ML20151R064
| ML20151R064 | |
| Person / Time | |
|---|---|
| Site: | Rancho Seco |
| Issue date: | 04/15/1988 |
| From: | SACRAMENTO MUNICIPAL UTILITY DISTRICT |
| To: | |
| Shared Package | |
| ML20151Q793 | List: |
| References | |
| GCA-88-248, STP.1154, NUDOCS 8804270230 | |
| Download: ML20151R064 (71) | |
Text
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GCA 88-248 Attachment 1 STP.1154 Remote Shutdown Panel Test f
8804270230 000415 2 DR ADOCK ODO
11 STP.1154 RDDTE SHtTIDOWN PANEL TEST SECTION SUBSECTION TITLE PAGE 1.0 TEST OETECTIVES ~1.
2.0 SPECIAL TEST EQUIPMENT 1 3.0 PREREQUISITES 1 INITIAL CONDITIONS 2 4.0 ,
5.0 LIMITS AND PRECAUTIONS -3 l ;
6.0 PROCEDURE 4 ,
7.0 ACCEPTANCE CRITERIA 21 I
8.0 REFERENCES
22 9.0 ENCIDSURES 26 I 9.1 Icop Calibration List 27 9.2 Recorder Installation 29 9.3 Plant Readings 31 9.4 IDADS Surveys 47 )
I 9.5 Procedure A.51 Excerpt 51 l
9.6 Indicated s. Actual Pressurizer 57 level 9.7 Signature / Initials Sheet 58 9.8 Ral;cho Seco Test Iog 59 I
9.9 Test Procedure Authorization Form 60 4
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1 1 1%v. O STP.1154 - i i
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STP.ll54 REMOTE SHUTDOWN PANEL TEST 1.0 TEST OBJECTIVES ;
1.1 To functionally demonstrate the Shutdown Auxiliary Control Panel (H2SD) indications and controls (except the MU TNK ISOL SFV-23508 l valve and the DHR WMP A SUCT. FROM BWST SEV-25003 valve) . NOTE:
Operations Procedure C.13A "Remote Shutdown" will be used only as
- a guide for development of STP.ll54 relative to Reactor Coolant System (RCS) cooldown and inventory control methodology.
2.0 SPECIAL TEST EQUIPMENT l 2.1 Four, four channel strip chart recorders with DC Voltage input I amplifiers, or equivalent.
l 3.0 PREREQUISITES l
3.1 Loop calibration dates are recorded on Enclosure 9.1 and are within a current calibration period. /
3.2 Communications have been established between the l EFIC panels H7IFWAl and H7IFWB1, Main Control Room, Valve isolation panel H7ISFV23811, the Turbine deck and Auxiliary shutdown panel H2SD. /
J 3.3 The plant chemistry department has been notified of this test performance. /
3.4 A pre-test briefing has been conducted, using the l Test Briefing Checklist, with all test participants. / l 3.5 The Shift Supervisor has given permission to perform this test by Ligning Enclosure 9.9, Test Procedure j l Authorization Form. / i l
Rev. 0 STP.ll54 - 1 l
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l 4.0 INITIAL CONDITIONS 4.1 The Condensate Storage Tank (CST) contains at least 270,000 gallons as indicated by LI-35803 on HISS. /
4.2 The data collection recorders are installed per Enclosure 9.2 and their serial numbers are recorded in the Rancho Seco Test Log. /
4.3 The plant is in Hot Shutdown per Operations Procedure B.4, Plant Shutdown and Cooldown with RCS temperature at approximately 545 degrees and pressurizer level at approximately 190 inches. /
4.4 Valve HV-20560,101 STM B TO AUX STM is OPEN. /
4.5 Valve HV-20565, 1Di STM A TO AUX STM is OPEN. /
4.6 A Steam Analysis for isotopic activity has been accomplished on the Main Steam System. /
LIQIE : DO NOT hang the following clearance at this time.
4.7 A clearance has been requested which opans breakers 52-2B136, OISG E-205A TO AUX STM HDR, HV-20565 and 72-B203, STM 'D3 AUX F.P. TURBINE MOV HV-30801. __
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5.0 LIMITS AND PRECAUTIONS 5.1 The auxiliary feedwater pump motor start limitations are:
5.1 .1 No more than five starts are allowed in any-twenty - four hour period.
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5.1 .2 If the motor starts from ambient temperature and runs for not more than two minutes, the motor may be restarted one time following motor coastdown to rest.
5.1 .3 After the motor has been running continuously for a minimum of four hours, it may be stopped, allowed to coast down to rest, and restarted one time.
5.1 .4 Under all circumstances other than 5.1.2 and 5.1.3, the motor must be stopped for a minimum of five hours before another single start is permitted.
5.2 The CST water must meet the chemistry specifications per the Unit 1 Chemistry Manual R.5.
5.3 Hotwell level shall not exceed 48 inches without Shift Supervisor 2 l
approval.
l 5.4 For the following valver to not exceed the 5 minute duty cycle or operate more than ten times la any hour:
5.4 .1 !!V-20577 AFW Isolatirn Valve.
i 5.4 .2 HV-20578 AFW Isolation Valve. ;
l 5.4 .3 HV-20581 AFW Isolation Valve. I 5.4 .4 HV-20582 AFH Isolation Valve.
5.5 No more than three reactor coolant pumps may be operated when the I reactor coolant temperature is below 500 F as indicated on wide range temperature indicator.
5.6 Main feedwater shall be reestablished slowly in order to maintain stable primary to secondary heat transfer conditions.
5.7 The pressurizer shall not be filled with water above the 290 inch level.
5.8 The pressurizer level shall not be decreased below the 45 inch level.
5.9 The number of personnel performing this test Procedure will not exceed that required by Procedure OP-C.13A, "Remote Shutdown".
Rev. O STP.ll54 - 3 i
6.0 PROCEDURE' Initials /Date NOTE : Operations should plot the heatup and cooldown rates.
NOTE : A Signature / Initials Sheet (Enclosure 9.7) and a Rancho Seco Test Log (Enclosure 9.8) shall be maintained by the Test' Director during the-conduct of this test.
NOTE : The data collection recorders may be started and stopped at the discretion of the Test Director. Starts and stops are to be logged in the Rancho Seco Test Log.
NOTE : The start and stop time of each procedure subsection is to be noted in the Rancho Seco Test LO9-NOTE : If steps 6.4 .1 through 6.4 .5 are to be repeated for training only, then no Acceptance criteria need be met nor will Quality control' involvement be required for the repeated steps. Steps that must be performed to support lineup and restoration for repeating steps 6.4 .1 through 6.4 .5 include:
Section 3.0 - steps 3.2 through 3.5.
Section 4.0 - steps 4.1, 4.3 through 4.7. .
Section 5.0 - all steps. l Section 6.1 - all steps.
Section 6.3 - steps.6.3 .4, 6.3 .6 through 6.3 .9, 6.3 .18. l Section 6.4 - steps 6.4 .1 through 6.4. 5.
Section 6.5 - all steps. l Section 6.6 - all' steps except 6.6 .3.
i NOTE: Control Room action to-control RCS inventory i:.: not required unless pressurizer level is approaching the limits in 5.7 and 5.8.
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Rev. 0 l STp.1154 - 4
6.1 INITIAL LINEUP 6.1 .1 ATTACH a clearance tag with breaker 52-2B136, OTSG E-205A TO AUX STM HDR HV-20565, OFF. -/
6.1 .2 At panel HlSSE, VERIFY AFW PUMP P-318 TURBINE STM INLET VLV, HV-30801 is CLOSED. /
NOTE : The following step will disable the steam to K-308, P-318 turbine drive. P-318 motor may be started from panel HlSSE if the pump is needed.
6.1 .3 At panel HlSSE, POSITION the AFW PUMP P-318 keyswitch to START PERMITTED. /
NOTE : HV-20560 may be closed from the Control Room if required to isolate the two Main Steam Lines from each other, since HV-20565 has been disabled in the open position. The two Main Steam Lines may be isolated from each other for operation of EFIC Vector logic.
6.1 .4 ATTACH a clearance tag with breaker 72-B203, STEAM-TO AUX F.P. TURBINE MOV HV-30801, OFF. /
6.1 .5 ESTABLISH the pressurizer level at approximately 190 inches (100 - 200 inches) as indicated at panel HlRC, LR-21503. / l FOTE : Control of FV-20562, PV-20571, i SFV-23811, FV-20527 and TV-20528 6 will be transferred to panel j H2SD. MCR control of FV-20531, FV-20532 and the~ panel HISSE j EFIC Initiate / Test Matrices will ;
be isolated.
6.1 .6 A Licensed Operator is positioned at panel H2SD and Operators are positioned as needed at panels H7IFWA1, H7IFWB1 and H7ISFV23811. /
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Rev. 0 STP.1154 - 5 l
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PROCEDURE (Continued) Initials /Date ILOIE : The following steps will cause an EFIC ABf Initiation in Channel A.
6.1 .7 At panel H7 Inia 1, POSITION the EFIC ISO SWITCHES as indicated:
6.1 .7.1 Switch 43-1 to ISOIATE. /
6.1 .7.2 Switch 43-2 to ISOIATE. /
6.1 .7.3 Switch 43-3 to ISOIATE. /
NOTE : The following step will cause an EFIC ABY Initiation in Channel B.
6.1 .8 At panel H7IMiB1, POSITION the EFIC ISO SWITCH, 43 to ISOIATE. /
6.1 .9 CHECK the following:
6.1 .9.1 At panel h2SD, VERIFY that the ABY FIDW CONTROL VALVE CH. A, EV-20527 HIC Auto light is ON. /
6.1 .9.2 At panel H2SD, CHECK that the STM LINE "B" ADVs, PV-20562A, B, C HIC Auto BLPB is ON and the position demand meter indicates 0% (less than 5%). /
6.1 .9.3 At panel H2SD, VERIFY that the Ani FLOW CONTROL VALVE CH.A, FV-20528 HIC Auto light is ON. /
6.1 .10 At panel H2SD, CHECK that the SDi LINE "A" ADVs, PV-20571A, B, C HIC Auto BLPB is ON and the position demand meter indicates 0% (less than 5%). /
6.1 .11 At panel H7ISEV23Sil, POSITION the 43 ISOIATION SWITCH to ISOIATE. /
6.1 .12 At panel H2SFA, CHECK that the HP INJECTION IDOP A SFV-23811 OPDI and CIDSED BLPBs are OFF. /
6.1 .13 At panel H2SD, CHECK that the HP INJECTION LOOP A SFV-23811 OPEN BLPB is OFF and CIDSED BLPB is ON. /
Rev. O STP.ll54 - 6
PROCEDURE .(Continued) Initials /Date ILOTE : The following step will inhibit
.the M W flow to OTSG A.
