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Rev 0 to Technical Rept TR-5364-3, Analysis of Pressurizer Safety Valve Discharge Piping Sys,W/Drained Loop Seals Per NUREG-0737,II.D.1 Unit 1, Vols 1 & 2.W/two Oversize Drawings.Aperture Cards Are Available in PDR
	ML17334A492
Person / Time
Site:	Cook
Issue date:	07/18/1983
From:	; TELEDYNE ENGINEERING SERVICES
To:	;
Shared Package
ML17334A491	List: ML17334A490; ML17334A492; ML17334A493;
References
	RTR-NUREG-0737, RTR-NUREG-737, TASK-2.D.1, TASK-TM TR-5364-3, TR-5364-3-R, TR-5364-3-R00, NUDOCS 8312210225
	Download: ML17334A492 (239)
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AMERICAN ELECTRIC POWER SERVICE CORPORATION 2 BROADWAY NEW YORK, NEW YORK 10004 TECHNICAL REPORT TR-5364-3 REVISION 0 BOOK 1 OF 3 DONALD C.COOK NUCLEAR GENERATING STATION ANALYSIS OF PRESSURIZER SAFETY VALVE DISCHARGE PIPING SYSTEM, WITH DRAINED LOOP SEALS PER NUREG 0737, II.D.l, UNIT 1 JULY 18, 1983 PV'TELEDYNE ENGINEERING SERVICES 130 SECOND AVENUE WALTHAM, MASSACHUSETTS 02254 617-890-3350

H'echni cal.Report TR-5364-3 Revision 0-r<-TELEDYNE ENGINEERING SERVICES TABLE OF CONTENTS

1.0 INTRODUCTION

2.0 CONCLUSION

S 3.0 SYSTEM DESCRIPTION/DISCUSSION 4.0 THERMAL FLUIDS ANALYSIS 4.1 Introduction 4.2 RELAP Model 4.2.1 Pressurizer Conditions 4.2.2 Valve Modeling 4.2.3 Discharge Piping 4.2.4 quench Tank 4.3 RELAP Model Control Volumes 4.4 Valve Flow Rate Calculation 4.5 RELAP,Plots 4.6 Force Time History Plots 4.7 RELAP Input 4.8 REP IPE Input 4.8.1 REPIPE Input-Section A 4.8.2 REPIPE Input-Section B 4.9 Appendix,A 5.0 STRUCTURAL ANALYSIS 5.1 SV Transient Thermal Analysis 5.2 Transient Shock Analysis 6.0 ANALYTICAL RESULTS 6.1 Stress Sumary 6.1.1 Equation C-1 Stresses 6.1.2 Equation C-2 Stresses 6.1.3 Equation C-3 Stresses 6.2 Support Loads Book 1 of 3 Book 2 of 3 PAGE 3-1 4-1 4-1 4 3 4-3 4-4 4-4 4-4 4-11 4-19 4-25 4-63 4-134.4-154 4-155 4-161 4-169 5-1 5-2 5-2 6-1 6-5 6-16 6-27 6-38

Techni cal Report TR-5364-3 Revision 0 A TELEDYNE ENQINEERINQ SERVICES TABLE OF CONTENTS ont nued: 6.3 Valve Accel erations 6.3.1 DBE Seismic Accelerations 6.3.2 SV Transient Shock Valve Accelerations 6.4 Nozzle Loads 6.5 Valve Loads PAGE 6-79 6-80 6-84 6-88 6-94 7.O,DRAWINGS

8.0 REFERENCES

9.0 COMPUTER ANALYSIS 9.1 RELAP Input 9.2 REPIPE Input 9.2.1 REPIPE Input Section A 9.2.2 REPIPE Input Section B 9.3 Thermal Case 3 Input/Output 9.4 SV Transient Shock Input Book 3 of 3 7-1 8-1 Technical Report TR-5364-3 Revision 0<<TELEDYNE , ENGlNEERINQ SERV!CES

1.0 INTRODUCTION

American Electric Power Service Corporation (AEPSC), purchase order number 02676-820-1N, authorized Teledyne Engineering Services (TES)to analyze the Pressurizer Safety/Relief Valve Discharge Piping per NRC NUREG-0737, Item II.D.l for the Donald C.Cook Nuclear Power Plant, Unit 81..This activity was performed in accordance with the TES quality Assurance program which meets the requirements of 10CFR50, Appendix B, and ANSI N45.2.11 as interpreted by Regulatory Guide 1.64, Revision 2.The scope of work for this effort is described in detail in Teledyne Engineering Services Technical Proposal PR-5653 (Reference 9), dated May 14, 1981 and modified as stated in AEPSC letter dated November 29, 1982, from Mr.Sam Ulan (AEPSC)to Mr.L.B.Semprucci (TES);in AEPSC letter from Mr.Sam Ulan (AEPSC)~~~~~~~to Mr.P.D.Harrison (TES)dated March 15, 1983 (References 1 and 11)and in TES letter 5364-44 from Mr.P.D.Harrison (TES)to Mr.S.'Ul an (AEPSC)dated May 28, 1983 (Reference 10).The majority of the analysis was performed after the receipt of AEPSC letters dated November 29, 1982 and March 15, 1983 (References 1 and ll), which were issued after more complete information was available from the EPRI data.This analysis was performed using 1 arge digital.computer programs supplemented with any necessary hand calculations.

The RELAP5 MOD1 Cycle 14 computer program was used to do the thermal fluid transient analysis.The structural analysis, for all loading conditions, was done utilizing the TMRSAP computer program.The size of the pressurizer safety/relief valve discharge piping system was so large that the computer models, for both RELAP and TMRSAP, strained the limits of the programs.This condition necessitated multiple RELAP runs in order to execute the thermal fluid transient analysis for the appropriate length of time.For the structural analysis it was necessary to expand the core of the TMRSAP program in order to avoid an overconservative overlap analysis.

J' Technical Report TR-5364-3 Revision 0~~2-1 rs-TELEDYNE ENQINEERlNQ SERV(CES

2.0 CONCLUSION

S The analysis per formed by TES on the Pressurizer Safety/Relief Valve Discharge Piping System with the Safety Valve loop seal drained, indicates that all criteri a of NRC NUREG-0737, Item II.D.1 are met, with the foll owing qualifications:

1)Valve accelerations due to the SV transient shock condition for valves SV-45A, SV-45B and SV-45C exceed the vertical allowable of 2g's (Reference 14).The accelerations exceed the allowable by less than 1g and, therefore, it is TES's opinion that these valve accelerations are acceptable.

However, setting the criteria of acceptance of these accelerations is out of the TES work scope and is, therefore, the responsibility of others.2)The supports listed below exceed the loads given on the-As-Built l support drawings (see Section 6.2).These support loads, while exceeding.

the previous loads, do so in most cases by a small percentage.

However, acceptance of these loads is out of the TES work scope and is the responsibility of others.1-GRC-R-585 1-GRC-R-589 1-GRC-R-591 1-GRC-R-601 1-GRC-S-608 1-GRC-R-613 1-GRC-S-614

,1-GRC-R-616

Technical Report TR-5364-3 Revision 0 2-2<<TELEDYNE-ENQINEERINQ SERVlCES This report documents that the safety/relief valve discharge piping for.Unit 1 is acceptable for emergency conditions assuming drained loop seals.TES Technical Report TR-5364-1, Revision 0 (Reference 2), which is based on the as-built condition, documents the acceptability of the system for normal and upset conditions.

Draining the loop seals will not affect the normal and upset conditions.

The purpose of the loop seals was to protect the safety valves from leaking by keeping free hydrogen and high temperatures away from the valve seats.It should be noted that while draining the loop seals relieves the overwhelming stress on the discharge system,'ee TES Technical Report TR-5364-1, Revision 0 (Reference 2), it also leaves the valve seats unprotected and, therefore, susceptible to leaking.While it is beyond the responsibility of TES, this~~~~~~~~~condition can result in serious consequences and should be investigated.

Support load su@vary sheets have been included in this report for all supports and supercede the loads reported in TR-5364-1.

Technical Report TR-5364-3 Revision 0~~3-1-rs-TELEDYNE ENGlNEERlNQ SERVlCES I'.0 SYSTEM DESCRIPTION/DISCUSSION The Pressurizer Safety/Relief Valve Discharge Piping System consists of all of the piping from the pressurizer nozzles, down to the sparger in the quench tank.This information is depicted on-TES drawing E-5763, Revision 3, generated from AEP drawings 1-GRC-6, sheets 1, 2, 3, and 4;1-GRC-7;1-GRC-8;1-GRC-9;1-5435-8;1-RC-6, sheets 1, 2, 3 and 4;1-RC-7;1-RC-8;and 1-RC-9.The"Discharge" piping constitutes a very large system resulting in a large computer model.The size and geometrical complexity, which is due mainly to the sweeping curves around the pressurizer, complicates the modification effort in addition to causing longer run times..Modification of this complex system, to attempt to secure satisfactory

~~~~~~"Safety Valve Discharge" results, is limited to draining the SV loop seals.Heating the loop seals is not a viable"fix" because of the size of, the loops.These long loops contain sufficient quantity of water such that on SV Discharge, the water'eal does not"flash" completely enough to reduce the very high loads caused by the water slug.Modification to the support system is also a poor option because of the very limited space in the annulus around the pressurizer, which makes construction very difficult.

Technical Report TR-5364-3 Revision 0 4.0 THERMAL FLUIDS ANALYSIS 4-1><-TELEDYNE ENQINEERINQ SERVICES 4.1 Introduction The following thermodynamic fluid analysis determines the fluid forces which act on the pressurizer safety valve discharge piping of the American Electric Power Service Corporation (AEPSC)Donald C.Cook Nuclear Power Plant, Unit 1.These forces are generated by the sudden opening of the pressurizer safety valves during one of the pressurizer transients described in the AEP letter of November 29, 1982 to TES (Reference 1).These fluid forces and the resulting loads and stresses on the piping system became of increased concern as a result of the incident at Three Mile Island.'Following this incident, the NRC issued NUREG 0578 and NUREG 0737, which required that each utility determine the effect of safety/relief valve operation upon the valve and the discharge piping.An elaborate program involving both testing and analysis was established under the general management of the Electric Power Research Institute (EPRI).The EPRI program included intensive testing of safety and relief valves as well as a full scale safety valve test facility, built at Combustion Engineering in Connecticut.

Simultaneously, an analytical program was initiated to choose and test a computer program which would predict the fluid forces;REL'AP5 MOD1 was chosen.RELAP5 MODl is the latest in the family of RELAP programs developed at the Idaho National Engineering Laboratory.

The D.C.Cook Units 1 and 2 pressurizer safety valves have"Cold Loop Seals".A"Cold Loop Seal" is a subcooled slug of water trapped between the safety valve seat and the pressurizer nozzle by a loop of piping.The function of this slug of water is to prevent the safety valve from leaking, this is.accomplished by keeping free hydrogen away from, and maintaining reduced.temperatures at the valve seat.While the loop seal provides a benefit, it also~~~~~~has a serious drawback.When the safety valve opens, the loop seal is, shot through the discharge piping with tremendous force.In TES Technical Report TR-5364-1, TES performed a fluid analysis to determine the magnitude of the loads applied

Technical Report TR-5364-3 Revision 0 4-2 r<-TELEDYNE ENQINEERINQ SERVICES~~~to the discharge piping by the propulsion of the cold loop seal.These loads were calculated to be greater than 100,000 lbf for a single safety valve discharge.

The simultaneous discharge of the pressurizer's three safety valves with loop seals could result in loads of over 300,000 lbs.As explained in TR-5364-1, TES also performed a sensitivity study to determine if raising the loop seal temperature (by electrical trace heating)would reduce the loads.Increasing the loop seal temperature did lower the loads.somewhat, however, a significant reduction was not obtained.It was then suggested that the loop seals should be drained so that when the safety valves operated, they would discharge steam only.This report presents the analysis for the steam discharge that was performed for the Unit 1 pressurizer safety valves..The maximum fluid force calculated in this analysis is 24,000 lbf for simultaneous discharge of all three safety valves.It can be seen that draining the loop seals provides a significant force reduction.

In this analysis, as before, TES has used RELAP5 MOD1 version 2.11 as it is made available through Control Data Corp with a.post-processor, REPIPE version 3.10, which calculates the fluid forces.This version of RELAP5 MOD1 is identified by the following computer job control language at Control Data Corporation:

BEGIN, RELAP5;R5M2, INPUT=INPUTFILE, SCM=377000B The computer analysis procedure for the thermal analysis portion is included in Appendix A.RELAP5 calculates hydrodynamic data for control volumes in each segment of pipe.REPIPE then takes this data and defines two force time histories for each segment, one set for inlet junction forces and the other for outlet junction forces.A TES generated program, SAP2SAP, adds these force time histories.

Finally, one force-time history for each segment of axial, unbalanced.loads is analyzed structurally.

Technical Report TR-5364-3 Revision 0 4.2 RELAP Model 43 I<.TELEDYNE ENGlNEERIMQ SERVCEFi 4.2.1 The D.C.Cook pressurizer was modeled as a single time dependent volume with the following transient condition as specified by the AEPSC, November 29, 1982 letter to Mr.L.B.Semprucci, pages 1-7 (Reference 1):~Ef1 ft Pressure Time History (in the pressurizer) 2750 o-e2750 2750 2700 2700 Pressure (ps')2600 650 2600 2667 2550 o'2555 2500 0 2514 0.5 1.0 Time (Sec)These are the same safety valve pressure boundary conditions that were used in analyzing the quarter model cold loop seal case of TR-5364-1 (Reference 2).

Technical Report TR-5364-3 Revision 0~~s>-TELEDYNE ENGINEERING SERVICES 4.2.2 Safety valves were modeled as RELAP junctions emulating Crosby HB-BP-86 valves (Reference 3)with orifice areas of 0.01897 Ft2 and a valve opening time of 0.010 seconds.Valve orifice areas were calculated using the Crosby Valve and Gage Company Drawing No.H-51688, Revision A (Reference 3)provided by AEP, and RELAP (Run ID BAICDRO)implementing rated flows.Calculated values are included in Section 4.6 and Figure 4.6.1.4.2.3 Discharge piping was modeled from all safety and power operated relief valves to the quench tank.This discharge piping=included the following pipe sizes: 3 inch, 12 inch 4 inch, 6 inch 4 inch 3 inch, 6 inch SCH 40 SCH 40S SCH 120 SCH 160 Friction factors for long and short radius elbows and reducers were taken from technical paper 8410 by Crane (Reference 4).Calculations of these frictional losses are included in Appendix A.The discharge piping is defined in segments of straight sections from;elbow to elbow, valve to elbow, etc.4.2.4 The quench Tank was modeled in two parts, the sparger and the tank itself, using cylindrical volumes containing water and air.The quench tank volumes were taken from Westinghouse Dwg.No.110E272 (Reference 5).The sparger for D.C.Cook is a perforated pipe submerged in water within the quench tank as indicated in Figure 4.2.1.It is represented in RELAP as a pipe similarly submerged and of equal volume.

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Technical Report TR-5364-3 Revision 0 4-11 A TELEDYNE ENQINEERINQ SERVICES 4.3 RELAP Model Control Volumes The"Evaluation of RELAP5/MOD1 for Calculation of Safety/Relief Valve Discharge Piping Hydrodynamic Loads" report prepared by Intermountain Technologies Inc.(Reference 6)recommends using ten or more control volumes per bounded segment when modeling valve discharge piping for RELAP5, while avoiding significant control volume length differences to preserve pressure wave shapes.The ten control volume criteria recommended by ITI was adhered to by TES in all cases, except in piping arcs and in segments less than three feet in length.The D.C.Cook discharge piping is modeled using as few as one control volume per segment (pipe segments with lengths less than 0.5 feet)and up to thirty-two control volumes per segment.Arc modeling for Unit 1 is represented in Figure 4.3.1.All arcs for Unit 1 were modeled in RELAP as having no fluid losses.Essentially, RELAP alculates these as straight sections of pipe.REPIPE, however, distributes the calculated forces to pre-assigned node points matching the TES structural models.model wer e: Average control volume lengths used for the D.C.Cook RELAP Unit 1~Pi e Size Avera e C.V.Len th 3 inch SCH 160 6 inch SCH 160 4 inch SCH 40S 6 inch SCH 40S 12 inch SCH 40 3 inch SCH 40 4 inch SCH 120 0.4644 feet 0.5264 feet 0.4471 feet 0.8614 feet 0.8064 feet 0.4744 feet 0.5056 feet The schematic of the discharge system modeled in RELAP for the SV nit 1 model is represented in Figure 4.7.1.

Technical Report TR-5364-3 evision 0 4-12 A TELEDYNE ENQINEERINQ SERVICES quench Tank modeling was achieved using twenty control volumes and twenty junctions.

Eighteen volumes comprise the sparger model while the remaining two are single volumes modeling the water and air spaces of the quench tank.The water and air volumes as determined from Westinghouse Dwg.No.110E272 (Reference 5)were input to RELAP to insure proper quenching capacity.Eighteen control volumes forming the sparger are initially 88K full of water representing a submerged pipe.The discharge holes were modeled as a single hole with an area of.7773 ft.2 at a point on the sparger where the sum of the small hole areas equal the 12 inch schedule 40 discharge area.Finally, the tank rupture disk is modeled as a pressure actuated valve placed on the air volume and set to blow out at 100 psig discharging to atmosphere.

