ML18003A871

Forwards Three Tables Re Filter Sludge Activity Calculations (Normal & Design) & Feed Streams to Vol Reduction Sys (Unit 2 Operation),Per P Kadambi Request for Use in Preparation of Des

ML18003A871
Person / Time
Site:	Harris
Issue date:	02/02/1983
From:	Zimmerman S CAROLINA POWER & LIGHT CO.
To:	Harold Denton Office of Nuclear Reactor Regulation
References
LAP-83-04, LAP-83-4, NUDOCS 8302070271
Download: ML18003A871 (10)

Text

REGULATO INFORMATION DISTRIBUTION TEM (RIOS) r AGCESSION NBR;8302070271 DOC,DATE: 83/02/Q2 NOTARIZED: NO DOCKET FACIL:50-400 Shearon Har,ris Nuclear Power Plant~ Uni,t 1~ Carolina 05000400 50 401 Shear on Harr is Nuclear power Planti Unit 2r Car olina 05000401 AUTH ~ NAME AUTHOR AFFILIATION ZIMMERMAN<S,R~ Carolina Power L Light Co ~

~RECIP ~ NAME RECIPIENT AFF IL'IATION DENTONrH ~ R>> Office of Nuclear Reactor Regulationr Dir ector

SUBJECT:

Forwards three 'tables re filter isludge activity calculations (normal L design) F feed streams 'to vol reduct'ion >sys '(Unit 2 operation)gper,P Kadambi r equest -for =use in preparation of DES'ISTRIBUTION CODE: BQ01S,COPIES 'RECEI VEO: LTR,. g'NCL ~ O SIZE:..

TITLE: Licensing Submittal:,PSAR/FSAR Amdts 8 Related Correspondence NOTES:

RECIPIENT 'COPIES REC IP IENT COPIFS ID CODE/NAME LTTR ENCL ID CODE/NAME LT'TR ENCL NRR/OL/AOL 1 0 NRR LB3 BC 1 0 NRR LB3 LA 1 0 KADAMBIg P 01 1 1 INTERNAL>> ELD/HDSi 1 0 IE FILE 1 1 IE/DEP EPDS 35 1 IE/DEP/EPLB 36 3 3 NRR/DE/AEAB 1 0 NRR/DE/CEB 11 1 1 NRR/DE/EQB 13 2 '2 NRR/DE/GB 28 2 2 NRR/DE/HGEB 30 1 1 NRR/DE/MEB 18 1 1 NRR/DE/MTEB 17 1 1 NRR/DE/QAB 21 1 1 NRR/OE/SAB 24 1 1 NRR/DE/SEB 25 1 1 NRR/DHFS/HFEB40 1 1 NRR/DHFS/LQB 32 1 1

.NRR/DHFS/OLB 34 1 1 NRR/DL/SSPB 1 0 NRR/DS I/AEB 26 1 1 NRR/DS I/ASB 1 1 NRR/DS I/CPB, 10 1 1 NRR/DSI/CSB 09 1 1 NRR/DSI/ICSB 16 1 NRR/DSI/METB 12 1 1 NRR/DSI/PSB 19 1 1 NRR DS I/RAB 22 1 1 NRR/DSI/RSB 23 1 1 EG FI 04 1 1 RGN2 3 5 3 RM AMI/MIB 1 0 EXTERNAL>> ACRS 41 6 BNL(AMOTS ONLY) 1 1 DMB/DSS (AMDTS) 1 1 FEMA REP DI V 39 1 1 LPDR 03 1 1 NRC PDR 02 1 1 NSIC 05 1 1 NTIS 1 1 TOTAL NUMBER OF COPIES REQUIRED: LTTR 53 ENCL 46

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CÃQE, Carolina Power 5 Light Company FFe s3 ]983 LAP-83-04 Mr. Harold R. Denton, Director Office of Nuclear Reactor Regulation United States Nuclear Regulatory Commission Washington, DC 20555 SHEARON HARRIS NUCLEAR POWER PLANT UNIT NOS. 1 AND 2 DOCKET NOS. 50-400 AND 50-401 SAFETY REVIEW QUESTION RESPONSE SUPPLEMENT

