ML17264B108
| ML17264B108 | |
| Person / Time | |
|---|---|
| Site: | Ginna  |
| Issue date: | 11/14/1997 |
| From: | ROCHESTER GAS & ELECTRIC CORP. |
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| References | |
| NUDOCS 9711240147 | |
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GINNASTATIONCOLRCycle27Revision0COREOPERATINGLIIVIITSREPORT(COLR)Responsiblemanagei(/iw/evEffectiveDateControlledCopyHo.9'7ii240i4797iii7PDRADOCK05000244DR R.E.GinnaNuclearPowerPlantCoreOperatingLimitsReportCycle27Revision0ThisreportisnotpartoftheTechnicalSpecifications.ThisreportisreferencedintheTechnicalSpecifications.
TABLEOFCONTENTS1,0COREOPERATINGLIMITSREPORT2.0OPERATINGLIMITS........~~2.1SHUTDOWNMARGIN.....~~2.2MODERATORTEMPERATURECOEFFICIENT.2.3ShutdownBankInsertionLimit.2.4ControlBankInsertionLimits.2.5HeatFluxHotChannelFactor(FQ(Z))~~2.6NuclearEnthalpyRiseHotChannelFactor(F"~)2.7AXIALFLUXDIFFERENCE.2.8RCSPressure,Temperature,andFlowDeparturefromBoiling(DNB)Limits2.9BoronConcentration.~~~~Nucleate333344553.0UFSARCHAPTER15ANALYSISSETPOINTSANDINPUTPARAMETERS
4.0REFERENCES
6FIGURE1-RE(UIREDSHUTDOWNMARGIN.FIGURE2-CONTROLBANKINSERTIONLIMITS................8FIGURE3K(Z)NORMALIZEDFo(Z)ASAFUNCTIONOFCOREHEIGHTo~~~~9FIGURE4-AXIALFLUXDIFFERENCEACCEPTABLEOPERATIONLIMITSANDTARGETBANDLIMITSASAFUNCTIONOFRATEDTHERMALPOWER.10TABLE1-UFSARCHAPTER15ANALYSISSETPOINTSANDINPUTPARAMETERS.....11ICOLRCycle27,Revision0 R.E.GinnaNuclearPowerPlantCoreOperatingLimitsReportCycle27Revision01.OCOREOPERATINGLIMITSREPORTThisCoreOperatingLimitsReport(COLR)forGinnaStationhasbeenpreparedinaccordancewiththerequirementsofTechnicalSpecification5.6.5.TheTechnicalSpecificationsaffectedbythisreportarelistedbelow:3.1.13.1.33.1.53.1.63.2.13.2.23.2.33.4.13.9.1"SHUTDOWNMARGIN(SDM)""MODERATORTEMPERATURECOEFFICIENT(MTC)""ShutdownBankInsertionLimit""ControlBankInsertionLimits""HeatFluxHotChannelFactor(Fo(Z))""NuclearEnthalpyRiseHotChannelFactor(F"<<)""AXIALFLUXDIFFERENCE(AFD)""RCSPressure,Temperature,andFlowDeparturefromNucleateBoiling(DNB)Limits""BoronConcentration"COLRCycle27,Revision0 2.0OPERATINGLIMITSThecycle-specificparameterlimitsforthespecificationslistedinSection1.0arepresentedinthefollowingsubsections.TheselimitshavebeendevelopedusingtheNRCapprovedmethodologiesspecifiedinTechnicalSpecification5.6.5.AllitemsthatappearincapitalizedtypearedefinedinTechnicalSpecification1.1,"Definitions."2.1SHUTDOWNMARGIN(LCO3.1.1)(LimitsgeneratedusingReference1)2.1.12.1.22.1.3TheSHUTDOWNMARGINinMODE2withK.<<<1.0andMODES3and4shallbegreaterthanorequaltothelimitsspecifiedinFigure1forthenumberofreactorcoolantpumpsinoperation.TheSHUTDOWNMARGINinMODE4whenbothreactorcoolantpumpsarenotOPERABLEandinoperationandinMODE5shallbegreaterthanorequaltotheoneloopoperationcurveofFigure1.TheSHUTDOWNMARGINrequiredinLCOs3.1.4,3.1.5,3.1.6,3.1.8,and3.4.5shallbegreaterthanthelimitsspecifiedinFigure1forthenumberofreactorcoolantpumpsinoperation.2.2MODERATORTEMPERATURECOEFFICIENT(LCO3.1.3)(LimitsgeneratedusingReference1)2.2.1TheModeratorTemperatureCoefficient(MTC)limitsare:TheBOLARO/HZP-MTCshallbelesspositivethan+5.0pcm/'Fforpowerlevelsbelow70%RTPandlessthanorequalto0pcm/'Fforpowerlevelsator'bove70%RTP.TheEOLARO/RTP-MTCshallbelessnegativethan-42.9pcm/'F.where:AROstandsforAllRodsOutBOLstandsforBeginningofCycleLifeEOLstandsforEndofCycleLifeHZPstandsforHotZeroTHERMALPOWERRTPstandsforRATEDTHERMALPOWER2.3ShutdownBankInsertionLimit(LCO3.1.5)(LimitsgeneratedusingReference1)2.3.1Theshutdownbankshallbefullywithdrawnwhichisdefinedasz221steps.ICOLRCycle27,Revision0 2.4ControlBankInsertionLimits(LCO3.1.6)(LimitsgeneratedusingReference1)2.4.1ThecontrolbanksshallbelimitedinphysicalinsertionasshowninFigure2.2.4.2Thecontrolbanksshallbemovedsequentiallywitha100(+5)stepoverlapbetweensuccessivebanks.2.5HeatFluxHotChannelFactorFZ(LCO3.2.1)(LimitsgeneratedusingReferences1and2)2.5.1Fo(Z)s~FJ"K(Z)whenP)0.5PFo(Z)s~F*K(Z)0.5whenPs0.5where:Zistheheightinthecore,Fo2.45,K(Z)isprovidedinFigure3,andTHERMALPOWERPRATEDTHERMALPOWER2.6NuclearEnthalRiseHotChannelFactorF"(LimitsgeneratedusingReference1)(LCO3.2.2)2.6.1F"F"~*(1+PF*(1-P))where:FATPPF~0.3,andTHERMALPOWERPRATEDTHERMALPOWER2,7AXIALFLUXDIFFERENCE(LCO3.2.3)(LimitsgeneratedusingReferences1and3)2.7.12.7.2TheAXIALFLUXDIFFERENCE(AFD)targetbandis+5%..TheactualtargetbandsareprovidedbyProcedureRE-11.1.TheAFDacceptableoperationlimitsareprovidedinFigure4.COLRCycle27,Revision0 2.8RCSPressureTemeratureandFlow