~~~igure 4.2.1 represents the D.C.Cook Unit 1 and 2 quench Tanks.Pressure in the ir volume of the quench tank never exceeded 30 psia during the Unit 1 SV transient case of steam and drained loop seals RELAP5 run for 0.5 seconds.

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O.BY++DATE~~I~D>LT'PORV St=c7-i aM BRAHaRES~7'E'E'5 SHEET NO.7-OF PROJ.NO." FIGURE 4.3.1-6 70?Sg~Lg uA A<'>~'4~/~Aa Sea nues E/g/A+///9 S/3 gN6L~N QPANC//5///g 5 lg.5'&L VL)Log Sub'.TUN Joe 5HG L~N~4o3 gO/ZB gonzo/('uesr~su~g go/SN&LJLPM 406 ShlC,t 2 V~@I go7+o~uu4"@RANCH~5 o8 5N6~uA/4ogo/(gr~nrse w)

Techni cal Report TR-5364-3 evision 0 4-19 A TELEDYNE ENQINEERINQ SERVICES 4.4 Valve Flow Rate Calculation

'The following values were used in valve modeling considerations:

Valve T e TES Flow2 Max Rating>Actual Rate Calculated For Steam Bore Area Opening LBM HR I 3'C Accum.~IN2 Time Sec Crosb 452,393 afety Relief Val ve 435,000 3.6 in2 0.010 (Ref.15)The maximum rating for steam at 3X accumulation value is from the Crosby Valve~~and Gage Safety Valve Drawing No.H-51688, Revision A (Reference 3).2 Flow rate at 2500 psig plus 3X accumulation.

Technical Report TR-5634-3 evision 0 4-20 r<TELEDYNE ENGINEERING SERVICES The valve flow rates normally used by TES in the RELAP analysis of the SVs would be a 15K increase in the ASME rated flow: 1(C to consider the ASME underating of the theoretical flow and 5X to cover tolerances.

However, in this particular case, Westinghouse has provided AEPSC with a sumary of the EPRI flow rate tests of the Crosby 6M6 safety valve (Reference 7).Also, see Figure 4.4.1-4.A comparison was made in an effort to achieve a more realistic flow rate.The flow rate chosen which most closely bounds the test data is the following ASME flow rate.All calculations are included as Figure 4.4.1.WT=51.5 AP ASME rated flow: WR=51.5A (1.03P+14.7)(.9)(.966)C where: (Ref.8)WT=theoretical flow WR=rated flow coefficients:

1.03-applies 3X accumulation 0.966-valve flow coefficient 0.9-represents theoretical flow rate reduced lOX to equal ASME rating C=1.0771 calculated on Figure 4.4.1-2 following.

TR-5364-3)<TELEDYNE ENQINEERINQ SERVICES Revision 0 4-21 DATE+~88 HKD.BY~~DATE~~gosS)6H vAa vE MODEL.+LOW AIRED CAg.C'>ger/gjQS SHEET NO.OF FIGURE 4.4.1-1&p: A~E ZecZZ-A/.8-FFZ<.

g$IIJ8 yyg42 (/ye~)g.C/OS+)pygmy ROD+<: Il8-BP 8b VALW NANT)CT gp g~+ag/~A Z l4/FS7IIJ/Cv//048'ZPLY1 l4'CAP-VO<O5 4$'VIEPV OI'RESSc4 IZER SAFETY Y8L IIE PEEFOR NA A'CE AS OBSERVES e/TIE'PR7 SACHET)An)9/ELIZA VALVE 7ESr P@OC<rQA'.7Es~zLEcov ur/r/I Mg.sAvr zEQL/L7 A'CH CRos8>$8za z-0-8 CHQS8 Y 6Ng VAL VE PROPERTIES MlInfV FAC7-VEEN 7 V/'Z'v/gDZL A/O S/l)w'/Af8 h/O.: CZOS8)VALVE'eAC<E.

aO.:SPR/IJe LO~Xea SAeEr>VALVE://g 8p gg dM$: F/-51/+ji'PEV.A gO4Z'IBA (4): S.64k Z n DESI&jg SFl PAESS.(P~g~): g$gy Pg/)8/SClldPGZ

~~Qg: O.AW CALCglli 7/OAJ o<MAÃFlDAJ A'7F (~<)ruE.FOz.z,OWlnJC~

AmuwP7Ionls An/CO~ias-AATIWLs AR'a ptABE-IA/5'E 7$A P/lhlJC<Cdg FOP 8'ZlAPD MOSS L.1'TIIZ FolLouud6 CALCVLATINLs A cMS7AIJT SEr PNwu~'E g~Eo ro cALcvLA7E A Flow)ANFA Foz~eF RzuIpw AoszL AA)s Z)O~S'fOr O'ZcEssAR/L Y 8'Ec KESs&p-f REWgg/Zrg IA)P&C4MJTIC45 g 7/I&'E ARE VAR/OVAL Ega r/OA)$4 IJ8 EA pEPIME IJ78/-IESULYS YIELDIAJ5 8/F/=PARFAIT FLOuJ RATEs.ALL O/=7IIESE A'E PRESENTED IAI 7PE PA'OCZZVnlC~

NSE';A~~ONEATr NC SZi ZCVu SUCFI 7'IIA7 I7 AJWX8 BF CONS&'ATIl/E'F COMA'ti'E8 H/ITII TEST TA 8l/7/7 4/OUL 0 ST/L L 8E'~FALI57 IC TR-5364-3 (>TELEDYNE ENQlNEERlNQ SERVlCES Revision 0 OATE~>-I~KD BY~MDATK~063 4-22 c/Qs'BY bed wA L vE EF~APS~OUI F~Oa/fed CA/-C./Illri045 SHEET NO.OF s FIGURE 4.4.1-2 VARiOUS Fi Ou)PA7ES FOX SNAB CA'CMV VALVE PEON DirFZEEiJ7 SO~RcG zoo~pro.ay usoJo spy,,~~)X/.a~A,(s os.~+A.t)e~'Vv'/IE'RE Ag=9 6I/O sn'~r-4I/85 pug A',-0 gab Z.Fled 8'A7E 8)MIAN Egg~)~g.g>,g<(g.pg p.+gI, g)g Pg y)<AC70e g.P rAdrS e)VO.ACCOddr AAOVWACmÃII/y 7ÃlZRZIJ(ZS (Astro: rcooueArz~woe ohio zqu)ou~)=40 Ppb/h/s.Fcou)88'rE'y Me/6 ops.ca~)=5<z~Ao(4o9p

~f4.F)(o.~)

//FRF K'4.o btlls Isr/IE vAcur pIEszdroo wJ badoew&(Iron).a)=49O'CBB.

~"lu mp~485000 IbA~)4.PLOW PIl7E'Y USe)Cc E@N.m)>-Wl.S~Ag (X.OS P+<I/I')<~P~(7I/IS IS'I/F ISA//tS/4E S QAJ.ZITI(OUI gAiVVFACTP/I@I&

7VCEjQb'~g

)0.//06 Pss r-f000 c=/0"C'f If-X41Z/zpg-ZO64)~-SOS NSV/h G.+/O&A'A7E 8)VSIIJG Zgnr Cu,)~=~V.SA,(V.OZP,+II/.g]C,.W.O.

y C=4 OVVH PIAxwvM 7E57Ez Fl@LE/Are'/zp.@g

~Cu)~=//III/POP 4/

4 TR-5364-3~)<TELEDYNE ENQINEERINQ SERVICES Revision 0 4-23 DATE O KD.BY~DATE~~cl'O~Y'e&v c.va-YS'LA/5 pfOSzi a.ou 8A'EA C/ICVMri045 SHEET NO.~OF~PROJ.NO.~ZAN I FIGURE 4.4.1=3 I/)ZlAP PPPBEL FaA'HE bbfd CA'OSS)LIJO'u=~i54893//8AM>Oe AaueP77OnJ X 7 PASZ 4.ug=As'93/h/pv=415.40 lh/~~PHIAL&i IIE'OMPV7EI A VAf 882 CS A vw~vw wucL OPEN Ma<iu 7'~N 8AzCngg P.PdZZ P~FLO~A'A7W Q Hd%OPE'eggy 412.9l/5I~WLOW PAra@9O l~oPEein)c<=tSa.o</III~EEi-APW FLOE A)PEA uwlcH><<PS Mg=fZs-d6 IS CAL CO'Zii/The 8Y e/7F4P'OZ.A7IO~

pa~y y<xsw vz499 438.ot-fIX 9'9'0 gZSa3 kLOcV

Technical Report TR-5364-3 Revision 0 4-24 FIGURE 4.4.1-4.~TELIEIÃbK MSSN SRfCB)600 FIGURE 3-5 STEAN OISCHARGE CYCLE (STABLE)CROSBY 6M6 500 400 30 O B 200 10-Qxc~~,'~~~gsgu&ie-KR

~r V4<Vd~~Po~~H V<~,)pe ogggiBVB~gh/W+CO~Z~iEC sic VE W~r a~o6 hlC+P-)yyo$'<~yN~~d gS~W/~re u"000 2100 ID A g7~th 41 Ol~to t4 Ol Ql W Cll 2200 2300 2-"00 Tank Pressure (psia)'5CC 2500 2700 Techni cal Report TR;5364-3'sion 0 4-25 A TElEDYNE ENQtNEERlNQ SERVtCES 4.5 RELAP Plots The following plots represent RELAP mass flows, pressures and qualities at various points along the discharge piping.The ordinate axis may not always be correct;many times multipliers will be off (CDC is aware of this problem in RELAP).However, the plots do depict trends accurately and are calculated and reported in RELAP every 0.001 seconds.Correct peaks and times at which they occur are listed with each trace.A RELAP volume schematic precedes the plot set for the transient steam case.

echnical Report TR-5364-3 Revision 0 A TELEDYNE ENQINEERINQ SERVlCES 4-26 DATE~BY CHOATE~+A Zl gP~oDEL Sch&YHTZC uuZ'r g f44'V Gt war N~SHEET NO.OF.3 FIGURE 4.5.1-1 gg(ol ygig o@pe.5oo o qo 3IO g((O IDIO g C)P I gO

