolation valves Standby liquid control storage tanks Hydraulic control unit for CRDs Scram discharge volume 5
vent and drain valves
RBS USAR TABLE 9.3-5 POST-ACCIDENT SAMPLING SYSTEM ANALYSES INSTRUMENTATION Design Design Design Parameter Method Bases Range Bases Accuracy Bases Time 1 of 1 August 1987 Gross acti-Gamma spectroscopy 0.1 Ci/ml to
+50 percent
<3 hours vity gamma 10 Ci/ml spectrum Boron Plasma spectometry 0 - 6000 ppm
+5 percent
<3 hours Titrimetry (manitol) 1 - 100 ppm Chloride Offsite analysis N/A N/A
<96 hours Total dis-GE dissolved gas procedure 25 cc/kg to
+50 percent
<3 hours solved gas 50 cc/kg greater
+30 percent than 50 cc/kg pH Micro electrode 1-13 pH units
+0.3 pH units
<3 hours Hydrogen Gas chromatograph 50 - 2000 cc/kg
+10 percent
<3 hours 0 - 50 cc/kg
+5 percent Dissolved Via dissolved hydrogen Verifies that N/A
<3 hours oxygen concentration at greater dissolved than 10 cc/kg oxygen is less than 0.1 ppm
RBS USAR TABLE 9.4-1 ENVIRONMENTAL AND SYSTEM DESIGN PARAMETERS FOR HVAC
16 (See note 27 on page 5 of 5)
Operates Provision Degree of Under for Rad Temperature (°F)
Pressure (in W.G.)
Rel. Humidity (%)
ESF Redundancy Post-Monitor at Normal Post Normal Post Normal Post Power (Major Accident Release Range LOCA Range LOCA Range LOCA Reqd.
Components)
Condition Point 16
12 9 Revision 18 1 of 5 Control building 75 max 80 max 0.125 min 0.125 min 20-70 20-70 Yes 2-100%
Yes Yes, at main control 65 min 65 min (18)
(18) intake room 9
Control building A.C. equipment 90 max 90 max 0.125 min 0.125 min 20-60 20-60 Yes 2-100%
Yes Yes, at room (for main 60 min 60 min (18)
(18) intake control room equipment) 12
Control building 90 max 90 max Atmos Atmos 20-85 20-85 Yes 2-100%
Yes Yes, at battery rooms 60 min 60 min intake Control building switchgear, refrig 104 max 104 max Atmos Atmos 20-90 20-90 Yes 2-100%(5)
Yes Yes, at machinery rooms, 40 min 40 min intake inverter rooms and cable vaults Control building 104 max 104 max Atmos Atmos 20-90 20-90 Yes 2-100%
Yes Yes, at general areas 40 min 40 min intake 3
14 13 8 4 Fuel building 96 max 125 max Equal or Equal or 20-90 20-90 (6) 2-100%
(6)
Yes general areas 40 min less than less than 0.00
-0.25 (21)(22) 13
Fuel Pool 96 max 125 max Equal or Equal or 20-100 20-100 (6) 2-100%
(6)
Yes area 40 min less than less than 0.00
-0.25 (21)(22)
Cubicles 120 max 138 max Equal or Equal or 20-90 20-90 (6) 2-100%
(6)
Yes 40 min less than less than 0.00
-0.25 (21)(22) 4 8 14
RBS USAR TABLE 9.4-1 (Continued)
16 (See note 27 on page 5 of 5)
Operates Provision Degree of Under for Rad Temperature (°F)
Pressure (in W.G.)
Rel. Humidity (%)
ESF Redundancy Post-Monitor at Normal Post Normal Post Normal Post Power (Major Accident Release Range LOCA Range LOCA Range LOCA Reqd.
Components)
Condition Point Revision 18 2 of 5
12 8
Auxiliary building NA Uncon-NA
-0.25 min NA Uncon-Yes 2-100%
Yes Yes SGTS system trolled trolled Auxiliary building 122 max 132 max Atmos
-0.25 min 20-90 20-100 Yes 2-100%
Yes Yes general areas 40 min 40 min (19)
(19)
Auxiliary building 122 max 127 max Atmos
-0.25 min 20-90 20-100 Yes 2-100%
Yes Yes cubicles (17)
(17)
(19)
(19) 40 min 40 min 8 12 16
Radwaste building 96-104 NA
0.00 NA 20-90 NA No (7)
No Yes all areas max 40 min Turbine building 96-120 NA
0.00 NA 20-90 NA No 3-50%
No Yes all areas max Exh fans 40 min Offgas, condensate, 75(8)-
NA
-0.125 NA 20-90 NA No 2-100%
No Yes and demineralizer 120 max buildings 40 min Offgas char vault
-40 min NA
-0.125 NA 0
NA No 2-100%
No Yes 16
15 9 Diesel-gen bldg:
operating area 120 max 120 max Atmos Atmos20-100 50 Yes 2-100%
Yes Yes 40 min(23) 40 min(23) 2 min(24) 2 min(24) 9
control room 104 max 104 max Atmos Atmos20-100 50 Yes 2-100%
Yes Yes area 40 min(23) 40 min(23) 2 min(24) 2 min(24) 15
Standby service 109 max 109 max Atmos Atmos20-100 20-100 Yes 2-100%
Yes No water cooling 40 min 40 min tower; swgr, transfmr, and pump rooms
RBS USAR TABLE 9.4-1 (Continued)
16 (See note 27 on page 5 of 5)
Operates Provision Degree of Under for Rad Temperature (°F)
Pressure (in W.G.)
Rel. Humidity (%)
ESF Redundancy Post-Monitor at Normal Post Normal Post Normal Post Power (Major Accident Release Range LOCA Range LOCA Range LOCA Reqd.
Components)
Condition Point Revision 18 3 of 5 Standby service 104 max 104 max Atmos Atmos 95 max 95 max Yes 2-100%
Yes No water cooling 35 min 35 min tower; remote air intake room Standby service 102 max 106 max Atmos Atmos 40 100 Yes 10-100%
Yes No water cooling 25 min tower; fan deck
12 Reactor building 90 max NA(9)
NA 20-50 (13) NA Yes 3-50%
Yes Yes containment 70 min
+/-8.3 (25)
2 Reactor building 145 max NA
+41.7 to NA 20-50 (13) NA (10) 6-25%
No Yes drywell 70 min 0.0 (26) 2 16
14 Reactor building 120 max NA
-3.0 min
-0.50 min 12-100 NA Yes 2-100%
Yes Yes annulus 40 min (14) (20) (15) (20) 12 14
3 Control building 90 max 90 max Atmos Atmos 20-60 20-60 Yes 2-100%
Yes Yes, at remote shutdown 40 min 40 min intake panel rooms 3
15 Fire pumphouse 104 max NA
-0.125 NA 100 max NA No None No No 40 min 15
Water treatment 104 max NA 0.125 NA 100 max NA No None No No building 60 min Makeup water 120 max NA Atmos NA 100 max NA No 2-100%
No No intake structure 65 min and switchgear house Motor generator 120 max NA 0.125 NA 100 max NA No None No No building 25 min Demineralized 104 max NA
-0.125 NA 100 max NA No None No No water pumphouse 40 min
RBS USAR TABLE 9.4-1 (Continued)
16 (See note 27 on page 5 of 5)
Operates Provision Degree of Under for Rad Temperature (°F)
Pressure (in W.G.)
Rel. Humidity (%)
ESF Redundancy Post-Monitor at Normal Post Normal Post Normal Post Power (Major Accident Release Range LOCA Range LOCA Range LOCA Reqd.
Components)
Condition Point 16
Revision 16 4 of 5 March 2003 Normal switchgear 104/80 NA 0.25/
NA 90/20 NA No 2-100%(11)
No No building max
-0.125 75/25 min Auxiliary boiler 104 max NA
-0.125/
NA 100 max NA No None No No building 40 min
-0.25 Cooling tower 109 max NA 0.125 NA 85 max NA No None No No switchgear house 40 min
2 Electrical and 122 max(17)122 max(17)-0.125 NA 100 max 50 max No (12)
No No piping tunnels 40 min 2
Circ H20 pH and 104 max NA 0.125 NA 100 max NA No None No No switchgear room 60 min Auxiliary control 72/104 NA
-0.125/
NA 100 max NA No 2-100%
No No building max
-0.25 60/72 min Clarifier area 104 max NA 0.125 NA 100 max NA No None No No switchgear house 40 min Hypochlorite area 104 max NA 0.125 NA 100 max NA No None No No switchgear house 25 min Blowdown pit NA max NA NA NA 95 max NA NA NA NA NA NA min (16)
RBS USAR TABLE 9.4-1 (Continued)
Revision 16 5 of 5 March 2003 (1)
Outside design conditions: Summer: 96°F dry bulb, 81°F wet bulb Winter: 25°F dry bulb (2)
Normal conditions: Those operating conditions that exist during routine plant operation or testing, including normal plant operation, shutdown, and hot standby.
(3)
No heating is provided to maintain a minimum of 40°F following LOCA and loss-of-offsite power.
(4)
Conditions list are essentially steady state and do not reflect transients.
(5)
Refrigeration machinery room: 1-100% normal 2-100% accident (6)
Normal supply and exhaust system operates only in normal mode. Charcoal filtration system operates only in accident mode. ESF required only in accident mode.
(7) 3-50% exhaust fans 2-100% filter units and exhaust fans (8)
Sample room only.
(9)
During accident one unit cooler runs as part of containment heat removal system.
(10) ESF power provided on loss-of-offsite power only.
(11) Plus 1-100% battery and computer rooms.
(12) (2) systems 2-100%; (8) systems 1-100%.
12 9 (13) During shutdown conditions elevated relative humidities may be present. Humidity is maintained to prevent condensation.
9
14 (14) Negative pressure of at least -3 W. G. provided by annulus pressure control system.
