ML17324B003

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Rev 0 to Books 1-3 of Analysis of Pressurizer Safety/Relief Valves Discharge Piping Sys Per NUREG-0737,II.D.1,Unit 1.
ML17324B003
Person / Time
Site: Cook American Electric Power icon.png
Issue date: 06/06/1983
From:
TELEDYNE ENGINEERING SERVICES
To:
Shared Package
ML17324B004 List:
References
RTR-NUREG-0737, RTR-NUREG-737, TASK-2.D.1, TASK-TM TR-5364-1, TR-5364-1-R, TR-5364-1-R00, NUDOCS 8608060052
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8608060052860730PDRADOCK05000315PPDRL\i'~~,1TECHNICALREPORTTR-5364-1REVISION0BOOK1OF15DONALDC.COOKNUCLEARGENERATINGPLANTANALYSISOPPRESSURIZERSAPBTY/RELKFVALVESDISCHARGEPIPINGSYSTEMPERNUREG073V,ILD.I,UNTFIJUNE6,1983 l'i'iF AMERICANELECTRICPOWERSERVICECORPORATION2BROAOWAYNEWYORK,NEWYORK10004TECHNICALREPORTTR-5364-1REVISION0BOOK1OF15DONALDC.COOKNUCI.EARGENERATINGSTATIONANALYSISOFPRESSURIZERSAFETY/RELIEFVALVESDISCHARGEPIPINGSYSTEMPERNUREG0737,II~0.1,UNIT1JUNE6,1983N'TELEDYNEENGINEERINGSERVICES130SECONDAVENUEWALTHAM,MASSACHUSETTS02254617-890-3350 4('I~~'I,1(%hICtt,C\r,~~fII0I1C:'Ij1A~r TechnicalReportTR-5364-1Revision0TABLEOFCONTENTSATELEDYNEENGINEERINQSERVICESPAGE

1.0INTRODUCTION

2.0CONCLUSION

S3.0SYSTEMDESCRIPTION/DISCUSSION4.0THERMALFLUIDSANALYSIS4.1Introduction4.2RELAPModel4.2.1PressurizerConditions4.2.2ValveModeling4.2.3DischargePiping4.2.4quenchTank4.3RELAPModelControlVolumes4.4quarterModel4.5Unit1PORVModel4.5.1CondensateModeledCase4.5.2,PORVModeledTransient4.6ValveFlowRateCalculation4.6.1SVFlowRate4.6.2PORVFlowRate4.7RELAPPlotsBook1of152-13-14-14-1434-34-44-54-54-164-264-'364-364-364-404-414-.424-454.7.1Unit1-Condensate/SteamCase4.7.2Unit1-400oSolidLiquidCase4.7.3quarterModel-ColdLoopSeal/SteamCase4464-1664-2444.8ForceTimeHistoryPlotsBook2of154-2604.8.1Unit1-Condensate/SteamCase4.8.2Unit1-400oSolidLiquidCase4.8.3quarterModel-ColdLoopSeal/SteamCase4.9RELAPInput4-2614-3204-3924-4204.9.14.9.24.9.34.9.44.9.5PORVCondensate/SteamCondensate/SteamRestartPORVSolid400oLiquidPORVSolid400oLiquidRestartSVColdLoopSeal(quarterModel)4-4214-4394-4484-4674-472 ga'\pl4Aft/C~ia<ajh~ra-pEWI'*r"0P~(tis/.Ag,J Technica1ReportTR-5364-1Revision04.10REPIPEInputTABLEOFCONTENTSContinued)iTELEDYNEENQINEERINQSERVICESPAGE4-4784.10.1Unit1-ModelSectionA4.10.2Unit1-ModelSectionB4.10.3Unit2-(quarterModel)4.11APPENDIXA5.0STRUCTURALANALYSIS5.1DeadweightAnalysis5.2ThermalAnalysis5.3SeismicAnalysis5.4Force/TimeHistoryAnalysis5.4.1PORVTransient5.4.2SVTransient6.0ANALYTICALRESULTS6.1StressSu@naryBook3of154-479'-4894-4965-15-25-25-25-75-75-86-16-16.1.16.1.26.1.36.1.46.1.56.1.6EquationA-1StressesEquationA-2StressesEquationB-1StressesEquationB-2StressesEquationB-3StressesEquationC-1Stresses6-66-176-286-396-506-616.2SupportLoads6.3ValveAccelerations6.3.1DBESeismicValveAccelerations6.3.2PORVTransientShockValveAccelerations6.4NozzleLoads6.5ValveLoads6.6MiscellaneousCalculations6.6.1ThermalBoundaryDisplacements6.6.2OBESpectra6.6.3DBESpectra7.0DRAWINGS

8.0REFERENCES

6-726-1056-1066-1106-1146-1206-1266-1276-1336-1407-18-1 ifqfINC4'L TechnicalReportTR-5364-1Revision0ATELEDYNEENGlNEERINQSERV(CESTABLEOFCONTENTSContinued9.0COMPUTERANALYSIS9.19.29.39.49.59.69.7RELAP/REPIPEInputDeadweight/ThermalInput/OutputOBESeismicX-YInput/OutputOBESeismicY-ZInput/OutputDBESeismicX-YInput/OutputDBESeismicY-ZInput/OutputPORVTransientShockInputBook4of15Book5of15Books6,7of15Books8,9of15Books10,11of15Books12,13of15Books14,15of15

~I1I"llICI~I!

