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| number = ML12271A451
| number = ML12271A451
| issue date = 08/13/2012
| issue date = 08/13/2012
| title = Callaway, Unit 1, Enclosure 4 to ULNRC-05893, Figure 1, Callaway NPDES Flow Diagram.
| title = Enclosure 4 to ULNRC-05893, Figure 1, Callaway NPDES Flow Diagram.
| author name =  
| author name =  
| author affiliation = Ameren Missouri
| author affiliation = Ameren Missouri
Line 14: Line 14:
| page count = 1
| page count = 1
}}
}}
=Text=
{{#Wiki_filter:24.480.000 1 TRASH RACKS DC u > INTAKE STRUCTURE 288' COO PUMP LUBE WELL SCReEN WA-ER 24.480.000 I 40.3?o.ooo HEATER DR A. IN/ BLOW DOWN RAW WATER BYPASS TO PLAN I J I SCHARGC. L INC. 3000000 144000 EXCESS 'LJW 0-17.280.000 SPRAY WATER 576.000 SUMP
* I I I 009 0 ( 6000) : 1 4400000 I WATER TREATMENT PLANT STILLING BASIN 11 NTERMI TENT I 5 MILE P(PELINE TO PLA\IT COAGrANT STILLING BASIN --l RApiD POL YELECnOL YTE -----" CrLOR I NAT] ON _r------------t PUMP STATION SLUDGE Q SUPERNATANT 42oooo BLOW occu-OUTF AL_ 003 TO PLANT DOWN LATCRY CLAR(F(ERS
-------'-330000 ( 3) SLUDGE PUMP STATION
,. _____ _ LINE ZERO FLOW NE-------1 RA:NFALL SED(MENTATION LAGOON WTP 24.480.000 CLEARWELL MAKEUP BYPASS I OWC.H I 0 PLANT DISCHARGE LINE 3.320.000 (14.400.000)
OUTFALL 016 I I I I S-RVICE WA ER SYSTEM TO UHS I
I TTENT CIRCULATING WATER SYSTEM I EYAPORAT(CN 16.185.000
\ COOL lNG TOWER I IVVVVVVVV' SLOWDOWN OUTFALL BASIN 002 TO PLANT DISCHARGE LINE 4.840.000 ( 1 4, L 00, 000 ) CALLAWAY DRIFT 135000 Tll-ATMENT CIIEMICALS 568000 CPM FIGURE 1 NPDES FLOW DIAGRAM ACID l.)ISPC.HSANI HYPOCHLORITE/
SODIUM IDE CORROSION INHIBITOR
,--------MAKEUP DEMIN STORAGE TANK REACTOR 1\/AKEUP WAT:::R STORAGE TANK ,'--------
RECYCLE 5000 NOTES: 1. ALL PLANT OUTFALLS 009 TIE INTO A SINGLE PIPELINE WHICH DISCrARGES TO THE MISSOJRI RIVER JUST DOWN OF THE INTAKE STRUCTURE.
2 ALL SYSII:.MS HAVI:. t31:.1:.N S!Mlf-llli-H.Ll l-OR CLAR!IY. 3 ALL SYSTEMS AND MOST SIGNIFICANTLY, RADWASTE TREATMENT, ARE DESIGNED FOR FLEXIBIL:TY.
IN RADWASTE, THE LEVEL IS DICTATED BY olRADIO_OGICAL CONTAMINATION, AN) NRC MANDATED DISCI-ARGE CRITERIA.
AND blTHE NEED. FEASI8ILITv AND ECONOMICS OF RECYCLE VS. DISCHARGE.
4 ALL FLOWS IN gpd UNLESS OTHERWISE SPECIFIED.
5 DETAILS OF THE RADWASTE TREATMENT SYS-EW ARF PROVIDFD FOR PliRPOSFS ONI Y. 6 FLOWS IN PARENTHESES DAILY MAXIMUM. ,---------------1 I TO BORON I : RECYCLE SYSTEM : I I VJLUME CONTROL TANK I OILY WASTE SEPARATOR SYSTEM I I I SEE RADWASTE I : TREATMENT
: I I OVERF_OW ,------------------, FIRE PUMPHOUSE DIESEL FUFI 0 11 " 0 1 08000 BED DE MIN CATION o::MII\ I I OILY WASTE SUMP RECOVERY WELL WC.ILAN8S f-LOW 10 SUPERNrANT PUMP 27.000 (400001 LANDS SANITARY LAGOONS EOUALIZ/\TIOI\
BAS(N w-p CLEARWELL
>-w z-< wz "'"' OCW "' w > 0 DEM(N WASTE SUM=' ,---------------------, I I I I 1 SEE TO STEAl>.' 1 1 RAJWASTE GENERATOR 1 : -REATMENT SLOWDOWN : ..... I SYSTEM I I I "' Q_ "' 0 0 0 "' "' """"' W<t DEMINERALIZED WATER SYSTEM WATER TREATMEN PLAN-BUILDING FLOOR DRAINS LIFT STAT(ON / \ I NEUTRALIZATIO' BASIN " /
* pf-ADJUSTMENT iACIJ OR CAUS-ICI SAN! TARY WASTE SAND f-l L II:.R 0 CHLORINATION.EMERGE\JCv i-----------
