ML21055A292
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POST TREATMENT "22) Co/,JD ~ SYSTEM NOTES:
- 1. THE FOLLOWING DEFlNITJONS ARE USED Off THlS DIAGRAM:
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DESIGN DAILY VOLIJIIIE - EXPECTED VOLft DURING STEADY STATE NORML OPERAT!Ofol. I:-I C LE.A NI N ti EQUIPMENT IS NOT MAJ!li'llll1 EXPECTED VOLL'ME DURING UNSTEADY DWG. 2:029 TABLE. ':mII TU~ 61t,,11:, BI.DC;i 011.
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~FSAR SECTION 11,2-17 2 MAXIMUM VOLUME STATE OPERATION SUCH AS STARTUP, SHUTDOWN HI GIi EQU l f'l'ENT LEAKAGE, ETC ,
400 C:,A,L., I IPHAS-e e / w ro .::.or,Jc,"-.
,,, / NORMAL ACTIVITY ACTIVITY LEVEL EXPECTED DURING NORMAL
£..:::....} S1:.PAAATO~ c.6 *_yr I I OPERATION. REACTOR WATER ACTIVITY TlJRB!NE 61..DG
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' '-----+-L~-~T~o=-=P~o-~=-:t=A-=-=e-U:.::_=._:-------Jl-t-----:c.o;-.:-:0:-:1..-:1-:--N-:-"';:-----------_j,__ CONCENTRATION ,66 µCI/ML. THE CORROSION PRODUCT REACTOR WATER ACTIVITY CONCENTRATION r----sie.,\M ~
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WA.iE.~ DESIGN ACTIVITY JS O.lµC/ ML. ACTIVITY LEVEL EXPECTED DURING OPERATION WITH
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1\/\J\/\/V' C.ONDE:.N'?fl<' D,':>ilLl..f\iE. FUEL LEAKAGE, REACTOR WATER ACTIVITY CONCENTRATION IS 4,85 µClM... THE CORROSION PRODUCT REACTOR WATER,CONCENTRAT!ON ACTIVITY
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IS 0,1 /.,IClli'll. G BUILDING F1.00P- .---135, (* 11...1- J--{& ~~M CAUTION: ~AX!r'lll!'1 \/Otft AND l'IAXll'IU!'I ACT!VlTY Allf i'iOT NECESSARILY CONCURRENT DWG 202.9 Rl!.A.,,:roR. --.....1 '-,...!lo! ORA1tJ cot..Lec:roR.. ~--1 - - - -
-- .-,. - - - = __ .. L ___ I__ _J 2, FRACTIONAL VALUES ON CHARTS DENOTE NUMBER OF lTEi'IS PER OCCURANCE TAe>L.i:. llI I I BLDt:a i:..ooR ,,. _~ TANK ETCHED o tl. E.YAPOAATO~
DIVIDED BY HUMBER OF DAYS BETWEEN EACH OCCURANCE (1,E, 24/30 DRUMS/DAY Dw'G. 2.02.9
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MEANS 24 DRUMS ARE PROCESSED ONCE EVERY 30 DAYS)
- s.u.ieie- I 3, DESIGN DAILY VOLUME AND N0~"1AL DAILY ACTIVITY ARE
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TA!:>1.t iZZI[ AVERAGE VALUES CALCULATED OVER A PERIOD OF A YEAR
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Zf:>OOC WAL- 't..V/>P CRAIN~ !-<<1111---1 TO ACCOUNT FOR VARIATIONS DURIHG THAT PERIOD.
~a-------------... I f,101.DI.IP TA~\<'. 4. WASTE SYSTEM INPUT ACTIVITIES ARE BASED ON A REACTOR WATER-TO-STEAM Tu Rl!li ~ t.
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~ 5.