TechnicalReportTR-5364-1Revision0-A-TELEDYNEENQlNEERINGSERVfCES1.0.INTRODUCTIONAmericanElectricPowerServiceCorporation{AEP),purchaseordernumber02676-820-1N,authorizedTeledyneEngineeringServices(TES)toanalyzethePressurizerSafety/ReliefValveDischargePipingperNRCNUREG-0737,ItemII.D.1,fortheDonaldC.CookNuclearPowerPlant,UnitPl.ThisactivitywasperformedinaccordancewiththeTES(}ualityAssuranceprogramwhichmeetstherequirementsof10CFR50,AppendixB,andANSIN45.2.11asinterpretedbyRegulatoryGuide1.64,Revision2.ThescopeofworkforthiseffortisdescribedindetailinTeledyneEngineeringServicesTechnicalProposalPR-5653{Reference1),datedMay4,1981andmodifiedasstatedinAEPletterdatedNovember29,1982,fromMr.SamUlan(AEP)to,Mr.L.B.Semprucci(TES)andinAEPletterfromMr.SamUlan(AEP)toMr.P.D.Harrison(TES)datedMarch15,1983(References2and3).ThemajorityoftheanalysiswasperformedafterthereceiptofAEPlettersdatedNovember29,1982andMarch15,1983(References2and3),whichwereissuedaftermorecompleteinformationwasavailablefrom,theEPRIdata.Thisanalysiswasperformedusinglargedigitalcomputerprogramssupplementedwithanynecessaryhandcalculations.TheRELAP5MOD1Cycle14computerprogramwasusedtodothethermalfluidtransientanalysis.Thestructuralanalysis,forallloadingconditions,wasdoneutilizingtheTMRSAPcomputerprogram.'hesizeofthepressurizersafety/reliefvalvedischargepipingsystemwassolargethatthecomputermodels,forbothRELAPandTMRSAP,strainedthelimitsoftheprograms.ThisconditionnecessitatedmultipleRELAPrunsinordertoexecutethethermalfluidtransientanalysisfortheappropriatelengthoftime.ForthestructuralanalysisitwasnecessarytoexpandthecoreoftheTMRSAPprograminordertoavoidanoverconservativeoverlapanalysis.

III'gItj"I,rit)Q'4~~a'El, TechnicalReportTR-5364-1Revision02-1r>TELEDYNEENGINEERINQSERVICES

2.0CONCLUSION

STheanalysisperformedbyTESonthePressurizerSafety/ReliefValveDischargePipingSystemindicatesthatallcriteriaofNRCNUREG-0737,ItemII.D.1ismetfornormalandupset(PORVdischarge)conditionsandisnotmetfortheemergency(SVdischarge)condition.Evaluationofnormalandupsetconditionsrequiredstructuralanalysisfordeadweight,thermal,OBEseismic,andPORVtransientshockloadingconditions.DetailsofthevariousloadingsconsideredareprovidedinSection5.BasedonpreliminarySVthermalhydrodynamictransientanalysis,excessiveloadsandstresseswereanticipatedand,therefore,itwasdecided;foreconomicreasons,thataquartermodelSVthermaltransientanalysis(RELAP5)shouldbeperformedtochecktheadequacyofthesystemfortheemergencycondition.Inaddition,duetothesimilaritiesoftheUnit1andUnit2geometries,itwasdeterminedthattheresultsofoneunitcouldbeconsideredapplicabletotheotherunit.Thequartermodelconsistedofthepipingfromthepressurizer,throughvalveSV-45C,andcontinuingdowntothequenchtank,forUnit2.TheSVtransientanalysisconsideredonlytheeffectofvalveSV-45Copening.Theresultsofthequartermodelanalysisindicatedsubstantialfailureoftheentirequartermodelgeometry.ConsideringthatTESisrequiredtoanalyzeforthesimultaneousopeningofallthreeSVvalves(Reference3),whichisamoresevereloadingcondition,itisevidentthatthequartermodelanalysisissufficienttoprovethefailure,fortheemergencycondition,ofbothUnits1and2.Therefore,thisreportforUnit1containsnoanalysisorresultsfortheSVthermalconditionortheSVthermaltransientshockcondition.ResultsoftheSVquartermodelanalysisperformedforUnit2arecontainedintheUnit2report,TESTechnicalReportTR-5364-2(Reference6).

fq~y'Irs~t.sCta0 TechnicalReportTR-5364-1Revision02-2r>TEif23YNEENGINEERINQSERVICES.Section6containsastresssumaryofallnodepoints,asummaryofsupportloads,valveaccelerationcalculations,asumaryofpressurizerandquenchtanknozzleloads,andalistingofthemomentsontheendofeachvalveforallloadingconditions.ItshouldbenotedthatvalvesNRV-151,NRV-152,NM0-151,NM0-152,'ndNMO-153areinexcessoftheveriticalaccelerationcriteriaof2gforthePORVthermalshocktransientcondition.ThesevaluesareconsideredacceptablepertheapprovalgivenbyAEPintheirletterofMay26,1983fromMr.SamUlanofAEPtoMr.P.D.HarrisonofTES(Reference7).

~FCCCCY~':fFC2~fAr!:.~sf~~CCC~,~C TechnicalReportTR-5364-1Revision03-1-r<-TELEDYNEENGINEERINGSERV(CES3.0SYSTEMDESCRIPTION/DISCUSSIONThePressurizerSafety/ReliefValveDischargePipingconsistsofallofthepipingfromthepressurizernozzles,downtothespargerinthequenchtank.ThisinformationisdepictedonTESdrawingE-5763,Revision2,generatedfromAEPdrawings1-GRC-6,sheets1,',3,4;1-GRC-7;1-GRC-8;and1-GRC-9.The"Discharge"pipingconstitutesaverylargesystemresultinginalargecomputermodel.Thesizeandgeometricalcomplexity,whichisduemainlytothesweepingcurvesaroundthepressurizer,complicatesthemodificationeffortinadditiontocausinglongerruntimes..Modificationofthiscomplexsystem,toattempttosecu'resatisfactory"SafetyValveDischarge"results,islimitedtodrainingtheSVloopseals.Heatingtheloopsealsisnotaviable"fix"becauseofthesizeoftheloops.TheselongloopscontainsufficientquantityofwatersuchthatonSVDischarge,thewatersealdoesnot"flash"completelyenoughtoreducetheveryhighloadscausedbythewaterslug.Modificationtothesupportsystemisalsoapooroptionbecauseoftheverylimitedspaceintheannulusaroundthepressurizer,whichmakesconstructionverydifficult.Anotheraspectofthesystemthatcouldbeimprovedisthesettingoftheconstantspringsupports.Duringthedataextractionofthedeadweightanalysisresults,itwasobservedthatthesupportsinthePORVloopareawerecausingsignificantupwarddisplacementsofthepipingsystem,asdetailed'inSection'.2.Thestressesintheseregionsarehighand,althoughtheydonotexceedtheallowable,theycouldbereducedbyre-adjustmentofthespringsettings.