6.1 .14 At panel HlRI, DEPRESS'the OTSG A M W ISOIATION, HV-20515, CIDSE BLPB and CHECK the following at panel HlRI: /
6.1 .14.1 HV-20515 OPEN BLPB is OFF. /
6.1 .14.2 HV-20515 CIDSE BLPB is ON. /
6.1 .15 Verify closed FWS-108, Bypass for HV-20515. /-
6.1 .16 At panel HlRI, DEPRESS the A STARTUP Di VALVE-Bailey Hand / Auto station HAND pushbutton and CHECK that the HAND indicator is ON. /
6.1 .17 At panel HlRI, POSITION the A STARTUP FW VALVE Bailey Hand / Auto station toggle switch to LOWER and RELEASE when the position demand meter indicates 0% (less than 5%). /
ILOTE : The following step will inhibit the M W flow to OTSG B.
6.1 .18 At panel H1RI, DEPRESS the OTSG B MD1 ISOIATION, HV-20516, CI.OSE BLPB and CHECK the following at panel HlRI: /
6.1 .18.1 HV-20516 OPEN BLPB is OFF. /
6.1 .18.2 HV-20516 CIDSE BLPB is ON. /
6.1 .19 Verify closed WS-109, Bypass for HV-20516. /
6.1 .20 At panel HlRI, DEPRESS the B STARTUP Di VALVE Bailey Hand / Auto station HAND pushbutton and i CHECK that the HAND indicator is ON. / I 6.1 .21 At panel H1RI, POSITION the B STARTUP Di VALVE l Bailey Hand / Auto station toggle switch to -
IDWER and RELEASE when the position demand meter indicates 0% (less than 5%). /
6.1 .22 CHECK that the OTSG levels are being controlled automatically by EFIC Ani flow control. /
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l Rev. 0 l STP.1154 - 7 l
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PROCEDURE (Continued) Initials /Date 6.1 .23 At panel HISSt, DEPRESS the AFW ISOL VLV, HV-20577, OVERRIDE BLPB and CHECK that the OVERRIDE BLPB is ON. /
6.1 .24 At panel HISSE, DEPRESS the AFW ISOL VLV, HV-20582, OVERRIDE BLPB and CHECK that the OVERRIDE BLPB is ON. /
EgIE : HV-20577 and HV-20582 are to be closed due to the Control Room controls of TV-20531 and FV-20532 are isolated.
6.1 .25 At panel HISSE, DEPRESS the AFW ISOL VLV, HV-20577 CLOSE BLPB and CHECK the following indications: / _
6.1 .25.1 The HV-20577 OPEN BLPB is OFF. /
6.1 .25.2 The HV-20577 CLOSE BLPB is ON. /
6.1 .26 At panel HISSE, DEPRESS the AFW ISOL VLV, I HV-20582 CLOSE BLPB and CHECK the following indications: /
l 6.1 .26.1 The HV-20582 OPEN BLPB is OFF. /
6.1 .26.2 The HV-20582 CLOSE BLPB is ON. / )
HQIE : The H2SD PZR LEVEL indicators, j LI21503B and LI-21503D, are i uncompensated. The Indicated l vs. Actual correlation is on l Enclosure 9.6. l HQIE : The H2SD Operator is to j minimize charging to the RCS I while controlling pressurizer l level in a band of 85 - 135 inches uncompensated as indicated on LI-21503B by using the H2SD SFV-23811 controls.
The corresponding compensated level band is 100 - 200 inches.
6.1 .27 At panel H2SD, Jog OPEN HPI LOOP A valve SFV-23811 until the panel HlRC PRESSURIZER LEVEL LV-21503 Bailey Hand / Auto station position demand meter indicates 0% (less than 5%). /
Rev. O STP.ll54 - 8
Initials /Date PROCEDURE (Continued)
At panel HlRC, DEPRESS the PRESSURIZER LEVEL 6.1 .28 LV-21503 Bailey Hand / Auto station HAND /
pushbutton and CHECK that the HAND light is ON.
6.1 .29 At panel H2SD, ADJUST SFV-23811 to establisha 130 inches (85 - 135 inches) on the panel H2SD /
LI-21503B indicator.
6.1 .30 Maintain the RCS in Hot Shutdown conditions per Initial Condition step 4.3 with EFIC automatically controlling OTSG levels Operator manually controlling pressurizer leve /
with SFV-23811.
Rev. O STP.ll54 - 9
PROCEDURE (Continued) Initials /Date 6.2 OISG Level Control at Panel H2SD.
ILCLT_E : The H2SD Operator is to minimize charging to the RCS while controlling pressurizer level in a band of 85 - 135 inches uncompensated as indicated on LI-21503B by using the H2SD SFV-23811 controls.
The corresponding compensated level band is 100 - 200 inches.
6.2 .1 At panel H2SD, DEPRESS the Ani CO!EROL VALVE FV-20527 HIC Hand BLPB and CHECK that the Hand BLPB is ON. /
6.2 .2 RAISE the OTSG A level to approximately 35 inches, as indicated on the H2SD LI-20509, using Hand control of the H2SD FV-20527 HIC. /
6.2 .3 LOWER the OTSG A level to approximately 27.5 inches, as indicated on the H2SD LI-20509, using Hand control of the H2SD FV-20527 HIC. /
6.2 .4 At panel H2SD, DEPRESS the AFW CONTROL VALVE FV-20527 HIC Auto BLPB and CHECK that the Auto BLPB is ON. /
6.2 .5 At panel H2SD, DEPRESS the ARY ColGROL VALVE FV-20528 HIC Hand BLPB and CHECK that the Hand BLPB is ON. /
6.2 .6 RAISE the OTSG B level to approximately 35 inches, as indicated on the H2SD LI-20510, using Hand control of the H2SD '
6.2 .7 LOWER the OTSG B level to approximately 27.5 inches, as indicated on the H2SD LI-20510, using Hand control of the H2SD FV-20528 HIC. /
6.2 .8 At panel H2SD, DEPRESS the AFW CONTROL VALVE TV-20528 HIC Auto BLPB and CHECK that the Auto BLPB is ON. /
Rev. O STP.ll54 - 10
PROCEDURE (Continued) Initials /Date 6.2 .9 Maintain the RCS in Hot Shutdown conditions per Initial Conditions step 4.3 with EFIC automatically controlling OTSG levels and with the H2SD Operator manually controlling pressurizer level with SFV-23811. /
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PROCEDURE (Continued) Initials /Date 6.3 OTSG Pressure Control at Panel H2SD.
HQI.E : The H2SD Operator:is.to ~
minimize charging to the RCS-while controlling pressurizer level in a band'of'85 - 135 inches uncompensated as indicated on .LI-21503B by using -
the H2SD SFV-23811 controls.
.The corresponding compensated' level band is 100 - 200 inches..
6.3 .1 At panel H2SD, DEPRESS theLPV-20571 Hand BLPB and CHECK that the Hand BLPB is ON. /
6.3 .2 At panel H2SD,. DEPRESS the PV-20571 HIC Left Arrow BLPB and RELEASE _when the position demand meter indicates 0% (less than 5%),. /
6.3 .3 At panel HlRI, VERIFY the following conditions:-
(THROITLE the valves as necessary to_ achieve condition),
6.3 .3.1 TBV PV-20561 Red and Green-indicating lights are ON. /
6.3 .3.2 TBV FV-20563 Red and Green indicating lights are ON. /
6.3 .3.3 TBV PV-20564 Red and Green indicating lights are ON. /
6.3 .3.4 TBV.FV-20566 Red and Green indicating lights are ON. /
NOTE : The following step will allow the OTSG pressure to be controlled by the ADV controls at panel H2SD.
HQTE : The observer on the Turbine Deck should be alerted that the ADvs could open at anytime.
6.3 .4 At panel H2SD, POSITION the TURBINE BYPASS VALVE MANUAL CIDSE switch HS-20561 to CIDSE. /
Rev. O STP.ll54 - 12
PROCEDURE (Continued) Initials /Date 6.3 .5 At panel HlRI, CHECK the following conditions:
6.3 .5.1 TBV PV-20561 Red indicating light is OFF. /
6.3 .5.2 TBV PV-20561 Green indicating light is ON. /
6.3 .5.3 TBV PV-20563 Red indicating light is OFF. /
6.3 .5.4 TBV PV-20563 Green indicating light is ON. /
6.3 .5.5 TBV PV-20564 Red indicating light is OFF. /
6.3 .5.6 TBV PV-20564 Green indicating light is ON. /
6.3 .5.7 TBV PV-20566 Red indicating light is OFF. /
6.3 .5.8 TBV PV-20566 Green indicating light is ON. /
6.3 .6 At panel HlRI, DEPRESS the A TURB BYP VALVES Bailey Hand / Auto HAND pushbutton and CHECK that the HAND light is ON. /
6.3 .7 At panel HlRI, POSITION the A TURB BYP VALVES Bailey Hand / Auto station toggle switch to IDWER and RELEASE when the position demand meter indicates 0% (less than 5%). /
6.3 .8 At panel HlRI, DEPRESS the B 'IURB BYP VALVES Bailey Hand / Auto HAND pushbutton and CHECK that the HAND light is ON. /
6.3 .9 At panel HlRI, POSITION the B TURB BYP VALVES Bailey Hand / Auto station toggle switch to IDWER and RELEASE when the position demand meter indicates 0% (less than 5%). /
ILOT_E :
The Clock times recorded in. the body of this procedure are to record the start and stop times of steam release to the atmosphere.
6.3 .10 At panel H2SD, MAINTAIN OTSG pressure at approximately 1000 psig as indicated at panel H2SD PI-20547, for at least 15 minutes using Hand control of the H2SD PV-20571 HIC. /
Rev. O STP.ll54 - 13
PROCEDURE (Continued) Initials /Date 6.3 .11 RECORD the clock time that steam was observed from the ADVs:
6.3 .11.1 Clock time = hrs /
(Steaming to atmosphere) 6.3 .12 At panel H2SD, DEPRESS the PV-20562 Hand BLPB and CHECK that the Hand BLPB is ON. /
6.3 .13 'At panel H2SD, DEPRESS the PV-20562 HIC Left Arrow BLPB and RELEASE when the position demand meter indicates 0% (less than 5%). /
6.3 .14 At panel H2SD, DEPRESS the PV-20571 HIC Left Arrow BLPB and RELEASE when the position demand meter indicates 0% (less than 5%). /
6.3 .15 RECORD the clock time that no steam was observed ,
from the ADVs: l 6.3 .15.1 Clock time = hrs / j (Not steaming to atmosphere) '
l 6.3 .16 At panel H2SD, MAINTAIN OTSG pressure at ,
approximately 1000 psig as indicated at panel I H2SD PI-20548, for at least 15 minutes using Hand control of the H2SD PV-20562 HIC. /
1 6.3 .17 RECORD the clock time that steam was observed '
from the ADVs:
6.3 .17.1 Clock time = hrs /
(Steaming to atmosphere) 6.3 .18 Allow the RCS to return to Hot Shutdown conditions per Initial condition step 4.3 with the H2SD Operator manually controlling OTSG pressure using the H2SD ADV controls and l pressurizer level with SEV-23811. EFIC will automatically control OTSG levels. /
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PROCEDURE (Continued) Initials /Date 6.4 RCS Temperature Control at Panel H2SD.