Ill SLPPL Y 206DOO (5760001 ,------,I OEM(N ' }---------10-j CLEAR f-1--..(
L:_j )----CARBCN 1-lLIC.R WELL 4300 BACK WASH I 30000 I POTABLE WATER SYSTEM PLANT USE I 1---CHLORINATION 0 0 0 "' ...... 0 0 0 w 0 0 0 "' 0 0 0 "' CAT(JN DEMIN IF i ER ANION DEMIN MIXED BED OEM IN BLDG su*MP F IRE WATER 0 SIOHAGC. TANKS-121 FL!SH TO SWR REGENERATI0\1 CHEM(CALS (ACID & CAUSTICJ I
* Fl liSH WATFR TJ EQUALIZATION BASIN 1000 DEM(N STORAGe TANK TJ POWER OLOCK SYSTEIAS 27000 (360000) I I I G COAL-ESCER O(LY OIVF FLOJR FILTER WASTE 1000 DRAIN SUMP SJLID WASTE DISPOSAL (93600) U \J I-STCRAGE POWER BLOCK 216000 If CONDENSATE STORAGE I\
RECYCLING PRIMARY LOOP 106800 GPM VESSEL (PRESSURIZED WAIC.RJ STEAM GENERATORS (41 ?0000 MAKEUP FROM I I DEM:N I STORAGE I TANK I I I I I I I 35000 GPM HOT WELL TURBINE AND CONJENSER AUX LARY EQU(PMENT i I I I I I I I I I oSSENT(AL SI:.RVICI:.
WATER SYSTEM WTP CLEARWELL "AKtUe HEAT SINK lUHSJ PJNLl to NET RAINFALL DRAFT CJOLI\IG IOWC.H 2'6000 GPM BORON RECYCLE REGENERATION CHEMICALS
* CONDENSATE POLISHER DEMJ\J(SJ
!
WASTES II _I HIGH & LOW TDS I 3000 SEE RADWASTE I TREATMENT I t FROM [)FMIN STORAGE TA'K L ________ j RADWASTE TREATMENT SYSTEM tALL RADWAS E DEMINERALIZERS ARE NON-RECENERATIVEJ REACTOR COOLANT WATER 2500 I / EVAP FEED DE MIN m6 \_ri< HOLD-UP \f--.-------7-r'.,_
EVAP-f------< F :L TEY "-TANK ORA.TOR LIQUID RADWASTE "A'' TRAIN REACTOR / WAS-E ' 3000 eOU I PMENT ----.--j HOI 0-LP f---{ r1RAINS TANK eVAP 'Fm FILTER ' WASTE FVAPO Rt\TOR EVAP CONC f-lLIC.H L: au 10 WASTE CHARC ALlSOHtl TO IZATION EQUAL BA S(N EVAP CDND DE MIN DORIC ACID I AN< EVAP CDNO DEMIN TO PLANT SWR LIQUID RADWASTE SYSTEM ''B" TRAIN DRAIN TO SW'l AUX BLJG. FLOOR DRA:'s 6000 RADWASTE BLDG. FLOOR DRAINS FUEL BLJG. FLOCR DRAINS LAUNDRY AND HOT SHOWER LAUNDRY & 500 SHOWER WAS-EWATER SECONDARY LIQUID WASTE PO-ENTIALLY RA[)JOACT"VF FLOOR DRAINS 12000 SLW DRA(N COLLECTOR TANK FLOCR DRAIN TAN' LAU\IDRY & HOT SrCWER TANK B I AlJN)Rv & -10T SHOWER TANK A FLOOR ( N TANK STRAIN ,,---, ' D TANK F: LTER FILTER WASTE I TOR T DEM(N SLW h-.-------------------------------'---;;-c_..., E V A"O-f-'---_Jc_-,---------,---------, RATOR CIL WASTE OIL STORAGE tOISPOSED OFF SITE ) EVAP FILTER OF eVAP CONO FILTER W M TA'K FILTER AL*PS WASTE Q(L DISP-OSAL EVAP *CJNO TAN< WASTE MONITOR TANK A WASTF Mot\! TOR TANK B POTENTIALLY RADWASTE PROCESSING SYSTEMS SECCNDARY LIQUID WASTE FLCDR DRAINS 12000 (SUMrSJ (1440001 NON RADIJACT(VE AUXILARV 3UILDING EQU(PMENT DRAINS TUR3INE BUILDING SUMPS 'lECYCLE TO 'lEACTOR MAKEUP WA-ER STORAGE TANK A DISCHARGE MONITOR TANK B DISCHARGE MONITOR TANK CALSTIC ACID AJD ADD O(L SEP. FILTER RCTTJMS TANK SLW DEM(N >---4-1 S T RA ( N SLW I TO'l TANK CONDENSATE
______ _j POL( SHER REGEN:RATION WASTE 3000 LOW TDS (100000) ________________
STEAM GENERATOR BLOWDOWN A FILTER REGEN f-EXCf--AN REGEN HeAT EX CHAN STR*A l N h--\ BLJW DOWN 'IL TER ( 2 ) BLJWDOWN MIXED BEJ DE MIN B_OWDOWN MIXED BoD OEM IN RECYCLE TO ---'l-1 HOTWELL 216000 SLOWDOWN SURGE TAN' RECYCLE TO COI\JI:.NSA I C.
TANK TO REPRCCESS LOW TDS A I CAD-D27BA I 02/12/08 OUF ALL 001 TO =>LAI\T O:SCHARGE L:'e 27.000 (298.0001}}