hg'=~~~4IQilL'~IfAI TechnicalReportTR-5364-1Revision04-1-ATELEDYNEENGINEERINGSERVICES4.0THERMALFLUIDSANALYSIS4.1IntroductionThefollowinganalysisdeterminesthefluidforceswhichactonthepressurizersafetyandreliefvalvedischargepipingoftheAmericanElectricPowerDonaldC.CookNuclearpowerPlant,Units1and2.TheseforcesaregeneratedbythesuddenopeningofthepressurizersafetyandreliefvalvesduringoneormoreofthepressurizertransientsdescribedintheAEPsupplied1982lettertoTES.Theseforces,theresultingstressestheyapplytothepipingsystem,theresultingloadstheyimposeon'thepipesupports,andtheloadstheytransmittothesafetyandreliefvalvesbecameofincreasedconcernasaresultoftheincidentatThreeMileIsland.FollowingtheThreeNileIslandincident,theNRCissuedNUREG0578andNUREG0737whichrequiredthateachutilitydeterminetheeffectofsafety/reliefvalveoperationuponthevalveandthedischargepiping.AnelaborateprograminvolvingbothtestingandanalysiswasestablishedunderthegeneralmanagementoftheElectricPowerResearchInstitute(EPRI).Intensivetestingofsafetyand~eliefvalveswasperformedatseverallocationsacrossthecountry.AfullscalemodelofthepressurizeranddischargepipingwasbuiltatCombustionEngineeringinConnecticut.'imultaneously,ananalyticalprogramwasinitiatedtochooseandtestacomputerprogramwhichwouldpredictthefluidforces;RELAP5MODlwaschosen.ThisisthelatestinthefamilyofRELAPprogramsdevelopedattheIdahoNationalFngineeringLaboratory.Inthisanalysis,TEShasusedRELAP5MOD1Version2.11asitismadeavailablethroughControlDataCorpwithapost-processor,REPIPEversion3.10,whichcalculatesthefluidforces.

I~'k~$glPiIAes~C TechnicalReportTR-5364-1Revision04-2-ri-TELEDYNEENGlNEERlNGSERVlCESThisversion.ofRELAPSNOD1isidentifiedbythefollowingcomputerjobcontrollanguageatControlDataCorporation:BEGIN,REIAP5,R5N2,INPUT=INPUTFILE,SCM=377000BThecomputeranalysisprocedureforthethermalanalysisportionisincludedinAppendixA.RELAP5calculateshydrodynamicdataforcontrolvolumesineachsegmentofpipe.REPIPEthentakesthisdataanddefinestwoforcetimehistoriesforasegment.Onesetofinletjunctionforces,theotheroutletjunctionforces.SAP2SAPaddstheseforcetimehistories.Finally,oneforcetimehistoryforeachsegmentofaxial,unbalancedloadsisanalyzedstructurally.

C+w~l TechnicalReportTR-5364-1Revision04-3>s-TELEOYNEENGlNEERINQSERVICES4.2RELAPModel4.2.1TheD.C.CookpressurizerwasmodeledasasingletimedependentvolumewiththefollowingtransientconditionsasspecifiedbytheAmericanElectricPower11/29/82lettertoLBS,pages1-7:Case1::~Sf'llSteam,LoopsealCaseZyooZhs'dPressurelWD/)gp+gR@~49pPc~o-e-o-p-ppgpg+PaloZt'o4pp25rgJ/OTime(Sec)

"('w,.:f~q;~.~=hlW4y/0 TechnicalReportTR-5364-1Revision0isTELEDYNEENQINEERlNQSERVICESPORVSteam/CondensateSlugsCase255025002450Pressurepsi2400235023000.8Time(Sec)1.20.4Case2:ContinuousWarmWater=400oF(SamepressureasPORV,Case1)4.2.2SafetyvalvesandpoweroperatedreliefvalvesweremodeledasRELAPjunctionsusingthefollowinginformation:SafetyValvemanufacturerCrosbyHB-BP-86(Ref.13)0if'CJJiTi0.022Ft20.010Sec.PORVMasoneilanNO-38-20721(Ref.14)0.00806Ft21.0SecValveorificeareaswerecalculatedusingtheEPRISafetyandReliefValveTestReport(Reference16)andRELAP(RunIDBAICDRO)implementingratedflows.CalculatedvaluesareincludedinSection4.6.1.

is'>'lyI'I1)I' TechnicalReportTR-5364-1Revision045]<TELEDYNEENGINEERINGSERVICES4.2.3Dischargepipingwasmodeledfromallsafetyandpoweroperatedreliefvalvestothequenchtank.Thisdischargepipingincludedthefollowingpipesizes:3inch,12inch4inch,6inch4inch3inch,6inchSCH40SCH40SSCH120SCH160Frictionfactorsfor1.5Dorshortradiusbendsandreducersweretakenfromtechnicalpaper8410byCrane.CalculationsoftheselossesandconstantsareincludedinAppendixA.SegmentlengthsusedarelistedinFigures4.2.1and4.2.2forbothmodels.Thedischargepipingdefinessegmentswithsegmentsdescribedasstraightsectionsfromelbowtoelbow,valvetoelbow,etc.Also,alistingofRELAP5inputisincludedinthisreport.TheSRVmodelismodeledfromonesafetyvalvetothequenchtank.Thiswasdeterminedtobeanadequaterepresentationofsafetydischargepipingforbothunitsandwillsubsequentlybereferredtoas"TheQuarterModel".TheQuarterModelismodeledutilizingUnit2'sgeometry.'.2.4TheQuenchTankwasmodeledintwoparts:thespargerandthetankitself.TheQuenchTankismodeledusingcylindricalvolumescontainingwaterandair.ThevolumesizesareequaltoquenchtankvolumesprovidedonWestinghouseDwg.No.110E272.ThespargerforD.C.CookisaperforatedpipesubmergedinthewaterwithinthequenchtankasindicatedinFigure4.2.3ofthisreport.ItisrepresentedinRELAPasapipeequalinvolumeandsimilarlysubmerged.

