ML20086T073
| ML20086T073 | |
| Person / Time | |
|---|---|
| Site: | Beaver Valley |
| Issue date: | 12/27/1991 |
| From: | DUQUESNE LIGHT CO. |
| To: | |
| Shared Package | |
| ML20086S924 | List: |
| References | |
| OST-2.11.14, NUDOCS 9201060121 | |
| Download: ML20086T073 (84) | |
Text
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, B.V.P.S.
- 0.H. g gf,,,g l BEAVER VALLEY POWER STATION k- M 4 AT A-UNIT NO. 2 G6T 2.11.1 0 Page i of e OPERATING SURVE!LLANCE TEST SURVEILLANCE TEST Nor TECIINICAL SPECITICATION KETEkENCE: TREQUENCY: 1 4.0.5 and WNSD Tech. Bulletins l OST 2.11.14 NSD Tb 81 10 and NSD-TB 80 11 R ,
TITLE: SAFETY INJECTION SYSTE!! TULL PLOW TEST '
'0FERATING ?l0DE PERFORF1ED BY: DATE C0f!PLETflii~
_R MUIRING TEST: _1 2 3,4 1 t _ __ ,
TEST RESULTS (To be completed by test performer)
{ } Test completed and SATISFACTORY TOTAL MI.N ilotRS I
( ) The following problems were encountered:
A/dk) AfV/f/#su .Z~W pad 6'fE.S~ ,
F/At ffN~ AAf4MCE 47 JA. _
[ ] Corrective action taken or initiated:
[ ] FfWR NO. (If Written) f TEST REVIEWED BY IST COORDINATOR DATE _
i
~
TEST REVIEWED BY SHIFT SUPERVISOR _ ., DATE
[ ] Procedure properly completed and 'iATISTACTORY
[ j Comments:
lEST REY!EWED BY OPERATING SUPERVISOR DATE _
( ) SATISTACTORY and APPROVED
( ) Connents:
ISSUE I REV 5 9201060121 PDR ADDCK Q $$334 PDR P
m-.,vey,e,.-yf....-r.,-,.m,w.,,,w.w--w.,m._ _ . , . , , .
. - .. -r,.-
4 l l .
. B.V.P.S. 0.H. 2.55A 4 . i OST 2.11.14 Page 2 of 85 !
MFETY INJECTION SYSTEM Tl'LL PLOW TEST PL'RPOSE To demonstrate the operability of the Low Head and liigh llead Safety l Injection System in the injection mode and to perform inservice testing of the system check valves in acuordance with ASME IST Program.
NOTE: Parts A and B of this procedure are written so that tha* ay be accomplished independently of each other.
LOW IIEAD SAFETY INJECTION _Tl".L Flok TEST i [
-A.
ACCEPTANCE CRITERIA PART A AsMgps 1_ . J2SfE*P21A at.d .B: ; Low liend Safety Inicction Pens. operate at 2 the Low liesd Safety In,lection Tump mnmum Operating Curve.
- 2. The check- valves listed on Attachment T operate (forward flow test) within the requirements of the ASMC IST Program (T.S. 4.0.5) (Check valve operation is acceptable as determined using Attachment G;.
- 3. The following check valves operate (forward flow test) within the l requirements of the ASME IST Program (T.E. 4.0.5) (check valve operation is acceptable if 1. above is met).
- a. [2 SIS *6) LilSI Pump 21% Disch Check
- b. . [2 SIS *7) DIS 1 Pump 21B Disch Check INITIAL CONDITIONS - PART A Initials / Date
- 1. NSOF's or NSS's approval has been obtained for the performance of this test. ./ ll
- 2. The operator (s) performing this test have reviewed PART -A of this procedure anJ the applicable
/
Att achtuent s . _
- 3. The Plant is in Mode 5, 6 or 6 with no fuel in vessel. /_ _
- 4. The instruments listed on Data Sheets 2 and 3 are ;
in current calibration. _ /__
- 5. The LHSI Injection and Recirculation Flow Paths are-available, filled and vented. / ,
ISSUE 1 REV 5 -
4 am - ..q, y-. m,-m._m,. ,..,,,,,,m%y.p.m....m .,y,-,,,yy. ,,.w<,,,g. ...,,,,,..,_yp,.r,,.,yy_,,p,gypw ,,,.,ypwg _. ,,,p,.y.,,wyw , , y .w-ww,
(_
e B.V.P.S. 0.M. 2.55A.4 .
OSf 2.11.14 Page 3 of $$
- 6. RWST [2QS5*TK21A] Itoron concent ration is great er than or equal to 2000 ppm. /
l l' 7
[2QSS*L1100A(B)] RWST Level is > La Lo Level Ala rm ;
(440 in.) or transfer to re c i r c u l at i.an phase is defeated and RWST Level is sufficient for LHS! Pump i NPSil requirements > 33 inches indicated. _/ 1 l B. [2R}lS*P21A(b)) RHK Pump is running. /_ l l 9. [2RCS Ll462] PRZR Cold Calibrated Level is 15 to 2S?. when reactor vessel head is installed. __ /
l 10. The pressurizer is vented to Centainment Atmosphere. /
l 11. Overpressure Protection ystem is in service or a 2 3.14 square inch vent ex *ts in the RCS. /
l 12. The IST Coordinator or cesignee is available to support this test. /
- 15. The fuel pool is isolated from the refueling cavity when the reactor vessel head is removed. /
- 14. Radeon has been notified of any anticipated decrease of refueling cavity level. /
PRECAUTIONS AND LIMITATIONS - PART A
- 1. PRZR Cold Cal level shall be maintained between 15-8 0 *. .
l INSTRUCTIONS - PART A initials / Date NOTE: If desired coordinate this procedure with 0.'!- 2 .11. 4 . C " Filling Reactor Refueling Cavity" and/or OM-2.20.4.li " Draining The Refueling Cavity To The RVST".
l 1. Obtain a calibrated portable vibration meter, Bently Nevada Model TK8 or equivalent, and record
'hter I.D. Number and Cal. Duo Date on Data
. 1. /
ISSUE 1 REV 5
. . _ _ - . . . . , , , _ . . . _ , _ - . _ _ _ _ _ _ _ . . , - . _ . _ , . . _ - . . _ _ - . - . _ . - _ - . _ _ _ _ . - - . _ . . . _ . . , , _ u_. _ - , _ - . , . . _ . _
1 B.V.P.S. 0.H. 2,55A 4 .
OST 2.11.14 Page 4 of 85
- 2. Establish communications between the following four locations: LilSI Pumps (Sfsds Elev 718'), the refueling cavity (Cnmt Elev 767') (if head is off), l
[2RilS*15) RWST Outer Centainment Isol (Sfgds Elev 729' in "C" RSS Pump Cubicle) and the Control Room.
/ I
- 3. To decrease Pressurizer (refueling cavity) Level as necessary throughout PART A of this procedure, perform the followings
- a. Open either of the following valves to align a l RilS Pump 21 A(B) to the RWST. /
- 1) [2RilS*105) RWST and Ref Cavity, Fuel Pool l Hdr Isol Trn A, Cnet El. 686, if Train A
- is an standby, or
- 2) [2RHS*106), RWST and Ref Cavity, Tuol ,
Pool lidr Iso! Trn B, Crtat El. 700, if Train B is in standby.
I
- b. Open [2RilS*107), RWST inner Containment Isol.
Cnst El. 718. /
- c. Open l2RHS*15) RWST Outer Containment Isol. __
/ !
- d. Use the running RHR pump or start Standby RiiS Pump in accordance with OM 2.10.4.A "RHS Startup" as necessary to reduce Pressurizer (refueling cavity) Level. /
CAUTION: THE FOLLOWING STEP MAY VIOLATE TECHNICAL SPECIFICATION 3.4.1.3 OR 3.9.8.1. REFER TO Tl!ESE TECHNICAL SPECIFICATIONS FOR EXPLANATIONS ARD ACTIONS PRIOR TO PERTORMING THE NEAT STEP.
- e. Throttle or close [2RitS*MOV720A) and/or
[2Rha*MOV720B] RHR Return to B and C Loop, respectively, as necessary to push RHR flow to the RWST. /
ISSUE 1 REV 5
. .-=-..e w.- .-vw..--m--w ,,-,o ,--,.+,v,.e-4,w, m.---,-v-...,--.~,v,
. n. y~,y-w. = -r-- ..re,2+ -r ,,- - v--wm*
t li.V.P.S. - 0.M. 2.55A.4 .
OST 2.11.14 Page 5 of 85 l A. c -
0:3 following computer points on a one (1)
...... .iends
- a. [LO50DA) EWST Level _ __ /
- b. [LO501A) KWST Level ./
- c. [T0500A] Refuel Vtr Stg TK21 T. / __
- d. [T0500A) Refuel Vtr Stg TK21 T. /_
- e. [T0480A] PR2R Vtr Temp [2RCS TE453) /
S. Energize the following valve power supplies:
- a. 480VAC [MCC*2-E11) Cub 4D power r.upply for
[2 SIS *MOV8809A). /
- b. 480VAC [M2C*2 E11) Cub 6D power supply for l2 SIS *MOV8BB8A). ____ / _ _,
- c. 480VAC [MCC*2-E12) Cub 3D power supply for
[2 SIS *MOV8809B). /__
- d. 480VAC [MCC*2 E12] Cub SD power supply for
[2 SIS *MOV8888B). /
- 6. Perform the following valvo alignment:
- a. Open {2 SIS *MOV8809A,B) L11SI PP 21A, 21B Suct Isol. __ /
- b. Check [2 SIS *MOV8890A,B] LHSI PP 21A, 21B Mini Flow Recirc Isol control switch in AUTO. /
- c. Check de energized closed [2 SIS *MOV8811A,B)
Recire Spray PP 210, 21D Disch Crossover to LilSI PP 21A, 21B in accordance with 20M 51.4,D Attachment 2. /
- d. Check close [2 SIS *MOV863A B) LilSI PP 21A, 21B Disch To 101S1 Pumps 1 sol. / *
- e. Check open [2 SIS *MOV8887A,B) LHSI PP 21A, 21B Disch To Hot Leg Isol. _ /_
- f. Check close [2 SIS *MOV8889) LilSI Pump Comb Disch To Hot Legs isol. /
ISSLT 1 REV 5 e
f B.V.P.S. + 0.H. 2.55A.4 .
OST 2.11.14 Page 6 of 85
- g. Check close 1251SANOV8868A,B] LilSI PP 21A, 21B Disch To Cold legs Iso!. /_
l 7. Record [2 SIS P1936] U{SI lump 21 A Inlet Pressure.
Local (2 SIS P1938) = p$ig _ _ _ /
NOTE: If the head is removed, then the LHSI pump will be discharging to the refueling cavity at 4000 to 5000 gpm. This flow would result in 0 to 7 inches per minute rise in the refueling cavity Icvel when no water is being traaaferred to kWST from RHS. The water level rise will he less when water is being transferred from KIIS to RWST while the LHSI pump is running.
- 8. If the head is removed, then lower the refueling cavity to 55 inches below the Cnmt Bldg operating deck. (2 feet below the refueling cavity Level Low alarm setpoint of 31 inches below the deck.)
(otherwise N/A). __ /
l 9, Start [2419*P21A) Low llead SI Pump. / j
- 10. If the head is removed, then monitor the refueling cavity level (otherwise N/A). /
- a. If refueling cavity level rises to 20 inches below the Cnmt Bldg operating deck, or Ann.
A6-2A RETUELING CAVITY LEVEL HIGH/LOV/ TEMP HIGli energizes, stop [2 SIS *P21A] Low Head SI Pump and lower the refueling cavity (otherwise N/A). /
- 11. Verify the fol?owings
- a. [2 SIS-II21A) LHSI Pump 21A Current is 5 31 i amps (runout amps). VB-Section A / I
- b. [2 SIS *MOV8890A] 21A Low Ilead SI Pump Minimum Flow Recirc. Isol Viv opens. RED indicating light illuminated. BB Section A / _
l ISSUE 1 REV 5 1
t
t 6.V.P.S. + 0.M. 2.55A.4 . 1 OST 2.11.14 Page 7 of 85 I
- c. [2 SIS *P21A] LilSI Pump operation is normal, i.e., no;se, vibration, leakage, etc. is not excessive. (If pump opesation is questionable stop the pump.) /
CAUTION: MINIMI2E THE TIM" THE FLOV IS OPEN TG THE RCS TO PREVENT PRZR OR REFUELING CAVITY I OVERFILL.
I
- 12. Perform the following v h : BB Section A
- a. Open [2 SIS *MOV8888A] 21A Low Head 81 Pump Disch to Cold Legs. /
- b. Open [2 SIS *MOV8888B) 21B Low Head S1 Pump Disch to Cold Legs. /
i
l 13. When [2 SIS *P21A) LHSI Pump discharge pressure and flowrate stabilize, record the following:
- a. Vibration on Data Sheet 1. /_ __
- b. Inlet pressure, discharge pressure, PRZR level, flowrate and computer time on Data Sheet 2. /
- c. Print the trend data from Step 4. /
l
- 14. Close the following valves:
- 15. Verify [2 SIS *MOV8890A) 21A Low Head SI Pump Minimum Flow Recire Isol Viv opens. BB Section A /
l 16. Stop LHSI Pump [2 SIS *P21A] by placing its control l switch to PULL-TO-LOCK. I
- a. Calculate [2 SIS *P21A] LHSI Pump Developed Pump l Hsad (H) as required on Data Sheet 2. /
ISSUE 1 REV 5
, , -, , - . . - , , ,-- , r~ -- - , , - ,
0 B.V.P.S. - 0.M. 2.15A.4 .
CST 2.11.14 Page 8 of 85
- 17. Adjust PRZR cold cal level to 15 to 25*. thead installed) or return refueling cavity to 55 inches below the Cnmt Bldg operating deck. /
- 16. Record [2 SIS-P1939] LilSI Pump 21B Inlet Pressure.
Local
[2 SIS-P1939) a psig /
l 19. Start [2 SIS *P21B] Low llead S1 Pump. / l
- 20. If the head is removed, then monitor the refueling cavity (otherwise N/ A). /.
