ML17319A960: Difference between revisions

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{{#Wiki_filter:-PRESSURIZER VENTINGOPERATION AEP/AMPREYISION0MARCH19818107210420 810715PDRADOCK05000315F'DR  
{{#Wiki_filter:-PRESSURIZER VENTING OPERATION AEP/AMP REYISION 0 MARCH 1981 8107210420 810715 PDR ADOCK 05000315 F'DR  
~1 PRESSURIZER VENTINGOPERATION A.PURPOSETheobjective ofthisinstruction istospecifytherequiredoperatoractionsandprecautions necessary toventnon-condensible gasesfromthepressurizer vaporspace.Thisinstruction mayalsobeusedasanalternate methodofdepressurizing
~1 PRESSURIZER VENTING OPERATION A.PURPOSE The objective of this instruction is to specify the required operator actions and precautions necessary to vent non-condensible gases from the pressurizer vapor space.This instruction may also be used as an alternate method of depressurizing
'thereactorcoolantsystemwhichmayberequiredbytheactionsofanotheroperating instruction.
'the reactor coolant system which may be required by the actions of another operating instruction.
B.INITIALCONDITIONS CAUTION:Thepressurizer ventshouldrot'beusedastheprimarymeansofdepressurizing theRC$duringaninadequate corecoolingevent.RefertoInadequate CoreCoolingGuidelines-forappropriate operatoractionsandprecautions.
B.INITIAL CONDITIONS CAUTION: The pressurizer vent should rot'be used as the primary means of depressurizing the RC$during an inadequate core cooling event.Refer to Inadequate Core Cooling Guidelines-for appropriate operator actions and precautions.
NOTE:Thisguideline assumesthatthereactorcontainment conditions arenearnormal"nd:anaccuratepressurizer pressureandlevelindication
NOTE: This guideline assumes that the reactor containment conditions are near normal"nd: an accurate pr essurizer pressure and level indication
<isavailable.
<is available.
CAUTION:Donotopenthepressurizer ventwhilethesafetyinjection systemisinoperation unlessanRCSdepressurization isrequiredbyanEmergency Operating Instruction.
CAUTION: Do not open the pressurizer vent while the safety injection system is in operation unless an RCS depressurization is required by an Emergency Operating Instruction.
1.Samplinghasindicated thepresenceofasignificant quantityofnon-condensible gasesinthepressurizer vaporspace.2.Abnormal'onditions havebeenexperienced withthepressurizer levelandpressurecontrolsystems3.Pressurizer sprayis-ineffective inreducingthepressurizer pressure.
1.Sampling has indicated the presence of a significant quantity of non-condensible gases in the pressurizer vapor space.2.Abnormal'onditions have been experienced with the pressurizer level and pressure control systems 3.Pressurizer spray is-ineffective in reducing the pressurizer pressure.March, 1981 Revision 0 Page 1 4.Plant events have occurred (such as inadvertent gas addition, accumulator tank discharge, core uncovery, etc.)that may result in non-condensible gases being collected in the pressurizer.
March,1981Revision0Page1 4.Planteventshaveoccurred(suchasinadvertent gasaddition, accumulator tankdischarge, coreuncovery, etc.)thatmayresultinnon-condensible gasesbeingcollected inthepressurizer.
