Text

Attached Replacement & Revised Pages of Appendix I Submittal. Both the Releases and the Doses Have Changed Due to the Subject Modification
	ML18219D904
Person / Time
Site:	Cook
Issue date:	07/20/1977
From:	Tillinghast J; Indiana Michigan Power Co, (Formerly Indiana & Michigan Power Co)
To:	Case E; Office of Nuclear Reactor Regulation
References
	Download: ML18219D904 (26)
	v • d • e

U.S. NUCLEAR REGULATORY COM ION NRC FORM 195 (2 76I NRC DISTRIBUTION FoR PART 50 DOCKET MATERIAL DOCKET NUMBER FILE NUMBER Mr. E.

Case FROM: Indiana

& Mich Powe'r Co New York, NoY 10004 J. Tillinghast DATE OF DOCUMENT 7-20-77 D)TE )EAVED

%LETTER ORIGINAL C3 COP Y QIVOTORIZED JgUNC LASS IF I E D PROP INPUT FORM NUMBER OF COPIES RECEIVED ar6 DESCRIPTION Ltr notarized 7-20-77 furn addi inf on Appendix I & trans the following:

2P ENCLOSURE Replacement

& revised pages to the original submittal of Appendix I....

(1 cy encl rec')

llP PL ~ NAM 'onald C.

Cook Units 1 & 2 APPENDIX I DISTRIBUTION AFTER ISSUANCE OF A LICENSE

'5CKNO~KDGFD DHL 7-25 77 SAFETY BRANCH CHIEF:

PROJECT MANAGE LIC ASST:

NFORMATION FOR ACTION/I

(

RE R

PDR I&E OELD GOSSICK & STAFF BUTLER GRIMES DENTON LTR BALLARD AMMILL HULMAN MARKEE J.

COLLINS 2

KREGER VERDERY INTERNALD RI BUTION IST LPDR:

TIC ACRS EXTERNAL DISTRIBUTION CONTROL NUMBER 772060079

'A i/A NRC FORM 195 {2.76)

1

\\

INDIANA R MICHIGAN POWER COMPANY P. O. BOX 18 BO WL IN 6 G RE EH STAT ION NEW YORK, N. Y. 10004 duly 20, 1977 CO Donald C. Cook Nuclear Plant Unit Nos.

1 S

2 Docket Nos.

50-315 and 50-316 DPR No.

58 and CPPR No. 61 Rggg foot/

Mr. Edson G. Case, cting Da.rector Office of Nuclear Reactor Regulation U.S. Nuclear Regulatory Commission Washington, D.C.

20555

Dear Mr. Case:

The Appendix I calculations for the Donald C. Cook Nuclear Plant indicated that the total annual estimated liquid radioactive release, as conservatively calculated, could exceed the objective of the annex (Docket-RM-50-2) to Appendix I.

The cal-culated value of 6.4 curies per year, as compared to the objective of 5 curies, was found to be caused mainly by the release of radioactive cations to the circulating water system from the Steam Generator Blowdown Treatment System under the assumption that the steam generator tube leakage has occurred.

In order to reduce the projected liquid radioactive release to the environment. under the conservative assumptions, the Steam Generator Blowdown Treatment System in each unit will be modified.

The anion bed demineralizers are to be changed to mixed bed.

The liquid releases have been recalculated to reflect this modification and the total is now well below 5 curies per reactor per year.

772060079

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Mr. E. G. Case July 20, 977 Attached please find 40 copies of replacement pages 4, 21, 22, 23, 26, 27, 28, 98,

100, 101, and 103 for the original Appendix X submittal.

Both the releases and the doses have changed due to the subject modification.

Very truly yours, 1'g ast Vice President JT:mam Attachment Sworn and subscribed to before me on this Zo day of July 1977 in New York County, New York Notary Public KATHLEEN BARRY NOTARY t'UttUC, Steto ol New York No. 4W606i92 Qualitied in Queens County 4ttificnto tiled ln New York tsounttt Coninussru.

'rptrus (rturch 3it, l97$

cc:

G. Charnoff R. C. Callen P.

W. Steketee R. Walsh R. J. Vollen D. V. Shaller Bridgman R. S. Hunter

PI 0

I

(

r =g pt4 I I II 4

P 4

I 4r h ~

I

- Il4 4

~

II Ig P(

X K~Pt",I 4

I I'

Il Il I

.r,r S

4

'I lc '.

ez6 e zi ln'ae l fJ'l0 (JivlSSZQQl!;l Lll3li'f1000 03Al~338

bleed stream is based on plant experience.

Deaerated=.equipment drain waste is processed with the shim bleed stream.