A TELEDYN: E,NC (N=ENlwao wva~~Technical Report TR-5364-3 4-27 OAT E d2~~~Z BYTES~~DATE~5 rFELAP/YODEL 9 CgZ/4AVZ'C~8'rm 4WC5 Jo$0I Og SHEET NO.~~OF~Soaol FIGURE 4.5.1-2 AJA FM yowl~,o0@gol oooo v~So~o IO oooo(logos pi/A<oC+o oF I Sinai'/pool~(0)g8 gin9 Qoo'.gIIW gilgt PotS~soy Technica>Rgp~<L++<QNQg+tNQ Spp+CP$TR-5364-3 Revision 0 Q j,...OAT I;~'~~'~~.BY~DRTE~~~5 8 EzsP a~~ozL zcgzwN'7~C.

~~~577PEtl&(l2i~SHCET NO..~OV.FIGURE 4.5.1-3 sa>~Qi11$@$2'!u5C'iiry 8tit g 8@gal sicily'npg, g](BE st3ol CD Xl CD (I 0>~Ol X CII CAI M 0 AO I OP CD Kl CD'o O f+g Ad 33 fCc LS LS TlNE tSECl

~~

CS 8)Q y3I.I4 d,u58 ILS.L$TltC lKCl CV U D~-I m m Pa KlWW CD W lD C I 0 Vl K GO W Wo 0 WO I C)xl (D a O PI Xl ITl Q 0)-fll 0 , m M Ysl CD Kl Cb C I 0 Ql M Vl CAN~Mo 0 AO I AP Cl CD O S/m.zy o A'>O O 00 A1 Aa A'5 TltK tSEC)

Kl M W Xl 6)(I 0 Vl K M Ca)%Me+0 WO I tD A)CI O C+/7~~q.g~o.WP A1 LS Tie (SEC)Oe4 AS F H'4 I xt M w CD Xl Al (I O Ql X M CA%~Wo 0 WO l C)tD a O.C 3/96/ll ggg, g~a, A8~O g7 X C Cl o D a.a L'5 TltK lSECl CD M CD (I 0~'Vl&III Ao 0 WO I CD Xl CD a O 3.yg.jygg n.ZZg~CS IIt 0 00-~8~g o.d'28'La 0.3 TlNC lKCl Pl Sm Q O (D lD Rl fD C I 0~~Vl 3 tA~r~~0 WO I C)A)O C+V'P Wgz.tg g 4.4~k LO a.a TitK lSECl U O l m C>>C 0

Gl M A)(I O Vl~tA GDM Ql~0 WO l Ql GO~C)lD'tl O II 3/7~4 O>>eW~W o.a M Tl%(KC)O O C4%ITl Q C 0 0) 0 Kl w w lD M lD I 0 Q1~lA 40%Q A 0 WA I GO~CO x7 lD a O/7~A 0 R Ill lSKCl OoS I lD X7 tD I O.Vl K V)Col M No~M 0 WO I Ql QJ C)Kl fb O/1 I~W O O at LS L3 TllC (SECS I I

/7 L2 L2 Tl%tSECl l SS LS 1.$TNE ISKC)

/~5 Q+d r Z g5 M L5 all%.[SEC)0.4 U O m m ITl%fTl Q CO m 0-l9 WCD C I 0~'Vl M M Cs)N JO+4 0 WO I Al tD ED O s 3 8/)7 O O L1 L$Tlirt lSECl Pa AIMS CD KI CD (I 0 CJl~CA Ca)N~o OI~o O WO I CO Zl CD O I rt O O La IL3 TllC fSEC) i J m-I-l (D WA)C I 0~.Vl 2 M~~o O WO I/7 jS jig ILS Owl INC (SEC)Ooi L5 O C7 m m Ps

Tl%tSEC) 0 CD M CD (I O Ql X GO D~We 0 WO I C)CD o C+Pa CD WCD I O" 0 Z Vl QJ+~o 0 WO I C)CD n O S C+O O aa LS TIKE tSECl CD W (D I 0~~CJl K CO Ca)N Me~M 0 WO I CA~ID lD CJ O gO-gC Zy 2 Q doe&~g 4<<O C7 zzs9.i~.oi~~TlNE (SKCl 0.4 lD R7 CD C I 0'2 CA N Q Ao 0 WO I Ql Z7 tD u O~s Ct'k zW.</~.~~>I Vl AQ~eO CI 00 z g5'g g pO.Or&~aa L5 Tl%(SEC)D+4 Pa 4 t ITl Xl Pl iK Q U)ITI C 0 u~WJ~a:o%ee CD X7 CD (I O Ol$A GJK 0 wo I Qt I XI CD C I 1 Zygo Z Q CD.d83~O O Ll L'I lilC tSECl Ca CD WtD 1 O~CA&Vl 4J M O WO 1 QP~Xl CD o O s Ca

ÃIMW CD~ID (-I O Vl Z CA M~Ch~O WO I (pJ CD'I CII I O I Ct'7)Pl cZ:Q Pl o a La LS TllC (KCl 0.5 T

III (Me Vl O R7 CD I O C17~GO V~mo W O I Ql II)o O/7 zN air.Vga Q~a gg A CU;-f7'&O d ILO L3 L$TlNE tSECl Oo5 C7 U m 5m I iQ'-(n ITI K;"~%2%: jpi7;Ap.

KIMW CD R7 CD I 0~~CSl M Col N 0 WO I CV C)CD O~go,Z5+O.ZS@~o.a L3 Ill tSECl CD M CD (I O Vl F Vl Ca)N Wo 0 Ah I OP C7 CD Cl O 3 LR L$?1%tSEC)LS ED WA)I 0~'Ul~GD N Mo~Wo 0 WO I C)lD O s QO e4 g/7.~~,~u.988~I Vl H~~R-'h.C7 O LR L$ENC (SEC)L4 L5 C7 C7 m m W

CD Xl CD I 0 Vl M Vl GO N 0 WO I Ql CsP~lD-X7 CD u O S S'PR 8 D R gd o d OO O.a 05 TNC tSKCl Tl%lSECl o O m m Pa 0.$TllC lSEC)O O m m SS Ll.Ll LS TINE tSECJ a.c CD Xl CD (I Cl Ol K Vl 43K~a+Wo 0 WCl I Ql CO Kl CD'n O 3!7,~~.gag 0,9t/~Cl Q~CS gd R d ILO.La LS TltC lSECl U O m fll 0

Technical Report TR-5364-3 ision 0 4-63 A TELEDYNE ENGIMEERlNQ SERVlCES 4.6 Force Time Histor Plots The following are force versus time plots for each pipe segment at a node point described by the structural model.A drawing indicating force placement precedes the set.Since the force time histories were plotted after balancing and merging(i.e.

SAP2SAP and MERGE), each plot is unbalanced force versus time from 0.0 to 0.5 seconds.Unit 1 has 67 pipe segments and correspondingly 67 force'ime histories.

TR-5364-3 A TELEDYNE ENQIN=ERIMQ SERVlCES Revision 0 BY DATE~CH Y M~DATK+~8 FIGURE 4.6.1-1 4-64~RV~MdrCli A~P=Pd~AV S~a~"7Wc,~~80 SHEET NO~OF S""RVICES,,,ppTELEDYN=

ENGIN=ERIMQ TR-5364-3 Revisio 0 D ATE+~+8Z OATEN/~~BY N Tif 0=~Vair'&OP~5 P>~~Ž~CHK HgJng gg~CS 2 4 4 Zg FIGURE 4.6.1-2 SHEET NO..~OF 7 PROD.NO.~+'~~s~ro rsz~r8I s Qzg,~u.~(y 0o C3~o iQss@Qa)Qsz Qso~f8(rsz so" Xc 2b~o/(.g~(zz (res

.Technical ReP~~TF~DYN Revision 0 4-66 By/..DATE~~.cH><<~eaTE~<>>g/H>>a~QTR VCPVAQ~~~dg~+4<<h'MUD)+.r":IU (Ih)~Q SHEET NO'F FIGURE 4.6.1-3Qss Qs(.QI QB QSQ i/Qis Qac

Technical Report TR-5364-3 Revision 0 4-67 IIH@51NG sERYIGEs SAP2SAP VERiFICATION 5364.6-JUL-83.DC COOK-UNIT) r SV NODIFICATION TINE/FORCE TABLE 1, MAGNITUDE AT NODE POINT 620 Technical Report TR-5364-3 Revision 0 4-68~NBNN~~o sERv~cEs SAP2SAP--VER IF I CAT ION 5364 6-JUL-83 DC COOK-UNI Tl e SV NODIFI CATION TINE/FORCE

'TABLE 2e NAGNITUDE AT NODE POINT tO Ol 00 03 O0 LLI~CD IK C)CIQ l 00 e.28 TINE 0.43 0.5C eo 00 LD 00 I 08 I Technical Report TR-5364-3 Revision 0 4-69~SHRIVING sERvt SAP2SAP VERIFICATION 5364 6-JUL-83 DC COOK-UNITtt SV NODIFICATION TINE/FORCE TABLE 3e MAGNITUDE AT NODE POINT CES CO CO 00 o0 T I NE 0.36 0.43 0.5(

Technical Report TR-5364-3 Revision 0 4-70 NfmtIINIIING SERYICES 6-JUL."83 SAP2SAP VERIFICATION 5364 DC COOK"UNITle SV NODIFICATION TINE/FORCE TA8LE 4~NAGNI TUDE AT NODE POINT 536 IO a Ol OJ EO CO a lO LO CD lY a U tO'a 0 lO C9 l 00 0.6 0.5(a CFl Od L!7 l

,e Technical Report TR-5364-3 Revision 0 4-71 lllBIIINI!NG SERV!CES 6-JUL-83 SAP2SAP VER IF I CAT ION 5364 DC COOK-UNI T1 e SV NODIF I CAT IOH TINE/FORCE TABLE Si MAGNITUDE AT NODE POINT.o lh CD Of o CD O:~Of C3 lK o 4 t OD~2 O.SD Ol CO o tO Technical Report TR-5364-3 Revision 0 4-72 NBNN1NG sERYIGEs 6-JUL"83 SAP2SAP VER IF I CAT I ON 5364 DC COOK-UNI Tl e SV MODIFICATION TINE/FORCE TABLE 6t MAGNITUDE AT NOOK POINT 550'I r Ol tO CO Ol O!O QJ~CD IK C)Q (D I 0.0 0.5 CV ED lO tD t CO tO C7 t LO tO C5 t Technical Report TR-5364-3 Revision 0 4-73 IIHNSI HG SERVICES SAP2SAP VERIFICATION 5364 6-JUL-83 DC COOK-UNIT) e SV NODIFICATION TINK/FORCE TABLE 7e MAGNITUDE AT NODE POINT 555 QJ CO~I Cl Q h LO CV Cg I I E Dh CO CII I Ol CO O I IA Ch CO I Technical Report TR-5364-3 Revision 0 N)88fINGSERVICES SAP2SAP VER I F I CAT I ON 5364 6-'UL-83 DC COOK" UNI T1 t SV NODIFI CAT ION TINE/FORCE TABLE 8.MAGNITUDE AT NODE POINT 560 CO o Cl OlI F 0 0.50 lK=-C)OJ CO CO Ol I Technical Report TR-5364-3 Revision 0 4-75 tk%5lHG sERYIGKs SAP2SAP VERIFICATION 5364 6-JUL-83 DC COOK-UNIT l I SV NODIFICATION TINE/FORCE TABLE 9~NAGNI TUDE AT NODE POINT EO OI OLLJ~IK Cl U CO A Ol o CV 00 07 0'4 0.9 T I NE 0.36 0 43 Technical Report TR-5364-3 Revision 0 4-76~59@liNs seRvices SAP2SAP VERIFICATION 5364 6-SUL-83 DC COOK-UNIT)

I SV NODIFICATION T INE/f ORCE TABLE)0~HACNI TUDE AT NODE POINT CV Ol tO 08~++O Cb o~C7 0 Cl LO CQ@00 0.0.E.3S, 0.43 CV lO

'I t.1 Technical Report TR-5364-3 Revision 0 4-77 3lhfNNIRG SERVICES SAP2SAP VERIFICATION 5360 s-ou}.-ss DC COOK-UNI T l,'V NODIF I CAT ION TINE/FORCE TABLE 1 1.NAGNI TUDE AT NODE POINT 00 0 0.43 D.50 Technical Report TR-5364-3 Revision 0 4-78 tl&fHltlNG SERVICES SAP2SAP VERIFICATION 5364 6-JUL-83 DC GOOK UN I T 1~SV NOD I F I CAT I ON TINE/FORCE TABLE 12'AGNITUDE AT NODE POINT 360 CO OJ C7 Cl CI~@I IX C)U C5 Yl 0 00 0.0~TI E.36 0.43 0.50 Technical Report TR-5364-3 Revision 0 4-79DHNNI NG SERV I CES SAP2SAP VERiFICATION 5364 6-JUL-83 DC COOK-UNI T1 e SV NODIF I CATION T I NE/FORCE TABLE 1 3 r NAGNI TUOE AT t tODE POINT 355 a CO lO CO~t9 CD VS I 00 OF 0.0.E 0.43 0.50 M ED CO CO I Technical Report TR-5364-3 Revision 0 4-80 NBNIING SERVICES 6-JUL-83 SAP2SAP VERIFICATION 5364 DC COOK" UHI T)e SV NOD IF I CAT I OH TINE/FORCE TABLE)4 e NAGH I T UDE AT HODE POINT, 350 LO o CA CO OJ M tO CD C)Q Ol LO LO I 00 0 0 0.89 Technical Report TR-5364-3 Revision 0 4-81 8388)ING SERVICES 6-JUL"83 SAP2SAP VERIF ICATION 5364 DC COOK-UNI T f.SV NODIF I CAT ION TINE/FORCE TABLE f 5e NAGNI TUDE AT NODE POINT 00 0 0 Technical Report TR-5364-3 Revi,sion 0 4-82 II ESBBIIING SERVICES 6-JUL-83 SAP2SAP VER IF I CAT I OH 5364 DC COOK-UNITl, SV NODIFICATION TINE/FORCE TABLE l 6e NAGNI TUDE AT NODE POINT a CD CD lY C)~e'l lO O W 00 0 I OF 0~0.43 CO Cl l Technical Report TR-5364-3 Revision 0 4-83.NIENNING SERVICES 6-JUL"'83 SAP2SAP VERIF I CAT ION 5364 DC COOK-.UNIT) e SV NODIFICATION TIRE/FORCE TABLE)Te MAGNITUDE PT NODE POINT h OJ Y7~~+~07~lO a 00 OF'.T 0.3 0.

Technical Report TR-5364-3 Revision 0 4-84 N~S(NING SERVICES SAP2SAP VERIFICATION 5364 DC COOK UNIT1~SV NODIFICATION T I ME/FORCE TABLE 1 8~NAGNI TUDE AT NODE POINT h lO Ol o l9 O CO CV QJ 00 0 C)I O O CV I C)CO A CV I 00 0 3 0.