5.An RCS depressurization is required.by another operating instruction and pressurizer spray is~not available and/or the use of the power operated relief~valves is not desirable.
5.AnRCSdepressurization isrequired.byanotheroperating instruction andpressurizer sprayis~notavailable and/ortheuseofthepoweroperatedrelief~valvesisnotdesirable.
6.The reactor vessel head has been vented, if required, prior to venting the pressurizer
6.Thereactorvesselheadhasbeenvented,ifrequired, priortoventingthepressurizer
., C.IMMEDIATE ACTIONS None KttE'P i NOTE: If the pressurizer is being vented because large quantities of non-condensible gases are preventing a depressurization, then the actions of steps marked by an asterisk are not applicable.
.,C.IMMEDIATE ACTIONSNoneKttE'PiNOTE:Ifthepressurizer isbeingventedbecauselargequantities ofnon-condensible gasesarepreventing adepressurization, thentheactionsofstepsmarkedbyanasteriskarenotapplicable.
1.Terminate any changes to the reactor coolant system that may be in progress and bring the RCS to as-close to a steady-state condition.
1.Terminate anychangestothereactorcoolantsystemthatmaybeinprogressandbringtheRCStoas-closetoasteady-state condition.
as possible.*2.If not already performed, sample the pressurizer vapor space for the presence of non-condensible gases.If a signficant quantity of non-condensible gases is not found, then return to the appropriate operating instruction.
aspossible.
March, 1981 Revision 0 Page 2
*2.Ifnotalreadyperformed, samplethepressurizer vaporspaceforthepresenceofnon-condensible gases.Ifasignficant quantityofnon-condensible gasesisnotfound,thenreturntotheappropriate operating instruction.
!.'1 l~g~3.In preparation for venting;isolate the containment purge and exhaust systems and the pressure vacuum relief line and start all available containment air circu lation equipment 4.Increase the RCS sub-cooling to (insert plant specific value wnich is 50'F above the value which is the sum of the errors for the temperature measurement system used, and for the pressure measurement system translated into temperature using the sat-uration tables)by either initiating an RCS pressurization or by dumping steam from the non-faulted steam generators.
March,1981Revision0Page2
NOTE: If the pressurizer is being vented for the purpose of initiating RHR operation and the RCS temperature is less than 350'F, then additional sub-cooling margin is not required.5.Perform the actions of Appendix A to determine the maximum allowable time period or venting.6.If no+already performed, manually block the low pressure SI-initiation if the permissive is energized.
!.'1 l~g~3.Inpreparation forventing;isolatethecontainment purgeandexhaustsystemsandthepressurevacuumrelieflineandstartallavailable containment aircirculationequipment 4.IncreasetheRCSsub-cooling to(insertplantspecificvaluewnichis50'Fabovethevaluewhichisthesumoftheerrorsforthetemperature measurement systemused,andforthepressuremeasurement systemtranslated intotemperature usingthesat-urationtables)byeitherinitiating anRCSpressurization orbydumpingsteamfromthenon-faulted steamgenerators.
