ML20126K559
| ML20126K559 | |
| Person / Time | |
|---|---|
| Site: | Davis Besse  |
| Issue date: | 04/11/1985 |
| From: | Parker M, Quennoz S, Wise S TOLEDO EDISON CO. |
| To: | |
| References | |
| SP-1104.02, NUDOCS 8507300328 | |
| Download: ML20126K559 (95) | |
Text
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. _i DISTl:1~ UTION U dAt$ h 1
0 - o Crig6n-C, Responeeble Section Heed Action f 9 c/(, _ P e C .. M r P,,e COPIES TO BE MODIFIED POR IMMEDIATE IMPLEMENTATION l
,^ DAVIS-BESSE NUCLEAR POWER STATION UNIT 1 TEMPORARY MOOlFICATION REQUEST
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IS PROCEDURE REVISION REQUIRED PREP ARED .,
APPPOVED SY my DA,E DATE APPROVED BY \ DATE -
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., RECOMMENDED helrman) */ DATE APR 'll 1985 OATE
- & QA APPROVED BY (Menasse APPROVED BY (Station Superintendent)
All8' of Quellty Assuranch OATE
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~ APR 111985
1 1
Di Tal8UTION l
. DBAB 4 Ortgins, Responsble Secstra Head Actfin ;
e _ Flie Copy, Messer File COPIES TO BE MODIFIED FOR IMMEDIATE IMPLEMENTATION g, DAVIS.BESSE NUCLEAR POWER STATION . UNIT 1 i. 3, ds TEMPORARY MOD!FICATION REQUEST i-c e u. A ED 6926 '3 C3% h SECTION 1 PROCEDURE TITLE AND NUMBER
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! Original. Responese.e section Mead Action Fik Copy. Meever F: e COPIES TO BE MODIFIED FOR IMMEDI ATE !.V8LEMENTATICN
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REASON FOR CHANGE st AL\l6 hAO 7 t 3 t5 7 G 5:E%9c E.b TD THE nA. Rou6 icce M ,
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IS PROCEDURE REVISION REQUIRED -
Yes No if no, tNs mocification is weeld until PREPARED BY DATE
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APPROVED BY "
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.RO EDURE TITLE AND NUMS
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SECTION 2 COMMENTS
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b SECTION 3 SAFETY REVIEW Yes C No NSR change in the facility es described in the PSAR.
9 Yes O NSR change la the prhree es asecribed in the PSAR.
No%
Yes C No NSR test or emperiment not described in the FS AR.
t Yes No Chengo in the Technical Specifications.
NOTE: If any of the above Section Ill are "Yes", a Section IV Safety Evesuetion she64 he performed, uneens this le part of a FCR.
(FCR No. If appl 6cebee).
Yes C No qK Decre=o in me .ffectivenes. of the induewisi S.eurity Fi.n. if this i. "vso . th. change cannot be m.de ,ethout r N RC concurrence.
SECTION 4 SAFETY EVALUATION Yes C No The probeeility of occurrence or the conesquences of en accident or mesfunction of equipment important to esfety f - '
prow 6ovely evalueced in the Safety Analysis Report may be increased.
Yes No A possibil!ty for en accident or melfunction of a different type then any evolueted prewtovely in the Sefety Analvela Report may be created.
+
Yes C No The mergen of safety as defined in the besos for any Technical Specification le reduced.
NOTE: If any of Section IV is "Yes", en "Unreviewed Safety Question
- Is involved and the change cannot be made without NRC concurrence. (FCR No. *f appelceb6e)
SECTION S FOR DELETIONS OR ADQlTIONS OF FROCEDURES, A TEMPOR ARY MOOlFICATION MUST BE SUSMITTED FOR AD 1906.02 AND/
OR A01838.00,lF AFFLICABLE.
Yes C No AD 1905.02 Temporary Modification submitted Yes N AD 183840 Temporary Modification submitted SECTION 6 POR ADDITIONS, DELETIONS,NSR MOOlFICATIONS, AND MOOlFICATIONS REQUINII4G S Af tTV EV ALUAflOf.3, ANO NeR/ NUN.
NSR CHANGES.
SRB Comments:
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. SP 1104.02 Davis-Besse Nuclear Pcwer Staticn LMt Ib. 1 Systen Precedure SP 1104.02
.N AND PURIFICATICN SYSTEM -
im L ,, J Becord of A,W and Canges Prepared By Jadachew, Nissen 6/17/75 Date S'.dInitted BY I e r Stalter 7/22/75 Sec~1cn Head Date .' ~~ pr. z ....;-c'.=a BY Jack Evans 7/22/75 SE Chaim Date QA 3W N/A Quality Assurance Direc cr Date AW:cVed BY Jack Evans 7/22/75 Plant Manager Date Pensiat SP3 QA Plant Manager No. hus:=-daticn Date Approved Date Agrcr/al Eate 20 CEC 121964 N/A A O-- g sz.fuj8+-
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1 SP 1104.02.11 , s l 1. PURPOSE 1.1 To provide procedures for operating the Makeup and Purification System in each of the following modes: . Mode Section Startup 4.0 Normal Operation 5.0 Shutdown of Makeup System 6.0 Infrequent Operations 7.0 The normal functions of the Makeup and Purification System are: 3 1. To control the Reactor Coolant System inventory during all ! phases of normal reactor opeartion.
- 2. To receive, purify, and recirculate reactor coolant water.
- 3. To maintain the required boron concentration of the reactor j coolant system. .
I 4. To add lithium hydroxide to the reactor coolant system for pH control.
,_ 5. To add hydrogen and hydrazine to the reactor coolant system for oxygen control.
{_
- 6. To degas the reactor coolant system.
- 7. To provide injection water for the seals of the reactor coolant pumps.
I
- 8. And to add borated water to the core flooding tanks.
The makeup and purification system is operated during all phases of the-nuclear steam supply systems (NSSS) operation, including startup, power operation, and shutdown. The system may also be operated during refueling by employing the purification equipment through interconnections to the decay heat removal system. During normal NSSS operation, one makeap pump continuously supplies high pressure water from the makeup tank to the seals of the reactor coolant pumps, and to a makeup line which is connected to the reactor inlet thru a high pressure injection line. This line is the only interconnection between the makeup , system and the high pressure injection system. Makeup flow to the reactor coolant system is cegulated by the makeup control valve (NU 32), which operates on signals from the liquid level controller of the reactor coolant system pressurizer. 4 m T y w-- - F
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- A control valve (MU 19) in the RC pump seal injection line
- l automatically maintains the desired flow rate to the seals.
', Needle valves in the individual seal injection lines are used to 1 manually throttle flow to the seals of each pump. A part of the water supplied to the seals leaks into the reactor coolant - system. The remainder returns to the makeup tank after passing i through one of the two seal return coolers. The se' con'd seal 11 return cooler is placed in service when running a makeup pump on_ recire flow only, to maintain the makeup tank temperature less than 140*F. Seal water inleakage to the reactor coolant system requires a continuous letdown of reactor coolant to maintain the desired coolant inventory. In addition, letdown of reactor coolant is required for removal of inpurities and boric acid from the reactor coolant and to accommodate volume changes in the reactor coolant system during changes in power level.. Reactor coolant is removed from one of the reactor inlet lines, cooled during
- passage through one of the letdown coolers, passed from the containment vessel through a containment isolation valve, reduced in pressure during flow through the letdown flow control .
station, passed through the purification desineralizer prefilter, and then passed through a purification desineralizer. Normally the letdown flow is routed through one of two mixed bed Purifica-1 tion Demineralizers 1-1 or 1-2 to maintain good chemistry (low l chlorides and fluorides) and to remove radiciodines to keep the s dose equivalent iodine low. The mixed bed purification desin- a eralizer will also remove radiocesium and other gross activity. The " operational" mixed bed Purification Demineralizer will be Li7 saturated and the " Spare" mixed bed Purification Demineralizer will be normally unsaturated with Li7 . The Purification De-i mineralizer 1-3 can be used for additional radiocesium, gross activity and Li7 removal when needed as indicated by C&HP. A
, three-way valve (MU 11) directs the coolant either through the i purification makeup filter to the makeup tank or to the clean 3
radioactive waste disposal system. The normal letdown flow rate
- is 45 gps. This permits recirculation of one reactor coolant
! system volume through the purification train during a 24 hour period. The maximum letdown flow rate allowed at full reactor pressure is 140 gym. This flow rate permits changing boron concentration by bleeding coolant from the reactor coolant l system during xenon peaking following a 50 percent power change.
During this period, non-borated reactor grade water is added to 1 the reactor coolant system to dilute the boric acid concentration in the reactor coolant system. This is done to compensate for e; the negative reactivity addition resulting from the xenon-
! peaking.
1 Normally, the three-way valve Mull, when in the open position,
- directs flow to the Makeup Tank. If the boric acid concentration
.in the reactor coolant is to be changed, the feed and bleed J
s 3 SP 1104.02.5 permissive indicating light, IL-Mull must be illuminated. This
- light is interlocked to the Integrated Control System which i gives the permission for boron. changes by illuminating the light i IL-Mull. If the boric acid concentration in the reactor coolant
{ is to be reduced, the three-way valve is placed in the closed -- { position to direct.the letdown flow to the clean radioactive , waste disposal system. Boric acid removal is accomplished in j the clean radioactive waste disposal system either by directing
; the letdown flow through a deborating desineralizer or BA evap i with the effluent returned to the makeup tank, or by directing the letdown flow to a clean waste receiver tank. The level in I
the makeup tank is maintained with deborated water from primary , water storage tank or with desineralized water from the station demineralized water storage tank. The flow of desineralized water is measured and totaled by an inline flow integrator and 3 associated instrumentattan. The flow of'desineralized water to
- the makeup tank is controlled remotely by the makeup tank feed
. flow valve. During normal operation the flow integrator (batch I
controller), the integrated control system interlock, or the i operator will terminate dilution. The above procedure for , reducing the reactor coolant system boric acid concentration is - the feed and bleed method. i
, The makeup tank also receives chemicals for addition to the i reactor coolant. Chemicals in solution'are injected into the s letdown flow upstream of the makeup filters and then passed into
- (i,,. the makeup tank which serves as a final mixing location. A 5 hydrogen overpressure is maintained in the tank to ensure that the required amount of dissolved hydrogen remains in the reactor coolant.
i System control is accomplished remotely from the control room
- with the exception of the seal return coolers, and the cation 1 desineralizer 1-3. The letdown flow rate is established by the block orifice (RO-MUS) during normal opeartion, but may be increased by opening the letdown control valve (MU 6). The operational and' spare purification demineralizer 1-1 and 1-2 can be placed in service by remote positioning of the demineralizer j isolation valves. The cation demineralizer 1-3 can be placed in j' service by remote positioning of the isolation valve. However, to place the cation desineralizer 1-3 in series with one of the purification desineralizers 1-1 or 1-2 requires using manual i
valves. Diverting the letdown flow to the clean radioactive
- waste treatment system is accomplished by remote positioning of 1~ the'three-way valve and the valves in the clean radioactive waste disposal system. This should always be done flowing j through the " Spare Purification Domineralizer" to recover the a contained Li7 . The control valve in the injection line to the
, reactor coolant pump seals is automatically set by a' flow con-trolle'r to maintain the desired total flow rate to the seals.
~
I e i e
4 SP 1104.02.19 s Coolant at the refueling boron concentration is supplied to the ! reactor coolant system for preoperational fill by using the boric acid pumps and the clean waste receiver transfer pumps or . the demineralized water supply pumps. The fill line bypasses the makeup tank and makeup pumps and connects into the RC System through the normal makeup control valve (HU 32). When the fill operation is completed, the auxiliary fill line is secured; makeup and inventory control is then continued by operation of a makeup pump. Makeup and purification valves MU3, MU33, MU38 and MU66A through D have auxiliary air supplies in the form of air volume tanks. These tanks come into effect in the event of a' loss of station air. Upon a loss of instrument air, a check valve in the control air supply line isolates the air volume tank from the supply line. The air volume tank contains enough air at high enough pressure to stroke the valve closed and maintain it closed. Should instrument air be lost, and the in line check valve leak, automatic actions take place to protect against uncontrolled letdown. The air volume tank has a P3L which is initiated at tank pressure of 85 PSIG at which time a computer . trouble alarm Q839 is typed out (The PSL resets at 93 PSIG). Should the air volume tank pressure drop to 75 PSIG the respective valve is then signaled to closed by the PSLL through an interlock. The makeup and purification system provides makeup to the s reactor coolant system to replenish inventory lost due to a ., $ small rupture in the reactor coolant system pressure boundary. - The makeup control valve senses a decrease in pressurizer level and positions itself to maintain level. A high flow alarm may be associated with the increase in additional makeup, and following this alarm will be a low makeup tank level alarm. During this condition, the water supply to the suction of the makeup pumps should be transferred to the BWST by using the three-way valve (MU 3971 in the closed position). If the makeup tank level drops to 10 inches, a signal will automatically position the three-way valve MU 3971 to provide suction from the BWST. If MU 3971 does not transfer on low makeup tank level of ten inches, a 45 second time delay will automatically trip the makeup pumps (The time delay starts with the signal to position MU 3971 to provide suctiou from the BWST at ten inches in the MU Tank.) At 86 inches (increasing) in the makeup tank, the makeup pump suction autcmatically transfers from the BWST to the makeup tank. 19 C The makeup tank has two redundant compensated level indicators. One is powered from NNI-X (LIMU16-1) and the other is powered from NNI-Y (LIMU16-2). Both level indicators are located next to each other on the same front console of the control room. The makeup and purification system also has a tap to the radiation
.. . ,. . . . . . ~ - - . .~.. - .. .. . - . - - . . . - - - _ - . _ . . . - ._ -
E. . i , 4 5 SP 1104.02.13 ! ~h !~ ,. monitoring system (RI 1998). This is used to monitor the , reactor coolant for fission products due to failed fuel during j- operation. ! The makeup system also has a boron analyzer which monitors .. ! ! the boron concentration in the reactor coolant system., The " boron concentration is recorded on AR 1999 located on control room panel C5703. The recorder has four ranges shown by IL 199A through D. The ranges are noted by the following: INDICATING LIGHT RANGE + - IL 1999A 0-550 ppe Boron j IL 19998 500-1050 paa Boron. i IL 1999C 1000-1550 ppe Boron ! IL 1999D 1500-2050 ppe Baron ? The Makeup and Purification System serves no emergency function. { The following information is taken from nameplate data: " i i - - Makeup Pump Motor. ' j Manufacturer: Westinghouse Type LAC Inductor Motor Model HSDP i . ,e Frame 5010 - S j ', g Insulation Class B f . Horsepower 450 Volts 4000 , l Amps (full load) 57 i RPM 1776
.W eight 3420 lbs.
{ J Makeup Pump Manufacturer Bingham i Size 2 x 3 x 7 1/2 i Type 12 stage centrifugal
- RPM .
5400 Capacity 150 GPM . Desian Conditions l Pressure 3050 psig Temperature 200*F
-Flow 60 GPM NPSH at Design Flow i5 feet
- Total Developed Head 3800 feet-j CAUTION
- Minimum recireviation lines must be open during normal pump operation.
i ' Normal Operatina Conditions 1 Pressure (Suction) 0-100 psig i s I l
4 6 SP 1104.02.1 m (Discharge) 2510 psig Temperature (Suction) 120*F Flow 60-150 GPM Radial Bearing Temperature 150*F Gear Bearing Temperature (Pump End) 130'F - (Pump Center) 130*F , (Motor Center) 130'F (Motor End) 130*F Thrust Bearing Temperature 140*F Makeup Pump Speed Increaser (Gear Box) Manufacturer Westinghouse Ident. No. PO 35880-2 Figure No. RH-SU 1023-6 Cat. No. 6831D66G01 Ratio 3.029 Service HP 450 Input RPM 1778 Seal Return Coolers Design Conditions Pressure Tube /Shell 150/150 psig Temperature Tube /Shell 200/250*F Flow Tube /Shell 42/40 GPM Heat Transferred 0.5 Mbtu/hr '..
- a)
Normal Operating Conditions Pressure Tube /Shell 50/100 psis Inlet Temperature Tube /Shell 140/95'F Outlet Temperature Tube /Shell 120/115'F
, Flow Tube /Shell 4.0/40 GPM Makeup Tank Design Conditions Pressure 100 psig Temperature 200'F Volume (Total) 4301 gallons (Usable) 3086 gallons Volume per inch of level 30.9 gallons Distance between level taps 100 inches 1' Normal Operating Conditions Pressure 15-35 psig Hydrogen Partial Pressure 0-21.8 psig Temperature _125'F Water Volume 2992 gallons Level 73 inches
7 SP 1104.02.1
'N RCP Seal Injection Filters Desian Conditions Pressure 3050 psig Temperature 200*F -.
Flow 50 GPM , Pressure Drop at Design Flow 6.5 psig Normal Operatina Conditions Pressure 2500 psig Temperature 130*F Flow 32 GPM - Differential Pressure 3.4 psig Purification Desineralizer Design Conditions Pressure 150 psig Temperature 200*F Volume when full (Resin) 50 cu. ft. (Water) 65 cu. ft. . Flow 70 GPM Normal Operating Conditions Pressure 25 psig (7' (ii, Temperature Pressure drop 120*F 8 psig Flow 45 GPM Letdown Coolers
- Design Conditions Pressure Tube /Shell 2500/200 psig Tempeature Tube /Shell 600/350*F Flow Tube /Shell 70/400 GPM Heat Transferred 16.19 abtu/hr d
Normal Operation Corditions Pressure Tube /Shell 2200/100 psig Inlet Temperature Tube /Shell 557/95'F Outlet Temperature Tube /Shell 120/176*F Flow Tube /Shell 45/400 GPM Purification Demin Filter and Makeup Filter Design Conditions Pressure 150 psig Temperature 200*F flow 140 GPM Maximum Differential Pressure 75 psig W 'n
_.. ._ _ _ _ _ _ .. Z . ._rc M _. - L_ _ ^ . ~__.._.:._ _
~ ~'
- s . .
8 SP 1104.02.20 m Normal Operatina Conditions ', Pressure 150 psig Temperature 120*F Flow 45 GPM Nominal Rating, Microns 1 - i Clean Pressure Drop at Rated , Flow (140 GPM) 5 paid
- 2. PRECAUTIONS AND LIMITATIONS 2.1 The following limits and precautions are taken from "NSS Limits and Precautions", PP 1101.01.