Technical Report TR-5364-3 Revision 0 4-85 NcfNNING sERYIcfs SAP2SAP VERIFICATION 5364 DC COOK-UNI T1 r SV NOD IF I CAT ION TINE/FORCE TABLE 1Se MAGNITUDE AT NODE POINT 310 0.0 3 0.50 Technical Report TR-5364-3 Revision 0 4-86@~SlNIlNG sERYIGEs SAP2SAP VERIFICATION 5364 6-JUL-83 DC COOK UN I T)~SV NODIF I CAT ION TINE/FORCE TA8LE 20.NAGN I TUDE AT NODE POINT 300.0 0~0 3 0.50~PI I O CV D I V7 Yl l Technical Report TR-5364-3 Revision 0 4-87 N)B(SING SERVICES SAP2SAP VERIF I CAT ION 5364 6" JUL-83 DC COOK-VNI T 1.SV MODIF I CAT I ON TIME/FORCE TABLE 21 r MAGNI TVDE AT NODE POINT tO CO o LLIcl~I lK C)Q CO I a 04 I 00 TXl1E 0.1 0.2S 0.36 ED I Technical Report TR-5364-3 Revision 0 4-88 BtLNEN t NG sERY1GEs SAP2SAP VERIFICATION 5364 6-JUL-83 DC COOK-UNI T)e SV NODIF I CAT ION TINE/FORCE TABLE 22.MAGNITUDE AT NODE POINT QO 00~Ci O I+OJ&ca lY~04 TINE 0.1 0.29 0.36 D I Ol Cl tO Technical Report TR-5364-3 , Revision 0 4-89 kkfQNING SERVICES 6"JUL-83 SAP2SAP VERIFICATION 5364 DC COOK-UNI T1 r SV NOD IF I CAT I ON TINE/FORCE TABLE 23~NAGNI TUDE AT NODE POINT 130 Ol o h C7 CO~oo O~a i TINE 0.)0.29 0.36 0.43 0.50 Technical Report TR-5364-3 Revision 0.4-90NHII811NG SERVICES 6-JUL-83 SAP2SAP VERIFICATION 5364 DC COOK-UNIT l.SV t10DIF ICATION TINE'/FORCE TABLE 24.NAGNITUDE AT NODE POINT l260~CV~Cl 9 I 00 TINE 0.1 0.29 0.36 0.43 0.$0 Ocv O CV Technical Repor t TR-5364-3 Revision 0 4-91 BANNING SERVICES 6-JUL-83 SAP2SAP VERIFI CAT ION 5364 DC COOK UN I T 1~SV NODI F I CAT I OH TINE/FORCE TABLE 25.NAGHI TUDE AT NODE POINT)20 a CA CO CD LO a0 00o Ol O~6 l 0 4 TINE 0.21 0.29 0.36 0.50 UJ Do CO CD a CO h C5 LIl CV I Technical Report TR-5364-3 Revision 0 4-92 5LfIIN[ING SERV1CES 6-JUL-83 SAP2SAP VERIFICATION 5364 DC COOK-VNI T 1 v SV NODIF I CAT ION TINE/FORGE TABLE 26r MAGNITUDE AT NODE POINT~~I 0!O tO 1 00 0 0.)4 TINE 0.1 0.29 0.36'.43 0.50 CO CI LO~co O I&a U Cl A 1 CO CO CO I Technical Report TR-5364-3 Revision 0 4-93 N)SNI'tNG sERYIcEs SAP2SAP VERIFICATION 5364 6-JU'83 DC COOK" UHI T i.SV NOOIF I CAT ION TINE/FORCE TABLE 2T.NAGNITUDE AT NODE POI'HT O 0 00 M C7 f t9 D D 0.0.)4 T I NE 0.29 0.36 0.43 00 o C5 OJ I Technical Report TR-5364-3 Revision 0 4-94~lILflINltING sERYIcEs SAP2SAP VERIFICATION 5364 6-JUL-83 DC COOK-UNIT l e SV NODIFI CATION TINE/FORCE TABLE 28.NAGHI TUDE AT NODE POINT 0 00 l/)ED I 0.0T 0.14 T I NE 0 21 0.2 0.36 0.43'O~I Technical Report TR-5364-3 Revision 0 4-95 LIILNNLING SERVICES 6-JUL-83 SAP2SAP VERIFICATION 5364 DC COOK-UNI T1 e SV HODI F I CAT ION TINE/FORCE TABLE-29.MAGNITUDE AT NODE POINT 00 O.OF 0.14 0.36 Technical Report TR-5364-3 Revision 0 4-96 8)flIt I I N G SERVICES 6-JUL-83 SAP2SAP VERIF I CAT I ON 5364 DC COOK-UNI T).SV NODIF I CAT ION TINE/FORCE TABLE 30.MAGNITUDE AT NODE POINT 102 0 00 lO Cl Ol I O.OT O.l4 T I NE.2)0.0.43 0.50QJ CO~CO C)~CO U 7 Ol CO I Technical Report TR-5364-3 Revision 0 4-97 O NBNIItiG SERVICES SAP2SAP VERIFICATION 5364 6-'JUL" 83 DC COOK"UNIT 1 e SV NODIFICAT IOH TINE/FORCE TABLE 31.MAGNITUDE AT Nf'DE POINT.0 O.OF 0.)4 T I HE'.ll 0.9 0.36 0.43 O LO I C)OJ 04 CO I Technical Report TR-5364-3 Revision 0 4-98 lkfliNk't NG sERYI GEs SAP2SAP VERIFICATION 536'4 6-JUL" 83 DC COOK-UHITI

~SV NODIFICATIOH TINE/FORCE TABLE 32e MAGNITUDE AT NODE POINT 00 0.07 0)4 T I NE 02)0 9 0.36 0.43 Technical Report TR-5364-3 Revision 0 4-99 SH(NING SERVICES SAP2SAP VERIFICATION 5364 6-JUL-85 DC COOK-UHI T i.SV NOD I F I CAT I OH TINE/FORCE TABLE 33 e NAGHI TUDE AT NODE POI HT O.OT 0.)4 0.T IVE 0 9 t'-4~0.50 tO ill I CD O 0~h CD~e 4-7 C)LO Ok Technical Report TR-5364-3 Revision 0 4-100 NL 8(I I N G SERV 1 GES 6-JUL-83 SAP2SAP VERIFICATION 5364 DC GOOK"UNI T1.SV NODIF I CAT ION T I HE'/FORCE TABLE 34~NAGNI TUDE AT NODE POINT 184 IO CO PO o CO QJM~I IK CD Q CO lO'CO I O a OJ I 00~7 T I NE 0-1 0.29 0.36 0.50 CO I V r lt'c 1~c j"c cc yclIlcc))c c 8 P 1 11 o gc'-c c 1l cy I 1 1 ll c h H 1 lc:~I a.1' Technical Report TR-5364-3 Revision 0 4-101 kkSkIIRG SERVICES SAP2SAP VERIFICATION 5364 6-JUL-83 DC COOK-UNITt e SV MODIFICATION TIME/FORCE TABLE 35~MAGNITUDE AT NODE POINT t82 00 T INE 0.1 0.29 0.36 0.45 0.50 f 0 Technical Report TR-5364-3 Revision 0 4-102 III4BNI ING SERVICES SAP2SAP VERIF I CAT ION 5364 DC COOK-UHlTl

~SV MODIFICATION TIME/FORCE TABLE 36e MAGNI TUDE AT NODE POINT hs.CAYl h O CO 00 TINE 0.2)0-29~0.36 0.43 Technical Report TR-5364-3 Revision 0 4-103 I!IBII81I NS SERVICES 6"SUL-83 SAP2SAP VER IF'I CAT ION 5364 DC COOK-uNITi.

SV MODIFICATION TIME/FORCE TABLE 3Te MAGNITUDE AT NODE POINT 1T6 CO Ol~7 0.21 0.29 0.36 0.45 0.50 LLtcu Mcu~CO~@I h I Technical Repor t TR-5364-3 Revision 0 4-104 lN)IIIIIING SERYICES 6" JUL-83 SAP2SAP VERIF I CATION 5364 DC COOK UNIT 1 r SY HODIFI CATI"ON TINE/FORCE TABLE 38.MAGNITUDE AT NODE POINT Ol o Cl CO cO 00 0 4 T I NE 0.21 0'9 0.36 0.43 le IO I CD o CO h I Cll l/l Af Ol Technical Report TR-5364-3 Revision 0 4-105 k@SNIING SERVI CEG SAP2SAP VERIFICATION 5364 6-JUL" 83 DC COOK-UN I T/e SV NOD IF I CAT ION TIME/FORCE TABLE 39~NAGHI TUDE AT NODE POINT Cl 0)h CO lO I 00 O.l 4 TINE 0-'2'l'.29 0.36 0.43 lO o l~ca C)CL'D 0)I Ol Ok h I Technical Report TR-5364-3 Revision 0 4-106 84$lf51NS SERV1CES SAP2SAP VERIFICATION 5364 6-JUL" 83 DC COOK-UHI Tl e SV NODIFI CATION TINE/FORCE TABLE 40 e HAGN I 7 UDE AT NODE POINT')57 0 CD 0 Dl CV I 00 0.0.14 T IME 0 2'I 0.9 36 0.43 0 F 50 CO CO CCl CO I~I@~e a~@I Cl l/)CO l1l CV I CV Ol Y)Yl I CD O Technical Report TR-5364-3 Revision 0 4-107IIILS(NING SERVICES SAP2SAP VERIFICATION 5364 6'-SUL"83 DC COOK-UNIT1 e SV NODIFI CATION TINE/FORCE TABLE 41~MAGH I TUDE AT NODE POI HT 150 IA Y7 ED I 00 0.07 0.14 T INE.36 0.43 0.50 CO Ol lO I~C)M~~ED oP U 7 Technical Report TR-5364-3 Revision 0 4-108@LANSING SERVICES SAP2SAP VERIF I CAT ION 5364 6-JUL-83 DC COOK"UNITl.

SV MODIFICATION TIME/FORCE TABLE 42e MAGNITUDE AT NODE POINT 0 00 C)0 CV 0.07 O.l4 TINE.2]9+36 0-43 C9 lO LO I Cg CO o CD I Technical Report TR-5364-3 Revision 0 4-109 8)5(IIRG SERVICES 6"JUL"83 SAP2SAP VERIFICATION 5364 , DC COOK-UNITt e SV MODIFICATION TIME/FORCE TABLE 43.MAGNITUDE AT NODE POINT, 146 o IO lO 00 O.OT~0-14 T I ME 0.21.9.35'0.43 0.50 OJ a CII I CO 9 I~CI Lt I CII LO I LO CV IO h I IO If)O J Technical Report TR-5364-3 Revision 0 4-110 N)N/NING SERVICES SAP2SAP YERIF I CATION 5364 6-SUL-83 DC COOK-UNI T l e SY NODIFICATION TINE/FORCE TABLE 44'AGNI TUDE AT NODE POINT'44 0.07 0.14...TINE 0-21 29 0.36 0.43 O.SO Technical Report TR-5364-3 Revision 0 4-111%8/NING sERYIGEs'AP2SAP VERIFICATION 5364 6-JUL-83 DC COOK-UNIT 1 e SY'ODIFICATION TINE/FORCE TABLE, 45'AGNITUDE AT NODE POINT h Cl CV LLJ (CD IX C)Q Al I aa T I NE 0.1 0.29 0.43 0.50 t Y J V 1 I C, h I 1 ll'E I j 1 ff tl/1 k J jl$I EQ L f i~v 9 J l Technical Report ,TR-S364-3 Revision 0 4-112 Nlf(NIING SERVICES SAP2SAP.VERIFICATION 5364 6" JUL" 85 DG COOK UNI Tl r SV HODIFICATION TINE/FORGE TABLE 46'AGNITUDE AT NODE POINT 240 o tO~, 0 I LlJg)&ca~Pl~At 00 T I HE 0-l 0.29 0-36 0.43 0.50 a I Technical Report TR-5364-3 Revision 0 4-113 QBNIING SERVICES SAP2SAP VERIFI CAT ION 5364 6" JUL-83 DC COOK-UNIT) e SV NODIFICATION TINElFORCE TABLE 4F'e MAGNITUDE AT NODE POIHT 00 7 T I NE 0.i 0.2a 0.36 0.45~ca&n C)~m~tD O tO I C)CO CO I g C f k 0 Technical Report TR-5364-3 Revision 0 4-114 1)LfNNING SERVICES 6"JUL"83 SAP2SAP VER IF I CAT ION 5364 DC COOK UNIT l r SV MOOIFICATIOtt TIME/FORCE TABLE 48'AGNITUDE AT NODE POINT CD h h CV00~7 TIME 0.1 0.28 0.36 0+43 hJ~CDw C)~CO CO IO I lO lO 0 a CD I I 41 g)4'I I II 11 4 4.4 I'I la V&11 I" I I'I 4 yl 1 I I I 4 I Technical Report TR-5364-3 Revision 0 4-115 NLfNNING sERv'tcEs SAP2SAP VER IF I CAT'ION 5364 6" SUL-83 DC COOK UNIT 1 r SV HODIFICATIOH TINE/FORCE TABLE 49~MAGNITUDE AT NODE POINT 229 00TINE 0.2>0.2a 0.3S 0.43 0.50 Technical Report TR-5364-3 Revision 0 4-116 lkiSlNIIIIG SERVICES SAP2SAP VERIFICATION 5364 6" JUL"83 DC COOK-UNITt e SV MODIFICATiON TIME/FORCE TABLE'0e MAGNITUDE AT NODE POINT 225 0 00 I 0 0.14'TIME.2)0.29 0.36, 0.43 0.50 CV Ol C5 I CV 0 I UJ~CD~C)a CO CII Ltl I h a 0

Technical Report TR-5364-3 Revision 0 4-117 N)SIIING SERVICES SAP2SAP VERIFICATION 5364 6-JUL-83 DC COOK-UN'I T1~SV MODIFICATION

,-TINE/FORCE TABLE 5l.MAGNITUDE AT NODE POINT 222 Lll Ol CO 04 0 00 0.T I NE.2l 0.29 0.36 0.43 O.SO' Technical Report TR-5364-3 Revision 0 4-118 IIILHINII NG SERVICES 6-SUL-83 SAP2SAP VERIF I CAT ION 5364 DC COOK-UNI T1 e SV NODIF I CAT ION TINE/FORCE TABLE'52'AGNITUDE AT NODE POINT 214 CO 0 O C4 I 00 0.0 T I NE 0.2)0.29 0.36 0.45 0.50 Technical Report TR-5364-3 Revision 0 4-119 N)INNING SERVICES 6-JUL-83 SAP2SAP VERIFICATION 5364 DC COOK-UNIT)