CAUTION:-The venting operation may result in pressure decreasing below the SI setpoint.Action should be taken to manually block the automatic SI signal when the permissive is energized.
NOTE:Ifthepressurizer isbeingventedforthepurposeofinitiating RHRoperation andtheRCStemperature islessthan350'F,thenadditional sub-cooling marginisnotrequired.
*7.Increase charging flow to maximum to limit the depressurization rate during the venting period.Pressurizer level will trend upward during the venting operation.
5.PerformtheactionsofAppendixAtodetermine themaximumallowable timeperiodorventing.6.Ifno+alreadyperformed, manuallyblockthelowpressureSI-initiation ifthepermissive isenergized.
March, 1981 Revision 0 Page 3 0 I E 8.Open the vent isolation valves in one pressurizer vent flowpath.NOTE'f one or both valves fail to open, close both valves and open the isolation valves in the parallel flow path.9.Close both vent isolation valves when: a)The time period determined in Step 5 is met, OR*b)Pressurizer pressure decreases by 200 psi, OR c)Pressurizer level increases above 80 of span, OR d)Reactor coolant sub-cooling deer ases below (insert plant specific valve which is the sum of the errors for the temperature measurement system used, and for the pressure measurement system translated into temperature using the'aturation tables).I 10.Re-establish normal charging flow and restore the pressurizer water level to the normal operating range.ll.If the venting was terminated prior to removing enough of the non-condensible gases to restore normal pressurizer control or to reduce pressure to the required condition, then return to Step 4.NOTE: If multiple venting operations are required and the containment hydrogen concentration is equal to or greater than 3 volume percent, the provisions must be made to March, 1981 Revision 0 Page 4 5 BESSURIZ ER F l&IJRE 2 I'ate J a/a%i DONALD C.COO<NUCLEAR rLANT uNIT NOS.1 AND.Z  
CAUTION:-Theventingoperation mayresultinpressuredecreasing belowtheSIsetpoint.
"'A,HaTL r CCN7I't SKI a C t1~---0 Ig I'V v+-e)ILL EI.O~I': flILl.nt'L'I4~-~OLf.;.:)I'b UEN7;RIAL;a='ThMC.L FLIa.-n~g MQT a-"t~<<l>CIIf.~EMIR UrdIT TflAIIJ-ar<I ZmTr-r~2 E A.C.>l 6, TIEAI~!2 E./a E.!)B'VRA,I<SRN E Fdg Sort[REACTOR.RNO PRCS~uR I?.Eg VENTS'L'ar Is(7OPa XILgl'llUab Ut.N'V LIN>>T I=.i~a Y"~fl Y>>'5 a'.anal Qt f.5t.h 0 F.a"L c.Iat>I 0 Vni Va=I I I I I I I ll'l ALACK 0I417 8 t'a'6.5 o Ti l 5 L'ii Ht.Rag aaI!.:1~Ll".'aa=a TLatb)~'.IQQ'i I:.Dovsa-'~liaa.Ate SOLE, HO I Ea VALV F I I I I I I I I I.I I,)I Hl ALAIIVI U/ah l T r\~tlgfaa>X)EN~t'LaM a C<SL.t'.l I.ltF.'3t'I VKhhY'lMF.
Actionshouldbetakentomanuallyblocktheautomatic SIsignalwhenthepermissive isenergized.
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*7.Increasechargingflowtomaximumtolimitthedepressurization rateduringtheventingperiod.Pressurizer levelwilltrendupwardduringtheventingoperation.