Dear Mr. Denton:

Carolina Power & Light Company (CP&L) hereby transmits one original and forty copies of the following three tables regarding activity inputs to the Volume Reduction System (VRS):

1. Filtex Sludge Activity Calculations (Normal)

2. Filter Sludge Activity Calculations (Design)

3. Feed Streams to the Volume Reduction System (2 Unit Operation)

These tables have been requested by your Mr. Prasad Kadambi for use in preparation of the Draft Environmental Statement (DES). We understand that data other than that supplied by our letter of December 13, 1982 is being used by the staff in calculating the activity levels of the volume reduction system output. Specifically, the decontamination factor of the volume reduction system and the selection of inputs to the volume reduction system are being based on extremely conservative assumptions made by the staff in the absence of detailed technical information on certain system processes. We are presently obtaining more test data to support the presently presented process information and trust that provision of the information will allow the staff Iyol 8QQQ02 > lto asmo7O~"~OSOOos<O DR @DOCK pQR 9

411 Fayetteville Street o P. O. Box 1551 o Raleigh, N. C. 27602

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H. R. Denton to revise their assessment of the volume reduction system and to subsequently revise the activity inputs for use in the Final Environmental Statement.

Please contact my staff if you have any questions.

Yours very truly, S. immerman Manager Licensing 6 Permits JDK/pgp (6094C9T5)

CC: Mr. N. Prasad 1hdambi (NRC) Mr. Wells Eddleman Mr. G. F. Maxwell (NRC-SHNPP) Dr. Phyllis Lotchin Mr. J. P. O'Reilly (NRC-RIX) Ms. Patricia T. Newman Mr. Travis Payne (KUDZU) Mr. John D. Runkle Mr. Daniel F. Read (CHANGE/ELP) Dr. Richard D. Wilson Chapel Hill Public Library Mr. G. 0. Bright (ASLB)

Wake County Public Library Dr. J. H. Carpenter (ASLB)

Mr. J. L. Ihlley (ASLB)

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0 FILTER SLUDGE ACTIVITY CALCULATIONS (NOMOLL)

TASLE 1 Filter. Syatea Particulate Activity uCi/cc Diasolved Activity uCi/cc Hssa of I-131 I-133 Co-SS Co-60 Ca 134 Ca-137 I-131 I-133 Co-58 Co-60 Ca>>134 Cs-137 ~Li ulema}

Spent Raain Sluice 1.26(0) 2.06(-l) 6.53(-1) 2.75(-1) 1.83(0) 1.49(0) 2.86(-1) 4 18( 1) 68( 2) 2o10( 3) 2.63( 2) 90( 2) 179(7) filtat 1 1 3 Fuel Pool Ski~t 2+16(1) 2.74(0) 1.90(-5) 2.70(-5) 1. 10(-6) 1.40(-7) 1.70(-6) 1.20(-6) 9.536(7)

Piltet Rafualinb Mater 6.99 (0) 8.90(-1) 1.90(-5) 2.70(-S) 1.10(-6) 1.40(-7) 1.70(-6) 1.20(-6) I 590(8) filter o Naate Evaporator 1.33(-2) 2. 35(-3) 6.73(-5) 3.29(-7) 1.34(-6) 2.08(-7) 2.57(-6) 4.92(-7) J.059(6)

Condenaata filter Seal Qatar Retutn 2o60(2) 3o40(l) 2.86(-1) 4.18(-1) 1.68(-2) 2.10(-3) 2.63(-2) 1.90(-2) 6.352(6)

Piltet Seal qatar 1.90(2) 2.54(1) 2.86(-1) 4.18(-1) 1.68(-2) 2.10(-3) 2.63(-2) 1e90(-2) 4.533(6)