DearturefromNucleateBoilinLi~i(ICII34i)(LimitsgeneratedusingReference4)2.8.12.8.22.8.3Thepressurizerpressureshallbez2205psig.TheRCSaveragetemperatureshallbez577.5F.TheRCStotalflowrateshallbea170,
200gpm(includes4%minimumflowuncertaintyperRevisedThermalDesignHethodology).2.9BoronConcentration(LCO3.9.1)(LimitsgeneratedusingReferences1and5)2.9.1TheboronconcentrationsofthehydraulicallycoupledReactorCoolantSystem,therefuelingcanal,andtherefuelingcavityshallbez2300ppm.3.0UFSARCHAPTER15ANALYSISSETPOINTSANDINPUTPARAMETERSThesetpointsandinputparametersfortheUFSARChapter15accidentanalysesarepresentedinTable1.Thevaluespresentedinthistableareorganizedbasedonsystemandmajorcomponentswithineachsystem.ThefailureofacomponentorsystemtomeetthespecifiedTable1valuedoesnotnecessarilymeanthattheplantisoutsidetheaccidentanalysessince:(1)anindicatedvalueaboveorbelowtheTable1valuesmaybeboundedbytheTable1values,and(2)thesetpointorparametermaynotsignificantlycontributetotheaccidentanalysesfinalresults.ThemajorsectionswithinTable1are:1.0ReactorCoolantSystem(RCS)2.0HainFeedwater(HFW)3.0AuxiliaryFeedwater(AFW)4.0HainSteam(HS)System5.0TurbineGenerator(TG)6.0ChemicalandVolumeControlSystem(CVCS)7.0EmergencyCoreCoolingSystem(ECCS)8.0Containment9.0ControlSystems10.0SafetySystemSetpoints11.0SteamGeneratorsCOLRCycle27,Revision0
4.0REFERENCES
2.3.4.5.WCAP-9272-P-A,WestinghouseReloadSafetyEvaluationHethodology,July1985.WCAP-10054-P-AandWCAP-10081-NP-A,"WestinghouseSmallBreakECCSEvaluationModelUsingtheNOTRUMPCode,"August1985.WCAP-10924-P-A,Volume1,Rev.1,andAddenda1,2,3,"WestinghouseLarge-BreakLOCABest-EstimateMethodology,Volume1:ModelDescriptionandValidation,"December1988.WCAP-10924-P-A,Volume2,Rev.2,andAddenda,"WestinghouseLarge-BreakLOCABest-EstimateMethodology,Volume2:ApplicationtoTwo-LoopPWRsEquippedwithUpperPlenumInjection,"December1988.WCAP-10924-P-A,Rev.2andWCAP-12071,"WestinghouseLarge-BreakLOCABestEstimateMethodology,Volume2:ApplicationtoTwo-LoopPWRsEquippedWithUpperPlenumInjection,Addendum1:ResponsestoNRCguestions,"December1988.WCAP-10924-P,Volume1,Rev.1,Addendum4,"WestinghouseLBLOCABestEstimateMethodology;ModelDescriptionandValidation;ModelRevisions,"August1990.[ApprovedbyNRCSERdated2/8/91]WCAP-8385,"PowerDistributionControlandLoadFollowingProcedures-TopicalReport,"September1974.WCAP-11397-P-A,"RevisedThermalDesignProcedure",April1989.WCAP-11596-P-A,"gualificationofthePHOENIX-P/ANCNuclearDesignSystemforPressurizedWaterReactorCores,"June1988.COLRCycle27,Revision0 30l1l20'm1xV)(1500.1.45)(1500,1.00)ACCEPTABLEOPERATIONONELOOPOPERA'nON~OLOOPOPERAllONUNACCEPTABLEOPERATION(0.2.45)(0,1.80)15001000500COOLANTgpRONCONCENTRATION(ppm)FIGUREIREQUIREDSHUTDOWNMARGINCOLRCyc1e27,Revision0 2203200~~380$<6Oo.$40~120.a100N80CL~~60ca40o2000(0,164(0,53)10BBank1834~'666,'100,184)CBankankDB(30,20304060,60708090t00CorePower(Percentof1520Mg/T)*Thefullywithdrawnpositionisdefinedasa221steps.FIGURE2CONTROLBANKINSERTIONLIMITS~COLRCycle27,Revision0 0.2N~1.0u0.8U)C'65e0606$~~KK04CPN~~l5F020Tota(Fz=2.460~E't~K0.01.011.7831.00.00,02.04.06.08.0Elevation(ff)10.011.783FIGURE3K(Z)-NORMALIZEDFo(Z)ASAFUNCTIONOFCOREHEIGHTCOLRCyc1e27,Revision0