<<~I 0 0 VALVE NUMBER SHT.NO.FUNCTION FLOYI I}I A G SVSTEIn 924i9A 92498 92490 9249D 9249E 9249P 9250A 9250B 92500 9250D 9250E 9250" 9236 9239A 9239B 9244 330 331 332 333 334 335 336 337 33B 339 340 341 342 343 344 DRV}NING CONTROL SYSTEM DRUM}IING CONTROL SYSTEH DRfRf}IING CO}<<TROL SYSTEM DRU}OIING CONTROI SYSTFH DRU}f}GNG CONTROI.SYSTEM DRV}OfING CONTROL SYSTFH DRLYfMI}}C CONTROL SYSTAf DRIDQ}ING COhTROL SYST}2f DRIBQflttG CONTROL SYSTEM DR}BOflt}C CONTROL SYSTEM DRUHHINC CONTROL SYSTEH DRUMMING CONTROL SYSTEH DRIPHIhG CONTROL SYSTEM DRU}0}ttiC CONTROL SYSTKH DRU}QII}tC CONTROL SYSTEM 110E197 Sh.2 110E197 Sh.2 110E197 Sh.2 IIOLI97>>.2 110E 197 S}1.2 110E197 S}I.2 110E197 Sh.2 110E197 Sh.2 110E197 Sh.2 110E197 Sh.2 I IOEI97 Sh.2 110E197 Sh.2 110E197 S}L.2 110E197 Sh.2 110E197 Sh.2 I-PV-I<<3-PV-I 220 I-PV-2 2-PV-R 220 I-Pv-3 2-Pf-3 2zl I-PV-4}2-FV-4 22 I PRESSURI'ZKF<<'.
March,1981Revision0Page3 0IE 8.Opentheventisolation valvesinonepressurizer ventflowpath.
VER I ISOLATION PRESSURE!ZER.
NOTE'foneorbothvalvesfailtoopen,closebothvalvesandopentheisolation valvesintheparallelflowpath.9.Closebothventisolation valveswhen:a)Thetimeperioddetermined inStep5ismet,OR*b)Pressurizer pressuredecreases by200psi,ORc)Pressurizer levelincreases above80ofspan,ORd)Reactorcoolantsub-cooling deerasesbelow(insertplantspecificvalvewhichisthesumoftheerrorsforthetemperature measurement systemused,andforthepressuremeasurement systemtranslated intotemperature usingthe'aturation tables).I10.Re-establish normalchargingflowandrestorethepressurizer waterleveltothenormaloperating range.ll.Iftheventingwasterminated priortoremovingenoughofthenon-condensible gasestorestorenormalpressurizer controlortoreducepressuretotherequiredcondition, thenreturntoStep4.NOTE:Ifmultipleventingoperations arerequiredandthecontainment hydrogenconcentration isequaltoorgreaterthan3volumepercent,theprovisions mustbemadetoMarch,1981Revision0Page4 5BESSURIZERFl&IJRE2I'ateJa/a%iDONALDC.COO<NUCLEARrLANTuNITNOS.1AND.Z  
VEh'T ISOLA~ION PRE.SBURI Z E'VE.NT150LAT ION P'R'FSSURIZEI." VER i!SOLAR 109<<zG54c44 Zf"5 C44 2fc 54C4 4 zf-.5m4 4 I-HV'~!>-I-IV-.l 220 HEAD VE.I'<<T ISO}ANION zc 5 con I-IHV-2.<<"I-IV-c;P<<Y I-WV-3 2 HV-3 221 I-HV-4, 2.I-IV-4 22 I-IK&~}VFN I I&r31 WW}OM HK AD VE.NT IGC>LA'PION I-IE.<<E<<D VE.N ISOLA ION 2Q 5-SC4 Zt" 54C-k 4 Zf" 6 4C44 i'i EC}<ate gI<<!f If;EL<<<<'EY0 27<<50 g~t<<rn<I<<'<<P.~g C<<AE<<<</Akll 359>><<~I I r}<<i i'L>><<<<r<</I~ll i>>>><<I>><<J<<<<t l X 0 T-0<<7<<<<<<1<<<<<<I<<<<fl U o~~Qg ny<<o r<<O>n A 0 O Z I Z 0 r m n tV~>>>>pl-~.Qz 0 e~~~)a) 4J I O lOA~p Rll OPEN RI2 R21 D PEII R22 VAt.V E I-PV-3 2-PV-3 I-PV.4 2-PV-+I-HV-3 2-HV.3 I-HV-$2-HV" r IOA, Ncr.0 ENCRGI=E.2o TO OPEN he 20 20 n rr.O ra.20[hc NOTES I.5 UALVE NO.2.I/O SEE SS.9EV.~AM.P.~Sate.T l~3.CASL=TRAIN"'rp'AGN=TIC REE.D SWI TCHES Yi"s'i~pnouse Ele"Ir'c Corp"raliol Mv~,,, INDIANA AND MICHIGAN ELECTRIC CO.~LQC C UNIT NO 182.ELEMENTARY Vr 1RIII 1 6 rip/g J.6a-~/A>/~SOLE.NOID VAL'VE 5QLBQ.7 SHEET-22 I 0 CP 5~
"'A,HaTLrCCN7I'tSKIaCt1~---0IgI'Vv+-e)ILLEI.O~I':flILl.nt'L'I4~-~OLf.;.:)I'b UEN7;RIAL;a='ThMC.LFLIa.-n~gMQTa-"t~<<l>CIIf.