NOTE : The H2SD Operator is to minimize charging to the RCS while ,
controlling pressurizer level in ;
a band of 85 - 135 inches uncompensated as indicated on l LI-21503B by using the H2SD SFV- l 23811 controls. The corresponding compensated level band is 100 - 200 inches.
NOTE : The H2SD Operator is to minimize l charging to the RCS by anticipating '
pressurizer level changes which will result from heatup and cooldown transients. i.e. Prior to each cooldown, start with pressurizer level at the top of the allowed band and RCS temperature at approximately 545 degrees.
6.4 .1 RECORD the readings required on Enclosure 9.3 Section 9.3.1. / __
6.4 .2 IDWER the RCS temperature, as indicated on the H2SD TI-21032C, by approximately 20 F (at least 17 degrees) using the H2SD control of ADV PV-20562. /
6.4 .3 RAISE the RCS temperature, as indicated on the l H2SD TI-21032C, by approximately 20 F I using the H2SD control of ADV PV-20562. /
6.4 .4 Check pressurizer level to establish the I conditions per Initial Condition step 4.3 with tha H2SD Operator manually controlling OTSG pressure using the H2SD ADV controls, pressurizer level with SFV-23811 and EFIC automatically controlling OTSG levels. /
6.4 .5 RECORD the readings required on Enclosure 9.3 Section 9.3.2. /
6.4 .6 IDWER the RCS temperature, as indicated on the H2SD TI-21031C,by approximately 20 F (at least !
17 degrees) using the H2SD control of ADV '
PV-20571. /
Rev. O STP.ll54 - 15
PROCEDURE (Continued) Initials /Date 6.4 .7 RAISE the RCS temperature, as indicated on the H2SD TI-21031C, approximately 20 F using the H2SD-control of ADV PV-20571. /
6.4 .8 Check pressurizer level and establish the conditions per Initial Condition step 4.3 with the H2SD Operator manually controlling OTSG pressure using the H2SD ADV controls, pressurizer level with SFV-23811 and EFIC automatically controlling OTSG levels. /
6.4 .9 RECORD the readings required on Enclosure 9.3 Section 9.3.3. /
6.4 .10 IDWER the RCS temperature, as indicated on the H2SD TI-21031C and TI-21032C, by approximately 20 F (at least 17 degrees) using the H2SD controls of PV-20562 and PV-20571. /
6.4 .11 RAISE the RCS temperature, as indicated on the H2SD TI-21031C and TI-21032C, approximately 20 F using the H2SD controls of PV-20562 and PV-20571. /
6.4 .13 RECORD the readings required on Enclosure 9.3 Section 9.3.4. /
6.4 .14 Check pressurizer level and establish the conditions per Initial Condition step 4.3 with the H2SD Operator manually controlling OTSG pressure using the H2SD ADV controls, pressurizer level with SFV-23811 and EFIC automatically controlling OTSG levels. /
ILCTE : The next step is satisified if the previous 30 minutes of control maintained the plant in Hot Shutdown conditions.
6.4 .15 Maintain Hot Shutdown conditions for at '
least 30 minutes using H2SD controls. /
Rev. O STP.1154 - 16 l
PROCEDURE (Continued) Initials /Date 6.5 Transfer Control to the Control Room and Restore to Normal.
6.5 .1 At panel HlRC, VERIFY that the PRESSURIZER LEVEL LV-21503 setpoint is set to match or just below actual level. /
6.5 .2 At panel H1RC, DEPRESS the PRESSURIZER LEVEL LV-21503 Bailey Hand / Auto station AUTO pushbutton and CHECK that the AUTO light is ON. /
6.5 .3 At panel H7ISFV23811, POSITION the 43 ISOLATION SWITCH to NORMAL. /
6.5 .4 At panel H2SFA, CHECK that the HP INJECTION ILOP A SFV-23811 OPEN and/or CLOSED BLPBs are ON. /
6.5 .5 At panel H2SFA, CLOSE the HP INJECTION IDOP A valve SFV-23811. /
6.5 .6 At panel HlRC, VERIFY that the PRESSURIZER LEVEL LV-21503 Bailey Hand / Auto station is controlling pressurizer level. /
NOTE : The following step will enable TBV control in the Control Room.
6.5 .7 At panel H2SD, POSTIION the TURBINE BYPASS VALVE MANUAL CIDSE switch HS-20561 to AL"IO. /
6.5 .8 At panel HlRI, match signals and DEPRESS the A TURB BYP VALVES Bailey Hand / Auto AUTO pushbutton and CHECK that the AUTO light is ON. /
6.5 .9 At panel HlRI, match signals and DEPRESS the B TURB BYP VALVES Bailey Hand / Auto AUTO pushbutton and CHECK that the AUTO light is ON. /
6.5 .10 At panel H2SD, DEPRESS the PV-20562 HIC Left Arrow BLPB and RELEASE when the position demand meter indicates 0% (less than 5%). /
6.5 .11 At panel H2SD, DEPRESS the PV-20571 HIC Left Arrow BLPB and RELEASE when the position demand meter indicates 0% (less than 5%). /
6.5 .12 RECORD the clock time that no steam was observed from the ADVs:
6.5 .12.1 Clock time = hrs /
(Not steaming to atmosphere) ,
1 Rev. O STP.ll54 - 17
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_ Initials /Date PROCEDURE (Continued) .
At panel HlRI, VERIFY that the OTSG pressure / _
6.5 13 is being controlled by the TBVs.
/
At panel H2SD, DEPRESS the PV-20562 Auto 6.5 .14 BLPB and CHECK that the Auto BLPB is ON.
/
At panel H2SD, DEPRESS the PV-20571 Auto _
6.5 .15 BLPB and CHECK that the Auto BLPB is ON.
At panel H7InfA1, POSITION the EFIC ISO 6.5 .16 SWITCHES as indicated: /
16.1 Switch 43-1 to NORMAL.
6.5 /
Switch 43-2 to NORMAL.
6.5 .16.2 /
Switch 43-3 to NORMAL.
6.5 .16.3
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At panel H7InfB1, POSITION the EFIC ISO 6.5 .17 SWITCH, 43 to NORMAL.
6.5 .18 At panel HlRI, CHECK that the SIM LINE "B"AD /
the position demand meter indicates _
0% (less than 5%) .
6.5 .19 At panel HlRI, CHECK tht.t the STM LINE "A"AD the position demand meter indicates /
0% (less than 5%) .
CAUTION : MAIN FEEDWATER SHALL BE REESTABLISHED SLOWLY IN l ORDER TO MAINTAIN STABLE PRIMARY TO SECONDARY HEAT TRANSFER CONDITIONS.
Restore MBf to OTSG A and OTSG B per Enclosure / _
6.5 .20 9.5, Operations Procedure A.51 Excerpt.
Remove the clearance tag and POSITION breaker / 52-B136, l
6.5 .21 OTSG E-205A TO AUX STM HDR HV-20565, to ON.
22 At panel H2YS, VERIFY that valve HV-20565 /
6.5 is OPEN.
Remove the clearance tag and POSITION breaker / 72-B203 6.5 .23 STEAM TO AUX F.P. TURBINE MOV HV-30801, to ON.
Rev. 0 STP.ll54 - 18 1
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PROCEDURE (Continued) Initials /Dato 6.5 .23 At panel HlSSE, VERIFY valve HV-30801 is CIDSED. /
6.5 .25 At panel HISSE, POSITION the Ani PUMP P-318 -
keyswitch to I.OCK OUT. /
6.5 .26 Allow the-RCS to return to Hot Shutdown conditions per Operating Procedure B.4. /
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PROCEDURE (Continued) Initials /Date 6.6 Restoration.
6.6 .1 NOTIFY the Chemistry Department that an Isotopic sample of the Main Steam lines is required and that this test is complete. '/
6.6 .2 NOTIFY the Shift Supervisor that the plant testing portion of this test'is complete and.
I that the AFW lineup should be verified per Operating Procedure A.51 and required operability verifications performed. /'
6.6 .3 Restore'the recorder connections identified on Enclosure 9.2. /
6.6 .4 PERFORM the IDADS surveys per Enclosure 9.4 and attach the survey printouts to this test. /
6.6 .5 Ensure all test participants have signed and initialed the Signature / Initials Sheet, Enclosure 9.7. /
Rev. O STP.ll54 - 20
. . . _ _ _ _ - ___-_-______i
7.0 ACCEPTANCE CRITERIA 7.1 The following were functionally demonstrated from panel H2SD with four RCPs running and the plant in Hot Shutdown:
(References 8.2.1, 8.4.1, 8.4.9 and 8.4.13) 7.1 .1 The TBV Emergency Close solenoids caused the TBVs to close.
(Steps 6.3 .3.1, 6.3 .3.2, 6.3 .3.3, 6.3 .3.4, 6.3 4, 6.3.5.1, 6.3 .5.2, 6.3 .5.3, 6.3 .5.4, 6.3 .5.5, 6.3 ~5.6, 6.3 .5.7, 6.3 .5.8.
7.1 .4 The PV-20562 ADVs were used to control SG pressure when in Hand.
(Step 6.3 .16) 7.1 .5 The PV-20571 ADVs were used to control SG pressure when in Hand.
(Step 6.3 .10) 7.1 .6 The RCS temperature was reduced in a controlled manner through the manual operation of the ADVs.
(Steps 6.4 .2, 6.4 .6, 6.4 .10) 7.1 .7 The RCS inventory was maintained through the use of the HPI' LOOP A SFV-23811 control.
(Steps 6.4 .15) 7.1 .8 The OTSG A level was controlled through manual operation of the AFW Flow Control Valve, FV-20527.
(Steps 6.2 .2, 6.2 .3) 7.1 .9 The OTSG B level was controlled through manual operation of the AFW Flow Control Valve, FV-20528.
(Steps 6.2 .6, 6.2 .7) 7.1 .10 The SG levels were automatically controlled at setpoint through the EFIC signals to the AFW Flow Control Valves.
(Step 6.1 .23) 7.1 .11 The plant was maintained (at the Hot Shutdown Panel, H2SD) in a Hot Shutdown condition for at least 30 minutes with ADV manual control, EFIC. automatic SG level control, and manual control of RCS inventory using the HPI LOOP A 3FV-23811.
(Step 6.4 .15) 7.1 .12 The H2SD panel remote indicators were functional.
(Step 6.4 .1 - Enclosure 9.3.1, Enclosure steps 9.3 .l.21 through 9.3 .l.33; Step 6.4 .5 - Enclosure 9.3 .2, Enclosure steps 9.3 .2.21 through 9.3 .2.33; Step 6.4 .9 -
Enclosure 9.3 .3, Enclosure steps 9.3 .3.21 through 9.3 .3.33; and Step 6.4 .13 - Enclosure 9.3 .4, Enclosure steps 9.3 .4.21 through 9.3 .4.33.)
