ML20126K579
| ML20126K579 | |
| Person / Time | |
|---|---|
| Site: | Davis Besse  |
| Issue date: | 04/03/1985 |
| From: | Quennoz S TOLEDO EDISON CO. |
| To: | |
| References | |
| SP-1106.07, NUDOCS 8507300336 | |
| Download: ML20126K579 (63) | |
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System Procedure SP 1106.07 Main Feedwater System w 5 Record of Approval and Changes Prepared by Larry Bladel and J . Dennis .,,,, n . f. ,,.i,, 2/5/74 Date Submitted by % O M9 ' S /34# !7 5 Dat
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- 1 SP 1106.07.0 l f* l
, 12 1. PROCEDURE To provide a procedure for operation of the Feedwater System in the following modes:
MODE SECTION Feedwater Cleanup 5 t- Feedwater System Startup and Normal Operation 6 Feedwater System Shutdown 7 Feedwater System Layup During a Plant Shutdown and Cooldown 8
; The Feedwater System consists of the following major components:
- 1. Booster Feed Pumps (BFP) (2)
- 2. Main Feed Pumps (MFP) (2)
- 3. Main Feed Pump Turbines (MFFI) (2)
- 4. HP Heaters (2) strings of 3 each
- 5. Main Feedwater Control Valves (2) ,
- 6. Startup Feedwater Control Valves (2)
The.BFP, MFP and MFPT will be referred to as one unit, MFP, throughout this procedure, f'! , The flow path of the Feedwater System is as follows: from the
\,_;/ deserator outlet to the suction of the BFP then the suction of the
! MFP. The outlet from the MFP's goes into a common header before l feeding the two strings of HP Heaters. The discharge of the heaters goes to a common header which splits to supply feedwater to the two (2) steam generators through a main control valve and/or a startup control valve. Prior to the filling of the steam generators for plant startup and operation, the feedwater quality will have to be brought into chemistry j specifiestion acceptable for use in the steam generators. Before l starting cleanup of the Feedwater System, the MFP will be placed on turning gear and warmed up. 1 The cleanup is accomplished by circulating condensate from the hotwell through the following components as follows: , 1. Condensate Pumps
- 2. No. 1 LP Heaters
- 3. Condensate Polishing Desineralizer 1 4. No. 2 LP Heaters
- 5. Deserator Heaters j 6. Deserators
- 7. MFP's
- 8. HP Feedwater Heaters
- 9. Feedwater Control Valves l
- _ - . . _ . -. _ _ . __ _ . . _ - . . _ . . ~ . _ - - _ - _ _ - _ .. . _ _ _ . . - . - - _ _
d 2 SP 1106.07.7 m The feedwater is circulated by a NFP through the HP Heaters, feedwater
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J control valves to the condenser ~ hotwell through recirculation valve, FW 523. A velocity of 2 fps (condensate pump ficw of about 6000 gps) should be maintained through the major piping system during the initial phase of cleanup. The deserator will be on level control during this time. After the initial velocity flush of feedwater system, the NFP will be 7l placed in standby and the SUFP will be started using HIS 579. Auxiliary steam pressure in the deserator is increased to 2.3 psig to
-heat the feedwater to a higher temperature for 0: removal (pegging
- steam). The feedwater cleanup will be terminated when it has reached 7 the desired specifications for steam generator fill.
i W n the steam generators are to be filled, the Startup Feed Pump ' (SUFP) will be started and feedwater from the. deaerator storage tanks vill be added to the steam generators to bring them up to the startup level of 961 - 99% on the operate range. During steam generator 4 waraup, the startup control valve mini line bypass will be fully
; open. Steam generator level will be controlled with the steam 4
generator drain valve bypass from the Control Room. When the turbine " i bypass valves open to maintain OTSG pressure at 870 psig during plant ' startup the startup feedwater control valves are throttled to maintain 35% to 70% on SG operate level prior to going critical and when OTSG i] feedwater chasistry is within specifications, the OTSG's are drained 7 to low level limit. At approximately 1% power a MFP is placed on line and the SUFP is stopped.
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2' j Below 251 power, fe'edwater flow is controlled to maintain the steas j
- generator levels a~t the fixed low level limits. Between 25 and 100% j power, the steam generator levels are allowed to vary with p wer and feedwater flow to achieve the desired heat transfer tate from the 1
primary to secondary system. Feedwater flow is controlled by using I the main and startup feedwater control valves, controlled by loop feedwater demand signals. The main feedwater pump turbine speed is controlled by the total feedwater demand signal and a feedwater control valve AP signal. The total feedwater demand signal is used 4 to drive the main feedwater pump turbine to a speed that should provide adequate feedwater flow. MFPT speed is fine tuned by use of
- the feedwater centrol valve AP. This feedback insures that the pumps are running at a speed that always provides a AP across the feedwater control valve. Less'than 30 psid across the feedwater control valve initiates a "W Valve AP Low" alarm in the control room indicating that NFPT discharge pressure is too low.
> Prior to reaching 55% reactor power, the second MFP will have to be started and will be in the recirculating mode at minimum speed. , Above this power both MFP's will be operating. l Normal OTSG operating conditions (100% power and flow): l l
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s 3 SP 1106.07.8 {
- 1. Pressure (primary / secondary) 2155/910 psig
- 2. Temperature (primary) ,608 F (in) 556aF (out)
(secondary) M *F (in)
- 570*F (out)
- 3. Flow (primary / secondary) 74/5 3 MLB/HR per loop A list of Feedwater Heater Resets and Reset locations in provided on Attachment 1.
- 2. LIMITATIONS AND PRECAUTIONS i
2.1 The limitations and precautions associated with this procedure i are listed with the section of the procedure they are directly related to. i 3. REFERENCES 3.1 Procedures
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3.1.1 Condensate System Procedure, SP 1106.16 3.1.2 Operational Chemical Control Limits PP 1101.04 3.1.3 Plant Startup, PP 1102.02 3.1.4 Plant Shutdown and Cooldown, PP 1102.10 3.1.5 OTSG 78.11, Drain and Layup, SP 1106.08 1.1.6 Demerators, SP 1106.17 3.1.7 Feedwater Heaters, SP 1106.18 3.1.8 LP FW Heaters, SP 1106.19 3.1.9 Main Feed Pump and Turbine, SP 1106.20 3.2 TED NQAM (Nuclear Quality Assurance Manual) 8l 3.3 Bechtel Drawings (P&ID's) 3.3.1 M006-B, Feedwater System 3.3.2 M007, Steam Generator Secondary System , 3.3.3 M003, Main Steam and Reheat System , 3.3.4 M006-A, Condensate System i 3.3.5 M020, Auxiliary Steam System i
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l l 4 SP 1106.07.6 - 6 3.4 USAR, Chapter 10, Section 10.4.7 , 4. PREREQUISITES
- 4.1 Feedwater System is filled and/or vented (Enclosure 1, Feedwater l 6 System Elevation Diagram). The Shift Supervisor will direct filling acd venting operations. Depending on the layup conditions, the Feedwater System may require only venting prior to startup.
4.2 The remaining prerequisites associated with this procedure are listed with the sections of the procedures to which they apply.
- 5. FEEDWATER CLEANUP NOTE: The Feedwater Cleanup will be done in conjunction with the Plant Startup Procedure, PP 1102.02.
5.1 Prerequisites 5.1.1 Plant startup has progressed to a point where the main turbine and NFPT's cre on gear, a condensate pump is - in service, two condensate polisher (s) are in service, at least two cire pumps are operating, the gland steam seal and turbine drains are in service, vacuum has 6 been established in the main condenser and the OTSG's . are in wet layup (see Plant Startup Procedure PP 1102.02, , i Section 5). - 5.1.2 The NFP's are in the standby condition as per SP 1106.20, Main Feed Pump and Turbine Operating Procedure. i 5.1.3 Ensure Valve Verification List A is completed. Attachment 2 may be used to assist in locating valves. 5.2 LLaitations and Precautions l 5.2.1 25% flow (2.8 MPPH) is required for initial stages of cleanup (three to four hours). A single condensate polishing desineralizer is only good for 5324 gym (2.66 MPPH). Therefore, it is necessary to have two polishers in service. l 6 5.2.2 If a MFFT is used during oxygen removal, pegging steam i flow must be controlled to prevent exceeding Auxiliary Boiler capacity. Sufficient steam must be availtole , to supply the steam seal header (approximately 32,000 lb/hr), and steam jet air ejector (approximately 4,290 lb/hr) and.to run a MFPT (approximately 10,000 lb/hr). 5.2.3 During feedwater cleanup, if the Control Room alarm annunciates for the condensate polishers on High AP of . 1 0
5 SP 1106.01.6 / 25 psi, shift to one of the standby polis'ters and have the Chem Lab precoat the expended polisher per condensate polisher procedure, SP 1106.22, Condensate Demineralizers. 5.3 Procedure 5.3.1 Check closed the Main and Startup Feedwater Control Valves. SP6A SP6B SP7A SP7B 6 5.3.2 Open FW 104 and throttle FW 33 to obtain 2 to 3 K gpm (1.5 MPPH) condensate flow. 5.3.3 Perform Valve Lineup List B, Feedwater Cleanup Lineup. 5.3.4 Lineup auxiliary steam to the Main Feed Pump Turbines. .