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TR->>64-i~A~TELEDYNEENQINEERINQSERVICESRevision0BYA-DATE~ICHKD.BY~~CHOATE+gOMA~2)C.1"00<vrrc~~ld&au.~7A7/Oa'e/rS<5z.dz4cilgN4"E~6SHEETHO.OF~zPROJ.NO./ZgVEA/CdTAVEIS7~/EAI:C>L/nJSEPW/TA'=A'//-'~NLSGE&.zUS7-~/i=("')'x/I-//E/d//7Ã7//F.'ATi=h'EVEL;/KA1307TOhlOFIHE7AAJKi-A/zw(~),.I0nuuusvz:u;iAZWCus.Au-Aw3ziz~oNziC,>PCFrCv'--We~a)=~z.Vsaa-.p"Stk~ST/7UTiltJ6N70=QAQ<ggyg88J1-56ZSQs-~)'/8-/340=Bv'AILA@AEA'Od:"5~AFIGURE4.2.3-3 4-13TechnicalReport~jr'ELEDYNEENQINEERINQSERVICESRevision0(BY+A+DATE~/LUJDoA/ALoc.coLAOHHD.BY~K~DATE~II83I/UC'A//SEALaTATICAJ<ALIISYIZdEVCL(-.A~P'<WLL,IV6SHEETNO.OF~PROJ.NO.D+'5Ln=/I.FSM<<@=h=Z.4eVse=h~P=~~.Fs+z.~eyei/8g~=K>8+uzIoIIroF.LIAro//~u//~acr.F//ou7//eJomw.OF7iVE~v'EA/CHrAdK-Q-//=gYL'-=>15gk>POLI:'IFIOF.OF7//EO/BiVCH7AA/L'O7EA<ATŽE~r'FACE:<10MiVI4T=A'U/PRICE,70THEC~!JT"A'/7QFIOKIZAAJTAL~-"C7/OAJ077Hz~~rAR6EP~C8'~==-.~:.;~4+\C/Elhi/7OFAJATEglZVFL'AJgIhiVCFPTArtfK8'OS'/LIF1ZEAL~G=6M'f$,'L/PLUPIEOFÃHTEÃIPJ~~0K/JC.~/?RAN'='IIF&(g'aWee!C=-Ay=aZZnweef~W7ZW~us/I'.as%'loLUI/IE'F-AIR'A)~~&'EAJCh'/'lg-/ISIC64-1)<TELEDYNEENQINEERINQSERVICESRevision0BYSA2DATE'/-XF-83CHKD.BYE+DATE~4-15Z)ONAIDC.COO/Qg+LEpp((y5/lj.a7871&J~IVITS4r~Z.kE~LiV'5"ifÃnJC//~/IAJARP~L/Alb.SHEETNO.OF~PROJ.NO.IEQw~~o-pZIIji,tIoWkfj.II~j>~I~C1qI-I-IIQ00~SI!FIGURE4,2,3-6 TechnicalReportTR-5364-1Revision04-16]5TELEDYNEENGINEERINGSERVICES4.3RELAPModelControlVolumesTheEvaluationofRELAP5/MOD1forCalculationofSafet/ReliefValveDischarePiinHdrodnamicLoadsreportpreparedbyIntermountainTechnologies,Inc.recommendsusingtenormorecontrolvolumesperboundedsegmentwhileavoidingsignificantcontrolvolumelengthdifferencestopreservepressurewaveshapes.ThetencontrolvolumecriteriarecommendedbyITIwasadheredtoexceptinpipingarcsandinsegmentslessthanthreefeetinlength.TheD.C.Cookdischargepipingismodeledusingasfewasonecontrolvolumepersegment(pipesegmentswithlengthslessthan0.5feet)anduptothirty-twocontrolvolumespersegment.ArcmodelingforbothunitsisrepresentedinFigures4.3.1and4.3.2.AllarcsforUnits1and2weremodeledinRELAPashavingnofluidlosses.Essentially,RELAPcalculatestheseasstraightsectionsofpipe.REPIPE,however,Jdistributesthecalculatedforcestopre-assignednodepointsmatchingtheTES~~structuralmodels.AveragecontrolvolumelengthsusedfortheD.C.CookRELAPUnits1and2modelwere:PioeSizeAveraeC.V.Lenth3inchSCH1606inchSCH1604inchSCH40S6inchSCH40S12inchSCH403inchSCH404inchSCH1200.4644feet0.5264feet0.4471feet0.8614feet0.8064feet0.4744feet0.5056feetAschematicofthedischargesystemsmodeledinRELAPforthePORV~~~~~~Unit1modelandtheSRV1/4modelforUnit2aregiveninFigures4.7.1and4.7.2,respectively.

Technica1ReportTR-5364-1Revision04-17ATlHEDYNEENGINEERINQSERVICESquenchTankmodelingwasachievedusingtwentycontrolvolumesandtwentyjunctions.Eighteenvolumescomprisethespargermodelwhiletheremainingtwoaresinglevolumesmodelingthewaterandairspacesofthequenchtank.ThewaterandairvolumesasdeterminedfromWestinghouseDwg.No.110E272wereinputtoRELAPtoinsureproperquenchingcapacity.Eighteencontrolvolumesformingthespargerareinitially88Kfullofwaterrepresentingasubmergedpipe.Thedischargeholesweremodeledasasingleholeofequivalentareaattheendofthepipe(aconservativeassumption).Finally,thetankrupturediskismodeledasapressureactuatedvalveplacedontheairvolumeandsettoblowoutat100psigdischargingtoatmosphere.(Figure4.2.3representstheD.C.CookUnits'and2quenchTank).