~SV MODIFICATION TINE/FORCE TABLE 53 MAGNITUDE AT NODE POINT 208.0 00 CO h 0.0 0.14 TINE 0 21 0.29 0 43 0 50 Technical Report TR-5364-3 Revision 0 4-120 NHIINIIRG SERVICES SAP2SAP VERIFICATION 5364 6-JUL"83 DC COOK-UNIT) e SV MODIFICATION TIME/FORCE TABLE 54 e MAGNITUDE AT NODE POINT 298 Ol Ol CO'l Ol IO o QJ CO CC CO o h 00 0 0.1 0 1..36 0.45 0.50 o C)o l

Technical Report TR-5364-3 Revision 0 4-121 NHNIIRG SERVICES 6-JUL-83 SAP2SAP VERIFICATION 5364 DC COOK-UHI T)o SV NOD IF I CAT ION TINE/FORCE TABLE 55~NAGHI TUDE AT NODE POINT o oo h yo IO Q~9 I~cv Oe 0~Pl 0.21 I NE 0.0.36 h lO CO I CV Ol Cb CO I Technical Report TR-5364-3 Revision 0 4-122~IILfNNING SERVICES 6-JUL"83 SAP2SAP VERI F I CAT ION 5364 DC COOK-UNIT1 e SV MODIFICATION TIME/FORCE TABLE 56 e MAGNITUDE AT NODE POINT h 0 00 0 Ol TINE 0.21 0.29 0.36 0.43 0

Technical Report TR-5364-3 Revision 0 4-123 NH(hNING sERYIGEs SAP2SAP VERIFICATION 5364 DC COOK-UNITl e SV MODIFICATION TIME/FORCE TABLE 57 e MAGNITUDE AT NODE POINT Ol Ol ha tb Ol 00 0.07 0.14 T INE 0.21 0.29 0.56 0.45 C)CO Ol~~~ocO 0 I QJ'%3~~lO~Y)~CV Cb Cl CO Y)1 CO Yl 0 Cl P t II Technical Report TR-5364-3 Revi s i on.0 4-124 lkhIIIING SERVICES SAP2SAP VERI F'I CAT I ON 5364 6-JUL-83 OC COOK" UNI T l e SV NOOIF I CAT ION T I NE/FORCE TABl E 58 e NAGHI TUDE AT NODE POINT 00 0.07 0.T I NE 0.21 0.29 0.36 CV O~I QJ&la O~~CO~OJ CO CV n LO Technical Report TR-5364-3 R'evision 0 4-125 NL'NN11NG sERYIGEs SAP2SAP VERIFICATION 5364'"JUL"83 DC COOK-UNIT)e SV NODIF I CAT ION TINE/FORCE TABLE'9 e NAGNI TUDE AT NODE POINT 00 O-OT 0.1 TINE 0.2l 0.29 0.36 0..50 Technical Report TR-5364-3 Revision 0.4-126 Bf@NS I NG SERVICES 6-JUL"83'SAP2SAP VERIFICATION 5364 DC COOK-UNI T l e SV NODIFI CAT ION TINE/FORCE TABLE 60 e MAGNITUDE AT NODE POINT 60 lO o CO 00 0.07 0.14 T I NE 2l 0.2S 0.36 0.43 0.50 OJ~CV I~ca OCI C)ll it>CV CO I Technical Report TR-5364-3 Revision 0 4-127 r NkfllNkING SERVICES SAP2SAP VERIFICATION 5364 6-JUL-83 DC"COOK-UNIT1 e SY MODIFICATION TINE/FORCE TABLE 61 e NAGNI TUDE AT NODE POINT r ,Ol CV 0 00.07~14 TINE'1 0~29 0.36 Technical Report TR-5364-3 Revision 0 4-128 6NNIING sERvIcEs SAP2SAP VERIFICATION 5364 6" JUL-83 DC COOK-UNIT1r SY NODIFICATIOH TINE/FORCE TABLF 62.e NAOHITUOE AT HOOE POINT 48 h O O 00 0.07 T I ME 0-21 0.29 0.43 O.S0, CO Al CO I Technical Report TR-5364-3 Revision 0 4-129 llhjtNIING SERYICES SAP2SAP VER IF I CATION 5364 6" JUL-83 DC COOK UNI T l r SV fhODIFI CATION TINE/FORCE TABLE 63~NAGNI TUDE AT NODE POINT IO Cb o h tO CV 0 00 0.07 TIME 0.2)0 29 0'3 rr 0~Ol 0 CO CO I Technical Report TR-5364-3 Revision 0 4-130 BANNING SERVICES SAP2SAP VERIF I CAT ION 5364 6" JUL"83 DC COOK'UNIT1~SV NODIFICATION T I t1E/FORCE TABLE 64.NAGN I T VDE AT NODE POINT..Q)00 0.0 0.14 T INE 0.1 0.2S 0.36 0-43 Oe50~ca~&I Y)04 CD I CD CV OJ CO I PA O Technical Report TR-5364-3 Revision 0 4-131@LSN31HG sERYI GEs SAP2SAP VER I F I CAT I ON 5364.6" JUL-83 DC COOK-UNI T1 e SV NODIF I CAT ION TINE/FORCE TABLE 65 e NAGNI TUDE AT NODE POINT 00 0 0 0.I 4 T INE 0.21 0.29 0.56 0.43 Technical Report TR-5364-3 Revision 0 4-132 NB(Nfrws sEsvrcEs SAP2SAP YERIFICATION 5364 6"JUL-83 DC COOK-UNIT l.SV NODIF I CAT ION-T I NE/FORCE TABLE~66~NAGNI TUDE AT NODE PO I NT'ooo ce N O@J 9 I 0.14 TINE.2l 0.29 0.SS 0.43 Technical Report TR-5364-3 Revision 0 4-133l51583ING SERViCES 6-JUL-83 SAP2SAP VERIF I CAT ION 5564 OC COOK" UNI T1 r SV MODIFICATION T'INE/FORCE TABLE'l, MAGNITUDE AT NODE POINT CO Ol0 Ol CO I 00 07~l4 0.T I NE 0.29 0.36 0.43

Technical Report~~TR-5364-3 Revision.O 4-134 A TELEDYNE ENGINEERINQ SERVICES case.Included here is the RELAP5 MODl input listing for the transient steam The SV model has: 375 volumes 374 junctions Heat structures were not included in the RELAP model because of the program capacity.Including heat structures would have further reduced the number I~~~~~~~~of avail able control volumes.This is a conservative assumption, ITI (Reference 6)s'howed higher loads were computed without heat structures.

.RELAPS 1~014 PEACTOR: Loss oF coot.ANT ANALYsIs PRoGRm LISTING OF INPUT DATA FOR O':QE 1 1=D.C.COOK UNIT1 3 SV S OPEN 2 r DISCHARGE PIP!N<G 3*THIS IS THE NiG):)BERING SYSTEM FOR UNIT1'S RELAP MOPFL 4 4 WHERE COMPONENT:S,NUMBERED IN THE;"-'"5-"'4'"100)s ARE VALVE SV-45C AND ARC 1.LEVEL'69~'-2>>"'"""""'

4 200'S ARE VAl VE SV-45B mD ARC 2 LEVEL 670'-10" 7 t 300 5 ARE VALVE SV 45A ARN ARC 3 LEVEL 672 6'n'4 40P)S ARE PORV NRV-151 AND ARC>>A>>9 4 500'S ARL=PORV NRV-153 AND ARC"8" 10 4 600'S ARE PORV NRV-152 AND ARC"C"" ii""*""'"""'"""""'700'S AND 800'S ARE 6>>AND 12>>MAIN DISCHARGE PIPING-" 12 4 900'S QUEENCH TANK PORTION 13 4 999 ATMOBSPHERE 14 O MO CO'O 15]6 17 100 NE'M TRAN ASNT 18 101 RUN 19 102 BRITISH BRITISH 20 104 NOACT ION 2i ttettttetrtteteett Getttfefttfttftfftffftttt 23 4 TIME STEP CCDNTROL 24 tttettttttttfttett 4444444feefttttt44444tttt 25 26 201 0.500.1.-.~"4, 11001)5150)250 27 28 29 eeeef erect trterrtt teeee44eeeeffetefetfefff 30 4 MINOR E+ITS t 31 etettteeittetetert<<tettfeeeeeeteetteffff fft 32'3"'*301"'F'LOWJ 10fR&i0000 34 302 MFLOMJ 206~00 35 303 MFLOWJ 30600ippo 36 304 MFLO'MJ 3080)OPPQO.

37 305 MFLOMJ 2080)1100 38 306 MF LOW J 702~00 39 307 MFLOXJ 1080)00000 40, 308 MFLONJ 9770)PPPOO 41 4 42 309 QUALS 1052)00000 43 310 QUALS 1070'Ppooo 44 311 QUALS 1073:80000 45 312 QUALS 70 10:10000 46 313 QUALS 811970000 47 314 OVALS 8132)60000 48.315 QUALS 97818'0000

.49 316 QUALS 2052~0 50 317 QUALS 2070 top 51 318 QUALS 305$POOPO 52 319 QUALS 207260000 53 320 QUALS 3070)POOP 54 321 QUALS 307180000 55 56 323 P 105ZPOOOO.,CHKD,,,....BY

~A'pgT))),'

Zp-gg

RELA I/O'l4 REACTOR LOSS OF COOLANT ANALYSIS PROGRAM PAG 2 57 58 59 60 Bt 62 63 64 65 BB 67 68: 70 71...7.2'"73 74 75 76'7 78 79 80 81 82 83 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99 100 101 102 l03 104 105 106 107 108 109 110 111 112 113 114 GQ4 P 107010000~6 P 107330000 3~7 P 701010000 3.'31 P 8 1 1970000 3:32 P 8 13260000 2.33 P 978020000~34'P.978030000~5 P 205200000 3:36 P 2070 f 0000%37 P 305200000 3:38 P 207260000~9 P 307010000 sAO P 307180000 r r e t t t t t t t t f't t f t r t t t f t t t t t t t t t f t t f f f t t t t FORCE CARDS FOR REPIPE r at t t tf t t tf f f t tf t f f t tf f tf t t f f t f f tf t t tt t PIPING DOWNSTREAM OF THE PORV'S 2001 5, 215 2002 4 1 1010000!4 1 1020000~4 1 1030000, 411040000, 411050000 2003 411060000~411070000, 411080000, 411090000, 411100000 2004 411110000, 411120000, 411130000, 411140000, 411150000 2005 411160000,411l70000,41!180000,4'l!!SOOOO 2006 51 1010000, 51 1020000, 51 1030000, 51 1040000~5!!050000 2007 511060000e 5!!070000,51]080000,511090000,511100000 2008 51 1 1 10000, 51 1 120000, 51 1 130000, 51 1 140000, 511150000 2009 511160000,511170000) 511180000,511190000 2010 611010000~611020000,611030000,B11040000,611050000 201 1 6 1'l060000, 61 1070000, 61 f080000 r 2012 515010000,515020000,515030000, 0'l5040000,515050000 2014 5 15060000, 515070000 i 515080000, S 15090000, 515100000 2015 515110000,515120000,701010000,513010000 r r SV ARC FROhl VALVE 45A bOWfl iO ELEVATION 672'" 2018 301010000, 303010000, 303020000,303030000, 303040000 2019...305010000,305020000,305030000,305040000,305050000 2020 305060000,305070000,305080000,305090000,305100000 2021.....3051.10000

~305120000'05130000.

305140000r 305150000,....,.............,...., 2022 305160000, 30S170000, 305180000, 305190000, 305200000 2023-307010000.307020000,307030000,307040000,307050000 2024 307060000,307070000,307080000,307090000,307100000

2025,307 1 10000 307 120000t 307130000~
307 140000t307150000 I 0~.Vl X"---------'"-------
lA-GJ M O MA C)
RELAP 115/014 REhlOTWR LOSS OF COOLANT ANALYSIS PROGRAM 2026 30716000>>.307170000,307180000,801010000 116 117 118 1'l9 120 121~t SV ARC FR(OH VALVE 45B DOWN TO ELEVATION 670'0" 122 123 2029 201010100<0 203010000.
203020000, 203030000;203040000 124 203Q 205010f0010,205020000,205030000,205040000,2050500QQ 125 2031 205080(00lp
~205070000, 205080000, 205090000, 205 jppppp 126 2032 205110>00lp
~205120000,205130000,205140000,205150000 127 2033 205160lOOS>.
205170000,205180000,205190000, 205200000 128 2034 20701ptOOt0.207020000,207030000,207040000,207050000 129 2035 20708ONO<O