- 1. Place steam traps ST41, ST42, and ST43 in the Startup Mode.
- 2. Slowly open AS177, Auxiliary Steam to MFPT Stop g Valves.
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- 3. Slowly open AS270, MFPT Auxiliary Steam Supply Valve.
NOTE: It is necessary to manually throttle the Auxiliary Steam to the MFPT to 185 psig. 6 5.3.5 Roll a Main Feed Pump up to approximately 200 psi discharge pressure or sufficient speed to show adequate recire flow per Attachment 6. NOTE: The Main Feed Pump will be discharging through the recirculation line to the deaerator until FW cleanup is established. 5.3.6 If during FW cleanup, it is necessary to increase Main Feed Pump speed greater than 1030 RPM, close the first stage drain valve from the Control Room on Main Feed Pump 1-1 (1-2) using HIS 1950 (HIS 1944). 6 NOTE: Main Feed Pump speed should be held less than 1030 RPM until its oil temperature is increased to 110*F. I l
I f 6 SP 1106.07.8 5.3.7 Start the 25% firsh flow by performing either one of the following:
- 1. Slowly crack open FW166 and throttle as necessary to obtain 1.4 MPPH on each HP FW heater group 1 and 2 flow indicators FI580 and FI581. (2.8 MPPH total flow.)
- 2. Open FW163 SG 1 FW Cleanup Recire Valve to condenser and FW164 SG 2 FW Cleanup Recirc to condenser. Then slowly open FW loop 1 and 2 startup control valves using R/A stations ICS33B and ICS33A respectively to obtain 1.4 MPPH on '
each loop 1 and loop 2 Startup FW flow indicators FI SP3B and FI SP3A. NOTE: It may be necessary to increase the ] operating Main Feed' Pump speed, using 8 the manual pistol grip HS 805D (806D) to maintain 200 psig discharge pressure on the Main Feed Pump. Coordinate this . with increasing FW flow. Also the deaerator drain (FW33) may need to be closed or throttled to prevent condensate pump run out. . 5.3.8 Maintain loop 1 and 2 FW flow to 1.4 MPPH on loop 1 . i) and loop 2 FW flow indicators. 5.3.9 During the 25% flow flush, there may be insufficient Auxiliary Steam capacity to maintain all the Auxiliary Steam loads. The operator will have to closely monitor the 235 psig steam header pressure gauge in the Control Room (PI 1659). 5.3.10 Monitor condensate polisher performance during FW cleanup. If limit of high AP (25 psid) or high conductivity (0.5 unho/cm) is reached, place a standby polisher in service and precoat the extended polisher per Condensate Polishers Procedure, PP 1106.22. NOTE: If polishers are being rapidly depleted on conductivity due to feed and condensate system wet layup chemicals, the conductivity limit can be extended to 1.0 paho/cm with C&HP concurrence. 5.3.11 Continue the 25% flow flush until the C&HP Section determiner by sampling that the FW iron content is less than 100 ppb at the outlet of the HP FW heaters. t _ _ _ _ _ _ _ _ _ _ ~
9 7 SP 1106.07.8 5.3.12 Shutdown the running Main Feed Pump per SP 1106.20. NOTE: If the first stage drain valve was closed on the MFP, open it at this time. i 5.3.13 Repeat Steps 5.3.5 through 5.3.11 using the other MFP train. 8l 5.3.14 If using Step 5.3.7.1, close FW166 and open FW170 until total FW flow is approximately .15 MPPH (300 GPM). If using Step 5.3.7.2, slowly throttle loop 1 and 2 startup control valves until total FW flow is approximately .15 MPPH (300 GPM). l 8l NOTE: If the first stage drain valve was closed on the MFP, open it at this time. 5.3.16 Place the startup feed pump in service per SP 1106.27. 5.3.17 Throttle to obtain 300 gpa (.15 MPPH). , NOTE: If the SUFP is NOT available, use a MFPT for 02 removal. If using a MFPT, flow can be greater than 300 gpa. At the Shift Super-visor's discretion, a HFPT can be used ( instead of the SUFP. (The SUFP is the s,- preferred method.) 5.3.18 Place pegging steam on the deserator and slowly heatup the deaerators. 5.3.19 Increase pegging steam pressure until 2.3 psig is reached on both deaerators. 5.3.20 Place ST 14 and ST 15 in the startup mode. (These traps will be kept in the startup mode with the bypasses open.) l 5.3.21 It may be necessary to throttle flow through FW 33 at this time to allow deaerator heating to occur. Control flow on FW 33 to turn over Deaerator H 20, f 8 heatup the system, and maintain within the Auxiliary l Boiler steam flow capacity. NOTE: Ensure that both MFP's warmup lines are in service. Trend MFP suction temperature computer points T-044 and T-051 to ensure both deaerators heatup together. 5.3.22 When the feedwater system and deaerator have reached
8 SP 1106.07.7 7 temperature equilibrium at approximately 220', open > the outside deaerator vents approximately 1/4 turn open. NOTE: When setting the deaerator vents, ensure
" play" in the valve is taken up.
5.3.23 Circulate the FW in this manner until the Chen & HP Department determines by sampling that the W at the 7 outlet of the HP FW Header meets the applicable , specifications of PP 1101.04 or the following: 02 <7 ppb FE <100 ppb Cond <0.5 paho/cm 5.3.24 When the FW is cleaned up, throttle back en FW33 to reduce the loads on the Aux Boiler but avoid throttling back to the point where the condensate line starts to water h===ar due to low flow. 5.3.25 Notify C&HP to place one of the polishers in " Hold".
- 6. FEEDWATER SYSTEM STARTUP AND NORMAL OPERATION 6.1 Prerequisites 6.1.1 Condensate System is in operation as per SP 1106.16. ~N
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6.1.2 Feedwater cleanup has been completed as per this procedure, Sectica 5. 6.1.3 MFPT is on turning gear as per SP 1106.20, Main Feed Pumps and Turbine Operating Procedure. 6.1.4 OTSG level is 250 i 50 inches of full range. (35% to 70% on the operate range.) 6.2 Limitations and Precautions 6.2.1 The Steam generator shall be considered dry when the startup range level indication decreases to or below 8 inches. This condition will require manual actuation of auxiliary feedwater and injection of same through the auxiliary nozzles until minimum level is established, at which time normal feedwater flow through the main nozzles may be restored. The main feedwater nozzles are not to be used when the OTSG is in the dry condition as this may cause thermal shocking of the lower tubesheet. 6.2.2 The maximum OTSG heatup and cooldown rate is 100*F/hr.
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m 9 SP 1106.07.6 6.2.3 Maximum temperature difference between feedwater line temperature and steam generator lower downcomer temperature is 350*F, when using the main feedwater nozzles. This difference can be calculated by using
" LWR DNCMR TEMP" TI SP8B (TI SP8A) and " MAIN FW TEMP" TI SP1 located on the Control Room Feed Pump Console.
6.2.4 Just before reaching 180*F RCS temperature, establish the FW minimum bypass flow. Open W 612 and FW 601 (Main FW Stop Valves), then locally open FW 139 for loop 1 and W 44 for loop 2. W minimum bypass flow 6 of greater than or equal to 32 gpa should be maintained when RCS temperature is greater than or equal to 180*F. This flow must be maintained until 5% power is exceeded. FW temperature must be maintained greater than 90*F. 6.2.5 Minimum OTSG operating water level is 35 inches on the Startup Range.