(15) -0.50 W. G. min negative pressure with respect to outside atmosphere provided by standby gas treatment system post accident.
(16) Limiting relative humidity only.
14
16 2 (17) Normal and post LOCA maximum temperature in the main steam tunnel (north) is 135°F.
2
13 (18) A pressure up to +5.0 W. G. may result with Control Room Fresh Air System train(s) operating.
(19) A pressure up to -9.0 W. G. may result with SGTS train(s) operating.
(20)
A pressure up to -14.0 W. G. may result with SGTS train(s) operating.
(21)
A pressure up to -2.0 W. G. may result with Fuel Building Charcoal filter train(s) operating.
12 13
14 (22)
Fuel Building integrity is only credited during fuel handling accidents involving recently irradiated fuel.
14
15 (23)
Diesel Generator in standby (24)
Diesel Generator running during winter minimum temperature 15
(25)
Normal pressure range for reactor building containment is equivalent to +/-0.3 psig.
(26)
Normal pressure range for reactor building drywell is equivalent to +1.5 psig to 0.0 psig (+1.2 psid to -0.3 psid).
(27)
The design parameters (Temperature, Pressure, Relative Humidity) represent the range of environmental design parameters for general areas or buildings. Refer to design specification 215.150, Environmental Design Criteria, for the requirements of specific areas.
16
RBS USAR TABLE 9.4-2 DESIGN DATA FOR THE AUXILIARY BUILDING HVAC SYSTEM Equipment Design Data Revision 3 1 of 4 August 1990
- 1. Main Control Room Air-Conditioning Units Equipment Mark No.
1HVC*ACU1A&B This system includes two 100-percent units and two 100-percent electric duct heaters
3
- a. Air-Conditioning Units:
Air flow capacity 38,200 scfm Cooling capacity 980 mbh Leaving air temperature 60.6°F dB Chilled water flow 101 gpm 3
- b. Heating Coils:
Equipment Mark No.
1HVC*CH1A&B Type Electric, finned tubular Heating capacity 65 kW
- 2. Standby Switchgear Room Air-Conditioning Units Equipment Mark No.
1HVC*ACU2A&B This system includes two 100-percent units, two 100-percent return air fans, and six battery rooms exhaust fans (two 100-percent fans for each room)
3
- a. Air-Conditioning Units:
Air flow capacity 29,330 scfm Cooling capacity 950 mbh Heating capacity 50 kW Leaving air temperature 66.2°F dB Chilled water flow 62.3 gpm 3
- b. Return Air Fans:
Equipment Mark No.
1HVC*FN2A&B Type Vaneaxial Air flow capacity 25,330 scfm Static Pressure 4.5 in W.G.
Equipment Design Data Revision 3 2 of 4 August 1990
- c. Battery Rooms Exhaust Fans:
Equipment Mark No.
1HVC*FN3A,B,C,D, E,F Type Centrifugal, non-sparking Air flow capacity 1,430 cfm Static pressure 2.6 in W.G.
- 3. Chiller Equipment Room Air-Conditioning Units Equipment Mark No.
1HVC*ACU3A&B This system includes two 100-percent units, one ventilation supply fan, and one ventilation exhaust fan
3
- a. Air-conditioning units:
Air flow capacity 3,500 scfm Cooling capacity 165 mbh Leaving air temperature 90.0°F dB Chilled water flow 28 gpm 3
- b. Supply fans:
Equipment Mark No.
1HVC-FN6 Type Centrifugal Air flow capacity 1,100 scfm Static pressure 2 in W.G.
- c. Exhaust fan:
Equipment Mark No.
1HVC-FN11 Type Centrifugal Air flow capacity 1,100 scfm Static pressure 1 in W.G.
- 4. Main Control Room Charcoal Filter Trains Equipment Mark No.
1HVC*FLT3A&B This system includes two 100-percent filter trains with associated boosters and decay heat removal fans
- a. Charcoal filter trains:
(1) Charcoal filters:
Type Deep bed,
Equipment Design Data Revision 17 3 of 4 Capacity 4,000 cfm Media Impregnated coconut shell charcoal Radioiodine removal 98% elemental iodine and 98% methyliodine, test at 70%
relative humidity Depth of each bed 4 in Face velocity 40 fpm Ignition temperature 340°C Density 30 lbs/ft3 (2) HEPA filters:
Type High efficiency, dry Capacity 4,000 cfm Media Fiberglass U.L.
Class I Efficiency, based on 99.97% with 0.3 micron DOP test (MIL-STD-282)
DOP aerosol Pressure drop, clean 1.0 in W.G.
(3) Prefilter:
Type Medium efficiency, dry Capacity 4,000 cfm Media Fiberglass Efficiency 80% NBS dust spot test Pressure drop, clean 0.45 in W.G.
(4) Heater:
Type Finned tubular Capacity 23 KW Stages One (5) Moisture separator:
Type Multiple bed Capacity 4,000 cfm
7 Media Louvers and Glass or Stainless steel pads 7
Equipment Design Data 4 of 4 August 1987 Pressure drop, clean 1.0 in W.G.
- b. Booster fans:
Equipment Mark No.
1HVC*FN1A&1B Type Centrifugal Air flow capacity 4,000 cfm Static pressure 20 in W.G.
- c. Decay heat removal fans:
Equipment Mark No.
1HVC*FN8A&B Type Centrifugal Air flow capacity 100 cfm Static pressure 1.0 in W.G.
- 5. Smoke Removal Fans Main Control Room Equipment Mark No.
1HVC-FN9 Type Vaneaxial Air flow capacity 13,200 cfm Static pressure 5.7 in W.G.
Standby Switchgear Rooms Equipment Mark No.
1HVC-FN10 Type Centrifugal Air flow capacity 4,000 cfm Static pressure 11 in W.G.
RBS USAR TABLE 9.4-3 DESIGN DATA FOR THE FUEL BUILDING HVAC SYSTEM Equipment Design Data 1 of 5 August 1987 1.
Supply Air System Air Conditioning Unit Equipment Mark No.
1HVF-ACU1 Total design air flow (outside), cfm 9,000 This system consists of a builtup air-conditioning unit with two 100-percent capacity supply fans.
The following are the major components with design data:
a.
Filters Type Horizontal, roll Airflow capacity, cfm 9,000 Filter pressure drop (dirty),
in W.G.
1.5 Face velocity (Max), fpm 475 Filter efficiency (average) 20% min (ASHRAE dust spot test) b.
Heating coil Type Electric finned tube Heating capacity, kW 57 Number of stages 4
c.
Cooling coil Design pressure/temp psig/°F 200/300 Type Chilled water Total cooling capacity, mbh 740.1 No. of coils 1
No. of circuits per coil 30 d.
Supply air fan Type Vaneaxial Airflow capacity, cfm 9,000 Total pressure capability, in W.G.
5.58 Speed, rpm 3,500 Motor, hp 15 Type of discharge Horizontal
Equipment Design Data Revision 15 2 of 5 May 2002 2.
Unit Coolers a.
CRD Water Pump Area Equipment Mark No.
1HVF-UC1 Cooling capacity of cooler, mbh 190.5 Cooler airflow, cfm 7,200 Fan type Vaneaxial Motor, hp 15 Filter type Disposable Filter efficiency (average) 20% min (ASHRE dust spot test)
- 15 b.
General Area El. 70'-0" Equipment Mark No.
1HVF-UC2 Cooling capacity of cooler, mbh 214.5 Cooler airflow, cfm 5,500 Fan type Vaneaxial Motor, hp 5
Filter type Disposable Filter efficiency (average) 20% min (ASHRAE dust spot test) c.
New Fuel Receiving Area Equipment Mark No.
1HVF-UC3 Cooling capacity of cooler, mbh 121.2 Cooler airflow, cfm 3,600 Fan type Vaneaxial Motor, hp 3
Filter type Disposable Filter efficiency (average) 20% min (ASHRAE) dust spot test) 15*
d.
General Area El. 113'-0" Equipment Mark No.
1HVF-UC4 Cooling capacity of cooler, mbh 304.2 Cooler airflow, cfm 8,700 Fan type Vaneaxial Motor, hp 10 Filter type Disposable Filter efficiency (average) 20% min (ASHRAE dust spot test) e.
General Area & Fan Room Equipment Mark No.
1HVF-UC5 Cooling capacity of cooler, mbh LTR Cooler air flow, cfm 4,200
Equipment Design Data 3 of 5 August 1987 Fan type Vaneaxial Motor, hp LTR Filter type Disposable Filter efficiency (average) 20% min (ASHRAE dust spot test) f.
Fuel Receiving and Cask Washdown Area Equipment Mark No.
1HVF-UC6 Cooling capacity, mbh 261.9 Cooler air flow, cfm 7,700 Fan type Vaneaxial Motor, hp LTR Filter type Disposable Filter efficiency 20% min (ASHRAE dust spot test) g.
General Area and Electric Equipment Area Equipment Mark No.
1HVF-UC7 Cooling capacity of cooler, mbh 342.0 Cooler Air Flow, CFM 10,250 Fan type Vaneaxial Motor, hp LTR Filter type Disposable Filter efficiency (average) 20% min (ASHRAE dust spot test) h.
Charcoal Filter Rooms Equipment Mark No.
1HVF-UC8 Cooling capacity of cooler, mbh LTR Cooler air flow, CFM 4,500 Fan type Vaneaxial Motor, hp LTR Filter type Disposable Filter efficiency (average) 20% min (ASHRAE dust spot test) 3.
Exhaust Air System Exhaust Fans Equipment Mark No.
1HVF-FN8A & 8B Type Vaneaxial Airflow capacity, cfm 10,000 Total pressure capability, in W.G.
4 Speed, rpm 3,500 Motor, hp LTR
Equipment Design Data 4 of 5 August 1987 Type of discharge Horizontal 4.
Charcoal Filtration System Equipment Mark No.