The input rate for this stream was assumed to be about 5% of the shim bleed rate.

2. 3 Results Results from the GALE gas run are presented in Table 2. 3-1.

Note that discharge rates for argon-41 (25 Ci/yr) and carbon-14 (8 Ci/yr) have not been included in the GALE output.

These values are not cal-culated in the GALE code, but are specified in Regulatory Guide 1. 112 backup material.

The GALE code does not partition tritium, argon-41 and carbon-14 among discharge points, however, they are assumed to be discharged as ground releases along with all other effluents.

It is apparent from Table 2. 3-1 that the gaseous radwaste treatment system meets the discharge rate limitof the 10CFR50 Appendix I annex, 1

curie of I-131 per year per reactor.

Results from tlute GALE liquid run are given in Table 2. 3-2.

It is apparent from Table 2. 3-2 that the liquid radwaste treatment system meets discharge rate limits of the 10CFR50 Appendix I annex, 5 curies per year per reactor.

Table 1. 2-1 Comparison of Estimated Dos s ~vith Appends I Design Objectives Plant:

D. C. Cook Nuclear Plant Unit 1 or 2 Appendix I Reference Sec. ILA Effluent Liquid Applicable Organ Total body Estimated Doses (mr em/year)

0. 031 Appendix I Objective 3 mrem/reactor HN 50-2 Objective 5 mrem/site (total~

body or any organ)~

Sec. II.B.1 Noble Gas Any organ Air dose (y)

Air dose (B)

0. 059 1.7 4.7 10 mrem/reactor 10 mrad y/reactor 10 mrad y/site 20 mrad p/reactor 20 mrad P/site or Sec. Il.B.-2 Noble Gas Total body 0.9 5 xnrem/reactor 5 mrem/site Sec. II'C Skin Airborne Iodine Any organ and Particulate 2.6

5. 7(1) 15 mrem/reactor 15 mrem/site 15 mrem/reactor 15 mrem/site (1) Total. infant thyroid dose minus noble gas (plume) contribution

~

Table 2. 2-1 LiSting of GALE InPut CardS CARD capn chan CARD CARD CARn rARD TnsTFL CARD CARn

(:APD 10 11 1?.

13 14 CARO

(.'APJ)

CARD CARD CAPO CAPO CARD capn CARO 19

(.ARn CARD cARD CARO CAPn cARO capo CARO 27 CARD CARD CaRn CARO CARO CARO CARO CARD CARO CARD TAU3 CARO CARO CARO CARD CARO FVN FF.JP PFLAUN CARD CaRD CARD 45 OI UHN NUHRER

))))))))))?>?22?7?2?33333333334444444444555%55SSSS666F66666677777777778

]234567490]234S67890]?34567890]?34567490]?.'34S67890]234S67490]234567890]234567890 1

OONAI.D c conK IJNITS 1

OR 2

PWR

?

PnwTH THFPMAL PowER LFVEL (HFGbwhTTS) 3391

'cvnL MacS nF PPIMARY COOLANT (TMO~JSA"Ins LRS) 561.

LFTOWN PRI Ia>Y SYSTFM LETDOWN RATF (GPH) 7% ~

cRFLp I.ETnowN I.ATI0N DF'MINFpALI7FR F'LOw (GpM) 7 ~ 5 6

NOGGIN

<UH4FP OF STFAH GENFRATOPS 4 ~

7 TOT hl STFAM FLOW (MII LION I.RS/HR) 14 ~ 7 8

WST MASS nF STE AM IN EACH STFA< liENERATO>

(THnlJSAND LOS) 6 ~ 5S WLI PASS nF LIQIJID IN Ear4 STFAM GENFRATnR (THOUSAND L8S)

]4.7 TMSC TOTAL MASS OF SECONDARY cnnLANT (THOI)SAND LRS) 2100 ~

8I WDWN PLOWDnWN-THOU L8/HR 36 'LOWOOWN TREATMENT-INPUT Oe]onR?.

0 RFGFNT CONDFNSATE DEMINFRALI7FR PFGFNFRATION FRFnlJENCY (DAYS) 0 ~

FFCOM CONDF~SATF.

DFHINFRALI7fR FLOW FRACTInN 0 ~

OILUT RADWASTE DILUTION FLO'4 (THnU )AND GPH) 745 ~

15 SHI!I RLEFD RATF.

) 6200 ~

GPO 16 nFI 1

E40FCS

?