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6.2.6 The OTSG minimum level is 25.6 inches (SFRCS Low Level Trip Setpoint). 6.2.7 Minimum allowable feedwater tenperature to the main. feed nozzles is 90*F, except when secondary side filling conditions exist as per SP 1106.08, SG Secondary
. Side Fill, Drain and Layup.
(TS 6.2.8 Maximum OTSG operating water level is 84% of operating 3.4.5) range (348" on Full Range instrumentation) while in modes 1 through 4. 6.2.9 Steam generator fill water chemistry must be in accordance with PP 1101.04, Operational Chemical Control Limits. 6.2.10 Steam Generator level indications are dependent on containment temperature. Because an elevated reference leg temperature causes the indicated level to be higher than the actual level, calibration curves must l be used to correctly determine Steam Generator level. . These curves are given in Attachment 3 for Startup I Range, Attachment 4 for Operate Range, and Attachment l 5 for Full Range. Each range includes reference leg i temperatures from 68 - 250*F, as measured by containment 1 temperature indicators TI 1356, TI 1357, TI 1358, or l computer points T 298, T 302, and T 306. l The conditions need be considered only under accident l l
l 10 SP 1106.07.6 -s I conditions which cause high containment temperature. Also note that pressurizer and core flood tank levels will be similarly affected by containment temperature. 6.3 Procedure 6.3.1 Conditions are as follows:
- 1. The OTSG's are being maintained at less than or equal to 84% (preferably at 35% to 70%) on the Operate Range by throttling S/G 1-1 (1-2) Drain Line Isolation Bypass Valve MS 611A (MS 603A) or S/G 1-1 (1-2) Drain Line Isolation Valves MS 611 (MS 603).
- 2. The SUFP is in operating supplying mini feed through FW 139 and W 44 to the OTSG main feed
, nozzles.
- 3. At least one MFP is in standby condition.
- 4. Vacuum is established in the main condenser.
- 5. The main turbine is on gear.
._3
- 6. One condensate pump is in service and one polisher )
. also. -
6.3.2 When plant startup has progressed to the point where the fourth RCP has been started and the turbine bypass valve begins to dump steam to the condenser to maintain l 870 psig in the main steam lines (Tave @ 530*F), 6 increase feedwater flow using the startup control valve to maintain 35% to 70% on the operate range. > Use FIC ICS 33B in hand for SG 1-1 and FIC ICS 33A in hand for SG 1-2. CAUTION: If SUFP discharge pressure is less than 900 psig or if full load amps of 44 amps is exceeded, it will be necessary to start a MFP to maintain SG level. 6 6.3.3 Just prior to going critical place the steam generators on low level ILeits by performing the following steps. NOTE: If a delay occurs in going critical or going to Mode 1 after Steam Generators are on low level limits, it may be necessary to raise Steam Generator levels to 250 1 50 inches on SG full range level instruments (35% to 70% on operate range) and perform a fill,
11 SP 1106.07.6 soak and drain sequence to maintain Steam Generator water chemistry. If Steam Generator water chemistry is NOT within spec, the reactor may not be taken above 5% power until it is in spec. To place the Steam Generators on low level limit control, perform the following steps.
- 1. Place Loop 1 Feedwater Demand H/A Station (ICS 32B) in AUTO.
NOTE: Ensure the Feedwater ratio on the AT c controller (ICS 30) is at 50%.
- 2. Place Loop 2 Feedwater Demand H/A Station (ICS 32A) in AUTO.
- 3. Place Loop 1 Main Feedwater Valve H/A Station (ICS 35B) in AUTO.
- 4. Place Loop 2 Main Feedwater Valve H/A Station (ICS 35A) in AUTO.
- 5. Level FW flow off to hold constant SG levels of 250 t 50 inches on the SG full range level instruments (35% to 70% on the operate range).
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- 6. Using the Steam Generator drain valves, decrease SG 1evels.
- 7. When the SG levels approach minimum level (35" in the startup range instruments), place the Startup Feedwater Valve H/A Station's meter selector switch from "POS" to " MEAS VAR".
CAUTION: Steam Generator automatic low level limit is blocked when the Startup Feedwater Valve H/A Stations are in Hand. SG 1evel of 26.5" will initiate steam line rupture isolation and aux feedwater start. Drain SG's very slowly below 45".
- 8. When SG level reaches the low level limit (35")
on ICS SG 1 (2) ON LO LVL LIMIT alarm will - annunciate in the Coatrol Room. Adjust SG drains to hold SG level at 35" and use the Startup Feedwater Valve H/A Station to adjust SG level as necessary. The SG drains should be just cracked open or closed.
t : 12 SP 1106.07.7 ,_
- 9. When SG 1evel has steadied out at 35" and no /
error exists in " MEAS VAR" (as indicated by the meter reading 50%), place the Loop 1 and 2 Startup Feedwater Valve H/A Stations in "AUT0" ICS 33B and ICS 33A respectively and place the Delta Tc Controller (ICS 30) H/A Station in "AUT0" with a FW ratio of 50%.
- 10. Slowly close the SG drains MS 603A, MS 611A, MS 603, and MS 611 if not already closed. Also close the reach rod SG lower tube sheet drains in Containment, MS 863 on SG 1-1 and MS 889 on SG 1-2, and in the Turbine Building close the SG Drains to the Condenser, MS 873, SG 1-1 Drain to LP Condenser and MS 895, SG 1-2 Drain to HP Condenser. Refer to AD 1839.02 for locked valves.
6.3.4 At approximately 1% power, place the Standby Main Feed Pump on line per SP 1106.20 Main Feed Pump and Turbine Procedure. - 6.3.5 Increase NFPT speed as necessary to overcome SUFP discharge pressure. 6.3.6 When the MFP is providing flow to OTSG's, stop the "[} SUFP per SP 1106.27 SUFP operating procedure. J 7 NOTE: SUFP suction valves (FW91 or FW32), SUFP discharge valve (FW106) and the TPCW valves to SUFP coolers (CW196 and CW197) must be shut and the close power fuses for SUFP Brkr (AD210) must be removed after SUFP is shutdown. 6.3.7 Close FW 33 and FW 104. l 6.3.8 At approximately 15% reactor power, main block valves ' FW 779 and FW 780 will open and feedwater control valves, SP6A and SP6B, will start to control feed flow. ) 7 NOTE: If FW 779 or FW 780 bind and remain closed, vent the bonnet of FW 799 through bonnet vent valves FW 800 and FW 801 or vent the bonnet of FW 780 through bonnet valves FW 802 and FW 803. 6.3.9 A second MFP will be started at 450 MW generator load i according to SP 1106.20, MFP and T System Procedure.
. . - ~ _- .. . -
I 13 SP 1106.07.6 NOTE: A list of Feedwater Heater Resets and Reset locations is provided on Attachment 1.
- 7. FEEDWATER SYSTEM SHUTDOWN
! 7.1 Prerequisites 7.1.1 It is designed to shutdown the plant as per PP 1102.04 Plant Shutdown and Cooldown.
7.2 Limits and Precautions 7.2.1 See Section 6.2 7.3 Procedure 7.3.1 At 450 MWe decreasing take either 1-1 or 1-2 NFP off the line per SP 1106.20 Main Feed Pump and Turbine Operating Procedure. 7.3.2 After all regulating rods and safety rod groups except groap 1 are inserted as per PP 1102.10 Plant Shutdown and Cooldown, place Main Feedwater and Startup Feedwater control valves (ICS 35A and B and ICS 33A and B) in hand and slowly increase and maintain OTSG levels to between 35% and 70% on the Operate Range. Maintain less than a 100*F/hr cooldown rate. NOTE: When any Main or Startup Feedwater control valve is placed in hand, the Rapid Feedwater Reduction (RFR) portion of the ICS will no longer target feedwater flow or MFPT speed on a reactor trip. ; 7.3.3 Perform Valve Lineup List E to lineup OTSG drains to the condenser. NOTE: If required as an aid in controlling SG level, position SG tube sheet drain valve bypass valve (s) MS 611A (MS 603A) from the CTRM Panel C5721. If it is planned to remain in Mode 3, at the Shift Supervisor's discretion, only lower tube sheet drains MS 863 and MS 889 need to be opened. If so,
" INFO TAG" h'IS 611A and HIS 603A in the Control Room. These are controlled per AD 1839.02, Locked Valves. Inform the Shif t Supervisor that for multiple Containment entries, ST 5061.05 is required every 72 hours and should be completed per I&C's ST
14 SP 1106.07.6 s schedule. Place the due date and time for ST 5061.05 on the plant equipment status board. NOTE: If the water in the Steam Generators is out of spec, start the following sequence: fill, soak (approximately two hours), and , drain Steam Generators. Continue this procedure until the water in the SG's is within spec. If the chemistry is out of limits after eight hours, the system must be cooled to less than 400*F. LIMITS: C1 1.0 ppe max Sodium 2.0 ppa max Cation Conductivity 10.0 unho/cm Silica 2.0 ppe max 7.3.4 When decay heat load is low enough and when necessary for proper SG level control, transfer from the NFPT to the Startup Feedwater Pump (SUFP) by perfonsing the - following: If Turbine Bypass valves go closed in auto or have to be closed to stop or limit cooldown, place SUFP on and take off MFPT. If the SUFP is not available, transfer the NFPT to auxiliary steam.