- a. If refueling cavity level rises to 20 inches below t$g operating deck or Ann A6 2A REFUELI: CAVITY LEVEL ll!GH/ LOW / TEMP llIGli energizes, then stop [2 SIS *P21B] Low llead S1 Pump and lower the refueling cavity level (othe rwise N/a). /
- 21. Verify the following:
- b. Verifv [2 SIS *MOV8890B) 21B Low llead SI Pump Minimum Flow Recire. Isol viv opens. BB l Section A / I
- c. [2 SIS *P21B) LMSI Pump operation is normal, i.e., noics, vibration, leakage, etc. is not excessive. (If pump operation is questionable stop the pump.) /
CAUTION: MINIMIZE THE TIME THE TLOW IS OPEN TO THE RCS TO PREVENT PRZR OR REFUELING CAV1' ' l OVERFILL.
l 22. Perform the following: BB Section A l
- c. Verify [2 SIS *MOV8890B) 21B Low Head S1 Pump Minimum Flow Recire Isol closes. /
ISSUE 1 REV 5
i B.V.P.S. 0.H. 2.$$A.4 .
OST 2.11.14 Pace 9 of 85 l 23. When l2 SIS *P21B) Li!SI Pump disc.hstge pressure and flowrate stabilize, record the following:
- a. Vibration on Data Sheet 1. /.
- b. Inlet pressure, discharge pressure, PEZR level, flowrate and computer time on Data Sheet 3. /
- c. Print the trend dat rom Step 4. / l
- 24. Close the followinE a'alves: l
- a. [ 2SISitMOV8888A] 21A Low Head SI Purp Disch to Cold Legs /_ i
- b. [2 SIS *MOV8888Bj 21B Low Ilead SI Pump Disch to Cold Legs ,, / I l 23. Verify (2 SIS *MOV8890B) 21B Low Head 51 Pump Minir-um Flow Recire Isol Ylv opens. lib Section A / !
l 26- Calculate [2 SIS *P21Bl LilSI Pump Developed Pump licad (H) as required an Data Sheet 3. /_
l
- 27. Adjust ?RZR cold cal levnl to 15 to 25*. (head installed) or return refueling cavity to desired level. /
CAUTION: MINIMIZE Tile TIME THE FLOW IS OPEN TO T)(L RCS TO PREVENT PR2P OR REFUELING CAVITY OVERFILL.
- 28. Open [2SI5*MCV8889) Low Head SI Pumps Disch to Hot i Legs Isol. BB Section A / I
- 29. Record LHSI Pump flowrate, computer time and PRZR level,
- a. [2 SIS *FIS946) n , gym /
- b. Computer Time /
- c. . [2RCS*LI462] = % (BB Section B) !
_/. _ l ISSUE 1 REV 5 e
, . , - . . , - - , - -r-- ~ , , - - -
.r 1 - , w ,ww-.,.--.-m -,-,-,-,,,,,v.,,.u.,+ ,- m- ,,w,, , ,v,-,,-e, -,,,n m - -
B.V.P.S. 0.M. 2.55A.4 .
OST 2.11.14 Page 10 of 85
- 11. Print the trend data from Step 4. _ / l l 32. Stop '[2 SIS *P21B] Low liead SI Pump B by placing its control switch to PULL T0+LOCJ:. _ / __
l- 33. Complete Attachment G to verify LHS1 full flow test data. /__
- 34. Close the following valves:
- a. [2 SIS *MOV8809A) LHS1 PP 21A Suct Isol. /
- b. (2 SIS *MOV8809B) LHSI PP 21B Suct Isol. __ _ / __
i
- 35. De energize the valves energized in Step 5. /
- l. -36. Close the valves opened in Step 3 or to the desired l configuratien as determined by the NSOF or NSS. /
- 37. Stop thu trend and attach the trend data to this OST. _/
- 38. Consult the Acceptance Criteria for acceptable performance. /
l 39. Inform the NSS or NSOF of the completion of Part A of the test. /
- 40. Complete the applicable portions of front coversheet. / _,,
i f
ISSUE 1 REV $
.-,,,;,,,,,-w,.,~,-,,..m,w. .,~..y_..-,_...,,.~,.,,w_~,%.,c,-,..-. ,,,,.m,,_-nv., y.,. ,,,,s , . - - - - . . , . . . . , . - ~ , , - - , _ _ , - . - , . . .
_- ____.___ __e . . -_ . __ . _ _ . _ _ _ . _ _ _ _ _ _ - -
B.V.P.S. - 0.M. 2.55A.4 .
OST 2.11.14 Page 11 B. M
~ HIGH HEAD SAFETY INJECTION n'LL TLOW TEST ACCEPTANCE CRITERIA _ -
PART B attf"g p gr JA)
E
- 1. _[2CHS*P21 A ,I4. and Cl Centrifugal Charging Pump operate at 2 the High Head Saf ety Inject wn rump .mnuaum Lperama; curve, (Attachment C, D, j j
E) I l 2. Injection Line Branchline flows using the strongest pump are within l t 3 gpm of each other. (Steps 49, 65, 73, 80) )
l 3. The check valvos listed on Attachment L operate (forward flow test) within the requirements of the ASME IST Program (T.S. 4.0.5) (Check )
valve operation is acceptable as determined using Attachment M). 1
{
- 4. The following check valves operate (forward flow test) within the requirements of the ASME IST Program (T.S. 4.0.5) (check valve l operation is acceptable if 1. above is met), i
- a. l
[2 SIS *27) RWST to HHSI Pump Chack I
- b. [2CHS*22) Chg PP 21A Disch Check
- c. [2CHS*23] Chg PP 21B Disch Check l
- d. [2CHS*24] Chg PP 21C Disch Check INITIAL CONDITIONS - PART B Initials / Date
- 1. - NSOF's or NSS's approval has been obtained for the performance of this test. /
- 2. The- operator (s) performing this test have reviewed this procedure. /
- 3. The Plant is in Mode 5, 6 or 6 with no fuel in vessel. /
- 4. The instruments listed on Data Sheets 5, 6, and 7, and Attachment J are in current calibration. /
- 5. The HHSI-Injection and Recirculation flow paths are available, filled and vented. j
/
l l
l l ISSUE 1 t
EV5
- l
,e-s.mww-.------w.,, -.--e.
- v. ,, arm._,,~m,,,--.e.-,a.,-,--gv- ,..p,;,.n.,.,,,+m,,,,,m,w,,--s,---m--,,,av-m-m,wne~r~,w,,---a,,,,m.-w.x-m.,r-,x,en m-,,->,,, w . cw , m,---.y---me
l
, B.V.P.S. - 0.M. 2.55A.4 . ,
OST 2.11.14 l Page 12 of 85 1
- 7. umps are available in accordance with The OM 2.7.4.A. charging p' PlacingA Charging /HHS1 Pump In !
Service Or In Standby". /
- 8. [2QSS*TK21A] KWST Boron concentration is greater than or equal to 2000 ppm. /
- 9. [2RCS L1462) Cold Cal Prst Level is 10 30'l, when the reactor vessel head is installed. BB Section B. / ;
- 10. [2QSS*L1100A(B)] RWST Level is > Lo Lo Level Alarm I (440 in. ) o - transfer to recirculation phase is defeated and RWST is sufficionet for HHSI Pump NPSH requirements > 173 inches indicated level. / j
- 11. The Pressurizer is vented to Containment Atmosphere. /
- 12. The Cold Overpressure Protection System Train A ;
and/or B is in service or a 2 3.14 square inch vent exists in the RCS. /
- 14. [2QSS-P22A,B) Refueling Vtr Cooling Pumps are ;
stopped. BB Sectica B /
- 15. [2RHS*P21A(21B)) RHR Pump is running. BB Section l A. The opposite train is in standby in accordance with OM-2.10.4.A. " Residual Heat Removal System l Startup". _ / I
- 17. The IST Coordinator or designee is available to support this test. /
- 18. The previous stem micrometer readings have been recorded on Attachment K from the last performance -
of this OST. /
- 19. The fuel pool is isolated from the refueling cavity when the reactor vessel head is removed. / _
- 20. Radeon n?.. been notified of any anticipated decrease of refueling cavity level. /
ISSUE 1 R e.V 5 85
.., 4-m,-.,.,,,,,-,m..,-_-,.,,,.mm,, ,,,,,..~,mr,-..,m,,-c._,,,e,-.,,,....-,4-,,.,,,-,...._,.-,.-.,--s
B.V.P.S. 0.M. 2.55A.4 . i OST 2.11.44 i Page 13 of 85 !
l PRECAUTIONS AND LIMITATI NS J PART B j i
l- 1. Do not operate a Charging Pump en a flow path of <. ;
60 gpm or > 550 gpm. l l
l l 2. PRZR level should be maintained between 15 BM. ;
during the performance of this test. l INSTRUCTIONS PART h Ir31tials / Date l 1. Obtain a calibrated portablo vibration motor, Dently+ Nevada Model TKB or equivalent, and record the Meter I.D. Number and Cal. Due Date on Data Sheet 4.
l
- 2. Obtain an outside micrometer to measure valve stem l position for the 10151 Throttle Valves.
Instrument I.D. No. i l Cal-Due Date _ / _ / _ /
r l 3. To decrease pressurizer (refueling cavity) IcVel-as necessary, perform the following:
- a. Open either of the following valves to elign a l RiiS Pump 21A (21D) to the RWST. /,
g 1) [2RitS*105 ) RWST and Refueling Cavity Hdr i A 1501., Cnmt El 686', if Train 3 is in standby, or 2)- (2RHS*106) RYST and Refueling Cavity lidr B Isol., Cnmt El /00', if Train B is in standby.
El 71t /
- c. Open [ 2RilS*15] RWST Outside Cnmt Isol., I l
(Safeguards el. 729' in "C" RSS Pump Cubicle).
/
- d. Use the running RHR pump or start the standby
- RilS= Pump' in accordance with OH 2.10.4.A "RHS Startup as necessary to reduce pressurizer or refueling cavity level. /
ISSUE 1 l
REV 5
, . . . - ,,-,,.+..-,,--_,-....ww,%.y ,,,,y-_,.,,,,-,,.,mv,c....w.,,m-~,.
, B.V.P.S. 0.H. 2.55A.4 .
OST 2.11.14 ,
Page 14 of 85 j t
CAUTION: Tile POLLOWING STEP MAY VIOLATE TECllNICAL SPECIPICATION 3.4.1.3 OR 3.9.8.1. REPER TO THESE TECilNICAL SPECIPICATIONS POR EXPLANATIONS AND _
ACTIONS PRIOR TO PERPORMING Tl!E NEXT STEP.
- e. Throttle or close [2RilS*MOV720A) and/or (2RilS*t!0V7^4P] RilR Return to B and C Loop, i respective ', as necessary to push RHR flow to the RWST. /
l 4. Place the following computer points on trend,
- n. [T0110A] Cl!G P21A INBD BRD TEMP [2CllSTE201A1] /
[2CHSTE201A2] /
f.
[70102A] CHG P21A THR BR~ S110E T [2CllSTE201A] / '
- g. [T0113A) C110 P21A L.O. COOLER DISC T
-(2CHSTE250A] /
l S. Establish communications between the Charging Pump Cubicles, Cnet Elev 693', refueling cavity (if head 1s off) and the Control Room. _
/
CAUTION: DO NOT OPERATE A Cl!ARGING PUMP UNLESS A FLOW PATH OF AT LEAST 60 GPM EXISTS.
- 6. Place (2CHS*P21A] Charging Pump in service in -
accordance- with OM-2.7.4.A. " Placing A Charging /Hl!SI Pump In Service Or In Standby". /
- 7. Verify the charging pump suction is aligned to the RWST.
- a. _Open the following valves:
g
- 1) [2CHS*LCV115B) -Charging Pump Suction ytive from RWST.
/
ISSUE 1 REV S
,-,_-,-.-,---e-n.- n n,_cne ,n,- --- -.-. - , , - . - . . -. ,v-,-
B.V.P.S. 0.H. 2.55A.4 .
OST 2.11.14 Page 15 of 85
- 2) [ 2 CHS* LCV115D) Charging Pump Suction valve from RWST. /
- b. Close [2CitS*HCYli.2) RHS Letdewn Flow Control l Valve. ,/_
- c. Close the following valves:
l
- 1) [2CHS*LCV115E] Charging Pump Suction from 6 the VCT. /
- 2) [2CHS*LCV115C) Charging Pump Suction from the VCT.
l
/
l 8. Verify 12CHS LI112A(115A)) Volume Control Tank Level stabilizes. VB Section A /
l 9. Throttle [2CHS*HCV186) Shaft Seal Flow Control V1v to maintain 21A,B,C, RCP Shaft Seal Flow [2CES-FI124A.127A,130A) at 6 13 gpm to available RCP(n) and coolant loop (s). DB/VB Section A _ _/
l 10. Throttle [2CllS*FCV122) Charging Pump Disch Flow l Control Viv and establish Charging Line Flow [2CHS-FI122) at 60-70 gpm. BB/VB Section A /
l 11. Close [2CHS*dOV275A) 21A Charging Pucp Minimum Flow Isol Viv. BB Section A / l 12 Perform the following valve alignment check:
- a. Check closed [2 SIS *HCV86CA,666B] RHSI Disch To Cold Leg Injection. / ,
- b. Check closed [2 SIS *MOV836) High Head To Cold -
Leg Injection Isol. /
- c. Check closed [2 SIS *MOV867B,867D) HMSI Pumps Isol To cold Leg Injection. /
- d. Check closed [2 SIS *MOV869A,869B) 10151 Hot Leg Injection Isol. / ,,,_
- e. Check open [2 SIS *MOV641) High Head To Cold Leg Injection Isol. /
- f. Check closed [2CHS*FCV160) Reactor Coolant Loop Fill Hdr Flow Control Valve. /
ISSUE 1 REV 5
_ _ ._.___--m__---------- - --- ' * - - - - - - - - - - - - ~ ~ - - -' '
, B.V.P.S. - 0.H. 2.55A.4 .