4.The maximum allowable venting period is then determined from curve 81 (RCS Pressure vs.Hydrogen Flow Rate).This curve was generated from a calculation which determined the flow rate of hydrogen at various RCS pressures through a 3/8" orificed line.The calculation assumed pure hydrogen which is conservative since the gaseous void in the vessel head will probably be some mixture of gases including steam.February, 1981 Revision 0 Page 12
~EMIRUrdITTflAIIJ-ar<IZmTr-r~2EA.C.>l6,TIEAI~!2E./aE.!)B'VRA,I<SRNEFdgSort[REACTOR.RNOPRCS~uRI?.EgVENTS'L'arIs(7OPaXILgl'llUabUt.N'VLIN>>TI=.i~aY"~flY>>'5a'.analQtf.5t.h0F.a"Lc.Iat>I0VniVa=IIIIIIIll'lALACK0I4178t'a'6.5oTil5L'iiHt.RagaaI!.:1~Ll".'aa=aTLatb)~'.IQQ'i I:.Dovsa-'~liaa.AteSOLE,HOIEaVALVFIIIIIIIII.II,)IHlALAIIVIU/ahlTr\~tlgfaa>X)EN~t'LaMaC<SL.t'.l I.ltF.'3t'I VKhhY'lMF.
~~r y~~~ooae~0~Oat~~4~0~0~O~~0 ATTACHi~)ENT 5 TO AEP:HRC:05i'8}}
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<<~I00VALVENUMBERSHT.NO.FUNCTIONFLOYII}IAGSVSTEIn924i9A92498924909249D9249E9249P9250A9250B925009250D9250E9250"92369239A9239B924433033133233333433533633733B339340341342343344DRV}NINGCONTROLSYSTEMDRUM}IING CONTROLSYSTEHDRfRf}IING CO}<<TROLSYSTEMDRU}OIING CONTROISYSTFHDRU}f}GNG CONTROI.SYSTEMDRV}OfING CONTROLSYSTFHDRLYfMI}}C CONTROLSYSTAfDRIDQ}ING COhTROLSYST}2fDRIBQflttG CONTROLSYSTEMDR}BOflt}C CONTROLSYSTEMDRUHHINCCONTROLSYSTEHDRUMMINGCONTROLSYSTEHDRIPHIhGCONTROLSYSTEMDRU}0}ttiC CONTROLSYSTKHDRU}QII}tC CONTROLSYSTEM110E197Sh.2110E197Sh.2110E197Sh.2IIOLI97>>.2110E197S}1.2110E197S}I.2110E197Sh.2110E197Sh.2110E197Sh.2110E197Sh.2IIOEI97Sh.2110E197Sh.2110E197S}L.2110E197Sh.2110E197Sh.2I-PV-I<<3-PV-I220I-PV-22-PV-R220I-Pv-32-Pf-32zlI-PV-4}2-FV-422IPRESSURI'ZKF<<'.
VERIISOLATION PRESSURE!ZER.
VEh'TISOLA~ION PRE.SBURI ZE'VE.NT150LAT IONP'R'FSSURIZEI."
VERi!SOLAR109<<zG54c44Zf"5C442fc54C44zf-.5m44I-HV'~!>-I-IV-.l 220HEADVE.I'<<TISO}ANIONzc5conI-IHV-2.<<"I-IV-c;P<<YI-WV-32HV-3221I-HV-4,2.I-IV-422I-IK&~}VFN II&r31WW}OMHKADVE.NTIGC>LA'PION I-IE.<<E<<D VE.NISOLAION2Q5-SC4Zt"54C-k4Zf"64C44i'iEC}<ategI<<!fIf;EL<<<<'EY0 27<<50g~t<<rn<I<<'<<P.~gC<<AE<<<</Akll 359>><<~IIr}<<ii'L>><<<<r<</I~lli>>>><<I>><<J<<<<tlX0T-0<<7<<<<<<1<<<<<<I<<<<flUo~~Qgny<<or<<O>nA0OZIZ0rmntV~>>>>pl-~.Qz 0e~~~)a) 4JIOlOA~pRllOPENRI2R21DPEIIR22VAt.VEI-PV-32-PV-3I-PV.42-PV-+I-HV-32-HV.3I-HV-$2-HV"rIOA,Ncr.0ENCRGI=E.
2oTOOPENhe2020nrr.Ora.20[hcNOTESI.5UALVENO.2.I/OSEESS.9EV.~AM.P.~Sate.Tl~3.CASL=TRAIN"'rp'AGN=TIC REE.DSWITCHESYi"s'i~pnouse Ele"Ir'cCorp"raliol Mv~,,,INDIANAANDMICHIGANELECTRICCO.~LQCCUNITNO182.ELEMENTARY Vr1RIII16rip/gJ.6a-~/A>/~SOLE.NOID VAL'VE5QLBQ.7SHEET-22I 0CP5~
4.Themaximumallowable ventingperiodisthendetermined fromcurve81(RCSPressurevs.HydrogenFlowRate).Thiscurvewasgenerated fromacalculation whichdetermined theflowrateofhydrogenatvariousRCSpressures througha3/8"orificedline.Thecalculation assumedpurehydrogenwhichisconservative sincethegaseousvoidinthevesselheadwillprobablybesomemixtureofgasesincluding steam.February, 1981Revision0Page12
~~r y~~~ooae~0~Oat~~4~0~0~O~~0 ATTACHi~)ENT 5TOAEP:HRC:05i'8}}

