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{{#Wiki_filter: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 ~
{{#Wiki_filter:REGULATO INFORMATION DISTRIBUTION TEM (RIOS) r AGCESSION NBR;8302070271 DOC,DATE: 83/02/Q2 NOTARIZED:
  ~RECIP ~ NAME                     RECIPIENT AFF IL'IATION DENTONrH ~ R>>                     Office of Nuclear Reactor Regulationr Dir ector
NO FACIL:50-400 Shearon Har,ris Nuclear Power Plant~
Uni,t 1~ Carolina 50 401 Shear on Harr is Nuclear power Planti Unit 2r Car olina 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 DOCKET 05000400 05000401


==SUBJECT:==
==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:..
Forwards three 'tables re filter isludge activity calculations (normal L design)
TITLE: Licensing Submittal:,PSAR/FSAR Amdts                       8 Related Correspondence NOTES:
F feed streams 'to vol reduct'ion >sys '(Unit 2 operation)gper,P Kadambi r equest -for =use in preparation of DES'ISTRIBUTION CODE:
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
BQ01S,COPIES
            .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
'RECEI VEO: LTR,. g'NCL ~ O SIZE:..
TITLE: Licensing Submittal:,PSAR/FSAR Amdts 8 Related Correspondence NOTES:
RECIPIENT ID CODE/NAME NRR/OL/AOL NRR LB3 LA INTERNAL>> ELD/HDSi IE/DEP EPDS 35 NRR/DE/AEAB NRR/DE/EQB 13 NRR/DE/HGEB 30 NRR/DE/MTEB 17 NRR/OE/SAB 24 NRR/DHFS/HFEB40
.NRR/DHFS/OLB 34 NRR/DS I/AEB 26 NRR/DS I/CPB, 10 NRR/DSI/ICSB 16 NRR/DSI/PSB 19 NRR/DSI/RSB 23 RGN2 EXTERNAL>>
ACRS 41 DMB/DSS (AMDTS)
LPDR 03 NSIC 05
'COPIES LTTR ENCL 1
0 1
0 1
0 1
1 0
2
'2 1
1 1
1 1
1 1
1 1
1 1
1 1
1 1
1 1
1 1
3 5 3 6
1 1
1 1
1 1
REC IP IENT ID CODE/NAME NRR LB3 BC KADAMBIg P 01 IE FILE IE/DEP/EPLB 36 NRR/DE/CEB 11 NRR/DE/GB 28 NRR/DE/MEB 18 NRR/DE/QAB 21 NRR/DE/SEB 25 NRR/DHFS/LQB 32 NRR/DL/SSPB NRR/DS I/ASB NRR/DSI/CSB 09 NRR/DSI/METB 12 NRR DS I/RAB 22 EG FI 04 RM AMI/MIB BNL(AMOTS ONLY)
FEMA REP DIV 39 NRC PDR 02 NTIS COPIFS LT'TR ENCL 1
0 1
1 1
1 3
3 1
1 2
2 1
1 1
1 1
1 1
1 1
0 1
1 1
1 1
1 1
1 1
1 1
0 1
1 1
1 1
1 1
1 TOTAL NUMBER OF COPIES REQUIRED:
LTTR 53 ENCL 46


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C&#xc3;QE, 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
C&#xc3;QE, 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:==
==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 asmo7O~"~OSOOos<O 8QQQ02 DR @DOCK pQR 9
Iyol
> lto 411 Fayetteville Street o P. O. Box 1551 o Raleigh, N. C. 27602


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):
~ I re p
: 1. Filtex    Sludge      Activity Calculations (Normal)
L~ (4 g)$
: 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
 
                        ~I re p
L~
(4 g)$ ~
Y 1
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Line 49: Line 110:


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.
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.
Please contact my staff if you have any questions.
Yours very truly, S. immerman Manager Licensing 6 Permits JDK/pgp   (6094C9T5)
Yours very truly, S.
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)
immerman Manager Licensing 6 Permits JDK/pgp (6094C9T5)
Wake County Public Library              Dr. J. H. Carpenter (ASLB)
CC:
Mr. N. Prasad 1hdambi (NRC)
Mr. G. F. Maxwell (NRC-SHNPP)
Mr. J.
P. O'Reilly (NRC-RIX)
Mr. Travis Payne (KUDZU)
Mr. Daniel F.
Read (CHANGE/ELP)
Chapel Hill Public Library Wake County Public Library Mr. Wells Eddleman Dr. Phyllis Lotchin Ms. Patricia T.
Newman Mr. John D. Runkle Dr. Richard D. Wilson Mr. G. 0. Bright (ASLB)
Dr. J.
H. Carpenter (ASLB)
Mr. J. L. Ihlley (ASLB)
Mr. J. L. Ihlley (ASLB)


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0 FILTER SLUDGE ACTIVITY CALCULATIONS (NOMOLL)
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}
TASLE 1
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)
Filter. Syatea I-131 Particulate ActivityuCi/cc I-133 Co-SS Co-60 Ca 134 Ca-137 I-131 Diasolved Activity uCi/cc Hssa of I-133 Co-58 Co-60 Ca>>134 Cs-137
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)
~Li ulema}
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)
Spent Raain Sluice 1.26(0) filtat 2.06(-l) 6.53(-1) 2.75(-1) 1.83(0) 1.49(0) 2.86(-1) 4 18(
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)
1) 1 68( 2) 2o10(
In]ection  filter
3) 2.63( 2) 1 90( 2) 3 179(7)
,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)
Fuel Pool Ski~t Piltet Rafualinb Mater filter Naate Evaporator Condenaata filter Seal Qatar Retutn Piltet Seal qatar In]ection filter
Peed  Filter Recycle Evaporator 3.86(-4)    6.58(-5)
,Recycle Evaporatot Peed Filter 1.14(-2) 2+16(1) 2.74(0) 6.99 (0) 8.90(-1) 1.33(-2)
Condensate   Filter                                                                                                                                   1.059(6)'.39(-2)
: 2. 35(-3) 2o60(2) 3o40(l) 1.90(2) 2.54(1) 5.80(-2) 1.90(-5) 2.70(-5)
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)
: 1. 10(-6) 1.40(-7) 1.70(-6) 1.20(-6) 9.536(7) 1.90(-5) 2.70(-S) 1.10(-6) 1.40(-7) 1.70(-6) 1.20(-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)
I o 590(8) 6.73(-5) 3.29(-7) 1.34(-6) 2.08(-7) 2.57(-6) 4.92(-7)
Caa Decay  Tark                                                3.99("1)
J.059(6) 2.86(-1) 4.18(-1) 1.68(-2) 2.10(-3) 2.63(-2) 1.90(-2) 6.352(6) 2.86(-1) 4.18(-1) 1.68(-2) 2.10(-3) 2.63(-2) 1e90(-2) 4.533(6) 2.86(-2) 4.18(-2) 1.68(-3) 2.10("4) 2.63(-3) 1.90(-3) 1.276(6)
Pilter                                                                                                                                                7.953(6)
Recycle Evaporator 3.86(-4)
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)
Condensate Filter Recycle Evaporator 8.48(0)
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)
Concentrate Iilter 6.58(-5) 3.02(0) 9.68(-1) 7.10(-1) 6.62(-1) 6.61(-1) 1.059(6)'.39(-2) 4 ~68(-2) 7.953(6) boric Acid filter 2.55(0) 1,81(0)
Filter Maate Evaporator                         4.03( I)   9.32(0)                                   1.08(-2)               2.08(-3) 2.57(-2)
Caa Decay Tark Pilter 3.08(-1) 3.41(-1) 6.62(-1) 6.61(-1) 3.99("1) 6.39(-2) 4.68(-2) 6.357(7) 7.953(6)
Filter                                                                                73( 2)             1 ~ 34(-2)                       1 ~ 90(-2) 1.059(7)
Reactor Coolan.t Pilter 6.71( 1) 8.40(0) 2'6( I) 4 18(
Laundty 4 Hot                            9.46(-3)   2.19(-2)                                                         1.45(-5)             3.86(-6)
1) 1 68( 2) 2 10( 3) 2'3( 2) 1 ~90( 2) 6 '57(7) fuel Pool Piltet 2.45(-l)
Shover Filter                                                                      9.17(-7)             6 ~ 30(-6)           2~ 10(-5)             3~               179(7)
Secondaty Maa e Filter 1.43(-2) 1.14(-4) 1,79(-3) 1.43(-5) 1.77(-2) 8.99(-3) 1.90(-5) 2.43(-6) 2.70(-5) 3.18(-6) 1.10(-6) 1.42(-7) 1.40(-7) 1.77(-8) 1.70(-6) 2.23(-7) 1.20(W) 1.S74(8) 1.61(-7) 6.357(7)
Ploor  Dra1,n                            1.59(0)    2.20(-1)                                                         1.46(-4) 1.82(-3)   1.33(-3)
Maate Evaporator Filter Laundty 4 Hot Shover Filter Ploor Dra1,n Piltet 4.03( I) 9.32(0) 9.46(-3) 2.19(-2) 1.59(0) 2.20(-1) 73( 2) 1.08(-2) 1 ~ 34(-2) 2.08(-3) 2.57(-2) 1 ~90(-2) 1.059(7) 9.17(-7) 6 ~ 30(-6) 1.45(-5) 2 ~ 10(-5) 3.86(-6) 3 ~ 179(7) 8.97(-3) 1.66(-3) 1.06(-3) 1.46(-4) 1.82(-3) 1.33(-3) 1.589(8)
Piltet                                                                              8.97(-3)  1.66(-3)   1.06(-3)                                   1.589(8)