ESDEO

].f5 17 coLLFrTION 7 ~ 5 DAYs ppncEss 1

4 DAYs FpAcT DIscH 0

]

18 DEAFR E()IJIP ORAININPIJT 810 GPn AT 1

0 PCA nFI 1 oE3DFCS

] oE<nfo 1 ~ E4

?O' COLI.ECTION 7 ~ 5 DAYS PPOCESS 1,4 DAYS F PACT DISCH 0 ~ I CLEAN 'WASTE 4?5o 0,]8 2?.

DFI, 1.F30FCS 1 ~ F4ncn 1

E4 23 coLI FcTIoN ll ~ 6 ohvs ppncEss 0.

Davs FRACT DIsc4

?4 DIRTY WASTF INPUT 9SO

~

GPD AT 0 ~ 026 PCA 25 DFI

) ~ E30FCS 1

E40FO 1

E4 26 COLl.F.'rTION 5.2 DAYS PPnCFSS 0.

DAYS FRACT DISCH RLOWOnWN FRACTION PPOCESSFn l.

28 OEI 1 ~ E40FCS 1 ~ E30FO loE4

?.9 COLt.ECTION 0 ~

DAYS PROCESS 0 ~ 007 DAYS FRACT OISCH 1 ~ 0 30 RFGENERANT fLOW RATF.

GPn 0 ~

31

" "'FI 1, nfCS 1, nfn 1 ~

'?.

coLI.ErTIDN 0 ~

DAYs PPOCEss 0 ~

DAYc'RArT DIscH 0 ~

33 GAS STP IPP ING O=NONF.

1=FIJLL LETDOWN STR IPP ING 2-"VFNT Tn VCT 0

34 TAU]

HOLDU> TIMF. FOR XENON (DAYS) 90

'S TAU2 HOLDU> TIMF. FOR KRYJ'TON (nhYS) 90.

3c FILL TIHF.

OF DECAY TANKS FOR THE GAS STRI>PER (DAYS) 0 ~

37 GAS WhSTF'YSTEH HEPA YES ENTER YFS OR LF'AVF. 8LANK 38 AUXILIARY BLDG CHARCOAL HEPA YFS YFS OR LFAVE ALANK 39 CONVOL CONTAIN"IFNT VOLUHE (MILLIO'I CU FT) 1,]4 40 CFH CONT A INHFNT ATHOSPHFRE CI. F hNIJP RATF (THOI)SANO CFM)

] h ~

41 CNTMT-SHIJTOOWN PURGF.

CHAPCnAL HFPA YES YFS OR LFAVE 8LNK 36 4?

CNTMT-NAPMAL PURGE RhTf(l FM) 0 ~

CHARrnAL HEPA YFS OR 43 FRACTION IODINE RFLEASED FROM 8LOWDOWN TANK VFNT 0 ~

44 FRAcTIDN 100INE RELEAsED FROM MAIN cnNDENsFR AIR FJFcT 1

0 DETERGENT WASTF.

OECON FACTOR

, lo0

~ ~

Table 2. 3-1 CALZ Gas Results DONALD C COOK UNITS 1

OR 2'HERHAL POWER LEvEL (HEGawaTTS)

PLANT CAPACITY FACTOR HASS OF PPIHARY COOLANT (THOUSANDS LBS>

Pc,RCFNT FUEL WITH CLADDING DKFKCTS.

PRIMARY SvsTEH LETOOwN BaTE (GPH)

LE'TOOWN CATION DE)iINERALI7ER FLO'w (GPH)

NUHBER OF STEAH GENERATORS TDTaL sTEaH FLow (HILLIQN LBsrHR)

MASS OF STEAH IN EACH STKaH GENERATOR (THOUSAND LBS)

HASS OF LIQUID IN EACH STFAM GENERATOR (THOUSAND LBS)

PWR 3391 00000 0 80 561 00000

~ 1200 75 Ooooo 7 50000 4 00000 14 70000 6.5sooo 134 70000 TOTA!

MASS Of SECONDARY COOLANT (THOUSAND LBS) 2100 00000 SLOWDOWN PATE (THOUSAND LBS/HB) 36 F 0000 BLOWOOWN IS NOT PROCESSED THPOUGH COND DEHIN CONOFNSATE OEHINERALIZER REGENERATION FREQUENCY (DAYS) 0 F 00000 0 00000 745 00000 CONDENSATE DEHINERALIZER FLOW FRACTION RADWASTE DILUTION FLOW (THOUSAND GPH)

LIQUID WASTE INPUTS FRACTION FRACTION COLLECTION DECAY 5TREAH FLOW RATE OF PCA DISCHARGED TIHE TIHE (GAL/OAY)

(DAYS)