Latest revision as of 04:21, 18 March 2019

Enclosure 4 to ULNRC-05893, Figure 1, Callaway NPDES Flow Diagram.
ML12271A451
Person / Time
Site: Callaway Ameren icon.png
Issue date: 08/13/2012
From:
Ameren Missouri
To:
Office of Nuclear Reactor Regulation
References
ULNRC-05893
Download: ML12271A451 (1)


Text

{{#Wiki_filter:24.480.000 1 TRASH RACKS DC u > INTAKE STRUCTURE 288' COO PUMP LUBE WELL SCReEN WA-ER 24.480.000 I 40.3?o.ooo HEATER DR A. IN/ BLOW DOWN RAW WATER BYPASS TO PLAN I J I SCHARGC. L INC. 3000000 144000 EXCESS 'LJW 0-17.280.000 SPRAY WATER 576.000 SUMP

  • I I I 009 0 ( 6000) : 1 4400000 I WATER TREATMENT PLANT STILLING BASIN 11 NTERMI TENT I 5 MILE P(PELINE TO PLA\IT COAGrANT STILLING BASIN --l RApiD POL YELECnOL YTE -----" CrLOR I NAT] ON _r------------t PUMP STATION SLUDGE Q SUPERNATANT 42oooo BLOW occu-OUTF AL_ 003 TO PLANT DOWN LATCRY CLAR(F(ERS