,d With one MFPT operating at required speed ~~~
NOTE: - and the feedwater control valves in hand, exercise caution when transferring from the MFPT to the SUFP. The feedwater control valve delta P change may necessitate feed-water valve repositioning to maintain SG level at 35% to 70% on the operate range. Loss of feedwater pressure could actuate the steam and feedwater rupture control system. The capacity of the SUFP is approximately 1.3% of full power. Depending on core power history decay heat may be as high as 1.7% one hour after reactor shutdown. The total feedwater flow (FI SP3A and SP3B) should be less than approximately 100,000 lb/hr when changing over from the MFPT to the SUFP.
- 1. Start the SUFP as per SP 1106.27
- 2. Open FW 106 SUFP discharge to the EP FW heaters and check closed FW 102.
- 3. Place operating MFPT Bailey Station (MGU ICS 36B or ICS 36A) in hand and decrease it to the low
~~
I i
/
l l
, 15 SP 1106.07.8 8l speed stop. While decreasing speed, ensure SUFP l discharge pressure is maintained above 900 PSIG and SUFP amps is maintained below 44 amps.
8l 4. Obserse SUFP amps, discharge pressure, feedwater control valve delta P (PDI SP5B, SP5A) and OTSG level. I 8 7.3.5 Transfer MFPT control from ICS to NDT-20 per SP 1106.20. i i 7.3.6 Decrease MFPT speed until green "LSS" limit illuminites using manual pistol grip HS 805D (HS 806D). _ _ 7.3.7 Place MFPT on turning gear as per MFPT Operating Procedure SP 1106.20. Lineup (or ensure it is lined up) auxiliary steam to the MFPT's to provide a backup pump (s) to the SUFP. i 7.3.8 If Nain Feedwater System is being used to achieve natural circulation during cooldown, increase both ^ OTSG levels to approximately 60% to 70% on the operate range to provide maximum natural circulation. This step is performed after the Decay Heat pumps are started but prior to stopping all RCP's.
. 7.3.9 When the RCS temperature is 200*F and prior to reaching
- 190*F, increase the OTSG levels to 97% to 99% on the operate range or to the level and temperature restric-tions as per Enclosure 2.
7.3.10 Cooldown the deserators and decrease feedwater tempera-ture to prevent hot feedwater from keeping the OTSG's and RCS hot as cooldown progresses. The deaerator drain valve to the condenser FW 104 can be used to aid in decreasing FW temperature.
- 8. FEEDWATER SYSTEM LAYUP DURING A PLANT SHUTDOWN AND C00LDOWN 8.1 Prerequisites 8.1.1 The RCS has been cooled down to less than 200*F with the turbine bypass valves closed and feedwater minimum flow in service.
8.1.2 C&HP has been notified that sufficient quantities of hydrazine and ammonia must be available. 8.1.3 The Chemical Addition System is operable. 8.2 Procedure 8.2.1 Perform Valve Lineup List D being careful to maintain l l l
16 SP 1106.07.7 __ s SUFP amps less than 44 amps and discharge pressure ~'- greater than 900 PSIG. a 8.2.2 C&HP should sample and add hydrazine and ammonia as necessary to maintain hydrazine 200 ppe and no less than 50 ppe and ammonia 10 ppe and no less than 3 ppa. 8.2.3 The feedwater system should be recirculated for 16 hours at 360 GPM to obtain two turnovers of the feedwater system before sampling. 8.2.4 When chemistry is in spec., the SUFP may be shutdown as per SP 1106.27 SUFP Operating Procedure. 7 NOTE: SUFP suction valves (FW91 or FW32), SUFP discharge valve (FW106) and the TPCW valves to SUFP coolers (CW197 and CW196) must be shut and the close power' fuses for SUFP breaker (AD 210) must be removed after SUFP is shutdown. 8.2.5 Circulate the feedwater system as directed by C&HP when chemistry is out of spec using the SUFP.
; )
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% of 14 VALVE VERIFICATION LIST A l
i Feedwater System Startup and Normal Operations i 4 Verification List Only - Consult Shift Supervisor Prior to Repositioning In Plant Valves P&ID NO. VALVE VALVE VERIFY l VALVE DESCRIPTION Coord. NUMBER POSITION BY t CONTROL ROOM M-006B HP FW Mtr 1-1-6 FW Outlet Isolation C-6 W 440 Open ! HP FW Htr 1-1-4 FW Inlet Isolation M-006B l 4 Valve E-6 FW 448 Open M-006B i HP W Htr 1-2-6 W Outlet Isolation C-8 W 450 Open i M-006B
- HP FW Htr 1-2-4 FW Inlet Isolation E-7 FW 459 Open .
M-006B HP W Ntr FW Bypass Valve C-7 W 460 Closed S/G 1-2 Main FW Control Valve M-007 Isolation H-5 FW 779 Open* S/G 1-1 Main W Control Valve M-007 Isolation H-9 FW 780 Open* l - M-007 , S/G 1-2 Main W Stop Valve H-3 W 601 Open* M-007 S/G 1-1 Main W Stop Valve H-11 FW 612 Open* ROOM 404 MAIN CORRIDOR (RACA) M-007 In i W Loop 1 Flow Transmitter 2 H-8 FTSP2B2 Service l M-007 In
- l. W Loop 1 Flow Transmitter 1 H-8 FTSP2B1 Service FW Loop 1 Flow Transmitter 2 M-007 Source H-10 SP2B2A Open l
FW Loop 1 Flow Transmitter 2 M-007 Source H-10 SP2B2B Open ! W Loop 1 Flow Transmitter 1 M-007
- Source H-10 SP2BIA Open FW Loop 1 Flow Transmitter 1 M-007 Source H-10 SP2 BIB Open M-007 i S/G 1-1 FW Hde Vent Valve H-11 W 145 Closed CONTAINMENT M-007 i FW Loop 1 Vent Inside Containment C-12 FW 148 Closed 4
- Closed during F.W. Cleanup.
I, 1 .I 1 . - - . - - - - _ . - - . . - . _ _ , - - _ - - . - _ . , _ - , - - . _ . , - - - . .
20 SP 1106.07.7 - Sheet No. 2 of 14 VALVE VERIFICATION LIST A - Feedwater System Startup ani Nonnal Operations Verification List Only - Consult Shift Supervisor Prior to Repositioning In Plant Valves
.P&ID NO. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY M-007 W Loop 1 W Ring Drains Inside CTMT C-11 W 149 Closed M-007 W Loop 1 FW Ring Drains Inside CTNT C-11 W 150 Closed M-007 W Loop 2 Vent Inside CTNT : C-1 FW 158 Closed M-007 W Loop 2 Ring Header Drains C-1 W 159 Closed M-007 FW Loop 2 Ring Header Drains C-1 W 160 Closed ROOM 303 MECHANICAL PENETRATION ROOM #3 M-007 In Main W 1 SG 1 Press J-11 PDS2686A Service M-007 In Main W 1 SG 1 Press J-10 PDS2686B Service ,
M-007 In Main W 1 SG 1 Press J-11 PDS2686C Service M-007 In Main W I SG 1 Press J-10 PDS2686D Service SG 1-1 Wet Lay Up Recirc Line M-007 Instrument Tap F-11 W 2686D Closed 7 SG 1-1 Wet Lay Up Recirc Line M-007 Instrument Tap F-11 W 2686B Closed M-007 W Loop 1 Hydro Test Pump Connection H-12 MS 743 Closed M-007 FW Loop 1 Drain Valve H-12 W 26 Closed Mn W 1 and SG 1 PDS 2686C and D M-007 Source V1v H-11 W 2686F Open Mn W 1 and SG 1 PDS 2686A and B M-007 Source V1v H-11 FW 2686E Open M-007 S/G 1-1 FW Hdr Drain Valve H-11 FW 146 Closed M-007 MW to SG 1 PDS 2686C & D Source Valve H-11 FW 2686C Open 7 M-007 MFW to SG 1 PDS 2686A & B Source Valve H-11 FW 2686A Open ROOM 314 MECHANICAL PENETRATION ROOM s/'t 7 7 SG 1-2 Wet Lay Up Recirc Line M-007 Instrument Tap F-2 , FW 2685D. Closed l
21 SP 1106.07.7
/.