~207070000, 207080000, 207090000, 207100000 130 2036 207 1 10lOOtD.207 120000i 207130000, 207 140000, 20?150000" 131 2037'" 207 j6ONOt0,207170000,207180000,207190000,2Q72QQQOQ 132 2p38 2072 10100(0, 207220000, 207230000, 207240000, 207250000 133 2p39 20726C'IOOlp, 805010000 134 135 136 137 138 139 14p t Sy ARC F~VALVE 45C OOWN TO ELEVATION 669'" 141 142 2Q42 10101~<), 103010000$
.103020000, 103030000$
.103040000..
143 2043 10508JrA).
105020000, 105030000, 105040000, 105050000 144 2044 10506dr~, 105070000, 105080000, 105090000, 105100000--"" j45-'2@45'j051MrA, 105120000, 105130000, 105'l40000, 105150000 146 2046 1051~a 105170000, 105180000, 105190000, 105200000 147 2047 1070&/~~107020000,'l07030000, 107040000, 107050000 148 2048 10706WAH, 107070000, 107080000, 107090000, 107100000 j 49" 2P49 1Q71 MrÃrg, 107120000, 107130000, 107140000, 107150000 150 2050 10718K<>A).
107170000$
107180000, 107..190000i 107200000 151 2051 j0721WA4 107220000,'lp?230000.
107240000, j07250000 152 2P52 10728CP<jt9, 107270000, 107280000,'107290000, 10730000P 153 2053 1073 1M'), 107320000, 107330000, 809010000 154'155 156 t 157 158 t 159 16Q ttttittttttt
~~trttttttttttttttttttttttitttttttttttttttttttttttttttt j6j"-gl'5 RUN QF PELAP INCiUbES'S'AFETY" RELiEF"VALVE CiAES'ANO'NAiN 162 t OISCHARGE LJlfE BETWEEN ELEV.684'-9" TO ELEV.649'-1/2" 163 tttttt$ttttttt~~~tttttttttttttttttttttttttttttttttttttttttttttttttt 164 165 166 167 168 tfttfi'ettttt at~~ttttttttttttttttttttt'tt 169 t TRIP%t 17p it it it tt t t t t~t~~t et it t it t'tt it if it f if$$$171 172 fD-Ãt.A)I n~'l K o mn I CD mH~m
RELAP yo'l4 REACTOR G~S,-'OF COOLANT ANALYSIS PROGRAM 501 TIME 0 GF NULL 3 0.0 L s VALVE OPENING TRIP 74 502 TIME 0 GE NULP i 5.0 L t JOB TERMINATION TRIP 175 515 P 982Q1QQQQ GE@NULL 0 1 14.7 L t WENCH TANK RUPTURE PRESS.176 600502, 177*178 sssssftsffsssssttrrrr--" r tssssrrrr AGsstftftfssffffsssfsfsffffffs Sf Srrtr~GP>>=>>Gtfftt'Stfttffftftffftff 180 s s HYOROD KNthtt1 t'COMPONENTS sssssr~rr>>>>+ssftfsttttststfsttffst 181 s" tssssssssf
~rr>>182 sttstfttftstsssfts
~rr~ssssts~rr<<~~sstttffttttftftfffsfffffffftffff 183 sf tsststss err~ssf sf st ttf ttttftf sf f tt 185*SAFETY VALVES DI~~E SECTION 186 ttftttstttsfftssssss>>
f tttssssss<<<<
~ftttfffftffftttttttf 187 188 189 f s r r<<>>a t t s f t t t f t f t f t t s s s t.t f f f f f t f t f s t t f t f t f t s t s f f 191 t SAFETY VAj VE r1,xriSCHARGING AT ELEV.669'-2" ARC 1 s t f s f f s s t tt t f f t f f f f t f s f f t t t t f f t t f t t t t t f s f t f t 192 ftstftftfststtttsr
~>>>><<-193 194 t PRESSURIZER COJ4vW1ssNT 195 1010000"PRSRZ41",~VPVOL 196 1010200 2 197 1010101 0.20.500..0.0.0.00005 0.11 198 1010201 0.~2500..1,2514., 1..3,2555., 1..5,2600., 1~~7 2667.1.99 1010202 9 2700 1 1 2740 1 1 3 2745 i 1 5 2747 1 1 7 2748 200 1010203 1.9~2750., 1 201 202 s PIPE COMPONENTS 203 1020000"PRZ1-EXIT'LGJUN 204 1020101 101000000%%~000 0.0 0.0 0.0 1QQQ 205 102020i 1 0.0 0~0.0 206 207 s VALVE UPSTREAM 208 209 1030000 LS1 IN" 210 s NO.OF VOLS.211 1030001 4 212 s VOL.FLOW AREA 213 1030101 0.14653 4 214*VOL.LENGTHS 2 i 5 1030301 0.3490 2 16 1030302 0.4236 217*VOL.CAL.AUTO 218 1030401 0.0 219*VERT.ANGLES 220 1030601 45.1 221 1030602 0.0 222 t PIPE ROUGHNESS 223 1030801 1.513-4 0 A'A 4 224 f GJUN.LOSS COEFF*'25*'1O309Oi" O.O918 22B'030902 0.0 lg 0 227 228 1031001 00 4 229 h 230 1031101 1000 t RELAP/014 REACTOR LGc'SS OF COOLANT ANALYSIS PROGRAN PAG 5 231 232 1031201 2 2500.1,0.0,0~0 4 233 234 t INITIAL JUN FLO'MS 235 1031300 236 1031301 0.0 0.0"'0 3 237 t 238*LOOP SEAL 239 1040000 JUN-LS1" SNGLJUN 240 1040101 1030'10000 105000000 0.00.1836 0.183B 1000 241 1040201 1 0.0 0.0 i 0.0 242 243'*1050000 LPSL 1 P IPE 244 1050001 20'45 1050101 0.14653 246 t 247 1050301 0.50 248 1050302 0.6203 2<0.249 250 1050401 0.0 251 252 1050601 253 1050602 0~0 10 254 1050603 90."20 255 256 1050801 1.513-4 00.0 20 257 , 258 1050901 0.0 CO 0 6 259 1050902 0.1836 W 1836 7 260 1050903 0.0 CP 0.9 261 1050904 0.1836 CP.183B 10 262 1050905 0.0 cP.0 19 263 264 1051001 00 265 266 10511O<<000 267 t*268 1051201 2 2500...1'0.0 0.0 20 269 270 1051300 271 1051301 0.0 0.0 r0~0 19 272 273 t CROSBY BNB MFETY VALVE kf SV-45C" 274 275 1060000"SVN01" V.'ALVE t VALVE OPEN I/iTH PROG.START" 276 1060101 105010000 107000000 0.01897 0.0 0.0 0100 1.0 1.0 277 1060201 1 0.0 P 0 0.0 278 1060300 NTRVLV 279 1060301 501 505'100.0.0*VALVE Of'ENS QITH PROG.START 280 281 i'ALVE OOWNSTR~PIPING 282 1070000"OKNSTRM/<" PIPE 283 1070001 33 t 285 1070101 0.20069 33 285 287-1070301 0.5261 288 , 1070302 0.9943-RJM W CD WrD I~~V)~.e-Y.o QP O p ITl I.Qg RELAP ii 014 REACTOR l.OSS Us COOLANT ANALYSIS PROGRAM 289 1070303 0.9132 290...1070304 0.8472 30 291 1070305 1.085 292 293 1070401 0.0 294 295 1070601 0.0 296 1070602-90 297 1070603 0.0 298 299 1070801 1.52-4 0."P 300 1070901 0.0 0.0 301 1070902 0.18 0.18-4 302 1070903 0.'0 0.0'l4 303 1070904 0.18 0.18 15 304 1070905 0.0 0.0 32 305 306 107 1001 00 33 307 1071101 1000 32 308 309 1073201 4 17.7'!20'-0 93424 310 311 1071300 1 3'l2 107130'1 0.0 0.0 0.0 313 314 315 316 i'tijtjti~<<-t it*titiiitiitititttttittttjitiiitttjtj 318 j SAFETY VALVE N2 DIS~GING AT ELEV.670'"10" ARC 2 319 tiifif fiit j if if<<i jtf it<<+>itttttttttittttttittttttitttttjtjifttifi 320*PRESSURIZER COMPOltlTtN
'2 1 2plp'000-<<PRSRZ<2 T~VOL 322 323 2010101 0.2p.500.0 O.0.0.00005 0.1'j'24 2010200 2"" 2pj02pj"" 0 25pp.1..: 4~,~3,2555., 1~5,2600., 1..7,2667.','f:
326 2010202.9, 2700., 1.1'740.i 1.1.3, 2745., 1.1.5, 2747., 1.1.7, 2748.p 1.327 2010203 1.9,2750., 1.328 329*PIPE COMPONENTS 330 2020000"PRZ2 EXIT"<<jeGLdUN 331 332 2020101 201000000 20~00 0.0 0.0 0.0 1000 333 334 2020201 1 0.0 0.0 335 336 j VALVE UPSTREAM 33i 2030000"LS2 IN" 338*Np OF VPL.339 2030001 4 340*VOL.FLOW AREA 341 2030'lp{0.14653 4 342 j VOL LENGTHS 343 2030301 0.3490 1 344 2030302-0.4236 4 345 t VOL.CAL.AUTO.346 2030401 0.0 4 RELAP/014 REACTPR LOSS OF'.<<ODLANT ANALYSIS PROGRAM PAG 7 347 i VERT.ANGLES 348 2030601 45.349 2030602 0.4 350 351 PIPE ROUGHNESS 2030801 1.513-4 0.0 352 353 354 JUN 203090{2030902 LOSS COEFF.0.0918.0.0918 0.0 0.0 355 356 2031001 00 4 357 358 2031 101 1000 3 359 360 2031201 2 2500.0.4 361*INITIAL JUN.FLOWS 362 2031300 1 363 2031301 0.0 0.0 0.0 1.0 0.0 0.0 364 365*LOOP SEAL 366 367 2040000"JUN-LS2" 368 2040101 203010000 2050hKPA70 0.0 0.1836 0.1836 369 2040201 1 0.0 0.0 370 371 2050000"LPSL 1" PIM , 372 2050001 20 373 374 2050101 0.14653 20 375 376 2050301 0.50 10=377 2050302*0.6203 20 378 379 2050401 0.0 20 380 381 2050601-90.7 382 2050602 0.0 10 383 2050603 90.20 384 385 2050801 1.513-4 0.20 38B 387 2050901 0.0 0.0 388 2050902 0.1836 0.18M 389 2050903 0.0 0.0 390 2050904 0.1836 0.182@391 2050905 0.0'.0 392 i 393 2051001 00 20 394 395 2051101 1000-19 39B~397 2051201 2 2500.20 398 i INITIAL JUN.FLOWS 399 2051300 1 400 2051301 0.0 0;0 0.0!9.401 402 i CROSBY 6MB SAFETY VALVE~2 SV-456 403 404 2060000"sv N02 VALVE CO%1 RELAP 1/014 REACTpR LOSS pF:'OOLANT ANALYSIS PROGRAM 1.0 0.0*VALVE OPEN WITH PROG.START tttttt tttttt 2667., 1.1.7,2748., 1.2p60101 2p5010000 2070~~0 0.0189?0.0 0.0 0100 1.0 408 2060201 1 0.0 0,0 0~'i 407 2060300 MTRVLV 408 2060301 ,501 502 100.409 410*VALVE DOWNSTREAM PIP!N+I 411 2070000"DWNSTRMiY2" P IP+." 412 4 13 207000'I 26 414 2070101 0.20069 26 415 416 2070301 0.5261 4 417 2070302 0.9271 14 418 2070303 0.8852 23 419 2070304 1.085 26 420 421 2070401 0.0 26 422 423 2070601 0.0 4 424 2070602-90.14 425 2070603 0.0 26 426 427 2070801 1.52-4 0.2<.428 429 2070901 0.0 0.0 430 2070902 0.18 0.18..4.431 2070903 0.0 0.0 432 2070904 0.18-0.18 14 433 2070905 0.0 0.0 434 435 2071001 00 26 436 437 2071101 1000 25 438 439 2071201 4 17.7 120.0~93424 0 26 440 441 2071300 1 442 2071301 0.0 0.0 0.0 443 444 t 445 ttttttttttttttttttttttttttt>ttttttttttttttttttttttttttttttttt 44B-t SAFETY VALVE g3 Df~GING AT EL'EV.672 i Bn ARC 3 447'tttttfttttttttttttttttttgtttttttttttttttttttttttttttttttttttt 448 449 t PRESSURIZER CO'MPONffff 450 3010000"PRSRZP1" TMDf!OL 451 3010200 2 452 3010101 0.2p.5pp.0, 0.0.0.00005 0.453 3010201 0..2500.,1..
1,'i614~1~.3.2555..1..5,2600.', f"."'" 7454 30'l0202.9,2700.~1.1.1,,$740., 1.1.3,2745., 1.1.5,2747.q 1.455 3010203 1.9,2750., 1.456 t PIPE COMPONENTS 457-'"3020000--"-"P'RZ3'XIT" 5f jCilalUN 458 302010'1 301000000 30309Q000 0.0 0.0 0.0 1000 459 460 3020201'1 0.0 0.0 P.U 461 t VALVE UPSTREAM 462 P Al 0~~---.~--~~~-~" CA V~------'--=o-T o I~O*-~.~