03T 2.11.14 Page 16 of 85
- g. Check closed [:CllS*MOV380A,B] Alternate l Miniflow Isol. /
l 13. Open the following valves: BB Section A
l 14. Adjust Charging ' sine Flow and Shaft Seal Flow as required to establish a combined flowrate of 45-50 +
gpm (enter 0 if seal injection is isolated).
- a. [2CHS FI124A] - = spm (6 13 gpm) /
- b. [2CHS-FI127A) --- = gpm (6-13 spm) /
- c. [2CHS-F1130A] --- = gpm (6 13 gpm) -/
- d. [2CHS-F1122) --= gpm ,/
- e. a. + b. + c. + d. = gpm (45 50) (1) /
(2) /
OAUTION: THE HHSI PUMP FLOW SHOULD BE LIMITED TO s 550 GPri TO PREVENT PUMP RUNOUT.
l 15._ Record [2 SIS *FI943) High Head Safety Inject! Flow and calculate total HHSI Pump flowrate,
- a. [2 SIS *FI943) --------------- - = _ _ gpm _j,,
- b. Flowrate from Step 14.o. ------ = gpm /
l
- c. Total flowrata = a. + b. = spm (1) /
(2) /,,_,
- 16. If flow in Step 15.c is 345 gpm to $50 spm, then go-to Step 17. Otherwise, throttle [2 SIS *67. 68, and 1 69] HHSI Pump Throttle to Loop C, B, A Cold Legs in 1/8 turn increments equally on each valve in the same direction until 550 gpm (545 gpm to 550 gpm) total flowrate is achieved on [2 SIS *FI943).
1 ISSUE 1 REV 5 t
.ow,-w., ,,,,mm , w-
..__. _ _ _ _ _ _ _ . __ . _ _ . __ _ _ ~ _ __
B.V.P.S. - 0.H. 2.5$A.6 .
OST 2.11,14 Page 17 of 85 l 17. Record 1015 I Cold Leg Inj. Lire Plowrates and calculate the combined flowrat e for each combinat ion of two Cold Leg Inj. Lines.
- a. [2 SIS-PI975) ---- = .z. . .a gpm /
- u. [2 SIS TI976) --- =
. ._ z. a a gpm / __
- c. [2 SIS FI977) - - = v.c...a gpm ./_
- d. Camum ; m 4 au __ ,___,,c (1) /_
!*2' : : ...o r7 (2) /
I I
- 18. Record [2CilS*P21A] Charging Pump Vibration on Data Sheet and inlet pressure, discharge pressure, and t ... rate on Data Sheet 5. /
l 19. Calculate [2CilS*P21A) Charging Pump Developed Pump Head (ll) and Flowrate (Q) as required on Data Sheet
- 5. _/
- 20. Place the following. computer points on tie <.id,
- a. lT0120A) ClIG P21B INBD BRD TEMP [*irrsr. 91B1) /
[2CHSTE201B2] /__
f.
[T0104A) C110 P21B THR BRG Sl!0E T [2CHSTE210B] /__
- g. [T012*A) CHG P21B L.O. COOLER DISC T
[2C95TE250B] __ /
CAUTION: DO NOT OPERATI A CilARGING PUMP UNLESS A FLOW PATH OF AT LEAST 60 GPM EXISTS.
[ 21. Stop [2CHS*P21A] Charging Pump by placing its control switch to STOP and then in PULL TO LOCK. _ /___
- 22. Place [2CHS*P21B] Charging Pump in service aligned to the RWST in accordance with OM-2.7.4.A. " Placing A Charging /HHSI Pump In Service Or in Standby". /
ISSUE 1 REV 5
__m
B.V.P.S. 0.H. 2.55A.4 .
OST 2.11.14 Page 18 of 85 l 23. Verify > 60 gpm Charging, Seal Injection Flow and Safety injection Total Flow, then close
[2CilS*MOY2"5E) Charging Pum;i 21B Mini Flow Ylv. __ /
l 24. Adjust- PRZR cold cal level to 15 to 25*. (head installed) or return the refueling cavity to desired level. _/_
l 25. Verify combined Cbarging Line Flow and Snaft Seal Flow is 45 50 gpm (entnr 0 if seal injection in l isolated),
- a. [2Cl!.c T1124A) = gpm (6 13) /__
- b. [2CHS Til27A) = gpm (6-13) _. /
- c. [2CllS F1130A) = gpm (6-13) /
- d. [2CliS T1122) = gpm /
- e. a. + b. + ,;.. + d. r _ _ gpm (45 50) (1) /
(2)__ /,
CAUTION: Thl 10!SI PUMP TLN Sl;0U?.D C LIMTTED TO $
{
550 GP61 TO P!F. VENT fUK) RUNot.T.
l 26. Record (2 SIS
- Tis 41) liigh llead Safety Injection Flow and calculate tetal 10!Si Pump flowrato,
- s. [2 SIS *T1943) -- - ---- --- = gpm _/
- b. Flowrate from Step 25.c.-- - a gpm _, /
- c. Total flowrate a a. + b. = _ gpm (1) /
(2). _/__
- 27. If flow in Step 26.c is $45 gpm to 550 gpm, then go to Step 28. Otherwise, throttle [2 SIS *67, 68, ad
- 69) 10151 Famp Throttle to Loop C, B, A Cold Legs in 1/8 turn increments equally on oach valve in the same direction until 550 gpm (545 gpm to 550 gpm) total flowrate is achieved on [2 SIS *TI943).
- 28. Record 10151 Cold Leg Inj. Line Flowrates and l calculate the combinwd flowrate for each combination of two Cold Leg Injection Line flows.
I
- a. (2 SIS-TI975) = 4tM+iM" gpm /
ISSLT 1 REV 5
4 B.V.P.S. - 0.H. 2.$$A.4 .
OST 2.11.14 Page 14 of 85
- b. [2 SIS F1976) a -
^^ . . spm /
c.
~
[251S TI'377) =, .m spm /
- d. {_-' .'._,m: (1),
_ _ _ e. r ,- / __
! '? d '
(2) / __
l 29. Record [:CilS*P21D) Charging Pump Vibration an Data Sheet 4, and inlet pressure, disc arge orcasure, and flowrate on Data Sheet 6, ,_
_ /_ ,
l 30. Calculate 12CHS^P21B) Charging Pump Developed Pump ilead (11) and Flowrote (Q) as required on Data Sheet
- 6. , /_,
l 31. Place the following computer points on trend.
- a. [T0130A) C}lR P21C INPD BRD TEMP ._ _ _ /.
- c. {T0107A) ClIG P21C THR BRG OIL T /_
- d. [T0166A) CllG f.!!C DR CR IN!!D llRG _,,,, / _,,_
- e. [T0169A) LM P21C DR GR OTBD BRU /
- f. [T0106A) CHG P21C TlfR ED.G S!W T [2?llSTE2100) /
- g. [T0133A) Cl!G P21C L.O. CMLER DISC T
[2CllSTE250C) /
CAUTION: DO NOT OPERATE A Ci!AFGING yU;iP UNLESS A TLOV PATl! OT AT LEA 51 60 GPM EXISTS.
- 32. Stop (2CHS*P21B) Charging Fump by placing its control switch to STOP and then in PULL TO LOCK. /
- 33. Place [2CHS*P21C) Charging Pump in service aligned
! to the RVST in accordance with OM-2.7.4.A " Placing A Charging /HilSI Pump In Service Or In Standby". /
l 34. Verify > 60 GPM Charging, Seal Injection Flow and i Safety Injection Total flow, then close
[2CliS*MOV275C) Charging Pump 21C Mini Tiow V!v. /
ISSUE 1 REV $
1 ,
t
,4 -- ,-,...m - -- --er-~ - < ~ vw---- n - ' ' ' ' ' ' + * * ~ ' " " " ' ~ ' '
. D.V P.S. - 0.M. 2.55A.4 ,
OST 2.11.1i Page 20 of 85 l 35. Adjust l'RZR cold cal level to 15 to 25* (head l installed) or the refueling cavity to desired level. /
l 36. Verify combined Charging Line Flow and 6 haft Seal flow is 45 50 gpm (enter 0 if seal injection is isolated).
- a. {2CitS T1124A) = _
gpm (6 13) /, _
- b. (2CllS T!127A) = spe (6-13) __, ,__ / _
- c. [ 20.5 FIl30A) = gpm (6 13) , / _ _ _
- d. (2CHS T1122) = spm _/
- e. a. + b. 4 c. + d. a gpm (45-50) (1)_ /
(2)_ /.
CAUTION: THE 10(51 PUMP TLOW Sil0VLD BE LlHITED TO 5 550 GPM TO PREVENT PUMP RUNOUT.
l 37. Record (2SI5*FI943) liigh llead Safety Injection Flow and calculate total HilSI Pump flowrate,
- a. [2 SIS *FI943) --- - --- a spm /
- b. Flowrate from Step 36.e = gpm / l
- c. Total Flowrate = a. + b. = gpm (1) /,
(2) __/_
- 38. If flow in Step 37.c is $45 spm to 550 gpm, then go to Step 39. Otherwise, throttle [2 SIS *67, 68, and
- 69) KHSI Pump Throttle to Loop C, B A Cold Legs in 1/8 turn increments equally on each valve in the same direction until 550 gpm (545 gpm to 550 gpm) total flowrate is achieved on [2 SIS *FI943),
i
- 39. Record HlISI Cold Leg Inj. Line Flowrates and calculate the combined flowrate for each combination of two Cold Leg Inj. Lines, a, [2 SIS-F1975) = -Zinaa _; spm /
- b. [2 SIS F1976) = aam J: spm /
- c. [2 SIS FI977) = ::1. ., -
gpm /
ISSUE 1 REV 5
B.V.P.S. 0.M. 2.55A.4 .
OST 2.11.14 Page 21 ci 65
- d. -2, :, ,, - -- di
,.s _,, 2 - (11 /_
?? M ' a mau.) (2)._ / _.__ ,
l 40. Record [2CHS*P21C) Charging Pump Vibration on Data Shett 4 and inlet pressure, discharge pressure, and flowrate on Date Shent 7. __ _ /_
l 41. Calculate {2CHS*P21C) Charging Pump Developed Pump ifcad (H) and Plowrate (Q) at required on Data Sheet
- 7. - __I j 42. Determine the strongest and weakest Charging Pump from Data Sheets 5, 6 and 7. The strongest pump is the one with the highest actual pump head and the weakest is the pump with the lowest actual pump head. Record the pump rnark numbers. Strongest
, Weakest .
/
- 43. Plot a
-n Attachment 0 the developed pump head (H) for the " Strongest" Charging Pump from Data Sheets 5, 6 er 7 and determine the injection flow rate (corrected for system resistance) from the intersection of head (H) and the plotted curve.
Injection Flow Rate = gpm SOTE: If [2CHS*P21C) Charging Pump is the strongest pump, Step 44 may be marked l N/A, g
l 44. Stop [2CHS*P21C] Charging Pump. / l l 45. Reopen [2CHS*MOV257A, B or C) Charging Pump Min Flow Valve and start (unless already running) the strongest Charging Pump. / l l 46. Verify > 60 gpm Charging, Seal Injection Flow and Safety Injection Total Flow, then close
[2CHS*MOV275A,B, or C) for the running pump. /
- 47. Adjust PRZR cold cal level to 15 to 25% (head l installed) or return the refueling cavity to desired level. /
ISSUE 1 REV 5
)
_ - _ - - _ _ . - _ - _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . . . _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . - _ _ . - _ _ _ - _ _ . . - - _ . _ _ . - _ _ . - _ _ . - _ - _ - _ . - _ _ _ - - _ . - . - . _ _ . _ _ . - _ . . _ _ _ - __ __ _-_-___A
. B.V.P.S. 0.H. 2.55A.4 .
OST 2.11.14 Page 22 of 85 l I
l 48. Adjust Charging Line Flow and Shaft Seal Flow as l requited to establish a combined flowrate of 45 50 ;
spm (enter 0 if seal injection is isolated),
- a. [2CHS F1124A] +--
= _ spm (6 13) , /
- b. [2CHS FI.127A) - a spm (6 13) /
- c. {2CHS-FI130A) --
=, 'gpm (6 13) _ /
- d. (2CHS-F1122) -a spm _ /_
- e. a. + b. + c. + d. = gpm (45-50) (1) /
(2). /.
CAUTION THE HHSI TOTAL FLOW SHOULD BE 5 $50 GPM TO PREVENT PUMP RUNOUT.
- 49. Adjust Injection Flow Branch Lines .no the difference between the highest and lowest lines is 5 3 gpm and maintain injection flow on [2 SIS *FI943) at the injection flow rate recorded in Step 43,
+5/-0 gpm. /
$0. Record 12 SIS *F1943] High Head Safety injection Flow and calculate total HHSI Pump flowrato.
- a. [2S!S*FI943) -- ----- *---- -- = spm /_
i
- b. Flowrate from Step 48.e. --- = spm _ /
- c. Total flowrate = a. + b. = gpm (1) , /
(2) /
$1. Record HHSI Cold Leg Inj. Line Flowrates and calculate- the combined flowrate for each combination of two Cold Leg inj. Lines. ,
- s. [2 SIS-F1975) - - = XXXXX gpm /
- b. [2 SIS FI976) --- = XXXXX gpm / ,
- c. [2 SIS-F1977) --
= XXXXX gpm /
ISSUE 1
-REV 5 f
c.e 3 --.. --.# ..w..,+-w-. ,..c-.,--.-,n#we, ._.n-,,.-mw-rw--wwmve. ,ew -.vy-c.---,w-w ,,.,w,rw-we*<.rw--y -
y -r-v=w.w.--.- v- rw',~,g+e
l B.V.P.S. 0.M._ 2.55A.4 .
i OST 2.11.14 Page 23 of 85 i I
i
- d. Combined Flowrate gpm (1) _ /__ ,
-(Add Columns) (2)_ / :
Accept. Crit: The difference betweer, the &
highest and lowest line is 5 3 gpm.
l 52. Lock in position (251S*67, 68, 69] IIHSI Pump Throttle to Loop C, B, A Cold Les and record !
micrometer readings on Attachment l'. ___ _ / __ ,
-( _53. Open -[2 SIS *MOV8672) lillSI Pumps to Cold Log Injection Isol Viv. BB Section A / l l' $4. Close- [2 SIS *MOY867A) HHSI Pumps to Cold 'eg l
Injection Isol V1v. /
- a. Record [2 SIS *T1943] Ifigh Head Safety Injection "l Flow. {
/ -
gpm -
7 56. Close- [2 SIS *MOV867C) HHS; ' Pumps to Cold Leg "
Injection Isol Viv. /
-l a. Record [2 SIS-F194'l] High llead Safety Injection Flow. l
,,, /
Epm NOTE:- Steps. 57 and 58 should ,be performed l simultaneously to maintain charging pump total-flowrate at 60-550 spm.