In]ection filter

,Recycle Evaporatot 1.14(-2) 5.80(-2) 2.86(-2) 4.18(-2) 1.68(-3) 2.10("4) 2.63(-3) 1.90(-3) 1.276(6)

Peed Filter Recycle Evaporator 3.86(-4) 6.58(-5)

Condensate Filter 1.059(6)'.39(-2)

Recycle Evaporator 8.48(0) 3.02(0) 9.68(-1) 7.10(-1) 6.62(-1) 6.61(-1) 4 ~ 68(-2) 7.953(6)

Concentrate Iilter boric Acid filter 2.55(0) 1,81(0) 3.08(-1) 3.41(-1) 6.62(-1) 6.61(-1) 6.39(-2) 4.68(-2) 6.357(7)

Caa Decay Tark 3.99("1)

Pilter 7.953(6)

Reactor Coolan.t Pilter 6.71( 1) 8.40(0) 2 '6( I) 4 18( 1) 1 68( 2) 2 10( 3) 2 '3( 2) 1 ~ 90( 2) 6 '57(7) fuel Pool Piltet 2.45(-l) 1.43(-2) 1,79(-3) 1.77(-2) 8.99(-3) 1.90(-5) 2.70(-5) 1.10(-6) 1.40(-7) 1.70(-6) 1.20(W) 1.S74(8)

Secondaty Maa e 1.14(-4) 1.43(-5) 2.43(-6) 3.18(-6) 1.42(-7) 1.77(-8) 2.23(-7) 1.61(-7) 6.357(7)

Filter Maate Evaporator 4.03( I) 9.32(0) 1.08(-2) 2.08(-3) 2.57(-2)

Filter 73( 2) 1 ~ 34(-2) 1 ~ 90(-2) 1.059(7)

Laundty 4 Hot 9.46(-3) 2.19(-2) 1.45(-5) 3.86(-6)

Shover Filter 9.17(-7) 6 ~ 30(-6) 2~ 10(-5) 3~ 179(7)

Ploor Dra1,n 1.59(0) 2.20(-1) 1.46(-4) 1.82(-3) 1.33(-3)

Piltet 8.97(-3) 1.66(-3) 1.06(-3) 1.589(8)

FILTER SLUDGE ACTIVITY CALCULATIONS (DESIGN)

TABLE 2 Filter Systea Spent Resin Sluice I-131 1,26(l)

I-133 2,06(Q)

Particulate Activity uCi/cc 3

Co-58

'4(-1)

Co-60 1.49(-1) 7 Cs-134

'9(Q)

Cs-137 6.33(p)

I-131 2.90(0)

I-133 4.30(0)

Dissolved Co-58 1.5(-2)

Activity uCI/cc Co-60 I 9p( 3) 2 Cs 134

'0(0)

Ca-1 37 I,SO(0)

Hsss

~Ll ul 3,179(7) l~of tilter Fuel Pool Ski~r 2epl(l) 2,45(Q) 1.90(-4) 2.80(-4) 1.00(-6) 1.30(-6) I Sp( 4) 1.00(-3) 9 536(7)

Pilter Rsfuelinb Mater 6.53(0) 7.95(-1) 1.90(-4) F 80(-4) 1.00(-6) 1.30(-6) 1.50(-4) 1.00(>>3) 1.590(8)

Pilter Waste Fvaporator. 1.18(-2) 2.13(-3) 6.82(-4) I 11(-4)

~ 1. 19(-6) 1. 88(-7) 2.25(-4) 1. 50(-4) 1.059(6)

Condensate Pilter Seal Mater Return 2 32(2) 3.07(1) 2.90(0) 4.30(0) 1.50(-2) 1.90(-3) 2.30(0) 1.50(0) 6.352(6)

Pilter Seal Mater 1 70(2) 2 ~ 30(1) 2.90(0) 4.30(0) 1.50(-2) 1+90(-3) 2.30(0) 1.50(0) 4.533(6)