Rev. O STP.1154 - 21
8.0 REFERENCES
8.4 Manuals & Procedures:
Technical Specifications, Sections 3.1.2 and 4.1.1 8.4 .1-A.51, Rev. 35, Auxiliary Feedwater System 8.4 .2 AP.100, Rev.11, Process Standards (Miscellaneous) 8.4 .3 AP.101, Rev. 40, Reactor Coolant System 8.4 .4 AP.151, Rev. 6, Process Standards OTSG Secondary Side 8.4 .5 t AP.152, Rev. 22, Process Standards Feedwater and Condensa 8.4 .6 Systems 8.4 .7 AP.306 III-B, Rev 5, Unit 1 Chemistry Manual B.2, Rev. 46, Plant Heatup and Startup 8.4 .8 B.4, Rev. 44, Plant Shutdown and Cooldown 8.4 .9 C.13A, Rev. 8, Remote Shutdown 8.4 .10 E.05, Rev. 11, Excessive Heat Transfer 8.4 .11 i N 28.02-308, Instruction Manual, Emergency Feedwater Initiat o 8.4 .12 and Control System Volume 1 l i
Instruction Manual, Emergency Feedwater Initiat o 8.4 .13 N 28.02-309, and Control System Volume 2 lia, f SMUD Memo GCA 88-029, G. Carl Andognini to Frank J. Mirag 8.4 .14 (NRC) dated January 25, 1988 lia, SMUD Memo GCA 88-061, G. Carl Andognini to Frank J. Mira 8.4 .15 (NRC) dated February 8, 1988 i
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STP.1154 - 22 l J
Enaineerinq Diaarams DESCRIPTION SIE EE/
DEG 26 10 ONE LINE DIAG 480 VOLT SYSTEM 8.5 E 105
.2 9 ONE LINE DIAG 125 VDC .SYSTD4 PANELS 8.6 E 107 11 11 ONE LINE DIAG 120 VAC SYSTEM PANELS 8.7 E 108 12 25 ONE LINE DIAG 120 VAC SYSTD1 PANELS 8.8 E 108 21 14 ELDi DIAG AW PUMP P-318 TURB INLET 8.9 E 205 7 0 LOOP DIAG AFW FT-31902 & FT-31903 8.10 I 053 1 0 ICOP DIAG OTSG-A PRESSURE CH. A 8.11 I 054 2 0 LOOP DIAG OTSG-A PRESSURE CH. B 8.12 I 054 5 0 LOOP DIAG OTSG-A PRESSURE CH. A 8.13 I 054 6 0 LOOP DIAG OTSG-B PRESSURE CH. B 8.14 I 054 25 0 IDOP DIAG AW FLOW CNTRL FV-20528 CH 8.15 I 054 14 0 CNTRL IDGIC DIAG MW PUMP TURB HDR 8.16 I 200 8 CNTRL IDGIC DIAG 8.17 I 205 3 4 2 CNTRL LOGIC DIAG 8.18 I 205 ,
0 CNTRL IDGIC DIAG AFW ISOL VLVS l 8.19 I 1437 1 2 17 P&I DIAG H.P. & AUXILIARY TURBINES 8.20 M 530 f 2A 11 P&I DIAG H.P. & AUXIIJARY TURBINES 8.21 M 530 3 23 P&I DIAG H.P. & AUXILIARY TURBINES 8.22 M 530 1 15 P&I DIAG STEAM GENERATOR SYSTDi 8.23 M 532 2 9 P&I DIAG STEAM CENERATOR SYSTEM
' 8.24 M 532 3 10 P&I DIAG STEAM GENERATOR SYSTD1 8.25 M 532 1 21 P&I DIAG STEAM GENERATOR SYSTDI 8.26 M 533 Rev. O STP.1154 - 23
- - - ~ , _ w-- - _,
e P w- g. - _ ,
Encineerina Diacrams DWG SET REV DESCRIPTION 8.27 M 533 2 15 P&I DIAG STEAM GDIERATOR SYSTEM 8.28 M 533 3 16 P&I DIAG STEAM GDIERATOR SYSTD4 Rev. O STP.1154 - 24
Vendor Diaorams' DWG M M DESCRIPTION 8.29 N 28.02- 2 1 0 AFW P&I DIAG 8.30 N 28.02- 3 1 0 EFIC ORGANIZATION 8.31 N 28.02- 3 2 0 EFIC ORGANIZATION 8.32 N 23.02- 4 1 0 CNTRL IDGIC OTSG 8.33 N 28.02- 5 1 1 EFIC LOGIC OTSG A LEVEL INPUT 8.34 N 28.02- 6 1 0 EFIC IDGIC OTSG B LEVEL INPUT 8.35 N 28.02- 7 1 0 EFIC IDGIC OTSG PRESSURE 8.36 N 28.02- 8 1 0 INITIATE LOGIC 8.37 N 28.02- 12 1 0 OTSG IIVEL SDISING 8.38 N 28.02- 50 1 0 SYSTD4 BIDCK DIAG (EFIC) 8.39 N 28.02- 50 2 0 SYSTD4 BIOCK DIAG (EFIC) 8.40 N 28.02- 50 3 0 SYSTEM BIDCK DIAG (EFIC) 8.41 N 28.02- 50 4 0 SYSTD4 BIDCK DIAG (EFIC)
Rev. O STP.1154 - 25
9.0 ENCLOSURES 9.1 Loop Calibration List 9.2 Recorder Installation 9.3 Plant Readings 9.4 IDADS Surveys 9.5 Procedure A.51 Excerpt 9.6 Indicated vs. Actual Pressurizer Level 9.7 Signature / Initials Sheet 9.8 Rancho Seco Test Log 9.9 Test Procedure Authorization Form.
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Rev. 0 STP.ll54 -26
ENCIDSURE 9.1 I4OP CALIBRATION LIST STEP 3.1 9.1 .1 RECORD the Loop Calibration due dates for the transmitters indicated below:
Transmitter Calibration Number Due Date Initials /Date FT-31802 /
FT-31803 /
FT-31902 /
FT-31903 /
LT-20502A /
]
LT-20503B / l LT-20503D / I LT-20505A /
LT-20505B /
LT-20506A /
LT-20506B /
LT-20507A /
LT-20507B /
LT-20508A /
LT-20508B /
LT-21503B ,
/
LT-21503D /
LT-23502C /
LT-35803 /
ENCI4SURE 9.1 PAGE 1 OF 2 Rev. O STP.ll54 - 27 i
4 ENCIOSURE - 9.1 (Continued)
LOOP CALIBRATION LIST STEP 3.1 Transmitter Calibration Number Due Date Initials /Date PI-20545A /
PT-20545B /
PI-20546A /
PI-20546B '/
PT-21050 /
PI-21051 /
PT-31801 /
PT-31901 /
TI-21024C / ;
TI-21025C / ;
TI-21031C / .
TT-21032C / !
^
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ENCLOSURE 9.1 PAGE 2 OF 2 Rev. 0 STP.ll54 - 28
ENCLOSURE 9.2 RECORDER INSTALLATION STEPS 4.2 / 6.6.3 EqLE : The installation and subsequent Q.C. inspections will be accomplished
. on a Work Request per the instructions below. The Test Director is to RECORD the number of the Work Request used in the Rancho Seco Test Log.
-9.2 .1 The recorder channels are scaled as follows:
Channel #1 as Closed Left and Open Right (20 - 4 ma).- i Channel #2 as O gpm Left and' 900 gpm Right (0 - 10 VDC) .
Channel #3 as 6 inches Inft and 100 inches Right (0 - 10 VDC) .
Channel #4 as 700 psig Left and 1200 psig Right (5.8 - 10 VDC) 9.2 .2 The Recorder Al connections have been made as follows:
Channel #1 (FV-20527 valve position)
Panel H7J3819 TB-2 terminals 1 or 2 l Channel #2 (FI-31803 flow rate) l Panel H7J3819 TB-2 terminals 4 and 5 Channel #3 (LI-20505A OTSG A Level)
Panel H7J3819 TB-1 terminals 4 and 5 l
Channel #4 (PI-20545A OTSG A Pressure) i Panel H7J3819 TB-1 terninals 1 and 2 9.2 .3 The Recorder B1 connections have been made as follows:
Channel #1 (TV-20528 valve position)
Panel H7J3819 TB-2 terminals 13 or 14 i i
Channel #2 (FI-31903 flow rate)
Panel H7J3819 TB-1 terminals 25 and 29 Channel #3 (LI-20506A OTSG B Level)
Panel H7J3819 TB-1 terminals 16 and 17 Channel #4 (PI-20546A OTSG B Pressure)
Panel H7J3819 TB-1 terminals 13 and 14 ENCLOSURE 9.2 PAGE 1 OF 2 I
Rev. O !
STP.1154 - 29 I i
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i ENCIDSURE 9.2 (Continued)
RECORDER INSTALIATION 9.2 .4 The Recorder A2 connections have been made as follows:
Channel #1' (FV-20531 valve position)
Panel H7J3821 TB-2 terminals 1 cr 2 Channel #2 -(FI-31802 flow rate)
Panel H7J3821 TB-2 terminals 4 and 5 Channel #3 (LI-20505B OTSG A Level)
Panel H7J3821 TB-1 terminals 4 and 5 Channel #4 (PI-20545B OTSG A Pressure)
Panel H7J3819 TB-1 terminals 1 and 2 9.2 .5 The Recorder B2 connections have been made as follows:
Channel #1 (FV-20532 valve position)
Panel H7J3821 TB-4 terminals 1 or 2 Channel #2 (FI-31902 flow rate)
Panel H7J3821 TB-4 terminals 4 and 5 Channel #3 (LI-20506B OTSG B Invel)
Panel H7J3821 TB-1 terminals 16 and 17 i Channel #4 (PI-20546B OTSG B Pressure) ,
Panel H7J3821 TB-1 terminals 13 and 14 9.2 .6 Each recorder channel is labelled with the Input range and Indicator loop monitored.