TechnicalReport1S-TELEDYNEENGINEERINQSERVICESeBY+DATECHKO.BY~+~OATE~'783~om<~PqMooel@@9-Zg~if'3SHEETNO.<>'S//FIGURE4.3.1ggP:a&(cg~ct2-9/-8I0nqYl~4'I/E'~P!~Qr.roV',o,/,/.~o',,ibbTSTO/410E'SQgcS4OINOESIIOY TTechnicalReportReyisionPIITELEDYNEENGlNEERlNQSERVlCE$4-19BY-DATECHKD,BY~C~DATE2I~83SHEETNO.OFPROJ,NQ.FIGURE4.3.2-1IZ~AFM02)eZ.OFnile(a~~EVW77OV4~9'-2"(A/CX)~STI/)S5+r=-r.rsv~II/p.>okla.~c~&559'l0C"ePSCbVALVE'i.I3.70" TechnicalReport-ri-TELEDYNEENQINEERINQSERVICES4-20By'8DATE~~CHKOBY~OATS~+sc.cook'A'/7-4ARC~&~oem/'~'@zL~V.bN-'4o"SHEETNO.OF8FIGURE4.3.2-23'ElAPX61oDEloFAICDELE'LfA7/OAJ4r'V-IO(AA'C2)vAave/Mg.yb'IIgcI~c(NE&C55/(OSV-~y'e.///8,/g+IAE"/,g/hg\pyqp~Bosch-'<+PzwAEA'8-.QgP/+PALN/g~/Qg/~7~=ran'/rC//(rtZ/JOZZSaiwzu-i'zrivzzu@oarsuz~e.~xrcoxes~pe)~u)zAdC'PC//hS.

TechnicalReportTELEDYNEENGlNEERlNGSERVlCES4-21BYDATE~~8~CHKD.BYSCDATE~>i~3v.C.COO/C,UQI7Agg~C~ECbtSZg'/paaLgggQ'-'5"SHEETND.DF5'IGURE4~3~2-3W<~/="L/Ne/fee.,eZ~~VA77iOrV-'-~"(A/CZ)wlg)./Lyceca8"c,~sjQTj/TNC')~Ig'l/V',jI'iaC654'~Fgg/z>>=c//~eP//I/8J~/'c../:,'/JEP~~/AA'Ae:dggg~g=,y~//Jo/cn7~srtuCruZAL4ODFSg//I/r+c/PQ9E7fg/=l'hJQg~lg>grjP+Ec'c-pJ7'QHZ="/30pJ/AJAR/lgC'JCVTHS

TechnicalReportRevision0ATELEDYNEENQINEERINQSERYlCES4-22eY<>+DAve>~s4>CHKOBY,OATEYT23soJuniziwaRvsEc.rio~RE'tA'PHobGL.(D>~<5TPCRM)SHEETNO.OFsPROJ.NO.S36fFIGURE4.3.2-4OssoOs2s/o~.2%IIS'+IO>><IIII'OsssDqll>Ipl3oi~6'SAGEOsooOIo'2'o.g23',(p~gb2OIrt\+3ZAI3O3PAO335F TechnicalReportTR-5364-lRevision0EENQNEERINQSERVlCES4-23YOATEN~ciHKD.8Y~+DATE~Z~Sr7iec~@4's's"SHEETNO.OF55'IGURE4.3.2-5(oa~yoga(o, 0

TechnicalReportSHEETNO.OF/vM~'r)HA>hlAP.C,cosh)CcTIDP5p~A,McHCS+T'E'E.SBY~~DATE~><"~~CHKD.BY+DATE~~~~RemisionP]lTELEDYNEENGINEERINGSERVICES4-24FIGURE4.3.3-17~SAIC'.f4h/3O7I830@'SMGL,~NBOQ5NCrL~AIeoN0I8045N6rLJulINo725%08SNCL~EIPJBO(oSN&l~LI808su&LzvM/o7p

TechnicalReport-rS-TELEDYNEENQINEERINQSERVICES4-25ST<-<ORTS~>><~CHKO.BY++DATE~~~+~oNtT'PoRVSt=cT>cMBRAW)cRE5+75ESSHEETNO.OFzzPROJ,NO,+3++FIGURE4.3.3-270254&c3oAyHZ~n0taSNAKC.guuEJ5M-+ISZ9Si3gN~tuN3PAMC//l5///95lg.5N6LvsGo+$N&VUH+peSHCL~N~,IHoI2SBRANCHJog0/(yPzZSri~)40$SNABgZu~hJ008SNGLJuhlgo~gggoy'BRANCH4090/(EJJsr~OJF~)

TechnicalReportTR-5364-1Revision04-26ATELEDYNEENGINEERINGSERVICES4.49Nd1Beforebeginningtheas-builtanalysisforthesafetyvalves,itwasalmostcertainthattheloadswouldfailthesystem.AreviewofthetestingthatwasdoneatCombustionEngineeringinConnecticutindicatedthiswouldbethecase.ThecoldloopsealdischargetestatC.E.producedloadsof175Kips.TheD.C.CookUnits1and2pressurizershavethreesafetyvalveseachwithaloopseallargerthantheC.E.testfacilityloopseal.Therefore,itwasdecidedtomakeasmallRELAPmodeloftheD.C.CookSafetyValvedischargeline.Thismodelcontainsonesafetyvalve(SV45C)includingitsloopsealpipinganditsdischargepipingthrougharclevel669'-2"upto,butnotincluding,thequenchtank.Thismodelwouldbelessexpensivetorunthanthefullthreevalvemodel.Theresultsofthissmall(quarterModel)confirmedoursuspicionthatthecoldloopsealcasewouldfail.Italsoallowedustomakeaparemetricstudyofloopsealtemperatureinloadsasisshownbelow.Onlythesteamdischargeprovedtobeacceptable,therefore,TEShasrecomnenedtodraintheloopseals.LoopSealLoopSealTemperaturePositionofValveOpeningMaxLoadConditionoFLooSealTimeSecLBFColdColdHotHotHotHot(Sat.Water)Steam141o141o350o350o350o650o650oUpstreamDownstreamUpstreamUpstreamUpstreamUpstreamUpstream0.0100.0100.0100.0900.1300.0900.010115,000174,000156,000109,000124,00038,000,6,000Theloopsealtemperaturedistributionwascalculatedtobeinputto~~~RELAPandisincludedintheAppendixA.Thetemperaturesusedforthecoldloopsealr'angedfrom584.4oatthepressurizerto141.1oatthevalve.