1HVF*FLT 2A & 2B Total design air flow, cfm 10,000 This system consists of two 100-percent filter units with two 100-percent capacity exhaust fans.
Each filter unit consists of following components:
a.
Moisture separators Flow rate, cfm (max) 10,000 Pressure drop, in W.G.
1.0 Face velocity, fpm 40 b.
Electric heating coil Capacity, kW 57 Pressure drop, in W.G.
0.5 Type Finned, tubular c.
Prefilters Pressure drop, in W.G. (dirty) 1.0 Filter efficiency 80-85% NBS dust spot test Dust holding capacity 300 gm Filter media Fiberglass d.
HEPA filters Each cell, air flow capacity, cfm 1,000 Filter efficiency 99.97%
Pressure drop, in W.G.
1.0 Each filter cell size 24"x24"x11 1/2" e.
Charcoal filters Type Deep bed, rechargeable Capacity 10,000 cfm Media Impregnated coconut shell charcoal Radioiodine Removal 99% elemental iodine and 99%
methyliodine, test at 70%
relative
Equipment Design Data 5 of 5 August 1987 humidity Depth of each bed 4 in Face velocity 40 fpm Pressure drop, clean 1.0 in W.G.
Ignition temperature 340°C Density 30 lbs/ft³ f.
Exhaust fan Equipment Mark No.
1HVF*FN 3A & 3B Type Centrifugal Airflow capacity, cfm 10,000 Static pressure, in W.G.
16 Speed, rpm 1,720 Motor, hp 40 g.
Decay heat removal exhaust fan Equipment Mark No.
1HVF*FN 7A & 7B Type Centrifugal Airflow capacity, cfm 100 Drive Direct Static pressure, in W.G.
2.5 Motor, hp 0.5 h.
Heating coils Equipment Mark No.
1HVF-CH1 Type Finned tubular Heating capacity, kW 8
Equipment Mark No.
1HVF-CH2 Type Finned tubular Heating capacity, kW 3
RBS USAR Revision 16 1 of 4 March 2003 TABLE 9.4-4 DESIGN DATA FOR THE AUXILIARY BUILDING HVAC SYSTEM Equipment Design Data
- 1.
Standby Gas Treatment Units Equipment Mark No.
1GTS*FLT1A & 1B Refer to Section 6.5 for design data of SGTS
16 14 8
- 2.
Unit Cooler Equipment Mark No.
1HVR*UC2 Cooling capacity (mbh) 187.46 Cooler air flow (cfm) 6,700 Fan type Vaneaxial Motor (hp) 5 Cooling medium Standby service water Flow rate (gpm, max) 50 Leaving air temp dry/wet bulb (°F) 98.03/80.4
15 5
- 3.
Unit Cooler Equipment Mark No.
1HVR*UC3 Cooling capacity (mbh) 318.22 Cooler air flow (cfm) 13,000 Fan type Vaneaxial Motor (hp) 7.5 Cooling medium Standby service water Flow rate (gpm, max) 100 Leaving air temp dry/wet bulb (°F) 97.87/81.3
- 4.
Unit Cooler Equipment Mark No.
1HVR*UC4 Cooling capacity (mbh) 293.22 Cooler air flow (cfm) 11,800 Fan type Vaneaxial Motor (hp) 7.5 Cooling medium Standby service water Flow rate (gpm, max) 90 Leaving air temp dry/wet bulb (°F) 97.6/81.2 5 8 14 15 16
Revision 16 2 of 4 March 2003 Equipment Design Data
16 14 8A
- 5.
Unit Cooler Equipment Mark No.
1HVR*UC5 Cooling capacity (mbh) 721.91 Cooler air flow (cfm) 24,000 Fan type Vaneaxial Motor (hp) 50 Cooling medium Standby service water Flow rate (gpm, max) 185 Leaving air temp dry/wet bulb (°F) 97.35/80.0 8A
- 6.
Unit Cooler Equipment Mark No.
1HVR*UC6 Cooling capacity (mbh) 927.68 Cooler air flow (cfm) 31,000 Fan type Vaneaxial Motor (hp) 40 Cooling medium Standby service water Flow rate (gpm, max) 235 Leaving air temp dry/wet bulb (°F) 97.53/80.0 16
15 5
- 7.
Unit Cooler Equipment Mark No.
1HVR*UC7 Cooling capacity (mbh) 486.08 Cooler air flow (cfm) 19,800 Fan type Vaneaxial Motor (hp) 15 Cooling medium Standby service water Flow rate (gpm, max) 150 Leaving air temp dry/wet bulb (°F) 97.85/81.3 5 15
3
- 8.
Unit Cooler Equipment Mark No.
1HVR*UC8 Cooling capacity (mbh) 405.38 Cooler air flow(cfm) 18,000 Fan type Vaneaxial Motor (hp) 15 Cooling medium Standby service water Flow rate (gpm, max) 120 Leaving air temp dry/wet bulb (°F) 97.95/81.3 3 8 14
Revision 16 3 of 4 March 2003 Equipment Design Data
16 15 14 8 5
- 9.
Unit Cooler Equipment Mark No.
1HVR*UC9 Cooling Capacity(mbh) 692.07 Cooler air flow (cfm) 27,400 Fan type Vaneaxial Motor (hp) 30 Cooling medium Standby service water Flow rate (gpm, max) 210 Leaving air temp dry/wet bulb (°F) 97.16/81.1
- 10. Unit Cooler Equipment Mark No.
1HVR*UC10 Cooling Capacity(mbh) 118.66 Cooler air flow (cfm) 4,900 Fan type Vaneaxial Motor (hp) 5 Cooling medium Standby service water Flow rate (gpm, max) 37 Leaving air temp dry/wet bulb (°F) 98.06/81.3
- 11. Unit Cooler Equipment Mark No.
1HVR*UC11A & 11B Cooling Capacity(mbh) 1011.82 Cooler air flow (cfm) 53,000 (11A) and (11B)
Fan type Vaneaxial Motor (hp) 75 Cooling medium Standby service water Flow rate (gpm, max) 410 Leaving air temp dry/wet bulb (°F) 96.94/82.5 5 15 16
- 12. Unit Cooler Equipment Mark No.
1HVR-UC14 Cooling Capacity(mbh) 68.2 Cooler air flow (cfm) 4,570 Fan type Centrifugal Motor (hp) 10 Cooling medium Chilled water Flow rate (gpm, max) 11 Leaving air temp. dry/wet bulb (F°)
62.6/61.7 8 14
Revision 15 4 of 4 May 2002 Equipment Design Data
- 13. Supply Fans Equipment Mark No.
1HVR-FN6A & 6B Type Vaneaxial direct drive Air flow capacity (cfm) 10,000 Total pressure capability (in W.G.)
6 Speed (rpm) 3550 Motor (hp) 15 Type of discharge Horizontal
- 14. Roll Type Air Filter Equipment Mark No.
1HVR-FLT2 Total air capacity (cfm) 10,000 Filter pressure drop (dirty)
(in W.G.)
1.5 Face velocity (max, fpm) 475 Filter efficiency (average) 85% NBS Filter media thickness (in) 2
15
- 15. Extended Surface Type Filters Equipment Mark No.
1HVR-FLT7 Total air capacity (cfm) 10,000 Filter pressure drop (dirty)
(in W.G.)
0.7 Face velocity (max, fpm) 475 Filter efficiency (average) 95 ASHRAE 52-76 Filter media thickness (in) 22 15
- 16. Exhaust Fans Equipment Mark No.
1HVR-FN7A & 7B Air flow capacity (cfm) 10,000 Total pressure capability (in W.G.)
6 Speed (rpm) 3550 Motor (hp) 20 Type of discharge Horizontal
- 17. Electrical Duct Heater Equipment Mark No.
1HVR-CH1 Type Finned tubular Capacity 80 kW Stages 4
RBS USAR 1 of 4 August 1987 TABLE 9.4-5 DESIGN DATA FOR THE RADWASTE BUILDING HVAC SYSTEM Equipment Design Data 1.
Intake Filter Plenum a.
Roll type air filters Equipment Mark No.
1HVW-FLT4A & B Total air capacity (cfm) 39,200 Filter pressure drop (dirty)
(in W.G.)
1.5 Face velocity (max, fpm) 475 Filter efficiency (average) 85% NBS Filter media thickness (in) 2 b.
Extended surface type filters Equipment Mark No.
1HVW-FLT5A & 5B Total air capacity (cfm) 39,200 Filter pressure drop (dirty)
(in W.G.)
0.7 Face velocity (max, fpm) 475 Filter efficiency (average) 95 ASHRAE 52-76 Filter media thickness (in) 22 2.
Unit Cooler Sample Room, Laundry Room, and Formaldehyde Areas Equipment Mark No.
1HVW-UC5A & 5B Cooling capacity (mbh) 600 Cooler air flow (cfm) 6,300 Fan type Vaneaxial Motor (hp) 7.5 Cooling medium Chilled water Leaving air temp dry/wet bulb
(°F) 59.2/58.9 Flow rate (gpm, max) 80 Heating coil 30 kW 3.
Unit Cooler Equipment Mark No.
1HVW-UC1 Cooling capacity (mbh) 612.4 Cooler air flow (cfm) 13,700 Fan type Vaneaxial Motor (hp) 20 Cooling medium Chilled water Leaving air temp dry/wet bulb (°F) 74/70.5 Flow rate (gpm, max) 80
RBS USAR 2 of 4 August 1987 TABLE 9.4-5 (Cont)
Equipment Design Data Heating coil 70 kW 4.
Unit Cooler Equipment Mark No.
1HVW-UC2 Cooling capacity(mbh) 1421.8 Cooler air flow (cfm) 31,800 Fan type Vaneaxial Motor (hp) 30 Cooling medium Chilled water Leaving air temp dry/wet bulb (°F) 73.9/70.5 Flow rate (gpm, max) 187 Heating coil 160 kW 5.
Unit Cooler Equipment Mark No.
