ML17347A836

Forwards Application for Renewal of NPDES Permit for Facility Submitted to EPA on 880728

ML17347A836
Person / Time
Site:	Turkey Point
Issue date:	08/03/1988
From:	Conway W FLORIDA POWER & LIGHT CO.
To:	NRC OFFICE OF ADMINISTRATION & RESOURCES MANAGEMENT (ARM)
References
L-88-334, NUDOCS 8808170064
Download: ML17347A836 (41)

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~~M ACCESSION NBR:8808170064 DOC.DATE: 88/08/03 NOTARIZED:

NO DOCKET FACIL:50-250 Turkey Point Plant, Unit 3, Florida Power and Light C 05000250 50-251 Turkey Point Plant, Unit 4, Florida Power and Light C 05000251 AUTH.NAME AUTHOR AFFILIATION CONWAYPW.F.

Florida Power&Light Co.RECIP.NAME RECIPIENT AFFILIATION Document Control Branch (Document Control Desk)

SUBJECT:

Forwards application for renewal of NPDES permit for facility submitted to EPA on 880728.DISTRIBUTION CODE: COOID COPIES RECEIVED:LTR

/ENCL 2 SIZE: TITLE: Licensing Submittal:

Environmental Rept Amdt 6 Related Correspondence NOTES: RECIPIENT ID CODE/NAME PD2-2 LA EDISONPG INTERNAL: AEOD/DOA ARM/DAF/LFMB NRR/DEST/SGB 8D NUDOCS-ABSTRACT E~ZZr 01 EXTERNAL: LPDR NSIC COPIES LTTR ENCL 1 1 1 1 1 1 1 0 1 1 1 1 1 1 1 1 1 1 RECIPIENT ID CODE/NAME PD2-2 PD AEOD/DSP/TPAB NRR/DEST/ADE 8H NRR/DREP/RPB 10 OGC/HDS2 NRC PDR COPIES LTTR ENCL 1 1 1 1 1 1 4 4 1 0 1 1 TOTAL NUMBER OF COPIES REQUIRED: LTTR 18 ENCL 16 h~~

FLORIDA POWER&LIGHT COMPANY AUGUST, 3 1988 L-88-334 U.S.Nuclear Regulatory Commission ,Attn: Document Control Desk Washington, D.C.20555 Gentlemen:

Re: Turkey Point Units 3 and 4 Docket Nos.50-250 and 50-251 NPDES Renewal A lication As required by Section 3.2.3 of the Turkey Point Plant Environmental Protection Plan, attached is a copy of the application for renewal of the NPDES Permit for Florida Power'ight Company's Turkey Point Plant.This application was submitted to the U.S.Environmental Protection Agency on July 28, 1988.If there should be any questions, please call us.Very truly yours, W.F.C y Senior Vice President-Nuclear WFC/TCG/gp Attachment cc: Dr.J.Nelson Grace, Regional Administrator, Region II, USNRC Senior Resident Inspector, USNRC, Turkey Point Plant 8808i70064 880803 PDR ADOCK 05000250 P PNU co~l PEOPLE...SERVING PEOPLE b'4'L

=O.OX l'000,'g'uO BEACH, Fl 334084420 July 28, 1988 CERTIFIED MAIL RETURN RECEIPT REQUESTED Mr.Bruce R.Barrett, Director Mater Management Division U.S.Environmental Protection Agency Region IV 345 Courtland Street, NE Atlanta, GA 30365 Re: Turkey Point Plant NPDES Renewal Application Permit No.FL0001562

Dear Mr.Barrett:

Enclosed is the NPDES Renewal Application or Florida Power&Light Company's Turkey Point Plant.If there are any questions regarding this application, please direct them to Winifred Perkins at (407)694-3645 or Ron Hix at (407)694-3622.Sincerely, T.R.Fair Manager Environmental Permitting

&Programs TRF/RHH/bf Enclosures cc: J.P.Subramani-DER DERM an FPL Group company f I (fII(vin ereeS era SrreCed fOr ali re type, i.e..(2 CharSCrarrilnohi rOrmVIPP?OVCO.