TechnicalReportTR-5364-l)q~LEDYgEEgggEERiNGSERytCES4-27BY+~~OATE~+Z2CHKD.BY~>+DATE~/g/J//"/p~/OVdtb'~c~/gc.cv/~wcnl+<%YSHEETNO.OF1i/F7<V4'//,nlR'y/53/coWrac/~<:8'HE'W~4.d~4~ovggrrsr-rrFAFE=(r~gFrs-jest,.z@)r=r=rEg9gFrggyp/-r.,gooC4CM-~"/.%9O~ri~25/os&z5C/oDFl//O<)gcr2FfZ4>PC7Py)PA.Vg-42Q5qFrg.(18)jFFIG.4.4.1-1 TechnicalReport8>TELEDYNEENGINEERINGSERVlCES4-28sv~~+oAva~~>8~CHKO.BY~EsCATE~~TEST@~ipirALUrDfrauwSI~a~cu~8zr~SHEETNO.~OFtSViiV~8'Cr7+Qdq12'wF=-yOSrB(IWI)PvP&cd.gigaCrg,/0)3~-Ff/i,=(H&>8-Wp'IZp)r-ro&r<izorTEA=F'ros(s.FAYEEwr')(v'.ESE,rrr(+SBErr-AT.EFTErr))Y~~~Spy/ru'E~&fiv-aux<s~jzr+pripse'ud4)z.-gw9wrFIGURE4.4.1-2 TechnicalReportReyisionp9ETELEDYNEENQINEERINQSERVICES4-29SY<~~DATE'i8~;4<<fCHKD.BY~DATE~<AgrDVague&a<ggrVProdPeavw'g~pSHEETNO.OF8b8b'gzvzrXy5ZPriso0.9r//FrErv<<Ãr~4<dggwy~i@+ij~gy</>"-O'P7~~,-S9=9.2/87'<n-h,-;>HE.~rFlGURE4.4.1-3 TechnicalReportR;;0ATELEDYNEENGINEERINGSERVICES4-30EST~~~OATS~SEESCHKO.BY~~DATE>~j/~rgbVol6'~8ggzgygh'PontAge'>447ESHEETNO.OFEPROJ,NO./d//Uec-bi-/7.-fcUS&U'A,YflP-/$$0$y"(/P/J)r=d.rofH/./QN/+Z',<pz/7/.S'/O/A,+y,/dUS'AF)(!/"$+FP<BQOgFF)Ir)r~j//',/z&o7dr8c.cqg/g/PMAJFDxNAA.use<gnarl+~'L(.</P<-o'za)FIGURE4.4.1-4 TechnicalReportATELEDYNEENQlNEERlNGSERVlCESIBYPAYAFOATE~BZ2-CHKo.eY~~oaTE~~~~bw/'1J'cD/ov>46ME'P~cvuFM~~~>Rv'~xcSS.BMEETNO.OFvH~vZaz:NAY/5Iac///'eop/r/Ncr7KEE-O.d9$5r7<88gg/gM4M',/pF'ra.co8pr0F~Cgcc~c.c~;g.g.'9KCld.25'2iiI/7o~+Evened=yza(F/z.~zw~d.Ei8gWrFIGURE4.4.1-5 TechnicalReportRevision0ATElEDYNEENQlNEERINQSERV(CES4-32CHKD.BY~++DATE~~~Drtfr1'c&rovo4uwz5z<u~no~~agv'e'<E<SHEETNO.k<>F&I=a.rotag+rjy=MiaWv.cr)<(u.its~~<<)g3Jr'.@~9'ouivying'iui-i.u<zsiici-wgianrus~)2.&SPFIGURE4.4.1-6 TechnicalReport-ri-TELEDYNEENQINEERINQSERVICES4-33cHKD.8Y~QATK~TTPaEV}PfcE'w-'LOS.t~oQELEQFogQQQp~.'3NlT'HEETNp./pFPROD.NP.2&Oopic4)ue+IgP'i15z'JC+il<gC~'7i(ol~...g=.09zlr4Abut,c885~+hg"g-(,O92iH-')/j.oo8~>l')l.~(~PPfi)/(,(ZOC2,il'8~)=.f~77L~,@77T,TZI-'f.(;z.@X','=-~Yd'>'gieuiCi/)i/OSmPOll.I)'tO-;i.oa5Vkf~3,tuiNg~~rii'QA-)/(6cei-~4.987Lh~(,ageIf)~)/(,,molo8Ili)ofJ.J)8FIGURE4.4.2-1 TechnicalReportp)g~LQDYQQfNQpJQQQgQ$QRQ[CQ$4-34CHKO.ST~++OSTE~K~83~P-4Ih(LETSLug~OKLgQ.FoR.PELE).Ug)T'SHEETNOOS)/I~'QTIE,,/0~8gEO(r7/7/3FIGURE4.4.2-2 nm\AIVE+EIQQALli(LEAI~~TIIal~llJaCVO~AP..AIIPE')>C'm00fbX7(bI0Ul'XVl0W0IQlC)tDol~jeVi~~'].QGQf"r/hlC/./~<~144-'ci(/bO~ppAi.Q/IVCc/Seal/AC)p)H(IEhlRVisjNIC/J~~C>II/oOFI(illRE4.4.2-300mIIIZZ00