(-11,90)DONOTOPERATEINTHISAREAWITHAFDoUTSIOETHETARCETS~(11/0)80~OCI40I-Cll~ACCEPTABLEOPERATIONYAHAFD""""""""OUTSaETHETAROETBANDWITH<<1faPENALTYDEMATIONTNE(Q1,60)P1,60)ACCEPTABLE~~~~~y0~OPERATION200-20-100102030AXIALFLUXDIFFERENCE(%)FIGURE4AXIALFLUXDIFFERENCEACCEPTABLEOPERATIONLIMITSANDTARGETBANDLIMITSASAFUNCTIONOFRATEDTHERMALPOWERCOLR10Cyc'te27,Revision0 Table1:UPSARChapter5AnalysisSetpointsandutparametersItem4Item/NameValueRemarks:1.0RcoctorCoolantSystem(RCS)Upperheadvolwre,ft'pperPlenumvolune,ftoTopoffuelvolune,ftoInletnozzle(s)volune,totaloftwo,ftoutletnozzle(s)volune,totaloftwo,ftActivefuelvolrire,ft3Bottomoffuelvolurre,ftoLowerPLenrgrvolune,ftcDowncomervolunc,abovebottomofcoldleg,ftDowncomer,lowercoreplatetoelevationofthebottomofthecoldLegvolune,ftsBarrelbaffle,lowercoreplatetouppercoreplatevolrmre,ftTotalvolunc,ftoHotlegpipevolteperLoopvairft>ColdlegvoluaeperLoop+crossover,ftiRCpmpvoluncperpump,ft'oldlegpipeID,In./PurrpsuctionID,in.HotlegpipeID,in.Designpressure,psigDesigntemperature,FColdLegandHoti.egCenterlineElevation300.0580.250.343.237.4367.611.0514.3138.4278.2128.52449.178.7crossover=140.7coldLeg=46.819227.5/3129(28.969)2485650246'0uAboveuppersupportplate.Bottomofuppercoreplatetotopofuppersupportplate.Includesoutletholesinthebarrel.Topofactivefueltobottomofupper'oreplate,insidebarreLbaffle.Includesnozzleforgingprotrusionintovessel.Doesnotincludematingholeinbarrel,thisisincludedintheUpperPLenunvolune.BottomoffueltotopoffuelTopofLowercoreplatetobottomofactivefuel.BelowtopoflowercoreplateAbovebottomofcoldlegelevationtobottomofuppersupportplateTopofLowercoreplatetoelevationofbottomofcoldLegTopofLowercoreplatetobottomofupperccrcplate.IncludesnozzlesReactorCoolantPrsrrpHead-CapacityandNPSHcurvesforreactorcoolanzpumps/HomologousCurvesRatedRCpumpheadandflow,ft&gpmRatedRCpumptorqueandefficiency9ratedhead/flow,ft-lb,fractionRCPPrmpRatedPower(hot,556degreesF)RCPHotorRatedSpeed,RPMMomentofinertiaofpumpandmotor,lb-ftzRCpumpheat,MMt(max/minperpump)SeeHS&L252;90,00084Kefficiencyathotconditions4842BHP118980,0005,4HomologousCurvesareavailableinRETRAHPwppowervarieswithRCSterrpframapprox4MWtto5Mwt1.2CoreCOLRCycle27,Revision0 Table1:UPSARChapter5AnalysisSetpointsand~utParametersItem4Item/NameValueRemarks:Ratedpower,HWtReactorpoweruncertainty,gRTPBypass,XUpperheadbypass,gUpperheadtcngerature,degreesFHeattransferarea,fthmAveragecoreheatflux,Btu/hrft>15206.5Mproprietary59026,669189,440Thimbleplugsremoved.HighT~value.1.31.3.1FuelAssembliesHeightTotal,inches(lengthfrombottomofasscnhtytotopnozzle)FuelRodLength,inches(lengthfrombottomofpintotopofpin)Active,inches159.935149.138141.41.3.2FuelAssemblyGeometryHassoffuel,ibmHossofclad,ibmHumberoffuelpinsperfuelassembly(FA)Ho.ofFuelAssembliesFuelpinpitch,in.BottomnozzleweightandvotuncTopnozzle,w/insert,weightandvoluneFuelAsserrhtyresistance(coredPf(flow)],psif(lb/hr)FuelAssemblyfreeflowarea,in105,50025,9271791210.5569.1lbs.31.5in18.15lbs.62.9in'oredeltaP-"20psi9flow~170,200gpn34.75Thimbleplugsremoved.Singleassembly.1.3.3FuelpingeometryPelletdiameter,in.Clad00/IO,in./in.0.34440.400/0.35141.34ControlRod4InstruaentGurdcTubesHo.ofcontrolrodguidetubesHo.ofinstrunentguidetubesControlRodGuidetubeupperpart00/ID,in./in.InstrunentGuidetube00/ID,in./in.Guidetubelowerpart00/ID,in./in.ControlRodDropTimes,maximuns,scc.Controlrodmaximunwithdrawalrate,in./min.160.49/0.528.0.395/0.3500.4445/0.4825Hon-LOCA2.4LOCA3.045AltowanccsareaddedtotheTechSpecallowablevalueCOLR12Cycle27,Revision0 Table1=UFSAR('-rapter5AnalysisSetpointsandutparametersItemgItem/NameValueRemarks:Controlrodmaxim(rsinsertionrate,pcm/sec.ControlrodinsertionlimitsHotchannelradialpeakingfactorHeatFluxHotchannelfactorFq90SeeCOLR1.752.451.4pressurizercodesafetyvalveflowcapacity,Lbm/hrCodesafetyCodesafetySprayvalveSprayvalveSprayvalveSprayvalvePORVnumbervalveopentimevalvesetpointn(rmberflowcapacity,gpm/vaLvesetpoint-startopen/fulLopentimeconstant,sec.pORVflowcapacity,Lbm/hrpORVCvPORVopentimePORVclosetimegackupHeatersMinimusheatercapacityrequiredforLOOP,k'MHeaterbankcontrollertypepORVsetpoint[normal)open/close,psigpORVsetpoint(LTOP]open/close,psigpORVblowdowncharacteristicHeatercapacityw/bankcapacityandsetpoints,kifControlbanks288,0000.8secsealclearingtime2485psig22002260/231052179,00050gpm/(psid)1/21.65sec+transmitter3.95sec+transmitter2335/23154308000kWat2250psigand400kwst2220psigFullonat2210psigsndresetsat2220psig100proportional400kMRatingat2485psigplus3XaccumulationCrosbyModelHB-BP-86,size4K26Toleranceis+2.4X/-3X.proportionalAssedvalueSteamflowst2335psigRatingisforliquidrelief.ValvecharacteristicisquickopeningseeCopesVulcanSelectingandSizingControlValves8/75,page8,Table18forCvvstravelcurve.LTOPstransmitterisFoxboroE11GM-HSAE1,withatimeresponseof1sec(timeto90Koffinalvalueforstepinput)LTOPstransmitterisFoxboroE11GM-HSAE1,withatimeresponseof1sec(timeto90Koffinalvalueforstepinput)1.4.1pressurizervolusc(s)(100M/Ly(power)Lister,ft(100K/OXpower)Steam,ft(100M/OXpower)Total,ftpressurizerLD,ft-in396/199404/60180083624in/claddingthicknessis0.188inCOLR13Cyc'1e27,Revision0