In)ection Filter Recycle Evaporator 1.16(-1) 5.07(0) 2.90(-1) 4.30(-1) 1.50(-3) 1.90(-4) 2.30(-1) 1o$ 0(-I) 1.276(6)

Feed Pilter Recycle Evaporator 3.91(-3) 6. 78(-4) 1.059(6)

Condensate Pilter Recycle Evaporator 8.58(1) 3.10(1) 8.48(1) 5.62(1) 6.70(0) 6.80(0) 5.60(0) 3+70(0) 7.953(6)

Concentrate Filter boric Acid Filter 2.58(1) 2.03(1) 2.69(1) 2.69(1) 6.70(0) 6.80(0) . 5.60(0) 3.70(0) 6o 357(7)

Gas Decay Tank 3.48(1) 7.953(6)

Filter Reactor Coolant 6.00(1) 7.63(0) 2 ~ 90(0) 4 ~ 30(0) I 50( 2) I 90( 3) 2 ~ 30(0) 1 ~ 50(0) 6 357(7)

Pilter I'll(p) 7.37(-1) 1.90( 4) F 80( 4) I 00( 6) I ~ 30( 6) I 50(H) lapp( 3) I S74(8)

Fuel Pool Pilter 2.45(0) 3.35(p) 1.33(-2) 1.61(-3)

Secondary Masts 1.02(-4) 1.29(-5) 2.47(-S) 3.28("5) 1.27(-7) 1.61(-8) 1.95(-5) 1.27(-5) 6.357(7)

Filter Masts Evaporator 3.64(1) 8.44(0) 6.82(-1) 1.11(-1) 1.19(-2) 1.88(-3) 2.25(0) 1.50(0) 1.059(7)

Filter s Laundry 4 Hot 2.47(-2) 5.65(-2) 2.39(-6) 1.65(-5) 3.78(-5) $ .48(-5) 1.01(-4) 3.179(7)

Shaver Pilter Floor Drain .1.42(0) 2.00(-1) 9.09(-2) 1.71(-2) 9.44(-4) 1.32(-4) 1.59(-l) 1+71(-2) 1.589(8)

Pilter

TABLE 3 FEED STREAMS TO THE UOLUME REDUCTION SYSTEM (2 UNIT OPERATION)

Filter'kWash Waste RO SW BRS Evap Evap Evap Evap Mass (Kg/yr) 2.23(+5) 9.67(+3) 7. 29 (+4) 3.18(+5) 5.81(+4)

Radfonuclfde (Cl/yr) NORMAL OPERATION Co-58 zoo (4) 9. 67 (-1) 5. 24 (-1) 6.64(-1} 0.0 Co-60 l. 41(3) 1. 51(-1) 7.95(-2) 8.33(-2) 0.0 I-131 3. 30(2) 4.87(+1) 4.33(+1) 1.09(+1) 3.89(+1)

I-133 1 ~ 73(2) 7.8O(+O} 6.7O(+O) 1.14(+1) 3.95(+1)

Cs-134 S.aO(1) 1. 87 (+1) 9.12(+0) 1. 05 (+Q) 3.25(+1)

Cs-137 7. 15(1) 1.37(+1) 6.76(+0) 7.53(-1) 2.15(+1}

DESIGN BASIS Co-58 9.64(3) 8. 64 (-1) 4.73(-1) l. 19 (+0) 0.0 Co-6Q 1.27(3) 1. 36 (-1) 8'. 54 (-2) 1.51(-1) 0.0 I-131 3. 92(3) 4.94(+2) 4. 39(+2) 2.21(+2) 3. 89 (+2)

I-133 3. OS(3) 8.02(+1) 6'.92(+1) 2.35(+2) 3.95(+2)

Cs-134 3. 7S(3) 1.63(+3) 7.88(+2) 1.83(+2) 3 '5(+2)

Cs-137 2. 91(3) 1.08(+3) 5.18(+2) 1.19(+2) 2.15(+2)

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