IrIVIO IVO.CueO4AraarIPPrOVer e4PIree/.dr WO GENERAL U.S.CNVIRONMCNTAL PROTCCTION ACCNCY I EPA I D NUMSER~VEhA GENERAL INFORMATION IA C 0/K I~Consoffdaord frsnnirsProgrsnr F F L D 0 0 0 7 3 3 6 8 3 0 (Read lhc"Genera(fnerrirer(one" before start(ne.r

~1~~~I.EPA I.D.NUMaIER III.FACILITY AME FACILITY'AILING ADDRES!V I AC ILITY'OCATION'"/f I=L 33101 lilrOES t I=LJOtslioc

i P'r(R 6 L T-TURKEY I" GIST;I SA)4U=~TUI.KcRS c v'VIPON hi(R rr:J'-uX~r13 l00'~1AI4 I+LrNCRAL INSTRUCTIONS<<

If a praplfntsd label has been-provided,.affix it in the designated space: Revfesv the In(olin.ation carefullY if any of It Is lncorrear cross through it snd enter the correct data fn the appropriate fill-In ares befovv-Abo If eny of the prsprintsd data is sbsarrt.(tfre.areeStrs-tfre left of the label grace (lstr.the;infonnelforr that shoufd afrpssrl, please provide It1n the proper fili-fn srss(sf below.;If the Isbsl fs complete snd correct, youlnaed not complete Items I.III, V, snd Vl (srrcafst.-V(-B Ivhiclr m%T be comp(clad rs(ford(esa)" Complete sll items if no label has been provkiatL Refer to the instructions for dstaf~ltem".descrfp-tfolls and for ths lsgsi authorlaatlone Under which this data is collected.

II.POLLUTANT CHARACTERISTICS INSTRUCTIONS:

Complete A through J to determine whether you need to submit any permit application folmS tO the EPA.If you anssvac"yaa"..to any questions, you must submit this form and the supplemental form listed in the parenthesis following tha question.Mark NXN in the box in the third column if the supplemental form is attached.If,you answer"no" to each question, you need not submit any of these forms.You may answer Nno" if your activity is excluded from permit requirements; saa Section C of the instructions.

Sea also, Section O of the instructions for definitions of bold-faced tetmL SPCCIFIC QUCSTIONS Tae NO~O O$1 ATTAcNC SPCCIFIC QUCSTIONS~O N ll Tao No ATT*CNCO A.Is this facility s publicly owned treatment works wnich results in s discharge IO waters of the U.S.t IFORM 2AI Is lnis s SCiiily wnic current y results in I argeS lo waters of ths U.S.other lhsn those described in A or 8 above?FORM 2C E.Does or will this facility treat, store, or dispose of hazari)ous wsslsst IFORM 3)8.Doss or will this facility (either err(sting or profsossdf X include 5 concentrated animal feeding operation or aquatic animal production fac8lty whfch results in a discharge to waters of the US.?IFORM 28)5 l is a proposed so ily o sr drsn osa escn in A or B sboyof which will result in a discharge to of the U't FORM 2D)F, Do you or will you inject at this facility fndustrisl or X municipal effluent below the lowermost stratum con-taining, within ons quarter mile of the well bore, underground sources of drinking walsrt IFORM 4)X ll 1\$$0 vou oc wl you Infect al I Is sci I'Iv shy p U wsler or other fluids which sra brought lo the surface in connection with conventional oil or natural gss pro-duction, inject fluids used for.enhanced recovery of oil or natural gas, or inject fluids for storage of Ifquid h drocsrbons?

IFORM 4)X$4 1$$4 H.Do you or will you Inject at this facility fluids for spe-cial processes such as mining of sulfur by the Frasch , process, solution mining of minerals, in situ combus tion of fossil fuel, or recovery of geothermal enerffyL IFORM 4)Ir 4 4.~~s l Is aci Ily a pfo stationary Rrurce w I Is one of the 28 Industrial categories Ifsted in the in.strUClions and which will potentially emit 100 tons per year of sny air pollutant regulated under the Clean Air Act and msy affect or be located in sn attsfnmsnt area?IFORM 6)III.NAME OF FACILITY SNIP T U R K E Y P 0 I N T P L A N T I~Il$4 IV.FACILITY CONTACT h.NAMc aI TITLc ((ae4 f(re4 Ia (lilt)~1~s ly 5 p IXIlce I.I~NOT one of the 28 industrial categories listed in the fnstluCtiOOS end which will potentially emit 260 tons.par year of eny elf Pollutant fsgUlatsd Under the Cfaarl4 Afr,Aa and may affsa or be located in an~rea?IFORM 6)AIC Cr I r r,vr retlkgl 44~.PNoNC (area code Ie no.i.C 2 BURKETT T 6 CROSS J PLANT MGR~4 44~4 V.FACILITY MAILING ADDRESS 246 130~4~I~1 44 r4 rrr h STRCCT OR P.O SOX 3P.O.BOX 4769 CCCSTT OR TOWN 4PRINCETON Vl, FACILITY LOCATION AISTRCCT ROUTC.NO OR OTNCR,SPCCIFIC 59 5MI EOPFLA CITY~~I~Sr COUNTY NAMC DADE~.~r 4 rvv'pv44 orlrIrA ,r" Cl C STAT Or CIP COOC.F 4 vrm$44 PL 3'3092..I.i'm'+~~TCfSXW