Revision as of 10:06, 6 July 2018

Pressurizer Venting Operation.
ML17319A960
Person / Time
Site: Cook  American Electric Power icon.png
Issue date: 03/31/1981
From:
INDIANA MICHIGAN POWER CO. (FORMERLY INDIANA & MICHIG
To:
Shared Package
ML17319A959 List:
References
AEP-AMP, PROC-810331-01, NUDOCS 8107210420
Download: ML17319A960 (18)


Text

-PRESSURIZER VENTING OPERATION AEP/AMP REYISION 0 MARCH 1981 8107210420 810715 PDR ADOCK 05000315 F'DR

~1 PRESSURIZER VENTING OPERATION A.PURPOSE The objective of this instruction is to specify the required operator actions and precautions necessary to vent non-condensible gases from the pressurizer vapor space.This instruction may also be used as an alternate method of depressurizing

'the reactor coolant system which may be required by the actions of another operating instruction.

B.INITIAL CONDITIONS CAUTION: The pressurizer vent should rot'be used as the primary means of depressurizing the RC$during an inadequate core cooling event.Refer to Inadequate Core Cooling Guidelines-for appropriate operator actions and precautions.

NOTE: This guideline assumes that the reactor containment conditions are near normal"nd: an accurate pr essurizer pressure and level indication

<is available.

CAUTION: Do not open the pressurizer vent while the safety injection system is in operation unless an RCS depressurization is required by an Emergency Operating Instruction.

1.Sampling has indicated the presence of a significant quantity of non-condensible gases in the pressurizer vapor space.2.Abnormal'onditions have been experienced with the pressurizer level and pressure control systems 3.Pressurizer spray is-ineffective in reducing the pressurizer pressure.March, 1981 Revision 0 Page 1 4.Plant events have occurred (such as inadvertent gas addition, accumulator tank discharge, core uncovery, etc.)that may result in non-condensible gases being collected in the pressurizer.

5.An RCS depressurization is required.by another operating instruction and pressurizer spray is~not available and/or the use of the power operated relief~valves is not desirable.

6.The reactor vessel head has been vented, if required, prior to venting the pressurizer

., C.IMMEDIATE ACTIONS None KttE'P i NOTE: If the pressurizer is being vented because large quantities of non-condensible gases are preventing a depressurization, then the actions of steps marked by an asterisk are not applicable.

1.Terminate any changes to the reactor coolant system that may be in progress and bring the RCS to as-close to a steady-state condition.

as possible.*2.If not already performed, sample the pressurizer vapor space for the presence of non-condensible gases.If a signficant quantity of non-condensible gases is not found, then return to the appropriate operating instruction.

March, 1981 Revision 0 Page 2

!.'1 l~g~3.In preparation for venting;isolate the containment purge and exhaust systems and the pressure vacuum relief line and start all available containment air circu lation equipment 4.Increase the RCS sub-cooling to (insert plant specific value wnich is 50'F above the value which is the sum of the errors for the temperature measurement system used, and for the pressure measurement system translated into temperature using the sat-uration tables)by either initiating an RCS pressurization or by dumping steam from the non-faulted steam generators.

NOTE: If the pressurizer is being vented for the purpose of initiating RHR operation and the RCS temperature is less than 350'F, then additional sub-cooling margin is not required.5.Perform the actions of Appendix A to determine the maximum allowable time period or venting.6.If no+already performed, manually block the low pressure SI-initiation if the permissive is energized.

CAUTION:-The venting operation may result in pressure decreasing below the SI setpoint.Action should be taken to manually block the automatic SI signal when the permissive is energized.

  • 7.Increase charging flow to maximum to limit the depressurization rate during the venting period.Pressurizer level will trend upward during the venting operation.

March, 1981 Revision 0 Page 3 0 I E 8.Open the vent isolation valves in one pressurizer vent flowpath.NOTE'f one or both valves fail to open, close both valves and open the isolation valves in the parallel flow path.9.Close both vent isolation valves when: a)The time period determined in Step 5 is met, OR*b)Pressurizer pressure decreases by 200 psi, OR c)Pressurizer level increases above 80 of span, OR d)Reactor coolant sub-cooling deer ases below (insert plant specific valve which is the sum of the errors for the temperature measurement system used, and for the pressure measurement system translated into temperature using the'aturation tables).I 10.Re-establish normal charging flow and restore the pressurizer water level to the normal operating range.ll.If the venting was terminated prior to removing enough of the non-condensible gases to restore normal pressurizer control or to reduce pressure to the required condition, then return to Step 4.NOTE: If multiple venting operations are required and the containment hydrogen concentration is equal to or greater than 3 volume percent, the provisions must be made to March, 1981 Revision 0 Page 4 5 BESSURIZ ER F l&IJRE 2 I'ate J a/a%i DONALD C.COO<NUCLEAR rLANT uNIT NOS.1 AND.Z