1HVW-UC3 Cooling capacity (mbh) 585.7 Cooler air flow (cfm) 13,100 Fan type Vaneaxial Motor (hp) 15 Cooling medium Chilled water Leaving air temp dry/wet bulb (°F) 74.1/70.5 Flow rate (gpm, max) 76 Heating coil 63 kW 6.
Unit Cooler Equipment Mark No.
1HVW-UC4 Cooling capacity (mbh) 603.6 Cooler air flow (cfm) 13,500 Fan type Vaneaxial Motor (hp) 20 Cooling medium Chilled water Leaving air temp dry/wet bulb (°F) 74/70.5 Flow rate (gpm, max) 78 Heating coil 65 kW 7.
Charcoal Filtration Unit Equipment Mark No.
1HVW-FLT1A & 1B Each filter unit consists of the following components:
a.
Moisture Separator (Demister)
Flow rate (cfm) 4,000
RBS USAR 3 of 4 August 1987 TABLE 9.4-5 (Cont)
Equipment Design Data Pressure drop (in W.G.)
1.0 Face velocity (fpm, max) 250 b.
Electric heating coil Capacity (kW) 57 Pressure drop (in W.G.)
0.5 Type Finned, tubular c.
Prefilters Pressure drop (in W.G., clean) 0.45 Filter efficiency 78% average ASHRAE 52-68 dust spot test Dust hold capacity 300 gm Filter media Fiberglass d.
HEPA Filters Each cell air flow capacity (cfm) 1000 Filter efficiency (DOP test) 99.97 Pressure drop (in W.G.)
1.0 Each filter cell (size) 24" x 24" x 11 1/2" e.
Charcoal Filters Type Rechargeable Filter efficiency for removal of elemental iodine (at 90% rh) 95%
methyl iodine (at 90% rh) 95%
Filter pressure drop (in W.G.)
(clean/dirty) 1.0/2.0 f.
Charcoal Filter Exhaust Fans Equipment Mark No.
1HVW-FN4A & 4B Type Centrifugal Air flow capacity (cfm) 4,000 Static pressure (in W.G.)
19 Speed (rpm) 3,550 Motor (hp)
Ltr g.
Decay Heat Removal Exhaust Fan Equipment Mark No.
1HVW-FN5A & 5B Type Centrifugal Air flow capacity (cfm) 100 Static pressure (in W.G.)
2.2
RBS USAR Revision 15 4 of 4 May 2002 TABLE 9.4-5 (Cont)
Equipment Design Data Speed (rpm) 3,450 Motor (hp) 0.5
- 15 8.
Main Exhaust Fans Equipment Mark No.
1HVW-FN1A,1B,&1C Type Vaneaxial Air flow capacity (cfm) 38,200 Static pressure (in W.G.)
6 Speed (rpm) 1750 Motor (hp) 50 15*
9.
Exhaust Filter Plenum a.
Roll Type Air Filters Equipment Mark No.
1HVW-FLT7 & 8 Total air capacity (cfm) 38,200 Filter pressure drop (dirty)
(in W.G.)
1.5 Face velocity (max, fpm) 475 Filter efficiency (average) 85% NBS Filter media thickness (in) 2 b.
Extended Surface Type Filters Equipment Mark No.
1HVW-FLT9 & 10 Total air capacity (cfm) 38,200 Filter pressure drop (dirty)
(in W.G.)
0.7 Face velocity (max, fpm) 475 Filter efficiency (average) 95 ASHRAE 52 Filter media thickness (in) 22
RBS USAR TABLE 9.4-6 COMPARISON OF NORMAL CHARCOAL FILTRATION SYSTEMS WITH REGULATORY GUIDE 1.140 REQUIREMENTS Radwaste Building Air Removal Tank Exhaust Containment Purge Hogging Pump Paragraph No.
Filtration System Filtration System System
C-1 "Environmental Design Criteria" 1.a In compliance In compliance In compliance 1.b In compliance In compliance In compliance 1.c In compliance In compliance In compliance 1.d In compliance In compliance In compliance C-2 "System Design Criteria" 2.a In compliance In compliance In compliance 2.b In compliance In compliance In compliance 2.c In compliance In compliance In compliance 2.d In compliance In compliance In compliance 2.e In compliance In compliance In compliance 2.f (1)
(1)
(1)
C-3 "Component Design Criteria and Qualifications Testing" 3.a In compliance In compliance In compliance 3.b In compliance In compliance In compliance 3.c (2)
(2)
(2) 3.d In compliance In compliance In compliance 3.e In compliance In compliance In compliance 3.f In compliance In compliance In compliance 3.g (3)
(3)
(3) 3.h (4)
(4)
(4) 3.i (5)
(5)
(5) 3.j In compliance In compliance In compliance 3.k (6)
(6)
(6) 3.l (7)
(7)
(7) 3.m In compliance In compliance In compliance C-4 "Maintenance" 4.a In compliance In compliance In compliance 4.b In compliance In compliance In compliance 4.c In compliance In compliance In compliance 4.d In compliance In compliance In compliance C-5 "In-Place Testing Criteria" 5.a In compliance In compliance In compliance 5.b In compliance In compliance In compliance 5.c In compliance In compliance In compliance 5.d In compliance In compliance In compliance
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C-6 "Laboratory Testing Criteria for Activated Carbon" 6.a (9)
(9)
(9) 6.b (10)
(10)
(10)
(1) Exception is taken to the amount of allowable air leakage in HVAC non-ESF charcoal filtration systems set by ANSI N509, 1980. See Table 1.8-1, Regulatory Guide 1.140 position.
(2) For HEPA filters and adsorber mountings, requirements of ANSI N509-1980 Section 5.6.3 are complied with except for the tolerance requirements. Tolerances for HEPA filters and adsorber mounting frames are sufficient to pass the bank leak tests of paragraphs 5.c and 5.d of the guide.
(3) Bed depths of charcoal adsorber units at RBS are 4 in, with a minimum residence time of 0.5 sec. Verification of filter efficiency is the objective; thus HEPA filters are tested in the shop and in the field for efficiency. Upon installation, and periodically thereafter, the filters are DOP tested in accordance with ANSI N510-1980.
(4) Exception is taken to Section 5.2.2.4 of ANSI N509-1980 which calls for a means of compaction to uniform density. Where uniform compaction can be demonstrated, compacting means are not required.
(5) 1.
System resistances are determined in accordance with Section 5.7.1 of ANSI N509-1980 except that fan inlet and outlet losses are not calculated in accordance with AMCA 201.
- 2.
Exception is taken to Section 5.7.2 of ANSI N509-1980. Copies of fan ratings or test reports are not necessary when certified fan performance curves are furnished.
- 3.
Exception is taken to Section 5.7.3 of ANSI N509-1980. Balancing techniques specified need not be followed. Maximum permissible vibration velocity level method need not be complied with.
- 4.
Exception is taken to Section 5.7.5 of ANSI N509-1980. Where AMCA certification ratings are submitted, documentation is not furnished.
(6) Airflow distribution is within +/-20 percent of the average airflow as tested in accordance with ANSI N510-1980.
Turning vanes are provided only where a uniform air distribution cannot be achieved.
Revision 17 3 of 3 (7) Exception is taken to Section 5.9 of ANSI N509-1980:
- 1. Dampers are not designed to the specification of ANSI B31.1.
- 2. Butterfly valves are not used.
- 3. Leakage rates for construction Class B, Leakage Class II and III are determined for one damper of each type instead of for every damper.
- 4. Dampers with shaft lengths of 24 in have a minimum shaft diameter of 1/2 in. Dampers with shaft lengths
>24 in and 48 in have a minimum shaft diameter of 3/4 in.
(Note: Items 1 and 2 do not pertain to containment penetrations.)
(8) Deleted.
(9) Exception is taken to the requirement that new activated carbon meets the physical property specification given in Table 1 of Regulatory Guide 1.140, 1979. The charcoal adsorbent now commercially available does not meet the physical requirements of Table 1, but does meet the requirements of ANSI/ASME N509-1980.
(10)Exception is taken to the requirements of conducting laboratory tests of representative samples as indicated in Table 2 of Regulatory Guide 1.140. Representative samples will be tested in accordance with ASTM D3803-1979.
RBS USAR 1 of 11 August 1987 TABLE 9.4-7 DESIGN DATA FOR TURBINE BUILDING VENTILATION SYSTEM Equipment Design Data 1.
Main Supply Subsystem Air-Conditioning Unit Equipment Mark No.
1HVT-ACU1 Total design air flow, cfm 34,000 This subsystem consists of a built-up air-conditioning unit with two 50-percent capacity supply fans.
The following are the major components with design data:
a.
Filter Type Horizontal, roll Airflow capacity, cfm 34,000 Filter pressure drop (dirty) in W.G.
1.5 Face velocity (max), fpm 500 Filter efficiency (average) 20% min (ASHRAE dust spot test) b.
Heating coil Type Electric, finned tube Heating capacity, kW 200 Numbers of stages 7
c.
Cooling coil Type Chilled water Total cooling capacity, mbh 1,335 No. of coils/No. of circuits per coil 2/27 Design pressure/temp., psig/°F 200/300 d.
Supply air fans, two 50-percent capacity Type Vaneaxial Airflow capacity each, cfm 17,000 Total pressure capability, in W.G.
7.56 Speed, rpm 35 Motor, hp 30 Type of discharge Horizontal
Equipment Design Data 2 of 11 August 1987 2.
Unit Coolers Subsystem a.
Unit cooler - general area NE Equipment Mark No.
1HVT-UC1A Cooling capacity, mbh 244.7 Cooler airflow, cfm 8,000 Fan type Vaneaxial Motor, hp 10 Cooling medium Chilled water b.
Unit cooler - general area north Equipment Mark No.
1HVT-UC1B Cooling capacity, mbh 244.7 Cooler airflow, cfm 8,000 Fan type Vaneaxial Motor, hp 10 Cooling medium Chilled water c.