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ENCI4SURE 9.2 PAGE 2 OF 2 Rev. O STP.1154 - 30 I
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. . ~= . . -
w ENCIDSURE 9.3 PLANT READINGS-Initials /Date 9.3 .1 Step 6.4 .1 Panel HlSSE 9.3 .l.1 SIM GEN A PRESSURE CH A PI-20545A Reading = psig
[ Baseline Information) /
9.3 .l.2~ STM GEN A PRESSURE CH B PI-20545B Reading = psig (Baseline Information) /
9.3 .l.3 STM GEN B PRESSURE CH A PI-20546A Reading = psig (Baseline Information] /
9.3 .1.4 STM GEN B PRESSURE CH B PI-20546B Reading = psig
[ Baseline Information) /
9.3 .1.5 STM GEN A ID RANGE LEVEL CH A LI-20505A Reading = inches (Baseline Information] /
9.3 .l.6 STM GEN A ID RANGE LEVEL CH B LI-20505B Reading = inches (Baseline Information] /
9.3 .l.7 SIN GEN B I4 RANGE LEVEL CH A LI-20506A Reading = inches (Baseline Information) /
9.3 .1.8 SIM GEN B ID RANGE LEVEL CH B LI-20506B Reading = inches (Baseline Information) /
ENCIDSURE 9.3 PAGE 1 OF 16 c
Rev. 0 STP.ll54 - 31 1
ENCIDSURE 9.3 (Continued)
PLANT READINGS Initials /Date Panel HlRI - NNI 9.3 .1.9 IDOP A RC WIDE RANGE TEMP Te (T017 #1)
Reading = ___ F (Baseline Information)- /
9.3 .l.10 LOOP B RC WIDE RANGE TEMP Tc (T016 #1)
Reading = F (Baseline Information) /
9.3 .1.11 IDOP A PRESSURE - STEAM GEN (P801 #1)
Reading = psig (Baseline Information) /
9.3 .1.12 IDOP B PRESSURE - STEAM GDi (P800 #1)
Reading = psig (Baseline Information)~ /
9.3 .l.13 IDOP A STM GEN LEVEL STARTUP (LO39 #1)
Reading = inches (Baseline Information) /
9.3 .l.14 IDOP B STM GEN LEVEL STARTUP (LO40 #1)
Reading = inches (Baseline Information) /
Panel HlRC 9.3 .1.15 RFACTOR COOIRIT PRESSURE PR 21037 Reading = psig (Baseline Information) /
9.3 .1.16 REACTOR COOIRTF PRESSURE PR 21038 Reading = psig (Baseline Information) /
9.3 .l.17 PRZR WATER TEMP (T009)
Reading = F (Baseline Information) /
9.3 .1.18 PRESSURIZER LEVEL (G185)
LR-21503 Reading = inches (Baseline Information) /
ENCIDSURE 9.3 PAGE 2 OF 16 Rev. 0 -
STP ll54 - 32
ENCLOSURE 9.3 (Continued)
PLANT READINGS Initials /Date Panel H4BS 9.3 .l.19 RC LOOP A TH TI-21033A Reading = F (Baseline Information) /
9.3 .l.20 RC IDOP B TH
~TI-21034A Reading = F
, (Baseline Information) / ,
Panel H2SD 9.3 .l.21 TeTI-21025E Reading = F (Baseline Information) /
9.3 .l.22 Th TI-21031C Reading = F (Baseline Information) /
9.3 .l.23 RC PRESSURE PI-21051 Reading = psig (Baseline Information) /
9.3 .l.24 RC PRESSURE ,
PI-21050 Reading = psig i (Baseline Information) /
9.3 .l.25 Te TI-21024C Reading = F (Baseline,Information) /
9.3 .l.26 Th TI-21032C Reading = F (Baseline Information) / ,
! I 9.3 .l.27 "A" OTSG LEVEL ,
LI-20509 Reading = inches l (Baseline Information) / '
9.3 .l.28 "A" OTSG PRESSURE PI-20547 Reading = psig (Baseline Information) /
9.3 .1. '2 9 "B" OTSG LEVEL I LI-20510 Reading = inches
't (Baseline Information] /
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Rev. O STP.ll54 - 33 i l
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P ENCLOSURE 9.3 (Continued)
PIANT READINGS Initials /Date-9.3 .1.30 "B" OTSG PRESSURE PI-20548 Reading = psig '
, (Baseline Information) /
9.3 .1.31 PZR LEVEL (UNCOMPENSATED)
LI-21503D Reading = inches (Baseline Information) /
- 9.3 .1.32 PZR LEVEL (UNCOMPENSATED)
LI-21503B Reading = inches (Baseline Information) /
9.3 .l.33 MU TANK LWEL LI-23502C Reading = inches (Baseline Information) /
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ENCLOSURE 9.3 PAGE 4 OF 16 4
Rev. O j STP.1154 - 34 4
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ENCLOSURE 9.3 (Continued)
PLANT READINGS Initials /Date 9.3 .2 Step 6.4 .5 Panel HISSE 9.3 .2.1 S m GEN A PRESSURE CH A PI-20545A Reading = psig (Baseline Information) /
9.3 .2.2 S m GEN A PRESSURE CH B PI-20545B Reading = .psig (Baseline Information] /
9.3 .2.3 S m GEN B PRESSURE CH A PI-20546A Reading = psig (Baseline Information) /
^
9.3 .2.4 S m GEN B PRESSURE CH B 1
PI-20546B Reading = psig (Baseline Information"j /
9.3 .2.5 S m GEN A ID RANGE LEVEL CH A LI-20505A Reading = inches (Baseline Information) /
9.3 .2.6 S m GEN A ID RANGE LEVEL CH B LI-20505B Reading = inches -
(Baseline Information] /
9.3 .2.7 Sm GEN B ID RANGE LEVEL CH A LI-20506A Reading = inches (Baseline Information) /
9.3 .2.8 Sm GEN B ID RANGE LEVEL CH B LI-20506B Reading = inches (Baseline Information] /
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STP.1154 - 35 i
t ENCIDSURE 9.3 (Continued)
PIANT READINGS Initials /Date Panel H1RI - NNI 9.3 .2.9 IDOP A RC WIDE RANGE TEMP Te (T017 #1)
Reading = F (Baseline Information) /
4 9.3 .2.10 LOOP B RC WIDE RANGE TEMP Te (T016 #1)
Reading = F (Baseline Information)-
/
9.3 .2.11 LOOP A PRESSURE - STEAM GEN (P801 #1)
Reading = psig (Baseline Information) /
9.3 .2.12 IDOP B PRESSURE - STEAM GEN (P800 #1)
Reading = psig (Baseline Information] /
9.3 .2.13 LOOP A STM GEN LEVEL STARTUP (LO39 #1)
Reading = inches (Baseline Information) / .
9.3 .2.14 LOOP B STM GEN LEVEL STARIUP (LO40 #1)
Reading = inches (Baseline Information) / '
Panel H1RC !
9.3 .2.15 REACIOR COOI. ANT PRESSURE PR 21037 Reading = psig (Baseline Information) /
9.3 .2.16 REACTOR COOIANT PRESSURE PR 21038 Reading = psig (Baseline Information) /
9.3 .2.17 PRZR WATER TEMP (T009)
Reading = 7 (Baseline Information] /
9.3 .2.18 PRESSURIZER LEVEL (G185) 1 LR-21503 Reading = inches (Baseline Information] /
ENCIDSURE 9.3 PAGE 6 OF 16 I
Rev. 0 STP.1154 - 36 4
i
ENCLOSURE 9.3 (Continued)
PLANT READINGS Initials /Date Panel H4BS 9.3 .2.19 RC LOOP A TH TI-21033A Reading = 0F (Baseline Information] /
9.3 .2.20 RC LOOP B TH TI-21034A Reading = F (Baseline Information] /
Panel H2SD 9.3 .2.21 TeTI-21025E Reading = F (Baseline Information) /
9.3 .2.22 Th TI-21031C Reading = F (Baseline Information) /
9.3 .2.23 RC PRESSURE PI-21051 Reading = psig (Baseline Information) /
9.3 .2.24 RC PRESSURE PI-21050 Reading = psig (Baseline Information) /
l 9.3 .2.25 Tc TI-21024C Reading = F (Baseline Information] /
9.3 .2.26 Th TI-21032C Reading = F (Baseline Information) /
9.3 .2.27 "A" OTSG LEVEL LI-20509 Reading = inches (Baseline Information) /
i 9.3 .2.28 "A" OTSG PRESSURE PI-20547 Reading = psig (Baseline Information] /
9.3 .2.29 "B" OTSG LEVEL I LI-20510 Reading = inches !
(Baseline Information) /
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Rev. O I STP.ll54 - 37
ENCIASURE 9.3 (Continued)
PLANT READINGS Initials /Date 9.3-.2.30 "B" OTSG PRESSURE
~PI-20548 Reading = psig (Baseline Information) /
9.3 .2.31 PZR LEVEL (UNCOMPENSATED)
LI-21503D Reading = inches (Baseline Information] /
9.3 2.32 'PZR LEVEL (UNCOMPENSATED) -
LI-21503B Reading = inches (Baseline Information] /
9.3 .2.33 MU TANK LEVEL LI-23502C Reading = inches (Baseline Information) /
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Rev. 0 3 STP.1154 - 38 l I
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ENCIDSURE 9.3 (Continued)
PLANT READINGS Initials /Date 9.3 .3 Step 6.4 .9 Panel HISSE 9.3 .3.1 Sm GEN A PRESSURE CH A PI-20545A Reading = psig ,
(Baseline Information) / i 9.3 .3.2 Sm GDI A PRESSURE CH B PI-20545B Reading = psig (Baseline Information] /
9.3 .3.3 S m GEN B PRESSURE CH A PI-20546A Reading a psig (Baseline Information) - /
9.3 .3.4 S m GEN B PRESSURE CH B PI-20546B Reading = psig (Baseline Information) /
9.3 .3.5 STM GDI A ID RANGE LEVEL CH A l LI-20505A Reading = inches (Baseline Information) /
9.3 .3.6 STM GDI A ID RANGE LEVEL CH B LI-20505B Reading = inches (Baseline Information) /
9.3 .3.7 Sm GDi B ID RANGE LEVEL CH A LI-20506A Reading = inches 2
(Baseline Information) /
9.3 .3.8 Sm GDI B LO RANGE LEVEL CH B LI-20506B Reading = inches
] (Baseline Information) /
DiCIDSURE 9.3 PAGE 9 OF 16 Rev. O STP.1154 - 39 I
ENCI.OSURE 9.3 (Continued)
PI. ANT READINGS Initials /Date Panel H1RI - NNI 9.3 .3.9 I.OOP A RC WIDE RANGE TEMP Tc (1017 #1)
Reading = F (Baseline Information) /
9.3 .3.10 IDOP B RC WIDE RANGE TEMP Tc (T016 #1)
Reading = F (Baseline Information) /
9.3 .3.11 IDOP A PRESSURE - STEAM GEN (P801 #1) -
Reading = psig (Baseline Information) /
9.3 .3.12 IDOP B PRESSURE - STEAM GEN (P800 #1)
Reading = psig (Baseline Information] /
9.3 .3.13 LOOP A STM GEN LEVEL STARTUP (LO39 #1)
Reading = inches (Baseline Information) __
/
9.3 .3.14 IDOP B SIM GEN LEVEL STARTUP (LO40 #1)
Reading = inches (Baseline Information) /
Panel H1RC 9.3 .3.15 REACIOR COOI. ANT PRESSURE PR 21037 Reading = psig (Baseline Information] /
9.3 .3.16 REACIOR COOI. ANT PRESSURE PR 21038 Reading = psig (Baseline Information) / ;
9.3 .3.17 PRZR WATER TEMP (T009)
Reading = F ';
[ Baseline Information)
/
9.3 .3.18 PRESSURIZER LEVEL (G185) ,
, LR-21503 Reading = inches '
(Baseline Information) /
ENCLOSURE 9.3 PAGE 10 OF 16 1 l;
- Rev. O STP.ll54 - 40 ,
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4 ENCLOSURE 9.3 . (Continued) .
FLANT READINGS Initials /Date.
Panel H4BS 9.3 .3.19 RC LOOP A TH TI-21033A Reading = F (Baseline Information] /
9.3 .3.20 RC LOOP B TH TI-21034A Reading = F (Baseline Information] /
Panel H2SD 9.3 .3.21 Te TI-21025E Reading =- F ,
(Baseline Information) / ,
9.3 .3.22 Th TI-21031C Reading = F (Baseline Information] /
9.3 .3.23 RC PRESSURE. ,
PI-21051 Reading = psig (Baseline Information] / .