Sheet No. 3 of 14 VALVE VERIFICATION LIST A Feedwater System Startup and Normal Operations Verification List Only - Consult Shift Supervisor Prior to Repositioning In Plant Valves tP&ID NO. VALVE VALVE VERIFY Y VALVE DESCRIPTION Coord. NUMBER POSITION BY SG 1-2 Wet Lay Up Recire Line M-007 7 Instrument Tap F-2 W 2685B Closed M-007 W Loop 2 Hydrotest Pump Connection H-2 MS 741 Closed M-007 FW Loop 2 Drain Valve H-1 FW 157 Closed Mn FW 2 and SG 2 PDS 2685C and D M-007 Source Viv H-3 FW 2685E Open da FW 2 and SG 2 PDS 2685A and B M-007 Source Viv H-2 FW 2685F Open M-007 S/G 1-2 FW Hdr Drain Valve H-3 FW 155 Closed ROOM 313 B.A. MIX TANK AND HATCH AREA M-007 S/G 1-1 W Hde Drain Valve H-10 FW 144 Closed (. - ROOM 707 DEAERATOR HEATER BAY Main Feed Pump 1-2 Recirculation M-006B Valve Outlet Bypass D-10 FW 37 Closed Main Feed Pump 1-2 Recirculation M-006B Scaled Valve Isolation G-9 FW 29 Open M-006B MFP 1-2 Min Flow Line Drain D-10 FW 27 Closed Main Feed Pump 1-2 Recirculation M-006B Line Vent Valve E-9 FW 31 Closed Main Feed Pump 1-2 Recirculation M-006B In Valve E-9 FW 438 Service Main Feed Pump 1-2 Recirculation M-006B Sealed Valve Outlet Isolation C-9 FW 35 Open Startup Feedwater Pump 1-1 Minimum
~
M-006B Recirculation Division Valve B-4 FW 98 Closed Startup Feedwater Pump 1-1 Minimus M-006B Scaled Recirculation Isolation B-4 FW 96 Open Startup Feedwater Pump 1-1 Minimum M-006B Scaled Recirculation Isolation B-5 FW 97 Open Main Feed Pump 1-1 Recirculation M-006B Sealed Valve Outlet Isolation C-4 W 34 Open M-006B In Main Feed Pump 1-1 Recirculation Valve E-4 FW 428 Service Main Feed Pump 1-1 Minimum Flow M-006B
, Line Drain C-6 FW 9 Closed I
b
4
. I i
22 SP 1106.07.4 -
' ~' i Sheet No. 4 of 14 VALVE VERIFICATION LIST A I '
Feedwater System
. Startup and Normal Operations j dl Verification List Only - Consult Shift Supervisor Prior to Repositioning In I Plant Valves
, P&ID NO. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY Main Feed Pump 1-1 Recirculation M-006B Line Vent G-4 FW 30 Closed Main Feed Pump 1-1 Recirculation M-006B Sealed Valve Isolation E-3 FW 28 Open Main Feed Pump 1-1 Recirculation M-006B Valve Outlet Bypass D-3 FW 36 Closed ROOM 514 HEATER BAY 623' Deserator Storage Tank 1-2 Outlet M-006B Isolation Valve C-10 FW 2 Open M-007 - S/G 1-2 FW Hdr Vent Valve H-5 FW 152 Closed S/G 1-2 FW Loop 2 Flow Transmitter M-007 1 Source H-6 SP2A1A Open S/G 1-2 FW Loop 2 Flow Transmitter M-007 4 Open 1 Source S/G 1-2 FW Loop 2 Flow Transmitter H-6 M-007
~'
SP2A1B 9l 2 Source H-6 SP2A2A Open ; S/G 1-2 FW Loop 2 Flow Transmitter M-007 2 Source H-6 SP2A2B Open M-007 S/G 1-1 FW Nde Vent Valve H-8 FW 141 Closed HP FW Her 1-1-4 Inlet Press Indica- M-006B tion Source E-6 FW 447 Open M-006B HP FW Hte 1-1-4 Outlet Line Vent D-6 FW $5 Closed HP FW Ntr 1-1-4 Outlet FW Press M-006B Indicator Source E-6 FW 446 Open M-006B HP FW Hte 1-1-4 FW Side Vent Valve E-5 FW 53 Closed M-006B E-6 FW 51 Closed _HP FW Htr 1-1-4 FW Inlet Drain Valve M-006B KP FW Htr 1-2-4 Outlet Line Vent D-7 FW 56 Closed KP FW Htr 1-2-4 Outlet FW Press M-00eB Indication Source E-7 FW 456 Open M-006B HP FW Her 1-2-4 FW Side Vent Valve E-8 FW 54 Closed M-0068 HP FW Xtr 1-2-4 FW Inlet Line Drain E-7 FW 52 Closed HP FW Hte 1-2-4 FW Inlet Press M-006B In j Indication E-8 PI 458 l Se rvice I ,
^ -- --
- ' - - - - ^
. 23 SP 1106.07.4 Sheet No. 5 of 14 VALVE VERIFICATION LIST A Feedwater System Startup and Normal Operations l 4l Verification List only - Consult Shift Supervisor Prior to Repositioning In Plant Valves P&ID NO. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY 4
HP W Etr 1-1-4 FW Inlet Press M-0068 In Indication E-6 PI 447 Service HP FW Her 1-2-4 Outlet FW Press M-006B In Indication E-7 PI 456 Service HP FW Htr 1-1-4 Outlet FW Press M-006B In Indication E-6 PI 446 Service Deserator Storage Tank 1-1 Outlet M-0068 Isolation Valve C-3 W1 Open ROOM 430 HEATER BAY AREA 603'
^
MFP Outlet !!de to Aux Sta Edr M-0068 Desuper Htr F-7 W 49 Open M-006B MFP 1-2 Discharme Isolation F-7 W 46 Open M-006B t
' ( .,. MFP 1-2 Discharme Edr Drain F-7 W 48 Closed ,
HP FW Etr 1-2-5 W outlet FW M-0068 In Press Ind D-7 PI 454 Service M-0068 In 4 HP W 1-1-5 Outlet W Press Ind D-6 PI 444 Service M-0068
- HP W Ntr 1-2-5 W Inlet Drain D-7 FW 60 Closed M-0068 HP W Mtr 1-2-5 W Side Vent Valve D-8 W 62 Closed HP FW Htr 1-2-5 FW Outlet Line M-006B i Vent Valve D-8 FW 64 Closed M-006B HP FW Mtr 1-2-4 FW Inlet Line Drain F-7 FW 50 Closed HP W Ntr 1-2-5 FW Outlet FW Press M-006B
, Ind Source D-7 FW 454 Open
- HP W Ntr 1-2-4 W Inlet Press M-006B Indication Source E-8 FW 458 Open l
HP FW Her 1-1-5 Outlet FW Press M-0068 Indication Source D-6 W 444 Open i HP W Her 1-1-5 Outlet Line M-006B l Vent Valve D-5 W 63 Closed i S/G 1-1 Startup FW Control Valve M-007 l Isolation H-8 FW 142 Open i S/G 1-1 FW Warm-Up Rectre Valve M-007 to Demerator H-8 FW 143 Closed j M-000B HP FW Rtr Train #2 FW Flow Ind Source D-8 W 581A Open i i
24 SP 1106.07.7 of 14 VALVE VERIFICATION LIST A Feedwater System Startup and Normal Operations
. Verification List Only - Consult Shift Supervisor Prior to Repositioning In Plant Valves P&ID NO. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY HP W Htr Train #2 W Flow Indication M-006B Source D-8 W 581B Open 7l ifP W Mtr Train #1 W Flow Indication M-006B
_Seurce D-5 W 580A Open EE W Htr Train #1 W Flow Indication M-006B Fource D-5 W 580B Open Loop 1 Startup W Flow Transmitter M-007 Source H-9 SP3BB Open Loop 1 Startup W Flow Transmitter M-007 Source H-9 SP3BA Open S/G 1-1 Startup W Control Valve M-007 Bypass J-9 W 139 Closed M-007 In S/G 1-1 Startup W Control Valve H-10 SP7B Service S/G 1-1 Startup W Control Valve h-007
,A Isolation H-10 W 161 Open M-006B HP W Htr 1-1-5 W Inlet Drain D-6 W 59 Closed M-006B HP W Htr 1-1-5 W Side Vent Valve D-5 W 61 Closed M-006B MFP 1-1 Discharge Hdr Drain E-6 W 47 Closed M-006B MFP 1-1 Discharge Isolation Valve F-6 W 45 Open M-006B
?l SUFP 1-1 to Main W Line Isolation F-6 W 106 Closed M-007 In S/G 1-1 Main W Control Valve H-10 SP6B Service Loop 1 Main W Control Valve Differ- M-007 ential Pressure Transmitter Source H-9 SPSB2A Open MW Block Viv W 780 Bonnet Vent M-007 Valve H-8 W 803 Closed 7 MW Block Viv W 780 Bonnet Vent M-007 Valve H-8 W 802 Closed S/G 1-1 W Cleanup Recirculation M-007 to Condenser J-10 W 163 Closed HP W Htr 1-1-6 Outlet W Press M-006B Indication Source C-6 W 442 Open HP W Hte 1-1-6 W Outlet Line M-006B -
Vent C-5 W 71 Closed Main Feedwater Line Cleanup to M-007 Condenser H-7 W 166 Closed e i