Unit cooler - air compressor area Equipment Mark No.
1HVT-UC2 Cooling capacity, mbh 576.9 Cooler airflow, cfm 18,000 Fan type Vaneaxial Motor, hp 7.5 Cooling medium Chilled water d.
Unit coolers - reactor feed pump area Equipment Mark No.
1HVT-UC3A,3B,3C
&3D Cooling capacity, mbh 576.9 Cooler airflow, cfm 18,000 Fan type Vaneaxial Motor, hp 7.5 Cooling medium Chilled water e.
Unit coolers - reactor feed pump area Equipment Mark No.
1HVT-UC4A,4B Cooling capacity, mbh 244.7 Cooler airflow, cfm 8,000 Fan type Vaneaxial Motor, hp 5
Cooling medium Chilled water
Equipment Design Data Revision 15 3 of 11 May 2002
- f.
Unit coolers - condenser and CCW pump area Equipment Mark No.
1HVT-UC5A&5B Cooling capacity, mbh 576.9 Cooler airflow, cfm 18,000 Fan type Vaneaxial Motor, hp 7.5 Cooling medium Chilled water
- g.
Unit cooler - chiller area Equipment Mark No.
1HVT-UC6 Cooling capacity, mbh 576.9 Cooler airflow, cfm 18,000 Fan type Vaneaxial Motor, hp 7.5 Cooling medium Chilled water
- h.
Unit coolers - chiller area Equipment Mark No.
1HVT-UC7&8 Cooling capacity, mbh 244.7 Cooler airflow, cfm 8,000 Fan type Vaneaxial Motor, hp 5
Cooling medium Chilled water
- i.
Unit cooler - condenser tube withdrawal area Equipment Mark No.
1HVT-UC9 Cooling capacity, mbh 244.7 Cooler airflow, cfm 8,000 Fan type Vaneaxial Motor, hp 5
Cooling medium Chilled water
15
- j.
Unit cooler - condenser cubicle north Equipment Mark No.
1HVT-UC10 Cooling capacity, mbh 244.7 Cooler airflow, cfm 3,600 Fan type Vaneaxial Motor, hp 5
Cooling medium Chilled water 15
Equipment Design Data 4 of 11 August 1987 k.
Unit cooler - steam tunnel Equipment Mark No.
1HVT-UC11 Cooling capacity, mbh 1452.5 Cooler airflow, cfm 24,000 Fan type Vaneaxial Motor (2), hp 40 Cooling medium Chilled water l.
Unit cooler - lube oil purifier room Equipment Mark No.
1HVT-UC12 Cooling capacity, mbh 244.7 Cooler airflow, cfm 8,000 Fan type Vaneaxial Motor, hp 10 Cooling medium Chilled water m.
Unit cooler - switchgear area and heater bay Equipment Mark No.
1HVT-UC13 Cooling capacity, mbh 244.7 Cooler airflow, cfm 8,000 Fan type Vaneaxial Motor, hp 10 Cooling medium Chilled water n.
Unit cooler - heater bay area Equipment Mark No.
1HVT-UC14A&B Cooling capacity, mbh 1217.5 Cooler airflow, cfm 24,000 Fan type Vaneaxial Motor, hp 50 Cooling medium Chilled water o.
Unit cooler - general area Equipment Mark No.
1HVT-UC15 Cooling capacity, mbh 244.7 Cooler airflow, cfm 8,000 Fan type Vaneaxial Motor, hp 10 Cooling medium Chilled water
Equipment Design Data 5 of 11 August 1987 p.
Unit cooler - general and air removal pump area and general area south Equipment Mark No.
1HVT-UC16A,B,C&17 Cooling capacity, mbh 244.7 Cooler airflow, cfm 8,000 Fan type Vaneaxial Motor, hp 16A,B,C 5
17 10 Cooling medium Chilled water q.
Unit cooler - air ejection and PRV cubicle Equipment Mark No.
1HVT-UC18A,B&C Cooling capacity, mbh 68.3 Airflow capacity, cfm 1,300 Fan type Centrifugal Motor, hp 1.5 Cooling medium Chilled water r.
Unit cooler - moisture separator/
reheater area east Equipment Mark No.
1HVT-UC19A&B Cooling capacity, mbh 741.4 Airflow capacity, cfm 14,000 Fan type Vaneaxial Motor, hp 20 Cooling medium Chilled water s.
Unit cooler - turbine well Equipment Mark No.
1HVT-UC20 Cooling capacity, mbh 1541.4 Airflow capacity, cfm (2 fans each 20,000 cfm) 40,000 Fan type Vaneaxial Motor (2), hp 30 Cooling medium Chilled water t.
Unit cooler - moisture separator/
reheater area west Equipment Mark No.
1HVT-UC21A&21B Cooling capacity, mbh 1057.3
Equipment Design Data 6 of 11 August 1987 Airflow capacity, cfm 22,000 Fan type Vaneaxial Motor, hp 30 Cooling medium Chilled water u.
Unit cooler - general area north Equipment Mark No.
1HVT-UC22 Cooling capacity, mbh 244.7 Airflow capacity, cfm 8,000 Fan type Vaneaxial Motor, hp 16A,B,C 5
17 10 Cooling medium Chilled water v.
Unit cooler - steam seal evaporator/radwaste reboiler area Equipment Mark No.
1HVT-UC23A&B Cooling capacity, mbh 68.3 Airflow capacity, cfm 1300 Fan type Centrifugal Motor, hp 1.5 Cooling medium Chilled water w.
Unit coolers - general area el 123'-5" Equipment Mark No.
1HVT-UC24A,B,C&D Cooling capacity, mbh 244.7 Airflow capacity, cfm 8,000 Fan type Vaneaxial Motor, hp 10 Cooling medium Chilled water x.
Unit cooler - general area iodine filter room Equipment Mark No.
1HVT-UC25A&B Cooling capacity, mbh 244.7 Airflow capacity, cfm 8,000 Fan type Vaneaxial Motor, hp 5
Cooling medium Chilled water y.
Unit cooler - roof above moisture separator
Equipment Design Data 7 of 11 August 1987 Equipment Mark No.
1HVT-UC26 Cooling capacity, mbh 1217.5 Airflow capacity, cfm 24,000 Fan type Vaneaxial Motor, hp 50 Cooling medium Chilled water 3.
Off-gas area/condensate demineralizer area area ventilation subsystem a.
Unit cooler - condensate demineralizer tank area Equipment Mark No.
1HVT-UC27 Cooling capacity, mbh 72.0 Airflow capacity, cfm 1,300 Fan type Vaneaxial Motor, hp 1
Cooling medium Chilled water b.
Unit cooler - condensate demineralizer solution area Equipment Mark No.
1HVT-UC28 Cooling capacity, mbh 79 Airflow capacity, cfm 2,600 Fan type Vaneaxial Motor, hp 1.5 Cooling medium Chilled water c.
Unit cooler - condensate denimeralizer tank cubicle Equipment Mark No.
1HVT-UC29 Cooling capacity, mbh 374.7 Airflow capacity, cfm 7,000 Fan type Vaneaxial Motor, hp 7.5 Cooling medium Chilled water d.
Unit cooler - glycol tank and pump area and hydrogen analyzer area Equipment Mark No.
1HVT-UC30 Cooling capacity, mbh 345.9 Airflow capacity, cfm 11,400 Fan type Vaneaxial Motor, hp 7.5 Cooling medium Chilled water
Equipment Design Data 8 of 11 August 1987 e.
Unit cooler - regenerator/
desiccant dryer cubicle Equipment Mark No.
1HVT-UC31A&B Cooling capacity, mbh 39.5 Airflow capacity, cfm 1,300 Fan type Vaneaxial Motor, hp 1
Cooling medium Chilled water f.
Unit cooler - off-gas condenser cubicle Equipment Mark No.
1HVT-UC32 Cooling capacity, mbh 237.2 Airflow capacity, cfm 6,000 Fan type Vaneaxial Motor, hp 5
Cooling medium Chilled water g.
Off-gas refrigeration units Equipment Mark No.
N64B012A&B Cooling capacity, Btu/hr at temperature - 40°F 72,000 Airflow capacity, cfm 6,500 Air handling unit external static pressure, in W.G.
2.0 Temperature of condensing water °F 105 Maximum water head loss, ft 15 Waterside design pressure, psig 150 Fouling factor, water side 0.0005 Condenser water flow rate, gpm 42 Refrigerant type R-22 4.
Exhaust Air Subsystem a.
Main exhaust fans Equipment Mark No.
1HVT-FN1A,B&C Airflow capacity, cfm 22,000 Total pressure capability, in W.G.
11.75 Speed, rpm 3,500 Motor, hp 60 Type of discharge Horizontal b.
Off-gas area exhaust fans Equipment Mark No.
Equipment Design Data Revision 15 9 of 11 May 2002
15 Airflow capacity, cfm 7,700 Total pressure capability, in W.G.
9.25 Speed, rpm 3,500 Motor, hp 20 Type of discharge Horizontal 15
- 5.
Charcoal Filtration Subsystem Equipment Mark No.
1HVT-FLT1 Each filter unit consists of the following components:
- a.
Moisture separator (demister)
Flow rate, cfm 5,000 Pressure drop, in W.G.
1.0 Face velocity, fpm (max) 40
- b.
Electric heating coil Capacity, kW 25 Pressure drop, in W.G.
0.5 Type Finned, tubular
- c.
Prefilters Pressure drop, in W.G. (clean) 0.45 Filter efficiency 78% average ASHRAE 52-68 dust spot test Dust holding capacity, gm 300 Filter media Fiberglass
- d.
HEPA filters Each cell, airflow capacity, cfm 1,000 Filter efficiency, DOP test 99.97%
Pressure drop, in W.G.
1.0 Each filter cell size 24"x24"x11 1/2"
- e.