9.3 .3.24 RC PRESSURE PI-21050 Reading = psig (Baseline Information) /
- 9.3 .3.25 Te TI-21024C Reading = F l
(Baseline Ir. formation) /
9.3 .3.26 Th TI-21032C Reading = F j (Baseline Information) /
9.3 .3.27 "A" OTSG LEVEL LI-20509 Reading = inches '
(Baseline Information) /
9.3 .3.28 "A" OTSG PRESSURE PI-20547 Reading = psig
) (Baseline Information] /
9.3 .3.29 "B" OTSG LEVEL LI-20510 Reading = inches l (Baseline Information) /
ENCLOSURE 9.3 PAGE 11 OF 16 j 0
l Rev. O STP.ll54 - 41 W
.a .. . -- - . . . - - , - ,- - - - . . , . . e.--
ENCI.OSURE 9.3 (Continued)
PIRIT READINGS Initials /Date ;
9.3 .3.30 "B" OTSG PRISSURE PI-20548 Reading = . psig (Baseline Information] /
9.3 .3.31 PZR LEVEL (UNCOMPENSATED).
LI-21503D Reading = inches (Baseline Information) '/
9.3 .3.32 PZR LEVEL (UNCOMPENSATED)
LI-21503B Reading = inches (Baseline Information] /
9.3 .3.33 MU TANK LEVEL LI-23502C Reading = inches (Baseline Information] /
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4 ENCIDSURE ~ 9.3 (Continued)
PIANT READINGS Initials /Date- '
9.3 .4 Step 6.4 .13 !
Panel HISSE r 9.3 .4.1 S m GEN A PRESSURE CH A ,
PI-20545A Reading = psig ,
'[ Baseline Information] / -
9.3 .4.2 SIM GEN A PRESSURE CH B ;
PI-20545B Reading = psig (Baseline Information) / ,
9.3 .4.3 SIM GEN B PRESSURE CH A PI-20546A Reading =' psig ,
(Baseline Information) /
9.3 .4.4 STM GEN B PRESSURE CH B l PI-20546B Reading = psig !
(Baseline Information] /
9.3 .4.5 Sm GDi A I4 RANGE LEVEL CH A LI-20505A Reading = inches '
(Baseline Information] /
9.3 .4.6 Sm GDI A LO RANGE LEVEL CH B LI-20505B Reading = inches (Baseline Information] /
9.3 .4.7 SIM GDI B I4 RANGE LEVEL CH A
. LI-20506A Reading = inches I (Baseline Information) /
9.3 .4.8 SIM GEN B ID RANGE LEVEL CH B LI-20506B Reading = inches (Baseline Information] / ;
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I ENCIDSURE 9.3 PAGE 13 OF 16 Rev. O I STP.ll54 - 43
-~
ENCIDSURE 9.3 (Continued)
PIANT READINGS ' Initials /Date l Panel H1RI - NNI 9.3 .4.9 IDOP A RC WIDE RANGE TEMP Te (T017 #1)
Reading = F (Baseline Information] /
9.3 .4.10 IDOP B RC WIDE RANGE TEMP Te (T016 #1)
Reading = F (Baseline Information] /
9.3 .4.11 IDOP A PRESSURE - STEAM GEN (P801 #1)
Reading = psig (Baseline Information] /
9.3 .4.12 IDOP B PRESSURE - STEAM GDI (P800 #1)
Reading = psig (Baseline Information) /
9.3 .4.13 IDOP A STM GEN LEVEL STARTUP (LO39 #1)
Reading = inches (Baseline Information] /
9.3 .4.14 LOOP B STM GEN IIVEL STARIUP (LO40 #1)
Reading = inches (Baseline Information) /
Panel HlRC 9.3 .4.15 REACTOR COOIRIT PRESSURE PR 21037 Reading = psig (Baseline Information) /
9.3 .4.16 REACTOR COOIRIT PRESSURE PR 21038 Reading = psig (Baseline Information) /
9.3 .4.17 PRZR WATER TEMP (T009)
Reading = F (Baseline Information) /
9.3 .4.18 PRESSURIZER LEVEL IR-21503 Reading = inches (Baseline Information] /
ENCIDSURE 9.3 PAGE 14 OF 16 Rev. O STP.1154 - 44
ENCLOSURE 9.3 (Continued) <
PIANT READINGS Initials /Date Epnel H4BS 9.3 .4.19 RC LOOP A TH TI-21033A Reading = F (Baseline Information) /
9.3 .4.20 RC LOOP B TH 2
TI-21034A Reading = F ,
(Baseline'Information) /
Panel H2SD 9.3 .4.21 Te TI-21025E Reading = F (Baseline Information) / 1 9.3 .4.22 Th TI-21031C Reading = F ,
(Baseline Information) /
l 9.3 .4.23 RC PRESSURE r PI-21051 Reading = psig i (Baseline Information) / ,
9.3 .4.24 RC PRESSURE PI-21050 Reading = psig ;
(Baseline Information) /
f 9.3 .4.25 Te TI-21024C Reading = F (Baseline Information] / <
9.3 .4.26 Th TI-21032C Reading = F (Baseline Information) /
9.3 .4.27 "A" OTSG LIVEL
- LI-20509 Reading = inches (Baseline Information) /
l 9.3 .4.28 "A" OTSG PRESSURE PI-20547 Reading = psig '
(Baseline Information] /
9.3 .4.29 "B" OTSG LEVEL LI-20510 Reading = inches (Baseline Information) /
l i I
ENCIDSURE 9.3 PAGE 15 OF 16 l Rev. O STP.ll54 - 45
DiCIDSURE 9.3 (Continued)
PINrr READINGS Initla1s/Dato 9.3 .4.30 "B" OTSG PRESSURE PI-20548 Reading = psig (Baseline Information) /
9.3 .4.31 PZR LEVEL (UNCOMPDISATED)
LI-21503D Reading = inches (Baseline Information) /
9.3 .4.32 PZR LEVEL (UNCOMPDISATED)
LI-21503B Reading = inches (Baseline Information) /
9.3 .4.33 MU TANK LEVEL LI-23502C Reading = inches (Baseline Information) /
DiCIDSURE 9.3 PAGE 16 OF 16 Rev. O STP.ll54 - 46
I i
I i
'i ENCLOSURE 9.4 l IDADS SURVEYS !
STEP 6.6 .4 9.4.1 PERFORM an IDADS survey for the time span of sections 6.1, 6.2
' 6.3, 6.4 and 6.5 using the following IDADS points:
ANAIDG 4
F9000 MAKZUP FIDW FT-23603 (GPM)
F9003 HPI IDOP A FIDW FT-23807 (GPM)
LOO 8 RC PRESSURIZER LVL 1 DP (IN)
LOO 9 RC PRESSURIZER LVL 2 DP (IN)
P9035 RCS PRES IDOP A 4
P9036 RCS PRES IDOP B T016 RC LP B COLD LEG TEMP - WIDE RNG T017 RC LP A COLD LEG TEMP - WIDE RNG T051 SP OTSG A SHELL TDiP NO.1 (DEG F)
T052 SP OTSG B SHELL TEMP NO.1 (DEG F)
Use the Digital points listed in 9.4.4 as a mask.
I /
Completed By Date 2
i ENCICSURE 9.4 ~ PAGE 1 OF 4 Rev. O STP.1154 - 47
ENCLOSURE 9.4 (Continued)
IDADS SURVEYS
' STEP 6.6 .4 9.4,2 PERFORM an IDADS survey for the time span of s3ctions 6.1, 6.2 6.3, 6.4 and 6.5 using the following IDADS points:
ANAI.OG LO39 SP OTSG A SU RNG LVL (INH 2O)
LO40 SP CfrSG B SU RNG LVL (INH 2O).
L9811 EFIC CH A SG-A I.O RANGE LEVEL (INCHES)
L9812 EFIC CH B SG-B ID RANGE LEVEL (INCHES)
P800 SP OTSG B OUTLET STEAM PRESS P801 SP OTSG A OUTLET STEAM PRESS P9801 EFIC CH A SG-A PRESSURE P9802 EFIC'CH B SG-B PRESSURE Use the Digital points listed in 9.4.4 as a mask.
/
Completed By Date ENCIDSURE 9.4 PAGE 2 OF 4 Rev. O STP.1154 - 48
ENCIDSURE 9.4 (Continued)
IDADS SURVEYS STEP 6.6 .4 9.4.3 PERFORM an IDADS survey for the time span of sections 6.1, 6.2-6.3,-6.4 and 6.5 using the following IDADS points:
ANALOG F013 SP OTSG A SU.FDRIR SP'(INCHES)
F014 SP OTSG B SU FDWIR SP (INCHES)
F9660 AIW FIDW TO OTSG A IT-31802 (GPM)
F9661 AIW FIDW TO OTSG A- TT-31803 (GPM)
F9662 AIW FIDW TO OTSG B FT-31902 F9663 AIW FIDW TO OTSG B IT-31903 Use the Digital points listed in 9.4.4 as a mask.
/
Co:npleted By- Date l
ENCI4SURE 9.4 PAGE 3 OF 4 Rev. O STP.ll54 - 49 l
)
-- . -. ... . _ . = . - _.
ENCLOSURE 9.4 (Continued) '
IDADS SURVEYS STEP 6.6 .4 9.4.4- Use the following Digital IDADS points as the mask for each of '
surveys prepared for sections 6.1, c.;,.6.3, 6.4 and 6.5:
DIGITAL i E1416 EFIC B ISOLATE SWITCH E1417 EFIC A ISOLATE SWITCH I G1820 EFIC B SG-B MANUAL ADV'S G1821 EFIC A SG-A MANUAL ADV'S L1846 EFIC A SG-B MANUAL LVL CNTRL L1847 EFIC A SG-A MANUAL LVL CNTRL Zl822 ATMOSPHERIC DUMP VALVE W-20562B ;
i Z1823 ATMOSPHERIC DUMP VALVE W-20562A '
Z1824 ATMOSPHERIC DUMP VALVE W-20571B ,
i Z1825 ATMOSPHERIC DUMP VALVE W-20562C ,
Z1827 ATMOSPHERIC DUMP VALVE W-20571A Z1829 ATMOSPHERIC DUMP VALVE PV-20571C l 29020 HPI LOOP A SFV-23811 I i
l l
ENCIDSURE 9.4 PAGE 4 OF 4 I l
Rev. O STP.1154 - 50 l
ENCIDSURE 9.5 P90CEDURE A.51 EXCERPT TRANSFER FROM AFW TO MIW STEP 6.5 .20 m: W e Shift Supervisor may N/A any steps in Enclosure 9.5.
M: When the 'IF' part of an 'IF...THEN' statement is not satisfied the step is to be marked N/A.
M h e following Enclosure is to be performed by an Operator.
M: h e following is an excerpt from Procedure A.51, Rev. 34 for the transfer of OTSG B AEW to MIW.
Sign off lines for each step have been added for record keeping within this procedure.
1 7.6 Transferrina From Auxiliary Feedvater to ' Main Feedwater.