RELA 463 464 465 4ee 467 468 469 470 471 472 473 474 475 476 477 478 479 480 481 482 483 484 485 486 487 488 489 490"4S1 492 493 494 495 496 497 498 499 500 501 502 503 504 505 506 507 508 509 510 511 512 513 514 5'IS 516 517 518 519 520 1/014 3030000 t 3030001 REACTOR LOSS OF O'ODLANT ANALYSIS PROGRAM"LS2 IN" PIPE 4 3030101 0.14653 4 t 303030 I 0.3125 1 3030302 3030401 0.4236 4 0.0 4 3030601 45.1 3030602 0.0 4 3030801 1'13-4 0.0'C 3030901 0.0918 0.0918 3030902 0.0 0.0 1 3 3031001 00 t 3031101 1000 3 3031201 2 2500 1.O.O 0.0 4 3050302 0.6203 20 3050401 0.0 20 3050601-90.7 3050602 0.0 10 3050603 90.20 3050801 1.513-4 0.0 20 t 3050901 0.0 0.0 3050902 0.1836 0.1836 3050903 0.0 0.0 3050904 0.1836 0.1836 3050905 0.0 0.0 3051001 00 20 t 305110'000 19 6 7 9 10 19 t 3031300 1 3031301 0.0 0.0 0.0 3040000"aJUN-LS3" SNGLdlW'3040101 303010000 305000000 0.0 0.1836 0.'l836 3040201 1 0.0 0.0 0.0 3050000"LPSL 2" PIPE 3050001, 20 t 3050101 0.14653 20 3050301 0.5 10 1000 PAG (D M(D I o'Vl'K lh a-wo 1'C7 (b' RELA 1/014 REACTOR LOSS OF COOLANT ANALYSIS PROGRAM 10 521 3051201 2 2500.1.0 0.0 0.0 20 522 523 3051300 1 524 3051301 0.0 0.0 0.0 19 525 e 526 e CROSSBY 6M6 SAFETY VALVE l'3 SV-45A 527 528 3060000.".SV N03" VALVE t VALVE OPEN WITH PROG.START 529 3060101 305010000 307000000'".01897 0.0 0.0 0100 1.530 3060201 1 0.0 0.0 0.0 531 3060300 MTRVLV 532 3060301 501 502 100.0.0 t VALVE OPENS WITH PROG.START 533 534 e VAL'.VE DOWNSTREAM PIPING"3p70ppp"DWNSTRMP3e PIPE 536 3070001 18 537 538 3070101 0: 20069 18 539 540 3070301 0~5261 4 541 3070302 1.034 12 542, 3070303 0;801 15 543 3070304 1.085 j8 544 545 3070401 0~0 18 546 547 3070601 0'0 4""'"'"'""""""'"'--------'"--""---"---""-"'"-'-"---*
".."--~--~------~-~~~-~548 3070602-90.12 549 3070603 0.0 18 5 t 50 551 3070801 1~52 4 0.18 552 553 3070901 0.0 0.0 3 554 3070902 0.18 0.18 4 555 3070903 0.'0 0.0 11 556 3070904 0.18 0.18 12 557 3070905 0.0 0.0 17 t 558 559 3071001 00 18 560 307 1 101 1000 17 561 562 3071201 4 17.7 120.0.93424 0.18 563 564 307 1300 565 3071301 0.0 0.0 0.0"""" j7'"""------'-
""" 5 e 567 568 eteteeeeeeeettttetttettttttetttttttttttttttt "569 e g54V DISCHARGE SECTIpN 57p tete eeet ee eeet ettttettittttttf ttf eeet tttf tet 571 2 573 t t e f f e e e e e e e e e t t t tt f et et t t etc tet t tt et tet et et et t tete'et 574 e POR~/NRV-151 DISCHARGE LINE ARC"A" 575 ieetteee~eetettetttet\ttttttettttttttttt'etttttftttttt 576 577~578 4110000"PORV1" PIPE 0.W.O 1 RELA 01/014 REACT:10R LOSS OF COOLANT ANALYSIS PROGRAM 579 4110001 19-580 581 4110101 0.054132 17 582 4110102 0.200989'l9 583 584 4110301 0.372',....4.585 4 i 10302 0.3859 8 586 4110303 0.581,, 1'7 587 4110304 0.349 19 , 588 589 4110401 0.0 19 590 591 4110501 0.0 4 592 4 1 10602-90.8 593 4110603 0.0 19 594 595 4110801 1.53-t4.0.17..596 4110802 1.52-=4~0 19 597 598 4110901 0 0 0 0 3 599 4110902 0.20848 0.2088'4"""" 600 4110903 0.0.0.0 7 601 4110904 0.20848 0.2088 8 602 41 10905 0.0 0.0 16 603 4110906 0.378@4 0.1565"'j7'04 4'1 10907 0.0 0.0 18 605 606 4111001 00 19 607 4111101 1000 18 608 609 4111201 4 1 7~7 120.0.93424 0.0'""'""j 9" 610 611 4111300 1 612 4111301 0.0 rO 0 0.0 18 613 614 4120000"ENrd+MAIN" SNGL JUN 615 41201014110.~00 701000000 0.0 0'.-j8'P." j'8'000 616 4120201 1 (P-0 0.0 0.0 617 8 619 ttttttttttttttt stttttttttttttttttftttttttttttttttttt 620 t PORV NRV-103 DISCHARGE LINE ARC"6" 621 titteettattttr<+tttttttttttttttttttttttttttttattttett 622 623 624 625 5110000"PONl2L INE" PiPE 626 5110001 19 627 628, 5110101 0.05132,, 18 629 5110102 0.08i840 19 630 631 51'l0301 0.4:W3 3 6325110302 0.3620 7 633 5110303 0.35 9 634 5110304 0 6098 18 635 5110305 0.371 19 636~-----~~-Cb.~.AD C I 0~Vl&~~-~~4(i-M,W 0 WO~-I-Dl RELAPSE I/014 637 5110401 REACTOR:~OSS OF COOLANT ANALYSIS PROGRAM 0.0 19 PAG 12 638 639 5110601 0.0 3 640 5110602-90.7....641 5110603 0.0 19 642 643 5110801 1.53-4.0 644 5110802 1.34-4.0 19 645 646 5110901 0.0 0.0 2'47"-" 5i10902 0.2088 0'088 3 648 5110903 0.0 0 0.6 649 5110904 0.2088 0~2088 7 650 51 10905 0.0 0~'0, 17 651 5110906 0.0544 0.0399 j8'52 653 5111001 00 19.654 t 655 5111101 656 657 51 1 1201 658 1000 18 4 17 7 120.0.93424 0.0 19 659 5111300 1 660 511'130'1 0.0 0.0 0.0 18 661 662 5120000"JUNC" SNGL JUN 663 5120101 5110100003 51300000p'"p.0 0.p 0.0 1000 664 5120201 1 0.0 (P 0 665 666 C 667 668 5130000"4X4X3TEE"-
669 5130001 0 670 5130101 0.08840 0.3524 0.0 0.0 0.0 0.0 1.34-4 0.0 Pp 67'5130200 4 17.7 120.0.93424 0.'0"0.'0'72 673 674 5140000"4 IN JOHS" SNGL JUN 5130iOONP 515000000"" 0.'0" 0 0"p 676.5140201 1 0.0 8 0 0-0 677'"""'i""-"" 678 5150000"4INSCK4+" PIPE 679 5150001 12 680 681 5150101 0.0884 10 682 5150102 0.20069 12 683 684 5150301 0.3524 1, 685 5150302 0.6963 10 686 5150303 0.349 12 687 688 5150401 0.0 689 , 690 5150601 0.0 691 692 5150801 1.34-4 0;0 10 693 5150802 1.52-4 P 0 12-694Ã7, M.W O WO ,, C)-o O jVH~.m a~.m.ZO Pl Rim
RELAP 4/0)14 REACTOR LOSS OF COOLANT ANALYSIS PROGRAM PA 13 695 696 697 698 699 700 701 702 703 704 705 706 707 708 709 710 711 712 713 714 715 716 717 718 719 720 721 722" 723.724 725 726 727 728 729 730 731 732 733 734 735 736 737 738 739 740 741 742 743 744 745 746 747 748 749 750 751 752'.1509901 0.0 0.0 5".509902 0.1483 0.0815 51509803 0.0 0.0 t 5-5 i:O01 00 5;5)1101 1000 11 515t2201 4 17.7 120.0.93424 0.0 12<1512800 301 0.0 0.0 0.0 11 t 0"000"ENTERMAIN" SNGLalUN 5160t101 515010000 701000000 0.0 0.18 0.18 3000 51602201 1 0.0 0.0 0.0 f ft'%ttttttttttttttt
~tftttttttttttttttttttttttttttttt RV NRV-152 DISCHARGE LINE ARC"C" tttyaattttftttttttttetttttttttttttttttttttttttttttttt t 12 611OMO 61<0~1"PORVDISC3" PIPE 8 t g 11<i101 0.05132 8 611>@01 0.3723 4 g11~02 0.3646 8 61 1~01 00 8 e 61 iry601 0.0 4 61 141602-90.8 611rJN01 1.53-4.0 8 61 A%01 0.0 0.0 611M02 0.2088 0.2088 4 61M%03 0.0 0.0 611 0001 00 6 1 1 9101 1000"'1[5201 4 17.7 120~0.93424 0.0 8 611 ti 300 1 611 5301 0.0 0.0 0.0 7 6124900"PORVLINE" SNGLJUN 61/0101 611010000 513000000 0.0 0.1932 0.1932 1000 6120201 1 0.0 0.0 0.0~t f Otttttttttf tttttttttttttttttttttttttttt e HAIN DISCHARGE LINE SECTION~f+f tttttttttttttttttttttttttttttttttttttt o Ro C)m
RELAP/014 REACTpR LpSS pp CCOOLANT ANALYSIS PROGRAH PAG 14 CONNECTION TO HAIN LEONE AT ELEV.672'-6" 753 754 755<HAIN DISCHARGE LINE 756 7010000"ENTERHAIN" BP~CH 757 7010001 0 758 7010101 0.20069 0.7035 0:0 0.0 0.0 0.0 1.52-4 0.0 00 759 70'l0200 4 17 7 12P'.0.93424 0.0 0.0 760 761 7020000""HAINLINE4 SNGLUUUN 762 7020101 701010000 7030006000 0.0 0.0 0.0 1000 763 7020201 1 0.0 0.0 0.00 764 765 7030000"MAINLINE" PIPE 766 767 7030001 14 768 769 7030101 0.20069'l2 77p 7p30102 p.777p8 14 t 112 IN LINE STARTS HERE 771 772 7030301 0.7035 1 773 7030302 1.0076 12 774 7030303 0.5834 14~.12 IN LINE STARTS HERE 775 776 7030401 0.0 14 777 i 778 7030601 0.0 1 779 7030602-90.14 780 781 7030801>>4Ž1.52-4 0.12 782 7030802 1.69-4 0.14 783 784 7030901 0.180 0.180 785 7030902 0.0 0.0 786 7030903 0.493 0.2045 787 7030904 0.0 0.0 13 788 789 7031001 00*14 790 7031101 1000 13 791 792 7031201 4 17.7 120.0;.93424 0 0'14 793 794 7031300 1 795 7031301 0.0 0.0 0.0 796 797 798 7040000"HAINLINE" SNGL~............,..........
799 7040101 703010000 801OCt9000 0 0 0 0 0 0 1000 800 7040201 1 0-00.0 P.P 801$02 3080000"CON.1" SNGLJUt~803 3080101 3070100pp 8p1000000 0.0 0.156 0.'156'ppp'""-'"'--'04 3080201 1 0.0 0.0 0, 0 805**806 807 808 809 810
RELA 1/034" 811 812 813 814 815 816 8'17 818 819 820 821 822 823 824 825 826 827 828 829 830 831 832 833 834 835 836 837 838 839 840 841 842 843'44 845 846 847 848 849 850 851 852 853 854 855 856 857 858 859 860 861 862 863 864 865 866 867 868 REACTOR LOSS OF COOLANT ANALYSIS PROGRAM 8010QW>0."12-BRANC1" BRANCH Sp ipon~1...., 0.8010'" 41 0.77708 0.8334 0.0 0.0-90.-0.8334 1.69-4 0.0 00 80102000.417.7 120.0.93424 0.0 0.0'C 80200000"MAINLINE" SNGL JUN Sp201C01 801010000 803000000 0.0 0.0 0.0 1000 80202101 1 0.0 0.0 0.0 803~00"MAINLINE" SNGLVOL 8p30~gp1 0.77708 0.8334 0.0 0.0-90.-0.8334 1.69-4 0.0 00.80302iop.,.
4, 17.7 120.0.93424 0.0 0.0 t CONNECTION TO MAIN LINE AT ELEV.670'-'10" 80400~"MAINLiNE" sNGLJUH 8Q4Q1r01 803010000 805000000 0.0 0~0 0.0 1000 80402W1 1 0.0 0.0 0.0 20800~"CON.2" SNGLJUN**20801rP1 207010000 805000000 0.0 0.156 0.15B 1000 2pspjcD1 1 0.0 0.0 0.0 80500~"HAINBR.3" BRAIvcH 8050&P1....,0...,........