TechnicalReportTR-5364-1Revision04-36ATELEDYNEENGINEERINGSERVICES4.5Unit1PORVModelTheinletpipingtothePORV'sisslopedtowardthevalves.Therefore,duringnormaloperatingconditionsasaturatedwater(condensate)loopsealisformedattheinlettothePORV.AsspecifiedinAmericanElectricPower'sletterofNovember29,1982,referringtoPORVtransientconditions,thefollowingcasesweremodeled:CaseTransientCondensate/SteamDischarge400oSolidLiquidDischarge4.5.1Thewayinwhichthecondensate/steamcaseloopsealwastobemodeledwasdecidedbyusingtwomethodsonasmallsamplemodel.a~b.LowequalitySteamLoopSeal(SaturatedConditions)SolidLoopSeal(SaturatedConditions)Alowqualitysteamloopsealproducedoscillatorymassflowratesthroughthevalve.Theseoscillationsweresevereenoughtocauserejectionofthismodelandtochoosethesolidcondensatecase.TheseoscillationsaretheresultofnumericalinstabilitiesinRELAPschokingcorrelation.Thisisduetotheseverechangeinsonicvelocitiesinthetransitionrangebetweensubcooledwaterandsteam.4.5.2Bothcases(loopsealand400oFsolidliquiddischarge)weremodeledandrunonRELAPandREPIPE.Theresultingforcetimehistorieswerecompared.Itwasnotclearatthislevelwhichcasewasmoresevere.Therefore,theforcetimehistoriesforbothcaseswereinputtothestructuralprogram.Itcouldthenbeseenthatthe400oFsolidwaterdischargeconditionwasthegoverningcase.

TechnicalReportTR-5364-1Revision04-37->s-TELEDYNE.ENGINEERINQSERVICESBoththeloopsealandthesolidwatercaseexhibitedunstablebehavior(o'sciIlationsintheflowrate).Theloopsealcaseshowedtheseoscillationsinthetransitionregionatthetailendoftheloopsealasitpassedthroughthevalve.RELAPtendstocauseflowrateoscillationsbecauseoftheseverechangeinsonicvelocitiesbetweensubcooledwaterandlowqualitysteam.Theseflowrateoscillationsresultinhighforceswhichtendtobeoverlyconservative.Inthe400oFsubcooledwatercase,thereasonfortheflowrateoscillationwasmoreobscure.Atapproximately.400secondstheflowsuddenlydecreasesapproximately30Ibm/secinlmsec.ThiscanbeseeninSection4.7.2.AcarefulreviewoftheRELAPoutputdidnotrevealagoodphysicalreasonforsuchbehavior.Reasonsforsuchbehaviorcouldbe1.Asuddenreductioninthevalveareavs.timedata.l2.Abuildupofbackpressureinthedischargelinewhichwillcausethevalveflowrateto'uddenlydecrease..3.Asuddendecreaseinpressureinthepressurizerboundaryconditionwhichwouldresultinreduced-flow.Allthesethingswerecheckedtoseeiftheywerepossiblesourcesoftheflowratefluctuation.Butthereviewindicatedthattheywerenotthesourceoftheproblem.

TechnicalReportTR-5364-1Revision04-38r<TELEDYNEENGlNEERINGSERVlcESApartialtabulationofthisreviewisshownbelow:UNITIValveJunction¹410Cont.Yol.41101Cont.Vol.40926ReferenceRELAPRunBHFRFGGlowUnit.1200-600msecSo1idRed.Time.408.409Junction¹410Flow111.1883.424Cont.Yol.¹409260.00.0Cont.Vol.¹41101p248.89245.55Cont.Vol.¹40926p2342.83058.Itcanbeseenthatthedownstreampressuredoesnotexhibitasuddenincreasethatwouldreducetheflowthroughthevalve.Theupstreamqualityremainszerosothattheflowthroughthevalveissubcooled.Thepressureincreasesupstreamwhichcorrespondstoasuddenreductioninflowarea.However,theflowareaincreasesitdoesnotdecrease.Thepressurizertimedependentvolumedoesnotexhibitanysuddenchangeinpressurewhichwouldcorrespondtothisflowchange.PastexperiencewiththeRELAPprogramshasshownproblemswithsubcooledwaterandlowqualitysteamflow.Theseproblemshavemanifestedthemselvesassevereoscillationsintheflowrate.ItisouropinionthattheresultsfromtheRELAPrunarehighlyconservativeandoverpredictthefluidforces.

TechnicalReportTR-5364-1Revision04-39ATELEDYNEENGlNEERlNQSERVlCESMhenthefluidforcesfromthisRELAPrunarecombinedwiththeseismic,deadweight,andthermalexpansionloads,theallowableswereslighltyexceeded.SincetheprincipalfluidloadsappeartobearesultofaninstabilityintheflowratepredictedbyRELAPandnotaresultofanactualphysicalphenomena,itwasdecidedthattheseloadswereoverlyconservativeandcouldjustifiablybereducedby20K.'hefluidforcespresentedinSection4.8andelsewhereinSection4.0aretheascalculatedloadsandhavenotbeenreducedby2(C.ItshouldbenotedthatanalternativemodelingpracticethatcouldhavebeenemployedinthesolutionofthisproblemwouldhavebeentomakethePORVvalvestimedependentjunctionsandspecifythevalveflowrate.Hadthisbeendone,theflowrateoscillationandtheirresultingforceswouldneverhaveoccurred, Techni,calReportTR-5364-1Revision04-40ri-TELEOYNEENGINEERINGSERVICES4.6ValveFlowRateCalculationValveTeTESFlowRateCalculatedLBM/HRMaxRating*ForSteamBoreArea93XAccom.~IN~OpeningTimeSecC~rosbSafetyReliefValve523,332435,0003.6in20.010(Ref.18)Masoneilan199,000OpdReliefValve1.0(Ref.16)*Themaximumratingforsteamat3XaccumulationvalueisfromtheCrosbyValveJandGageSafetyValveDrawingNo.H-51688,RevisionA.

