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. /"8\\ /REACTOR WATe.lc:. '-. iU 1.:e,I t-.11:.. 2 1 NOTES:
- 1.
THE FOLLOWING DEFlNITJONS ARE USED Off THlS DIAGRAM: 2, 3,
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7, 8, 9, DESIGN DAILY VOLIJIIIE - MAXIMUM VOLUME NORMAL ACTIVITY DESIGN ACTIVITY EXPECTED VOLft DURING STEADY STATE NORML OPERAT!Ofol. MAJ!li'llll1 EXPECTED VOLL'ME DURING UNSTEADY STATE OPERATION SUCH AS STARTUP, SHUTDOWN HI GIi EQU l f'l'ENT LEAKAGE, ETC, ACTIVITY LEVEL EXPECTED DURING NORMAL OPERATION. REACTOR WATER ACTIVITY CONCENTRATION,66 µCI/ML. THE CORROSION PRODUCT REACTOR WATER ACTIVITY CONCENTRATION JS O.lµC/ ML. ACTIVITY LEVEL EXPECTED DURING OPERATION WITH FUEL LEAKAGE, REACTOR WATER ACTIVITY CONCENTRATION IS 4,85 µClM... THE CORROSION PRODUCT REACTOR WATER,CONCENTRAT!ON ACTIVITY IS 0,1 /.,IClli'll. CAUTION: ~AX!r'lll!'1 \\/Otft AND l'IAXll'IU!'I ACT!VlTY Allf i'iOT NECESSARILY CONCURRENT FRACTIONAL VALUES ON CHARTS DENOTE NUMBER OF lTEi'IS PER OCCURANCE DIVIDED BY HUMBER OF DAYS BETWEEN EACH OCCURANCE (1,E, 24/30 DRUMS/DAY MEANS 24 DRUMS ARE PROCESSED ONCE EVERY 30 DAYS) DESIGN DAILY VOLUME AND N0~"1AL DAILY ACTIVITY ARE AVERAGE VALUES CALCULATED OVER A PERIOD OF A YEAR TO ACCOUNT FOR VARIATIONS DURIHG THAT PERIOD. WASTE SYSTEM INPUT ACTIVITIES ARE BASED ON A REACTOR WATER-TO-STEAM DECONTAMINATION FACTOR OF 1000. ACTIVITY SHOWN !S OF PLANT ORIGIN AND DOES NOT lNCUJDE BACK-GROUMl ACTIVITY DECAY IS CONSIDERED IN THE CALCULATION OF EQUILIBRIUM ACT! \\I l TY ! ilCLUDED 1 N THE D l AGRAM, 'I/ATER SENT TO CONDENSATE STORAGE MUST MEET THE FOLLOWHiG REQIJ!REMENTS (PH AND*CONDUCTIVlTY APPLY AFTER CORRECTION IS f'IADE FOR DISSOLVED co2J.
- 1.
SPECIFIC COHOOCT!VJTY a 2s0c < l/11'1HOS/CM 2, PH a 2s0c NEUTRAL < 6-S l
- 3.
SILICA (AS SIO,,) <1,0 f'Pi'l 1l, CHLORIDE (AS Cl-l < 0,01 l'Pi'l 5, BORON (AS B03 J < 0.1 Pl'!l1
- 6.
ACTIVITY < 3 x 10-3 µCl/Ml. MAXIMUM PRESSURE DROP ACROSS SERVICE SIDE Of All COOLING COILS IS 10 PSI. A MAXIMUM ACTIVITIES GIVEN FOR !TEMLZl',ARE THOSE WHIC~ WOULD OCCUR IF THE PLANT DISCHARGED TO THE LIMIT OF 10-7µ C/ML CONTINUOUSLY, A
- 10.
THE BLOWDOWN WATER Fl.OW RATE FOR lTEM J73,(CANAL FLOW RATE) IS A MINIMUM OF 10,000 GPM. A 11, LJQU!D ASSUMED FOR ITEM~ JS 201 SODIUM HYDROXIDE SOLUTION.
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THE WASTE SLUDGE QUANTITIES ARE BASED ON NO BODY FEED ADDITIONS, 14, DEM!NERALIZERS ARE NORMALLY OPERATED IN SERIES, ElTHER BED MAY BE PLACED IN THE LEAD POSITION.
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FLOCULATION TANKS ARE IN PLACE BUT ARE NOT INTENDED FOR USE 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 OPERATION WITK 8 BACKWASHES PER DAY OCCURING DURING STARTUP 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.
- 18.
RANGES SHOWN FOR PRESSURES AND FLOW RATES ARE FOR NOR~.AL OPERATING CONDITIONS. FOR SPECIFIC OPERATING CONDITIONS REFER TO PUMP PERFORl'IAl'IC~ CURVES,
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I\\ i\\ /)_ .f\\ LINES flb., ~- e+/-!!.,, AND a!i:i, ARf. FOR THE PRECOAT FILTERS. THESE FILTERS ARE ~OR USE OMLV'iN THE EVENT OF FAILURE OF BOTH ETCHED DJSC FILTERS AHD, COIISEQUENTLY, HAVE NO NORl'!AL FLOWS DR ASSOCIATED BATCH SOLIDS. A A 20, LINES Lili AND ~ ARE DIRECTED INTO CONDENSATE PHASE SEPARATOR A ONLY, 21, 2~ DRUMS CONTAINING ONE SPENT OIL COALESCER CARTRIDGE BUNDLE EACH WILL BE GtNERATED PER YEAR, THE ANNUAL INVENTORY BREAKDOWN BASED ON NORMAL AND DESIGN BASJ~ ACTIVITIES JS PRESENTED ON DRAWING 6M721-2030, 1, 22, DURING SPENT RESIN TANK VOLUME TRANSFER iLJNE a_fu) 1011 GALLONS OF 25 WT% SLUDGE WI LL BE TRANSFERRED FOLLOWED BY A 1011 GAi.i ON RINSE, I CL!:.AN*UP PHAS~ !:>EPARATOR DeW I s..oti !ii E.Qu1F'MfJ,,i T ~Ii',.II 9iAIN !:>UMP ~2 ~ 1 1 I I,:.\\sT~ _ ,_,..~ "'r:--.-:::--- A I Bu1L,1NG I -7 '"-L.-Al I *1,,,100 '1A't)
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}I 1-!I. - lio ".,QO <'.;ii\\l.., PHASE SEPARATOR I"' ND'E '19 __J I .,,~******-*~~ (A-7) rCE::N:T;-;:R"l"F'LJil!G~eE' I l 0 TO (.0'!,.iOEt-.!St,,iE. \\ i -*..,.I STORA~E OR _/ FLOO~ l)R... IN Fil.TE.I<. t,A,(.J( WA:il-+ '. F *4) WA.~ Tf:. C.OLl.l:C.TOI< Fl L 1e.~ BALI<. 'NP,!, M (C*'!'_) C0"117c/o,/S,A TE. Fl1.Tell:/ Dt:M1 f'J - B,... c.,. W";;,1-f Fuf:.1. PIJOI. r 1--r' 2!>' CONDENSATE r--~** PHASE SEPARATOR (2) /'i7'~ --~ 11,800 GAL 1 0d1,._____ ~ I l,..Q \\ {J_1~--------------- )>---- l I.
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