FILTER SLUDGE ACTIVITY CALCULATIONS (DESIGN)
FILTER SLUDGE ACTIVITY CALCULATIONS (DESIGN)
TABLE 2 Filter Systea Spent Resin Sluice I-131 1,26(l)
TABLE 2 Filter Systea Particulate ActivityuCi/cc I-131 I-133 Co-58 Co-60 Cs-134 Dissolved Activity uCI/cc Cs-137 I-131 I-133 Co-58 Co-60 Cs 134 Hsss of Ca-1 37
I-133 2,06(Q)
~Ll ull~
Particulate Activity uCi/cc 3
Spent Resin Sluice 1,26(l) tilter 2,06(Q) 3'4(-1) 1.49(-1) 7'9(Q) 6.33(p) 2.90(0) 4.30(0) 1.5(-2)
Co-58
I 9p( 3) 2'0(0)
                                            '4(-1)
I,SO(0) 3,179(7)
Co-60 1.49(-1) 7 Cs-134
Fuel Pool Ski~r Pilter Rsfuelinb Mater Pilter Waste Fvaporator.
                                                                    '9(Q)
Condensate Pilter Seal Mater Return Pilter Seal Mater In)ection Filter Recycle Evaporator Feed Pilter 1.16(-1) 2epl(l) 2,45(Q) 6.53(0) 7.95(-1) 1.18(-2) 2.13(-3) 2 32(2) 3.07(1) 1 70(2) 2 ~ 30(1) 5.07(0) 1.90(-4) 2.80(-4) 1.00(-6) 1.30(-6)
Cs-137 6.33(p)
I Sp( 4) 1.00(-3) 9 536(7) 1.90(-4)
I-131 2.90(0)
F 80(-4) 1.00(-6) 1.30(-6) 1.50(-4) 1.00(>>3) 1.590(8) 6.82(-4)
I-133 4.30(0)
I ~ 11(-4)
Dissolved Co-58 1.5(-2)
: 1. 19(-6)
Activity uCI/cc Co-60 I 9p( 3)   2 Cs 134
: 1. 88(-7) 2.25(-4)
                                                                                                                                        '0(0)
: 1. 50(-4) 1.059(6) 2.90(0) 4.30(0) 1.50(-2) 1.90(-3) 2.30(0) 1.50(0) 6.352(6) 2.90(0) 4.30(0) 1.50(-2) 1+90(-3) 2.30(0) 1.50(0) 4.533(6) 2.90(-1) 4.30(-1) 1.50(-3) 1.90(-4) 2.30(-1) 1o$0(-I) 1.276(6)
Ca-1 37 I,SO(0)
Recycle Evaporator 3.91(-3)
Hsss
: 6. 78(-4)
                                                                                                                                                          ~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)
Condensate Pilter 1.059(6)
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)
Recycle Evaporator Concentrate Filter boric Acid Filter Gas Decay Tank Filter 8.58(1) 3.10(1) 2.58(1) 2.03(1) 8.48(1) 5.62(1) 6.70(0) 6.80(0) 2.69(1) 2.69(1) 6.70(0) 6.80(0) 3.48(1) 5.60(0) 3.70(0) 6o 357(7) 7.953(6) 5.60(0) 3+70(0) 7.953(6)
Pilter Waste Fvaporator.                        1.18(-2)      2.13(-3)                        6.82(-4) I 11(-4)
Reactor Coolant Pilter Fuel Pool Pilter 2.45(0) 3.35(p)
                                                                                                    ~          1. 19(-6)   1. 88(-7) 2.25(-4) 1. 50(-4) 1.059(6)
Secondary Masts Filter Masts Evaporator Filter Laundry 4 Hot Shaver Pilter Floor Drain Pilter 6.00(1) 7.63(0) 1.33(-2) 1.02(-4) 1.61(-3) 1.29(-5) 3.64(1) 8.44(0) 2.47(-2) 5.65(-2)
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)
.1.42(0) 2.00(-1) 2.39(-6) s 1.65(-5) 3.78(-5)