&CNTIFICR'~"-C+sr$4~~f4"'@~>>ON PALM D 4$.'f'Irl~~$$$.4r k A<-AIL'CCSTVOltTOWN

'" 6PLORIDA CITY~STAT C ZIf CODCr PL 3303 ,OI EPA Form 8610-1 IRev.1M0)CONTINUE ON REVERSE (specify)C THIRD IS~~~~Vill.OPERATOR INFORMATION ONTINUED FROM THE FRONT Vll.SIC CODES (4&igi t, in order of priority)A II I It ST (specI fy/7 4 9 1 ELECTRIC SERVICES~'~~(specify)(specify J~SCCOND o vouRTH V A, NAME F L 0 R I D A P 0 W E R&L I G H T C 0~I~c.sTATus or oecRATDR (Enter the appropriate letterinto the answer box/if"Other", speclfyJ la the~usted ln l sane VlllrA allo owners r Qg YES'I.NO S~aa~r D, PHoNe (area code R.na)...AL S c STATE P c PRIVATE M c UBLI (other tr)an federal orstate/0 c OTHER (spec(fy)C STRCCT OR P.O.OOX~S (specify J C A 407 694 3635 I~I~I~)I$$SS~~P.O.B 0 X 1 4 0 0 0 I~P, CITY OR TOWN~S IX~r~)Ir<<r<<~)Asrsr)ln 8 JUNO BEACH I~Is the facility located on Indian landsr L 3 3 4 0 8 C3YE ggNO.as~e~I~)e)~I X.EXISTING ENVIRONMENTAL PERMITS A.Nrocs (D(scharr(es to Surface Water/C T 9NFL0001 562 I~I~II I~s.uIc (Underground

/niectlon of Flu(ds)o.9 so (A(r Em(ss(ons from Proposed Sources/C T I 9 P'I 0~~I~~)~~C 0TH cR (spec(fy J I~C't I 9 U~S I~~)\~c.ncaA (//asardous Wastes)C T~(spec(fy)State IWWTS c 0TH cR (specify J (specify J County IWWTS C T I C T I 9RFLD00073 3 6839 IWO-016~'I'I~~I~~S~~~)~~~I~XI.MAP Attach to this application a topographic map of the area extending to at leastone mile beyond property boundaries.

The mipgmtsttow",',-the outline of the facility, the location of each of its existing,and proposed intake and discharge structures, each of its haiartfous wasta-treatment, storage, or disposal facilities, and each well where it injects fluids underground.

include all springs, rivers and ather sur'face.water bodies in the map area.See instructions for precise requirements..

XII.NATURE OF BUSINESS (provideabrief descriplion Electric Power Generating Station I".~SIC,~S l j<<II I~~I XIII.CERTIFICATION (ass/natttscsforle)

I canlfy Vnda.penlsftyof:fav'v~.'I.

persfsna(ii/~Feanhecf'nQi aif'ffss."ar)bmit ted.attachmentr and,'.tilit-Minyan;,fiiqu~of;Siiar.

'"'""" forebtiJKhg~7irfonr(a application, i believe tisat'tf)e infoimation ia true accu<<ate and carqplihCJ.ans iwafsr.'thnt2here.araiignificfurt pena false information, inctuding the possibility of fine and imprIconment;.