SHIH BLEED RATE 6 20K~03 1

000 F 100 " '

500 I ~ 400

'ECONTAH I

I-ooE+o4 1 ~ 00K+03 OEAER EQUIP DRAIN 8

)OK~02 1

000

+100 7+500 1+400 loooE+03 CLE'AN WASTE 4 25K+02

~l80 1+000 1 I ~ 600 0 ~ 000 DIRTY wasTE 9 '0K~02

~ 026 I F 000 5 ~ 200 0 F 000 1 ~ 00E+03 BLOWOOWh I 04E+05 1 000 0 F 000

~007 1 ~ 00K~04 VNTRc,ATEO BI.O'WDOWN 0

.1 000 0 ~ 0 0 ~ 0 1 ~ 00E 00 INATION FACTORS CS OTHERS 2 ~ OOE+05 I ~ OOK+05 1.00K+05 1.00E 04 1 00Ki04 1

00E+04 1-OOK+o4 1-OOE+04 l-ooc.+03 I ~ 00K+04 I ~ OOK 00 I ~ 00K 00 GasECUs wasTE INPUTS THERE IS NOT CONTINOUS STRIPPING OF FULL LFTOWN FLOW 4 8681 90 00000 90 00000 FLOW RATE THROUGH GAS STRIPPER (G?H)

HOLr.UP T IHE FOR XENON (DAYS)

HOLDUP TIHE FOR KRYPTON (PAYS)

FILL TIHE OF DECAY TANKS FOR THK GAS STRIPPER (DAYS) 0 00000 PRIHaRv cnnLaNT LEar.

TO AUXILIABvB(.OG (LB/pav)

AUXI(.IAPY BLDG LEAK IODINE.PARTITION FACTOR GAS

.iASTE SYSTEHPARTICVLATE RELEASE FRACTION AUXI(. IARY BLDG IODINE'ELEASE FRACTION PARTICULATE RELEASK FRACTION CONTA INHENT VOLUHE. (HILLION CU FT)

FPECUENCY OF PR IHARY COOLANT DEGASSING (TINES/YR)

PRIHARV TO SECONDARY LEAK PATE (LB/OAY)

THc,PE 15 A KIDNEY FILTER Cpt(TA INHENT ATHOSPHERE'LEANUP RATE (THOUSAND CFH)

PURGE TIHE OF CONTAINHENT (HOURS)

THERE Is NOT A CONDENSATE OEHINKRALIZER 160 '

00750 01000 1 00000 F 01000 1

18000 20 100

'6 00000 16.00000

'01 40 '

00000 01000 CNTHT-SHUTDOWN PURGE IODINE RELEASE FRACTION paRTlcULATE RELEasK FR~cTIDN THERF.

IS NOT A CNTHT BLDG (.OW VOLUHE PURGE sTEA> LEAK TO TURBINE RLGG (LBS/'>

1700 F 00000 0 ~ 00000 1 00000 FRACTION IODINE RELEASED FROH BLOWDOWN TANK VENT FRACTION Ioplt(E RFLKASFD FPOH HAIN CONDENSER AIR EJECT THERF IS NOT A CRYOGENIC OFFGAS SYSTEH IOOI.")F PART I T ION FACTOR (GAS/LI QUID)

IN STFAH GENERATOR FPEOUFNCY OF CNTHT BLDG HIGt{ VOL PURGE(TIHKS/YR)

Table 2. 3-2 GALE Liquid B,(;suits 10f 2 f)ONALO C C>OK UNITS 1

OA 7 THFR>>af.

PnwFR LFVFL f<FGAwaTTS)

PLANT CAPACITY FACTOR

>*SS OF PPIMARY COOLANT (THOUSANDS I RS)

PFACFNT Ff)FL WITH CLAAAI>>G OFFECZS PAIWAAY SYSTEH TOOMN RATF, (GPM)

LFTCf)WN CATION OEHINFPALI7EA FLOM (GP~)

Nlf>>RFR OF STEAM GFNFRATOAS TATAl. STFALf FLOW (MILI.ION I.RS/HR)

<ASS f)F STEAM IN FACH STEAM GFNERATOR (THOllSANO I BS)

Mass nF LInuID IN EACH sTra>

('FNFAATCA (THnusaND LBs)

>ASS OF WATFR IN STEA< GFNFAATORS (THAUSANn LRS)

TOTaL AMASS OF SECONDARY Cnnl ANT (THOUSAND l.RS)

RLownf)WN PATE (THnusAND LRR/HA)

PAII ARv TO SECONDARY LE'AK PaTE (LRS/DaY)

Cf)Nl'.FNSATE OFMINEPALI7FR PEGENERAT ION FREOllFNCY (DAYS)

FISSTnN PRODUCT CARRY-OVEP FRacTION HAL(lGFN CARRY-OVER FRACTION CONOFNS*TE OE)4INERALIZER FLOM FRACTION RAOWASTE DILUTION FLOW (THOUSAND GPM)

PWR 3391 nono n ~ ~0 Sei.oooo 1200 7g.nnnn 7.5ono F 0000 F 14-7O00 e i5500 134 7000 538 '000 2lnn. nnOO 3f +noon 160.