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)
$.48(-5) 1.01(-4) 3.179(7) 9.09(-2) 1.71(-2) 9.44(-4) 1.32(-4) 1.59(-l) 1+71(-2) 1.589(8) 2 ~ 90(0) 4 ~ 30(0)
In)ection Filter Recycle Evaporator 1.16(-1)                                      5.07(0)              2.90(-1) 4.30(-1)     1.50(-3)   1.90(-4)   2.30(-1) 1o$ 0(-I) 1.276(6)
I 50( 2)
Feed  Pilter Recycle Evaporator 3.91(-3) 6. 78(-4)                                                                                                                     1.059(6)
I 90( 3) 2 ~ 30(0) 1 ~50(0) 6 357(7)
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)
I'll(p) 7.37(-1) 1.90( 4)
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)
F 80( 4)
Gas Decay Tank                                                  3.48(1)                                                                                  7.953(6)
I 00( 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)
I ~ 30( 6)
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)
I 50(H) lapp( 3)
Fuel Pool  Pilter  2.45(0)  3.35(p)      1.33(-2)      1.61(-3)
I S74(8) 2.47(-S) 3.28("5) 1.27(-7) 1.61(-8) 1.95(-5) 1.27(-5) 6.357(7) 6.82(-1) 1.11(-1) 1.19(-2) 1.88(-3) 2.25(0) 1.50(0) 1.059(7)
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)
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)
Mass (Kg/yr)
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)
Filter'kWash 2.23(+5)
I-133              1 ~ 73(2)         7.8O(+O}          6.7O(+O)             1.14(+1)   3.95(+1)
Waste Evap 9.67(+3)
Cs-134              S.aO(1)           1. 87 (+1)       9.12(+0)             1. 05 (+Q) 3.25(+1)
RO Evap
Cs-137            7. 15(1)         1.37(+1)         6.76(+0)            7.53(-1)   2.15(+1}
: 7. 29 (+4)
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)
SW Evap 3.18(+5)
I-133              3. OS(3)         8.02(+1)         6'.92(+1)           2.35(+2)   3.95(+2)
BRS Evap 5.81(+4)
Cs-134              3. 7S(3)         1.63(+3)           7.88(+2)           1.83(+2)   3 '5(+2)
Radfonuclfde (Cl/yr)
Cs-137              2. 91(3)        1.08(+3)          5.18(+2)             1.19(+2)   2.15(+2)
Co-58 Co-60 I-131 I-133 Cs-134 Cs-137 zoo (4) l.41(3)
: 3. 30(2) 1 ~ 73(2)
S.aO(1)
: 7. 15(1)
NORMAL OPERATION
: 9. 67 (-1)
: 1. 51(-1) 4.87(+1) 7.8O(+O}
: 1. 87 (+1) 1.37(+1)
: 5. 24 (-1) 7.95(-2) 4.33(+1) 6.7O(+O) 9.12(+0) 6.76(+0) 6.64(-1}
8.33(-2) 1.09(+1) 1.14(+1)
: 1. 05 (+Q) 7.53(-1) 0.0 0.0 3.89(+1) 3.95(+1) 3.25(+1) 2.15(+1}
Co-58 Co-6Q I-131 I-133 Cs-134 Cs-137 9.64(3) 1.27(3)
: 3. 92(3)
: 3. OS(3)
: 3. 7S(3)
: 2. 91(3)
DESIGN BASIS
: 8. 64 (-1)
: 1. 36 (-1) 4.94(+2) 8.02(+1) 1.63(+3) 1.08(+3) 4.73(-1) 8'. 54 (-2)
: 4. 39(+2) 6'.92(+1) 7.88(+2) 5.18(+2)
: l. 19 (+0) 1.51(-1) 2.21(+2) 2.35(+2) 1.83(+2) 1.19(+2) 0.0 0.0
: 3. 89 (+2) 3.95(+2) 3'5(+2) 2.15(+2)