Table1:UFSARChapter5AnalysisSetpointsandutparametersitem0Xtem/NameValueRemarks:SurgelineID,in.SpraylincID,in.Surgelinevoluneft8.753.06218.4Surgelineis10inschedule14014.2PressurizerLevelLowerleveltapelevationUpperleveltapelevationpressurizerlevelvsXpowerDistanceNotLegCenterlinetoLowerTap,ftHaximmlevelallowedforsteambubble,X257'275'%powerLevel0X35X100X50X10.75087pressurizerlevelisrampedlinearlybetweenthesepoints.NotusedinChapter15analyses.1.5RCSPlows,TemperatureandPressuresTotalreactorcoolantflow,gpm(15Xplugging)Totalreactorcoolantflow,gpm(15Kplugging)Averagereactorcoolanttecperature,degreesF(fullpower/N2P)Reactorcoolantpressure,psigReactorcoolantflowuncertainty,XnominalReactorcoolanttemperatureuncertainty,degreesFReactorcoolantpressureuncertainty,psiDNBLimit(safetyanalysislimit)170,200177,300559to573.5/5472235a301.40UscfornonDNBUscforstatisticalDNBCycle26T~=5611.6LowTcaperatureOverprcssurcProtection(LTDP)HinimuaRCSventsize,squareinchesNo.ofSipcscapableofinjection(PDRVs/vent)HaxiaampressurizerlevelforRCPstart,X0/1381.7FuelHandling/DoseCalculationsHaxigullreactorcoolantgrossspecificactivityHaximmreactorcoolantdoseequivalent1.131HaxinxmsecondarycoolantdoseequivalentI-131Hinimmreactorcoolantboronconcentration,ppmHinimiareactorcoolantlevelHiniaxmspentfuelpoollevelHinimuaspentfuelpoolboronconcentration,ppaHjnieunspentfuelpoolcharcoalfilterefficiency,XmethyliodineremovalHinfnxsapostaccidentcharcoalfilterefficiency,Xmethyliodineremoval100/bpCi/gm1.0pCi/gm0.1pCi/gm200023ftaboveflange23ftabovefuel3007070TStestingrequires90Kcff.TStestingrequires90Keff.COLR14Cycle27,Rev>sion0 ItemgItem/NameValueRemarks:Minimuscontrolroomcharcoalfilterefficiency,XmethyliodineremovalMinimustimebetweenreactorcriticalityandfuelmovement,hrs.SourceTermsusedfordosecalculationsDoseconversionfactorsMaximunGasDecayTankXenon-133concentration,Ci70100ORGEH2ICRP-30100,000TStestingrequires90Xeff.2.0MainFeedwater(MFII)FeedwatertemperatureversusloadPowerTecyerature102X425F70X385F30X322FDX100F100Xdesigntempis432degreesFFeedwaterSuctionTemperaturevspower,nominalFeedwaterSuctionPressurevspower,nominalPower98X70X50X30XPower98X70X50X30XTemperature345F319F295F259FPressure277psig282psig305psig370psig2.13.0Head-CapacityandHPSHcurvesHead-CapacityandHPSHcurvesformainfeedwaterpcsMainFeedwaterpump"RatedHeadMainFeedwaterpurp-RatedTorqueMainFeedwaterpump-MomentofinertiaElevationofstcamgeneratorinletnozzleElevationofmainfeedwaterpump,ftElevationofcondensatepump,ftMFIIregulatingvalveopentimeondemand,secMFIIregulatingvaLveclosetimeondemand,secMFIIregulatingvalveCv,fullstrokeLowLoadMFIIregulatingvalveCv,(bypassvalves)MFllHeaterresistance(deltap)AuxiliaryFeedwater(AFM)Minimusdesigntemperatureofthe~atersourceservicewater/CST(degreesF)MaxŽ~~designtemperatureofthewatersourceservicewater/CST(degreesF)SecHS&L2150'89.612257.75250.8331048.7seeHS&L032(*),5080,100Selectedflowsplitsareprovidedformodelvalidation.ElevationisatcenterofshaftAssunedvalue.Actualvalue-"684.EffectiveCv:includesbypasslineDesigndataontheHighPressureHeaters(2inparallel)isprovidedInitialAFlJwatersourcearetheCSTslocatedintheServiceBldg.SafetyRelatedsourceistheService'Matersystem(lake)."ValuedifferentforCHMTintegrity.initialAFIJwatersourcearctheCSTslocatedintheServiceBldg.SafetyRelatedsourceistheServicellatersystem(Lake).COLR15Cycle27,Revision0 