Charcoal Filters Type Rechargeable Filter efficiency for removal of Elemental iodine (at 90% RH) 95%
Methyl iodide (at 90% RH) 95%
Filter pressure drop, in W.G.
(clean/dirty) 1.0/2.0
Equipment Design Data 10 of 11 August 1987 f.
Charcoal filter exhaust fan Equipment Mark No.
1HVT-FN3 Type Centrifugal Air flow capacity, cfm 5,000 Static pressure, in W.G.
16.5 Speed, rpm 3,500 Motor, hp 30 g.
Decay heat removal exhaust fan Equipment Mark No.
1HVT-FN4 Type Centrifugal Airflow capacity, cfm 100 Static pressure, in W.G.
3.8 Speed, rpm 3,500 Motor, hp 1/3 6.
Sample Room Air-Conditioning System a.
Air Conditioning Unit Equipment Mark No.
1HVT-ACU2 Airflow capacity, cfm 4,000 Filter type Disposable Cooling coil Type Direct Expansion Cooling capacity, mbh 222.1 Entering air temp, db/w.b. °F 81.8/69.5 Leaving air temp, db/w.b. °F 55/53.5 Supply Fan Airflow, cfm 4,000 Total pressure capability, in W.G.
1.0 Type of discharge Horizontal Heating Type Electric Open-Type Capacity, kW 40 b.
Water Cooled Condensing Unit Equipment Mark No.
1HVT-CUR2 Capacity, mbh 222.1 Entering condenser water temp, °F 96 Leaving water temp, °F 106
Equipment Design Data 11 of 11 August 1987 c.
Heating System Unit Heater General Area South Equipment Mark No.
1HVT-UH1 Type Electric Capacity, kW 40 Unit Heater General Area Heating Bay Equipment Mark No.
1HVT-UH2 Type Electric Capacity, kW 30 Unit Heater Fire Protection Room Equipment Mark No.
1HVT-UH3 and UH4 Type Electric Capacity, kW 5
Heating Coil Area Above Moisture Separator Equipment Mark No.
1HVT-CH1 Type Electric -
Finned Tubular Capacity, kW 89.4 Heating Coil Offgas Bldg Glycol Tank and Pump Area Equipment Mark No.
1HVT-CH2 Type Electric -
Finned Tubular Capacity, kW 12
Equipment Design Data 4*
Revision 4 11a of 11 August 1991
- 4 7.
Steam Tunnel Air Conditioning System A.
Air Conditioning Unit Equipment Mark No.
1HVT-ACU4A Air Flow Capacity, CFM 14,000 Cooling Coil Type Direct Expansion Cooling Capacity, BTUs/Hr 300,000 B.
Air Conditioning Unit Equipment Mark Nos.
1HVT-ACU4B, 4C Air Flow Capacity, CFM 7,000 each Cooling Coil Type Direct Expansion Cooling Capacity, BTUs/Hr 150,000 each C.
Air Cooled Condensing Unit Equipment Mark Nos.
1HVT-CUR4 and 5 Capacity, BTUs/Hr 600,000 each
RBS USAR Revision 15 1 of 3 May 2002 TABLE 9.4-8 DESIGN DATA FOR THE ENGINEERED SAFETY FEATURES VENTILATION SYSTEMS Equipment Design Data Diesel Generator Rooms Exhaust Fans
15 Equipment Mark No.
1HVP*FN2A & B Type Vaneaxial Capacity 110,000 cfm Static pressure 1.75 in W.G.
Motor 100 hp Equipment Mark No.
1HVP*FN3A Type Vaneaxial Capacity 131,000 cfm Static pressure 3.5 in W.G.
Motor 100 hp Diesel Generators 1A & B Control Room Supply Fans Equipment Mark No.
1HVP*FN6A & B Type Centrifugal Capacity 3,500 cfm Static pressure 1.7 in W.G. (FN6A) 2.8 in W.G. (FN6B)
Motor 2 & 3 hp Diesel Generator 1C Control Room Supply Fan Equipment Mark No.
1HVP*FN6C Type Centrifugal Capacity 2,000 cfm Static pressure 0.75 in W.G.
Motor 1 hp 15
Diesel Generator Rooms Unit Heaters Equipment Mark No.
1HVP-UH1A, B, & C 1HVP-UH2A, B, & C Type Electric unit heater Capacity 7.5 kW Equipment Mark No.
1HVP-UH3A, B, & C 1HVP-UH4A, B, & C
Equipment Design Data Revision 16 2 of 3 March 2003 Type Electric unit heater Capacity 5 kW SSW Cooling Tower Pump House Pump Rooms Supply Fans
16 Equipment Mark No.
1HVY*FN1A, 1B, 1C, & 1D Type Vaneaxial Capacity 15,000 cfm (NOTE 1)
Static pressure 2 in W.G.
Motor 7.5 hp
6 SSW Cooling Tower Pump House Pump Rooms Unit Heaters Equipment Mark No.
1HVY-UH17 & 18 Type Electric unit heater Capacity 10 kW SSW Cooling Tower Switchgear Rooms Supply Fans Equipment Mark No.
1HVY*FN2A, 2B, 2C, & 2D Type Vaneaxial Capacity 6,200 cfm (NOTE 2)
Static pressure 1.5 in W.G.
Motor 3 hp 16
SSW Cooling Tower Switchgear Rooms Unit Heaters Equipment Mark No.
1HVY-UH15 & 16 Type Electric unit heater Capacity 10 kW 6
SSW Cooling Tower Remote Air Intake Room Supply Fans
15 Equipment Mark No.
1HVY*FN32A & 32B Type Vaneaxial Capacity 3,600 cfm Static pressure 1.25 in W.G.
Motor 5 hp 15
Equipment Design Data Revision 16 3 of 3 March 2003 SSW Cooling Tower Remote Air Intake Electric Duct Heaters Equipment Mark No.
1HVY*CH6A & 6B Type Finned tubular Capacity 12 kW
16 Notes:
1. The ventilation system capacity for pump room is ~20000 cfm when both fans (HVY-FN1A&C or HVY-FN1B&D) operate simultaneously.
2. The ventilation system capacity for switchgear room is ~10000 cfm when both fans (HVY-FN2A&C or HVY-FN2B&D) operate simultaneously.
16
RBS USAR TABLE 9.4-9 DESIGN DATA FOR REACTOR BUILDING VENTILATION SYSTEM Equipment Design Data 1 of 5 August 1987 1.
Containment Ventilation System a.
Containment unit coolers Equipment Mark No.
1HVR*UC1A, 1B
& 1HVR-UC1C Each containment unit cooler consists of the following components:
Filters Type Disposable, fiberglass Airflow capacity, cfm 50,000 Filter pressure drop (dirty),
in W.G.
0.50 Face velocity (max), fpm 480 Filter Efficiency (average)
ASHRAE 52-68 20 Cooling coils Design pressure, psig 200 Design temperature, °F 300 Type Chilled water/
service water Total cooling capacity, normal, mbh 2,543 LOCA, mbh 23,000 Flow rate normal, gpm 350 LOCA, gpm 540 Supply air fan Type Vaneaxial Airflow capacity, cfm 50,000 Total pressure capability, in W.G.
7.5 Speed, rpm 1,750 Motor, hp 150 b.
Recirculation fans Equipment Mark No.
1HVR-FN1A, 1B,1C & 1D Type Vaneaxial
Equipment Design Data Revision 16 2 of 5 March 2003 Airflow capacity, cfm 7,400 Total pressure capability, in W. G.
1.01 Speed, rpm 1,170 Motor, hp 2.0
- 2.
Drywell Ventilation System Drywell coolers Equipment Mark No.
1DRS-UC1A, B, C, D, E, & F Each drywell cooler consists of the following components:
Filters Type Disposable, fiberglass Airflow capacity, cfm 28,000 Filter pressure drop (dirty), in W.G.
0.5 Face velocity (max), fpm 480 Filter efficiency (average)
ASHRAE 52-68 20 Cooling coils
16 15 Total cooling capacity, mbh 2680.6 Design pressure, psig 200 Design temperature, °F 300 Type Chilled water Flow rate, gpm 334 Leaving air temp db/wb, °F 114/111.7 15 16
10 Supply air fan Type Vaneaxial Airflow capacity, cfm 28,000 Total pressure capability, in W.G.
8.78 Speed, rpm 3,500 Motor, hp 60
- 3.
Annulus Pressure Control System (Exhaust Fans)
Equipment Mark No.
1HVR-FN16A & 16B Type Centrifugal Airflow capacity, cfm 2,000 10
Equipment Design Data Revision 15 3 of 5 May 2002 Total pressure capability, in W.G.
8.20 Speed, rpm 1,750 Motor, hp 5
4.
Containment and Drywell Purge System
- 15 a.
Supply fan Equipment Mark No.
1HVR-FN8 Type Vaneaxial Airflow capacity, cfm 12,500 Total pressure capability, in W.G.
8.43 Speed, rpm 3,535 Motor, hp 50 15*
b.
Supply fan Equipment Mark No.
1HVR-FN13 Type Centrifugal Airflow capacity, cfm 7,000 Total pressure capability, in W.G.
2.0 Speed, rpm 1,150 Motor, hp 5
c.
Charcoal filter unit Equipment Mark No.
1HVR-FLT6 The charcoal filter unit consists of the following components:
Moisture separator (demister)
Flow rate, cfm 7,000 Pressure drop, in W.G.
1.0 Face velocity, fpm (max) 40 Electric heating coil Capacity, kW 32.0 Pressure drop, in W.G.
0.5 Type Finned, tubular Prefilter Pressure drop, in W.G. (clean) 0.45 Filter efficiency 78% average ASHRAE 52-68 dust spot test
Equipment Design Data Revision 18 4 of 5 Dust holding capacity, gm 300 Filter media Fiberglass
- d.
HEPA filters Each cell airflow capacity, cfm 1,000 Filter efficiency DOP test 99.97%
Pressure drop, in W.G.