DECONTAMINATION FACTOR OF 1000. ACTIVITY SHOWN !S OF PLANT ORIGIN AND DOES NOT lNCUJDE BACK-GROUMl 1 1 ! C7 /_4' P~li!.">O"-lNE.:L / ME.Oil.AL.
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8i.D'11 FLOOR!
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- 5. ACTIVITY DECAY IS CONSIDERED IN THE CALCULATION OF EQUILIBRIUM ACT! \I l TY ! ilCLUDED 1N THE Dl AGRAM,
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I * * ****************lfr-795\ -----< TD DIST, INLE~ BATCH TANK 7, 'I/ATER SENT TO CONDENSATE STORAGE MUST MEET THE FOLLOWHiG REQIJ!REMENTS (PH AND*CONDUCTIVlTY APPLY AFTER CORRECTION IS f'IADE FOR DISSOLVED co2J. PER AT I NA L PER FERMI 2 6 I F CI\SK CLEAA-111-lq ~ 1. SPECIFIC COHOOCT!VJTY a 2s0c < l/11'1HOS/CM 012.All-!5 . / e5 LJFSAR AAP'WA~~ SECTION 11,2,1 TANI, I II I~ -- A 11'- - CO ND - - AIR CC)t,lD 2 , PH a 2s c 0 NEUTRAL <6-S l
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- 3. SILICA (AS SIO,,)
1l, CHLORIDE (AS Cl-l 5 , BORON (AS B03 J
... <1,0 f'Pi'l
< 0 ,01 l'Pi'l
< 0 .1 Pl'!l1 C.129 AN" FOiJ!.cTH F/..OCR DI: C.O iJ )/ft I LLCi} *::_J I I I I FLOOR DR.A\N WA~Te 6. ACTIVITY < 3 x 10-3 µCl/Ml.
DWG 2029 rA6L!:. ID I DECON SHOP ).---1~ J 4 1 1 I 1 4,
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I CHEMILJ\1...L- ,U 1 1 1* 1COLL'eCi'OR. l7EM1Nl: !<."' L rl. E1' h : I I' /41'\ I COLLl:CTOR. D 1:MlNERA,LI li! R.. fRO\.I PORTAi:>Lc 8, MAXIMUM PRESSURE DROP ACROSS SERVICE SIDE Of All COOLING COILS IS 10 PSI.
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- .SOLUTIONS . ( \
II WA':>~ l!!::::::, A DEM INER .l\l.17.ER. 9, MAXIMUM ACTIVITIES GIVEN FOR !TEMLZl',ARE THOSE WHIC~ WOULD f I TANK [:>I I ~E.E. MCTI!l @ SEE NOTE {!j) j 'oYSTl:-M OCCUR IF THE PLANT DISCHARGED TO THE LIMIT OF 10-7µ C/ML [ LAe> Cii2AIIJ~ --------Ill I 1 ; , j I 5Z~"rAL. , D L-- I ~,-1--------1-----..., CONTINUOUSLY, A IT PORTABLE 10. THE BLOWDOWN WATER Fl.OW RATE FOR lTEM J73,(CANAL FLOW RATE) IS It : I I I A . /s'°\ MAINT£NANC£ SHOP If B£NCHTOP DECON
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CDIJO. A MINIMUM OF 10,000 GPM. A E SOLUTIONS 11, LJQU!D ASSUMED FOR ITEM~ JS 201 SODIUM HYDROXIDE SOLUTION. E r-rc
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- 13. THE WASTE SLUDGE QUANTITIES ARE BASED ON NO BODY FEED ADDITIONS,
!,,QUIPME.NT 14, DEM!NERALIZERS ARE NORMALLY OPERATED IN SERIES, ElTHER BED MAY BE t:MG 2.029 TAei L- f:. :J: Di2A1N i:.1".l-1AN'1~R. I COOl.lt..iq . 'Rwcu <FROM i WA "'"c, T '2. -Is>..
I I WA':>Te. 5A1-11P!.£ WA'STE 5AMPLi:.