; 6 25 SP 1106.07.8 Sheet No. 7
-. of 14 VALVE VERIFICATION LIST A Feedwater System Startup and Normal Operations Verification List Only - Consult Shift Supervisor Prior to Repositioning In Plant Valves P&ID NO. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY 8 M-007 W Mini Bypass to Cndsr Iso Viv E-2 W 170 Closed S/G 1-2 Startup FW Control Valve M-007 Isolation H-4 FW 162 Open M-007 In S/G 1-2 Startup W Control Valve J-4 SP7A Service M-007 In S/G 1-2 W Loop 2 Flow Transmitter 1 H-6 FISP2A1 Service M-007 In S/G 1-2 W Loop 2 Flow Transmitter 2 H-6 FTSP2A2 Service S/G 1-2 FW Cleanup Recire Valve to M-007 Cond J-3 W 164 Closed Loop 2 Startup FW Flow Transmitter M-007 Source J-4 SP3AB Open Loop 2 Startup FW Flow Transmitter M-007 Source J-4 SP3AA Open S/G 1-2 Startup FW Control Valve M-007 Bypass J-4 FW 44 Closed S/G 1-2 Startup FW Control Valve M-007 Isolation H-5 FW 154 Open S/G 1-2 W Warsup Recire Valve to M-007 Demerator H-5 W 153 Closed MFW Block Valve W 779 Bonnet Vent M-007 Valve H-4 W 801 Closed MFW Block Valve W 779 Bonnet Vent M-007 Valve H-5 W 800 Closed Loop til Main FW Control Valve Differ- M-007 ential Pressure Transmitter Source H-5 SP5A2A Open M-007 In S/G 1-2 Main FW Control Valve H-4 SP6A Service M-007 Cleanup Recirc to Condenser Vent K-10 FW 165 Closed ROOM 326 HEATER BAY AREA 585' M-007 FW Loop 2 Press Diff Switch Source H-3 FW 2685C Open M-007 FW Loop 2 Press Diff Switch Source H-3 W 2685A Open Loop r/1 Main FW Control Valve Differ- M-C07 ential Pressure Transmitter Source H-3 SPSA2B Open M-007 In Main FW 2 and SG 2 Diff Press J-3 PDS2685A Service 1
26 SP 1106.07.7 . .s Sheet No. 8 of 14 VALVE VERIFICATION LIST A Feedwater System Startup and Nonnal Operations Verification List only - Consult Shift Supervisor Prior to Repositioning In Plant Valves P&ID NO. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY M-007 In Main W 2 and SG 2 Diff Press J-3 PDS2685B Service M-007 In Main FW 2 and SG 2 Diff Press H-3 PDS2685C Service M-007 In Main W 2 and SG 2 Diff Press H-3 PDS2685D Service Loop #1 Main W Control Valve Differ- M-007 In ential Pressure Transmitter H-5 PDTSP5A1 Service Loop #1 Main FW Control Valve Differ- M-007 In ential Pressure Transmitter H-5 PDTSP5A2 Service , HP FW Rtr FW Edr Outlet Pressure M-006B In Transmitter B-6 PT 432 Service M-007 In Loop 2 Startup W Flow Transmitter J-4 FTSP3A Service M-0068 SUFP 1-1 to Condensar Isolation F-7 W 102 Closed ' SUFP 1-1 Discharge Differente.a1 M-006B J-1 W 2657A Open Press Source SUFP 1-1 Discharge Differenhal M-0068 J-1 FW 2657B Open
- Press Source M-007 HP W Ht( FW Hdr Outlet Drain Valve H-7 W 140 Closed Startup pd Pump 1-1 Feed Line M-0068 Vent Valve F-7 W 108 Closed Startup FW Pump 1-1 Feed Line M-006B 7l F-7 FW 107 Closed Drain Valve Ammonia Injection to HP FW Otilet M-006B Rdr Isol B-6 SC 22 Closed M-006B HP FW Outlet Ndr Sample Valve B-5 SS 33 Open HP FW Hte FW Hde Outlet - Sample M-006B B-7 SS' 31 Open Valve HP FW Htr FW Hde Outlet Pressure M-006B Transmitter Source B-6 W 432 Open HP W Htr W Hde Cutlet Sample M-006B B-8 SS 32 Open Valve Ammonia Injection to FW Header M-006B Isolation B-7 SC 24 Closed M-006B MP FW Htr 1-2-6 Outlet Line Drain C-7 FW 73 Closed Loop 1 Main W Control Valve Differ- M-007 In ential Pressure Transmitter K-9 PDTSP5B1 Service
s . 27 SP 1106.07.4 ( Sheet No. 9 of 14 VALVE VERIFICATION LIST A Feedwater System Startup and Normal Operations Verification List only - Consult Shift Supervisor Prior to Repositioning In Plant Valves P&ID NO. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY Loop 1 Main W Control Valve Differ- M-007 In ential Pressure Transmitter K-9 PDTSP5B2 Se rvice M-007 In Loop 1 Startup W Flow Transmitter H-9 FTSP3B Service M-006B In HP W Hte Train #2 W Flow Indication D-8 FT 581 Service M-006B In HP FW Her Train #1 W Flow Indication D-5 FT 580 Service HP W Ntr 1-1-6 Outlet FW Press M-006B In Indication C-6 PT 442 Service l Loop 1 Main W Control Valve Differ- M-007 . ential Pressure Transmitter Source H-10 SPSB2B Open M-006B HP FW Htr 1-1-4 Outlet Line Drain D-6 FW 57 Closed M-006B HP W Htr 1-1-6 FW Side Vent Valve C-5 W 69 Closed M-006B HP W Htr 1-1-6 W Side Drain Valve C-6 FW 67 Closed , HP FW Her 1-1-5 FW Outlet Line Drain M-0068 Valve D-6 FW 65 Closed HP FW Hte 1-2-6 FW Outlet Press M-006B Indication Source C-7 FW 452 Open HP FW Ktr 1-2-6 FW Outlet *Line Vent M-006B Valve C-7 FW 72 Closed HP FW Heater 1-2-4 FW Outlet Line M-006B Drain D-7 W 58 Closed HP FW Heater 1-2-6 FW Side Vent M-006B Valve C-8 W 70 Closed HP W Heater 1-2-5 FW Outlet Line M-006B ! Drain Valve D-8 FW 66 , closed HP W Hester 1-2-6 FW Side Drain M-006B Valve C-7 FW 68 Closed HP FW Htr 1-2-6 W Outlet Press M-006B In Indication C-7 PI 452 Se rvice ROOM 334-W AREA WEST OF CONDENSER 585' Demerator Stg Tank 1-1 to BFP 1-1 M-005B Sealed Suction D-2 FW 3 Open Fire Protection System to FW System M-006B Isolation J-6 FP 28 Closed i 6
._ . . _ _ . . - _ - . _.7 28 SP 1106.07.6 Sheet No. 10 of 14 VALVE VERIFICATION LIST A - Feedwater System Startup and Normal Operations Verification List only - Consult Shif t Supervisor Prior to Repositioning In Plant Valves P&ID NO. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY Deserator Stg Tanks to Condenser M-0068 Globe Valve F-9 W 33** Closed Deserstor Stg Tanks to Condenser M-0068 Pent #51 F-8 W 104** Closed Deserator Stg Tanks to Condensate M-006B Sta Tanka F-8 W 105 Closed M-0068 SUFP 1-1 to Condenser Vent Valve F-7 W 103 Closed Deserator Stg Tank 1-1 to 1-2 M-006B Outlet Crossover D-3 W 84 open Deserstor Stg Tank 1-2 to 1-1 M-0068 Outlet Crossover G-10 W 423 Throttled M-006B Sealed Deserstor Sta Tank 1-2 to BFP Suction F-11 W4 Open M-0068 MFP 1-2 Suction Line Vent Valve G-9 W 21 Closed Booster FW Pump 1-2 Discharge Flow M-0068 ' 'c. / Transmitter Source G-9 W 438A Open Booster W Pump 1-2 Discharge Flow M-006B Transmitter Source G-9 W 4388 Open M-0068 MFP 1-1 Suction Line Drain Valve G-3 W 10 Closed W Booster Pump 1-1 Discharge Flow M-0068 . Transmitter Source G-3 FW 428A Open FW Booster Pump 1-1 Discharge Flow M-006B Transmitter Source G-3 W 428B Open ROOM 252 MAIN FEED PUMP PIT M-0068 Booster FW Pump 1-1 Drain Valve F-2 W6 Closed M-0068 Booster FW Pump 1-1 Vent Valve F-2 W 38 Closed M-006B Booster W Pump 1-1 Drain Valve F-2 W 111 Closed Booster FW Pump 1-1 Suction M-006B Instrument Source F-1 F_W 466 Open Booster W Pump 1-1 Inlet Strainer M-006d 6 Diff Pressure Indication Souren D-2 W 464A Closed Booster FW Pump 1-1 Inlet Strainer M-006B l