-'n.nooo

~ nolo in)00 n.nooo 74S nOOO LIOUID WA5TE INPUTS STRFA<

FLAM RATE (GAL/DAY SHI>> +LEFO AATF e 20F+03 OFAEA Eof)I+ f)RAIN 8 ~ IOE+02 CLFAN wasTE 4 'SF+02 DIRTY WASTE 9,50E+02 RLOWDOMN 1 '4E+05 Uf'TREATED RLnwnn4N n.

FRACTION FRACTION COI LFCT OF PCa DISCHaRGED TIME (AAYS) 1 000 100 7 500 I.noo

.loo 7.soo

.18o

-'.nno ', II.()00

~ 026 I ~ 000 ST 200 1.noo n.noo 1

000 n

0 TON OFCAY T I HF.

(DAYS) 1 ~ 400 1.4nn 0 F 000 0 F 000 F 007 n.n I

I ~ nnE+04 I ~ OnE+03 I ~ onE+03 I ~ onE+03 I ~ onF+04 l OnE 00 CS OTHE'RS 2.00E OS l.nnE.OS I.one+05 I.nOE+04 1 ~ 00E+04 1 ~ noE+04 1 ~ 00E+04 1

noE~04 I ~ 00E+03 I ~ f(OE+04 00E 00 I 00E 00 DECONTAMINATION FACTORS 9n.nnnn 9n ~ nono O.nnOO

.olono l.onnno F 01000 lel800 lg nnno 40

'.nnnoo F 01000 THERE IS NOT A CNTMT RLOG LOM VOL PURGE STFa>>

l EAK TO TUARINF. BLOC. (LRS/HA) 1700.00000 FAACTI:lN IODINE RFLFASFO FAOH RLOWDf)WN TANK VENT n ~ 0000 FPACTInN IODINE RFLEASED FAOM MAIN CONOENSFR AIR EJECT 1.0000 GASEOf)S WASTE INPUTS THEAF IS NOT CONTINOUS STPIPPING OF FlfLL LFTOWN FLOW HOL(l>)P T l)AF.

FOR XFNON lDAYS)

HALOff> TIVE FOR KRYPTON lf'AYS)

FILL TIME 0F'FcAY TANKs FDA THE Gas sTAIPnFR (DAYs)

GAs wasTE sYsTFM PAPT IclfLATF RFLEASF.

FRACTION AlfXILI ARY BLDG IAOINF AELFASF FRACTION PaRTICULATE AFLEASE FRaCTION Cl:NTAINMENT VOLUMF (MILLI&MCll FT) cnNTalifMENT ATMOSPHERE cLFANUP RATF.

(THnusa>>D cFH)

F+Eof)F>>CY OF CNTHT RLOG HIGH VOL PURGF (TI>>FS/YR)

CNTNT-SHUTDOWN PUAGEIOOINF AFLEASE FRaCTION paATIclfLATE RELFasE FAacTIoN THERF. IS NO CRYOGENIC OFFGAS SYSTEM

Table 2. 3-2 (continued) 20f2 nON4LO C

COOK UNITS 1

OR 2 Llos) IO FCFLUE'NTS 4N~()4L RFLE4SFS TO ()ISCH4PGE CANAL

(( 4Y~)

(MICRO CI/NL) (t ICRO CI/>>L)

(CUPIES) cORpnsIAN 4NQ 4cTIY4TI0N pRODUGTs CP ~l 2.74C nl 1.86C-03 2.n3F-07

.noaa,

)>N 54 3 '3F+07 3'3F 04 4 ~ 9AC-OA

.ono'n'E'5 9 'AC 02 1

S6F 03 1 71F-07 hnap n

7

.npnhi

~ AOOIR

-Ao002 CF, S9 4 ~ 5>)".+AI c() <<8 7.)~c.nl CO eh 1 9?F+03 ZP AS e.SAF.nl Ne <5 3.5hc Oi NP239 2'<<F OA 9 78F-04 1 56C'7 1 ~ 96F 03 n.a.