'NASTE.
S,o,M P1...E. PLACED IN THE LEAD POSITION.
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TA"-!._ TA!,414 15. FLOCULATION TANKS ARE IN PLACE BUT ARE NOT INTENDED FOR USE I.....
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124,300 GA~ 74-l""""I 24,300 ~AL-J,-,1._
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1 21 000 C-1-1\LJJ ,4, DURING ,tlORMAL OPERATION,
- 16. LINE ,l,l;, HAS BEEN CALCULATED BASED ON AN AVERAGE DAILY BASIS, ONE BACKWASH IS EXPECTED TO OCCUR EVERY OTHER DAV DURING NORl'!AL Disc. I - - - OPERATION WITK 8 BACKWASHES PER DAY OCCURING DURING STARTUP
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Ii? E:AC.i'Oic. HeA*r 23,400 "!Al.., u.. I F'ILTE:R. ~ Al~ cooL.cR
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f w CONDITIONS. STARTUP HAS BEEN ASSUMED TO OCCUR 12 TIMES PER YEAR.
- 17. NET WEIGHTS OF DRUMS ARE 504 LBS, FOR RESIN ~ATERIAL AND 600 LBS, FOR RADSALTS. 50% OF NET WEIGHT l S ASPHALT.
D e,1.,.:,4_ 18. RANGES SHOWN FOR PRESSURES AND FLOW RATES ARE FOR NOR~.AL 1*nwc, 2029 I SPE:.t....1 I D T1>.e1..e. ll >"*
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~4 fit\ COND ge,;; I ;J OPERATING CONDITIONS. FOR SPECIFIC OPERATING CONDITIONS REFER TO PUMP PERFORl'IAl'IC~ CURVES, WA.T!R.. TA. 1--1 i(..
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- 19. LINES flb., ~- e+/-!!.,, AND a!i:i, ARf. FOR THE PRECOAT FILTERS.
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THESE FILTERS ARE ~OR USE OMLV'iN THE EVENT OF FAILURE OF BOTH
'-AB i;)~AIN':> >-------, r 1':i , RECYCLE _ / !=ROM ETCHED DJSC FILTERS AHD, COIISEQUENTLY, HAVE NO NORl'!AL FLOWS DR
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DWG 2029 '>, I
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I FROM PO£f~6Sl;:-nor-. I I 501.IDIFI""' FROM VAS t E
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I I DILUTIN 1 ~ RWClJ l,.rV\.. - 4k ~,, ASSOCIATED BATCH SOLIDS. A A 20, LINES Lili AND ~ ARE DIRECTED INTO CONDENSATE
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SAMPLE TANKS wATER -11 - - - - "*
~ FILTER TABt.E. 1II '--41.-i '/'olA":JTt. T:"'-""-L._-',...J 'COOLING. TCWER)>--- I\ PHASE SEPARATOR A ONLY,
, 250 GAL I ,::::_:: 1- * , ----
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21, 2~ DRUMS CONTAINING ONE SPENT OIL COALESCER CARTRIDGE
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"'- 58 I fE:.£.D D1vG 2029 ) , ~ I !Zil.17WA7Tii:
ew:ie::i ;1o 1 I BUNDLE EACH WILL BE GtNERATED PER YEAR, THE ANNUAL r-->'.:~ ti!'!* 1 INVENTORY BREAKDOWN BASED ON NORMAL AND DESIGN BASJ~ rAe.LE. r:;;: '/:;Qu,PMLN i 9J2AIN e>uMF' I
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I ACTIVITIES JS PRESENTED ON DRAWING 6M721-2030, 1, 22, DURING SPENT RESIN TANK VOLUME TRANSFER iLJNE a_fu) C 1-!I. - --,-:::::-::--..- --::,:-~, -;--7:zi:':j::::]1=11- II - 7I ,:.\sT~ _ __ i'I *1,,,100
,JS ,_,..~'1A't): * * ;)""'. ; ' . '*-"" - "'r:--.-:::--- ___ ... AI Bu1L,1NG 1011 GALLONS OF 25 WT% SLUDGE WI LL BE TRANSFERRED C l
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CK. r- !.,_ :'..C> I TAN~ . PHASE SLUDGE SEPARATOR TJ CJND. II~ : ' - - - - - ~ : . .,.,....._.. ~ ,_ 'vE'NT HO,'.)D TR.A<N :)
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/REACTOR WATe.lc:. '-.