,Diff Pressure Indiestion Source D-2 i FW 464B Open
**0 pen during feedwater startup.
29 SP 1106.07.6 Sheet No. 11 of 14 VALVE VERIFICATION LIST A Feedwater System Startup and Normal Operations Verification List Only - Consult Shift Supervisor Prior to Repositioning In Plant Valves P&ID NO. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY M-006B In MFP 1-1 Discharte Pressure Transmitter G-7 PT 473 Service M-006B In MFP 1-1 Discharge Pressure Indication H-7 PI 477 Service M-006B In MFP 1-1 Discharge Pressure Switch H-7 P3H 506 Service W Booster Pop 1-1 Discharge Flow M-006B In Transmitter G-3 FT 428 Se rvice 6 Booster FW Pump 1-1 Suction Strainer M-006B In Pressure Switch D-2 PSL 464 Service M-006A 4 Seal Water Drain Tank to Cond Vent F-2 W 42 Closed MFP 1-1 Seal Wtr Dru Tk Level M-006B In Control Valve H-2 FW 485 Service MFP 1-1 Seal Water Drain Tank Level M-006B Gate Src H-2 FW 778A Open MFP 1-1 Seal Water Drain Tank Level M-006B Gate See H-2 W 778B Open MFP 1-1 Seal Water Drain Tank Level M-006B in Gate H-2 LG 778 Service MFP 1-1 Seal Water Drain Tank Level M-006B Switch Src H-3 W 474A Open MFP 1-1 Seal Water Drain Tank Level M-006B Switch See H-3 W 474B Open MFP 1-1 Drain to Seal Water Drain M-006B _ Tank 1-1 H-3 FW 19 Open MFP 1-1 Seal Water Drain Tank Level M-006B LSL 474 & In Switches H-3 LSH 474 Service MFP 1-1 Seal Water Drain Tank to M-006B In Condenser H-2 FW 485 Se rvice MFP Seal Wtr Drn Tk 1-1 Level M-006D In Controller H-2 LC 485 Service MFP 1-1 Discharge Pressure Switch M-006B Source H-7 FW 506 open MFP 1-1 Discharge Pressure Transmitter M-006B Source G-7 . W 473 Open M-006D _MFP 1-1 Vent Valve G5 FV 40 Cloned MFP l-1 Discharge Pressure Indication M-006D Source H-7 FV 477 lOpen M-006B Main W Pmnp 1-1 Drain Valve H-5 W 12 Closed .
30 SP 1106.07.6 .s Sheet No. 12 ; of 14 VALVE VERIFICATION LIST A Feedwater System Startup and Normal Operations Verification List Only - Consult Shift Supervisor Prfor to Repositioning In Plant Valves P&ID NO. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY __ MFP 1-1 Seal Water Inlet Isolation M-006B Valve G-6 CD 48 Open MFP 1-1 Seal Water Inlet Isolation M-006B Valve G-6 CD 50 Open M-006B Main W Pump 1-1 Drain Valve H-5 W 11 Closed M-006B Booster FW Pump 1-2 Drain Valve H-10 W8 Closed Booster W Pump 1-2 Discharge M-006B Indication Source H-10 FW 486 Open M-006B Booster W Pump 1-2 Vent Valve G-10 FW 39 Closed M-006B Booster FW' Pump 1-2 Drain Valve H-10 W 113 Closed Booster W Pump 1-2 Suction Pressure M-006B Indication Source G-11 FW 494 Open
.i Booster W Pump 1-2 Suction Strainer M-006B 6 Different_ial Pressure Source F-12 FW 490A Closed Booster FW Pump 1-2 Suction Strainer M-006B Differential Pressure Source F-12 FW 490B Open 6 Booster FW Pump 1-2 Suction Strainer M-006B In Pressure Switch T-12 PSL 490 Service Seal Wtr Den Tk 1-2 to Condenser M-006A Vent Valve D-7 W 75 Closed MFP 1-2 Seal Wtr Drain Tk Level M-006B In Vent Valve H-12 FW 395 Service MFP 1-2 Seal Wtr Drain Tank Level M-000B In Cage H-12 LG $97 Service MFP Seal Water Drain Tank 1-2 Level M-006B Switch Source H-11 FW 493A Open MFP Seal Water Drain Tank 1-2 M-006B Level Switch 9ource H-11 W 493B Open MFP Seal Water Drain Tank 1-2 Level M-006B Cause Valve H-12 W $97A Opan MFP Seal Water Drain Tank 1-2 Level M-006B H-12 FW 597B open
_Cause Valve hfP 1-2 Drain to 3eal Water M-0068 Drain Tank 1-2 H-9 FW 20 Open MFP Seal Water Drain Tank 1-2 Level M-006B LSL 493 & In - Switches H-11 LSH 493 Service MFP 1-2 Seal Water Drain Tank Level M-0008 in Controller H-12 LC 395 Service
s , 31 SP 1106.07.4 Sheet No. 13
. of 14 VALVE VERIFICATION LIST A Feedwater System Startup and Normal Operations 4 Verification List Only - Consult Shift Supervisor Prior to Repositioning In Plant Valves P&ID NO. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY MFP 1-2 Discharge Pressure Transmitter M-006B Source G-7 W 484 Open MFP 1-2 Discharge Pressure Indication M-006B Source G-7 W 482 Open M-006B MFP 1-2 Vent Valve G-8 FW 41 Closed MFP 1-2 Discharge Pressure Switch M-006B Source G-7 W 582 Open M-006B MFP 1-2 Drain Valve H-8 W 14 Closed MFP 1-2 Seal Water Inlet Isolation M-006A .