1.00 Each filter size 24" x 24" x 11 1/2"
- e.
Charcoal filters Type Rechargeable Filter efficiency for removal of elemental iodine (at 90% RH) 95 Methyl iodide (at 90% RH) 95 Filter pressure drop, in W.G.
(clean) 1.0 (dirty) 2.0
- f.
Charcoal filter exhaust fan Equipment Mark No.
1HVR-FN14 Type Centrifugal Airflow capacity, cfm 7,000 Static pressure, in W.G.
16.25 Speed, rpm 3,600 Motor, hp 30
- g.
Decay heat removal exhaust fan Equipment Mark No.
1HVR-FN15 Type Centrifugal Airflow capacity, cfm 100 Static pressure, in W.G.
2.9 Speed, rpm 1,750 Motor, hp 1
- 5.
Annulus Mixing System (Disabled)
Equipment Mark No.
1HVR*FN11A & 11B Type Centrifugal Airflow capacity, cfm 52,500 Total pressure capability, in W.G.
12 Speed, rpm 1,180 Motor, hp 150
Equipment Design Data 5 of 5 August 1987 6.
Containment Heating Equipment Mark No.
1HVR-CH2 Type Electric Finned Tube Capacity, kW 130
RBS USAR TABLE 9.4-10 DESIGN DATA FOR THE MISCELLANEOUS BUILDINGS' HVAC SYSTEMS Revision 15 1 of 5 May 2002
- 1. Fire Pump House
- a. Exhaust Fans Equipment Mark Nos.
1HVY-FN3, 4, and 6 1HVY-FN5 and 7 Type Vaneaxial Vaneaxial Airflow capacity, cfm 8,000 25,080 Total pressure capability, in W.G.
0.375 0.375 Speed, rpm 1,750 875 Motor, hp 3
7.5 Type of Discharge Horizontal Horizontal
- b. Unit Heaters Equipment Mark No.
1HVY-UH1, 2, 3, 4, and 5 Capacity, kW 10 Air volume, cfm 750 Minimum throw, ft 27
- 2. Normal Switchgear Building 15
- a. Air Conditioning Units Equipment Mark Nos.
1HVY-ACU2 1HVY-ACU3A and B Filter type Disposable Disposable Airflow capacity, cfm 4,860 37,100 15 Cooling coil Type Direct Exp.
Direct Exp.
Cooling capacity, mbh 401 1476 Entering air temp., db/wb oF 88/74 96/81 Leaving air temp., db/wb oF 56/54 74/72 Supply fan Airflow, cfm 6,100 37,100 Total pressure capability, in W.G.
1.2 2.7 Type of discharge Vertical Horizontal Motor, hp 10 30
- b. Air-Cooled Condensing Units Equipment Mark Nos.
1HVY-CUR2 1HVY-CUR3A and B Capacity, mbh 401 1476 Entering air temp, condenser oF 96 96 Number of unloading steps 3
3 Refrigerant type R-22 R-22 Starting and operating low ambient temp oF 30 30
Revision 15 2 of 5 May 2002
- c. Exhaust Fans 15 Equipment Mark No.
1HVY-FN19A and B Type Vaneaxial Airflow capacity, cfm 27,230 Total pressure capability, in W.G.
2.5 Type of Discharge Horizontal
- d. Battery Room Exhaust Fan Equipment Mark No.
1HVY-FN21 Type Centrifugal Airflow Capacity, cfm 3,750 Total pressure capability, in W.G.
1.5 Type of discharge Top horizontal 15
- 3. Auxiliary Boiler Building
- a. Switchgear Room Air Conditioning Unit Equipment Mark No.
1HVI-ACU1 Filter type Disposable Airflow capacity, cfm 8,400 Cooling coil, type Direct Expansion Cooling capacity, mbh 30.05 Leaving air temp.
oF db/wb 74/73 Entering air temp.
oF db/wb 96/81 Supply fan, type Airfoil Airflow, cfm 8,400 Type of discharge Horizontal
- b. Air Cooled Condensing Unit Equipment Mark No.
1HVI-CUR1 Entering air temp, condenser oF 96 Number of unloading steps 3
Refrigerant type R-22 Starting and operating low ambient temp oF 30
- c. Exhaust Fan 15 Equipment Mark No.
1HVI-FN3 Type Vaneaxial Airflow capacity, cfm 7,850 Type of discharge Horizontal 15
- d. Boiler Room Exhaust Fans Equipment Mark No.
1HVI-FN1 and 2 Type Roof Ventilator Airflow capacity, cfm 4,600 Type of discharge Up, Vertical
Revision 15 3 of 5 May 2002
- 4. Water Treatment Building
- a. Air Handling Unit Equipment Mark No.
1HVJ-AHU1 Filter, type Roll Max. face velocity, fpm 500 Heating coil, type Electric Capacity, kW Supply fan, type Airfoil Airflow capacity, cfm 22,850 Total pressure capability, in W.G.LTR Type of discharge Horizontal
- b. Exhaust Fan 15 Equipment Mark No.
1HVJ-FN1 Type Vaneaxial Airflow capacity, cfm 22,430 Type of discharge Horizontal
- 5. Makeup Water Intake Structure and Switchgear House
- a. Supply Fans Equipment Mark No.
1HVY-FN23A and B Type Vaneaxial Airflow capacity, cfm 42,350 Type of discharge Horizontal
- b. Exhaust Fans Equipment Mark No.
1HVY-FN22A and B Type Vaneaxial Airflow capacity, cfm 42,250 Type of discharge Horizontal 15 8
- c. Heating and Ventilation Unit - Switchgear Area Equipment Mark No.
1HVY-ACU1 Filter type Disposable Airflow capacity, cfm 550 Cooling Coil Type N/A Cooling Capacity, mbh N/A Entering air temp oF db/wb 96/81 Supply Fan Airflow, cfm 550 Type of discharge Horizontal 8
Revision 15 4 of 5 May 2002
- 6. Electrical and Piping Tunnels
- a. Supply Fans 15 Equipment Mark Nos.
1HVY-FN11 and 14 1HVY-FN18 1HVY-FN12 Type Vaneaxial Vaneaxial Vaneaxial Airflow capacity, cfm 3,800 (FN11) 2,500 15,000 5,000 (FN14)
Total pressure capability, in W.G.
1.5 1.0 1.0 Type of discharge Horizontal Horizontal Horizontal
- b. Supply Fans Equipment Mark Nos.
1HVY-FN8 1HVY-FN9 and 10 Type Vaneaxial Vaneaxial Airflow capacity, cfm 7,500 4,600 Total pressure capability, in W.G.
1.0 2.0 Type of discharge Horizontal Horizontal/Vertical 15 8 Equipment Mark No.
1HVY-FN17 Type Vaneaxial Airflow capacity, cfm 7,500 Total pressure capability, in W.G.
1.5 Type of discharge Horizontal 8
- c. Exhaust Fans 9
Equipment Mark Nos.
1HVY-FN15A and B 1HVY-FN16A and B Type Vaneaxial Vaneaxial Airflow capacity, cfm 30,500 28,000 9
- d. Heating Coils Equipment Mark Nos.
1HVY-CH12 1HVY-CH13 Type Elec Finned Tube Elec Finned Tube Capacity 39.2 30 Equipment Mark Nos.
1HVY-CH17 1HVY-CH15 Type Elec Finned Tube Elec Finned Tube Capacity 39.2 26.2 Equipment Mark Nos.
1HVY-CH16 1HVY-CH11 Type Elec Finned Tube Elec Finned Tube Capacity 26.2 13.1 Equipment Mark Nos.
1HVY-CH10 1HVY-CH14 Type Elec Finned Tube Elec Finned Tube Capacity 78.4 14.1 Equipment Mark Nos.
1HVY-CH18 Type Elec Finned Tube Capacity 14.1
Revision 8 5 of 5 August 1996 8
- e. Inlet Filters Equipment Mark Nos.
1HVY-FLT8 1HVY-FLT9 1HVY-FLT10 1HVY-FLT12 Fan (1HVY-)
FN8 FN9 FN10 FN12 Filter area (in. x in.)
48x48 48x48 48x24 72x72 Equipment Mark Nos.
1HVY-FLT14 1HVY-FLT17 1HVY-FLT18 Fan (1HVY-)
FN14 FN17 FN18 Filter area (in. x in.)
48x48 48x48 24x48 8
1 of 1 August 1988 TABLE 9.5-1 POWER SOURCES FOR COMMUNICATION SYSTEM
- 1 Equipment Power Source Description Volts Ph Identification PP/PA 120 ac 1
1VBN-PNL 01A1 1VBN-PNL 01B1 Main control room 136"-0", and local non-class 1E power 1*
Portable intercom Independent battery system supplies PBX 120 ac 1
1VBN-PNL 04, El 110' Health physics bldg local non-class 1E power
- 1 Onsite radio Independent battery (hand-held supplies and local portable radio non-class 1E power, system) 1VBN-PNL (LTR), and 1IHS-PNLO1 for main control room consoles and base stations Plant-to-offsite Switchyard battery radio 1VBN-PNL (LTR), and 1IHS-PNL01 1*
GSU microwave Switchyard battery system 1VBN-PNL (LTR)
RBS USAR TABLE 9.5-2 ILLUMINATING LEVEL AND TYPE OF FIXTURES USED IN PLANT AREAS NECESSARY FOR SAFE SHUTDOWN OR EVACUATION OF PERSONNEL (a)20 percent of fixtures connected to UPS (b)20 percent of fixtures connected to standby source and switchable to other sources by administrative control (c)Means of egress and exit
- Area lighting required for safe shutdown.
1 of 1 August 1987 Normal Lighting Emergency Lighting Area Fixture FC Source Fixture FC 1.
Main control Fluorescent 75 (Main console)
UPS Fluorescent 20(a) room 75 (Computer)
Standby*
Fluorescent 20(b)
Battery pack Incandescent 0.5(c) 2.