I Makeup and Purification System 2.1.1 Maximum allowable letdown flowrate is 140 gpa. 2.1.2 A flow path to the makeup tank or to the waste disposal system must be provided before opening the letdown valve. 2.1.3 When pumping boric acid refer to the solubility Attachment 8 curve for minimum allowable solution temperature. 2.1.4 Before initiating flow on either side of heat exchangers , or coolers in this system: The cooler, all connecting -)
~
piping and components shall be filled and vented by reduced flow rates (preferably gravity flow). Also, establish component cooling water flows before primary water flows. NOTE: This precaution is necessary to prevent
- impact or water hammer forces on tubes and baffles.
i 20 1. Both letdown coolers are in service in parallel for normal as well as maximum letdown conditions. This will reduce the number as well as the !. severity of thermal transients encountered when placing a standby cooler in service.
- 2. To place a standby cooler in operation, the reactor coolant letdown should be admitted slowly
- 20 by stopping letdown, cut in cooler (open NUIA or IB) and slowly increasing letdown to desired
! value to minimize the thermal transients. 2.1.6 Cooling water flow through each letdown cooler is limited to a maximum of 400 GPM with a maximum transient limit of 500 GPM. l
ea, 9 SP 1104.02.13
's
, 2.1.7 Maximum RCP seal return flow through each seal return cooler is 42 GPM, or 3.3 psid.
NOTE: To improve RCP seal performance it is desired to raise the seal injection temperature. -- For this reason normally only one seal return cooler will be in service. If running a MU pump on recirc flow only, the second seal return cooler should be placed in service to maintain MU tank temperature less than 140'F. Running two MU pumps with only one seal return cooler in service for short periods of time is allowed (approxiantely { 1/2 hour). Normally, the 42 GPM flow limit will be exceeded only during shifting MU pumps and when two MU pumps are on during recovery from a reactor trip. 2.1.8 Cooling water flow to each seal return cooler is ILuited to a maximum of 40 GPM, or 14.5 psid. 2.1.9 Maximum allowable differential pressure across the RCP seal injection filters is 75 psid and the filter should be replaced at this time. , r' r 2.1.10 Maximum allowable flow per RCP seal injection filter i when clean is 50 gym. 2.1.11 Maximum allowable flow rate through each purification demineralizer is 70 GPM. 2.1.12 Minimum allowable flow rate through each purification demineralizer in service is 25 GPM. 2.1.13 Maximum allowable temperature in the makeup tank and in the letdown header upstream of the purifi-cation demienralizer is 135*F unless the demineralizers are bypassed. 2.1.14 Maintain the makeup tank hydrogen partial pressure between 0 and 21.8 psig. Refer to Section 2.3.3 of B&W Chemistry Manual 1385. Maximum tank 13 pressure is 100 psig. Normal operating pressure i should be maintained between 15-40 psig. 2.1.15 Minimum allowable makeup tank water level is 18" when the reactor is critical (10" level in the makeup tank transfers makeup pump suction from the makeup I tank to the BWST). i- - -
. _ . . . _ _ _ _ . _ . _ _ _ _ _ _ . _ __ _. ;_J. . _ :n _ ; . ZZ.___ . _ __z _ _ _ . . . _ . . . .
10 SP 1104.02.13
^
13 CAUTION: If MU 3971 does not automatically transfer #
)
on low makeup tank level, a 45 second time delay will automatically trip the makeup pumps. 2.1.16 Maximum allowable makeup tank water level is 100" (at 86" in the makeup tank, the makeup pump s'uction automatically transfers from the BWST to the makeup tank.)
- 2.1.17 The reactor coolant pump controlled bleedoff valves MU 59A through D should be opened after seal injection flow is established.
2.1.18 Prior to any rod withdrawal or boric acid dilution, the source range nuclear instrumentation should indicate at least 2 CPS. 2.1.19 The nuclear instrumentation will be continuously monitored during any reactivity changes. 2.1.20 All subcritical soluble boron changes in the reactor coolant system will be verified for each predicted change of 30 PPM. Makeup Pump and Motor . L 2.1.21 Maximum allowable pump radial bearing oil tempera-ture is 180*F. See computer points (CPT) T743, T744, T761, and T765. 2.1.22 Maximum allowable per gear bearing metal temperature is 175'F for:
- 1. Pump End - CPT T740, T758
- 2. Pump Center - T739, T757
- 3. Motor End - T737, T755
- 4. Motor Center - T738, T756
[ 2.1.23 Maximum allowable pump thrust bearing metal temperature is 170*F. See CPT T748 and T766. 2.1.24 Minimum allowable makeup tank pressure to satisfy pump NPSR requirements is 15 psig during normal operation,-and 5 psig during desasing of makeup tank. See Attachment 6 for minimum allowable MU tank pressure vs. flow. 2.1.25 Maximum allowable temperature at suction nozzle is 120*F when RCP seal injection is being supplied.
. + ~ . * - .
11 SP 1104.02.11 s
.' 2.1.26 (THE RECIRCULATION FLOWPATH FOR EACH MU PUMP SHOULD BE OPEN AT ALL TIMES.)
2.1.27 The MU pump auxiliary oil pumps should be exercised once per week by running each for two minutes to . . maintain lubrication film. (TS 2.1.28 Each MU pump should be run at least once per 4.1.2.3) month to ensure operability. 11 2.1.29 Operation of the makeup pumps on orifice bypass alone for longer than 15 minutes is not recommended but as long as the minimum flow is maintained, no pump damage will occur. For recirculating the MU tank for core flood tank-fill, operation on recire flow only is allowed. MU tank temperature is not to exceed 140'F and two seal return coolers should be in service. 2.1.30 Rated runout capacity of MU Pump is 350 GPM. 2.1.31 Maximum allowable makeup pump motor bearing oil ^ tempearture is 180*F. See CPT T747, T762, T745, and T763. 2.1.32 Maximum allowable makeup pump motor stator temperature ys is 266*F. See CPT T746 and T764. ( ' 2.1.33 Minimum makeup pump motor starting voltage is 80 percent of rated voltage. 2.1.34 Maximum allowable makeup pump motor voltage variation is 10 percent of rated voltage. 2.1.35 Maximum allowable makeup pump motor frequency variation is 5 percent. l 2.1.36 Maximum makeup pump motor time for locked rotor without damage at 100 percent voltage is 12 seconds. NOTE: A locked rotor is indicated by a lack of decline in starting current. 2.1.37 Number of allowed successive starts with motor initially at ambient temperature is two starts. Number of allowed successive starts with motor initially at rated temperature is one start. NOTE: An interval of five minutes with motor running or five minutes with motor not running must elapse before an additional start. 4
^ -~ --
t 12 SP 1104.02.14 3 2.1.38- Seal injection water flow is required to all reactor ~
l coolant pumps when reactor coolant temperature is above 150*F, except when operating in the loss of injection mode.
14 2.1.39 The makeup pump 1-1 (1-2) lube oil pressure switches are powered from DC control power to breakers AC105 (AD105). If DC control power is lost to the breaker, the makeup pump will trip on low lube oil pressure. 2.2 Do not start or continue to run a makeup pump with the reactor coolant system in a solid water condition. 2.3 Prior to positioning the three-way valve MU 11 to the bleed position, ensure that the downstream manual valves in the waste disposal system are open as directed by the Shift Supervisor. i 2.4 Fill water quality must meet requirements of'opeartional chemical control limits, PP 1101.04, Table 4.3. 2.5 A Radiation Exposure Permit (REP) shall be required for work , within Radiation Access Control Area (RACA) and work involving water which contains radioactivity. 2.6 Whenever one or more Reactor Coolant Pumps are operating, the Component Cooling Water Pump providing the RCP cooling water and .s
~
the Makeup Pump providing the RCP seal injection must be aligned 4
/
to opposite essential busses. However, it is permissible to - perfona ST 5011.03 on the Makeup Pump aligned to the same bus as the operating CCWpump, but the opposite makeup pump MUST be i placed back in service as soon as possible after completion of the test. (TS 2.7 The RCS flow rate through the core shall be >2800 GPM whenever I 3.1.1.2) a reduction is being made in the boron concentration of the RCS. (All modes) (TS 2.8 As a minimum, one of the following boron injection flow paths 3.1.2.1) and one associated heat tracing circuit shall be OPERABLE. (Modes 5 and 6) 4 a. A flow path from the boric acid storage system via a boric acid pump to a makeup pump to the RCS if only the boric acid storage system in Specification 3.1.2.8a is OPERABLE, or
- b. The flow path from the BWST via a makeup pump to the RCS if only the-BWST in Specification 3.1.2.8b is OPERABLE.
L (TS 2.9 Each of the following boron injection flow paths and at 3.1.2.2) least one associated heat tracing circuit shall be OPERABLE.
., .-n -
t 13 SP 1104.02.20
.s
- a. The flow path from the boric acid storage system via both boric acid pumps and one makeup pump to the RCS, and
- b. The flow path from the BWST via another makeup pamp to the RCS.
(TS 2.10 As a minimum, one makeup pump shall be OPERABLE and cap'able 3.1.2.3) of being powered from an OPERABLE essential bus. (Mode 5*) (TS 2.11 At least two makeup pumps shall be OPERABLE. (Modes 1, 2, 3.1.2.4) 3, and 4*)
*With RCS pressure >150 psig.
2.12 Should the makeup pumps or any portion of the system be removed from service for maintenance such that the boric acid injection flowpath from the boric acid addition system or BWST is unavailable, refer to the boron concentration control system procedure, SP 1103.04, for an alternate flowpath. 2.13 Flow through the letdown flow control valve NU6 should be , , maintained at >10 GPM. Flows of <10 GPM will result in a reduction of the life of the valve. 2.14 If an SFAS signal to some ESF equipment is " Blocked" (ie. overridden), that equipment is incapable of responding to either 1- any subsequent automatic actuation signal or the SFAS system-level manual actuate (" Trip") pushbutton on panel C5717. Before an operator " Blocks" any SFAS signal, he must assure that the safety function of that equipment is no longer needed. Afterward the operator is totally responsible for the proper operation of that equipment, including actuation if required, until the
" Block" is removed.
Reactuation, subsequent to a " Block", can be accomplished two 4 ways. First, at the equipment level, " Blocked" equipment will respond to the individual control switches for that piece of equipment. Second, at the SFAS system level, operation of the system-level " reset" pushbutton on panel C5717 will clear any output logic blocks in the system (output logic " Blocks" are the block switches next to the SAM light and on the output modules). The equipment will then respond to the system-level manual actuate (" Trip") pushbutton and to automatic actuation signals. For guidance on resetting the SFAS af ter a real or erroneous 20 trip, see Section 4. of EP 1202.01, "RPS, SFAS, Trip or SG Tube Rupture". 2.15 If an operator blocks an SFAS signal and changes the status of the actuated equipment, he is responsible for assuring proper equipment operation and reinitiation if required until the SFAS is reset. For guidance on resetting the SFAS af ter a real or v
_ _ _ _ _ . _ . _ . _ _ _ _ _ . _ . _ . . _ _ _ m .. ~ ..._. . . _ . _ _ . . . _ . . . - - _ . . . -- . .- l 14 SP 1104.02.20 m 20 erroneous trip, see Section 4.0 of EP 1202.01, "RPS, SFAS, SFRCS ~j Trip or SG Tube Rupture". 2.16 The conditions which must be satisfied before the operator may change the status of SFAS actuated equipment (Makeup and . Purification System) are as follows: ,
- 1) RCS makeup - the RCS makeup isolation valve may be overridden
. to the open position when RCS pressure is greater than 400 psig.
- 2) Reactor Coolant Pump (RCP) Seal Injection and Return - The RCP Seal Injection and Return Isolation valves may be overridden to the open position when RCS pressure is i
greater than 400 psig. i
- 3) RCS Letdown - The Letdown isolation valve may be opened as required to control RCS inventory when the RCS pressure is greater than 400 psig, given that no seismic event occurred.
, 4) CCW to Makeup Pump - The CCW to Makeup Pump valve may - be overridden to the open position when RCS pressure is greater than 400 psig, given that no seismic event occurred.
- 5) If plant conditions are stable at normal operating or hot standby conditions after a transient with no e'ridence g of an RCS leak, other systems may be overridden with the .t.+
Shift Supervisor's permission.
- 6) If there are any questionable conditions or any sign of an RCS leak, no safety systems will be bypassed without-20l approval of Station Management (Plant Manager of his designee).
2.17 Radioactive System Filter Changes 2.17.1 Isolate, drain and vent system filters only when Maintenance is prepared to perform the filter change. , 2.17.2 Draining, venting and opening filter housings are all potential causes of radioactive gaseous reledbes. Exercise caution during these operations and be prepared to take appropriate . action if a release does occur. 2.17.3 When venting filters for returning them to service, vent the minimum amount necessary to ensure the filter housing is completely filled and vented. 2.17.4 As soon as Maintenance completes the change of a 4 filter, it should be refilled, vented and placed in standby per the appropriate section of this procedure. l
15 SP 1104.02.20 N
,' 3. REFERENCES-(TS) 3.1 Technical Specifications, Section 3.1.1.2, 3.1.2.1, 3.1.2.2, 3.1.2.3, and 3.1.2.4 3.2 NSSS Limits and Precautions, PP 1101.01, Makeup and Purification System 3.3 NSSS Setpoints, PP 1101.02, Makeup and Purification System 3.4 Hydrogen Addition and Degasification, SP 1102.12 3.5 Boron Concentration Control, SP 1103.04 3.6 DH Removal System Operating Procedure, SP 1104.04 i 3.7 Chemical Addition System Operating Procedure, SP 1104.03 3.8 Component Cooling Water System Operating Procedure, SP 1104.12 3.9 Clean Liquid Radwaste System Operating Procedure, SP 1104.29 ,
3.10 Nitrogen Purge and Blanket System Operating Procedure, SP 1104.26 3.11 Gaseous Radwaste Disposal System Operating Procedure, SP 1104.27 3.12 Vibration and Loose Parts Monitor System Procedure, SP 1105.18 3.13 Nuclear Filter Cartridge Replacement and Removal, MP 1402.04 3.14 Operational Chemical Control LLeits, Plant Procedure PP 1101.04, Sec. 12 20 3.15 Davis-Besse Unit 1 USAR, Section 9.3.4 3.16 Makeup and Purification System Piping and Instrument Diagram M-031 3.17 ICS/NNI Instruction Manual (Bailey) 3.18 Vendor Technical !!anuals: 2 3.18.1 Pall Trinity (Makeup Filters and Prefilters) f 3.18.2 Pall Trinity (Reactor Coolant Pump Seal Injection Filters) 3.19 fonics Inc. , Demineralizer Instruction Manual #4546 l l l 3.20 Byron-Jackson Instruction Manuals on RC Pumps i 'I I
- . ~ , . - , - . _ _ _ . _ _ _ _ _
- ^
16 SP 1104.02.20
-s 8
3.21 Makeup Pump Aux Connection and Instrumentation, B&W Dwg. 173919E, File No. 2765 20 3.22 EP 1202.01, "RPS, SFAS, SFRCS Trip or SG Tube Rupture".
- 4. STARTUP PROCEDURE .
This section of the procedure is used to establish makeup flow and seal injection. The portions of this section concerned with initiation of seal injection apply also during recovery from loss of injection. 4.1 Prerequisites 4.1.1 Reactor coolant system pressurizer level instrumenta-tion is operable and is providing control signals to the makeup system. 4.1.2 Clean Liquid Radwaste System is operable as per procedure, SP 1104.29. 4.1.3 Component cooling water flow has been established . in the header supplying the makeup pumps and lube oil coolers, letdown coolers, and seal return coolers in accordance with the Component Cooling Water Operating Procedure, SP 1104.12. 4.1.4 Makeup tank pressure is being maintained between ' i 15 and 40 psig as per Hydrogen addition and Degasification Procedure, SP 1102.12. 4.1.5 Verify power is available to makeup and purification 20l components, see Attachment 1. 4.1.6 Makeup and Purification System is filled and vented and the makeup tank level is between 60-80 inches. Use level recorder LR-MU16. 4.2 Procedure 4.2.1 Verify system lineup in accordance with the makeup and purification system normal valve lineup, Valve Verification List A, with the following exceptions: 't
- 1. RC Letdown Block Orifice Is 4Ltion, MU 4, Closed.
- 2. RCP Seal Return Isolation Valve, MU 38, Closed.
- 3. Seal Injection Flow Control Valve, MU 19, in Manual Mode and Closed.
- 4. Normal Makeup Control Valve, MU 32, Closed.
17 SP 1104.02.13
- 5. RC Letdown Cooler 1-2 Inlet Isolation, MU IB, Open; and RC Letdown Cooler 1-1 Inlet Isolation MUIA open.
NOTE: RC Letdown Cooler Inlet Isolation Valves IA and IB are interlocked to the RC Letdown - Cooler CCW Inlet Motor Operated Valves
~
CC1409 and CC1410 such that when MU1A and MU1B are opened, the respective Component Cooling Water valve opens automatically. 4.2.2 Perform Makeup Pump Startup Checklist, Attachment 2 of this procedure for both makeup pumps. 13 1. Makeup Pump 1-1 complete.
- 2. Makeup Pump 1-2 complete.
i 4.2.3 Verify Component cooling water flows to the following components:
- 1. Makeup pumps gear lube oil and pump lube oil coolers "
i 1-1 (1-2) flow rate of 12 GPM per pump as read on local flow indicators FI 2190 (FI 2191).
- 2. Seal return coolers 1-1 (1-2) flow rate of 25 GPM per cooler as read on local flow indicators FI 2638 (FI 2642).
- 3. Letdown coolers flow rate of 400 GPM per letdown cooler as read on local flow indicator FI 1405 located on CCW return line.
NOTE: If FI 1405 is already indicating a flow rate, an increase of 400 GPM per letdown cooler should be established on this indicator. NOTE: Component Cooling Water Inlet Valves to letdown coolers will open on a signal from HIS MUIA (HIS MU1B), inlet to letdown coolers, before letdown is established to coolers. 4.2.4 Establish communications between control room and makeup pump room. CAUTION: IT IS ABSOLUTELY MANDATORY THAT THE RECIRC LINES ARE OPEN ON THE MU PUMPS. 4.2.5 Start makeup pump 1-1 (1-2 as follows:
~. L :.