/ '
NOTE: Steps 58 and 59 _will verify -Remote-position indication-in the open direction for [2 SIS *llCV86BB)..
58..Open [2 SIS *11CV868B) HHSI to -Cold Leg Throttling Valve as_ indication on BB Sectf.on A.- / -
f 1
l ISSUE 1 -
REV 5
=
- l. .
. u , ,m - - . . , . - -. . . . . . , - . - , - . . , , _ - . , . . - - , . . . _ . _ , -
. _ .. ,,-.. ,,- gy _v--,-
_ _ _ _ _ . _ _ ~ ._ ._ _ _ . _. _. _ _ _ _ _ _ __m. _ _ ......___._._m_.
. f B.V.P.S. 0.H. 2.55A.4 .
OST 2.11.14 Page 24 of 8'
$9. Verity (2 SIS *HCVS66B] is OPr.N as indicated by flow on [2515 F1943). .
[2 SIS-FI943) = gpm / __
, NOTE: Steps 60 and 61 should be performed ';
simultaneously to maintain charging pump total flowrate at 60-550 gpm.
Valve as indicated on BB Section A. /, I l 61. Open 12 SIS *MOV869B] High Head S1 Hot Leg Isol Viv by placing its control switch-to OPEN. BB Section A /_. ;
- 62. Verify Remote -position indication in the CLOSEL' t direction for [2 SIS *HCV868B) as follows:
'a. Verify ~ [2 SIS *HCV868B) is CLOSED, GREEN ,
indicating light illuminated.
i
- b. Verify no flow through l2 SIS *F1975, 976, 977).
l 63. Adjust PRZR cold cal level to 15 to 25% (head installed) or return the refueling cavity to 1
-desired level. __ / i l 64. Adjust combined Charging Line Flow and Shaft Seal l Flow to maintain 45 50 gpm (enter 0 if seal i
-injection is isolated). .
- a. [2CHS-F1124A] ----- = _____ gpm (6-13) /
- b. [2CHS F1127A) -- - = spm (6-13) /
- c. [2CHS-FI130A]------ = gpm (6 13) /
- d. [2CHS-FI122) ----- = gpm /
- e. a. + b. + c. + d. = gpm (45-50). (1) /
(2) /-
ISSUE 1 REV 5.
- a y . - - ~ -*-vn~+w,m--wn,,--w,w ,n.,,,ww.,__.n,w.m.,.w,n,w,,ca. me-,,,w,,-,m..mmmyw ,3-ywem,,. , y,.wy- -w y yr r - w- e ss.
- y. www miw-m
- r ey wy- er-ww y
I B.V.P.S. - 0.M. 2.55A.4 .
OST 2.11,14 Page 25 of 85 CAUTION: THE !!HSI TOT /L FLOV SHOULD BE 5 550 GPN TO PREVENT PUMP RUNOUT.
- 65. Throttle [2 SIS *54, 55, 66] HilSI Pump Throttle to ,
Hot Legs so the difference between the highest and i lowest lines is s 3 spm and maintain injection flow on [2 SIS *FI943) at the injection flow rate recorded in Step 43, +5/-0 spm. /.
- a. [2 SIS *F1943) -- --- -- -- = gpm /
- b. Flowrate from Step 64.e = gpm /_ l l
- c. Total Flowrate = a. + b. = spm (1) / I (2),, /
- 67. Record HHSI Inj. Line Flowrates and calculate the
- combined flowrate for each combination of two Inj. '
Lines,
- a. (2 SIS-FI985) -- = ,., XXXXX spm /
- b. [2 SIS-FI986) -- = XXXXX gpm /
c .- [2CIS-F1987) --- = XXXXX gpm __ /
P
- d. Combined Flowrate spm (1) /
(Add Columns) (2) /
- Accep Crit: The difference between the highest and lowest line is 5 3 gpm.-
- 68. Lock ~in position [2 SIS *66,54,55] HHSI Pump Throttle to Loop 21B, A, C Hot Legs end record micrometer readings on Attachment K. _/
- 69. Verify Remote position indication in the CLOSED direction for (2 SIS *HCV668A] HESI Disch to Cold Leg Injection as follows:
illuminated.-
ISSUE 1 REV $ '
-r- y..,-e-.<-.r- ar, -r.,,., +-- - ,, u r,,-. -,n.,.-m,'.-rwe
- ; w', v,,,, ~ --.-.m- - --n- .we --v.-e.-w,-~ -,,.,,,w -.,-,-a. ---. ~ - -- -m----r-,e-
. B.V P.S. 0.H. 2.55A.4 .
OST 2.11.14 l' age 26 of 85
- b. Open [2 SIS *MOV840) High Head to Cold Leg Injection Isol.
- c. Verify no flow through [2 SIS *FI971, 972, 973). ,
- d. Close [2 SIS *MOV640] liigh llead to Cold Leg Injection Isol.
NOTE: Stops 70.a and 70.b should be performed simultaneously to maintain charging pump total flowrate at 60-550 gpm.
- 70. Perform the followings j a. Close [2 SIS *MOV869B] High Head S1 !!ot Leg Isol V1v.. BB Section A l
/
l b.- Open [2 SIS *MOY869A) liigh 11ead SI Ilot Log Isol Viv. BB Section A. _/. _
l l 71' Adjust PRZR cold cal icvel to 15 to 25% (head installed) or return the refueling cavity to desired level. /.
- l. 72.' Adjust combined Charging Line riow and Shaft Seal Flow to maintain 45 50 spm (enter 0 if seal e injection is.fsolated),
- a. {2CHS+TI124A) -- - = rpm (6 13) /
- b. -[2CHS FI127A) - -- = _ spm (6 13) _/
- c. [2CHS-FI130A) ---- = gpm (6 13) /
- d. -[2CHS-TI122] ----. = spm /_
- e. a + b. +-c. + d.
= .spm (45-50) (1) /
(2) /
CAUTION: THE HHSI PUMP TOTAL FL0k' S110ULD BE 5 550 GPM TO PREVENT, PUMP RUN0tJr.
- 73. Throttle [2S!S*85, 86, 67) HilSI Throttle to Hot Legs so the difference between the highest and lowest lines is s 3 gpm and maintain injection flow on [2 SIS *F1940] at the injection flow rate recorded in Step 43, +5/-0 gpm. /
ISSUE 1 REV 5
B.V.P.S. 0.M. 2.5SA.4 .
OST 2.11.14 Page 27 of 85
- 74. Record [231C*T1940) liigh llead Saf ety injection Flow and calculate total 10151 Pump flowrate, a.- (2 SIS *T1940) - - -
- _ spm /_
- b. Flowrote from Step 72.e a gpm
/_ l .
- c. Total Flowrate = a. + b. = gym (1)_ /
(2) _/ l
- 75. Record 1111 5 1 Injection Line Flowrato and calculate the combined flowrate for each combination of two Injection Lines, i
, i
- c. [2 SIS FI983) --- = XXXXX gpm /
i I ;
- d. Combined Flowrate ., spm (1)__ /
(Add Columns) (2). / ,
. Accept Crit: The- difference between the '
highest and lowest line 5 3 gpm. l
- 76. Lock in position (2$1S*85,86,87] intS! Throttle !
Valve to Loop 218, A, C 11ot Leg and record micrometer readings on Attachment K. /_
NOTE: Steps 77.a and 77.b should be performed !
simultaneously to sr.intain charging pump total flowrate at 60-550 spm. >
l - 77. Perform the following: '
- a. Close [2 SIS *MOV869A] liigh liead St .liot Leg Isol
-! Viv. BB Section A '
/
.l
- i..
b,. Open [2 SIS *MOV836) liigh ifead SI Cold Leg Isol 1 V1v. BB 3ection A. /
t h
- 78. Adjust PRZR cold cal level to 15 to 25*4 (head finstalled) or- return the refueling cavity to desired level.- /
ISSUE 1 ;
REV 5 M
..,o y _ -, e,5 e . . - . ~,.~. --....,m_-,-m ..-.,._m..--,m..,-e_-,~4..-o4-~-m....., .._,.,,,,,..m.--..,._~..--~-.-s-=-._ - , . - - - +
1:
B.V.P.S. - 0.H.- 2.55A.4 .
OST 2.11.14 Page 28 of 85
- 79. Adjust combined Charging Line Flow and Shaft Seal l Flow to; maintain 45-50 gpm (enter 0 if seal-injection flow isolated).
- c. [2CHS-FI124A). = spm (6-13) /
- b. [2CHS-FI127A) = gpm (6-13) / l
- c. [2CHS-FI130A) = spm (6-13) _ /__
- d. [2CHS-F1122) = spm / )
- e. a. + b. + c. + d. = gpm (45-50) ( 1 ), /_ ;
(2) / l CAUTION: THE HMSI ? UMP TOTAL TLOW SHOULD BE $ 550 GPM TO PREVENT PUMP RUNOUT.
f 80. Throttle [2 SIS *97, 98, 99] HHSI Throttle to Cold r-Leps so the differer.ce between the highest and lowest lines is s 3 gpm and maintain f.njection flow on [2 SIS *FI940) at the injection flow rate recorded in Step.43, +5/-O'gpm.. /
l 81. Record [2 SIS *FI940] High Head Safety Injection Flow and calculatt total MHSI Pump flowtate.
- a. [2 SIS *FI940) ------- = gpm /_
- b. .Flevrate from Step 79.e = gpm / l
- c. Total Flowrate = a + b. = gpm (1) /
(2) /
- 82. Record HHSI Injection Lin. wates and calculate the combined flowrate for eac. nation of two Injection Lines,
- n. (2 SIS-F1971) =- XXXXX gpm /
- b. [2 SIS-FI972) = XXXXX gpm /__
- c. ,
.[2EIS-FI9'3] = XXXXX gpw /
- d. Combined Flowrate gpm (1) /
(Add Columns) (2) /
Accept Crit: -The difference between the highest and lowest line 1 3 gpm.
l ISSUE 1 REV 5 e
v - , - - - - - - -
,- m,-- - . , - , --
, B.V.P.S. - 0 M. 2.55A.4 .
OST 2.11.-14 Page 29 of 85 (lf 83._ Loc *. in position [2 SIS *97,98,99) HHSI Throttic to
-Cold Legs and record mi:rometer readings ' on
-Attachment K. _
/
. Isolation Valve. BB Section A. / l NOTE: -Steps 85 and 86 should -be performed-simultaneously to maintain charging pump total.flowrate at 60-550 gpm.
- 85. Close [? SIS *MOV836] High Head EI Cold Leg Isol Viv.
BB Section A- /-
~86. Open [2 SIS *HCV868A] HHSI -to Cold Leg Thrcttling i
-Valve as indicated on BB Section A. /
- 87. Verify- [2 SIS *HCV868A) is OPEN as indicated by flow '
on-[2 SIS FI940):
- J2 SIS-FI940) = gpm /
NOTE: Steps 85 and 89 should be performed l 1 simultaneously to maintain charging pnxp l total--flowrate_at 60-550 gpm. j
- 88. Closa [2 SIS *HCV668A) HHSI- to Cold Leg Thrattling l' Valve as indicated on BB Section A __ /
- I-
- 91. Verify .or fplace the following computer points on l
- trend, a,
[T0102A] [T0104A] ' [T0106A] CHG P21A, B, or C-
-THR BRG SHOE'T_[2CHS-TE210A, B or C). /
- b. [T0103A]- [T0105A] [T0107A) CHG P21A, B, or C THR BRG L.O. T [2CHS-TE212A, B, or- C) _ _ __
_,/
c .'- [T0113A]- [T0123A] - [T0133A] CHG P21A, B or'C- -
L.O. COOLER ' DISC T [2CHS-II250A, - B or. C) . .
/
ISSUE 1
-REV 5 ,
n v -- . w- - G. - ,+e..-emmer w -.,.-i-a vw -.-a c ,n- ,,w, y - - ,w ,---..m- - -- .=--
r --
B.V.P S. - 0.M. 2.55A.4 .
OST 2.11,14 Page 30 of'85
f ,' - [T0110A) [T0120A) .[T0130A) CHG P21A, B or C INBD BRG T [2CHS-TE201A1 B1 or C1). /
g, [T0111A] [T0121A] [T0131A] CHG P21A, B or C OUTBD BRG T [2CHS TE201A2, B2 or C2), /
CAOlION: DO NOT OPERATE A CHARGING PUMP UNLESS A FLOW PATH OF AT LEAST 60 GPM EXISTS,
- 92. 5 top the '[2CHS*P21A(B)(C)] strongest Charging Pump by placing its control switch to STOP. /
l 93. Reopen [2CHS*MOV275A(B)(C)]_ Charging Pump Mini Flow V1v and start the weakest [2CHS*P21A(B)(C)]
-Charging Pump by placing its control switch to START. /
- 94.-Verify > 60. gpm Charging and Seal Injection Flow and Safety Injection Flow, then close l
[2CHS*MOV275A(B)(C)) Charging Pump Mini Flow Viv. /
NOTE: Steps 95 and 96 should be performed simultta-ously to maintain . pump total flow rate at 550_ gpm, _
! 95. Close [2 SIS *MOV836), High Head SS Cold Leg Isol Viv,
/ !