'-330000 ( 3) SLUDGE PUMP STATION

,. _____ _ LINE ZERO FLOW NE-------1 RA:NFALL SED(MENTATION LAGOON WTP 24.480.000 CLEARWELL MAKEUP BYPASS I OWC.H I 0 PLANT DISCHARGE LINE 3.320.000 (14.400.000) OUTFALL 016 I I I I S-RVICE WA ER SYSTEM TO UHS I I TTENT CIRCULATING WATER SYSTEM I EYAPORAT(CN 16.185.000 \ COOL lNG TOWER I IVVVVVVVV' SLOWDOWN OUTFALL BASIN 002 TO PLANT DISCHARGE LINE 4.840.000 ( 1 4, L 00, 000 ) CALLAWAY DRIFT 135000 Tll-ATMENT CIIEMICALS 568000 CPM FIGURE 1 NPDES FLOW DIAGRAM ACID l.)ISPC.HSANI HYPOCHLORITE/ SODIUM IDE CORROSION INHIBITOR ,--------MAKEUP DEMIN STORAGE TANK REACTOR 1\/AKEUP WAT:::R STORAGE TANK ,'-------- RECYCLE 5000 NOTES: 1. ALL PLANT OUTFALLS 009 TIE INTO A SINGLE PIPELINE WHICH DISCrARGES TO THE MISSOJRI RIVER JUST DOWN OF THE INTAKE STRUCTURE. 2 ALL SYSII:.MS HAVI:. t31:.1:.N S!Mlf-llli-H.Ll l-OR CLAR!IY. 3 ALL SYSTEMS AND MOST SIGNIFICANTLY, RADWASTE TREATMENT, ARE DESIGNED FOR FLEXIBIL:TY. IN RADWASTE, THE LEVEL IS DICTATED BY olRADIO_OGICAL CONTAMINATION, AN) NRC MANDATED DISCI-ARGE CRITERIA. AND blTHE NEED. FEASI8ILITv AND ECONOMICS OF RECYCLE VS. DISCHARGE. 4 ALL FLOWS IN gpd UNLESS OTHERWISE SPECIFIED. 5 DETAILS OF THE RADWASTE TREATMENT SYS-EW ARF PROVIDFD FOR PliRPOSFS ONI Y. 6 FLOWS IN PARENTHESES DAILY MAXIMUM. ,---------------1 I TO BORON I : RECYCLE SYSTEM : I I VJLUME CONTROL TANK I OILY WASTE SEPARATOR SYSTEM I I I SEE RADWASTE I : TREATMENT

I I OVERF_OW ,------------------, FIRE PUMPHOUSE DIESEL FUFI 0 11 " 0 1 08000 BED DE MIN CATION o::MII\ I I OILY WASTE SUMP RECOVERY WELL WC.ILAN8S f-LOW 10 SUPERNrANT PUMP 27.000 (400001 LANDS SANITARY LAGOONS EOUALIZ/\TIOI\

BAS(N w-p CLEARWELL >-w z-< wz "'"' OCW "' w > 0 DEM(N WASTE SUM=' ,---------------------, I I I I 1 SEE TO STEAl>.' 1 1 RAJWASTE GENERATOR 1 : -REATMENT SLOWDOWN : ..... I SYSTEM I I I "' Q_ "' 0 0 0 "' "' """"' W<t DEMINERALIZED WATER SYSTEM WATER TREATMEN PLAN-BUILDING FLOOR DRAINS LIFT STAT(ON / \ I NEUTRALIZATIO' BASIN " /

  • pf-ADJUSTMENT iACIJ OR CAUS-ICI SAN! TARY WASTE SAND f-l L II:.R 0 CHLORINATION.EMERGE\JCv i-----------

Ill SLPPL Y 206DOO (5760001 ,------,I OEM(N ' }---------10-j CLEAR f-1--..( L:_j )----CARBCN 1-lLIC.R WELL 4300 BACK WASH I 30000 I POTABLE WATER SYSTEM PLANT USE I 1---CHLORINATION 0 0 0 "' ...... 0 0 0 w 0 0 0 "' 0 0 0 "' CAT(JN DEMIN IF i ER ANION DEMIN MIXED BED OEM IN BLDG su*MP F IRE WATER 0 SIOHAGC. TANKS-121 FL!SH TO SWR REGENERATI0\1 CHEM(CALS (ACID & CAUSTICJ I

  • Fl liSH WATFR TJ EQUALIZATION BASIN 1000 DEM(N STORAGe TANK TJ POWER OLOCK SYSTEIAS 27000 (360000) I I I G COAL-ESCER O(LY OIVF FLOJR FILTER WASTE 1000 DRAIN SUMP SJLID WASTE DISPOSAL (93600) U \J I-STCRAGE POWER BLOCK 216000 If CONDENSATE STORAGE I\