0Table1:UFSARChapter5Analysj.sSetpoi]ItsaTIcL,utParametersItemgItem/NameValueRemarks:StartuptimefortheauxiliaryfeedwaterImps,secHinimmdelayforAFMstart,secHaximuadelayforAFMstart,secAFMcontrolvalveopentimeondemand,secAFMcontroLvalveCv[ftowisf(dP)]TDAFMP,maximmflow,gpmAFM,minimusflows,bothgeneratorsintact,gpmHinfmuadelayforstandbyAFMstart,minTDAF'M-OIHDAFM-1HDAFM-47,TOAFMatLOLevelbothSGsH/A600TOAFMP200/SGHDAFMP200/SG10*TOAFMstartsonLOlevet(17K)inbothgensorUVonbothunit4'usses.HDAFMstartsonSI(seq),orI.OLeveleitherSG,ortripofbothHFPorAHSACHDAFMaccelerationtimetestresultsshowapproximately1.5s.ForHDAFM,LOOPonsequenceris47sec.TDAFMstartsatnominal17'nbothSGsHDAFMcontrolvalvesarenormatlyopenandthrottleclosedtocontrol,flowbetween200-230gpmNDAFMPvalvesare3Rockwellmodel¹A4006JKHYstopcheckvalves.TDAFMcontroLvalves(4297,4298)are3Fisher¹470-HS.SBLOCAassunes200gpaperSGwiththefaitureofoneDG4.0HainStemSystem(HS)Location(andelevation)ofcondenserdumpvalvesandatmosphericreliefvalvesFulLloadsteamlinepressuredrop,psiHSIsolationvalveclosetime[fullopentofullclose]closetimeisecHSIsolationvalveCv[flowisf(dp)]CSD.elev256'.875ARV-elev289'.563approx45NSIV-5.0checkvatve-1.0HSIV-23500checkvalve-17580Thisestimate,tothegovernorvalves,isprovidedforcomparisonpurposesonly.Thecheckvalveisassunedtoclosein1secunderreverseflow.4.1HainStemCodeSafetyValvesNumberofvalves(4perline)Valveflowcapacities-Total,Lbm/hr6621000Ratedflow(3XaccunutationperASHE,SectionIII):1085psfgo~~~~~~~~~~~~~~~797g700Lbm/hr(each)1140psig....~.....~~.....837,600ibm/hr(each)COLR16Cyc1e27,Revision0 ItemfItem/NameValueRemarks:ValveFlowvsSGpressure(psia),totalperbank(4valves),ibm/sec.1110111511201125113111361141115111611166117311811190120012051209121104091141191222223225227228342494646799859920931NumberofvalvesinbankValvesctpoint(s),(first/lastthree),nominal,psigVaLveblowdowncharacteristic41085/114015XmaximmValvesareCrosbyAHA-656R10SetpointtoleranceIs+1X/-3X.Nodelvalvesetpointat1.01(nominal),andfuLLflowat1.04(nominaL).4.2AtmosphericreliefvalvesNo.AtmosphericreliefvalvesAtmosphericreliefvalvesetpoint/Air-operated,psigAtmosphericreliefvalvesetpoint/Booster,psigAtmosphericreliefvalvecapacity,Lbm/hr21050DuringHotStandbyoperationsetpointIsloweredtocontrolnoloadTavg1060313550at1060psigNaxflowis3800005.05.1TurbineGenerator(TG)CondenserNo.ofcondenserdisapvalvescondenserdmsvalveopentime,secCondenserdmsvalveclosetime,secCondenserdumpvalvesetpoint(s)CondenserdumpvaLveCv[flowisf(dP)]ForTT:Tavg>5554valves,>5634valves;noTT:Tref+124valves,Tref+204valvesAssusingclosetime~openingtimeGnTTvalvescontrolopenat6.7X/F(PID)above547withfullopensctpointsasdescribed.On10XstepLoaddecreasesameratiowitha6FdeadbandfromTrefOesignCv(240)fromdesignconditions(302,500Lbm/hrsatsteamat695psig)6.0ChemicalandVoltmcControlSystem(CVCS)CVCScspscIty/pump3pmys,60gpmmsxeachNormalops:2chargingpumps-oncismanualat15-20gpmsndtheotherinautcmatic.ChargingpumpssrePDPsw/46gpmtotal-8gpmtoseals-3gpmleakage+5gpmintoRCS.40gpmLetdownCOLR17Cycle27,Revision0 Table1:UFSAR(-haPter5AnalysisSetpointsandutparametersItem4Item/NameValueRemarks:CVCSmfnfmua/pm',gpmTypeofcontroLLer(e.g.,p+1)andgains15PLD100K,180sec,10secReactorHakeupMateiSystem(QHl)RHllcapacfty/pulp2puris,60gpaeach7.07.17.1.1EmergencyCoreCoolingSystem(ECCS)ECCSDelivery'sRCSPressureResidualHeatRemoval(RHR)DeliveryHfnfmusRHRDelfvery,trainfailurevsRCSPressureHfnfaxjaRHRDelivery,twofxmysrunnfng,onelineblockedRCSPressure(psia)1551521501401201008060402014.7RCSPressure(psfa)1551541521501401201008060402014.7Delivery(gpm)0002506488369851115123213381365Delivery(gpm)00160252516830105612431406155216861720LOCAAppendixKcase.Trainfailureresultsfnonepunprunningwith10KdegradationwithonelinebLocked.LOCAAppendixKcase(offsftepoweravailablc).Twopumpsrunningwith10Kdegradationwithonelineblocked.71.2Safetyinjection(Sf)DeliveryvsRCSPrcssureHfnfmuaSidelivery,2pumpsoperating,oncLinespillingPress(psig)137513001200110010009008007006005004003002001000Delivery(gpm)0.062125167201229253273289305321336352368394SpillLOCAAppendixKcase.Trainfailure(gpm)resultsintwopunpsrunningwfth5X465degradationwithoneLinespillfngto465contafcment.465465465465465465465465465465465465465COLR18Cycle27,Revision0 