_. . - --.L _7.L - ..L. . - . . . L* :::? ^ L. . : ' = ... ; - ~ :- - 1 . . f 18 SP 1104.02.14 7
- 1. Start Makeup' Pump 1-1 (1-2) Main Oil Pump 1-1-1 ,
(1-2-1) using switch HIS-MU24A1 (HIS-MU24B1) on left ! console, panel C5704 from the control room or locally , with switch NP 371B (NP3728). NOTE: Wen Main Oil Pump 1-1-1 (1-2-1) is started, the DC Aux. Oil Pump 1-1-2 (1-2-2), providing the DC Aux. Oil Pump Switch, NP371C (NP372C) is not in " LOCK OUT", and Aux. Gear Oil Pump I will also start automatically. Red indicating 4 lights on each start switch for each respective pump will light to indicate pump running. 4 When starting or switching sakeup pump,
- j except for emergency start, station someone at the DC Aux. Oil Pump to verify that it starts after the Main. Oil Pump is started.
If the Aux. Gear Oil Pump or DC Aux. Oil Pump did not start automatically, dispatch an operator to inspect the pump for damage -- or abnormal conditions. The Aux. Gear Oil Pump may be started manually by using switch [ HIS-24A3 (HIS-24B3) on left console, panel } C5704 from the control room or locally l using switch NP371B (NP372D), after the pump c.g has been checked for proper operation. .
)
I NOTE: Makeup Pump will trip when lube oil systes '! pressure indicator decreases to 3 PSIG. The ' 14 lube oil pressure switches are powered from the DC control power to breaker. AC105 (NU
. pump 1-1) & AD105 (MU pump 1-2). When Main f oil Pump 1-1-1 (1-2-1) oil pressure reaches
- 15 psis as read locally on PI-MU 106A (PI-MU i 106B), the DC Aux. Oil Pump 1-1-2 (1-2-2)
! will automatically trip off and remain off l unless oil pump pressure decreases to 5 psig j at which time the DC Aux. Oil Pump will
- automatically start again. The DC Aux. Oil i Pump can then only be stopped locally using switch NP 371C (NP372C). When DC Aux. Oil '
I Pump 1-1-2 (1-2-2) automatically stops, place switches HIS-HU24A (HIS-MU2482) on left console, panel C5704 in control room in ,{ auto. This will place DC Aux. Oil Pump in j standby.
! When the MU pump is started and 12 psig oil pressure is reached on local PI-MU109A i (PI-MU1098), a timer is started which, after
,i
- -,,,,ng,, --. -- -r,-w-,..m -,.,--~------+.-a - - , . - - . . , , . - ~ ,-,,,---n.-- ---,r----,,---,--,r... ,--.m, g n,.- - , , , - -
t 19 SP 1104.02.14 i 4 or 5 minutes, will automatically stop the , Aux. Gear Oil Pump. Gear Oil pressure is i then maintained by the gear increaser shaft
, driven pump. . CAUTION: Do NOT attempt to manual,1y stop 1 , the Aux. Gear Oil Pump until at least 5 minutes after the NU l Pump is started, or the Aux. Gear ! Oil Pump logic will be confused i and the Aux. Gear Oil Pump will neither be automatically stopped j nor be able to be manually stopped.
5 If for some reason, oil pressure drops to 5 3 psig the Aux. Gear Oil Pump will automatically i start again. Aux. Gear Oil Pump can only be
- stopped if Makeup Pump is tripped or both
] Main and DC Aux. Oil Pumps are tripped. { 2. Have an operator check pump bearing site flow glasses , i that oil is flowing and normal oil pressure of >8 psig
! on the pump oil system indicator and between 3 and 10 j psig on the speed increaser oil system indicator to ensure proper lubrication.
s
- 3. Start makeup pump 1-1 (1-2) using switch HIS-NU24A
! (HIS-NU248) on left console, panel C5704 from the control room or locally with switch NP 371A (NP 372A).
; NOTE: Operator should complete Step 13 of Attachment 2 for starting of the makeup pump for proper operation.
- 4. Ensure Aux. Gear Oil Pump 1-1 (1-2) has stopped after MU pump 1-1 (1-2) is started. '
~ NOTE: Second makeup pump is in standby and ready i for operation. r 4.2.6 Have an operator adjust makeup flow control valve bypass flow needle valve NU 58A to 3 GPM flow as read on FI NU58 locally, if RCS pressure is less : than 50 psig. This will result in a minimum bypass flow of approximately 1 GPM at normal operation RCS pressure to prevent thermal shocking of the makeup piping to RCS, in the event normal makeup valve MU 32 ,
, :is closed for a period of time.
4.2.7 Establish Seal Injection to RCP pumps: N d f e* 1 i
__. __ v _ .. _ - ._ __ _ .. 20 SP 1104.02.8 s
- 1. Slowly increase seal injection flow by opening MU 19, Seal Injection Flow Control Valve in hand until a total seal injection flow indicates -12 GPM as read on FI MU 19 on control panel C5704. Adjust MU 19 H/A station setpoint knob to 32 GPM and place MU 19 H/A ..
station in auto. ,
- 2. Adjust the seal injection flow to each RCP as follows:
- a. Ensure pressure gauges are installed at PDT MU67 (downstream or low pressure side of PDT) and FT MU30B (upstress side of FT).
NOTE: These should be 3000 psi gauges with 10 psi increments and they should be calibration checked prior to use. i b. Ensure NU 19 H/A station is in auto and set for 32-36 GPM.
- c. Ensure MU 32 is closed and/or isolated such .
that no makeup flow is present. NOTE: FIMU58 is to be adjusted per Step 4.2.6 above.
- d. Set MU 231, 230, 232, and 233 as per Attachment ""j
, #7. .
- 3. Caution, RCS pressure must be >150 psig before establish-ing controlled bleedoff flow, open NU59A, NU598, MU59C and NU59D RCP seal return isoaltion valves. Open MU38, RCP Seal Return Isolation Stop Valve, to establish controlled bleedoff flow from the RCP seals from 8 Control Room on Panel C5717 (SEAS), using switch HIS-MU38. Flow may be read from computer points F835 for RCP 1-2-1, F855 for RCP 1-2-2, F795 for RCP 1-1-1 and F815 for RCP 1-1-2.
NOTE: Now that a flow has been established on the makeup pumps 1-1 (1-2), refer to Vibration and Loose Parts (V&LP) System Procedure, SP 1105.18, to compare the current makeup pump operation with its associated baseline power spectral density (PSD) signature and operating i limits. 4.2.8 Place pressurizer level controller LIC RC-14 H/A station in auto with its setpoint at 75". This will
- a 21 SP 1104.02.8 '5 place normal makeup flow control valve MU 32 in se rvice.
4.2.9 Open MU 4, RC Letdown Block Orifice Isolation Valve, with switch HIS-MU4 from the control room on panel . C5703, lef t console, and observe letdown flow on FI MU7 on panel C5703, left console, in the control room. 4.2.10 Adjust letdown flow to equal seal inleakage plus MU flow control valve bypass flow plus 10 GPM using HC-MU6 block orifice bypass valve if necessary, which can be opened from control room on panel C5703. Using nominal values mentioned above, this will be about 41 GPM, with a constant pressurizer level of 75". 1 GPM Example: 4 RCP (8 GPM Seal Injection - RCP controlled bleedoff) + 3 GPM MU valve bypass + 10 GPM = 41 GPM NOTE: This will assist in maintaining a uniform
^
outflow fram the pressurizer to the RCS piping during heatup to minimize thermal cycles in the pressurizer surge line. The makeup flow provides some control over
-, pressurizer level during changes in letdown flow. .y CAUTION: Letdown flow should be at least above minimum demineralizer flow requirements, 25 GPM, as specified in PP 1101.01, when a demineralizer is in service. Also flow through MU6 should be maintained at >10 GPM.
4.2.11 Increase letdown flow by opening letdown flow cont'rol valve MU 6, with hand control station HC-MU 6 located on panel C5703 in the control room, if required by fluid expansiou during plant startup. Refer to Step 5.2.2 of this procedure for equipment required in service at various letdown flow rates. 4.2.12 Close the three-way valve MU 11, using switch HIS-Mull on left console, panel C5702 from the control room, to bleed reactor coolant letdown flow to waste disposal if necessary to compensate for expansion volume or feed to the makeup tank. One of two of the Clean Waste Receiver Tanks will be used to store the borated water, ~24,000 gallons, generated during reactor coolant system heatup. The bleed liquid should be routed through the " spare" purification demineralizer to recover the Li7 in it.
t- . -. i ,
~
i 22 SP 1104.02.3 m
- l. NOTE: This barated water will be eventually used '/
s during RCS cooldown to fill the volume i left from reactor coolant contraction. 4.2.13 Establish required hydrogen concentration by controlling - hydrogen overpressure (15 psig) in the makeup tank in l accordance with the Hydrogen Addition and Degasification Operating Procedure, SP 1102.12. 4.2.14 Saturating a Mixed Bed Purification Domineralizer l with Boric Acid. i
- 1. Whenever flow is first established through a newly charged Mixed Bed Domineraliser, boron will j be removed. A RCS boron concentration drop of about 125 ppe can be expected from saturation of i
a 50 ft8 bed of NR-6. 3 2. RCS boron concentration should initially be i raised about 125 ppe or additions should be made j to compensate for the boron decrease during the . j saturation process. f { 3. When flow is established through the Purification s 1 Desineralizer, C&HP should analyze the Purification l Domineralizer Inlet, Outlet, and Pressurizer i Liquid for Boron,' Lithium and C1~ hourly for the . '.m")
'~~'
j , initial six hours, then every 2 hours for the j next twelve hours. 1 4. The boron removal rate will depend on the Purification '~ Domineralizer flow rate. At 40 spe RCS boron j should drop about 12-pps/ hour. j Section 4 Completed Date ! 5. NORMAL OPERATION
- 5.1 Prerequisites l
l 5.1.1 One or more makeup pumps are operating supplying { normal RC systes makeup, and RC pump seal injection. l 5.1.2 The system is in its normal lineup as per Valve ! Verification List A. , 5.1.3 The running component cooling water pump and Makeup , Pump are supplied from opposite essential 4.16 KV I buses to prevent the simultaneous loss of cooling and l seal injection water to the RCP's.,- l l 1 l
*--u---t t 7
- r eef- tv =**-+w-*TTwyMW- g- P yy yi ,-ee-*sw-g-4
erw+we* > + - - -P*--*- fi e-y+1+ e,n1. 4 ,- 4-y,- =--,-- -y*y' hg--mm'y,wre
o .- 23 SP 1104.02.15 5.2 Procedure 5.2.1 Ensure that the Limits of Section 2 (Plant Limits and Precautions) of this procedure are not exceeded. 5.2.2 The following equipment must be in service for the
- various letdown flow rates listed:
~
Letdown Letdown Makeup Letdown Flow Flow Rate Coolers Demineralizers Filters Control Valve ' (GPM) Renuired Reaufred** Renuired (MU61 In Service 25-45 1 1 1 No* 45-70 1 1 1 Yes 70-140 2 2*** 2 Yes
- Valid if Rsactor Coolant System is at normal operating pressure.
**0r bypass the desineralizers by opening MU 104.
*v*Normally, flow in excess of 70 gym thru the " operating"7Purifica-tion Demineralizer should be bypassed to comply with Li manage-ment policy (Section 5.2.10-5.2.12).
5.2.3 Increase or decrease letdoun and purificatica rate and utilize Purification Demineralizers as specified by the C&HP section to maintain the proper RCS chemistry. (..-- , NOTE: When it is necessary to increase letdown flow, use the letdown flow control valve j NU 6. The block orifice R0 MUS is sized to pass about 45 GPM at Reactor Coolant System Operating Pressure (2155 psis). ( 5.2.4 Observe makeup filter and purification desineralizer prefilter differential pressures. Use differential indicators PDI-MU13 and PDI-MU62 respectively located i in the control room on panel C5703. NOTE: When the makeup filter or desin prefilter differential pressure reaches 25 psid, write a Work Request to change the plugged filter. 15 NOTE: Makeup filters and purification desineralizer prefilter changeout can also be based on radiation levels as indicated by C&HP. 5.2.5 Maintain makeup tank hydrogen pressure between 15-40 psig to produce the desired hydrogen concentration in accordance with SP 1102.12, Hydrogen Addition and Degasification and as specified by the C&HP Section. I
\.s 1
5 i v -- -c-. m -_fp. -
,9 . . , , . . , --A-.,m,. g - _,.,.,i-p,.,,9%.__ -. , g- , , .,,,i - 9, ,,,,.p-m.--
~ . . . ~ - - .- - . _ - . . . ., .. . . . -.11- :. L. :. ~. .. - . . .- - . . .
24 SP 1104.02.12
. .s NOTE: The makeup tank pressure can also be maintained ,
using Nitrogen as a substitute for hydrogen should the hydrogen partial pressure be too high. Nitrogen loading of the Makeup Tank is done per SP 1102.12, Hydrogen Addition - - and Degasification, Section 9. . 5.2.6 With pressurizer level controller LIC-RC14 in automatic and setpoint at 180" normal level, observe pressurizer level on LRS-RC-14 to confirm the proper operation of the Normal Makeup Flow Control Valve MU 32. 5.2.7 Maintain askeup tank level between 55" and 85". NOTE: If it becomes necessary to add water to t the sakeup tank at the existing RCS boron concentration to bring the tank level to normal (73"), refer to Boron Concentration Control Operating Procedure, SP 1104.03. 5.2.8 The three-way valve MU 11 may be positioned using + switch HIS-MU 11 located on left console, panel C5702
. from the control room, to the clean liquid radwaste system to reduce the water inventory in the reactor coolant system or the makeup system if necessary during normal or transient plant operating conditions. ,%
NOTE: The alternate Clean Waste Receiver Tank
. will be used to collect the letdown flow
) from the RCS as per water management plan, 4 Section 4.4, PP 1101.06, Flow thru the
" Spare" Purification Demineralizer to
, recover Li7 when going to the Clean Waste i Receiver Tanks.
- 5.2.9 Observe normal RCP seal injection flow of 32 GPM on FI MU 19 on left console, panel C5704 in the i control room, and say be adjusted by using flow controller FIC-MU 19.
5.2.10 The normal valve lineup per Valve Verification List A has routed the letdown flow continuously through Purification Demineralizer 1-1. However, the roles (" Operational" and " Spare") of Purification Dewineralizers 1-1 and 1-2 will switch based on bed exhaustion, replaced with fresh resin, and becomes the " Spare"; the previous " Spare" then becomes the " Operational" desineralizer for the next time period. 12 The " Operational" desineralizer will be intentionally 1
- - -~-- - . . , _ . . - . . .
25 SP 1104.02.12 s
~
saturated with Li7 by multiple chemical additions and by production of Li7 from Baron-10. 1 12 5.2.11 The " Spare" demienralizer will not be intentionally saturated with Li? . But, once the " Operational" - desineralizer is saturated with Li 7 , all bleed liquid from the RCS and all flow for the purpose of 'Li 7 concentration reduction should be routed through the
" Spare" demineralizer. This will slowly saturate the
" Spare" with Li7 . It will then become the " Operational" demineralizer for the next tLee period. This will save about 5-10 kg of Li7 per time period, which is roughly one fuel cycle.
5.2.12 The Purification Demineralizer 1-3 is a Cation esin bed and will be used as directed by C&HP for radio-cesium and other gross activity removal. It can be used to reduce RCS Li7 concentrations in the event both Purification Demineralizers 1-1 and 1-2 are Li 7 saturated. Open inlet valve MU1903 to place this bed in service. - 5.2.13 Under unusual conditions the Cation and Mixed Bed Purification Demineralizers can be placed in series as directed by C&HP.
~.
(. 1. To place Mixed Bed Purification Demineralizer 1-1 (1-2) in series with the Cation Bed: l ' " ' ) a. Open MU119 (MU121), Mixed Bed Outlet to Cation . Bed Line Valve. v b. Close MU139 (MU140) Mixed Bed Outlet Valve. i
- 2. To place the paralleled Mixed Bed Purification Desineralizers in series with the Cation Bed:
1
- a. Open MU119 and MU121, Mixed Bed Outlet 1-1, 1-2 Outlet to Cation Bed Line Valves,
- b. Close MU139 and MU140, Mixed Bed 1-1, 1-2 Outlet Valves.
- 3. To return to one desineralizer operation af ter running in series with Cation beds
- a. Open MU139 (MU140) Mixed Bed Purification Demin 1-1 (1-2) Outlet Valve.
- b. Close MU119 (MU121) Mixed Bed Purification Demin 1-1 (1-2) to Cation Bed Valve.
f
- .m.-- - , . _ , _ - . . - - - - , - - - , c ,. ..--r- - _ - - -
.. . ~. - . - - - --- .. . - _ = =. .. -.- - -. - _~_ ---
. z .. .-- - . . - . . --
+ 26 SP 1104.02.20 S i 5.2.14 To switch makeup pumps during normal operation complete ,. i the following steps: ! NOTE: hoever one or more Reactor Coolant Pumps are operating, the component cooling water - i pump providing the RCP cooling water and j the makeup pump providing the RCP seal f injection must be aligned to opposite i essential busses. However, it is permis-sible to prform ST 5011.03 on the makeup pump aligned to the same bus as the operating ; I CCW pump, but the opposite Makeup Pump must i be placed back in service as soon as possible , after completion of the test. ! i i NOTE: h a not in emergency conditions, complete i Step 5.2.14. NOTE: 1) Before the operating NU pump is removed from i service, obtain a comparison of the current PSD signature with its baseline and operating limits.
- 2) Af ter the other MU pump is placed in service, obtain the same data as above. Refer to 20l V&LPH System Procedure SP 1105.18.
l< y . 1. Perform makeup pump startup checklist, Attachment 2 of i this procedure for both makeup pumps. r
- 2. Verify second seal return cooler is in service as !
second makeup pump recirculation flow of 35 sps will , exceed the maximum flow rate of one seal return cooler ] of 42 gym. t ! 3. Perform Step 4.2.5 of this procedure to start second f makeup pump. i
- 4. ha second pump is on the line, stop other makeup j pump from the control room or locally, j 5. N a makeup pump has coasted down to a stop after .
! approximately two minutes, stop makeup pump AC oil pump and gear AC oil pump of off going pump. ) LETDOWit C0OLERS i 5.2.15 To switch letdown coolers 1-1 (1-2) open the letdown , cooler inlet isolation valve NU 1A (NU 15) from the i { control room, 4 *.he second cooler and close the ! j letdown cooler .%t valve of the first cooler. i F I i i
. . _ . . . . . . _ . . _ . , . _ . _ . . , _ . _ . _ -,,_,..._....__ .._.._ _ _.. - -. _ _ _ _ ... _ _..__. ,. _ _ , _ . . . _ . . . . ~ , . _ _ .