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Latest revision as of 07:37, 7 January 2025

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 FACIL:50-400 Shearon Har,ris Nuclear Power Plant~

Uni,t 1~ Carolina 50 401 Shear on Harr is Nuclear power Planti Unit 2r Car olina 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 DOCKET 05000400 05000401

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 ID CODE/NAME NRR/OL/AOL NRR LB3 LA INTERNAL>> ELD/HDSi IE/DEP EPDS 35 NRR/DE/AEAB NRR/DE/EQB 13 NRR/DE/HGEB 30 NRR/DE/MTEB 17 NRR/OE/SAB 24 NRR/DHFS/HFEB40

.NRR/DHFS/OLB 34 NRR/DS I/AEB 26 NRR/DS I/CPB, 10 NRR/DSI/ICSB 16 NRR/DSI/PSB 19 NRR/DSI/RSB 23 RGN2 EXTERNAL>>

ACRS 41 DMB/DSS (AMDTS)

LPDR 03 NSIC 05

'COPIES LTTR ENCL 1

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REC IP IENT ID CODE/NAME NRR LB3 BC KADAMBIg P 01 IE FILE IE/DEP/EPLB 36 NRR/DE/CEB 11 NRR/DE/GB 28 NRR/DE/MEB 18 NRR/DE/QAB 21 NRR/DE/SEB 25 NRR/DHFS/LQB 32 NRR/DL/SSPB NRR/DS I/ASB NRR/DSI/CSB 09 NRR/DSI/METB 12 NRR DS I/RAB 22 EG FI 04 RM AMI/MIB BNL(AMOTS ONLY)

FEMA REP DIV 39 NRC PDR 02 NTIS COPIFS LT'TR ENCL 1

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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 asmo7O~"~OSOOos<O 8QQQ02 DR @DOCK pQR 9

Iyol

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

~ I re p

L~ (4 g)$

~

Y 1

d I

p

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. G. F. Maxwell (NRC-SHNPP)

Mr. J.

P. O'Reilly (NRC-RIX)

Mr. Travis Payne (KUDZU)

Mr. Daniel F.

Read (CHANGE/ELP)

Chapel Hill Public Library Wake County Public Library Mr. Wells Eddleman Dr. Phyllis Lotchin Ms. Patricia T.

Newman Mr. John D. Runkle Dr. Richard D. Wilson Mr. G. 0. Bright (ASLB)

Dr. J.

H. Carpenter (ASLB)

Mr. J. L. Ihlley (ASLB)

8, O

4 P

ll t

.r C

0 FILTER SLUDGE ACTIVITY CALCULATIONS (NOMOLL)

TASLE 1

Filter. Syatea I-131 Particulate ActivityuCi/cc I-133 Co-SS Co-60 Ca 134 Ca-137 I-131 Diasolved Activity uCi/cc Hssa of I-133 Co-58 Co-60 Ca>>134 Cs-137

~Li ulema}

Spent Raain Sluice 1.26(0) filtat 2.06(-l) 6.53(-1) 2.75(-1) 1.83(0) 1.49(0) 2.86(-1) 4 18(

1) 1 68( 2) 2o10(

3) 2.63( 2) 1 90( 2) 3 179(7)