A.NAM C 4 Ov)IICIAI TITS C (type or print)T.R.Fair, Manager Environmental Permitting

&Programs COMMENTS FOR OFFICIALUSE ONLY.C C~~I~EPA Form 3610-1 IRav.1040)R~Sr SION*C C DATC SIONCO.L'w:.ia V Ir IS.U.S.Ceveraaeat Prtattal Otsfce I Isn't'94~94$/59991 T~II r

-'sse'onnt or Ivoe in the unshaded areas onlv.EpA i.o.NvMuc,IRRcvpy lrnm iieni I vl ruriii ii PLD 000733683 OIWB iVo.2040~86 Approvel expires 7-31-88 FORM'NPDES iSEPA U.S.ENVIRONMENTAL PROT ON AGKNCY APPLICATION FOR PERMIT TO Dl GE WASTEWATER EXISTING MANUFACTURING, COMMERCIAL, MINING AND SILVICULTURAL OPERATIONS Consolidated Permits Program I.OUTFALL LOCATION For each outfall, list the latitude and longitude of its location to the nearest 15 seconds and the name of the receiving water.A.V L NUMOER lists O.LATITUOK X.MIII i.SEC~I CEO, C.LONGITUOE I, OEO.X.MIII,)~SEC o.REcEIvING wATER inamel 001 25 26 09 80 19 52 No discharae to waters of U.S.I I I I II.FLOWS, SOURCES OF POLLUTION, AND TREATMENT TECHNOLOGIES

'.Attach a line drawing showing the water flow through the facility.Indicate sources of intake water, operations contributing wastewater to the effluent, and treatment units labeled to correspond to the more detailed descnptianS in Item B.Construct a water balance on the line drawing by showing average flows between intakes, operations, treatment units, and outfalls.If a water balance cannot be determined (e.fs,/or certain mining actnlitfetJ, provide a pictorial description of the nature and amount of any sources of water and any collection or treatment measures.I B.For each outfall, provide a description of: (1)All operations contributing wastewater to the effluent, including process wastewater, sanitary wastewater,"ooling water, and storm water runoff;(2)The average flow contributed by each operation; and{3)The treatment received by the wastewater.

Continue cn additional Sheets if necessary.

OUT'ALLN.Erl e.OpKRATION lllsrl O, AVERAGE PLOW linclude unirsl z.OPERATIONlsl coNTRISUTING PLow 3~TRKATMKNT a.DESCRIPTION O.LIST COOKS PROII TALRLE EC I 001 Recirculated condenser coolina water Units 01, 02, 3 44 auxiliar e ui ment 2763 MGD Rec cled, reuse of treated effluent 4C coolin water Screenin No 3 T a tities list d under mass n bers in Part V A B and C rn~'I~~I"Jll uldellnee eu re s p>><<~oPIIIcIAL.UsK.oNI Y.fefflileisaa il~I EPA Form 3610-2C IRev.2-85)~<<>><<<<>>IIIR j VI PAGE I OF 4 I~II CONT E ONR I l,,lily

".ONTINUED FROM THE FRONT C.Except for storm runoff, leaks, or spills, are any~>e discharges aescribed in Items II-A or 8 interm>ttar seasonal I YES (complete the folto>ping tablet~+NO is~ection IIIJ 3.FREQUENCY 4.FLOWI.OUTFALL NUMBER'list j 2.OPERATION(LJ CONTRIBUTING FLOW (list J a.PAYS b.MONTHS PER WEE>A PER YEAR (specify (speci fv auerage I auerage I I VONV TCOIM AVCNA4C MAXIMVM OAIVY a.PLOW RATE (ln mgit J b.TOTAL VOLUME (specify u>lth unite).:C, DOR-<ATION I VONO TCIIM I, MAX>MOM AvcIIAOc oAII,Y (ln dayeJ N/A i III.PRODUCTION A.Does an effluent guideline limitation promulgated by EPA under Section 304 of the Clean Water Act apply to your fac>hty?'X>YEs (complete Item III BJ NO Ita tO Sect(on IVI 8.Are tne limitations m the applicable effluent guideline expressed in terms of proaucuon (or orher meesure of operer>ont?

YES icomplete Item III Ci g No Ieo io oection II I C.If you answered"yes" to Item III-B.list the quantity which represents an actual measurement of your ievel of production.

expressed in the terms and units used in the applicable effluent guideline, and indicate the affected outfaiis.OVANTITY ACN OAT 1, AVERAGE DAILY PRODUCTION C OPCNATIONo AROOVCTo MATCC>AI CTC O, VNIT5 OO MCATVNC 2.AFFECTED OIJTFALLS (tlet outfall numbereJ N/A IV.IMPROVEMENTS AoSttr>oo~orJ or A.Are you now required by any Federal, state or local authority ta meet any implementation schedule for the construction, upgrading Iyof waste-water treatment equipment or practices or any other environmental programs which may affect the discharges described ln this appii., Iaif>eludes, but is not limited ta, permILcooditfons~nlsttatfve oranfarcement orders, enforcement compliance schedule letters, stipulations,, grant or loan conditions.