96, Open-[2 SIS *MOV867B] High Head SI Cold Leg Isol V1v.
BB Section A / -l
- 97. Place the .following computer points in a one (1) minute trend:
- a. [LO500A] RVST Level -/
b.. -[LO501A] RWST Level /
- c. [T0500A] Refuel Wtr St TK21 T. /
d, [T0502A] Refuel Wtr Stg TK21 T. /
- e. [T0480A] PRZR Vtr_ Temp [2RCS-TE453) /
ISSUE 1 REV 5 e
.~-
+ -, - , _ . ,
.e B.V.P.S. - 0.M. 2.55A.4 .
OST 2.11.14 Page 31 of 85
'l 98. Adjust' PRZR cold cal level to 15 to 25*. (head
. ins ta lled) or return the refueling cavity to desired level. /
l 99. Verify combined Charging Line Flow and Shaft Seal Flow is 45-50 gpm (enter 0 if seal injection is isolated).
- a. [2CHS-F1124A] = spm (6-13) /
'b. [2CHS-FI127A] = spn (6-13) /
- c. [2CHS-FI130A] = gpm (6-13) /
- d. [2CHS-FI122] = apm /
e, a. + b. + c. + d. = gpm (45-50) (1) ,_ /
(2)_ /
CAUTION: THE HMSI PUMP TOTAL FLOW SHOULD BE s 550 GPM TO PREVENT PUMP RUNOUT.
100. Rec . [2 SIS *FI943] High Head Safety Injection Flow. PRL - evel, compucer time. and calculate totaj HHSI Pum owrate,
- a. PRER Level (2RC 462] = % (BB Secti B) /
- b. Computer Time __ /
- c. [2 SIS *FI943) ----- ---- = gpm /
- d. Flowr rom Step 99.e. = gpm / !
Total flowrate = c. + d. = gpm (1) *%sf 8 (2) N_ N !
101. Record HHSI Injection Line Flowrates. PRZR Level, computer time, and calculate the combined flowrate
-for each combination of two Injection Lines,
- a. PRZR Level [2RCS*aI462] = % (BB Section B) /
l b .- Computer Time /
l l c. [2 SIS-FI975] = XXXXX gpm /
ISSUE 1 REV 5
4
, B.V.P.S. - 0.M. 2.55A.4 .
OST 2.11.14 Page 32 of 85
- d. [2 SIS-FI976] = XXXXX spm / ._
- o. [2 SIS-FI977) = XXXXX spm /-.
- f. Combined Flowrate _
_ spm (1) /
(Add Columns) (2) /
- g. Print the trend data from Step 97. / l NOTE: Steps 102 and 103 should be performed l simultaneously to maintain charging pump total flowrate at 60-550 gpm.
l 102. Close [2 SIS *MOV867D) HHSI Pumps to Cold Leg ,
Injection 1 sol V1.v. BB Section A. /
103. Open [2 SIS *MOV869B) High Head SI Hot Leg Isol V1v.
l BB Section A. / l 104. Adjust PRZR cold cal level to 15 to 25% (head l
installed) or return the refueling cavity to desired level. /
105. Ver2fy combined Charging Line Flow and Shaft Seal Flow is 45-50 gpm' (enter 0 if seal injection is isolated). l
- a. [2CHS-FI124A] = gpm (6-13) /
- b. [2CHS-FI127A} = gpm (6-13) /
- c. [2CHS-FI130A] = gpm (6-13) /
- d. [2CHS-FI122) = gpm /
- e. a. +-b. + c. + d. = gpm (45-50) (1) /
(2) /
CAUTION: THE HHSI PUMP TOTAL FLOW SHOULD BE $ 550 GPM TO PREVENT PUMP RUNOUT.
106T neuw '
' SIS *FI943} High Head Safety Inject <
Flow, PRZR e , -outer time, and ate total HHSI Pump flowrate.
! a. PRZR Leve w LI462) = __ % (BB Sec B)
/
l-ISSUE 1 i
REV 5
,, B.V.P.S. - 0.M. 2.55A.4 .
OST 2.11.14 Page 33 of 85 b.% ,_ Computer Time
- c. [2 SIS *FI943) ------ =
___ r - /
- d. Flowrate from Ste .c = spm / l
- e. owrate = c. + d. = gpm (1) l (2) /
l 107. Record HHSI Injection Line Flowrates, PRZR level, computer time, and calculate the combined flowrate for each combination of two Injection Lines,
- a. PRZR Level [2RCSvLI462} =
,(BB Section B) /
- b. Computer Time /
- c. [2 SIS-FI985) = XXXXX gpm _
/
- d. [20!S-FI986) = '
XXXXX gpm /
- e. [2 SIS-FI987] = XXXXX gpm /
- f. Combined Flowrate gpm (1) /__
(Add Columns) (2) /
- g. Print the trend data from Step 97. / l NOTE: Steps 108 and 109 should be performed l simultaneously to maintain charging pump total.flowrate at 60-550 gpm.
l 108. Close [2 SIS *MOV869B] High Head SI Hot Leg Isol V1v. BB Section A / l
.. l 109. Open [2 SIS *MOV869A] High Head SI Hot Leg Isol Viv. BB Section A. / )
l 110. Adjust PRZR cold cal level to 15 to 25% (head installed) or return the refueling cavity to desired level. /
111. Verify combined Charging Line Flow and Shaft Seal Flow is 45-50 gpm (enter 0 if seal injection is isolated),
- a. [2CHS-FI124A] = gpm-(6-13) /
ISSUE 1 REV 5 7 y - - -
. B.V.P.S. - 0 M. 2.55A.4 .
OST 2.11.14 Page 34 of 85
- b. [2CHS FI127A) = gpm (6-13) /
- c. [ 2Cl!S -FI 130A] = gpm (6-13) /
- d. [ 2CllS-FI122) a gpm /
e, a. + b. + c. + d. = gpm (45-50) (1) /
(2) /
CAUTION: THE !!HS1 PUMP TOTAL FLOW S!!OULD BE S 550 GPM TO PREVENT PUMP RUN0tfr.
112. Record [2 SIS *FI940] High liead Safety Injection Flow, PRZR level, corputer time, and calc 21ste total lillSI Pump flowrate.
- a. -' Level [2RCS*LI462) =
, (BB S .on B) /
- b. Computer Time /
- c. [2 SIS *FI94 p -------- = ,
/
- d. F . te from Step 111.e = gpm / !
- e. Total Flowrate = c. + d. = gpm (1)
(2). l
_/
113. Record lulSI Injection Line Flowrate, PRZR level, l: computer time, and calculate the combined flowrate for each combination of two Injection Lines,
- a. PRZR Level [2RCS*LI462) = '. (BB Section B) / _
- b. Computer Time /
- c. [2 SIS-FI981) = XXXXX gpm /
- d. .[2 SIS-F1982) = XXXXX gpm /
- e. [2 SIS-FI983) = XXXXX gpm /
- f. Combined Flowrate _
gpm s1) /
(Add Columns) (2) /
- g. Print the trend data from Step 97. /
l ISSUE 1 REV 5 4
, B.V.P.S. - 0.M 2.55A 4 .
OST 2.11.14 Page 35 of 85 NOTE: Steps 114 and 115 should be performed simultaneously to maintain charging pump l total flowrate at 60-550 gpm.
l 114. Close- [2 SIS *MOV869A) liigh Head SI Hot Leg Isol Vlv. BB Section A /
! 115.'Open [2 SIS *MOV836] High Head SI Cold Leg Isol Viv. BB Section A. /.
l 116. Adjust PRZR cold cal level to 15 to 25% (head installed) or return the refueling cavity to desired level. /
l 117. Verify combined Charging Line Flow and Shaft Seal Flow is 45-50-gpm (enter 0 if seal injection is l
isolated). I
- a. [2CHS-FI124A] = gpm (6-13) /
- b. [2CHS-FI127A] = gpm (6-13) /
- c. [2CHS-FI130A] = gpr. (6-13) /
- d. [2CHS-FI122] = gpm /
- e. a. + b. + c. + d. a gpm (45-50) (1) /
(2) /
CAUTION: THE HHSI PUMP TOTAL FLOW SHOULD BE 5 550 GPM TO PREVENT PUMP RUNOUT.
. Record [2 SIS *FI940] High Head Safety Injection
, PRZR level, computer time, and calculat tota SI Pump flowrate,
- a. PRZR Lev 2RCS*LI462] = ,. (BB Section B) /
- b. Computer ilme -
/
- c. [2 SIS * ---------- = '
/
- d. . riowrate from Step 117 e = gpm- / [
- e. Total Flowrate = c. + d. = gpm (1) /
(2) % f N
i ISSUE 1 i REV 5 l- ,,
4- y- y ,- , , , - - , , , ,,e .., . . . . , . . - - -
B.V.P.S. - 0.M. 2.55A 4 .
OST 2.11.14 Page 36 of 85 119. Record HHSI Injection Line Flowrates, PRZR level, computer time, and calculate the combined flowrate for each combination of two Injection Lines,
- a. PRZR Level [2RCS*LI462] =
. (BB Section B) /
- b. Computer Time /
- c. [2 SIS-F1971] = XXXXX gpm / _
- d. [2 SIS-FI972] = XXXXX gpr /
- e. [2 SIS-F1973] = XXXXX gpm /
f, Combined Flowrate gpm (1) /
(Add Columns) (2) /
- g. Print the trend data from Step 97. / l l 120. Complete Attachment M to verify HHSI full flow test data and branchline test data using the weakest charging pump. /
121. If desired, close (2 SIS *MOV836] High Head SI Cold Leg Isol (otherwise N/A). /
l 122. Return the Charging / Safety Injection System and RHS Jystem to the desired configuration as determined by the NSOF or NSS. /
123. Stop the trend and attach the trend data to this OST. /
124. If required, verify boration flowpath in accordance with OST 2.11.10A, " Boron Injection Flowpath Power Operated Valve Exercise Modes 5-6" or OST 2.11.18, "LHSI Pump Boric Acid Flowpath Verification". _ _ _ . /
ISSUE 1 REV 5 m __ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ _ _ _ . _ _ _ _ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ . _ _ . _
- . .. . _ . . . _ . . . . _ . _ _ _ _ . _ _ . _ . . . . _ _ _ _ . - . _ = . - _ _ . _ . . _ . _ . . _
., B.V.P.S. - 0.M. 2.55A.4 .
OST 2.11.14 Page 37 of 85 ,
l 125. Consult .the _ Acceptance Criteria for-acceptable-performance. /
-l' ~126. Inform the NSS or_NSOF of-the completion of Part B of the test. /
-127. Iss'ue an'0MCN to OM 2.11.3. " Adjustment Table",-to include the new valve stem micrometer readings listed'on-Attachment K. / ,
128,-Complete the front cover sheet. /
ISSUE-1 REV 5 a
v -- . - , , , . - . . , = we -,4,- . ,...ww,.e-- --.--ww-- - - - + - - .*---a
, B.V.P.S. - 0.M. 2.55A.4 .
OST 2.11.14 Page 38 of 85 REFERENCES
- 1. BVPS-2 Technical Specification 4.0.5.
- 2. ASME XI, Section IWV, IWP.
- 3. BVPS OM-2.6 Reactor Coolant System.
- 4. BVPS OM-2.7 Chemical and Volume Control System.
- 5. BVPS OM-2.10 Residual Heat Removal System.
- 6. BVPS OM-2.11 Safety Injection System,
- 7. nVPS OM 2.13 Containment Depressurization System.
- 9. Westinghouse Technical Bulletin, NSD-TB-80-11, High Head Safety Injection Pump Flow Verification, 12/9/80,
- 10. Westinghouse Technical Bulletin, NSD-TB-81-10, Charging / Safety
. Injection Pumps, 10/13/81.
- 11. Westinghouse: Letter DMW-D-5445, Proposed Changes to Technical Specification, 4/14/86.
- 12. Letter from Westinghouse to J. W. Wade dated March 6, 1987, Number BV2-SET-058 "LHSI Check Valves Flow Test".
13.'BVPS-2 OMCN-2-87-195, 198, 200, 201, 202, 203, 205, 206, 207, 212, 213, 274, 275, 276, 277, 278, 279, 280, 294, OMDR-2-87-583, 584, .928 (Rev.
1).
=14. BVPS-2 OMCN-2-88-288 (Rev. 2)
- 15. DLW-89-581, -BVSET-88-011. " Full Flow Acceptance Criteria for Inservice Testing of Safety Injection System Check Valves", 3/5/89 (Rev. 3)
- 16. BVPS-2 OMCN-2-89-165; OMDR-2-89-0844, 0865 (Rev. 4)
- 17. BVPS-2 OMDR 2-89-1773, 1430, 1170, 1789; EM 30805, Instruction Manual 2502-290-001-001 (Rev. 5)
ISSUE 1 REV 5 t
, , . , ,--r --
,, B'V.P.S.
. - 0.M. 2.55A.4' .
OST 2.11.14 Page 39 of 85 DATA SHEET 1 NOTE: If the _ installed vibration pickup is out of service and a' portable vibration probe is_to be used, the vibration reading should be taken in the same location or as close as possible to the installed vibration-pickup monitor, The conditions of the " Restrictive Use" sticker must be met.
~
[2 SIS *P21A) Pump Vibration Data Date / / Time _.
Initials Junction Box Actual Reference Acceptable
-[2 SIS-VMP21A] Vibration Vibration Range (mils)-
I.D. (mils)- (mils)
[2 SIS-NBE121All 0.5 $1.5
[2 SIS-NBE121A21 0.18 51.5 Meter I.D. No. Portable Probe I.D. No. (if used)
Cal.'Due Date / -i / Cal. Due Date / /
i
[2 SIS *P21B] Pump Vibration Data Date- / / Time Initials
' Junction Box Actual Reference -Acceptable
[2 SIS-VMP21B]' Vibration Vibration Range (mils)
I.D. (mils) (mils)
[2 SIS-NBE121Bil 0.6 $1.8
[2 SIS-NBE121B21 0.45 51.5 Meter-I.D. No. , Portable Probe I.D. No. (if used)
Cal. Due Date / / Cal. Due Date / /
W e
ISSUE 1
. __c,- s -
. _ _ _ _ .- _ . . _ _ _ __ . . . _ . -.~ _ _. _... _ . _ . . __ __ _ _ - - _ _
, B.V.P.S. - 0.M. 2.55A.4 .