Fuel Pool Ski~t Piltet Rafualinb Mater filter Naate Evaporator Condenaata filter Seal Qatar Retutn Piltet Seal qatar In]ection filter

,Recycle Evaporatot Peed Filter 1.14(-2) 2+16(1) 2.74(0) 6.99 (0) 8.90(-1) 1.33(-2)

2. 35(-3) 2o60(2) 3o40(l) 1.90(2) 2.54(1) 5.80(-2) 1.90(-5) 2.70(-5)
1. 10(-6) 1.40(-7) 1.70(-6) 1.20(-6) 9.536(7) 1.90(-5) 2.70(-S) 1.10(-6) 1.40(-7) 1.70(-6) 1.20(-6)

I o 590(8) 6.73(-5) 3.29(-7) 1.34(-6) 2.08(-7) 2.57(-6) 4.92(-7)

J.059(6) 2.86(-1) 4.18(-1) 1.68(-2) 2.10(-3) 2.63(-2) 1.90(-2) 6.352(6) 2.86(-1) 4.18(-1) 1.68(-2) 2.10(-3) 2.63(-2) 1e90(-2) 4.533(6) 2.86(-2) 4.18(-2) 1.68(-3) 2.10("4) 2.63(-3) 1.90(-3) 1.276(6)

Recycle Evaporator 3.86(-4)

Condensate Filter Recycle Evaporator 8.48(0)

Concentrate Iilter 6.58(-5) 3.02(0) 9.68(-1) 7.10(-1) 6.62(-1) 6.61(-1) 1.059(6)'.39(-2) 4 ~68(-2) 7.953(6) boric Acid filter 2.55(0) 1,81(0)

Caa Decay Tark Pilter 3.08(-1) 3.41(-1) 6.62(-1) 6.61(-1) 3.99("1) 6.39(-2) 4.68(-2) 6.357(7) 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)

Secondaty Maa e Filter 1.43(-2) 1.14(-4) 1,79(-3) 1.43(-5) 1.77(-2) 8.99(-3) 1.90(-5) 2.43(-6) 2.70(-5) 3.18(-6) 1.10(-6) 1.42(-7) 1.40(-7) 1.77(-8) 1.70(-6) 2.23(-7) 1.20(W) 1.S74(8) 1.61(-7) 6.357(7)

Maate Evaporator Filter Laundty 4 Hot Shover Filter Ploor Dra1,n Piltet 4.03( I) 9.32(0) 9.46(-3) 2.19(-2) 1.59(0) 2.20(-1) 73( 2) 1.08(-2) 1 ~ 34(-2) 2.08(-3) 2.57(-2) 1 ~90(-2) 1.059(7) 9.17(-7) 6 ~ 30(-6) 1.45(-5) 2 ~ 10(-5) 3.86(-6) 3 ~ 179(7) 8.97(-3) 1.66(-3) 1.06(-3) 1.46(-4) 1.82(-3) 1.33(-3) 1.589(8)

FILTER SLUDGE ACTIVITY CALCULATIONS (DESIGN)

TABLE 2 Filter Systea Particulate ActivityuCi/cc I-131 I-133 Co-58 Co-60 Cs-134 Dissolved Activity uCI/cc Cs-137 I-131 I-133 Co-58 Co-60 Cs 134 Hsss of Ca-1 37

~Ll ull~

Spent Resin Sluice 1,26(l) tilter 2,06(Q) 3'4(-1) 1.49(-1) 7'9(Q) 6.33(p) 2.90(0) 4.30(0) 1.5(-2)

I 9p( 3) 2'0(0)

I,SO(0) 3,179(7)

Fuel Pool Ski~r Pilter Rsfuelinb Mater Pilter Waste Fvaporator.