Initial Conditions:
1 7.6 .1 AEW has been initiated on HISSE A and/or B Initiate / Test matrix.
7.6 .2 At least one RCP is running.
7.6 .3 SFAS condition does not exist.
7.6 .4 At least one Main Feed Pump is operable.
I 7.6 .5 OTSG levels are being maintained by AIW at EFIC Iow Iovel Setpoint. (27.5 inches on EFIC Iow Range instruments)
Procedure: i l
7.6 .6 For recovery of MEW to the 'A' OTSG, perform the following.
CAUTION : STEPS IN THIS SECTION MUST BE )
PERFVRMED SEQUENTIAILY OR OTSG l
OVERFEED RESULTING IN EXCESSIVE HEAT TRANSFER MAY RESULT.
ENCIDSURE 9.5 PAGE 1 OF 6 i l
Rev. O STP.ll54 - 51 1
Initials /Date ENCIDSURE 9.5 (Continued) 1 A.51 EXCERPT Step 6.5 .20 ,
7.6 .6.1 Place in MAND and run the demands to ZERO on the following Bailey control Stations:
7.6 .6.1.1 TV-20575, 'A' Startup Feedwater Control Valve. /
7.6 .6.1.2 FV-20525, 'A' Main Feedwater Control valve. / "
7.6 .6.2 Verify CLOSED FV-20529, 'A' Main Feedwater Block Valve. /
4 7.6 .6.2.1 Verify CLOSED FV-20575, 'A' Startup Feedwater Control Valve. /
7.6 .6.2.2 Verify CLOSED FV-20525, 'A' Main Feedwater Control Valve. / ;
7.6 .6.3 If the 'SG-A MSL' Trip Lights are lit on either EFIC Initiate / Test Matrix, THEN Depress 'MA!UAL' and ' RESET' for :
'SG-A MSL' on the respective Initiate / Test 4
Matrix. /
i 7.6 .6.4 IE the 'SG-A MFW' Trip Lights are lit on ;
either EFIC Initiate / Test Matrix, THEN Depress ' MANUAL' and ' RESET' for '
'SG-A MFW' on the respective Initiate / Test Matrix. / ,
7.6 .6.5 Check that 'SG-A MSL' and 'SG-A MFW' Trip '
4 Lights are OFF on BOTM EFIC Initiate / Test Matrices. /
1
- 7.6 .6.6 Verify a Main Feed Pump in service per i
OP A.50, Main Feed Pumps System. /
i 7.6 .6.7 Verify OPEN HV-20515, 'A' OTSG Feedwater Isolation Valve. /
7.6 .6.8 Adjust Main Feed Pump speed so that Feedwater Valve p is 50 to 70 psid as indicated on 1 PDI-20567, 'A' Loop Feed Valve p, on MlRI. /
l ENCLOSURE 9.5 PAGE 2 OF 6 1
Rev. 0 l 4
STP.ll54 - 52 I
o Initials /Date ENCIDSURE 9.5 (Continued) i A.51 EXCERPT Step 6.5 .20 CAUTION : MAIN FEEDWATER SHALL BE REESTABLISHED ;
f SIDWLY IN ORDER TO MAINTAIN STABLE- ,
i PRIMARY TO SECONDARY HEAT TRANSFER CONDITIONS. ;
2 M: It may be necessar'f to raise OTSG level
. above minimum level setpoint in order to cause the A1H control valves to close. -
4 7.6 .6.9 Slowly OPEN W-20575, 'A' Startup Feedwater Control Valve. /
j 7.6 .6.10 Maintain Feedwater p at 50 to 70 psid, by changing the Main Feed Pump speed as required. / ,
7.6 .6.11 Continue with Steps 7.6.6.9 and 7.6.6.10 until W-20527 and W-20531, AIM to 'A' OTSG Flow Control Valves, are CLOSED. / '
7.6 .6.12 WHEN FV-20527, AFW to 'A' OTSG Flow Control Valve is CIDSED, M depress OVERRIDE and CIASE HV-20581, AFW
- Block Valve to 'A' OTSG. /
4 i l 7.6 .6.13 M W-20531, AIM to ' A' CfrSG Flow Control >
l Valve is CIDSED, M depress OVERRIDE and CLOSE HV-20577, AIV Block Valve to 'A' OTSG. /
7.6 .6.14 Place in AUTO W-20575, 'A' Startup Feedwater j control Valve. / ;
1 ;
I 7.6 .6.15 Verify 'A' OTSG IAvel is being maintained at the ;
j Iow IAvel Limit Setpoint. / l i
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a i i j i
l ENCIDSURE 9.5 PAGE 3 OF 6 1
Rev. 0 STP.1154 - 53 i I I l !
_,,,,y. - , , - . . . ,_....__,.,___m-..- . , _ _ . _ , . . . . , , - - .
Initials /Date l ENCLOSURE 9.5 (Continued)
A.51 EXCERPP Step 6.5 .20
'B' OTSG, perform 7.6 .7 For recovery of MW to the the following:
CAUTION : STEPS IN THIS SECTION MUST BE PERFORMED SEQUENTIALLY OR OTSG OVERFEED RESULTING IN EXCESSIVE MEAT TRANSFER MAY RESULT.
- 7. 6 .7.1 Place in MAND the following Baileyand run Stations:
Control the demands to ZERO on FV-20576, 'B' Startup Feedwater Control /
7.6 .7.1.1 Valve.
FV-20526, 'B' Main Feedwater Control /
7.6 .7.1.2 Valve.
Main Feedwater Verify CIDSED W-20530, 'B' / ,
7.6 .7.2 Block Valve.
Verify CIDSED W-20576, 'B' Startup
/ . _ _ _
7.6 .7.2.1 Feedwater Control Valve.
'B' Main Verify CLOSED W-20526, /
7.6 .7.2.2 Feedwater Control Valve.
7.6 .7.3 H the 'SG-B MSL' Trip Lights are lit on either EFIC Initiate / Test Matrix, for IHEN Depress ' MANUAL' and ' RESETSG-B / MSL' on Matrix.
7.6 .7.4 H the 'SG-B MW' Trip Lights are lit on either EFIC Initiate / Test Matrix, for 21IEN Depress ' MANUAL' and ' RESETSG-B / __
MFW Matrix.
Check that 'SG-B MSL' and 'SG-B MW' Trip 7.6 .7.5 Lights are OFF on Bom EFIC Initiate / Test __
/ ___
Matriceo.
ENCIDSURE 9.5 PAGE 4 OF 6 Rev. O STP.1154 - 54
Initials /Date ENCIDSURE 9.5 (Continued) '
A.51 EXCERPT Step 6.5 .20 J
7.6 .7.6 Verify a Main Feed Pump in service per OP A.50, Main Feed Pumps System. /
7.6 7.7 Verify OPEN HV-20516, 'B' CTISG Feedwater Isolation Valve. /
7.6 .7.8 Adjust Main Feed Pump speed so that Feedwater ,
Valve p is 50 to 70 psid as indicated on PDI-20568, 'B' Loop Feed Valve p, on HlRI. /
i CAUTION : MAIN FEEDWATER SHALL BE REESTABLISHED SIDWLY IN ORDER TO MAINTAIN STABLE PRIMARY 'IO SECONDARY HEAT TRANSFER CONDITIONS.
ILQIE : It may be necessary to raise CTISG level above minimum level setpoint in order to cause the AFW control valves to close.
7.6 .7.9 Slowly OPEN W-20576, 'B' Startup Feedwater ,
,. Control Valve. / !
t 7.6 .7.10 Maintain Feedwater p at 50 to 70 psid, by changing the Main Feed Pump speed as required. /
l 7.6 .7.11 Continue with Steps 7.6.7.9 and 7.6.7.10 until l TV-20528 and TV-20532, ABf to 'B' OTSG Flow Control Valves, are CLOSED. / l 1 . 1 7.6 .7.12 MIEN FV-20528, Anf to 'B' OTSG Flow' Control Valve is CIDSED, THDi depress OVERRIDE and CIDSE HV-20578, Ani j Block Valve to 'B' OTSG. /
7.6 .7.13 WHEN FV-20532, Ani to 'B' OTSG Flow Control .
Valve is CIDSED,
, IliEH depress OVERRIDE and CIDSE HV-20582, ADY Block Valve to
'B' OTSG. /
1 7.6 .7.14 Place in AUTO W-20576, 'B' Startup Feedwater i control Valve. / )
l l
4 4
t !
ENCIDSURE 9.5 PAGE 5 OF 6 l i
Rev. O STP.ll54 - 55
Initials /Date ENCIDSURE 9.5 (Contintud)
A.51 EXCERPF Step 6.5 .20 7.6 .7.15 Verify 'B' OTSG Imvel is being maintained at the Iow level Limit setpoint. /
7.6 .8 Depress MANUAL and RESET for ' AIM' on the ' A' Initiate / Test Matrix. /
7.6 .9 STOP P-319, Auxiliary Feedwater Pump. /
7.6 .10 Depress MANUAL and RESET for 'AIV' on the 'B'
- Initiate / Test Matrix. /
7.6 .11 STOP P-318, Auxiliary Feedwater Pump. / i 7.6 .12 Depress the EFIC A Control Initiate BLPB. /
7.6 .13 Verify the EFIC A Control Initiate BLPB is OFF. /
7.6 .14 Depress the EFIC B Control Initiate BLPB. /
7.6 .15 Verify the EFIC B Control Initiate BLPB is OFF. /
j ENCICSURE 9.5 PAGE 6 OF 6 i
1 1
j Rev. O j STP.ll54 - 56 i
1
DiCI4SURE 9.6 INDICATED VS. ACWAL ,
PRESSURIZER LEVEL
~~
FiAste 101-17 s 340 ~'~
- -1 IN2cA3:3 T5 ACTUAL4LIEL VI3 FJ:TERD3 120 AT 125 F Ftr3 Terp.
2193 peig.(6 F F)
. 5 1528 psig (60C8 F)
~ ~
f .- , 1030psig(550*T)
~ '
8
~
2F- _ / - ; 6M poig (5CC Fl f -- - j 232 sig (40COT) ;
~ : -
- --': _~-
$2 -sig ()CC0F)
T g -
_-~- -
_--~ __
E-- _-_- .-- _=
3 i.