_ _ _ _ _. ~~_ - ' - ' ~ ~ l . I 27 SP 1104.02.1 i
-3; NOTE: Component cooling water inlet valve CC l 1409 (CC 1410) to letdown coolers are
( interlocked to open and close automatically with letdown cooler inlet isolation valves. l 5.2.16 To parallel letdown coolers 1-1 (1-2) open letdown cooler inlet isolation valve MU 1A (MU 1B) f' rom the control room of the second cooler. PURIFICATION DEMINERALIZERS l 5.2.17 To switch purification mixed bed desineralizers 1-1 (1-2) open mixed bed letdown inlet valve MU 10A (MU 108) from the control room, of the second demineralizer
- and close the mixed bed letdown inlet valve of the first demineralizer.
5.2.18 To parallel purification desineralizers 1-1 (1-2) open the mixed bed letdown inlet valve MU 10A (MU 10B) of the second cooler.
^
5.2.19 In the event of a small line break ($,3/4") the BWST can be used as a water supply for the sakeup pumps. 1 The three way valve MU-3971 should be positioned to the BWST supply mode before the makeup tank reaches g ,; the low level interlock to the makeup pumps (5 inches). q". :)
- 6. SHUTDOWN OF MAKEUP SYSTEM l 6.1 Prerequisites
! 6.1.1 Reactor coolant pumps are not in service. f 6.1.2 Discontinue makeup and letdown flows when permitted by reactor coolant systes conditions as specified in PP 1102.10, Unit Shutdown and Cooldown. 6.1.3 When the reactor coolant pumps are off, seal injection may be terminated when reactor coolant system temperature is less than 150'F. 6.2 Procedure 6.2.1 Close the Letdown Isolation Valve MU3. 6.2.2 Close the Normal Makeup Line Isolation Valve MU33. 6.2.3 Close the Seal Return Isolation Valve, MU 38. 6.2.4 Close the Seal Injection Flow Control Valve MU 19.
. - - _ . . - . . - - ~ . _ . . . . .
28 SP 1104.02.20 m 6.2.5 Stop the makeup pump (s). , 6.2.6 The makeup system is left with:
- 1. Makeup tank level at approximately 73". .
^
- 2. Makeup tank space filled with hydrogen or ' nitrogen.
- 3. All components and piping solidly filled with borated water.
- 4. Remaining valves in makeup and purification system are i in their normal position.
Section 6 Completed Date - ] i 7. INFREQUENT OPERATIONS l 7.1 Lithium Hydroxide and Hydrazine Addition-Lithium hydroxide l and hydrazine are supplied to the makeup tank to control pH and oxygen respectively in the RCS. LiOH and N H2 4 are injected into . l the makeup and purification system downstream of the purification
- domineralizers in accordance with the Chemical Addition system Operating Procedure, SP 1104.03. .
i. 4 7.1.1 Lithium may be removed from the RCS by changing . 4
- the letdown flow to the " Spare" desineralizer which '
normally will not be lithium saturated. If the l! " spare" desineralizer is saturated, route the flow l thru Purification Demineralizer 1-3. As a last l alternative feed and bleed can be used to reduce l Lithium concentrations. i 7.2 Makeup and Purification System Filter Replacement i j When the filter differential pressure increases to 25 PSID, , remove clogged filter from service and place spare filter in i service. 7.2.1 Seal Injection Filters f NOTE: Before removing the clogged seal injection filter, place the spare filter in service.
- 1. Returning Seal Injection Filter 1-1 to service.
(1) Close MU 480, MU 503 HU 505, MU 501, and MU 508. e 80 (2) Slowly open MU 221, Inlet Stop.* 5 i
29 SP 1104.02.20 10i (3) Very slowly open MU 224, Inlet Isolation Bypass Valve,* to allow filter housing to fill. (4) Slowly open MU 219 Inlet Isolation.* (5) OpenMU508andslowlycrackMU301,tovent until all air vented. Minimize flow out vent. (6) Close vent MU 501. (7) Close vent MU 508. (8) Open NU 223 Outlet Stop.* (9) Open MU 229 Outlet Isolation.* { (10) Close NU 218 filter 1-2 inlet isolation. 20 (11) Close MU 225 filter 1-2 Inlet Isolation Bypass Valve. Completed Date
- 2. Returning Seal Injection Filter 1-2 to service.
, - - (1) Close MU 481, MU 504, MU 506, HU $02, and MU 508, 20 (2) Slowly open MU 220, Inlet Stop.*
, (3) Very slowly open MU 225, Inlet Isolation Bypass ! Valve,* to allow filter housing to fill. (4) Slowly open MU 218 Inlet Isolation.*
. (5) Open MU 508 and slowly crack NU 502 to vent until all air is vented. Minimize flow out vent.
(6) Close vent 502. (7) Close vent 508. (8) Open MU 222 Outlet Stop.* (9) Open MU 228 Outlet Isolation.* (10) Close MU 219 filter 1-1 inlet isolation. 1 20 (11) Close MU 224 filter 1-1 Inlet Isolation.* Completed Date t w f
_ . . . . . . _ . . _ . . -.-.i . . . -. . . . _. I- ~...__.._..~.-_. ._. . - . . - _ _J - ~~. - - - - . . - 30 SP 1104.02.20 j m" i'
. 3. Removing Seal Injection Filter 1-1 from service.
~
I (1) Close MU 223 Outlet Stop. (2) Close MU 229 Outlet Isolation. .. (3) Close MU 219 Inlet Isolation. 20l (4) Close MU 224 Inlet Isolation Bypass Valve. (5) Close MU 221 Inlet Stop. (6) Open vent MU 501. (7) Open MU 508. (8) Open MU 480, MU 503, and MU 505. Drain for ten minutes, filter should be drained. (9) After the clogged filter is isolated and removed from service, maintenance may proceed with . . Nuclear Filter Cartridge Removal and Replacement Maintenance Procedure, MP 1402.04. Completed Date
- 4. Removing Seal Injection Filter 1-2 from service.
(1) Close MU 222 Outlet Stop. (2) Close MU 228 Outlet Isoaltion. ! (3) Close MU 218 Inlet Isolation. 20 (4) Close MU 225 Inlet Isolation Bypass Valve. (5) Close MU 220 Inlet Stop. (6) open vent MU $02. (7) Open vent MU 508. (8) Open MU 481, MU 504, and MU 506. Drain for ten minutes. Filter should be drained. (9) After the clogged filter is isolated and removed from service, maintenance may proceed with . Nuclear Fitler Cartridge Removal and Replacement Maintenance Procedure, MP 1402.04.
- Completed Date l
l 31 Sp 1104.02.20
- -s
- 5. Placing Seal Injection Filter 1-1 in standby.
a ! ! (1) Close NU 480, NU 503, NU 505, MU Sol, and MU 508. , 4 20 (2) Slowly open MU 221, Inlet Stop.* } (3) Very slowly open NU 224, Inlet Isolation Bypass l Valve *, to allow filter housing to fill. l (4) Slowly open NU 219 Inlet Isolation.* i !. (5) Open NU 508 and slowly crack NU 501 to vent i until all air is vented. Minimize flow out vent. ; ~ i 8 (6) Close vent MU 501. l 1 (7) Close vent MU 508. j (8) Close NU 221. i (9) Close NU 219. l 20 (10) Close NU 224. 1 -, Completed Date 4 lii 6. Placing Seal Injection Filter 1-2 in standby. l (1) Close NU 481, NU 504, NU 506, MU 502, and MU ;
- 508.
l 20 (2) 91t%1y open NU 220, Inlet Stop.* (3) Very slowly open MU 225, Inlet Isolation Bypass l 1 Valve,* to allow filter housing to fill. j (4) Slowly open NU 218 Inlet Isolation.* i (5) open MU 508 and slowly crack NU 502 to vent , until all air is vented. Minimize flow out vent. (6) Close vent 502. (7) Close vent 508. 1 (8) Close NU 220. j i e ] (9) Close NU 218. I i l 1 .I . 2 f
~. . . . . . . .. . . .. -. . .
l 32 SP 1104.02.20 20 (10) Close MU 225. , Completed Date
- NOTE: Just prior to filling and venting seal ..
. injection filter, contact Control Roca operator and warn of possible upset' in RCP seal injection flow. Crack open seal injection filter inlet valves slowly. 7.2.2 Makeup Filters:
- 1. When the 1-1 (1-2) MU filter differential pressure reaches 25 paid, place the spare filter in service by opening inlet valve MU 128 (NU 12A) from the control room on panel C5703, left console, using switch HIS MU12B (HIS MU12A).
CAUTION: Ensure the 1-1 (1-2) NU filter is in standby.
} 2. Isolate the clogged filter 1-1 (1-2) by closing inlet +
isolation valve NU 12A (NU 12B) from the control room 4 on panel C5703 left console using control switch HIS 1 NU12A (HIS MU12B).
- 3. When Maintenance is prepared to perform the filter -
,;)
change, perform Steps 4 through 13.
- 4. Close MU 177 (NU 161) filter outlet isolation valve locally. l
$. Check closed NU 174 (NU 166) NU filter 1-1 (1-2) vent, MU 110 N 2 /Demin Supply to Purif. Demin and NU 133 Demia Multipurpose.
- 6. Open MU 171 (MU 170) MU filter 1-1 (1-2) Disch to storage tank valve.
- 7. Open MU 172 (NU 163) MU filter 1-1 (1-2) refill valve.
- 8. Monitor Spent Resin Storage Tank level and pressure while performing Step 9.
CAUTION: The Spent Resia Storage Tank relief will lift at approximately 60 PSIG and the rupture disk will rupture at approximately 75 PSIC.
- 9. Open NN 102 and NN 103 N2 PCV Inlet and Outlet to Purification Demin to blow dry the filter with nitrogen for approximately five minutes while maintaining less than 50 PSIG in the Spent Resin Storage Tank. .
-- w - ,- , ,- _ --
33 SP 1104.02.15
'.l '
- 10. When the purge is complete, close NN 102 and NN 103.
( t
- 11. Close MU 172 (MU 163) and MU 171 (MU 170). [
- 12. Open MU 174 (MU 166) MU filter 1-1 (1-2) vent. .
CAUTION: This may cause a gaseous release. 'See Step y3 2.17.
- 13. Inform Maintenance the filter is isolated and drained and they may proceed with the Nuclear Filter Cartridge Removal and Replacement Maintenance Procedure MP 1402.04.
- 14. If it is necessary to flush the filter can after the used filter is removed but before the new filter is installed, perform the following steps after the filter can is buttoned up.
(1) Check closed NU 110 and MU 133. [ (2) Close MU 174 (MU 166). (3) Open MU 171 (NU 170) and MU 172 (MU 163). + (4) Monitor Spent Resin Storage Tank level and pressure while performing Steps (5) through (8). CAUTION: The Spent Resin Storage Tank relief (xs will lift at approximately 60 psig and 4 the rupture disk will rupture at - approximately 75 pois. 4 (5) Open DW 67 Demin Wtr Iso Viv to Purification l demin to flush the filter can. (6) After five minutes or when a one foot level increase is seen in the Spent Resin Storage Tank, close DW 67. (7) Open NN 102 and NN 103 for approxiantely five minutes while maintaining Spent Resin Storage Tank pressure less than 50 psig, i (8) When the purge is complete, close NN 102 and NN 103. (9) Close MU 171 (MU 17S) and MU 172 (MU 163). (10) Open MU 174 (MU 166) MU filter 1-1 (1-2) vent. CAUTION: This will cause a gaseous release. See Step 2.17.
... .. . - ,-. . . . - - . .- : . . - - . - .. - - . . . . . - . - . - - - - - ~
34 SP 1104.02.15 (11) Inform Maintenance the flush is complete and they ~l); nay proceed with the filter replacement. ' 1
- 15. When Maintenance has completed the filter change, perform Steps 16 through 23 to leak check the filter ,,
housing.
; 16. Inform the Control Room that the filter is about to be
- i leak checked. !
- 17. Check closed NU 171 (NU 170) and NU 172 (NU 163).
- 14. Crack open NU 12A (NU 128) NU filter 1-1 (1-2) Inlet Iso Valve.
- 19. Vent for the minimum amount necessary to ensur ethe filter is completely filled and vented.
] CAUTION: This may cause a radioactive gaseous release. j See Step 2.17.
~
! 20. Close NU 174 (NU 166) NU filter 1-1 (1-2) vent.
- 21. Check the filter housing for leaka.
- 22. Close NU 12A (NU 123) NU filter 1-1 (1-2) inlet valve. ..,.s i j j 23. Open NU 177 (NU 161) NU filter 1-1 (1-2) outlet valve. #'d Section 7.2.2 Completed By Date 7.2.3 Using makeup filter 1-2 as a substitute for purification i desin prefilter:
f
- 1. When the purification desineraliser prefilter differential pressure reaches 25 psid, place NU filter 1-2 in service, if possible, by performing the following steps.
CAUTION: Makeup filter 1-1 aust be in service or l bypassed before the 1-2 Nakeup filter can be used as the substitute for the purification desin profilter. If the 1-2 Nakeup filter , is in service as the Nakeup filter, the purification desin prefilter bypass valve NU 63 may be used until the 1-2 Nakeup filter is available or the purification desin refilter is replaced. J (1) Close MU 159 NU filter 1-2 inlet isolation and MU 162 MU filter 1-2 outlet isolation locally.
, .,, . w,.- - -- - - - .,,-v . + ~ - - , - . . - - . ,..,.n,,,,-..,.~._n,,m-e--. .n,n-n,~ - - . , . . - , . ..-- ,--.
_ _ _ _ _ . - _ ~._. _ . _ . . _ __ ___ . t 35 SP 1104.02.15 m ' (2) Open NU 93 Purif Demin Filter Bypass to NU filters locally. (3) Open NU 128 NU filter 1-2 Notor Operated Inlet. (4) Open NU 97 NU filter 1-2 outlet return to demineralizers locally. , (3) Close NU 94 Purif Domin Filter Inlet and NU 96 Purif Domin Filter Outlet.
- 2. When Maintenance is prepared to perform the filter i change, perform Step 3 through 11.
- 3. Check closed NU 99 Purif Demin Prefilter Vent, MU 110 N /Demin Supply to Purif Demin and NU 133 Demin Multipurpose.
- 4. Open NU 103 Purif Demin Prefilter Backwash Drain.
- 5. Open PW 8 Pri Wtr to Purif Demia Prefilter. .
- 6. Monitor Spent Resia Storage Tank level and pressure while performing Step 7. ,
CAUTION: The Spent Resin Storage Tank relief will
' , , lift at approximately 60 psig and the !
rupture disk will rupture at approximately
- 75 psig. l 1
- 7. Open NN 102 and NN 103 N PCV Inlet and Outlet to Purif Domin to blow dry the filter with nitrogen for !
approximately five minutes while maintaining less than ! 50 psig in the Spent Resin Storage Tank. ;
- 8. When the purge is complete, close NN 102 and NN 103.
- 9. Close PW 8 and MU 103.
- 10. Open NU 99 purif domin filter vent.
CAUTION: This will cause a gaseous relesse. See Step 2.17. , t
- 11. Inform Maintenance the filter is isolated and drained !
and they may proceed with the Nuclear Filter Cartridge l Removal and Replacement Maintenance Procedure MP 1402.04. I
- 12. If it is necessary to flush the filter can after the l used filter is removed but before the new filter is !
installed, perform the following steps after the ! filter can is buttoned up. !
36 SP 1104.02.15 (1) Check closed MU 110 2N /Penin Supply to Purif i Demin and MU 133 Demin Multipurpose. - (2) Close MU 99 Purif Demin Prefilter Vent. (3) Open NU 103 Purif Demin Prefilter Backwash Drain and PW 8 Pri Wtr to Purif Demin Prefilter. (4) Monitor Spent Resia Storage Tank level and pressure while performing Steps (5) through (8). ! CAUTION: The Spent Resin Storage Tank relief will lift at approximately 60 psig sad the rupture disk will rupture at approximately 75 psig. (5) Open DW 67 Demin Vtr Iso Viv to Purif Demin to flush the filter can. j (6) After five minutes or when a one foot level increase is seen in the Spent Resia Storage . l Tank, close DW 67, i ! (7) Open NN 102 and NN 103 for approximately five I minutes while maintaining less than 50 PSIG in the Spent Resia Storage Tank. . i
- (8) When the purge is complete, close NN 102 and NN
- 1 103.
(9) Close PW 8 and MU 103. (10) Open NU 99 Purif Demin Prefilter Vent. I CAUTION: This may cause a gaseous release. See Step 2.17. (11) Inform Maintenance the flush is complete and they may proceed with the filter replacement.
- 13. When Maintenance has completed the filter change, perfona Steps 14 through 21 to leak check the filter housing.
- 14. Inform the Control Room the filter is about to leak j checked.
- 15. Check closed MU 103 and PW 8.
- 16. Crack open MU 94 Purif Demin Prefilter Inlet.
I j i l I
37 SP 1104.02.18 N
~~
. 17. Vent for the minimum amount necessary to ensure the filter is completely filled and vented.
CAUTION: This may cause a radioactive gaseous release. See Step 2.17. -
- 18. Close MU 99 Purif Demin Prefilter Vent.
- 19. Check the filter housing for leaks.
- 20. Close MU 94 Purif Demin Prefilter Inlet.
- 21. Open MU 96 Purif Demin Prefilter Outlet.
- 22. To return the Purif Demin Prefilter to service and remove the 1-2 MU filter from service as the Purif Demin Prefilter, perform Steps 23, 25, 26, and 27. To return the Purif Demin Prefilter to service and remove the Purif Derin Prefilter bypass valve from service, perform Steps 23 and 24.
I
- 23. Open MU 94 Purif Demin Prefilter Inlet.
- i
- 24. Close MU 63 Purif Demin Prefilter Bypass.
i g s 25. Close MU 12B MU filter 1-2 inlet iso. s
- 26. Close MU 97 MU filter outlet return to desineralizers and MU 93 Purif Demin Prefilter Bypass to MU filters
. locally.
- 27. Open MU 159 MU Filter 1-2 Inlet Iso and MU 162 MU Filter 1-2 Outlet Iso locally.
Section 7.2.3 Completed By Date 7.3 Recovery from Letdown Isolation (135*F) A high temperature alarm (TSH 3745B) is set at 135'F (T715 "RC Letdown Temp Hi" on annunciator panel 2) and signals a high temperature in the delay coil downstream of the letdown ! coolers. The alarm also signals the letdown cooler inlet isolation valve, MU 2B, inside the containment vessel to close, thus protecting the purification demineralizers resins due to a decrease or loss of component cooling water flow to the letdown coolers. Should the cause of the high temperature trip be known, perform the following steps: 7.3.1 Manually override the high temp trip signal by holding 18l HIS-MU2B on the open position until the trip clears.