RECYCLING PRIMARY LOOP 106800 GPM VESSEL (PRESSURIZED WAIC.RJ STEAM GENERATORS (41 ?0000 MAKEUP FROM I I DEM:N I STORAGE I TANK I I I I I I I 35000 GPM HOT WELL TURBINE AND CONJENSER AUX LARY EQU(PMENT i I I I I I I I I I oSSENT(AL SI:.RVICI:. WATER SYSTEM WTP CLEARWELL "AKtUe HEAT SINK lUHSJ PJNLl to NET RAINFALL DRAFT CJOLI\IG IOWC.H 2'6000 GPM BORON RECYCLE REGENERATION CHEMICALS

  • CONDENSATE POLISHER DEMJ\J(SJ

! WASTES II _I HIGH & LOW TDS I 3000 SEE RADWASTE I TREATMENT I t FROM [)FMIN STORAGE TA'K L ________ j RADWASTE TREATMENT SYSTEM tALL RADWAS E DEMINERALIZERS ARE NON-RECENERATIVEJ REACTOR COOLANT WATER 2500 I / EVAP FEED DE MIN m6 \_ri< HOLD-UP \f--.-------7-r'.,_ EVAP-f------< F :L TEY "-TANK ORA.TOR LIQUID RADWASTE "A TRAIN REACTOR / WAS-E ' 3000 eOU I PMENT ----.--j HOI 0-LP f---{ r1RAINS TANK eVAP 'Fm FILTER ' WASTE FVAPO Rt\TOR EVAP CONC f-lLIC.H L: au 10 WASTE CHARC ALlSOHtl TO IZATION EQUAL BA S(N EVAP CDND DE MIN DORIC ACID I AN< EVAP CDNO DEMIN TO PLANT SWR LIQUID RADWASTE SYSTEM B" TRAIN DRAIN TO SW'l AUX BLJG. FLOOR DRA:'s 6000 RADWASTE BLDG. FLOOR DRAINS FUEL BLJG. FLOCR DRAINS LAUNDRY AND HOT SHOWER LAUNDRY & 500 SHOWER WAS-EWATER SECONDARY LIQUID WASTE PO-ENTIALLY RA[)JOACT"VF FLOOR DRAINS 12000 SLW DRA(N COLLECTOR TANK FLOCR DRAIN TAN' LAU\IDRY & HOT SrCWER TANK B I AlJN)Rv & -10T SHOWER TANK A FLOOR ( N TANK STRAIN ,,---, ' D TANK F: LTER FILTER WASTE I TOR T DEM(N SLW h-.-------------------------------'---;;-c_..., E V A"O-f-'---_Jc_-,---------,---------, RATOR CIL WASTE OIL STORAGE tOISPOSED OFF SITE ) EVAP FILTER OF eVAP CONO FILTER W M TA'K FILTER AL*PS WASTE Q(L DISP-OSAL EVAP *CJNO TAN< WASTE MONITOR TANK A WASTF Mot\! TOR TANK B POTENTIALLY RADWASTE PROCESSING SYSTEMS SECCNDARY LIQUID WASTE FLCDR DRAINS 12000 (SUMrSJ (1440001 NON RADIJACT(VE AUXILARV 3UILDING EQU(PMENT DRAINS TUR3INE BUILDING SUMPS 'lECYCLE TO 'lEACTOR MAKEUP WA-ER STORAGE TANK A DISCHARGE MONITOR TANK B DISCHARGE MONITOR TANK CALSTIC ACID AJD ADD O(L SEP. FILTER RCTTJMS TANK SLW DEM(N >---4-1 S T RA ( N SLW I TO'l TANK CONDENSATE ______ _j POL( SHER REGEN:RATION WASTE 3000 LOW TDS (100000) ________________ STEAM GENERATOR BLOWDOWN A FILTER REGEN f-EXCf--AN REGEN HeAT EX CHAN STR*A l N h--\ BLJW DOWN 'IL TER ( 2 ) BLJWDOWN MIXED BEJ DE MIN B_OWDOWN MIXED BoD OEM IN RECYCLE TO ---'l-1 HOTWELL 216000 SLOWDOWN SURGE TAN' RECYCLE TO COI\JI:.NSA I C. TANK TO REPRCCESS LOW TDS A I CAD-D27BA I 02/12/08 OUF ALL 001 TO =>LAI\T O:SCHARGE L:'e 27.000 (298.0001}}