80501i91 0.77708 0.8334 0.0 0.0-90.-0.8334 f.69-4 Q.o 00 4 17.7 120.0.93424 0.0 0.0 80 806(gpQO"MAINLINE" SNGLJUN SP601+1 805010000 807000000 0.0 0.0 0.0 8060~~1 1 0.0 0.0 0.0 t 1000 807~"MAINLINE" SNGLVOL 80701r'01 0.77708 0.8334 0.0 0.0-90.-0.8334 1.69-4 0.0 00 4 17.7 120.0.93424 0.0 0.0 8070~t ONNECTION TO HAIN LINE AT ELEV.669i-2" 808~*"MAINLINE" SNGLJVM spSQ 1'01 807010000 809000000 0.0 0.0 0.0 Bosom'01 i'" o.o"o.o'"o.o 1000 108(Y~"CON.3" SNGLJUN 1080$01 107010000 809000000 0.0 0.156 Q.156 1PPP 1080101'I 0.0 0.0 0.0 809<PA+"MAINBR4" BRANCH 8090<1 0 8090)01 0.77708 0.8334 0.0 0.0-90.-0.$334 1 67-4"" p.p-'"'0'0'" 809 C400.t 8100000 4 17 7 120 0 93424 0 0 0 0"HAINLINE" SNGL JUN 15 I A~Vl&Es cil w ,.0...4..O I QP....~...-.'n O PAt cr<<
RELA 1/014 869 870 871 872 873 874 875 876 877 878 879 880 881 882 883 884 885 886 887*888 889 890 891 892 893 894 895 896 897 898 899 900 901 902 903 904 905 908 907 908 909 910 911 912 913 914 915 916 917 918 919 920 921 922 923 924 925 926 8 100101 8100201 81 10000'-'MAINLINE" PIPE 97 8 1 10001 8110101 t 8110301.77708 97 1..O'149 14 0~.5303 18 00.5 22 8110302 8110303 8110304 0'53125 26~+.9908 56 8 110305 81 10306 0~5,, 64 8110307 00.8750 72 8110308 (P 5104 80 8110309 (P.4993 88 81 10310 1.0556 97 t 81 10401 O.o 97--90.14--45.is"--90.22--45.'6--90.56 (P.'0 80--90-88 d>.0, 97 11~69-4 0".97 0.0 13 (P.078 0.078 14 (Po 00'7 g 078., 0.078 18 4)0 00 21 (P.078 0.078 22 (9.0 0.0 25 (P.078 0.078 26 6).O 0.0 55 P.156 0.158 56 io.O 0 0 63 P.026 0.026 64 P.o 0.0 71 P.13 0.13 72 IO.O 0.0 79 8110601 8 1 10602 8110603 8 1 10604 8110605 8110608 8110607 8110608 t 8110801 8110901 8110902 8110903 8110904 8110905 8 1 10906 8 1 10907 8110908 8110909 8110910 8110911 8110912 8110913 8110914 8110915 0.156 8110916 0.158 80 io.o o.o""""s7" io.158 0.158 88 0.0 0.0 96 PO 97 8110917 8110918 8110919 t Sii1OOi 811110i 96 REACTOR LOSS OF COOLANT ANALYSIS PROGRAM 8 a09010000 8 1 1000000 0.0 0.0 0.0 1000 0.0 0.0 0.0 PAG 16 lD Kl lb I 0 Vl~l/l O WA 1 AP C)"-tb O mm IZ@m mm-z'-...Q-m"'----.--0 m 1c"'C'f 0 RELA 1/014 REACTOR LOSS OF COOLANT ANALYSIS PROGRAM PA 17 927 8111201 4 17.7 928 929 8111300 1 120.0.93424 0.0 97 930 8111301 0.0 0.0 0.0 96 931 932 933 8120000'"'MAiNOiSC=" SNGLi/UN 0.0 13 0.156 14 0.0 23 0.156 24 0.0 25 26 966 8131300 967 8131301'0.0 0.0 0.0'25 968 969 970 97 1 t tt t t t t t t t t t t t t t t t tt t t't tttt t t tt t t tt 934 8120101 81 10100049 813000000 0.0 0.156 0.156 1000 935 8120201 1 0.0 0.0 0.'0 936 937 8130000"MAiNLiNEt" PIPE 938 939 8130001 26 940 941 8130101 0.77708 26 942 943 8130301 1.0 14 944 8 130302 0.5 24 945*8130303 1.0208 26 946 947 8130401 0.0 26 948 949 8130601 0.0 24 950 8130602-90.'6 951 952 8130801 1.69-4 0.26 953 , 954 8130901 0.0 955 8130902 0.156 956 8130903 0.0 957 8130904 0.156 958 8130905 0.0 959 960 8131001.00 961 962 8131101 1000 25 963 964 8131201 4 17.7 120.0.93424 0.0 26 965 X7 lD 0~..CJl 2 Ul Ql~.O...W.O I CA~.O..-..XJ fD O 972*QUENCH TANK 973 ttttttttttttttttt
~'ttttttttttttttttt 974 975 97B 977 9770000.QTANK-ft1" SNGLJUW'78 9770101 813010000 978000000 0.979 9770201 1 0.0.0.980 981*SPARGER 12 fN SCH40 PiPE 982 983 9780000"SPARGER" PIPE 984 tNO OF VOLUMES 0.0.1000 REf Ap 1/014 REACTpR 1.OSS gs COOLANT ANALYSIS PROGRAM PA 18 985 9780001 18 986 t FLOW AREA 987 9780101 0.7773 18 988 t VOL..LENGTHS 989*9780301 1.125 2 990 9780302 1.1333 7 991 9780303 1.0 18 992 t VOL.VOLS.993 9780401 0.0 18 994 t 995 t VERTICAL ANGLES 996 9780601-90.7 997 9780602 0.0 18 998 t PIPE ROUGHNESS 999 9780801*1.69-4 0.0 1000 t JUNCTION LOSS COEr s 1001 9780901 0.0 0.0 6 1002 9780902 0.156 0.188,.....,..?...,.
1003 9780903 0.0 0.0 1004 t VOL.CONTROL FLAG 1005 978 1001 00 18 1006 t JUN.CONTROL FLAG 1007 9781101 1000 17 1008 t INITIAL COND.1009 9781201 4 17.7 1&a O.S3424 0.""2" 1010 9781202 3 17.7 1 20.0.0 0.18'1011" t""-"-'-JUN'NITIAL~~'.1012 9781300 1 10'13 9781301 0.0 0.0 0, G 1014 t SPARGER EXIT 1015 9790000"EXIT" SNGLJUN 1016 9790101 978010000 9w~p0000 0.0 1.0 1.0 11pp 1017 9790201 1 0.0.1018 t QUENCH TANK 1019 1020 t WATER VOL.1021 9800000"QT.WATER" Sl4%, Vpi 1022 9800101 260.4706 5.~7 0,0 0.0 90.5.6667 p.pp3 0.0 01 1023 9800200 3 17.7 120 1024 t INTERFACE 1025 9810000"INTERFACE" 1026 9810101 980010000 982~0 o 0 0.0 0.0 1000 1027 9810201 1 0.0 0.0'P.P 1028 t AIR VOLUHE 1029 9820000"QT.AIR" SNGLML10309820101 260.4706 1.24 P9...0.0 0.0 90.1.2439 0.pp3 p p p1 1031 9820200 4 17.7 1?4 0.93424 1032 1033 t RUPTURE DISC 1034 9830000"RUP.DISC VAL-VE 1035 9830101 982010000 99S%XNOO 1~77 0 0.1100 1036 9830201 1 0.0.1037 9830300 TRPVLV 1038 9830301 515~VALVE OPENING TRIP 1039 1040 1041 ttttt tttttttttttt t~it t t t t t ttt ttttttttt'tt-----'"------'-------------
-.--....,.1042 t PIPE OUTSIDE ENVIROMENT t CD MA>1 O C/l-0-W 0 1 Ql k'l.II II I I RELAP 1/014 REACTOR LOSS OF , OPLANT ANALYSIS PROGRAM Pn 19 1043 1044 1045 1046 1047 1048 1049 1050 1051 1052 1053 1OS4 1055 1056 1057 1058 1059 1060 1061 1062 1063 1064 1065 1066 1067 1068 1069 1070 1071 1072 1073 1074 1075 1076 1077 1078 1079 1080 1081 1082 1083 1084 1085 1086 1087 1088 1089 1090 109'1 1092 1093 1094 1095 1096 t t t t tt t't t t t t t t t t*t t t t t tt f t+<At t t tt t tt t tt f 9ggpppp<<ATMOSPHERE<
TMNOPVOL gggplpj"-'p'pp'p
""-" jpppp 0.0 0.0 0.0 0.0.00001 0.0 11 9990200 4 9990201 0 0 14 7 120.0 9284 t tt t t t ttt t t t t t t ttt t t tt ttte t>t t t ttt tttttt PLOT CARDS*ttttttttttttttttttttttff+Okttttttttttttt t 20300100 MFLOKJ 10600000ll-20300200 MFLOWJ 20600004>-
20300300 MFLOWJ 30600004il"-
20300400 MFLOWJ 30800004~.
20300500 MFLOWJ 20800004<.
20300600 MFLOWJ 70200000<.
20300700 MFLOWJ 10800004<20300800 MFLOWJ 97700000'W.
20300900 QUALS 1052000lT~
20301000 QUALS t0705000<-
20301100 QUALS 1073300(~20301200 QUALS 70101004~20301300 OVALS 8 1 197000~20301400 QUALS 813260~20301500 QUALS 978 1804~20301600 QUALS 205200~20301700 QUALS 207010~20301800 QUAl.s 30520~20301900 QUALS 20726066+20302000 QUALS 30701~20302100 OVALS 307180&&20302300 P 10520CKK+20302400 P'l0701(RH+
20302600 P 10733065+20302700 P 70101~20303100 P 81 197CKYr'+20303200 P 8 13260Ci A 20303300 P 9780200%20303400 P gi80304 W 203O3SOO P Z0520pp,r9 20303600 P.2070100,+.20303700 P 305200Cr,'W 20303800 P 20726~20303900 P 3070100A'0304000 P 307 180't END OF CASE Technical Report TR-5364-3 Revision 0 4-154 Ph TELEDYNE ENGfNEERING SERVlCES.4,8~PI E These are input listings of Control Data Corporation's RELAP post-processor, REPIPE.Each set represents direction cosines of the RELAP model as well as structural node assignments.
Og the Unit 1 SV model, it was necessary to break up the model in two sections, of approximately equal size, because of REPIPE's size limitations.
~In ut Set Model Section 4.8.1 4.8.2 0
Technical Report TR-5364-3 Revision 0 4-155-~>-TELEDYNE ENGINEERINQ SERVICES 4.8.1 REPIPE In ut-Section A
SPIPES INLINE 3~KBLQCK 300.KPIPE 13.KPLOTT'~KPRINT=-1, KPNV=1.KSTEP"-3, NOROPy=41 i 1900pp 51512PPPP 3Q718Cp, 0003, 207260000) 107330000, 978080000$
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Technical Report~~TR-5364-3 Revision 0 4-161 A TELEDYNE ENGINEERINQ SERVICES 4.8.2 REPIPE In ut-Section B SPIP INLI.K8LOCK=300.
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Technical Report~~TR-5364-3 Revision 0 4l69-s>-TELEDYNE ENQINEERINQ SERVICES 4.9 APPENDIX A
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7./gAZ 3050I 304 JCT MAO+2 ITEM IDENT NUMBER DRAWING NUMBER LI ST 0 F MA TERIA L DESCRIPTION MATERIAL O'T'Y 59 30302r IIO o70 3 0qO".3oa vALI/8 cvcIS x8 v4APAW S V-NII8A tX 3O3O I llO5 w///06 4//lo7 Il N///08//IIOZ pjl 4IIP>545 o/IIO9 W////O o IIO" 8 jj O8 CI 3OSCP7 59 SO I SOD/C P XXXOaRO 55'305ll 30'///c5 4///5'(2 JGT-204 JCT 7O<J'CT pl poo'lcll 5ITS<295 5I5lapOiV N l2I/-15/.F91+DE 22//,/o2 6 6//<l 03 0)"3 45 35'3oa-j LDO3O/35 2030 510 sps s/6/lO8/2 JL/'.T g.b~I,IIL 5OI S 5I508 5 Hp 4O V 2OEo VAL I/2 Q O 7,'/Q'IPE 5 I EE E PIPE 5 CI-lEDLILE go jay 02 8 308 J(T ZOIG 5 8 o~2" g&2g 7C/ZQ 7co0 i4 f4B O7r cO)205//.-45-o" pk IQ0.Q7G.o88w XD f'I AT@pk go~8 FACT IO 8//i S@OI4 208 JCT IO 7O JCT 2 X2X'8/'Q'07>/758/0 7GDISI 7O)es 15/op IDO/0/T/I/OP j/O 0)o o~+x'-/02'5//'OSOI/O4 ICT-I 06 IAA L I/F CiPCPS 8T SV-45C IOS2Q IO5I9 4o/0 O ,&7/G.Zoa7.777i g 77 J'CT PUN CO/Aj'Tj/N
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ML17334A492

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1.0 INTRODUCTION

2.0 CONCLUSION

8.0 REFERENCES

1.0 INTRODUCTION

2.0 CONCLUSION

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ML17334A492

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1.0 INTRODUCTION

2.0 CONCLUSION

8.0 REFERENCES

1.0 INTRODUCTION

2.0 CONCLUSION

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