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!:>EPARATOR DeW
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T ~Ii', .II I"' ND'E '19__J I * .,,~******-*~~ (A-7) rCE::N:T;-;:R"l"F'LJil!G~eE' I 0 ... i -*..,.I FOLLOWED BY A 1011 GAi.i ON RINSE, TO (.0'!,.iOEt-.!St,,iE. \ STORA~E OR _ / FLOO~ l)R...IN Fil.TE.I<. r 1--r' 2!>'
- REiURN TA~K.
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- SEPARATOR WA.~Tf:. C.OLl.l:C.TOI<
Fl L1e.~ BALI<.'NP,!, M ' /'i7'~
--~ 11,800 (2)
GAL r 3~CDNC
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FEED 6000 GAL I L9Ci's;, TD PORTABLE TIDN [ ' r- _*-* -- -- vv11rE.R ./ SEE NOTE i)IBI TO DISC.HA'RGI:.
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6M721-2028 LATEST REVISION K l -==--~ I C0"117c/o,/S,A TE. Fl1.Tell:/ l,..Q \ g f? . I . i---t--'"\,nJI
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F!..0'- JI ' j rvg::r*-. ]~ ~--~--4sc.;R-,c. J 0 J THIS IS A MICROSTATION PRODUCED DRAWING.
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I 'BOILE(~ J CHANGES OR REVISIONS MUST BE BROUGHT TO THE ATTENTION OF THE PLANT ENGINEERING L __ _ - - t:...QUIPMENT
- - - - - - - - IS --- NOT
___ _J THIS DRAWING WAS REFORMATTED EY INC.CODE i DESIGN GROUP TO ENSURE THAT CONFIGURATION CONTROL IS MAINTAINED. Detroit Edison Fermi 2 OPERATIONAL PER FERMI 2 MICROSTATION AT REVISION "t" . AU, UFSAR SECTION 11,5 K jDCD'S INCORPORATED, PREVIOUS APPROVAL S1GNA'I1JRES ARE ON FILE: ON MICROFILM IN DOCUMENT CONTROL PREPARED HY u DATE TITLE PROCESS FLOW DIAGRAM A PORTION OF THIS DRAWING IS AFFECTED BY THE FOLLOWJNG: EDP 37719,B015, ,EV, ¢ RADWASTE TC CHANGE DOCUMENT CHECKED SYSTEM IA A OTHER REVISIONS: BY DATE APERTURE CARD TITLE I Q.£<'. \.LI'- '";""q-u.~;' ,;,'\-1."- PROC DIAG RADWASTE SYS
- REF, LCR 19 012 Jr s, REv, 4 ~ APPROVED HY DA.TE PLANT IDENTIFICATION SYS'l'EM NUMBER ARMS RECIPIENT #
G1100 PREPARED BY DATE DATE DOCUMENT TYPE CODEDDDMEC NUC OPS FILE NO.I DATE ISSUED TO IS 1/J ADLER 2/19/19 z-n-11 EDP POSTING ENTRIES REQUIRE THE OTHER APPROVALS DATE 1801 <1 "'-::;._,ffi L APPROVED BY
..,------* DATE ADDITION OF THE ARMS STATUS CODE::
DRAWING- NUMBER REV. ollfl1'1 EITHER .. .AFC" OR "ASB" 6M721-2028 K 8 7 6 5 4 3 ? 1}}