Valve G-7 CD 49 Open MFP 1-2 Seal Water Inlet Isolation M-006A Valve G-8 CD 51 Open M-006B MFP 1-2 Drain Valve H-8 W 13 Closed (,,,,, M-006B In MFP 1-2 Discharge Pressure Indication G-7 PI 482 Service Booster W Pump 1-2 Discharge Flow M-006B In Transmitter G-9 FT 438 Service
. M-006B In MFP 1-2 Discharge Pressure Switch G-7 PSH 582 Service Booster FW Pump 1-2 Suction Pressure M-006B In Indication G-11 PI 494A Service Booster FW Pump 1 2 Suction Pressure M-006B In Transmitter G-12 PT 494 Service Booster FW Pump 1 2 Discharge Pressure M-006B In Transmitter H-9 PT 486 Service Boouer W Pump 1-2 Discharge Pressure M-006B In Indication H-9 PI 486A Service MFP 1-2 Discharge Pressure Trans- M-006B In mitter G-7 PT 484 Service Feedwater to Condenser Recirculating M-006A Isolation Valve G-5 W 201 Closed **
Feedwater to Condensor Recirculating M-006A Valve F-5 W $23 Closed ** W Booster Pump 1-1 Discharge Pressure M-006B In Transmitter F-2 PT 478 Service lM-006B In Booster FW Pump 1-1 Disch Press Ind iF-2 PI 478A . Service
**0 pen during feedwater cleanup.
32 SP 1106.07.4 3 Sheet No. 14 . of 14 VALVE VERIFICATION LIST A Feedwater System Startup and Normal Operations 4 Verification List Only - Consult Shift Supervisor Prior to Repositioning In Plant Valves PEID NO. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY Booster W Pump 1-1 Suction Press M-006B In Trans F-1 PT 466 Service Booster W Pump 1-1 Suction Press M-006B In Ind F-1 PI 466A Service W Booster Pump 1-1 Discharge M-006B Pressure Transmitter Source F-2 W 478 Open Reviewed by Date 4 Shif t Supervisor or Reactor Operator
.+
.1
.)
i 33 SP 1106.07.8 VALVE LINEUP LIST B i Feedwater Cleanup Lineup
- 1. Open FW 523, FW Cleanup Recir:culation to Condenser
- 2. Close FW 601, Loop 2 Main-FW Stop (Mech Pent Room #4) l
- 3. Close FW 612, Loop 1 Main FW Stop (Mech Pent Room #3)
- 4. Open FW 201, FW Cleanup Recire Iso Valve (MFP Pit)
- 5. Open FW 423, Deaer Xconn 81 Reviewed by Date Shift Supervisor or Reactor Operator l
l i l
\
Page 1 of 1
e . 34 SP 1106.07.4 ,3 Sheet No. 1 .; of 1 VALVE VERIFICATION LIST D Feedwater System Wet Layup Valve List 4 Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve P&ID NO. VALVE VALVE VERIFY i VALVE DESCRIPTION Coord. NUMBER POSITION BY SG 1-1 W Warmup Iso (Htr Bay Area M-007 603') H-5 W 153 Open SG 1-1 W Warsup Iso (Htr Bay Area M-007 603') H-8 FW 143 Open M-006A SG FW Warmup Recire to Deaer (657') C-10 W 203 Open M-006A SG W Warmup Recirc to Deser (657') C-10 W 202 Open M-006A SG FW Warmup Recirc to Deser (670') C-10 W 205 Closed M-006A ' SG W Warmup Recirc to Deser (670') C-10 W 204 Closed M-006A l SG FW Warmup Recirc to Deaer C-10 W 510 Open I Reviewed by Date .. 4 Shift Supervisor or Reactor Operator j
35 SP 1106.07.6 VALVE LINEUP LIST E OTSG Drain Valve Lineup
- 1. Open the following valves in Containment MS863 SG 1-1 lower tubesheet drain MS864 SG 1-1 lower tubesheet drain MS865 SG 1-1 lower tubesheet drain MS866 SG 1-1 lower tubesheet drain MS887 SG 1-2 lower tubesheet drain MS888 SG 1-2 lower tubesheet drain '
MS889 SG 1-2 lower tubesheet drain MS890 SG 1-2 lower tubesheet drain
- 2. Open the following valves in the Turbine Building MS873 SG 1-1 drain to LP Condenser MS895 SG 1-2 drain to HP Condenser
^
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36 SP 1106.07.3 ., F.W. HTR. HIGH LEVEL TRIP RESETS 1-1 (IT HD 300B (1-2 Norm Drn) 603' S of W end of 1-1 Htr (2) GS 346 (Sta Seal Dump to 1-1 Htr CTRM-Pan C5721 Local-603' W of TBS's) 1-2 (1) AS 958 (Flash Tk Vent to #2 Htr's) 603' W of TBV's ES 249 (LP W Htr 1-2 Ext Drain to Cond) CTRM Pnl. C-5722 1-3 (1) AS 2076 (Flash Tk Drn to 1-3 Htr) 657' NE of 2-3 Htr (2) ES 9845 (LPT 1-1 Ext NRV to 1-3 Htr) 657' E of 2-3 Htr (3) HD 291B (1-4 Htr Norn Drn) 623' NW of 1-4 Htr (ES 298 must be reset first) (4) ES 298A & B (LPT 1-1 Ext NRV's to 1-3 Htr) 603' E of N end of 2-5 Htr ES 415 (FW Htr 1-3 Ext Drain) CTRM Pnl C-5722 1-4 (1) HD 271B (1-5 Htr Norm Drn) 623' NW of 1-4 Htr (2) ES 382 (LPT 1-1 Ext NRV to 1-4 Htr) 603' Pit at SE corner ~of condenser " (3) ES 1654 (LPT Ext to 50# Hdr) 585' N of the Stat. Cing. Wtr. Unit ES 417 (FW Htr 1-4 Ext Drn) CTRM Pnl. C-5722 1-5 (1) HD 261B (1-6 Htr Nora Drn) 603' SW of 2-5 Htr , (2) ES 264 (HPT Ext to 1-5 Htr) 603' SW of 2-5 Htr ;) (3) RD 1541B1 (1st Stg Drn Tk to 1-5 Htr) 585' NW of 1-6 Htr - 1-6 (1) ES 256 (HPT Ext NRV to 1-6 Htr) 603' between HPT Exh to MSR 1-1 (2) RD 159B1 (2nd Stg Den Tk 1-1 to 1-6 Htr) 585' W of the N end of 1-6 Htr ES 252 (FW Htr 1-6 Ext Drn) CTRM Pnl C-5722 P 2-1 l (1) HD 331B (2-2 Htr Norm Drn) 603' Handrail W of the SPE's j (2) GS 957 (Sta Seal Dump to 2-1 Htr) CTRM Pan. C5721 Local-603' W of TBV's 2-2 AS 958 (Flash Tk Vent to the #2 Htr's.) 603' W of the TBV's ES 341 (LP FW Htr 2-2 Ext Drain to Cond) CTRM Pal C-5722 2-3 (1) AS 2597 (Flash Tk Den to 2-3 Htr) 657' NE of 2-3 Htr (2) ES 9846 (LPT 1-1 Ext NRV to 2-3 Htr) 657' E of 2-3 Htr (3) HD 381B (2-4 Htr Norm Den) 623' NW of 1-4 Htr (ES 325 must be reset first) (4) ES 325A & B (LPT 1-2 Ext NRV's to 2-3 Htr) 603' E of the N end of 2-5 Htr ES 411 (FW Htr 2-3 Ext Drain) CTRM Pal. C-5722 2-4 III HD 371B (2-5 Htr Norm Den) 623' NW of 1-4 Htr l (2) ES 377 (LPT 1-2 Ext NRV to 2-4 Htr) 603' Handrail W of the SPE's (3) ES 1654 (LPT Ext to 50# Hdr) 585' N of the Stat. Cing. Wtr. Unit ES 409 (W Htr 2-4 Ext Drain) CTRM Pal C-5722 Attachment 1 Page 1 of 2 r
, o 37 SP 1106.07.3 F.W. HTR. HIGH LEVEL TRIP RESETS 2-5 (1) HD 361B (2-6 Norm Drn) 603' SE of 2-5 Htr (2) ES 370 (HPT Ext NRV to 2-5 Htr) 603' SE of 2-5 Htr (3) RD 177B1 (1st Stg Drn Tk 1-2 to 2-5 Htr) 585' E of the N end of 2-6 Htr 2-6 s (1) ES 349 (HPT Ext KRV to 2-6 Htr) 603' Between HPT Exh to MSR 1-1 (2) RD 172B1 (2nd Stg Drn Tk 1-2 to .-6 Htr) 585' E of the N end of 2-6 Htr ES 413 (W Htr 2-6 Ext Drain) CTRM Pnl C-5722 9
Attachment 1 Page 2 of 2
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