Table1:UFSARChapter5AnalysisSetpointsandparametersItem4Item/NameValueRemarks:MinimunSidelivery,3punpsoperating,non-LOCAPress(psia)Oelivcry(gpm)Loop'A'oopUsedfornon-LOCAtransients,5XpumpdegradationMininnnnSidelivery,2pumpsoperatingnon-LOCAMaximunSidelivery,3punpsoperating,SGTR1390131512151115101591581571561551541531521511515Press(psia)1390131512151115101591581571561551541531521511515Press(psig)137513001200110010009008007006005004003002001000Igl1687147193231266297325352377400423445465485DeliveryLoop'A'gl869121162197228255281305328350370390409427LoopA(gpn)76128180221258'2903203483743984214434644855041997163214257295329360390418444469493516538(gpn)Loop871126169206239269296322346369391412432452Loop8(gpm)84141198245285321354385413440466490514536558Usedfornon-LOCAtransients,5Xpumpdegradation.TheKYPTPEmodelassunesnopumpdegradation.LoopAand8pressuresaresetequal.UsedforSGTR.7.3Ac~latorsMunsterofaccunulatorsTotalvolune,each,ft'iquidvolunclftmin/maxLiquidvoluneift-BestEstimateinitialprcssure,psig-Minimun/Maxlmun217501126/11541140700/790COLR19Cycle27,Revision0 Table1:UFSARChapter5AnalysisSetpointsandutparametersItem4Item/NameValueRemarks:initialtemperature,FBoronconcentration,ppm(mfn/max)1052100/2600LBLOCAHote-EaanalysesuseamaximusconcentratIonof3000ppm74RMSTRUSTTeIIperature,min/max,degreesFfffnfmuaRWSTvotIme,galRMSTboronconcentration,ppm(min/max)60/80300,0002300/2600Hote-EQanalysesuseamaxiImmconcentrationof3000ppm8.0Contafrmentinitialcontaf~ntpressurepiainitialcontainmenttemperature(LOCA/SLB)degreesFinitialrelativehuaidity,XSMteIIperaturemin/max,degreesFHaxfImmcontafmentleakage,wtX/daymin-14'max-16.790/1202030~/800.2~HfnfmuIIisusedforLOCAanalysis.Haxfmmisusedforthecontafwentintegritycases(SI.B).LOCAtemperaturelowerforPCTcalculations.SLBhfgherforcontairmentintegrity*Vatuedifferentforauxiliaryfeedwater8.1ContafImcntHeatSinksListingofPassiveHeatSinks,quantities,metal'fels~andconfigurationsseeHSSL8.2Concretedensity,conductivity,capacityBensities,ThermalConductfvitiesandHeatCapacitiesofHeatSinksInsulatfondensity,conductivity,capacity3.7ibm/fta0.0208BTU/hrFft1.11BTU/ftF150ibm/ft0.81BTU/hrFft31.5BTU/fthmFnote:mfnfImmconductivitycorrespondstomaximusdensity,andmaxfImmconductivitycorrespondstomfnfmundensity.Steeldensity,conductivfty,capacityStainlesssteeldensity,conductfvity,capacftyContafrmentfreevotune,mfn/max,cu.ft.GroundTNIperature(degreesF)OutsideAirTemperature,min/max,degreesFHTCforoutsidesurfaces490tbm/ft28BTU/hrFft54.4BTU/ftF496tbm/ft15BTU/hrFft54.6BTU/ftaF1,000,000/1,066,00055-10/1001.65BTU/hrftdegreesFbelowgradetemperatureCOLR20Cycle27,Revision0
'Table1:UPSAR(-hapter5AnalysisSetpointsandiputParametersItem4Item/NameValueRemarks:ContairrnentfancoolerperformanceContairltentsprayflow,min/max,each,gpmTenpHinHax(degF)(X106BTU/hr)1202.054F5522035.199.224040.8113.826046.8129.328052.9145.528654.7150.41300/18008.3OclaysforCRFCsandSpraypunpsCRFCdelay,offsitepoweravailable,secondsCRFCdelay,offsitepowernotavaflable,secondsContafnmentSpray,1300gpmeachfxlp,maxfmundelay,secContafreentSpray,1800gpmeachpunp,mfnfmundele/,secContafrInentOesfgnpressure,psigOfstanceBasementfloortoSpringline,feetOistanceSprfnglinetotopofdone,feet344428.5-oncpunp26.8-twopumps9/(14wLoOP)609552.5includes2.0secSIdelayincludes2.0secSIdelayThisdelayisfromthetfmeContainmentHi-Misetpointisreached.Itincludesinstrunentdelayandspraylinefilltime.Thisdelayisfromthetfmeofbreak.8.4ContairwentSurpHinimunwtXofHaOHTank309.0ControlSystems(Reactor,FM,przrLevel,Turbine,AFIJ)TavgversuspowerpressurizerpressureandlevelalgorithmsSOsecondarylevelalgorithmH/AN/AH/ATavgrampsLinearlyfrom547degreesFatOXpowerto561degreesFat100Kpowerpressurizerpressuresetpointisconstantat2235psig.PressurizerleveLreapsfrom35Kto50Kfor0to100Kpower(547-561degreesF).Levelremainsconstantat52Xto100Xpower.(Powerfromturbine1ststagepress.)10.010.'I10~1.1SafctySystemSetpointsReactorProtectionSystempowerrangehighneutronflux,highsettingnominalaccidentanalysisdelaytime,sec1.180.51.0910.1.2Powerrangehighneutronflux,Lowsettingnominalaccidentanalysis0.2500.350COLR21Cyc1e27,Revision0 