I ~ ITE 03 I ~ 2sE-07 1 ~ 73E-06 zeznE-07 0 ~

0 ~

1 AOF.-07 o.ooonn o.oonon

.oonon rnnL4NT cONcENTRATIONs MUCL IOE )'4) F -L IF F oR I>4RY SECON04R Y BORON RS HISC ~

WASTES (C))P IFS)

~ OAAA2

.Ohnnn

.Qnhnz

.Ahnnl

.Onn?1

.ohnn3 A.nnonn Q.onono

.onnnl

'.oonho

.Onaha

.Qnann

.OAAAO

~ annh?

.onnho o.onoho O.OOOAO

.Qonho

.nnooo

.noooo

.onono

.Aoono

.noon2

.onnno o.noono 0 ~ 00000

.oanoo SECON()4RY T()PR RLDG (CUR IFS)

(C()RIES)

.n0005

.Anool

.AOQA4

.nhn03

.nno43 A ~ Apnoo n.noooo

.Anool

.nooo6 canals

~ 00003

.onol4

.Aoona

~ A0134

~ 00017 A.nooon o.nnonn

.Anoa4 o.onono

.nnioo o.nohoo o.ohono

.n0400

~ hna70

.AOI4o

.nn?no o.hnnno 4DJqSTE()

OETFRGCNT TOT4L LWS TO 4L W4STES

( CUP IES)

(CI/VP)

(CI/YR)

TOTAL (CI/YR)

~ 00015 ooalna

.ono14

.onoo8

~ 00530 Q0890

~ 00140 F 00200

.PAQ04 FISSION 8P A3 RR aa cp 89 MO 99 TC 9O>C PUI03 "PUlae 4GI 1 0<

TF 177<

TE177 TFI?AV TE I?.c)

I 130 TE131"(

TE131 I

131 TEIL?

I '.37 I 133 I

134 CS134 I

13S CSi )6 CSI37 BA137H 9AI40 LA14h CE 144 ALL OT~

TOTAL (EXCFPT PPAO(j( TS I.OAF-AI 1 24F-h?

5.2AF+01 2 ~ 79F ~ Aa

? 5AF-01 3.9<c~ni 3,67C~A?

2 ~ 5 >c+A?

I.nsc-a?

3.9?C-nl 3 ~ 41F ~ 01 4 '0C-n?

5 '7C-Al ZSF+hn 1.74E-P/

a.p F

QA 3 2<<E+Ph 0 ~ 54C-07 a ~ 7<<c-p) 3 '7F.-A?

7.4qc.n?

2 '%F h'>

3hc~ai 1

1 ">r +94 1 ~ 77F-03 1.24F+AI 1.64F-AA 7.84C n?

TRITIU>>)

4'9F 03 95F-01 3 ~ 42C 04 8 21F-0?

4 69F-02 4.40F-05 78E-06 h ~

2'4C 04 a,31F-A4 1,37c 03 1.56c-n3 7 ~ ASF 03 2.44c-n3 I ~ 08C-03 7.64c-ni 7, ~ 64F-02 9'ar.

02 72C,-al 4 'QF-02 7 '6C-07 oi 1.23c-02 1 'nc 07 I ~ 56E 02

7. ~ 15F-04 1,47F-04 3 ~ 23F-05 4 '9C-03 I ~ 43F+00 I ~ 06F-07 6 '0C.-P7 4 'AF.-na 9~63F.-OA i+a?c-Os 5 ~ 01F-A9 1 ~23F-09 0 ~

2 22F-Oa

1. A9F.-Q7

1. SIC.-A7 4.seF-07 1 ~ 26F-O7 1 ~ +6C.-A7 3 '7E-A7 3.01F-nS 2.49F-ng 7.)>4E-A6 2.82E'-Os 4.4AE-n7 2 '4F-0>>>

8 '9E-AA 1.?7F.-OA 1.89F-A6 6 SIE-Ae 2.37E-Oa 2 '9F-Oa 4 '1E-09 1 62E-07 I ~ 23F.-04

.nonnn o.ooonn

.nonnn

~ AAA37

.Ann3n

.nonnh

.onnon o.oonnn

.Anonh

.Aonon

.nonni

.Annni

.nonon

.Aonnn

.nnnnh

~ 07.08A

.non)?

~ 00017.

.Ao?48

.nonnn

.oonna

.nooo4

.AQA03

.Annnr

.nnnns

.onoon

.nonan

.nonon

.noooi

~ 02470

.Ohno1

.Ohnal

.Ohnhn

.Onh44

.Onh41

.Onhhn

.Ohnhn h ~ Ohahn

.Ohnhn

.Onhhn

.OAAA2

.Ohnhl

.Onnn2

~ Ohnnl

.Onnnn

~ 07494

.Annie

~ 00179

~ 00730

.AAAA4

.OAOW3 F 00117

.Onhl3

.ohn?4 onn??