+YES (complete the folio>utng tableJ+No (go to Item ItrBJ I.IDENTIFICATION OF CONDITION, AORKKMKNTo KTC 2 AFP'KCTKP OLITFALLS a NOo ILCOVCOC OP O>CCII*OOC S, SRIKF DESCRIPTION OF PROJECT O N/A~~'o foe your dischergesJ you now have underway or which you plan.Indlcat>L whether each program is now underway or planned, and Indiattfpgjdlsr>actual or"-~--".a--.:: ':~..EPA Form 3610-2C (Rev.2-86)PAGE 2 OF 4 CONTINUE ON PAGE 3 CPA i.o.rIVSsOCRIcopy lrom iiem I Or eorm lr'A%TINUED FROM PAGE 2 000733683 i.INTAKE AND EFFLUENT CHARACTERISTICS

'orm riooroveo.

vhfB No.2040~86 Approval eroires 1 31.88~.9,&C: See instructions before proceeding

-Complete one set of tables for eacn outfall-Annotate the outfall number in the space provided.NOTE: Tables V-A, V.B, and V-C are included on separate sheets numbered V-1 through V.9.D.Use tne space below to list any of the pollutants listed in Table 2c-3 of the instructions, wnich you know or have reason to believe is discharged or may be cischargeo from any outfall.For every pollutant you list, bnefly describe the reasons you believe it to be present and report any analytical data in your possession.

POLI UTANT 2.SOURCE I.POLI UTANT 2.SOURCE N/A: VI.POTENTIAL DISCHARGES NOT COVERED BY ANALYSIS is any pollutant listed in Item V-C a substance or a component ot a substance wnich you currently use or manufacture aa an intermediate or final p<oductor.

byproducts

~"~fp~+t f>>'C~>>"...

.oisrrssar.cv>>~'w:

rIO leo ro item Vl BJ N/A EPA Form 3S10-2C (Rev.2.BS)PAGE'3 OF 4 CONTINUE'ON REVERSE

'.ONTINUED FROM THE FRONT VII.SIOLOG ICAL TOXICITY TESTING DATA Oo you nave any knowledge or reason to believe that any biological test for acute or chronic toxicity has recetving water in relation to your discharge within the last 3 yearsf~~vKS lldentify the testis)and describe their purposes betour)n made on any of your discharges or on a--~""i.s4-K)tto fao to Section Vfff)N/A VIII.CONTRACT ANALYSIS INFORMATION Were any of the analyses reported in Item V performed by a contract laboratory or consulting firm)K)vKS ft4t the name.address.and telephone number of, and pollutants analyzed by, each such laboratory or finn betour)+No fgo to Sectlotr IX)A.NAMK 8.ADDRKSS area code e no.~AR D list Environmental Science&Engineering, Inc.P.O+Box ESE Gainesville, FL 32602!(904)332-3318 All IX.CERTIFICATION rr,4 1 e~'I/certify under penalty of law that th/s document andallattachments were prepared under my direction or suparvisioninaccordance withe systimiteipnedto assure that tfualified personnelproperly gather andeyafuate theinformation submitted.

Based onmyintfuiry of the person or persons who manege thasystam or.those persons directlyresponsible forgathering theinformation, theinformation submitted/s.

to the best ofmyknowledgeandbelief, uue.accurate.andcotnpfete-l am aware that there are significant penalties for submitting falseinfonnation.including the possibility o/fine andimprisonment for knowing violations.

A, NAMK 4 oFplcIAL TITLK ltype ot'rltrt)T.R.Fair, Manager Environmental Permitting a Programs..((j+O.PHONK ISO.larea code&no.)(407)694-3635 D.DA TK SIC NKD~>>k EPA Forltl 361(AC (Revr 2 85)~CF A4FA I<ill>v<l<II ll l>nil>NI)2>I IV<k)SO AI)l)Ale'.)I

~'<p)>i's f 3 I a>>EI A>.o Ns>><>UI I'~~I~~Il~Nll IH NI I~lf I<)1>>>II Oi>T>As s N<>001 3.UNITS i<>><'rifv If bla)>k)4.INTA K E f<>pli<)>nil) 2.EFFLUENT PLEASE PRINT OR TYPE IN THE UNSHADED AREAS ONLY.You may lcpoii soi>>e or all of this information on separate sheets fuse the same format)instead of completing these pages.SEE INSTRUCTIONS.