Xtem4Item/NameValueRemarks:delaytime,sec0'10.1.3OvertemperaturedeltaTnominalaccidentanalysisdelaytime,secVariableVariable6.0Totaldelaytime-fromthetimethetenperaturedifferenceinthecoolantLoopsexceedsthetrip.setpointuntiltherodsarefreetofall10.1AOverpowerdeltaTnominalaccidentanalysisdelaytime,secVariableVariable2.0Hotexplicitlymodelledinsafetyanalysis10.1.5Highpressurizerpressurenominal,psigaccidentanalysis,psiadelaytime,sec24102.010.1.6Lowpressurizerpressurenominal,psigaccidentanalysis,psiadelaytime,sec18731775(non-LOCA)1715(LOCA)1905(SGTR)2.010.1.7Lowreactorcoolantflownominalaccidentanalysisdelaytime,sec91Kofnormalindicatedflow87XperLoop1.010.1.8Low-LowSGlevelnominalaccidentanalysisdelaytime,sec17KofthenarrowrangeLevelspanOXofnarrowrangeLevelspan2.0WhiletripsetpointcouldbeasLowas16K,AFllinitiationLimitsto17K10.1.9TurbineTrip(lowfluidoilpressure)nominal,psigaccidentanalysisdelaytime,sec45H/A2.0HotexplicitlymodeledinsafetyanalysisCOLR22Cycle27,Revision,0
~.~Table1-UPSARChapter15AnalysisSetpointsandInputparametersItemgItem/NameValueRemarks:10.1.10Undervoltagencminal,Vaccidentanalysisdelaytime.sec31501~5SafetyanalysisassunesRCCAsarereleased1.5scc.aftersctpointisreleased.10.1.11Undcrfrcqumcynominal,Hzaccidentanalysisdelaytime57.757.01.2Analysisisperformedbutnotexplicitlymodeledinsafetyanalysis.SafetyanalysisassunesRCCAsarereleased1'secaftersetpointisreached.10.1.12Intermediaterangenominal,RTPsafetyanalysis,RTPdelaytime,sec0.25H/AH/AHayfluctuateductocorefluxHotexplicitlymodeledinsafety'nalysis10.1.13SourceRangenominal,cpsaccidentanalysis,cpsdelaytime,sec1.4E+51ALOE+52.0Highestnominalvalue10.1.14HighPressurizerlevelnominalaccidentanalysisdelaytime,sec0.900.9382.010.210.2.110.2.1.1EnglneercdSafetyFeaturesActuationSystemSafctyinjectionSystem'Highcon'tailNcAtprcssureHominalsetpoint,psigAccidentAnalysissetpoint,psigoelaytime,sec4.06.0*3444w/LOOP*onlymodeledinaccidentanalysisforstartofcontainmentfancoolers.Timedelaysareforstartofcontainmentfancoolers.10.2.1.2LoupressurizerpressureHominalsetpoint,psig1750COLR23Cycle27,Revision0
~..~Table1:UFSARChapter15AnalysisSetpointsandinputparametersXtem4Xtem/NameValueRemarks:AccidentAnalysissetpoint,psiaDelaytime,sec1785,SGTR1730,non-LOCA1715,LOCA2.0102.13Lowate~linepressuleHominalsetpolnt,psigAccidentAnalysissetpoint,psigDelaytime,sec514372.72.0SeeHS&LSeeNS&L10.2.2ContairwmtSprayHominalSetpoint,psigAccidentanalysissetpoint,psigDelaytime,sec2832.528.5SecHS&LDelaytimeincludestimetofilllines.SeeHS&L10.2.3AFMSystemLcwlowate~generatorwaterNominalSetpointAccidentanalysissetpointDelaytime,sec17Xofnarrowrangeinstrunentspaneachsteamgenerator0Xofnarrowrangeinstrunentspaneachsteamgenerator2.0Apositive11KerrorhasbeenincludedtoaccountfortheSGlevelmeasurementsystematacontairraenttecperatureof286F10.2410.2.4.1SteamLineIsolationHighconteirsaentpressureNominalSetpoint,psigAccidentanalysissetpointDelaytime18H/AH/ANotexplicitlymodeledNotexplicitlymodeled10.24.2Highstemflow,coincidentwithlowTavgandSIHominalSctpointAccidentanalysissetpointDelaytime0.4E6lb/hrequivalentsteamflowat755psigandTavg<545FN/AN/ANoteflowsetpointisbelownominalfullpowerflowandthereforethisportionoflogicismadeupatpowerNotexplicitlymodeledHotexplicitlymodeled.SteamlineisolationisassumedconcurrentwithSI(i.e.2sdelay+'5svalvestroke)10.2.4.3High-highstemflow,coincidentSIHominalSetpointAccidentanalysissetpoint3.6E6lb/hrequivalentsteamflowat755psigN/AHotexplic>tlymodeledCOLR24Cycle27,Revision0 ItemfItem/NameValueRemarks:DelaytimeH/AHotexplicitlymodeled.SteamLineisolationisassumedconcurrentwithsi(i.e.2sdelay+5svalvestroke)10.2.5Feedwaterisolation10.2.5.1Highstemgeneratorwaterlevel110HominalSetpointAccidentanalysissetpointDelaytimeBillStemGeneratorsHeatloadperSG,BTU/hrPrimaryflowperSG,Klb/hrSteamflowperSG,Lb/hr(clean,unplugged)Secondarydesignpressure,psigSecondarydesignteaperature,FMaxicxlamoisturecarryover,XHarrowrangeleveltaplocations,inchesaboveTSsecondaryfaceMiderangeleveltapLocat'ions,inchesaboveTSsecondaryface85XofthenarrowrangeinstrunentspaneachSG100XofthenarrowrangeinstrunentspaneachSG2.02,602,000,000PluggingXFlowKlb/hr034950534630103428015338503,264,358at877psia10855560.10386/s/529/I8/~/529/eLnstrunentlooponlyDesignflowsatT,,~573.5FconditionsforT~~573.5FSGPressureDropsSecondarynozzletonozzledPQfullpower,psiSecondarynozzletonozzledPQfullpo~er,psiprimarynozzletonozzleunrecoverablepressureciropvs.plugging,psi14.77.5PluggingXappsi031.01533.271035.821538.72ValueistotaLstaticpressuredrop.PressuredropfromtopofU-bendtooutlet.SeeassociatedflowsforXplugging.11.2SGTubesHo.oftubesperSGTube00,inchesTubeaveragewallthicknessinchesMaxinxlatubelength,ftMinimustubelength,ftAveragelength,ft47650.7500.04370.20055.92561.988Includeslengthintubesheet(2x25.625")includeslengthintubesheet(2x25.625")includeslengthintubesheet(2x25.625")COLR25Cycle27,Revision0 