.onnho

~ PAOAO

.Onnno

.Ohonl

~ 03759

.Qnnho

.nnnn6

.oonno 00014

.Onn?6

.Oonno

.PAQAQ o.oonho

.onnhn

.Qnnna

~ onnho

.Ahnnl

~ Oaoha

.onnho

.Onhha

.OAA43

. n('nh4

~ PAA)1

.onn4o

.Pnhhl

~ 00041

.00012

~ 0:)018 00077

.Ohn?4

.onono

.Onnnn

.onnno

.Ooono

~ 00772

.aoooo

.nnnoo

.nonao

.nona9

.Onnl3

.normo

.oonno o.noono

.oonno nnaoa

.Ahoha

.oonno 00001

.noooo

.Aoono

~ 00293 AAA02

.ann15 00230

.nnooo 00003

.QA044

~ 00001

.nnnO2

~ 00002

~ 00000

.normo

~ 00000 00000

~ 00619

.naaol

~ A0007

~ hanol

.A0099

.hallo

.Aonoo

~ naann n.noooo

~ nnonl

.noonl

.nhnn4

.hpoa3

.00004 nAanl

~ naool

.n4910

~ n0033

~ nn217

.n1249

.nnn04

~ hnaa4

~ n0177 hh036

.npn58

.A0053

~ hoaaa

.Aaaol

.hanna 00002

~ 07120

.ooon4

~ 00021

.OAA03

~ 00307

+00343

.nnooo

.onoon n.nhonn

.Qnnn?

~ 00003

~ hnali

~ hn009

~ 00012

.nooo4

.Aono?

~ 152SS

~ 00104

~ 00673

~ 03879

.Ann)4 Ao?.61

.oaSSO

~ 00117.

~ 001A1

~ 00166

~ Anan?

.nooo?

~ nnona

.Aoone

~ 22120 o.normo o.nonoo o.normo P.phhna o.oonno

.nnnl4 F 00?40

~ 00044 o.nnnno o.onnno o.onnno o.nnnno 0 ~ Anpna o.normo 0 ~ naana

.Qnnne o.nnnoo o.normo o.hnnoo O.nhhna

.A)300 o.normo O.hhnno

.n?cno o.nnnno o.normo Q.normo

.Anszo o.n

~ 06234

~ QAQ04

~ 00021

~ 00003 oaa310

+00340

.pan)4

~ 0024 0

~ 00044

.Qnon2

~ 00003

~ QQDII

.Onnn9

~ 00017

~ 00004

~ paaa2 F 15000

~ 00100

~ PQ670

~ 03900 iaoa)4 F 01600 PQSSA

~ 00110 Czeha F 00170

~ 00002

~ OAA02

~ 00520

~ 00006

~ 28000 TRITIUM RFLF4SE 670 CURIES PER YEAR

(blank page)

TABLE 3. 3-8A Diffusion and Deposition Estimates for AllReceptor Locations Site:

D. C. Cook Release Point: All Season:

Grazing Computer Run ID: AX-2 Direction Distance to Nearest MilkCow (m)

x/Q (sec/m3) ep e e x/Q (sec/m3)

N/A D/Q (m"2) is nce o

ep e e Nearest Mea X/Q3

/Q3 Animal(m) sec/m

)

(sec/m

)

N/A D/Q m-2)

Distance o

Nearest Milk Goat (sec/m3) x/Q, (sec/m3) ep ete x/Q D/@

(sec/m3)

(m ~)

N/A ESE SE SSE 2900 4800 V081 7081

1. 2-6

2. 2-7

1. 1-V

1. 3-V

8. 8-9

1. 0-9

4. 8-10

5. 3-10 VV25

'7725 3862 6810 2434 4354 7425 6115

1. 9-7

1. 6-7

6. 1-V

1. 3-V

1. 2-6

2. 5-V

l. 2-7

1. 1-V

4. 6-10

6. 4-10

3. 8-9

5. 7-10

8. 6-9

1. 4-9

4. 7-10

3. 9-10 SSV/

Lake Lake Lake Lake Lake Lake Lake Lake Lake Lake Lake Lake NOTE:

N/Aindicates that diffusion information for this run was not used in dose calculations for receptors in this column.

(-) indicates receptor distance is greater than 8000m therefore no calculations were made.