OST 2.11.14 Page 40 of 85 -;
DATA SHEET 2 Pump No. [2 SIS *P21A]
Pump Head Verification Pg = Pump Inlet Press [2 SIS-PI938] = _ _ ps'ig Cal. Due Date Local !nitials/Date /
Pd = Pump Disch Press [2 SIS *PI943) = psig Cal. Due Date Local Initials /Date /
Q = Pump Flowrate [2 SIS-FI945] = gpm Cals Due Date _
VB Section A- l Initials /Date /
PRZR Level [2RCS*LI462] = , Cal. Due Date BB Section A Initials /Date /
Computer Time Initials /Date /-
Pump Head Determination:
H = (P d -
Pg ) x 2.31 ft/psig H=( psig:- psig) x 2.31 ft/psig H= ft (1) Initials /Date /
(2) Initials /Date /
Acceptance Criteria = Head (H)_ at Flow (Q) 2 pump minimum operating curve, (Attachment A) t l
l I
ISSUE 1 REV 5 s
,..-,y-- , -ev. .,-.c ----s. -v p, ~- .- , r-.. , , - . - ,n--, , , - - - , -
a,, -- -- ,
, B.V.P.S. - 0 H. 2.55A 4 .
OST-2.11.14 Page 41 of 85 DATA SHEET 3-Pump No. [2 SIS *P21B1 Pump Head Verification Pg = Pump Inlet Press [ SIS-PI939)_= psig Cal. Due Date Local. Initials /Date _/
Pd = Pump Disch Press t2 SIS *PI944] = psig Cal. Due Date Local Initials /Date /
- Q = Pump Flowrate [2 SIS-FI946] = gpm Cal Ne Date VB Section-A l' Inn als/Date / _.
- PRZR Level (2RCS*LI46' 2 ]= . Cal. Due Date BB_Section A Initials /Date /
Computer Time Initials /Date '/
Pump Head Determination:
H =_(P d - P1 ) x-2.31 ft/psig H =-(' - psig - psig) x 2.31 ft/psig H= ft
-(1) Initials /Date /
(2) Initials /Date /
- Acceptance Criteria = Head (H) at Flow (Q) 2 pump minimum operating curve, (Attachment B) 4 ISSUE 1 REV 5
-n r r ,-,r r . - - - -,n,-,-- r . -
e . . - , , , . . - ,,_, - ~ < - . . , - - , , . ~ - -
B.V 5.S. - 0.M. 2.55A.4 .
OST 2.11.14 Page 42 of 85 DATA SHEET 4 NOTE: If the installed vibration pickup is out of service and a portable vibration probe is to be used, the vibration reading should be taken in the same location or as close as possible to the installed vibration pickup monitor. The conditions of the "Restrictis e Use" sticker must be met.
[2CHS*P21AJ Pump Vibration Data Date / / Time Initials Junction Box Actual Reference Acceptable
[2CHS-VHP21A] Vibration Vibration Range (mils)
I.D. (mils) (mils)
[2CHS-NBE121All 0.6 $1.2
[2CHS-NBE121A2] 0.2 51.0 Meter I.D. No. _ Portable Probe I.D. No. (if used)
Cal. Due Date / / Cal Due Date / /
[2CHS*P21B) P g Vibration Data Date / / Time Initials _
Junction Box Actual Re f ere'nce Acceptable
[2CHS-VMP21B] ' Vibration Vibration Range (mils)
I.D. (mils) (mils)
[2CHS-NBE121B11 0.6 51.8
[2CHS-NBE121B21 0.6 s1.8 l Meter I.D. No. Portable Probe I.D. No. (it used) l-Cal. Due Date / / Cal. Due Date /___/
AW'K g2 ISSUE 1 REV 5
.e v- y
h
. B.V.P.S. 0.H. 2.55A,4 .
OST 2.11.14 Page 43 of 85 DATA >1 ET 4 (Continued) r
-(2 CHM ~P21C) Pump Vibration Data-Date / / . Time Initials Junction Box Actual Reference- Acceptable
[2CHS-VMP21C]. Vibration Vibration Range (mils)
I.D. (mils) (mils) 0.3
^
[2CHS-NBE121C11 $1.5
- (2CHS-NBE121C2] 0.25 51.5 MeterJI.D. No. Portable Probe I.D. No. (if used)
Cal. Due Date / / Cal. Due Date / /
i-.
l.
L l
l' ISSUE 1 REV 5 j
-*r w^7r- y *yg- -
.ws
- , B.V.P.S, - n.M. 2.55A.4 .
OST 2.11.141 Page 44 of 85
-DATA SHEET S' Pump No. [2CHS*P21Al Pump _ Head Verification Pj = Pump Inlet Press _[2CHS-PI151A] = psig Cal. Due Date _j; Initials /Date / 1 P
d Pump Disch Press [~.CH5-PI151B] = psig Cal. Due Date Initials /Date /_
Q = Pump Flowrate = a + b + c + d + e VB-Section A
- a. Shaft Seal' Vater Flow [2CHS-FI124A] gpm Cal. Due Date Initiala/Date /
- b. Shaft Seal Vater Flow (2CHS-FI127A) gpm Cal. Due Date Initials /Date _/ ,
- c. Shaft Seal Vater Flow [2CHS-FI130A) gpm Cal. Due Date , _ _
Initials /Date /, ,_ _
- d. Charging Line Flow-[2CHS-FI122A]
_____gpm Cal. Due Date-
- Initials /Date /
- e. HHSI Injection _ Flow [2 SIS-FI943] spm Cal. Due/Date ,,___,
Initials /Date / .
Q =_Flowrate = a + b + c + d + e = -gps. (1) Initials /Date /
(2) Initials /Date /
Pump Head Determination:
H ='(Pd x P g) x 2,31 ft/psig
- H=( psig - psig) x 2.31 ft/psig H= ft (1) Initials /Dete /
(2) Initisis/Date /
Acceptance Criteria = Head (H) at Flow (Q) 2 pump minimum operating curve.
(Attachment C) 1 ISSUE 1 REV 5
, ,.-n- ..,,-n, n . . , - . . ,-,--,----,-~------~-r~ . - - - ~ ~ - , ~ - - - - - , - - - - - - - - = ~ > - ~ ~
. . . - ~ _ . _ ... ..-.. , . ~ . , . . - .-. - - - . - _ . - - - - - . . . . . - . - . . . - . _ . ~ -
, B.V.P.S.'- 0.M. 2.55A.4 .
OST 2.11,14 Page 45 of 85 DATA SHEET 6 Pump No. [2CHS*P21Bj lump Head yerification Pg = Pump Inlet _ Press (2CHS-PI15;A) = __ psig Cal. Due Date.
Initials /Date /
-P Pump Disch Press [2 CMS-PI152B) = psig Cal. Due Date d
Initials /Date -/
_ Q = Pump Flowrate = a + b + c + d + e VB-Section A
- a. Shaft Seal Water Flow [2CHS-FI124A) gpm Cal. Due Date Initials /Date /
- b. Shaft-Seal Water Flow [2ChS-FI127A] spm Cal. Due-Date Initials /Date /
c._ Shaft Seal Water Flow-[2CHS-FI130A] gpm Cal. Due Date Initials /Date /
- d. Charging Line Flow [2CHS-FI122A] gpm Cal. Due Date Initials /Date /
- e. HHSI Injection Flow [2 SIS-FI943] gpm Cal. Due/Date Initials /Date /
Q =-Flowrate = a + b + c + d + e = gpm (1) Initials /Date /
(2) Initials /Date /
Pump Head Determination:
1 H=l(PgxP)x'2,31ft/psig g
LH =-( psig - _psig) x 2.31 ft/psig H= ft (1)_ Initials /Date /
(2)_ Initials /Date /
Acceptance Criteria = ' Head- (H) at_ Flow (Q) 2 pump minimum operating curve.
(Attachment D).
J 4
ISSUE 1
. REV 5
+* * -----e. em,-- ,i e r e. w- 4-,
. B.V.P.S. - 0.M. 2.55A.4 .
OST 2.11.14 Page 46 of 85 DATA SHEET 7 Pump No. [2CHS*P21C]
_ Pump Head Verification P g = Pump Inlet Press [2CHS-P1153A) = psig Cal. Due Date Initials /Date /____
Pd= Pump Disch Press [2CHS-P1153B] = psig Cal. Due bate Initialu/Date ___ /
Q = Pump Flowrate = a + b + c + d + e VB-Section A
- a. Shaft Seal Water Flow [2CHS-F1124A] gpm Cal. Due Date Initials /Date /_
- b. Shaft Seal Water Flow [2CHS-FI127A) gpm Cal. Due Date Initials /Date /
- c. Shaft Seal Water Flow (2CHS-FII30A] _gpm Cal Due Date ___
Initials /Date /
- d. Charging Line Flow [2CHS-FI122A] gpm Cal. Due Date Initials /Date /
, e. HHSI Injection Flow [2 SIS-FI943) gpm Cal. Due/Date Initials /Date /
Q = Flowrate = a + b + c + d + e = gpm (1) Initials /Date /
(2) Initials /Date /
Pump Head Determination:
H = (P x P ) x 2.31 ft/psig d 1 H=( psig - psig) x 2.31 ft/psig H= ft (1) Initials /Date , /
(2) Initials /Date /
Acceptance Criteria = Head (H) at Flow (Q) 2 pump minimum operating curve.
(Attachment E)
ISSUE 1
, REV 5
. B.V.P.S. - 0.H. 2.55A.4
- OST 2.1?. 14 Page 47 of 85 A'ITACHMENT A LOW IEAD SATETY INJECTION PUMP 12 SIS *P21A] liEAD CURVE 260 255 FT ---
GPM .-
' - ~ ~ ~
'~~.~*~~~
~~
~~~ ~ ~~
250 ~ ~^~~ ' ~ ^ ' ' - '
- f. - 4-,Q F. I .-- . _ - . .__x_,.
-1500 GPM -m - - - - .
~~
240 ^
~ ~ * ~ ~ ' ~ - ~~
^ ~ --
.. A
_ _ " " _ .^~-^
~
.._.7__ . y __. _ _ _._ .g _ __ _ , _ .
y.
g
-- - - . . . - - - . . :. ,-. ._ zu n __ _
v _- . _ _ _ _
_-_~._.
~
..,'**.y,._
+ - - -
_, !~ ~ ~~ '
+*,..-s
-- g
. _ _ - _29_5_7 GPM_-- _ - - -
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ISSUE 1 REV 5 o
w
B.V.P.S. - 0.H. 2.5$A.4 .
OST 2.11.14 Page 48 of 85 NITACHMENT B LOW HEAD SAFETY INJECTION PUMP
[2 SIS"P21B] HEAD CURVE 260 250 FT -
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, . B.V.P.S. - 0.M. 2.55A.4
- l OST 2.11.14 Page 49 of 85 ATTACH?!ENT C CliARGING PDiP [2CllS*P21 A) .
HEAD CURVE 7000
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. B.V.P..S. - 0.M. 2.-5 5 A . 4 - .
OST 2.11.14 7 Page $3 of 85 ATTACHMENT F
- - **1. - [2 SIS *6) LIISI =? ump 21A Disch Check.
- 2 . [2 SIS *7) LHSI Pump -21B Disch Check.
- 3. [2 SIS *107) LHSI Check to Loop 21 Cold Leg.
4._ [2 SIS *108) LHSI Check to _ Loop 22 Cold Leg.
I 5. [2 SIS *1P9)- LHSI Check to Loop 23 Cold Leg.
- 6. [2 SIS *128) LHSI Check to Loop 22 Hot Leg.
- 7. [2 SIS *129) LHS1 Check to Loop 23 Hot Leg.
- 8. [2 SIS *130) LHSI Pur.p Combined Disch Check to Loops 22 & 23 Hot Legs.
- 9. [2 SIS *132] LHSI Pump 21B Disch Check to Cold Legs.
- 10. [2 SIS *133) IRSI Pump 21A Disch Check to Cold Legs.
-11. (2 SIS *545_) SI-Check to Loop 22 Hot Leg.
- 12. [2 SIS *546] SI-Check'to Loop 23 Hot Leg.
13 [2 SIS *548] SI Check to Loop 21 Cold Leg.
1
- -These weighted' arm check. valves 'are also full stroke . tested in-0ST 2-1.10.
- -These ' pump-discharge check valves are also verified full-stroke-tested
-by_ meeting Acceptance Criteria, Step 3. (PART A)
ISSUE 1 REV 5 w v --
B.V.P.S. - 0.M. 2.55A.4 .
OST 2.11.14 Page 54 of 85 ATTACHMENT G EVALUATION OF LHS1 FULL FLOV TEST DATA NOTE: Contact the IST Coordinator or designee to complete the Acceptance Criteria evaluation in this attachment for LHSI full flow test data through the cold leg and hot leg check valves.
A. Determination of System Differential Head (SDH) for LHSI Cold and llot Leg Full Flow Acceptance Criteria
- 1. The following method is used to calculate system differential head in feet:
- a. System differential head (SDH) is defined as the system suction head minus the system discharge head. System head is composed of elevation heads and static pressures. The discharge elevation head is corrected to suction side fluid temperature and density conditions. It is calculated as follows:
SDH = (Zs)+(s{(144) -
(Zd)
Dd
, (Pd)(144) '
(Ds) Ds) (Ds) where:
Zs = Elevation of water level in the RWST Ps = Overpressure in the RWST Ds = Density of water in the RWST Zd = Elevation of water level in the RCS/ Pressurizer Pd'= Overpressure in the RCS/ Pressurizer Dd = Density of water in the RCS/ Pressurizer
- b. Determine water elevation from level:
[LO500A]
Zs = RWST-level of [LO501A] in. = XXX ft. elevation
[2QSS*L1100A(B)]
XXX %
Zd = Pressurizer level of = XXX ft. elevation
[2RCS*LI462]
(See ATTACRMENT P)
ISSUE 1 REV 5 L
. . - . - - ~ . - _ _ . . . - . - - .- . .-. . - . . - - -
4 1
B.V.P.S. --0.M. 2.55A.4 .