Standby switch-Fluorescent 35 Battery pack Incandescent 3
gear rooms 3.
Class 1E Fluorescent 20 Battery pack Incandescent 3
Battery rooms (enclosed &
casketed) 4.
Standby diesel Fluorescent 20 Battery pack Incandescent 3
generator areas 5.
Standby service Fluorescent 20 Battery pack Incandescent 3
water pumphouse 6.
Standby MCCs Fluorescent 20 Battery pack Incandescent 3
and load centers 7.
Remote shutdown Fluorescent 30 Battery pack Incandescent 5
panel rooms Standby*
Fluorescent 30 8.
Means of egress Fluorescent or 5
Battery pack Incandescent 0.5 and exit incandescent (all buildings)
RBS USAR TABLE 9.5-3 STANDBY DIESEL ENGINE LUBRICATION SYSTEM COMPONENTS 1 of 2 August 1987 Electric Motor-Engine-Driven Driven Lube Oil Lube Oil Pump Circulating Pump 1.
Pumps Quantity 1 per diesel 1 per diesel Type Gear Screw Capacity, gpm 345 40 Head, psig 75 15 2.
Lube Oil Cooler Quantity 1 per diesel Duty, Btu/hr 1,613,000 Design Conditions Tube Side - Jacket Water
- a. Inlet temp, °F 145.4
- b. Outlet temp, °F 149.4
- c. Flow, gpm 800 Shell Side - Lube Oil
- a. Inlet Temp, °F 182.4
- b. Outlet temp, °F 160.0
- c. Flow, gpm 320 3.
Lube Oil Sump Tank Quantity 1 per diesel Type Built in aux. skid Capacity, gal 514 gal high level
RBS USAR TABLE 9.5-3 (Cont) 2 of 2 August 1987 4.
Lube Oil Heater Circulating Pump Quantity 1 per diesel Capacity, gpm 40 Head, psig 15 5.
Lube Oil Heater Quantity 1 per diesel Output, kW 20 kW
RBS USAR TABLE 9.5-4 DESIGN DATA FOR DIESEL GENERATOR COMBUSTION AIR INTAKE AND EXHAUST SYSTEM 1 of 1 August 1987 HPCS Diesel Standby Diesel Generator Component Generators (Filter Only)
Intake Air Filter/Silencer Type Disposable cartridge Disposable cartridge Capacity (scfm) 14,194 10,700 Pressure drop (in W.G.)(max) 6.5 3.3 Media (packing)
Mineral wool High efficiency and 14 gauge filter paper hot-rolled steel Pressure (psia) 14.7 14.7 Exhaust Silencer Capacity (acfm) 31,600 23,000
RBS USAR TABLE 9.5-5 STORAGE OF GAS UNDER PRESSURE Container Stored Gas Maximum Est.
Est. Tank Design Pressure Pressure (1)
No.
Vol.
Gas (psig)
(psig)
(psig)
Tanks (cu ft)Ea.
Location Revision 20 1 of 3 Carbon Dioxide (3)
Fire Protection 1,800 850 1,000 64 3
Turbine Bldg, Basement Generator Purge (5) 450 300 357 1
308.7 Yard - approximately 90 ft from southeast corner of bldg Nitrogen
11 Nitrogen 3,360 2,400 3,200 20 1.88 Turbine Bldg (5 tanks)
Blanketing Auxiliary Bldg (7 tanks)
Radwaste Bldg (2 tanks)
Auxiliary Boiler Bldg 11
(6 tanks)
Nitrogen 3,360 2,400 3,360 3
1.88 Containment el 114' Storage for CRD Accumulators CRD Accumulators 2,000 (4) 2,000 2,000 145 2
16 Hydrogen (Generator Cooling - Backup Source) 16
Tube Trailer 4,000 2,400 3,800 30 7.7 Yard - approximately 90\\ft southeast of building Reserve Skids(2) 4,000 2,400 3,800 56 4.5 Air Instrument Air 135 120 135 3
96 Turbine Bldg Receivers Air Damper 150 120 135 6
8 Control, Auxiliary, and Accumulator Fuel Bldg Instrument Air 159 120 135 1
75 Radwaste Bldg Accumulator Radwaste Air 150 120 135 1
29 Radwaste Bldg Receivers
14 12 12 14
Container Stored Gas Maximum Est.
Est. Tank Design Pressure Pressure (1)
No.
Vol.
Gas (psig)
(psig)
(psig)
Tanks (cu ft)Ea.
Location Revision 20 2 of 3
13 Instrument Air System 4000 2400 2640 16 1.75 Control Building Air Bottles 13
Penetration Valve 200 120 150 1
212 Auxiliary Bldg Leakage Control 1
72 Auxiliary Bldg Isolation Valve 150 120 135 4
5.5 Auxiliary Bldg Accumulators 235 120 235 4
5.5 Reactor Bldg ADS Accumulators 300 150 300 7
8.8 Reactor Bldg Safety Relief 300 150 300 9
1.7 Reactor Bldg Valve Accumulators HPCS Diesel 275 250 275 2
64 Diesel Generator Bldg Generator Receiver Standby Diesel 275 250 275 8
76 Diesel Generator Bldg Generator Receiver Service Wtr Air 150 120 150 2
36.8 Reactor Bldg Accum Halon Fire Protection 3,000 360 1,000 54 0.26 Main Control Room Fire Protection 3,000 360 1,000 2
1.9 Aux Cont Bldg, el 123'-6" Fire Protection 3,000 360 1,000 6
3.5 Aux Cont Bldg, el 123'-6" Fire Protection 3,000 360 1,000 2
0.13 Norm Swgr Bldg, el 123'-6" Fire Protection 3,000 360 1,000 2
0.15 PAP Bldg Fire Protection 3,000 360 1,000 2
1.4 Services Bldg, Rm 305 Fire Protection 3,000 360 1,000 2
1.4 Services Bldg, Rm 353 Fire Protection 3,000 360 1,000 2
2.7 Services Bldg, Rm 302 Fire Protection 3,000 360 1,000 2
0.4 Services Bldg, Rm 302 Fire Protection 3,000 360 1,000 2
0.75 Services Bldg, Rm 205 Fire Protection 3,000 360 1,000 2
1.5 Services Bldg, Rm 206
Container Stored Gas Maximum Est.
Est. Tank Design Pressure Pressure (1)
No.
Vol.
Gas (psig)
(psig)
(psig)
Tanks (cu ft)Ea.
Location
(1)Safety valve or cylinder rupture disk set point (2)Deleted (3)Stored as liquified gas (4)Maximum working pressure (5)Liquid carbon dioxide in a low-pressure cryogenic storage unit
12 (6)Evaluation of effects due to failure of hydrogen and oxygen storage vessels for this system performed in accordance with EPRI Report NP-5283-SR-a, Guidelines for Permanent BWR Chemistry Installations - 1987 Revision.
12
Revision 20 3 of 3 Fire Protection 3,000 360 1,000 2
0.44 Met Instr Bldg Fire Protection 3,000 360 1,000 2
0.23 Met Utility Bldg Hydrogen in Nitrogen Hydrogen Analyzer 3,360 2,400 3,000 2
1.88 Auxiliary Bldg Calibration Gas Bottle Oxygen Hydrogen Analyzer 3,360 2,400 3,000 4
1.88 Auxiliary Bldg Reagent Gas Bottle
12 Hydrogen Water Chemistry(6)
Cryogenic Hydrogen NA(6)
Cryogenic Oxygen NA(6)
Bottled Hydrogen NA(6) 12
RBS USAR 1 of 2 August 1987 TABLE 9.5-6 STANDBY DIESEL GENERATOR COOLING WATER SYSTEM COMPONENTS Jacket Water Pumps Type Centrifugal Quantity 1 per diesel engine (engine driven)
Capacity 900 gpm NPSH 15 ft TDH 110 ft Jacket Water Cooler Type TEMA Class R ASME Section III, shell and tube Duty 12,030,000 Btu/hr Design Conditions (Plant)
Tube Side - Cooling Water Inlet Temperature 95°F Outlet Temperature 129°F Flow:
700 gpm Shell Side - Engine Jacket Water*
Inlet Temperature 175°F Outlet Temperature 144.9°F Flow:
800 gpm Heat Removal Design Overload Margin 110 percent Jacket Water Standpipe Quantity 1 per diesel engine Type Vertical Capacity 225 gallons to fill Engine 500 gallons to fill from jacket water inlet to jacket water outlet Jacket Water Heater Type Flanged immersion Quantity 1 per standpipe Output 48 kw (3 phase/60 Hz/460 V)
RBS USAR 2 of 2 August 1987 TABLE 9.5-6 (Cont)
Jacket Water Keepwarm System Circulating Pump Type Centrifugal Quantity 1 per diesel engine Capacity 50 gpm NPSH 15 ft TDH 50 ft Turbocharger After-Coolers Duty 3,695,000 Btu/hr Jacket Water Flow 450 gpm Jacket Water Inlet Temperature 150°F Jacket Water Outlet Temperature 165°F Heat Removal Design Margin 10 percent Data listed is for engine at full load operation, stabilized nominal full load temperature.
RBS USAR TABLE 9.5-7 HYDROGEN WATER CHEMISTRY SYSTEM ALARMS AND ISOLATIONS Revision 23 1 of 1 Parameter Alarm Isolation Hydrogen Flow Setpoint error High Loss of Signal Hydrogen Pressure Low High Oxygen Pressure High Low Oxygen Flow Setpoint error Hydrogen Area High Monitor Malfunction High-High H2/O2 Supply Systems Trouble System Trip Offgas Monitor Trouble Low O2 High O2 Isolation Local Manual Control Room Manual Reactor Power Loss of Signal Reactor Scram Note: The SCRAM contacts are wired into the Control Room Manual Shutdown switch circuit.
Full SCRAM