New Values for AEP Cook 10CFR50 Appendix I Report Table 5. 1-1(1)

. ~ ~

Pathwa Plume (661m N)

Ground (661m N)

Vegetables (1V12m NE)

Meat (2434m ESE)

Cow (2900m ENE)

Inhalation (661M N)

Totals Group Adult Teen Child Infant Adult Teen Child Infant Adult Teen Child Infant Adult Teen Child Infant Adult Teen Child Infant Adult Teen Child Infant

~

Adult Teen Child

. Infant.

Body

8. 9E-1

=

8. 9E-1

5. OE-2

2. OE-1

2. 3E-1

4. SE-1 0.

1. 5E-2

1. OE-2

1. SE-2 0.

2. 5E-2

3. 4E-2 V. 2E-2

1. 4E-1

3. VE-1

2. OE-1

2. 1E-1

2. 2E-1

1. 6E+0

1. 4F.+0

1. VE+0

1. 3E+0 Tract

8. 9E-1

5. OE-2

2. OE-1

2. 3E-1

4. VE-1 0.

1. 5E-2

1. OE-2

1. SE-2 0.

2. 4E-2

3. 3E-2

6. SE-2

1. 3E-1

3. 7E-1

2. OE-1

2. 2E-1

1. 6E+0

1. 4E+0

1. VE+0

1. 3E+0 Bone

8. 9E-1

5. OE-2

4. 4E-1

1. 3E-1

3. 2E-1 0.

5. 1E-2

8. 1E-2

1. 5E-2 0.

5. SE-2

2. 2E-2

5. SE-2

l. 2E-1

l. 4E-3

1. 2E-3

1. 9E-3

2. SE-3

1. 5E+0

1. 1E+0

1. 3E+0

l. 1E+0 Liver

8. 9E-1

8. 9E-'1

8. 9E-1

5. OE-2

2. OE-1

2. 4E-1

4. SE-1 0.

1. 5E-2

1. OE-2

1. SE-2 0.

2. 6E-2

3. VE-2 V. 6E-2

l. 5E-1

3. 7E-1

2. OE-1

2. 1E-1

2. 2E-1

1. 6E+0

l. 4>+0

- 1.VE+0

1. 3E+0 Kidne

8. 9E-1

5. OE-2

5. OE-2 5: OE-2

5. OE-2

2. OE-1

2. 3E-1

l. 8E-1 0.

1. 5E-2

9. 2E-3

5. 8E-3 0.

2. VE-2

3. 5E-2

2. 9E-2

3. VE-1

2. 6E-1

1. 3E-1

9. SE-2

1. 6E+0

1. 5E+0

1. 3E+0

1. 1E+0 Thyroid

8. 9E-1

5. OE-2

5. OE-2 V. VE-1

6. SE-1

1. 1E+0 0.

3. 6E-2

2. 4E-2

3. 9E-2 0.

6. 2E-1

9. 3E-1

1. 8K+0

4. 4E+0

8. SE-1

6. 3E-1

7. VE-1

1. 2E+0

3. 3E+0

3. 2E+0

4. 8E+0

6. 6E+0 Lun

9. 3E-1

5. OE-2

2. OE-1

2. 3E-1

4. 7E-1 0.

1. 5E-2

1. OE-2

1. SE-2 0.

2. 4E-2

3. 2E-2

6. SE-2

1. 3E-1

3. 7E-1

2. OE-1

2. 1E-1

2. 2E-1

1. 6E+0

1. 5~+0

1. SE+0

1. 3E+0 Skin

2. 5E+0

2) 5E+0

2. 5E+0

5. 9E-2

2. OE-1

2. 3E-1

4. 7E-l 0.

l. 5E-2 1:OE-2

1. SE-2 0.

2. 4E-2

3. 2E-2

6. SE-2

l. 3E-1

3. VE-1

2. OE-1

2. OE-1~

2. 2E-1 W

3. 3E+0

3. 1E+0

3. 4E+0

3. OE+0 Maximum offsite air dose from plume:

Beta

4. V mrad/yr Gamma

1. 7 mrad/yr (1)

Changes to Table 5. 1-1 8/31/V6 version 610m N

'10m N

Table 5. 2-1 Maximum Individual Doses from Liquid Effluents Donald C. Cook Unit 1 or 2 (mr em/yr)

Pathway Fish Drinking Shoreline Swimming Boating Total Age Group Adult Teen Child Infant Adult Teen Child Infant Adult Teen Child Infant Adult Teen Child Infant Adult Teen Child Infant Adult Teen Child Infant Skin

2. '?E-2

l. 5E-2

5. 9E-3 0.

3. 6E-3

2. OE-3

3. SE-3

5. VE-3

1. '?E-5

9. 2E-5

1. 9E-5

2. 2E-7

l. 2E-6