F 1_. ~ . .. .T_ . .. .:. i. i . . - . _ . . . _ _ _. .. J _ ._ _ _ ... .. .. . .. 38 SP 1104.02.18
- s Should the cause of the High Temperature Trip not be known, ';'d) perform the following steps:
7.3.2 Isolate the purification demineralizers 1-1, 1-2, 1-3 by closing the desineralizer inlet isolation . , valves NU10A, NU108, and NU 1903 from the control I room on panel C5703, left console, using 'swi'tches HIS-NU10A, HIS-NU10B, and HIS MU-1903 respectively. 7.3.3 Unlock and open the desineralizer bypass valve NU104 (locally). 7.3.4 Take immediate action to correct the cause of the high temperature letdown flow to the desineralizers:
- 1. Manually override the high temperature signal by 18{ holding HIS-NU2B in the open position until the trip clears.
- 2. Re-establish component cooling water flow in the header supplying the letdown coolers as per Component -
Cooling Water Operating Procedures, SP 1104.12. 7.3.5 Restore the makeup system to the normal valve lineup by opening MU 10A, NU 10B, and NU 1903 (if needed) purification demineralizers 1-1, 1-2, and 1-3 inlet 3 isolation valves and lock close demineralizer bypass 4
' ')
valve NU 104. Section 7.3 Completed Date 7.4 Recovery from Letdown Isolation (160*). A high.tempeature alarm (TSH 3745A) 'is set at 160'F (T715 "RC Letdown Temp Hi" on annunciator panel 2) and signals a high temperature in the delay coil downstream of the letdown coolers. TSH 3745A will signal RC letdown cooler 1-1 and 1-2 inlet isolation valves NU 1A and NU IB to close, thus protecting the purification demineralizers resins due to a decrease or loss of component cooling water flow to letdown coolers. 7.4.1 Isolate the purification desineralizers 1-1, 1-2, 1-3 by closing the demineralizer inlet isolation valves NU 10A, NU 10B, and MU 1903 from the control room on panel C5703 using switches HIS-NU10A, HIS NU10B, and HIS MU 1903 respectively. 7.4.2 Unlock and open the demienralizer bypass valve NU 104, (locally).
_a 39 SP 1102.04.10
'm 7.4.3 Take immediate action to correct the cause of the high temperature letdown flow to the demineralizers:
- 1. Reestablish component cooling water flow in the header supplying the letdown coolers as per component cooling . .
water operating procedure, SP 1104.12.0. . 10 2. Manually override the high temperature trip signal by holding HIS-MUIA (HIS-MU1B) letdown cooler 1-1 (1-2) inlet isolation valve on left console, panel C5703 in the control room, in the open position until the trip clears. 7.4.4 Restore the makeup system to the normal valve lineup by opening MU 10A, MU 10B, and MU 1903 (if needed) purification deminealizers 1-1, 1-2, and 1-3 inlet 3 isolation valve and lock close demineralizer bypass valve MU 104. Section 7.4 Completed Date 7.5 Preparing to Fill the Core Flood Tanks: 7.5.1 Prerequisites
- 1. Makeup system operational but shutdown as per Section
[ ,.) 6.2. , N-
- 2. Nitrogen system available as per Nitrogen Purge and Blanket System Operating Procedure, SP 1104.26.
, 3. Chemical Addition System available as per Chemical Addition System Operating Procedure, SP 1104.20.
- 4. Gaseous Radwaste System available as per Gaseous Radwaste Disposal. Operating Procedure, SP 1104.27, 7.5.2 Procedure
- 1. Drain NU tank to 24 inches to the reactor coolant drain tank by. opening MU 189 locally.
i
- 2. V(nt makeup tank of H2 Gaseous Radwaste System and purge tank with N 2-
- a. Open MU 395, Makeup Tank Vent to Gaseous Radwaste MU 14 inlet isolation valve.
- b. Open MU 185, Makeup Tank Vent to Gaseous Radwaste MU 14 Outlet Isoaltion Valve. i l
. I 1 l
40 SP 1104.02.11
~
- c. Open MU 14, Makeup Tank vent to Gaseous Radwaste System with Switch HIS-MU14 located in control room on panel C5703.
- d. Open MU 53, Nitrogen Supply to Makeup Tank from --
the control room on panel C5703 and purge the makeup tank with nitrogen for (later) minutes,
- e. When tank has been purged with about 2 volumes of N2 , have a sample taken. If H2 is still present purge one volume again and sample.
- f. When tank is purged of H2 close MU'53 N2 supply to makeup tank, MU 14 vent control valve to gaseous radwaste system, M 395 and MU 185 isolation valves for MU 14.
- 3. Sample for baron in the MU tank as per SP 1104.10, Sample System in the Nuclear Area Procedure.
- 4. Calculate the amount of boric acid to fill the MU tank .
with 3500 ppa boron as per SP 1103.04, Boron Concentration Control.
- 5. Isolate RC system, seal injection, letdown coolers, and purificatica desineralizers: -
- a. Close MU 214, RCP Seal Injection Flow Control Inlet Isolation.
- b. Close MU 58A, Normal Makeup Flow (FE MU 58)
Source Needle Valve.
- c. Close MU 209, Normal Makeup Flow Control Inlet Isolation.
- d. Close MU 38, RCP Seal Return Isolation with MU 38.
- e. Close MU 148, Three-way (MU 11) Outlet Isolation.
- 6. Add water and boric acid to the MU tank as per SP 1104.03, Chemical Addition Procedure, Section 5.
- 7. Pressurize with N2 to 20 PSIG with MU 53, Nitrogen Supply to Makeup Tank.
11 8. Start makeup pump 1-1 (1-2) as per Sections 4.2.2, 4.2.3.1, and 4.2.5 of this procedure. Recire for approximately two makeup tank volumes. Makeup tank
41 SP 1104.02.11
' ' ll temperature is not to exceed 140'F. Two seal return cooling should be in service.
- 9. Sample makeup tank to ensure that boron concentration is 3200 to 3500 ppa. ,
- 10. Stop makeup pump 1-1 (1-2) from control room or locally.
- 11. The core flood tanks can not be filled as per SP 1104.01, Core Flooding System Operating Procedure, Section 4, Method 1.
7.5.3 Return makeup system to shutdown conditions as per Section 6.2 of this procedure after filling the core flood tanks.
- 1. Sample for baron in the MU tank as per SP 1104.10, Sample System in the Nuclear Area Procedure.
- 2. Add primary or demineralized water and drain to the reactor coolant drain tank as necessary to bring .
makeup tank to correct boron concentration.
- 3. Start makeup pump 1-1 (1-2) as per Sections 4.2.2, 4.2.3.1, 4.2.5 of this procedure, and recire for five
; (5) minutes.
- 4. Sample Makeup Tank to ensure that boron concentration is back to the valve for that point in core life.
- 5. Stop makeup pump 1-1 (1-2) from the control room or locally.
- 6. Return makeup system to normaloperating flow, path:
- a. Open MU 214, RCP Seal injection flow control inlet isolation.
- b. Open MU 58A, Normal Makeup Flow (FE MU 58) Source Needle Valve.
- c. Open MU 209, Normal Makeup Flow Control Inlet Isolation.
- d. Open MU 38, RCP Seal Return Isolation with HIS-MU 38.
- e. Open MU 148, three-way (MU 11) outlet isolation.
Section 7.5 Completed Date _ _ . _ _ _ . . _ _ _ _ _ _ . _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ _ _ - _ _ _ . _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ _ . _ _ _ _ _ _ _ m ___._______ _-.-_ __._-.__________-_.______.____.____._-m_ -___ _
- ' ~~
- .J. _ _ . _.__._ _ _ _ _ ___2__.-_.__ ._
42 SP 1104.02.5 -, 7.6 Recovery from letdown isolation (135 PSIG). .f A high pressure interlock exists between the component cooling water system and the RC Letdown Cooler Inlet Isolation Valve MU2B, RC Letdown Cooler 1-1 Inlet Isolation Valve MUIA, and RC --- 5 Letdown Cooler 1-1 Inlet Isolation Valve MU1B. Pressu.re switches PSH 3759 and PSH 3763 monitor component cooling water header pressure downstream of letdown coolers 1-1 and 1-2. These pressure switches are interlocked ot the RC Letdown Cooler Inlet 5l Isolation Valve NU2B and close this valve upon a cooling water pressure of 135 PSIG. Pressure switches PSH3711 and PSH3712 monitor letdown cooler shell pressure and close the RC Cooler 1-1 Inlet Isolation MUIA and RC Cooler 1-2 Inlet Isolation MU1B respectively upon a shell pressure of 135 PSIG. All of the pressure switches trigger the annunciator and computer point alarm P101 on the alarm printer. 7.6.1 Letdown Cooler 1-1 in Service.
- 1. Verify RC Letdown Cooler Isoaltion Valves MU2B and MUIA are closed. -
- 2. Open RC Letdown Cooler 1-2 Isolation Valve MU1B using HIS NU1B, located on Control Room Panel C5703.
- 3. Press the open pushbutton on HIS MU2B located on "3.
Control Room Panel C5703 and verify that NU2B opens. , . ,/ 7.6.2 Letdown Cooler 1-2 in Service.
- 1. Verify RC Letdown Cooler Isolation Valves MU2B and MU1B are closed.
- 2. Open RC Letdown Cooler 1-1 Isolation Valve MU1A using HIS MUIA located on Control Room Panel C5703.
- 3. Press the open pushbutton on HIS MU2B located on Control Room Panel C5703 and verify MU2B opens.
I
( p) 6- . , 3
) -
*i Ilreakers & Switclies for Hakeup & Purification System Equipment ident. No. Hll 4 Hu 63 HU 10A HU 10B HU 1903 HU 11 Hll 40 HU 12A Equipment Letdown Purifica- Purifica- Purifica- Purifica- Tliree-Way Ba tcli Hakeup Name Pressure Lion Demin tion Demin Lion Demin Lion Demin Valve Feed Stop Filter 1-1 '
Heducer Filter 1-1 Inlet 1-2 Inlet 1-3 Inlet Valve 1-1 Inlet Inlet Iso Bypass Viv j/alve Viv Viv Control Room lilS-HU 4 tilS-HU 63 HIS-HU 10A tilS-HU 10B 111S-1903 tilS-HU 11 tilS-HU 40 tilS-HU12A Swi t cli/PaneI # C 5703 C 5703 C 5703 C 5703 C 5703 C 5702 C 5702 C 5703 I Control Room RC Let- Purif RC Let- RC Let- RC Let- RC Let- BA Batcli RC HU Fitr i Suit ch Name down Demin down Purf. down Purf. down Purf. down Stop Viv 1 In Valve Press Prefilter Demin 1 In Demin 2 In Demin 3 In Divert Viv Reduce Bypass Viv - Breaker No. BE-2259 BE-2268 BE-2262 BE-2263 BE 2271 BE 2278 BE 1109 BE 1125
& HCC E-22B E22B E-22B E228 E 22B E 22B E IIA EllA HCC 1.ocation BWST IITR BWST lit r BWST litr BWST litr BWST litr BWST litr BWST litr BWST litr (Area & Elev.) Area 565' Area 565' Area 565' Area 565' Area 565' Area 565' Area 565' Area 565' Area 8 Area 8 Area 8 Area 8 Area 8 Area 8 Area 8 Area 8 Local Control NV Hll 040 NV HU 630 NV HU 10A NV HU 10B NV 19030 NV HU 110 NV MU 400 NV HU 12A >
W Switcli No. SA Signals None None None None None None None None Verified By O &
'02 8 B-0 to
*R S
+
l _ _ __________m_- _ _ _ _ _ _ _ - _ _ -
t' f - t lireakers & Switches for Makeup & Purification System i
' Equipment ident. No. HU 12B P-3718 P-371D P-372-B P-3721) HU 3971 P 37-2 P37-1 Equipment Makeup HU Pump Hil Pump HU Pump HU Pump Three-Way tfD Pump HU Pump Name Filter 1-1 Hain 1-1 Aux l-2 Main 1-2 Aux From HU 1-2 1-1 1-2 Inlet Oil Pop Gear oil Oil Pmp Gear 011 Tk or BWST i Viv I-1-1 Pump 1-2-1 Pump to HU Pumps Control Room IIIS-tilll2B llIS-HU24A1 lilS-HU24A3 Ills-HU24B1 HIS-HU28B3 HIS HU 3971 IIIS-HU24B llIS-HU24A C 5703 C 5704 C 5704 C 5704 C 5703 C 5704 C 5704 Switch / Panel # C 5_704 Control Room RC HU HU 1%p I HU Pmp i HU Pop 2 HU Pop 2 RC HU Pop RC HU RC HU ,
1 Switch Name Fltr 2 AC Oil Gear AC AC 011 Cear AC Suction Pop 2 Pmp 1 In Vlv Pmp Oil Pop Pap Oil Pop Valve Breaker No. BF 1107 BE-Il91 BE-1192 BF-ll67 BF-Il68 BE 1127 AD-105 AC-105
& HCC F 11D E IID E IID F-11C F-11C EllD C1 (4160) CI(4160)
HCC I.ocation Boric Boric Acid Boric Acid #2 Hech #2 Hech Boric Acid High liigh Volt-(Areas & Elev) Acid Evap Evap rm Evap rm Penetration Penetration Evap Rm Voltage age Switch-Rm 565' 565' 565' Rm 565' Rm 565' 565' Switch- gear Room - Area 7 Area 7 Area 7 Area 7 Area 7 Area 7 gear Room A 585' Area B 585' 6 Area 6 o
# I' Local Control NV HU 12B NP 371B NP 371D NP 372B NP 372D NV 39710 NP 372A NP 371A Switch No.
SA Signals None None None None None None None None Verified By , i
$N
- c =
~ 9- St h
v-= b
) ) -
lireakers & Switches for Hakeup & Purification System
~59uipment Ident. No. Hil I A HU 111 HU 2B Hll 2A MU 59A Hil 59B Hil 59C HU 59D Equipment RC I.et- RC I.et- RC I.et- i.etdown RCP l-2-1 RCP l-2-2 RCP l-1-1 RCP 1-1-2 Name down down down Coolers Seal Return Seal Re- Seal He- Seal Return Cooler Cooler Cooler Outlet Valve turn turn Valve Inlet Inlet inlet Isolation Valve Valve Isolation Isolation Isolation Cont rol Room tilS-Hil I A tilS-Hll IB lilS-HU 2B lilS-HU 2A lilS HU 59A lilS HU 59B lilS-HU59C lllS-HU 59D Switch /Panell/ C 5703 C 5703 C 5703 C 5717 C 5717 C 5717 C 5717 C 5717 Control Room RC I.et- RC I.et- HC I.et- RC I.et- RCP 2-1 '
RCP 2-2 RCP l-1 RCP l-2 Switch Name down Clr down Clr down Clrs down Clra Seal Het Seal Ret Seal Ret Seal Het I in Viv 2 In Viv In Iso Vlv Out Iso Viv Iso Vlv Iso Vlv fireaker No. BF 1237~ BF 1238 BE-Il72 BE-Il71 IIE 1174 BE 1175 BE-Il?7 BE-1178
& HCC F 12A F 12A E 1111 EllB E IIB E 1111 E IIB EllB HCC I.ocation _CTHT CTNT Purge Fuel lland- Fuel lland- Fuel lland- Fuel lland- Fuel Hand- Fuel lland-(Area & Elev) Purge & & Exhaust ling Area ling Area ling Area ling Area ling Area ling Area Exhaust Fan 585' 585' 585' 585' 585' 585' 585' Fan 585' Area 8 Area 8 Area 8 Area 8 Area 8 Area 8 Area 8 Area 8 g 1.ocal Control NV HUDIA NV HU OlB NV HUO2B NV HUO2A NV HU 59A NV HU 59B NV HU 59C NV HU59D Switch No.
16 SA Signals None None None SA 271A SA 331E SA 331F SA 331G SA 33111 Veril_ied fly 5E
%S :
?
wi P,. O is 6
Breakers & Switches for Hakeup & Purification System j Equipment ! I slent . No. P-372C P-371C Ecluipment HU Pump HU Pump Name 1-2 Aux l-1 Aux ,.
, Oil Pop Oil Pop ;
l-2-2 1-1-2 . Control Room HIS-HU24B2 llIS-HII24A2 Switch /Panelf C 5704 C 5704 ' Control Room HU Pop 2 HU Pop 1 Switch Name DC Oil Pop DC Oil Pop g Breaker No. D-217 D-217 l
& HCC (1)C) (DC)
HCC 2 HCC 1 HCC LocaLion Low VolL- Low Volt-(Area & Elev) age age Switchgear Switchgear Room 603' Room 603' Area 6 Art:a 6 . I Local Control ~NP 372C NP 371C Switch No. $ ! SA Signals None None Verifical By o> a I s?? 5 i "R
- eg O CD O
m :3 . w P P A B
- s. .. !
s
'~
47 SP 1104.02.0 Makeup Pump Pre Startup Checkoff List Name: Makeup Pumps 1-1 & 1-2 Number: P 37-1 & P 37-2 Manufacturer: Bingham , Model: Type-CP Capacity: 150 GPM Head: 5800 Feet Pump RPM: 5400 Motor EP: 450 Motor RPM: 1800
- 1. Makeup pump electrical breaker is racked in.
Pump 1-1 Pump 1-2 AC 105 AD 105
- 2. Makeup pump AC main oil pump electrical breaker is closed.
AC Main Oil Pump 1-1-1 AC Main Oil Pump 1-2-1
^
B E11 91 (E11D) B Fil 67 (F11C)
- 3. Makeup pump DC aux oil pump electrical breaker is closed.
. DC Aux Oil Pump 1-1-2 DC Aux Oil Pump 1-2-2 D117 (MCC 1) D217 (MCC2)
- 4. Makeup pump AC aux gear oil pump electrical breaker is closad.
AC Aux Oil Pump 1-1 AC Aux Gear Oil Pump 1-2 B E11 92 (E11D) B Fil 68 (F11C)
- 5. Check for proper oil level in the motor, speed increaser gear box, and pump oil reservoir oil sight indicators.