~~
~ -
w ~ - _ - -~ _-~ _-
~
- l _ - - ~ -_:- - ~
g , . W- _ _
- 1
-- j 1
c ~-
g - ~ ) o._ _ - -
6
_ 'x =
g-_
\
- I
==; I fu % - __
)
i w_ _
$Q--_,_ - - ---
h --_- )
- _= l 100 150 200 250
- g. o 50 IN3 cam IITEL (WCOMPUSAm), inches DiCIDSURE 9.6 PAGE 1 OF 1 4
t Rev. O I STP.1154 - 57
ENCIDSURE 9.7 SIGNATURE / INITIALS SHEET NAME (PRINTED) SIGilATURE INITIAIS DiCIDSURE 9.7 PAGE _ OF_
t Rev. O STP.ll54 - 58
T ENCT.OSURE 9.8 Date Test Number STP.1154 RANCHO SECO TEST IDG TLE # _DATE_ _ TIME _ REMARFS
->F I
-w-l i
l l
1 ENCIDSURE 9.8 Rev. 0 l STP.1154 - 59 1 1
ENCIDSURE 9.9 TEST PROCEDURE AUTHORIZATION FORM TEST PPO.;EDURE NUMBER STP.1154 REVISION 0 TITLE REMOTE SHUTDOWN PANEL TEST
- _ _ = = - - - - - __== ==-- _ _ = = - =
PRETEST REVIDi COMPLETE /
TEST DIRECIOR .DATE RELEASED FOR PERFORMANCE /-
SRTP DIRECTOR DATE AUTHORIZATION TO CONDUCT TEST /
SRTP ASST DIRECTOR DATE
/
OPERATIONS SHDT SUPERVISOR DATE
- - , - - --___==r- --:==.====__====u___===
- TEST PERFORMANCE COMPLETE /
TEST DIRECTOR DATE
- READY FOR RESULTS REVID1 /
SRTP ASST DIRECTOR DATE
- INDICATES TESTING COMPLETE AND ACCEPTANCE CRITERIA HAS BEEN SATISFIED.
l ENCIDSURE 9.9 PAGE 1 OF 1 DID Rev. O STP.1154 - 60 l
GCA 88-248 Attachment 2 Comparison of OP-C.13A and STP.1154
GCA 88-248 Page 1 of 7 Attachment 2 COMPARISON OF OP-C.13A AND STP.1154 OP-C.13A STP.1154 "Remote Shutdown" "Remote Shutdown Test" Discussion Procedure initiated from Control Test initiated from stable hot 0 Initial C.13A actions ' automatically Room with: shutdown condition. MFW flow bring the plant to normal hot shut-to the OTSGs is isolated by the down pressures and temperatures with-0 Manual reactor trip MFW isolation valves. out further operator actions. The O Manual MFW pumps trip starting plant conditions of STP.ll54 0 Manual main turbine trip MFW pumps may be operated in essentially duplicate those of C.13A.
recirc mode to the condenser during STP to maintain them 0 Remote shutdown testing initiated in a standby status, at power was performed during initial plant startup. Manual reactor trips are planned to be performed during plant power ascension at 25%FP and 80%FP.
O Manual main turbine trip is planned to be demonstrated during plant power ascension at 25%FP.
Control Room is evacuated. Control Room is manned with The Control Room personnel and test normal shift complement. Control personnel at the remote shutdown panel of selected equipment and will maintain an open channel for functions is transferred to remote comunication during testing.
shutdown test personnel.
Page 2 of 7 COMPARISON OF OP-C.13A AND STP.1154 OP-C.13A STP.ll54 "Remote Shutdown" "Remote Shutdown Test" Discussion AFW is manually initiated from AFW is manually initiated by AFW/EFIC have been extensively tested, the Control Room (if time repositioning the EFIC isolation including the integrated test permits) at the EFIC channel A (electrical isolation from the STP.1113, "EFIC Hot Functional Test."
Initiated / Test matrix. Otherwise, Control Room) switches. AFW (if time did not permit initia- does not feed the OTSGs until tion from the Control Room) AFW low OTSGs level is sensed.
initiates when EFIC initiates on low OTSG level.
OTSG level is controlled auto- Automatic AFW control of OTSG OTSG level fill to the natural matically by AFW. A procedure level is demonstrated upon MFW circulation setpoint (317 inches) was
!!0TE states that if at any time isolation. Later in procedure, demonstrated by STP.667.
EFIC does not provide proper manual OTSG 1evel control is secondary plant control in AUTO, demonstrated in each generator.
then the operator should place the affected components in MANUAL.
ADV control of secondary side ADV control of secondary side STP.ll54 demonstrates both pressure is maintained automat- pressure is maintained auto- manual and automatic control of ically by EFIC. A procedure matically by EFIC. Later in test, secondary side pressure.
NOTE states that if at any time manual ADV control of secondary EFIC does not provide proper side pressure is demonstrated In both C.13A and STP.ll54, the-secondary plant control in AUT0, on both trains. TBVs are electrically isolated from then the operator should place the Control Room, and closed from the affected components in MANUAL. the remote shutdown panel.
m Page 3 of 7 COMPARISON OF OP-C.13A AND STP.ll54 i
OP-C.13A STP.Il54 ,
"Remote Shutdown" "Remote Shutdown Test" Discussion Renote shutdown panel indicators Remote shutdown panel indicator STP.1154 demonstrates the proper are scanned periodically to readings are recorded at various operation of the remote shutdown panel assure their proper operation and points during testing. indicators.
to verify control of plant response.
Shift Supervisor performs Not necessary and not C.13A training and walk-throughs emergency plan responsibilities. demonstrated by STP.1154 provide assurance that this function can be adequately performed.
Shift Supervisor maintains contact Communications capabilities are C.13A training and walk-throughs via walkie-talkies with operators demonstrated by STP.1154. provide assurance that these functions performing action within the Several isolation switches are can be adequately performed.
pl ant. Operator: performing positioned at locations away from actions away from the remote the remote shutdown panel. The shutdown panel are dispersed. number of personnel perfonning STP.1154 will not exceed that required by C.13A.
RCPs are secured to prevent RCPs remain operating to Discussion on justification for possible damage to the RCP provide forced circulation and tripping the RCPs in C.13A is provided seal packages. Natural circula- mixing. in Attachment 4. Natural circulation tion is established in the has been demonstrated for B&W plants RCS. on numerous occasions. Forced circulation is the preferred test configuration.
Page 4 of 7 COMPARISON OF OP-C.13A AND STP.1154 OP-C.13A STP.ll54 "Remote Shutdown" "Remote Shutdown Test" Discussion Reactor coolant letdown is isola- Reactor coolant letdown is main- Reactor coolant letdown and RCP bleed ted (SFV-22009 is closed). RCP tained constant from the Control off are necessary for the RCPs to bleed off is isolated (SFV-24013 Room. RCP bleed off is not receive sufficient seal injection is closed). manipulated. flow.
Control Room action to control primary system inventory is not called for unless the pressurizer level goes outside the band of 45-290 inches.
RCP seal injection is con- RCP seal injection flow is maire- RCP seal injection control is trolled by local manual opera- tained constant at nominal rate maintained in the Control Room during tion of the valve handwheel, for four operating RCPs (approx- STP.ll54 to minimize unnecessary risk observing a local flow meter. imately 40 gpm). to the RCP seals. Local manual opera-RCP seal injection flow is tion of seal inject valve was adjusted to approximately Control Room action to control demonstrated when the manual operator 12 gpm total flow. primary system inventory is not was installed in 1985.
called for unless the pressurizer level goes outside the band of 45-290 inches.
The RCS makeup flow path is Normal makeup system lineups are Remote shutdown panel control of realigned with the BWST feeding maintained, with recirc back to SFV-25003 (DHR Pump A suction from the makeup tank and the alternate the makeup pump remaining opera- BWST) was demonstrated by STP.1087.
l HPI/ makeup pump recirc path to ing throughout test to provide Remote shutdown panel control of l
the BWST established. Operator RCP seal injection. SFV-23508 (MU Tank Isolation) was manually starts the "A" HPI/ makeup demonstrated by STP.1091. C.13A pump from outside the Control Room. training and walk-throughs provide sufficient assurance that the timing and communications for manual valve lineups are adequate.
Page 5 of 7 COMPARISON OF OP-C.13A AND STP.1154 OP-C.13A STP.1154 "Remote Shutdown" "Remote Shutdown Test" Discussion Operators position and verify Not demonstrated in STP.1154. C.13A training and walk-throughs proper electrical power dis- provide assurance that these electri-tribution assuming train B must cal power alignment functions can be be deenergized to prevent spurious adequately performed. Emergency operation and (if appropriate) diesel generator operation has been assuming a loss-of-site-power. demonstrated by Technical Specifica-tion surveillance testing.
Operators deenergize various Not demonstrated by STP.ll54 C.13A training and walk-throughs equipment which cannot be provide assurance that equipment electrically isolated from the deenergization functions can be Control Room. This equipment properly performed. The Control Room includes certain HPI valves, the maintains suff':ient control of EMOV, pegging steam, reheater plant equipment during STP.1154 to isolations, normal makeup valves, take effective action to assure plant 3B busses, spray pumps, NSCW valves safety in the unexpected case that the to decqy heat and RB Coolers, test does not proceed as planned. For Main Steam to Aux Steam, decay example, the Control Room maintains heat cross tie, and LPI valves. control of the ADV block valves, the AFW motor-operated isolation valves, the normal makeup valve, and the HPI pump trip. Safety features equipment are maintained in normal standby lineups except as necessary for remote demonstrations.
Page 6 of 7 -
COMPARIS0N OF OP-C.13A AND STP.1154 OP-C.13A STP.1154 "Remote Shutdown" "Remote Shutdown Test" Discussion Operators electrically isolate Isolation demonstrated by C.13A isolates various train A from the Control Room selected STP.ll54 include the following: equipment to assure spurious operation train A equipment. due to Control Room fire does not EFIC AFW CONTROL VALVE LOOP A result in loss of plant control.
EFIC ADV CONTROL LOUP A STP.1154 only isolates those controls EFIC AFW CONTROL VALVE LOOP B which are demonstrated from the remote EFIC ADY CONTROL LOOP B shutdown panel. Post-installation HPI LOOP A SFV-23811 testing along with C.13A training and walk-throughs provides adequate assurance that C.13A isolations can be adequately accomplished.
Primary system inventory is RCP seal injection and RCS letdown STP.ll54 demonstrates operation of maintained by 12 gpm RCP seal flows are maintained constant. SFV-23811 from the remote shutdown injection flow with any additional Primary side inventory control is panel to control primary system requirements through SFV-23811 accomplished by operation of inventory.
to maintain 100-200 inches in SFY-23811 from the remote shutdown the pressurizer, panel to maintain pressurizer level in a band of 85-135 inches uncompen-sated (100-200 inches compensated).
The remote shutdown panel operator is to minimize charging to the RCS by anticipating pressurizer level changes which will result from heatup and cooldown transients.
Control Room action to control pri-mary system inventory is not called for unless the pressurizer level goes outside the band of 45-290 inches.
r__ __ ____ _ _ _ . -. _ _ _ _ _ _ _ _ _ _ _ - _ _ - - - - - _ _ _ - -___ _ _ -----___ __ - ___ _
Page 7 of 7 COMPARISON OF OP-C.13A AND STP.1154 OP-C.13A STP.1154 "Remote Shutdown" "Remote Shutdown Test" Discussion Cooldown the RCS using the ADVs RCS temperature control via the STP.1154 demonstrates control of to maintain pressurizer level at ADVs is demonstrated from the secondary side decay removal capabil-100-200 inches. RCS Tave is not remote shutdown panel by ity from the remote shutdown panel.
reduced below 5250F. series of three RCS cooldowns and heatups of approximately 200F.
The total of the cooldowns will be at least 500F. Hot shutdown condi-tions will be maintained for at least 30 minutes using H2SD controls.
GCA 88-248 Attachment 3 OP-C 13A Remote Shutdown 1
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