Condensate Pilter Seal Mater Return Pilter Seal Mater In)ection Filter Recycle Evaporator Feed Pilter 1.16(-1) 2epl(l) 2,45(Q) 6.53(0) 7.95(-1) 1.18(-2) 2.13(-3) 2 32(2) 3.07(1) 1 70(2) 2 ~ 30(1) 5.07(0) 1.90(-4) 2.80(-4) 1.00(-6) 1.30(-6)

I Sp( 4) 1.00(-3) 9 536(7) 1.90(-4)

F 80(-4) 1.00(-6) 1.30(-6) 1.50(-4) 1.00(>>3) 1.590(8) 6.82(-4)

I ~ 11(-4)

1. 19(-6)
1. 88(-7) 2.25(-4)
1. 50(-4) 1.059(6) 2.90(0) 4.30(0) 1.50(-2) 1.90(-3) 2.30(0) 1.50(0) 6.352(6) 2.90(0) 4.30(0) 1.50(-2) 1+90(-3) 2.30(0) 1.50(0) 4.533(6) 2.90(-1) 4.30(-1) 1.50(-3) 1.90(-4) 2.30(-1) 1o$0(-I) 1.276(6)

Recycle Evaporator 3.91(-3)

6. 78(-4)

Condensate Pilter 1.059(6)

Recycle Evaporator Concentrate Filter boric Acid Filter Gas Decay Tank Filter 8.58(1) 3.10(1) 2.58(1) 2.03(1) 8.48(1) 5.62(1) 6.70(0) 6.80(0) 2.69(1) 2.69(1) 6.70(0) 6.80(0) 3.48(1) 5.60(0) 3.70(0) 6o 357(7) 7.953(6) 5.60(0) 3+70(0) 7.953(6)

Reactor Coolant Pilter Fuel Pool Pilter 2.45(0) 3.35(p)

Secondary Masts Filter Masts Evaporator Filter Laundry 4 Hot Shaver Pilter Floor Drain Pilter 6.00(1) 7.63(0) 1.33(-2) 1.02(-4) 1.61(-3) 1.29(-5) 3.64(1) 8.44(0) 2.47(-2) 5.65(-2)

.1.42(0) 2.00(-1) 2.39(-6) s 1.65(-5) 3.78(-5)

$.48(-5) 1.01(-4) 3.179(7) 9.09(-2) 1.71(-2) 9.44(-4) 1.32(-4) 1.59(-l) 1+71(-2) 1.589(8) 2 ~ 90(0) 4 ~ 30(0)

I 50( 2)

I 90( 3) 2 ~ 30(0) 1 ~50(0) 6 357(7)

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) 2.47(-S) 3.28("5) 1.27(-7) 1.61(-8) 1.95(-5) 1.27(-5) 6.357(7) 6.82(-1) 1.11(-1) 1.19(-2) 1.88(-3) 2.25(0) 1.50(0) 1.059(7)

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

Mass (Kg/yr)

Filter'kWash 2.23(+5)

Waste Evap 9.67(+3)

RO Evap

7. 29 (+4)

SW Evap 3.18(+5)

BRS Evap 5.81(+4)

Radfonuclfde (Cl/yr)

Co-58 Co-60 I-131 I-133 Cs-134 Cs-137 zoo (4) l.41(3)

3. 30(2) 1 ~ 73(2)

S.aO(1)

7. 15(1)

NORMAL OPERATION

9. 67 (-1)
1. 51(-1) 4.87(+1) 7.8O(+O}
1. 87 (+1) 1.37(+1)
5. 24 (-1) 7.95(-2) 4.33(+1) 6.7O(+O) 9.12(+0) 6.76(+0) 6.64(-1}

8.33(-2) 1.09(+1) 1.14(+1)

1. 05 (+Q) 7.53(-1) 0.0 0.0 3.89(+1) 3.95(+1) 3.25(+1) 2.15(+1}

Co-58 Co-6Q I-131 I-133 Cs-134 Cs-137 9.64(3) 1.27(3)

3. 92(3)
3. OS(3)
3. 7S(3)
2. 91(3)

DESIGN BASIS

8. 64 (-1)
1. 36 (-1) 4.94(+2) 8.02(+1) 1.63(+3) 1.08(+3) 4.73(-1) 8'. 54 (-2)
4. 39(+2) 6'.92(+1) 7.88(+2) 5.18(+2)
l. 19 (+0) 1.51(-1) 2.21(+2) 2.35(+2) 1.83(+2) 1.19(+2) 0.0 0.0
3. 89 (+2) 3.95(+2) 3'5(+2) 2.15(+2)

0 v

~.

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