MU Pump 1-1 MU Pump 1-2 Motor Inboard Bearing: Motor Outboard Bearing: Speed Increaser Gear Box Reservoir Pump 011 Reservoir
- 6. Establish component cooling water to makeup pump gear lube oil and pump lube oil coolers by opening the following valves.
Attachment 2 Page 1 of 3 l
48 SP 1104.02.0 7 Makeup Pump 1-1 Makeup Pump 1-2 ,.;. CC 127 CC 128 CC 2190A CC 2191A --
~
CC 2190B CC 2191B Throttle CC 129 to establish a Throttle CC 130 to establish a 12 GPM flow rate as read on 12 GPM flow rate as read on FI 2190 . FI 2191 .
- 7. Open the pump suction valve:
Makeup Pump 1-1 Makeup Pump 1-2 NU 191 MU 190
- 8. Open the pump vent valves to prime the pump and then close the vent valves:
Makeup Pump 1-1 Makeup Pump 1-2 MU 195A and MU 429 MU 194 and MU 428 Perform this step only if makeup pump has been drained or NOTE: . makeup tank pressure was less than 5 psig while the pump ~~ :) was shutdown. ,
- 9. Open pump discharge pressure source valves:
Makeup Pump 1-1 Makrup Pump 1-2 MU 25A to PI MU 25A MU 25B to PI MU 25B
- 10. Open the pump discharge valves: .
Makeup Pump 1-1 Makeup Pump 1-2 MU 199 MU 198
- 11. (VERIIT THE PUMP RECIRCULATION VALVES ARE LOCKED OPEN 1 AND RESTRICT-ING ORIFICES ARE INSTAufn)
Makeup Pump 1-1 Makeup Pump 1-2 MU 205 (L.O.) MU 202 (L.O.) MU 206 (L.O.) MU 203 (L.O.) R.O. MU57A (installed) R.O. MU57B (installed) MU 479 (L.O.) MU 479 (L.O.) Attachment 2 Page 2 of 3
49 SP 1104.02.18 7 Seal Return Cooler 1-1 Seal Return Cooler 1-2 MU 269 (L.O.) MU 268 (L.O.) MU 271 (Closed) MU 270 (L.O.) 18 - NOTE: Normally seal return cooler 1-2 will be in service, and MU 270 must be locked open. Seal return cooler 1-1 will be in standby and MU271 closed. If seal return cooler 1-1 is in service, MU271 must be open and MU 270 closed.
- 12. Open pump suction pressure source valve to pressure indicators and verify suction pressure. Suction valve MU3971 is open* (i.e. from MU Tank). This is the normal suction.
Makeup Pump' 1-1 Makeup Pump 1-2 MU 1895 MU 1896 PI 1895 15 PSIG PI 1896 15 PSIG
- Pumps also can take suction from BWST (i.e. MU 3971 closed). If running MU Pump for testing, recirculating BWST, see ST 5011.03. ,
NOTE: If the BWST is the water supply for the MU pumps, then the 3-way valve (MU 3971) must be positioned at the BWST. Also the recirculation path must be changed from MU Tank to the BWST by closing MU 479 and then opening MU 208. ('- . j, Throttle HP29 one and 1/2 turns, open HP 1556 and HP 35. Also, verify that the BWST outlet supply valves are open: DH 79, HD 7A (DH 7B), DH 132 and DH 131 (DH 130, DH 129). 1 Controlled per AD 1839.02
- 13. After the pump is started, check the following:
Makeup Pump 1-1 Makeup Pump 1-2 Increasing Discharge Pressure Observe Pump for Excess Vibration
- Pump Leakage (Water)
Speed Increaser Leakage (011) Outlet Cooling Temperature (CCW) Check Oil Rings on Pump and Motor Pump Oil Sight Glasses for Flow Pump Oil Pressure 8 PSIG Gear Increaser Oil Pressure 10 PSIG
*If there is any question about excessive vibration, contact control room operator and have a PSD taken on the Vibration and Loose Parts Monitoring System.
Attachment 2 Page 3 of 3
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h 53 SP 1104.02.2
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54 SP 1104.02.2 ,
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_, 55 SP 1104.02.16
\. 1. Set Needle Valve 1. (MU 231) First perform Step 4.2.7.2 as written then do the steps below.
- a. Record the four individual seal flow rates and the dP measurement on Needle Valve 1.
FIMU30C FIMU30D FIMU30A FIMU30B MU231 No. Turns open
- b. Compute Cv for Needle Valve I where Cv = Flow throueh needle valve GPM J needle valve dP, PSI Cv MU231 Initial = MU231 dP =
Desired Cv is between 0.76 and 0.89, but closer to 0.89, if possible (this corresponds to a dP range of 110 to 80 PSI at 8 GPM). IF Cv is not in desired range, change needle valve position (to increase Cv, open valve and to decrease Cv, close valve). Wait until flow steadies, then record - Needle Valve 1 flow and dP and compute Cv. Repeat as necessary to obtain desired Cv. Flow rate through needle valve does not have to be 8 GPM; the desired Cv (which is valve position) can be obtained at various flow rates. s-: ' Cv MU231 Final = MU231 DP =
- 2. Determine number of turns open for Needle Valve I to use for preliminary setting of Needle Valves 2, 3, and -4.
- a. Close Needle Valve 1 and count number of turns and record.
NU231 No. turns open
- b. Re-open Needle Valve 1 to the number of turns open recorded in Step 2.a.
- c. When Needle Valve i flow steadies, record Needle Valve 1 flow and dP and compute Cv. If Cv is not as desired, change valve position and compute Cv and maintain record of number of turns open. Repeat as necessary to obtain desired Cv. Record number of turns open for final valve
- position.
MU231 No. turns open i Attachment 7 Page 1 of 2
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56 SP 1104.02.16 s 1 i 3. Preliminary setting of Needle Valves 2, 3, and 4. 2-Close Needle Valves 2, 3, and 4 and then re-open each valve to the final recorded number of turns open for Needle Valve 1 f rom - - Step 2.
- 4. Final setting of Needle Valve 2, 3, and 4.
- a. Flow in all four lines now should be about equal. (In the range 6-10 GPM.) If not, adjust Needle Valves 2, 3, and 4 one at a time as necessary as described in Step 4.b.
DO NOT ADJUST NEEDLE VALVE 1 (MU 231). The. desired flow for each line is 8 GPM, but do not adjust Needle Valve 1 to achieve this,
- b. Needle Valve 1 is the reference line. If the individual flow distribution is not satisfactory, determine which line flow is "off" the most, either above or below the desired flow (excluding Needle Valve 1). Throttle this line needle valve slightly, but do not throttle flow beyond desired +
flow valve (6-10 GPM). Wait for total flow to steady at
. setpoint before performing next step.
i c. Repeat Step 4.b. as necessary until a satisfactory flow distribution is obtained, but do not adjust Needle Valve 1 ', (MU231). j
- d. Record final position of valves 2, 3, and 4.
MU230 No. turns open MU232 No. turns open MU233 No. turns open e Attachment 7 Page 2 of 2
t i 57 SP 1104.02.17 7:ct:e :. ,
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4 58 SP 1104.02.14 - Sheet No. 1 VALVE VERIFICATION LIST A - of 25 Makeup and Purification System Normal /Prestartup Lineup
~
Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY CRTM OPERATED VALVES M-031 ** Mixed Bed 1-2 Letdown Flow Inlet C-12 MU 10B Closed Three-Way (Letdown to Radwaste Dr. MU Normal (to Tank) E-10 MU 11 MU Tank) Makeup Filter 1-1 Inlet Isolation D-9 MU 12A Open Makeup Filter 1-2 Inlet D-9 MU 12B Closed Makeup Tank 1-1 Vent (Pneumatic) G-10 MU 14 Closed Batch Flow Controller F-12 MU 39 Closed Batch Feed Stoo F-10 MU 40 Closed Purif Demin Filter Bypass A-10 MU 63 Closed ; Cation Bed L-3' Letdown Flow Inlet C-12 MU 1903 Clo.ed Makeup Tank 1-1 N2 Supt,1_y Isolation G-11 MU 53 J1osed Makeup Tank 1-1 H2 Supply Isolation H-11 MU '4 Closed Normal Makeup to RCS Isolation F-5 MU 33 Open RCP Seal Return Isolation E-5 MU 38 Open No rmal MU Pumps Suction Three-Way J-9 MU 3971 from MU Tk Mixed Bed 1-1 Letdown Inlet C-11 MU 10A Open Throttled ' RCP Seal Inj Flow Controller H-6 MU 19 Closed Letdown Stop V1v C-5 MU B Open Open Letdown block Orifice Isolation C-7 MU 4 Closed Letdown Flow Control C-7 MU 6 ' Closed 5*HU10A and MU10B may be positioned in accordance with Shift Supervisor's directions with the exception that one of them must be open. i
~ - - - - - - ,. - - - -
59 SP 1104.02.20
,m
', Sheet No. 2 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve P&lD No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY Open Makeup Flow Controller F-6 MU 32 Closed M-036 Open RC Letdown Clr 1-1 CCW Inlet D-4 CC 1409 Closed
- Open RC Letdown Clr 1-2 CCW Inlet E-4 CC 1410 Closed RM 300 M-031 RCP Seal Inj Filter 1-1 Inlet Isolation H-5 MU 219 #
RCP Seal Jnj Filter 1-1 Inlet Byapss H-5 MU 224 # 20 . RCP Seal Inj Filter 1-2 Inlet Bypass H-5 MU 225 # RCS Seal Inj Filter 1-1 Inlet Stop H-5 MU 221 # (' ~ - RCP Seal Inj Filter Vent Isolation H-5 MU 507 Closed (,) RCD Seal Inj Filter 1-1 Inlet Line Drain H-5 MU 503 Closed RCP Seal Inj Filter 1-1 Vent H-5 MU 501 Closed RCP Seal Inj Filter 1-1 Outlet Stop H-5 MU 223 # RCP Seal Inj Filter 1-1 Outlet Drain J-5 MU 480 Closed RCP Seal Inj Filter 1-2 Inlet Isoaltion H-5 MU 218 # RCP Seal Inj Filter 1-2 Vent J-5 MU 502 Closed RCP Seal Inj Filter 1-2 Inlet Stop H-5 MU 220 # RCP Seal Inj Filter 1-2 Inlet Line Drain H-5 MU 504 Closed RCP Seal Inj Filter 1-2 Outlet Line o Drain J-5 . MU 481 Closed .
*This valve has a " Normal" position which is different than its "Prestartup" position. The first position listed in the " Normal" and the second position listed in the "Prestartup" position.
#These valve positions shall be determined by the Shif t Supervisor, depending on which seal inj. filter is in service.
60 SP 1104.02.14 Sheet No. 3 VALVE VERIFICATION LIST A . of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List only - Consult Shift Supervisor Prior to Repositioning Valve P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY RCP Seal Inj Filter 1-2 Outlet Stop H-5 MU 222 # RCP Seal Inj Filter 1-2 Drain Isolation J-5 MU 506 Closed RCP Seal Inj Filter 1-2 Outlet Isolation H-5 MU 228 # RCP Seal Inj Filter Vent Isolation J-5 MU 508 Closed RCP Seal Inj Filters (PDT MU 62) Inlet Scurce J-5 MU 67A Open RCP Seal Inj Filters (PDT MU 67) Outlet Source J-5 MU 67B Open In RCP Seal Inj Filter Pressure Diff Trans J-5 PDTMU67 Se rvice RCP Seal Inj Filter Bypass H-5 MU 217 Closed 5 RCP Seal Inj Filter 1-1 Outlet Stop H-5 MU 229 # RCP Seal Inj Filter 1-1 Drain Isolation H-5 MU 505 Closed Mixed Bed 1-1 Resin Fill Inlet C-11 MU 130 Closed Mixed Bed 1-2 Resin Fill Inlet C-12 MU 131 Closed Mixed Bed 1-3 Resin Fill Inlet D-13 MU 132 Closed Resin Fill Line to Purif Demin 1-1, 1-2 Iso B-12 MU 382 Closed RM 302 Letdown (MU 91) Outlet Line Vent C-9 MU 92 Closed RCP Seal Return Cooler Line Vent E-7 MU 273 Closed RM 303 Normal Makeup to RCS Line Vent G-5 MU 213 Closed MU Pump Discharge (PT-MU 26) Source .H-6 MU 26 Open
//These valve positions shall be determined by the Shift Supervisor, depending on which seal inj. filter is in service.
61 SP 1104.02.14 A 1 Sheet No. 4 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List only - Consult Shif t Supervisor Prior to Repositioning Valve P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY In MU Pump Discharge PT MU26 Transmitter H-6 PTMU26 Service RCP Seal Inj FT-MU 19 Inlet Source H-6 MU 19A Open l RCP Seal Inj FT-MU 19 Outlet Source H-6 MU 19B Open l In RCP Seal Injection Flow Transmitter H-6 FTMU19 Service RCP Seal Inj Flow Control Inlet Isolation H-6 MU 214 Open RCP Seal Inj Flow Control Outlet Isolation H-6 MU 215 Open
~
RCP Seal Inj Flow Control Bypass H-6 MU 216 Closed Hydro Test Pap Disch Stop Valve J-6 MU 299 Closed Hydro Test Pop Disch Iso Valve J-6 MU 298 Closed
._ RM 304 Purif Demin 1-1, 1-2, 1-3 Vent Line Drn to Sta Vent C-11 MU 449 Closed l RM 314 l
l Purif Demin 1-1, 1-2, 1-3 Vent Isolation l to Sta Vent C-11 MU 440 Closed I l Purif Demin 1-1, 1-2, 1-3 Vent Line Den to Sta Vent C-11 MU 448 Closed RM 107 Makeup Tank 1-1 Vent Line Drain G-11 MU 441 Closed 4EST STAIRhELL Makeup Tank 1-1 LT MU 16-1 Inlet Source H-10 MU 16B Open Makeup Tank 1-1 LT MU 16-1 Inlet Source H-10 MU 16A Open l l LT MU In Makeup Tank 1-1 LT MU 16-1 H-10 16-2 Service Makeup Tank 1-1 LT MU 16-2 Inlet Source H-10 MU 16D Open t l l t I
. ...: . _, ..- - _.~...-. - .- .
j . . 1 I-62 SP 1104.02.14 . ~~ i -
- Sheet No. 5 VALVE VERIFICATION LIST A ./
Makeup and Purification System of 25 7, Normal /Prestartup Lineup Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve f f P&ID No. VALVE VALVE VERIFY j VALVE DESCRIPTION Coord. NUMBER POSITION BY Makeup Tank 1-1 LT MU 16-2 Inlet Source H-10 MU 16C Open . LT MU In f Makeup Tank 1-1 LT MU 16-2 H-10 16-1 Service i Makeup Tank 1-1 Press Trans (NU 21) { Source H-9 MU 21 Open i In Makeup Tank 1-1 Press Trans H-9 PTMU21 Service ! RM 209 l 1 Purification Demin Filter Backwash Drain C-10 MU 103 Closed Makeup Filter 1-1 Resin Disch to Stor Tk D-9 MU 171 Closed I Makeup Filter 1-1 Vent E-8 MU 174 Closed Makeup Tank 1-1 Outlet Line Vent to RC 1 Dr Tk J-10 MU 430 Closed l' { Makeup Tank 1-1 Outlet Line Den to RC Den Tk J-10 MU 431 Closed
\[}
1. !. Makeup Tank 1-1 Outlet Iso to RC Den Tk J-10 MU 189 Closed l l Purification Demin Filter Vent C-10 MU 99 Closed i a Makeup Filter 1-2 Inlet Line Vent D-9 MU 165 Closed l f l Makeup Filter 1-2 Vent D-9 MU 166 Closed Makeup Filter 1-2 Resin Disch to Stor Tk D-9 MU 170 Closed RM 20% [ !- Seal Return Clr 1-2 CCW Source to ! FI 2642 E-7 CC2642A Open Seal Return Clr 1-2 CLW Source to , FI 2642 E-7 CC2642B Open Seal Return Clr 1-2 CCW Flow Indicator M-036 In i (FI2638) E-7 FI 2642 Service l Seal Return Clr 1-2 CCW Inlet Iso E-7 CC 71 Open Throttled
, Seal Return Clr 1-2 CCW Outlet Iso 6E-7 CC 75 (40 ape) i L.
63 SP 1104.02.18 l Sheet No. 6 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List Only - Consult Shif t Supervisor Prior to Repositioning Valve - P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY M-031 RCP Seal Return Cooler Sample Isolation E-7 SS 15 Closed RCP Seal Return Inlet Leak Test for MU 38 E-5 MU 266 Closed RCP Seal Return Outlet Leak Test for MU 38 E-6 MU 267 Closed RCP Seal Return Cooler 1-1 Inlet Locked Isolation D-7 MU 269 Open i RCP Seal Return Cooler 1-1 Outlet 18 , Isolation D-7 MU 271 Closed 2 Seal Return Clr 1-1 & 1-2 CCW in Test M-036 Pres Source D-7 CC 3726 Closed Seal Return Cooler 1-1 CCW Drain Valve D-7 CC 79 Closed Seal Return Cooler 1-1 CCW Vent Valve D-7 CC 77 Closed Seal Return Clr 1-1 CCW Out Test Press
- Press Source D-7 CC 3722 Closed Seal Return Clr 1-1 CCW Source to FI 2638 D-7 CC2638A Open Seal Return Clr 1-1 CCW Source to FI 2638 D-7 CC2638B Open Seal Return Cooler 1-1 CCW Flow (FI 2638) In Indicator D-7 FI 2638 Se rvice Seal Return Cooler 1-1 CCW Inlet Iso D-7 CC 72 Open Throttled Seal Return Cooler 1-1 CCW Outlet Iso D-7 CC 76 (40 gpm)
RCP Seal Return Cooler 1-1 Inlet M-031 Locked Isolation D-7 MU 268 lOpen! RCP Seal Return Cooler 1-2 Outlet Locked Isolation D-7 MU 270 Open 2 RCP Seal Return Cooler Outlet Line Drain D-7 MU 272 Closed M-036 Seal Return Cooler 1-2 CCW Drain Valve E-7 CC 80 Closed Seal Return Cooler 1-2 CCW Vent Valve E-7 CC 78 Closed Seal Return Clr 1-2 CCW Out Test Press Source E-7 CC 3723 Closed t Controlled per AD 1839.02 18 2 If Seal Return Cooler 1-1 is put in service MU271 and MU270 can both be open with Shift Supervisor direction, but at least one of them must be open.
^ . - . . . - - .~^ .. L. . . .