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<<~I 0 0 VALVE NUMBER SHT.NO.FUNCTION FLOYI I}I A G SVSTEIn 924i9A 92498 92490 9249D 9249E 9249P 9250A 9250B 92500 9250D 9250E 9250" 9236 9239A 9239B 9244 330 331 332 333 334 335 336 337 33B 339 340 341 342 343 344 DRV}NING CONTROL SYSTEM DRUM}IING CONTROL SYSTEH DRfRf}IING CO}<<TROL SYSTEM DRU}OIING CONTROI SYSTFH DRU}f}GNG CONTROI.SYSTEM DRV}OfING CONTROL SYSTFH DRLYfMIC CONTROL SYSTAf DRIDQ}ING COhTROL SYST}2f DRIBQflttG CONTROL SYSTEM DR}BOflt}C CONTROL SYSTEM DRUHHINC CONTROL SYSTEH DRUMMING CONTROL SYSTEH DRIPHIhG CONTROL SYSTEM DRU}0}ttiC CONTROL SYSTKH DRU}QII}tC CONTROL SYSTEM 110E197 Sh.2 110E197 Sh.2 110E197 Sh.2 IIOLI97>>.2 110E 197 S}1.2 110E197 S}I.2 110E197 Sh.2 110E197 Sh.2 110E197 Sh.2 110E197 Sh.2 I IOEI97 Sh.2 110E197 Sh.2 110E197 S}L.2 110E197 Sh.2 110E197 Sh.2 I-PV-I<<3-PV-I 220 I-PV-2 2-PV-R 220 I-Pv-3 2-Pf-3 2zl I-PV-4}2-FV-4 22 I PRESSURI'ZKF<<'. VER I ISOLATION PRESSURE!ZER. VEh'T ISOLA~ION PRE.SBURI Z E'VE.NT150LAT ION P'R'FSSURIZEI." VER i!SOLAR 109<<zG54c44 Zf"5 C44 2fc 54C4 4 zf-.5m4 4 I-HV'~!>-I-IV-.l 220 HEAD VE.I'<<T ISO}ANION zc 5 con I-IHV-2.<<"I-IV-c;P<<Y I-WV-3 2 HV-3 221 I-HV-4, 2.I-IV-4 22 I-IK&~}VFN I I&r31 WW}OM HK AD VE.NT IGC>LA'PION I-IE.<<E<<D VE.N ISOLA ION 2Q 5-SC4 Zt" 54C-k 4 Zf" 6 4C44 i'i EC}<ate gI<<!f If;EL<<<<'EY0 27<<50 g~t<<rn<I<<'<<P.~g C<<AE<<<</Akll 359>><<~I I r}<><<<<r<</I~ll i>>>><><<J<<<<t l X 0 T-0<<7<<<<<<1<<<<<<I<<<<fl U o~~Qg ny<<o r<<O>n A 0 O Z I Z 0 r m n tV~>>>>pl-~.Qz 0 e~~~)a) 4J I O lOA~p Rll OPEN RI2 R21 D PEII R22 VAt.V E I-PV-3 2-PV-3 I-PV.4 2-PV-+I-HV-3 2-HV.3 I-HV-$2-HV" r IOA, Ncr.0 ENCRGI=E.2o TO OPEN he 20 20 n rr.O ra.20[hc NOTES I.5 UALVE NO.2.I/O SEE SS.9EV.~AM.P.~Sate.T l~3.CASL=TRAIN"'rp'AGN=TIC REE.D SWI TCHES Yi"s'i~pnouse Ele"Ir'c Corp"raliol Mv~,,, INDIANA AND MICHIGAN ELECTRIC CO.~LQC C UNIT NO 182.ELEMENTARY Vr 1RIII 1 6 rip/g J.6a-~/A>/~SOLE.NOID VAL'VE 5QLBQ.7 SHEET-22 I 0 CP 5~ 4.The maximum allowable venting period is then determined from curve 81 (RCS Pressure vs.Hydrogen Flow Rate).This curve was generated from a calculation which determined the flow rate of hydrogen at various RCS pressures through a 3/8" orificed line.The calculation assumed pure hydrogen which is conservative since the gaseous void in the vessel head will probably be some mixture of gases including steam.February, 1981 Revision 0 Page 12 ~~r y~~~ooae~0~Oat~~4~0~0~O~~0 ATTACHi~)ENT 5 TO AEP:HRC:05i'8}}