OST 2.11.14 Page 55 of 85 ATTACHMENT G (Continued)
- c. Determine overpressure in the RVST and pressurizer:
Ps = RVST open to atmosphere (14.7 psia) = 1 psig Pd = RCS/ Pressurizer open to containment atmosphere (14.7 psia) = 1 psig 5
- d. Determine the density of water in the RVST and Pressurizer using-Attachment Q:
[T0$00A}
Ds at RVST Water Temperature (T0502A] F
. (2QSS*T1100A(B)]
= XXX I) ft3 Dd at.RCS/PRZR [T0480A F = XXX Vater. Temp [ 2RCS*T;;453 ] ft3
- e. SDH = Zs + 0 IDd Zu i _,. +0
- - (Ds , , , ,
SDH =- XXX- - XXX = XXX FT.
g XXX 4
ISSUE 1 REV 5
, y y . . .-,y ,- - - , . , -e-_ m. ., .__-.._,.e_ _ . - - _ - > - - , _ ,,
B,V.P.S. 0,H 2.55A,4 ,
OST 2.11.14 Page 56 of 85 ,
ATTAR! MEN 7_0 (Continued)
- 2. Using th( cortput e r ad information and Data Sheets 2 and 3 find SDH for each LIISI Pump wuen flow is through the cold leg and hot leg check valves as fallows:
- a. SDit for [? SIS *P21A) thrcugh the cold leg check valves [2 SIS *6, 133, 132, 101, 108, 109, 348, 550, 5$2):
Za = _, in + 735.6 ft = ft elevation 12 in/ft Ed = t. = ft olevation De a; _T= lbm/ft3 Dd at T= lbm/ft3 SD}i = Za a Zd b Ds
_1 bm Il3 SD}l = ft
- gg Ibm it3 SDil = _ _ _
ft -
ft SDl! a ft REFERENCE STEFS: 4, 13.b 13.c, DATA SHEET .1, l ATTAC!lMt:NTS P, Q initials / Date PERTORMt:D BY: /
VERITIED BY: , . /,_.
- ISSf1 1 REV
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I B.V.P.S. 0.H.- 2.55A.4 .
OST 2.11.14 Page 57 of 85 ATTACil!!ENT 0 (Continued) i
- b. SDil for [2 SIS *P21b] through the cold leg check valves [2S1567, 123, ;32, 107, 108, 109, :48, 550, 552]:
j Zs = _ , in + 735.6 ft = ft elevation 12 in/ft ,
Zd a *
. = ft clovation Da at F= __ _ _ lbm/ft3 Dd at T= lbm/ft3 SDl! a Zs - Ed b Ds) ;
1 lbm I'3 SDil = _ ft -
ft ft3
_ J SD}i = ft -
, ft SDil = , it i
REFERENCE STEPS: 4, 23.b, 23.c, DATA S){EET 3, l A*ITAC}{MENTS P, Q Initials / Date PERFORMED BYr /
VERIFIED BY: / __ i ISSUE 1 REV $
n ;,: , . - - .. . .. - ,_ .. ._.. . - , . , . - - - - - . - _ . . - - . - - . - . - . . , - - . ....- . . - _ , - , - - .
~
. B.V.P.S. 0.H. 2.55A.4 .
i- OST 2.11.14 Page $8 of 65 MACll5!ENT G (Continued)
- . SDH for l2 SIS *P lB) through the hot log check valves [2 SIS *130, 128, 129, 545, 546):
Zn = __, in + 735,6 ft = it elevation 12 in/ft Zd = % = it elevation Ds at F=_ , Ibm /ft3 Dd at T= lbm/ft3 r"- Dd SLil
- Zs * ~d ,,_, ,
l Ds _
11,in )
SD){ = ft -
fg ( lbm ,
\ (g3 SDit = ft .- ft SDl! = ft REFERENCE STEPS: 4, 29.a.c. l A*17ACllMEhTS P, Q Initials / Date PERFORMED BY: /
YERITIED BY: ,, /
, ISSUE 1 REV 5
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D.V P.S. - 0.H. 2.554.4 .
OST 2.11.14 -
Page 59 of 8; i
I hTTACHMI:NT G (Continued) ;
i LilSI Cold Leg Full Flow Acceptance Criteria B. *
- 1. Ustng (2 SIS *P21A(B)] flows from Data Sheets 2(3), plot and label the point values for Total Flow / System Differential Head (SDH) on Attachment H. If each test point in to the rir,ht of the 100% pump performance curve, then acceptance criteria is satisfied and check valves [2 SIS *6. 7, 132, 133, 107, i 108, $Q9, 548, 550 and 552) are opening adequately for the LHS1 system flow to sailsfy the minimum safeguards flow requirements for TSAk accident I analye-e.
t
, Accepts ;, Critoria: natisfied/not satisfied (circle one) ,
Initials Date / /_
- 2. If a test. point is to the left of the minimum safeguards pump performance curve, the subject full flow test cannot be used to verify acceptable LHS1 i 4
flow ar.d check valve -performance. The check valves may or may not be-operating properly; additional testing and/or evaluation are required to evaluate LHSI system flow distribution and check valve performance. No i further conclusions can be drawn from the full flow surveillance test since the acceptance- criteria -has been developed as a conservative screening criteria based on the assumption that all additional system resistance is added to the system in the check valve location most critical to system flow distribution. If the failure to satisfy the acceptance criteria is due to additional resistance added elsewhere in the system, the adverse affect on
" flow distribution will be less severe and the reduction in branchline flow [
with respect to total flow will be less severe. Thus, minimum safeguards '
flow requirements as assumed in the FSAR accident analyses may still be !
satisfied.
- 3. If a test point is between the 100% pump performance curve and the minimum safeguards pump performance curve, the LHSI flow may be acceptable depending on actual pump performance. -The following method is used to determine the appropriate acceptance criteria
- a. Using the information from Data Sheets 2(3) and the pump curve for
[2 SIS *P21A(B)) (See Attachment A(B)), determine the pump performance i ratio. It is based on -the actual pump head test data from Data Sheets 2(3) and the corresponding 100% and minimum safeguards pump curve heads at the same flow. The pumn_ performance ratio is equal to:
Actual Pump Head - Minimum Safeguards Pump Curve Head 100% Pump Curve Head - Minimum Safeguards pump Curve Head r
Pump (XXX ft) - (XXX ft) (XXX ft)
Performance = = = XXX
~~~
Ratio (XXX ft) - (XXX ft) (XXX ft) t l
ISSUE 1 REV $
a _.J.- u , ._ 4 _
. . . . - . _ A. _,___,-,._,_, ..-.,,... .._ _..-, - - _.,-. -
r t
B.V.P.S. 0.H. 2.55A.4 .
OST 2.11.14 Page 60 of 85 ATTACHfENT C (Continued)
- b. The riow Acceptance Criteria Range is then determined from ;
Attachment H for the system differential head.
This range is determined by subtracting the flow value for the Minimum Safeguards Pump Performance Curve at SDH from the flow value for the 100'. Pump Performanco Curve at SDH.
Plov Acceptance 1 Criteria Nange = _ XAX _ GPM EL GPM = JXX __ GPM :
.at SDH
- c. -The actual full flow acceptance criteria is then determined by multiplying the Pump Performance Ratio times the Flow Acceptance Criteria Range and adding the result to the flow value for the Minimum Safeguards Pump Ferformance Curve at SDH on Attachmerit H.
~ ~
Acceptance Criteria =
(XXX) x (A3 GPM) + _XXXL GPM ,
= XXX GPM + XXX GPH = XXX GPM i
h l
ISSUE 1 REV 5 w- , 4. ~,.. , y- .- , - , . , , w... .--,g..-we .~.n_.,,-..y...,_-y,__ ,,,y~,_._,,,,..m,,,,,,_,m,,,,,-,,..,-.- n,.,.-
a
, B.V.P.S 0.M. 2.55A.4 .
OST 2.11.14 ;
Page 61 of 85 '
ATTACHMENT G (Continued) ;
- 4. If required, find the actual flow acceptance criteria through the cold i leg check valves for each LH6! Pump l2 SIS *P21A(B)] as follows: j
- a. For [2 SIS *P21A): -
Pump ( ft) - ( ft) ( ) ft !
Performance =
- i Ratio ( ft) -( ft) ( ) it i-
=
.. i T1ow Acceptance Criteria Range = GPM - GPM = ._ GPM at SDH .
t Acceptance Criteria- = (_ x GPM) + GPM
= - GPM + GPM
= GPM ACCEPTANCE CRITERIA If the actual flow is greater than the applicable acceptance criteria LilSI flow (
satisfies FSAR accident analyses assumptions and the subject check valves are opening adquately.
If the actual flow is less than the acceptance criteria, the test results are inconclusive relative to the performance of the LHSI system and 't subject check valves. Additional testing and/or evaluation are required to ;
evaluate LHSI system and check valve performance. .,
REFERENCE STEPS: DATA SHEET 2 and ATTACHMENT A Initials / Date PERFORMED BY __ / j VERIFIED BY: /_
i .-
ISSUE 1 REV 5 .
+
- - - - . g h-,,,, p. ,-g y, _7w y- y, _ , , , , ,,.,,mm___,__.._ . - - . - . . - .. . , _
. }
B.V.P.S. - 0.M. 2.55A.4 .
OST 2.11.14 Page 62 of 85 ATTACH':ENT_G (Continued)
- b. For [1 SIS *P21b): ,,
Puup ( ft) - ( ft) ( ) ft Performance = =
.F.4tio ( ft) - ( ft) ( ) ft ;
=
Tiow Acceptance Criteria Rango
- GPM - ___,GPM = GPM at SD}( ,
Acceptanco Criteria =( x GPM) + _
GPM
= GPM + GPM i
= __ GPM ACCEPTANCE CRITERIA If the actual flow is greater than the applicable acceptance criteria. LHS! flow satisfies TSAR accident analyses assumptions and the subject check valves aro opening adquately. If the actual flow is less ';han the acceptance criteria, the '
test results are inconclusive relative to the performance of the LHSI system and subject check valves. Additional testing and/or evaluation are required to i evaluate LHS! system and check valve performance.
REFERENCE STEPS: DATA SHEET 3 and ATTACHMENT B ,
initials / Data i'
PERFORMED BY: /_
J VERIFIED DY: _ _ . /_
i ISSUE 1 REV 5
. B.V.P.S. - 0.H. 2. 5A.4 .
OST 2.11.14 Page 63 of 85 A
- ACHMENT G (Continued)
- 0. Ills Hot Leg full flow Acceptance Criteria
- 1. Using the flow for [2 SIS *P21B] from Step 29.a. plot and label the point value for the total flow versus SDH (from Attachment G. Step A.2.c) on Attachment 1. If this test point is to the right of the curve on
' Attachment 1 then the acceptance criteria As satiefied and check talves {2S1S*128, 129, 130, 545 and $46) are opening adequately for the LilS1 system flow to satisfy the minimum safeguards flow requirements for TSAR accident analyses.
Acceptance Criteria: satisfied /not satisfied (circle one)
Initials Date __ _/ /
2.- If t he' test point. is to the left of the curve on Attachment-1, the subject full flow test cannot be used to verify acceptable LilSI flow and check valve performance. The check valves may or may not be operating properly; addica;.cl testing and/or evaluation -are required to evaluate LilS1 system flow :tribution and check valve performanc9.
No further conclusions can be drawn from the full flow surveillance '
test since the acceptance criteria has been developed as a conservative screening criteria based on the assumption that all additional system-resistance is added_ to the system in the check valve location rest critical to system flow distribution. If the failure to satisfy the acceptance criteria is due-to additional resistance added elsewhere in the system, the adverse af fect on flow distribution will be less severe and the reduction in branchline flow with respect to total flow will be less severe. 1hus, minimum safeguaids flow requirements as assumed in the TSAR accident analyses may still be satisfied.
9 ISSUE 1 REV 5
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B.V.P.S. - 0.M. 2.55A.4 OST 2.11.14 i Pap 68 of 85 i
ATTACHMENT J '
l instrument Cal. Due Date Initial $'Iate l _[
- 1. [2 SIS F1971)-liigh llead Pumps to _ / ___
Loop 21 Cold Leg l l
- 2. [2 SIS-FI972) liigh llead Pumps to _ /.
Loc.p 22 Cold Leg
- 3. [2 SIS F1973] liigh Head Pumps to _ / _ __ i Loop 23 Cold Leg 1
- 4. l2 SIS T1975) High llead Pumps to _ / _. _
Loop 21 Cold Leg '
- 5. [2 SIS-FI976) High Head Purrps to ,,_. . /,__
Loop 22 Cold Leg
- 6. [2 SIS F1977) liigh llead Pump to /_
Loop 23 Cold Leg
- 7. [2 SIS F1981) liigh llead Pumps to _ _ _ _ /_
Loop 22 llot Leg
- 8. [2 SIS FI982) }{igh llead Pumps to _ /.
Loop 23 llot Leg
- 9. (2 SIS-FI983) High Head Pumps to . __ / .
Loop 21 Hot Leg 10 [25!S-FI985)-High Head Pumps to /
Loop 22 llot Leg
- 11. [2 SIS-FI986) High }{ead Pump to /
Loop 23 Hot Leg
- 12. [2 SIS F1987) .lligh Head Pump to /
Loop 21 llot Leg
- 13. [2 SIS-FI940] HHSI Injection _/
Flow ISSUE 1 REV 5 L -
4 B.V.P.S. - 0.M. 2.55A.4 .
OST 2.11.14 '
Page 69 of 85 ATTACHMENT K PREVIOUS STEM MICROMETER STEM VALVE TURNS OPEN** READING
- MICROMETER
- INITIAL /DATE 2515454 2.0 /_
2 SIS *55 1 7/8 /
2 SIS *66 2.0 /
2 SIS *67 2 5/8 _ /
2 SIS *68 1-7/8 ,/
2 SIS *69 2-1/4 /
2 SIS *85 1-3/4 /
2 SIS *86 1-3/4- /
2 SIS *87 1-5/8 /
2 SIS *97 2 1/8 /
2 SIS *98 2-1/5 _, /
2 SIS *99 1-15/16 /
- Measured from top of the stem to top of the nut on the handwheel only after the last valve manipulation is in the open direction.