64 SP 1104.02.14 ~
\
Sheet No. 7 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List Only - Consult Shif t Supervisor Prior to Repositioning Valve P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY M-031 Locked MU Pump Min Recire Iso V1v E-6 MU 479 Open! Makeup Tank 1-1 Outlet Iso to RC Train M-040A Tk Hde F-8 MU 292 Open Isolation Valve Leak Test Before MU 3 C-5 MU 7r Closed Isolation Valve Leak Test After MU 3 C-5 T1 80 Closed Letdown Line Drain Downstream of MU 3 C-5 MU 81 Closed Letdowr. Line Sample Isolation to Per Sample C-5 SS 25 Closed Letdown Line Sample Stop Valve to Per Sample C-5 SS 24 Closed Letdown Line RO MU 5 Bypass Vent B-6 MU 82 Closed B-7 Closed
^
Letdown Line R0 MU S Bypass MU 83
~
Letdown R0 MU 5 Outlet Isolation C-7 MU 87 Open Letdown Flow Control Line Vent C-6 HU 84 Closed Letdown FC Inlet Isolation to MU 6 C-7 MU 85 .open M-031 Letdown FC Outlet Isolation C-7 MU 86 Open DH Remaval Clr Outlet to Letdown Line C-8 DH 123 Closed Letdown FE MU 7 Inlet Line Drain C-8 MU 88 Closed Letdown FT MU 7 Inlet Source C-8 MU 7A Open Letdown FT MU 7 Outlet Source C-8 MU 7B Open In Purif Demineralizer Filters LD Flow Trans C-8 FT MU 7 Se rvice Letdown FE MU 7 Outlet Line Vent C-8 MU 89 Closed Letdown Line PT MU 9 Source C-9 HU 9 Open a 1 Controlled per AD 1839.02 i
65 SP 1104.02.14 Q,
' ' _i Sheet No. 8 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List Only - Consult Shift Supervisor. Prior to Repositioning Valve -
P&ID No. VALVE
- VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY In Letdown Prefilter PI MU 9 B-8 PT MU 9 Service Letdown FE MU 7 Outlet Line Drain C-9 MU 90 Closed Letdown Sample Isolation C-8 SS 26 Closed Boron Analyzer (AE 1999) Inlet Source C-9 MU1999A Open Boron Analyzer (AE 1999) Outlet Source C-9 HU1999B Onen In Boron Analyzer C-9 AE 1999 Service Letdown Isolation to Desin Filter C-9 MU 91 Open Boron Analyzer Drain La Den Viv C-9 MU1999C Closed i
/. Boron Analyzer Ven La V1v C-9 MU1999D Closed b]l Failed Fuel Detector RE 1998 In C-9 RE 1998 Service Throttled /
~
RCP 1-1-1 Seal Inj Needle H-4 MU 232 1 Turn Open RCP 1-1-1 Seal Inj (FT MU 306) Inlet Source H-4 MU 30C Open RCP 1-1-1 Seal Inj (FT MU 30C) Outlet Source H-4 MU 30C Open i ' ~ In RCP 1-1-1 Seal Inj Flow Transmitter H-4 FTMU30C Service Inlet Leak Test Isolation for MU 66C H-3 MU 236 Closed w* RCP 1-1-1 Seal Inj Flow Isolation H-3 MU 66C Open Outlet Leak Test Isolation for MU 66C H-3 MU 240 Closed Throttled / i RCP 1-1-2 Seal Inj Needle H-4 MU 223 1 Turn Open i RCP 1-1-2 Seal Inj (FT MU 30D) Inlet { Source H-4 MU 30D Open i RCP 1-1-2 Seal Inj (FT MU 30D) Outlet .l Open }
.; Source iH-4 MU 30H ,
'dControl Room Operated Valve
- L. . ~ . .. - --..-.. - .- . - . - - - - -- - . - -- -
66 SP 1104.02.14 - Sheet No. 9 VALVE VERIFICATION LIST A ' of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve "' P&ID No. VALVE V LVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY In RCP 1-1-2 Seal Inj Flow Transmitter H-4 FTNU30D Se rvice Inlet Leak Test Isolation Valve for MU 66D H-3 MU 237 Closed RCP 1-1-2 Seal Inj Flow Isolation H-3 MU 66D Open Outlet Leak Test Isolation Valve for MU 66D H-3 MU 241 Closed Throttled RCP 1-2-1 Seal Inj Needle H-4 MU 230 1 Turn Open RCP 1-2-1 Seal Inj (FT MU 30A) Inlet Source K-4 MU 30A Open RCP 1-2-1 Seal Inj (FT MU 30A) Outlet ' Source K-4 MU 30E Open In RCP 1-2-1 Seal Inj Flow Transmitter K-4 FTMU30A Se rvice Inlet Leak Test Isolation Valve for MU 66A K-3 MU 234 Closed ~~'. RCP 1-2-1 Seal Inj Flow Isolation K-3 MU 66A Open Outlet Leak Test Isolation Valve for MU 66A K-3 MU 238 Closed Throttled ~ RCP 1-2-2 Seal Inj Needle J-4 MU 231 1 Turn Open RCP 1-2-2 Seal Inj (FT MU 30B) Inlet Source J-4 MU 30B Open RCP 1-2-2 Seal Inj (FT MU 30F) Outlet j Source J-4 MU 30F Open In RCP 1-2-2 Seal Inj Flow Transmitter J-4 FTMU30B Se rvice Inlet Leak Test Isolation Valve for MU 668 J-3 MU 235 Closed RCP 1-2-2 Seal Inj Flow Isoaltion J-3 MU 66B Open Outlet Leak Test Isolation Valve for MU 66B M-3 MM 239 Closed RM 212 LOWER M-031 i Wye Strainer PDI 1846 Inlet Source E-11 1 MU1846Ae0 pen 4
** Control Room Operated Valve l
l l l
- =
67 SP 1104.02.14 O. Jr Sheet No. 10 VALVE VERIFICATION LIST A - of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List Only - Consult Shif t Supervisor Prior to Repositioning Valve - P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY Wye Strainer PDI 1846 Outlet Source E-11 MU1846B Open In Wye Strainer PDI 1846 Instr E-11 PDI1846 Se rvice Three-Way (MU 11) Inlet Isolation E-10 MU 147 Open Three-Way (MU 11) Outlet Isolation E-10 MU 14B Open Mixed Bed 1-2 Outlet Line Multipurpose E-12 MU 114 Closed ! Mixed Bed 1-1 Spent Resin Drain D-11 MU 134 Closed - Wys Strainer Drain E-11 MU 145 Closed MU Filter Outlet Return to Demineralizers C-10 MU 97 Closed Purification Demin Filter Outlet Isolation C-10 ' MU 96 Open Mixed Bed 1-1 Outlet Line Multipurpose D-11 MU 115 Closed Makeup Filter 1-2 Inlet Line Drain D-9 MU 164 Closed Purification Demin Filter Outlet Drain C-10 MU 102 Closed Purif Demin Filter PDT-MU62 Inlet Source B-10 MU 62A Open Purif Demin Filter PDT-MU62 Outlet Source B-10 MU 62B Open In Prefilter 1-1 PDT MU 62 Instr - B-10 PDTMU62 Se rvice Makeup Tank 1-1 Vent Inlet Iso to MU 14 G MU 395 Closed Mixed Bed 1-2 Spent Resin Drain D-12 MU 135 Closed Cation Bed Outlet Line Multi-purpose E-13 MU 113 Closed i Makeup Filter 1-2 Inlet Isolation D-9 MU 159 Open I Makeup Filter 1-1 & 1-2 Bypass E-9 MU 158 Closed Purif Demin Filter Bypass to Makeup l l Filter' iD-9 PRJ 93 (Closed , m I
4 . . l h 68 SP 1104.02.14 ,_ I Sheet No. 11 VALVE VERIFICATION LIST A j- of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List only - Consult Shift Supervisor Prior to' Repositioning Valve - P&ID No. VALVE VALVE VERIFY l - VALVE DESCRIPTION Coord. NUMBER POSITION BY Cation Bed 1-3 Spent Resin Drain D-13 MU 136 Closed Demin Wtr Backwash Valve to Purif Demin i Filter B-10 PW 8 Closed Makeup Filter 1-1 & 1-2 PDT MU 13 Inlet Source E-9 NU 13A Open Makeup Filter 1-1 & 1-2 PDT MU 13 Outlet Source E-8 MU 138 Open In Makeup- Filter 1-1 & 1-2 PDT MU 13 E-8 PDTMU13 Service Purification Demin Filter Inlet Drain C-9 NU 101 Closed . Makeup Filter 1-1 Inlet Line Drain E-9 MU 173 Closed l Demin Wtr Supply to Purification Demin's B-14 DW 67 Closed I' Purification Demin Filter Inlet C-9 MU 94 Open
'T i Purification Demin Filter PDT-1911 Inlet- +c
- Source B-10 MU1911A Open
, Purification Demin Filter PDT-1911 Outlet l Source B-10 MU1911B Open In Letdown Prefilter PDT Instrument- B-10 PDT1911 Service Makeup Filter 1-2 Sample I .olation D-8 SS 16 Open Makeup Filter 1-2 Outlet Isolation D-8 MU 161 Open i a Makeup Filter 1-1 Outlet Isolation D-8 MU 177 Open Makeup Filter 1-2 Inlet Line Drain D-9 MU 433 Closed Makeup Filter 1-2 Outlet-Line Drain D-8 MU 168 Closed Makeup Filter 1-1 Outlet Line Drain E-8 MU 436 Closed j Makeup Filter 1-2 Refill Isolation D-8 MU 163 Closed . Makeup Filter 1-1 Refill Isolation D-8 MU 172 Closed ! F-10 ,I Batch Feedline Iso to Misc Waste Dr Tk , MU 155 , Closed i i 8
,. ..,,-,.~3 - _ , , _ . , , , _ , -,,x_,,,.-,..-.,_,,L_,,,,y,_,..,,., ,y,, _ _ _ _ . . , , , , . _ , , , , _ . _ . , , , , . ., __.y_,,,
\
s 69 SP 1104.02.14 Sheet No. 12 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve P&ID No. ' VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY Batch Totalizer Outlet Isolation F-11 MU 153 Open Batch Totalizer Bypass F-11 MU 154 Closed Batch Totalizer Inlet Isolation F-11 MU 152 Open Demin Wtr Inlet to FI 1901 Source B-14 DW1901A Open Demin Wtr Outlet to FI 1901 Source B-14 DW1901B Open In Demin Wtr FI 1901 to Purif Demin B-14 FI1901 Service RM 212 UPPER - Purification Demin Drain to Misc Waste Den Tk D-14 MU 112 Closed l ' N 2 /Demia Supply to Purif Demin C-14 MU 111 Closed MU System PW Fill Valve D-11 MU 116 Closed Mixed Bed 1-1 Outlet D-11 MU 139 Open Demin Multipurpose D-14 MU 133 Closed Purif Demin Bypass Vent C-11 MU 105 Closed Sealed Purification Demin Bypass C-11 MU 104 Closed Mixed Bed 1-1 Misc Inlet or Outlet C-12 MU 124 Closed Bixed Bed 1-1 Vent C-11 MU 106 Closed N 2 /Demin Supply to Purif Demin C-14 MU 110 Closed Mixed Bed 1-2 Inlet or Outlet C-12 MU 125 Closed Mixed Bed 1-1 Inlet Line Vent C-11 MU 127 Closed Mixed Bed 1-1 Inlet (MU 10A) Bypass C-11 MU 278 Closed Mixed Bed 1-2 Inlet (MU 10B) Bypass C-12 MU 279 l Closed , .
. . . . _ ~ - . ._ ..- . -- .- . . .. .- . . _ .
i 70 SP 1104.02.14 Sheet No. 13 VALVE VERIFICATION LIST A - of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve P&ID No. VALVE VALVE VERIFY i VALVE DESCRIPTION Coord. NUMBER POSITION BY I Mixed Bed 1-2 Vent C-12 MU 107 Closed I Mixed Bed 1-2 Inlet Line-Vent C-12 MU 128 Closed ) I Mixed Bed 1-2 Outlet D-12 MU 140 Open ,
; Mixed Bed 1-1 Outlet to Cation Bed Line D-12 MU 119 Closed Mixed Bed 1-2 Outlet to Cation Bed Line D-12 MU 121 Closed Cation Bed 1-3 Vent- C-13 MU 108 Closed N2/Desin Supply to Purif Demin B-14 MU 381 Open ;
Cation Bed 1-3 Inlet Line Vent C-13 MU 129 Closed Cation Bed 1-2 Inlet Line Vent C-13 MU 129 Closed . T, l ; i Cation Bed 1-3 Inlet or Outlet C-13 MU 126 Closed j Cation Bed 1-3 Outlet E-13 MU 141 Open l- Primary Str Supply to Purification
, Demin's B-13 PW 28 Closed i
t Purification Demin Filter Inlet Vent C-10 MU 98 Closed ! N2 Supply Isolation to Purification i Desin B-13 NN 103 Closed 1 [ Purification Demin Filter Outlet Vent C-10 MU 100 Closed i Makeup Filter 1-1 Inlet Line Vent D-9 MU 435 Closed i i Makeup Filter 1-2 Inlet Line Vent D-9 MU 434 Closed Locked . Makeup Tank 1-1 Inlet Isolation G-9 MU 182 Open Makeup Filter 1-2 Isolation D-8 MU 162 Open t Makeup Filter 1-2 Outlet Line Vent D-8 MU 167 Closed I Makeup Tank & Pumps Bypass'Line Vent l G-7 i MU 180 .' Closed : J 4 1
- . . - . . , . . _ _ . - . - . _ , ._.__,____._._,....._._,..,_,__._..m_._ - . - , , _ _ . . , _ . , . . _ . , . .- , . , . _ , . _ _ . _
. < s 71 SP 1104.02.14 (R.
. Sheet No. 14 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY MU Flow to DH Removal Pump suct Line Vent F-7 MU 276 Closed Makeup Flow to DH Removal Pump Suct F-7 MU 274 Closed Makeup Filter 1-1 Outlet Line Vent E-8 MU 175 Closed Batch Flow Controller Bypass F-12 MU 151 Closed Batch Flow Controller Inlet Isolation F-12 MU 149 Open Batch Flow Controller Outlet Isolation F-12 MU 150 Open RM 225 M-031 MU Pumps Suction Line Vent J-9 MU 444 Closed
~
MU Pump 1-1 & 1-2 Suetiou Sample Iso J-10 SS 18 Open l
-- Locked MU Pump 1-1 Inlet Isolation J-8 MU 191 Open!
MU Pump 1-1 Suction Line Flush J-8 MU 193 Closed MU Pump 1-1 Suction Press Source H-8 MU 1895 Open In MU Pump 1-1 Suction Press Indicator H-8 PI1895 Se rvice ! MU Pump 1-1 Discharge Press Source H-8 MU 25A Open 1 In l MU Pump 1-1 Discharge Pump Indicator H-8 PIMU25A Se rvice l l MU Pump 1-1 Discharge Line Flush Iso H-8 MU195A Closed 1 MU Pump 1-1 Discharge Line Flush Vent H-8 MU 429 Closed Locked MU Pump 1-1 Recire Iso to Seal Return H-7 MU 205 Opent Locked MU Pump 1-1 Recire Stop to Seal Return H-7 MU 206 Open! MU Pump 1-1 Outlet Isolaiton H-7 MU 199 iOpen 1 Controlled per AD 1839.02 1
~n 1
d 72 SP 1104.02.14 .s
- 1
- Sheet No. 15 VALVE VERIFICATION LIST A
! of 25 Makeup and Purification System Normal /Prestartup Lineup Ver'.fication List Only - Consult Shift Supervisor Prior to Repositioning Valve P&ID No. ' VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY
- MU Pump 1-1 CCW Inlet Stop Check to M-036 I Lube Oil Cirs J-10 CC 127 Open i MU Pump 1-1 CCW Lube Oil Clr (FI 2190) l Source Viv J-10 CC2190A Open MU Ptamp 1-1 CCW Lube Oil Cirs (FI 2190)
Source Viv J-10 CC21908 Open
- MU Pump 1-1 CCW Lube Oil Clrs In
; Indicator J-10 FI2190 Service MU Pump 1-1 CCW Out Stop Check from Lube Throttled Oil Cirs J-10 CC 129 (12 apa)
MU Pumps Discharse Line Vent H-7 MU 200 Closed Scaled l High Pressure Line Flow Test Isolation G-6 MU 208 Closed i Normal Makeup Flow (FT MU 31) Inlet Source F-6 MU 31A Open Normal Makeup Flow (FT MU 31) Outlet Source F-6 MU 31B Open } M-031 In ? Normal Makeup Flow Transmitter F-6 FTMU31 Service ! Normal Makeup Flow Controller Inlet 3 Isolation F-6 MU 209' Open Normal Makeup Flow Controller Outele
- Isolation F-6 MU 210 Open Normal Makeup Flow Controller Line Drain F-5 MU 212 Closed i
Normal Makeup Flow Controller Bypass F-6 MU 211 Closed
- Normal Makeup Flow (FE MU 58) Source /
) Needle F-6 MU 58A Open i ! Normal Makeup Flow (FE MU 58) Source F-5 MU 58B open Sealed 1 Makeup Tank & Pumps Bypass H-7 MU 178 Closed MU Pump 1-1 Seal Water Vent H-8 MU 34 Closed MU Pump 1-1 Seal Water Vent H-8 MU 35 Closed l MU Pump 1-2 Seal Water Vent J-8 MU 36 Closed l I MU Pump 1-2 Seal Water Vent ,J-8 iMU 37 tClosed < i i I
. _ - , . . - . _ , -. . _ . . - _ . _ _ _ , . _ . - _ _ _ _ , . _ . ~ . . . . _ . _ _ _ , _ , , _ _ _ - _ _ . . _ . , _ . _ _ _ , - . _ . _ . _ _ - -
l l - 73 SP 1104.02.14
.' 'O Sheet No. 16 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup i
- Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve P&ID No. VALVE VALVE VERIFY L
VALVE DESCRIPTION Coord. NUMBER POSITION BY High Press Line Flow Test Vent G-6 MU 439 Closed 1
! Makeup Tank 1-1 Outlet Line Drain J-9 MU 443 Closed Locked MU Pump 1-2 Inlet Isolation J-9 MU 190 Open 1 l MU Pump 1-2 Suction Line Flush J-8 MU 192 Closed t
MU System Hydro Test Connection Valve J-9 NU467 Closed e i MU Pump 1-2 Suction Press Source J-S MU 1896 Open In - j MU Pump 1-2 Suction Press Indicator J-9 PI 1896 Se rvice i MU Pump 1-2 Discharme Press Source- J-8 MU 25B Open In MU Pump 1-2 Discharge Press Indicator J-8 Service PIMU25B
~ M' 5 MU Pump 1-2 Discharme Line Flush Iso J-8 MU 194 Closed MU Pump 1-2 Discharte Line Flush Vent J-8 MU 42B Closed Locked l MU Pump 1-2 Recire Iso to Seal Return J-7 MU 202 Openi j ~
Locked MU Pump 1-2 Recire Stop to Seal Return J-7 MU 203 Open1 ! MU Pump 1-2 Outlet Isolation J-7 MU 198 Open MU Pump 1-2 CCW in Stop Check to Lube M-036
- Oil Clrs J-11 CC 128 Open MU Pump 1-2 CCW Lube Oil Clr (FF2190)
Source Viv J-11 CC2191A Open
, MU Pump 1-2 CCW Lube Oil Clr (FI2190)
Source Viv J-11 CC2191B Open , i MU Pump 1-1 CCW Lube Oil Clr Flow In l ! Indicator J-11 FI 2191 Se rvice l l MU Pump 1-2 CCW G 4 Stop Check from . Throttled ' Lube Oil Clr J-11 CC 130 (12 aps) l RM 227 ! l 1 Controlled per AD 1839.02 1 j - I 1 l . l
. 1
a i +
- j. 74 SP 1104.02.14 Sheet No. 17 VALVE VERIFICATION LIST A -
I of 25 Makeup and Purification System Normal /Prestartup Lineup f Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve i P&ID No. VALVE VALVE VERIFY j VALVE DESCRIPTION Coord. NUMBER POSITION BY
- Purif Demin to Misc Waste Den Tk Line M-031 f Drain B-13 MU 445 Closed Purif Demin to Misc Waste Den Tk Line
,1- Drain B-13 MU 446 Closed RM 236 , In j-Normal Makeup Flow Indicator F-5 FIMU58 Service i Normal Makeup Flow Line Leak Test Conn F-5 MU 452 Closed
*** INACCESSIBLE
! Purif Demin to Misc Waste Den Tk Line *** ! Drain B-13 MU 447 Closed j ***
- Makeup Tank 1-1 N2 & H2 Inlet Isolation H-10 MU 188 Open -
Makeup Tank 1-1 Outlet Line Vent J-9 MU 390 Closed , j ***
- Makeup Tank 1-1 Outlet Line Vent J-9 MU 388 Closed i ***
! Makeup Tank 1-1 Outlet Line Drain J-9 MU 389 Closed Spent Resin Tk Overflow Pup to Purif *** l Demin Vent B-14 WC 116 Closed i ***
! Makeup Tank 1-1 Sample Isolation H-10 SS 17 Open l Makeup Tank 1-1 Inlet Line Vent G-9 MU 184 Closed 1 Mixed Bed 1-1 Outlet to Cation Bed Line- ***
i Drain D-11 MU 118 Closed Mixed Bed 1-1 Outlet to Cation Bed Line *** i ! Vent D-11' MU 117 Closed Mixed Bed 1-2 Outlet to Cation Bed Line *** ! Drain D-12 MU 123 Closed i *** ! Mixed Bed 1-1 Outlet Line Drain D-11 MU 137 . Closed I' ! l*** 6 ! Mixed Bed 1-2 Outlet Line Drain D-12 lMU 138 1 Closed i I
***These ralves are inaccessible and need not be checked unless the Shift 4 Supervisor determines it necessary due to maintenance or evolutions j being performed in the area.