TechnicalReportTR-5634-1Revision04-41]iTELEDYNEENQINEERINQSERVICES,=4.6.1ThevalveflowratesusedinRELAPanalysisoftheSRVswereobtainedbyincreasingtheASMEratedflowby15K;l(CtoconsidertheASMEunderatingofthetheoreticalflowand5Xtocovertolerances.TESflowratecalculationsareincludedinFigure4.6.1.WT=51.5APASMEratedflow:WR=51.5A(1.03P+14.7)(.9)(.975)Cwhere:(Ref.17)WT=theoreticalflowWR=ratedflowcoefficients:1.03-applies3Xaccumulation0.975-valveflowcoefficient0.9-representstheoreticalflowratereduced1(CtoequalASMEratingTheequationTESusestocalculatethevalveflowrateisWmax=1.05x51.5A(1.03P+14.7)C(0.975)explainedabove.Thisisanincreaseof15KabovetheASMEratedflowas

TechnicalReportTR-5364-1Revision04-42-ri-TELEDYNEENGINEERINGSERVICES4.6.2TheMasoneilanPORVmaximumflowrateforsteamwastakenfromtheEPRISafetandReliefValveTestReortas199,000ibm/hr(Table4.5.1-1b).Avalveopeningtimeof1.0secondsisusedbasedontotalvalveopeningtimesofallMasoneilanvalvestestedlistedinTable4.5.2-1.Sincefullopentimesaveraged2.76seconds,withaminimumvalueof1.64seconds,TEShasassumed10(Copeningin1.0second,becauseindependenttestinghasshownthatflowisnotalwaysdirectlyproportionaltostemtravel.Mostoftenfullflowisobtainedbeforefullstemtravel.8ecause1secondisaverylongopeningtime,thiswasnotconsideredoverlyconservative.

TechnicalReportRevision0)<~TELEDYNEENQlNEERlNQSERVICES4-43svDATE~~jhCHKD.BY~f~DATE~~C~SYYam(V'A4-VGQ~~~~gagpLoWAQ~Ct0~7pcrASHEETNO.~OT2PROJ.NO.rP~a-aec.77lh'-7.P3.j,Iar8r78.7>>72(r78<)~4,&de/'B.BP-8firalucgrcurg~ic.h'Sl(c884).ACcpuler-P~&TCDQCixxoexY~tQcluarr7cnufccturrCPS+.SYVcluacCeca@.Ccpcpgc,)lo8N4ag2~:a'o~A.PICCJe~in~Qx'pl~~tpilif'IChheeeC'f~~p5i(jHe->>.84CatIah~oIPbxl=l~Pal.c(Vl)~'~VPAOngCod~~eC4rCke'On>finobkioe.ngWrruxr)IkeyCalculadranCscacaoonk74dater'ne.aRailx5a'('ccaieeanameandknecaaeor'lyrcjre-'rnwprC~'~i~f~cfjC7ri&.IE):nrraxglcua'n/~~an=rce-.e1l/CCCCVnd~mr~8.o,/~Mfarr7ICTCwC.C.Qf&~O4Mdp/2-77zy.2US>H(~CECI..V,i,x=l.o5'Slox3..cxae,(2'llSxiaxarq7'r)C.(5.).7S)C..i&OCor3.~-j~pO.?Z97P~e-iaer}Pae,i'28pgC,=l.o7]/ct}~~4~'n/...=~>>~~~~i'j.-Fig.4.6.1-1 TechnicalReportRevision0ATELEDYNEENGINEERINGSERVICES4-44CHKD.BY~DATE~CQciwel'~>vA<YE'~p~rhea~@kmGA~LA~SHEETHO.~OF2PROJ.NO.S<id,fQ/SZS,g'/o.OSrhr=/'/S,37~/oecTHE'ornrTvTEiz'QoorBAz~p'roloe.follefoencreein/heroniw+cK)0o&z.t+iloorc,4e.QCilofen'g-ISO.if/~cR~ro/e.C?gotooo~;~of/l.e~lE.~/Saoi+l~c.IRCLAPSflosoc'eo'i'ohetLuErwlrilesx)E/SB7~l~e(Col&4eO8bifinWfool;*ion,IQby7-138.DIAAoo=o./To//.org(ocoed)OQ2.M4>(v)O.OO8O(4/(Rev)Fig.4.6.1-2 TechnicalReportTR-5364-1Revision04-45-ATELEDYNEENGINEERINQSERVICES4.7RELAPPlotsThefollowingplotsrepresentRELAPmassflows,pressuresandqualitiesatvariouspointsalongthedischargepiping.SinceRELAPhadtoberestarted,theplottimescalesmayvary(i.e.0.0-0.2secondsor0.0-0.400seconds).Also,theordinateaxismaynotalwaysbecorrect;manytimesmultiplierswillbeoff(COCisawareofthisprobleminRELAP).However,theydodepictthetrendaccuratelyandarecalculatedandreportedinRELAPevery.0.001seconds.Correctpeaksandtimesatwhichtheyoccurarelistedwitheachtrace.PlotSetTransient4.7.1Unit14.7.2Unit14.7.3quarterModelCondensate/SteamCase400oSolidLiquidCaseColdLoopSeal/SteamCaseARELAPvolumeschematicprecedeseachplotset.

TechnicalReportTR-5364-1Revision04-46]iTELEOYNEENGINEERINGSERVICES4.7.1Unit1-Condensate/SteamCase

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  • TechnicalReportTR-5364-1Revision04-244ATELEDYNEENGINEERINQSERVICES4.7.3uarterModel-ColdLooSeal/StearaCase

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