- Number of turns open shows generally where the valve position is.
Actual position is determined by stem micrometer reading.
ISSUE 1 REV 5 v
.. _ ,- - - - - - - - - .v,,-._- -,...,-...-r-_.. ,% -. . . - . - - , , _ _ - - . - - , . . .,,,-.-,e,- .v.v,.- ,.,,....# ~ ,%s- r - %~ -. ,-
B.V.P.S. 3.M. 2.$$A 4 . j OST 2.11.14 Page 70 of 85 l
t ATTACllMENT L l i
i I i *2. [2 SIS *95) HHS! Line Check to RCS Cold Legs. ;
1
$. [251S*136] HHS! Check to Loop 21 Cold Leg.
- 7. [2 SIS *138) HHSI-Check to Loop 22 Cold Leg.
4
- 11. [2 SIS *$47)-51 Check to Loop 21 Hot Leg.
[
.14. -[2 SIS *124) HHSI Check to Loop 21 Hot Leg.- l 1
-16. [2 SIS *126) !!HSI Check to Loop 23 Hot Leg.
5
- The weighted arm check valves are also full stroke tested in OST 2 1 .10 . .
4 ISSUE 1 REV 5 s
u ~ m, e v s n -- m e n v, . w ~ v,e,sw=,.-w-,,ww,..-,- --en, , , , , ~,--.--,,,w,n,,,,,.ne,,%,,-- en--,w,,,,,.., --,,rg.~,--r,-n-,.o ,,w-...w,. .-,,r.-angr,- ,,
0
,. B.V.P.S. 0.M. 2.5$A.4 .
OST 2.11.14 Page 71 of 65 ATTACHMENT H EVALUATION OF HHS! FULL TLOV TEST DATA NOTE: _ Contact the IST Coordinator or designee to complete the Acceptance Criteria evaluation in this attachment for HHSI full flow test data through the cold leg and hot leg check valves.
A.- Determination of System Differential llead (SDH) for HilSI Cold and !!ot Leg rull Flow Acceptance Criteria
- 1. The following method _is used to calculate system differential head in feet:
- a. System differential head (SDH) is defined as the system suction head minua the system discharge head. System head is composed of elevation heads and static pressures. The discharge eleva ,n head s corrected to auction side fluid temperature and dens ty conditions. It is calculated as follows:
) (Zd) Oj_ + (Pd)(144)
SDM w (Zs) + II*)CI -
(Ds) Da (Ds) where:
Zs = E.1evation of water level in the RVST Ps = Overpressure in the RWST Ds = Density of water in the RWST Zd = Elevation of water level in the RCS/ Pressurizer Pd = Overpressure in the RCS/Presrurizer Dd = Density of water in the RCS/Pressuriger
~
- b. Determine water elevation from leveli
[LO500A)
Zs = RWST level of ILO501A1 in. = _XXX, ft, elevation (2QSS*L1100A(B)] L Ed = Pressurizer level of XX f = XXX ft. elevation
(?RCS*LI462)
(See ATTACHMENT P) l 1
ISSUE 1 REV 5 l
- D.V.P.S. - 0 M. 2.55A.4 .
OST 2.11.14 Page 72 of 65 ATTACHMENT M (Continued)
- c. Determine overpressure in the RWST and pressurizer:
Ps a RVST open to atmosphere (14.7 psia) = 0 psig Pd = RCS/ Pressurizer open to containment atmosphere (14.7 psia) = 1 psig
- d. Determine the density of water in the RWST and Pressurizer using Attachment Q:
i lT0500A)
Ds at RWST Vater [T0502A] F = XXX ,
Terrperature [2QSSnTIl00A(B)) ft3 lbm Dd at RCS/PRZR (T0480A] F = _.XXX Veter Temp [2hCS"TI452] ft3
- e. SD}l = Zs + 0 IDd Zd - +0
,, (Ds _
SDl! = ,XXX - XX, = XXX FT.
i_ _ ,_ (" '__
a ISSUE 1 REV $
.3 _
,c., ,, -< ... v%-- --w e mv.- , - - - - - - - ~ , - - - - - - * * - - * - -
4
. B.V.P.S. 0.M. 2,$$A.4 .
OST 2.11.14 Page 13 of 63 i t
Af!'ACHMENT H (Continued) >
- 2. Using the computer trended information, find SDl! for the weakest 'lliSI Pump when flow is through the cold leg and hot leg check salves as ;
follows:
1 ,
- a. $Dit for the weakest ifHSI Pump through the cold leg check valves
[2 SIS *95, 137, 138, 139) (Injection Mode) using combined flowrote: '
Zs = in + 735.6 ft = ft elevation 12 in/ft
". =
Zd = ___ ft elevation Ds at F=_ lbm/ft3 Dd at F= lbm/ft3 SDit = Zs - Zi lbm ) i SDil a f*3 ft -
gg Ibm
~
ft3 SDH =- ft -
ft ,
SDit a ft REFERENCE STEPS: 97, 101, ATTAChMEh7S P, Q l Initials / Date PET. FORMED BY: ./
,_ VERIFIED BY: /
' ISSLT 1 EV 5 se,r,~,.r.rr---- -v-,=---,-.-+-,..m.-+m-w . w w- ,we.wn ----r+wvv"--v+-- v~+-w+*m-- er * - ~ "
B.V.P.S. a 0 M. 2.55A.4 . j OST 2.11.14 i Page 74 of 85 l
ATTACH!!EN*T H (Cor,tinued) l l
- b. SDit for the weakest !!!!SI Pump through the hot Icg check valves (251S*84, 125, 126, 127, 547) (Recirculation Mode) using combined flowrate:
Zs=__ in + 735.6 ft = ft elevation 12 in/ft Zd = t a ft elevation Ds at F= lbm/ft3 Dd at __T a lbm/ft3 SDil = Zs - Zd (Dd__,
g Ds ,_
lbm It3 SDH = ft - 4 lbm
-gg A ft3 SDH = ft -
ft SDH = ft RETERENCE STEPS: 97, 107 ATTACHMENTS P, Q Initials _/ Date >
PERFORMED BY: /
VERIFIED BY: /
ISSUE 1 REV 5 l 4
B.V.P.S. 0.M. 2.55A.4 .
OST 2.11.14 [
Page 75 of 85 {
- ATTACHMENT 11 (Continued) ! I l
- c. SDH for the weakest HHS! Pump through the hot leg check valves t
[2 SIS *83, 122, 323, 124, 547] (Alt. Recirc Mode) using comble.ed t flowrates !
Zs = in + 735.6 ft a ft elevation 12 in/ft Zd = -% a
, it alevation Ds at __F= lbm/ft3 Dd at e-F= = lbm/ft3 '
SDit = Zs . 7d $ -(
Ds '
i lbm\
SDH u ft - I' i
1bm i ft ft3 SDH = ft -
ft SDH = ft-1 REFERENCE STEPS: 97,113 ATTACH!!ENTS P. Q l Initials / Date i
PERFORMED BY: / ;
i VERIFIED BY: /
i
, ISSUE 1 REV 5-
B.V.P.S. 0.H. 2.55A,4 .
OST 2.11.14 Page 76 of 6$
A1TACitMENT M (Continued) l
- d. SDil for the weakest IIllSI Pump through the cold leg check valves
[ SIS *94, 134, 135, 136) (Alt. Recirc Mode) using combined flowrate:
Zs = in + 735.6 ft = ft elevation 1; in/ft Zd = _% = ft elevation ,
Ds at F= lbm/ft3 Dd at ___T = _ lbm/ft3 ,
SDil = Zs - 2d Da' lbm SDil = - It3 ft l
fg Ibm ft3 SDH = ft -
ft SDH = ft REFERENCE STEPS: 97,119, ATTACllMENTS P, Q Initials / Date PERFORMED BY: / _ ,,,
\TRITIED BY: /
ISSUE 1.
REV 5
- , , ,- ,m-..,- ,,...,..~r r-e,--- --
I
- B.V.P.S. - 0.H. 2.55A.4 ,
OST 2.11.14 Page 77 of 85 ATTACHMENT H (Continued) l B. HH51 Branch Line Flow Acceptance Criteria
- 1. Using the smallest of two out of three combined flowrates from the following steps, plot and label the point values for flow / system differential head (SDH) on Attachment N. l Leg Mode Ref. Step Cold Injection 101.f.
Hot. Recirculation 107.f.
Hot Alt. Recirc 113.f.
Cold Alt. Recirc 119.f.
If each test point is to the right of the curve then the acceptance criteria is satisfied-and check valves [251S*83, 84, 94, 95,.134, 135, 136, 137, 138, 139, 547, 122, 123, 124, 125, 126 and 127) are opening .
adequately for the-HHS! system flow to satisfy the minimum safeguards flow requirements for TSAR s,cident analyses.
Acceptance Criteria: satisfied /not satisfied (circle one)
Initials Date / /
- 2. If a test point is to the left of the curve on Attachment N the-l subject flow test cannot be used to verify acceptable HH31 flow and check- valve performance. The check valves may or may not be operating
- properly; additional testing and/or evaluation are required to evaluate HHSI system flow distribution ar.d c'aeck valve performance.
i l
ISSUE 1 REV 5
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B.V.P.S. M. * '
- 2. %A. t 05T 2.11. I ts Page 79 or 85 ATIACHMENT O SAFETY INJECTION THROTTLE SETPOINT BASED ON STRONG PUMP TDH AT RUNOUT l 500.00 , , ; .:
i .
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1,200 1,250 1,300' 1,350 1.400 1,450 1,500 1,550 1,600 1,650 1,700 1.750 .
, HHSI PUMP TDH AT 550 GPM (FEET)
ISSUI 1 e RlV 5 i
- -r w e -
i B.V.P.S. - 0.H. 2.55A.4 .
, OST 2.11.14 Page 80 of 85 ATTACl!MTNT P CONTRbLnoo.9 INDICATION (*4)
_ [ 2RCS* L1462 ] ELEVATION (TT) 0 748.31 1 748.64
__ 2 748.97
_,_. 3 _ _ . . 749.30 _,
_ ~4 749.63 5 _ 749.96 l :
6 750.29 7 750.62 8 750.95 9 751.28 10 751.61 11 751.94 12 752.27 __
13 ____, 752.60 14 752.93 15 753.26 1
_16 753.59 17 753.92 18 754.25 -
19 754.58
. 2.S. _, 754.91 i
. .__ 21 755.24 i l-ISSUE 1 REV 5
(
B.V.P4R. - 0.M. 2.55A 4 .
OST 2.11.14 Page 81 of 85 ATTACHT , J (Continued)
CONTROL ROOM INDICATION (*,)
(2RCS*LI462] E1.EVATION (PT) g 22 755.57 23 755.90 24 756.23 25_ 756.56 26 756.89 27 757.22 ,
28 75L55
_ __2 9 757.88 30 758.21
, 31 758,54 32 758.87 33 759.20 34 759.53 .-
35 _
759.86 ,
36 760.19 37 760.52 __
38 760.85 39 761,18 40 761.51 41 761a 84 42 762.17 ._
43 762.50 _
ISSUE 1 REV 5 e -
O -- - -
_a
-o B.V.P.S. 0.H. 2.5$A.4 .
OST 2.11.14 Page 62 of 85 ATTACitMENT P (Continued)
CONTROL ROOM INDICATION (*s) 12RCS*L1462] ELEVATION (PT) 44 _ _762.83 44 763.16 46 763.49 47 _763.82_
48 :. A .15 49- 764.48 .__.
50 764.81 51 765.14 52 765.47 53 76L80 54 746.13 55 766.46 56 766.79 57 767.12 58 767.45 59 767.78 _
60 766.10 61 768.44 62 768.77 63 769.09 64 769.43 ___
65 769.76 __
ISSUE 1 REV 5 w
F-B.V.P.S. 0 M. 2.55A 4 .
0S4 2.11.14 logo 63 of 85 piAC}lNENT P (Contittued)
CONTEDL E00.'l INDICATION (',)
J2RCS*L1462] ELEVATION (ITil 66 770.08 67 770.42 68 770.75 69 771.07 __ ,
70 771.41 71 771.74 72 ' 772.06 73 772.40 74 772.73 75 773.05 1
ISSL'E 1 REV 5 t . .
~~
da .
f c' e
B.V.P.S. - 0.H.
2.55A.4 .
OST 2.11,14-Page 84 of 85 ATTACHMENT Q TEMPERATIRE (Fi DENSITY (lbm/ft 3)'~
32 62.414 33 62.418 34 62.418 35 62.4?0 ,,.,
36 62.420 37 62.420 38 62.425 39 62.425 40 62.425 41 62.426 1 42 62.426 43 62.426 44 62.426 45 62.42 46 62.42 47 62.42 48 62.42 49 62,41 50 62.41 51 62.41 52 62.41 53 62.40 54 62.40 55 62.39 62.39 56 57 4 62.39 58 l 62.38 59- 62.38 60 62.37 _
l 62' 62.36 64 62.35-66 62.33
- 68 62.32 B 70 n2.31 l
l-l ISSUE i REV 5 L
__3._
~
e f'
e B.V.P.S. - 0.M. 2.55A.4 .
, OST 2.11.14 Page 85 of 85 ATTACHMENT Q (Cor.tinued)
TEMPERATURE (F) DENSITY (Ibm /ft')
75 62.27 80 62.22 85 62.17 90 62.12 95 62.06 100 62.00 110 61.98 120 61.71 130 61.56 140 ,__ 61.38 ,
720 61.19 160 60.99 170 60.79 180 60.57 190 60.34 ISSUE 1 REV 5
, ,. , . _ . + - -