1
. - _ _ _ . - . - - - _ . _ . _., -. . , _ _ _ . - _ . _ . . - _ _ . . _ , - _ , . . _ _ . - . , . . . - . _ _ . _ _ - . _ _ . ~ - _ .
75 SP 1104.02.14
/* Sheet No. 18 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List Only - Consult Shif t Supervisor Prior to Repositioning Valve -
P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY Batch Feed Line Drain F-10 MU 156 Closed Batch Feed Line Vent E-10 MU 157 Closed Makeup Tank 1-1 Vent Outlet Iso to *** MU 14 G-10 MU 158 Closed Makeup Tank 1-1 Inlet Line Vent G-9 MU 183 Closed Makeup Tank 1-1 Inlet Line Drain G-9 MU 386 Closed Batch Feedline Vent to Misc Waste Dr Tk F-10 MU 438 Closed Batch Feedline Drain to Misc Waste Dr Tk F-9 MU 437 Closed Sample System Line from Mixed Bed 1-1 *** Outlet D-10 SS 19 Open Sample System Line from Mixed Bed 1-2 *** i f- s Outlet E-12 SS 20 10 pen ( ' ', *** Cation Bed Outlet Sample Line E-13 SS 21 Open Cation Bed Outlet Sample Isolation D-8 SS 22 Open Sampling Sys Return to MU & Purif Sys E-9 SS 501 Open Sampling Sys Return to MU & Purif Sys E-9 SS 502 Open Sampling Sys Return to MU & Purif1Sys E-9 SS 503 Open Sample Sys Valve Upstream of Thres-way *** Viv D-11 SS 137 Open Resin Outlet from Demin's Flush Valve E-11 MU 432 Closed RCP 1-2-2 Controlled Bleedoff Line Vent G-1 MU 419 Closed RCP 1-2-2 Controlled Bleedoff Line Vent F-1 MU 420 Closed (.
,RCP 1-2-2 Controlled Bleedoff Line Vent F-1 .MU 421 , Closed >
***These valves are inaccessible and need not be checked unless the Shift Supervisor determines it necessary due to maintenance or evolutions being performed in the area.
l . . - i
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I 76 SP 1104.02.14 _ 1
- Sheet No. 19 VALVE VERIFICATION LIST A / l of 25 Makeup and Purification System I Normal /Prestartup Lineup Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve -
1 P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY RCP 1-2-2 Controlled Bleedoff Line Vent F-1 MU 422 Closed RCP 1-2-2 Controlled Bleedoff Line Drain F-1 MU 413 Closed RCP 1-2-2 Controlled Bleedoff Line Drain F-1 MU 414 Closed RCP 1-2-2 Controlled Bleedoff Line Drain F-1 MU 415 Closed RCP 1-2-2 Seal Return Leak Test E-2 MU 251 Closed
** Open/
RCP 1-2-2 Seal Return Isolation E-2 MU 59B Closed RCP 1-2-2 Seal Return (FE-MU 60B) Inlet Iso E-4 MU 255 Open RCP 1-2-2 Seal Return (FE-MU 60B) Outlet Iso E-4 -MU 259 Open In RCP 1-2-2 Seal Return Flow Transmitter E-4 FIMU60B Service N
)
RCP 1-2-2 Seal Return FE-MU60B Bypass E-4 MU 263 Closed RCP 1-2-2 Seal Inj Line Drain (CTMT) J-1 MU 287 Closed RCP 1-2-2 Seal Inj Line Drain (CTMT) J-1 MU 288 Closed RCP 1-2-2 Seal Inj Line Vent J-2 MU 457 Closed RCP 1-2-2 Seal Inj Line Vent J-2 MU 456 Closed RCP 1-2-2 Seal Inj Line Vent H-2 MU 473 Closed RCP 1-2-2 Seal Inj Line Drain J-2 MU 459 Closed RCP 1-2-2 Seal Inj Line Drain J-2 MU 458 Closed RCP 1-2-2 Seal Inj Line Vent H-3 MU 472 Closed Sealed I RCP 1-2-2 Seal Inj Stop Check J-2 MU 243 Open I RCP 1-2-2 Seal Inj Stop Check J-2 iMU 328 Open
**CTRM viv.
i ( w ,- - --, - - , , - - -,
77 SP 1104.02.14 8 Sheet No. 20 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List only - Consult Shift Supervisor Prior to Repositioning Valve -- P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY RCP 1-2-2 Seal Inj Line Vent J-2 NU 404 Closed RCP 1-2-2 Seal Inj Line Vent J-2 MU 405 Closed RCP 1-2-2 Seal Inj Line Vent J-2 MU 406 Closed RCP 1-2-2 Seal Inj Line Drain J-2 NU 283 Closed RCP 1-2-2 Seal Inj Line Drain J-2 NU 284 Closed RCP 1-2-2 Seal Inj Line Vent (CTMT) J-1 NU 407 Closed RCP 1-2-2 Seal Inj Line Vent (CTMT) J-1 MU 408 Closed RCP 1-2-2 Seal Inj Line Vent (CTMT) J-1 MU 409 Closed
-~. RCP 1-2-2 Seal Inj Line Drain (CTMT) J-1 MU 285 Closed
.i RCP 1-2-2 Seal Inj Line Drain (CTMT) J-1 MU 286 Closed RCP 1-2-2 Seal Inj Stop Check Leak Test- J-2 NU 247 Closed RCP 1-2-1 Seal Inj Line Drain K-2 MU 280 Closed RCP 1-2-1 Seal Inj Line Drain K-2 MU 281 Closed RCP 1-2-1' Seal Inj Line Drain (CTMT) K-1 NU 282 Closed RCP 1-2-1 Seal Inj Line Vent K-2 NU 461 Closed RCP 1-2-1 Seal Inj Line Vent K-2 NU 460 Closed RCP 1-2-1 Seal Inj Line Vent K-2 MU 474 Closed RCP 1-2-1 Seal Inj Line Drain K-2 MU 463 Closed RCP 1-2-1 Seal Inj Line Drain K-2 MU 462 Closed RCP,1-2-1 Controlled Bleedoff Line Vent E-1 MU 417 Closed RCP 1-2-1 Controlled Bleedoff Line Vent .E-1 ,NU 418 i Closed
~.
. ~ .
s 78 SP 1104.02.14 , Sheet No. 21 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup 1 Verification List Only - Consult Shif t Supervisor Prior to Repositioning Valve P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY RCP 1-2-1 Controlled Bleedoff Line Drain E-1 MU 410 Closed RCP 1-2-1 Controlled Bleedoff Line Drain E-1 NU 411 Closed I RCP 1-2-1 Controlled Bleedoff Line Drain E-1 MU 412 Closed i RCP 1-2-1 Seal Return Leak Test D-1 MU 250 Closed
** Open/
- RCP 1-2-1 Seal Return Isolation D-2 MU 59A Closed i
RCP 1-2-1 Seal Return (FE MU60A) Inlet Iso D-3 MU 254 Open RCP 1-2-1 Seal Return (FE MU60A) Outlet Iso D-4 MU 258 Open In RCP 1-2-1 Seal Return Flow Transmitter D-4 FTMU60A Se rvice RCP 1-2-1 Seal Return RE MU 60A Bypass D-4 MU 262 Closed j RCP Seal Return Line Vent E-5 MU 309 Closed Sealed RCP 1-1-2 Seal Inj Stop Check H-3 MU 245 Open RCP 1-1-2 Seal Inj Stop Check Leak Test H-2 MU 249 Closed 4 RCP 1-1-2 Seal Inj Line Vent H-2 MU 451 Closed ' RCP 1-1-2 Seal Inj Stop Valve H-2 MU 326 Open RCP 1-1-2 Seal Inj Line Drain H-2 MU 289 Closed RCP 1-1-2 Seal Inj Line Veat G-2 MU 464 Closed RCP 1-1-2 Seal Inj Line Vent G-2 MU 477 Closed RCP 1-1-2 Seal Inj Line Vent G-2 MU 476 Closed RCP 1-1-2 Seal Inj Line Vent G-2 MU 455 Closed RCP 1-1-2 Seal Inj Line Vent G-2 MU 454 , Closed i
**CTRM viv.
s e , 79 SP 1104.02.14
,. m
, Sheet No. 22 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List only - Consult Shift Supervisor Prior to Repositioning Valve 1
P&ID No. ' VALVE VALVE VERIFY VALV2 DESCRIPTION Coord. fNUMBER POSITION BY RCP 1-2-2 Seal Inj Line Drain G-1 MU 478 Closed , _ _ RCP 1-2-1 Controlled Bleedoff Line Vent E-1 MU 416 Closed RCP 1-2-1 Seal Inj Line Drain K-2 MU 475 Closed 1 j RCP 1-P 1 Seal Inj Stop Check Leak Test K-2 MU 246 Closed Scaled K-2 Open RCP 1-2-1 Seal Icj Stop Check MU 242 CTNT RCP 1-2-1 Seal Inj Stop Valve K-2 MU 329 Open RCP 1-2-1 Seal Inj Line Vent K-2 MU 401 Closed RCP 1-2-1 Seal Inj Line Vent K-2 MU 402 Closed
! RCP 1-2-1 Seal Inj Line Vent K-2 MU 403 Closed RCP 1-1-1 Seal Return Leak Test F-2 MU 252 Closed
- Open/
RCP 1-1-1 Seal Return Isolation F-2 l*MU59CClosed RCP 1-1-1 Seal Return (FE MU 60C) Inlet Iso F-4 MU 256 Open RCP 1-1-1 Seal Return (FE MU 60C) Outlet Iso F-4 MU 260 Open In RCP 1-1-1 Seal Return Flow Transmitter F-4 FTMU60C Service Sealed RCP 1-1-1 Seal Inj Stop Check H-2 MU 244 Open RCP 1-1-1 Seal Inj Stop Check Leak Test H-2 MU 248 Closed RCP 1-1-1 Seal Inj Line Vent H-2 MU 450 Closed - RCP 1-1-1 Seal Inj Stop Valve H-2 MU 327 Open i RCP 1-1-1 Seal Inj Line Vent H-2 MU 466 Closed
**CTRM viv.
i I
a .. e 80 SP 1104.02.14 - Sheet No. 23 VALVE VERIFICATION LIST A , of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY RCP 1-1-1 Seal Inj Line Vent H-2 MU 465 Closed RCP 1-1-1 Seal Return FE MU 60C Bypass F-4 MU 426 Closed RCP 1-1-2 Controlled Bleedoff Line Vent F-2 MU 425 Closed 4 RCP 1-1-2 Controlled Bleedoff Line Vent F-2 MU 246 Closed RCP 1-1-2 Controlled Bleedoff Line Drain F-2 MU 427 Closed RCP 1-1-2 Seal Return Leak Test F-2 MU 253 Closed
** Open/
- RCP 1-1-2 Seal Return Isolation F-3 MU 59D Closed RCP 1-1-2 Seal Return (FE MU60D)
Inlet Iso F-3 MU 257 Open RCP 1-1-2 Seal Return (FE MU60D) Outlet Iso F-3 MU 261 Open In RCP 1-1-2 Seal Return Flow Transmitter F-2 FTMU60D Se rvice RCP 1-1-2 Seal Return (FE MU60D) Bypass F-3 MU 265 Closed RCP Letdown Clr 1-2 CCW Inlet Test Press Source E-4 CC 2545 Closed RCP Letdown Clr 1-1 and 1-2 Inlet Header Drain X-connect B-2 MU 64 Open RC Letdown Clr 1-2 Inlet Header Drain D-2 MU 69A Closed RC Letdown Clr 1-2 Inlet Header Drain D-2 MU 69B Closed RC Letdown Clr 1-2 CCW Inlet Source M-036 to PSH3712 E-5 CC 3712 Open RC Letdown Clr 1-2 CCW Outlet Source to PSH 3712 F-5 CC 3763 Open RC Letdown Clr 1-2 CCW Vent Valve E-5 CC 100 Closed RC Letdown Clr 1-2 CCW Inlet Isolation E-4 CC 97 Open
- Throttled l ;
RC Letdown Clr 1-2 CCW Outlet Isolation . E-5 .CC 103 Open i
**CTRM viv.
_~ _ __ -_ _ -- - O .. s N 81 SP 1104.02.14 th Sheet No. 24 VALVE VERIFICATION LIST A of 25 Makeup and Purification System Normal /Prestartup Lineup , Verification List Only - Consult Shif t Supervisor Prior to Repositioning Valve ~
'P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY t M-031 Letdown Line Delay Coil Drain C-4 MU 76 Closed Letdown Line Delay Coil Vent C-4 MU 77 Closed Letdown Line Delay Coil Vent C-4 MU 78 Closed . Letdown Line Delay Coil Drain C-4 MU 310 Closed Letdown Coolers Outlet Isolation C-4 HU 2A Open RC Letdown Line Drain C-2 MU 70 Closed 4
RC Letdown Line Vent C-2 MU 71 Closed RC Letdown Cooler Inlet Isolation C-2 MU 2B Open j (, - RC Letdown Line Vent
^
B-2 MU 72 Open RC Letdown Cooler 1-1 Inlet Isolation B-3 MU 1A Open RC Letdown Cooler 1-1 Outlet Stop Check B-3 MU 370 Open M-036 ). RC Letdown Cooler 1-1 CCW Drain Valve D-4 CC 101 Closed t RC Letdown Cooler 1-1 CCW Inlet Test Press Source D-4 CC 2543 Closed RC Letdown Cooler 1-1 CCW Inlet Source I to PSH 3711 ID-5 CC 3711 Open j RC Letdown Cooler 1-1 Outlet Source to PSH 3759 l D-5 3 CC 3755 Open i 4 RC Letdown Cooler 1-1 CCW Vent Valve 3D-4 CC 102 Closed
~
RC Letdown Cooler 1-1 CCW Inlet Isolation. D-4 CC 98 Open Throttled RC Letdown Clr 1-1 CCW Outlet Isolation D-5 CC 104 (400 gpm) M-031 RC Letdown Cooler 1-2 Inlet Line Drain iC-3 MU 73 Open I
! RC Letdown Cooler 1-1 Inlet Header Drain B-2 MU 68A Closed i
**CTRM viv.
= 'e J
I b
a .. s l 82 SP 1104.02.14
-w Sheet No. 25 VALVE VERIFICATION LIST A >
I of 25 Makeup and Purification System Normal /Prestartup Lineup Verification List Only - Consult Shift Supervisor Prior to Repositioning Valve - P&ID No. VALVE VALVE VERIFY VALVE DESCRIPTION Coord. NUMBER POSITION BY
** Closed /
RC Letdown Cooler 1-2 Inlet Isolation C-3 MU IB Open RC Letdown Cooler 1-2 Outlet Stop Check C-4 MU 369 Open j M-036 RC Letdown Clr 1-2 CCV Drain Valve E-4 CC 99 Closed 4
**CTRM viv.
)' Reviewed by Date (Shif t Supervisor or Ass't Shif t Supervisor) T i .
* .Y 1
i i l 1 END
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