ITable1:UFSAR(-'hap<<r5AnalysisSetpointsandutparametersItem4Item/NameValueRemarks:HlnfaaeU-bendradius,inchesHaxiaamU-bendradius,inchesU-bendradiusofshortesttube(s),inchesAverageU-bendradius,inchesTubestraightLength(oneside)abovesecondaryface,inches(min/max/average)Secondaryheattransferarea,ftperSGPrimaryheattransferarea,ft~perSGoverallbundleheight,ftabovesecondaryfaceofTS3.97954.0074.04424.51303/lg/310/i/308.18254,00147,80930.427Note:thisisnotthebendradiusfortheshortesttube.TubematerialSGTubeHaterialThermalConductivity,BTU-in/hr-ft'-FSGTubeHaterialSpecificNeatBTU/lb.FSB-163TempF200300400500600TempF200300400500600AlloyN06690Conductivity93100107114.5122Conductivity0.1120.11550.1190.12250.126Distancefromtopoftubebundleto33'RL,ft5.70311.311.3.1SGVoltmesSGSecondarySideVol~secondaryvolte,ft(total)SecondaryvoluneuptolowerNRLtap,ftSecondaryvoluneuptoupperNRLtap,ft4512.71893.23460.411.3.2RiserVolmesSecondarysidebundlevolune(TStotopofU-bendinsideshroud),fthmsecondaryriservolune,topofU-bendtospill-overpoint,ft'281.8507.0EquivalenttoLOFTRANriservolune.11.3.3DosncomerVolmesDowncomervolune,topofTStotopofU-b&,ft'owncomervolunc,topofUbQftospipoint,ft'59.61437.311.3.4SGPrimarySideValuateInletplenuaperSG,ftsOutletplenunperSG,fthm129.65129.65COLR26Cycle27,Revision0 Table1:UPSARChapter15AnalysisSetpointsandInputParametersXtemfXtem/NameValueRemarks:TubeprimaryvelumperSG,ftaPrimarytotalvoluneperSG,fthmCirculationratio(100Xpower,clean,unplugged)Tubesheetthickness,inches710.3969.65.3925.625Circulationratio=bundleflowgsteamflow.Assunes40,000Lbmghrblowdown.Includescladding.11.4SGPrimrySideDimensionsPHmaryheadradius,inchesDividerplatethickness,inchesInletandoutletnozzle,insidediametelcylindricalsection,inchesNozzledivergenceangle,degreesNozzleinsidediameteratplena,inchesNozzleLengths,inchesHeigthfromSGprimaryheadbottom(outside)totopofTs,inchesDistancetubesheetprimaryfacetohotlegcenterline,ft.58.3751.87531.2001130'7.0cylindricalsectionconicalsectiontotallength90'lle6.6548.7513.021.75Radiustocladsurface.11.5SGSecondarySideDimensionsLowershellinsidediameter,inchesLowershellthickness,inchesTubeshroudinsidediameter,inchesDistancetopoftubebundletotopofsteamnozzle,inchessteamnozzleflowrestricterarea,ft'istancesecondaryfaceofTStocenterlineoffeedwaternozzle,inchesDistancesecondaryfaceofTStocenterlineoffeedring,inchesCross-sectionalareaoftubebundleft~Distancetopoftubebundletospill-overpoint,inchesPrimarysideroughness,micro-inches1222.875114298.51.4407'i,37441.64178.0Hozzles,head60Tubes60Thisvalueistotalareainsideshroud.ThisvalueisequivalenttotheriserheightfortheDSG.valuesgivenareconservativeassunptions.SGSecondarySideMaterHassesSecondary~aterinventory,100)',power,T,,~573.5,noplugging,ibmSecondarywaterinventory,100'ower,T,559,noplugging,Lbn86,259liquid5,286steam85,547liquid4,675steamgestestimatevalue.gestestimatevalue.11.7SGPrimarySideHeadLossCoefficientsCOLR27Cycle27,Revision0 Item4Item/NameValueRemarks:gGinletnozzle/plenumlosscoefficient,ft/gpmgGoutletnozzle/plenumlosscoefficient,ft/gpmgGtubinglosscoefficient,ft/gpmSGCubinglosscoefficient,sCraightsection(in),ft/gpm'Gtubinglosscoefficient,U-bendsection,ft/gpm$0tubingLosscoefficient,straightsection(out),ft/gpm1.01E-09forID<<31.2<<3.31E-10forIO<<31.2<<9.62E-09forOXplugging1.32E-08for15Xplugging4.19E-09forOXplugging5.73E-09for15Kplugging1.02E-09forOXplugging1.40E-09for15Kplugging4.41E.09forOXplugging6.08E-09for15XpluggingForcubeID<<0.664",Ao>><<11.458fC2~A~~>>assumedtobeuniform.FortubeID<<0.664<<,A<<11.458ft,A,~>>"-9.739ft.Pluggingisassunedtobeuniform.Fortube10=0.664",Ao>>=11.458fc',A=9.739ft.Pluggingisassumedtobeuniform.FortubeID=0.664"~Ao"-11.458fthm,Al5>>=9.739ft2.Pluggingisassumedtobeuniform.COLR28Cycle27,Revision0 4