PLD000807461 V.INTAKE AND EFFLUENT CHARACTERISTICS (continued fro>n page 3 of Form 2-C)~~ART A-You must provide the results of at least one analysis for every pollutant in this table.Complete one t;ilile for iiach outfall.See instructions for adr)i(iona) details.PPLLUTANT u I gf'L I ls)(I)MASS'1 4.MAXIMUM DAILY VALUE:Is)CONCCNTNAT<OH (I))<AS~t~I CONC TNT<<ATION (1)MAI'.MAXI M Sg g(AY VALUE C.ON)/~VALUE u.No.Ol'NAL s S a.CONC EN TRAl lON 4.MASS COCCI hfNAT<ON I)I MALS a.LONG TLRM 4.NO OI" ANA1.VSES-:tt em(eel.;Xyge>l Demand<(f)OD).-i;C}le>(lice(xygen'Demand OP/)I>-.l~.~Tl)>>e1 Organic'bomtr O)".)TotaySusoendpd Pgf'PZSS)')~'.,<<I'I Iereturo" r'>)I>Imar)

'!'ALUE VALUE 2592 39 2 VALUE VALUE 1953 34 5 VALUE VALUE 1245 32.0 MGD'C VALUL V A L I IL 1245 24.5 33SQ MAXIMUM MAXIMUM MINIMUM 8 03 MINIMUM 8.03 ,M!It.s.Sl ANOARD UNITS 8.06 8.06 3.EFFLUENT POl LUT>ANT>AND.CAQ NO'f(ee>il(cbla) b.O~LICVE A~SANT e.~c-IEVC~NC~cHT>.NO.0 I YSES)IN><L Yes s Is CONCCHTHATION (II MASS (1)I~ALL (I)MASS (I)MAS~I CONCCNTNAT<ON I COHCCNTAATIOH CONC L H I<<AT<OH 2., AIP$>Mark"X" in column 2-a for each pollutant youknow or have reason to believe is present.Mark-X" in column 2-b lui U>ch pollutant you believe to be absent.If you mark column 2a for any pollutant!'h)oh is limited either directly;or (ndirectly but expressly, in en effluent limitationsguidelin,youmust provide the re uhs of ai least one analysis for that pollutant For other pollutants for wliich youmalk column 2a.you must provide quantitative data or an explanation of their presence in your discharge.

Complete one tal>le for each outfall.See lhe instructions lor adduional details and req>>ir em>>>>le i~ptI TL MARK'X'I.I)NITS 5.INTAKC f<lpII<)UJII e MAXIMUM DAILY VAI UE.MAXI pM ajar gtLY VALUE C.LONG TfpM pg}lri.VALI)l.I l>O Ol a.LONGE>>M ICATION I~MASS Lsrernlde~~2$()947-9)<5<5 m~/L lbs (5 2.C)lier(ne,-'..-.

nes);Pesldual.(If'-"<>.l>':

Not PreS 42 ntly chio inating....2 msf~L PCU lbs 41....2 100ml 15.~I" 0.63 I 1.4 X 10 0.45 5 2.2 X 10 mg/L lbs 0.46 1.4 X 10 5 EpA Form 3QO 20 fRev 2 8()}BASED ON 1987-1988 HISTORICAL PA(AE V-I DATA**BASED ON 1986-1987 HISTORICAL DATA CONTINUE ON REVERSE ITEM V 0 CONT INIIED I'itlJM F IIONT ly POLLUT-ANT AND CAS NO.((f cuoiloblc J a.NN ICVCI r IIN ICNT n.ua.~~c v~Ir r N I~Nr rr.MARK'X'CONCCNTNA'IION ltl MA~I I CONE I',N I@r AI I~rrr I'I IAAF~3.EFFLULI<T MAXlMUM I3*rL~uALtsL u.MAXIM M 3f p(Y VALUu C.l CI I I I~'I L I I M tlf III'rrll 1 rr I I~I~~rr,r~~rt p~Ir~I I I~I I Ill I I~r rl;I.L~1~I rI II I I tt I I't'I'i~~IAI~I, rrtl Ill I~~~~~Il-I~I I~p.Nltropan, Total Orpanlc (os NJ h'Oll and Grease','L Phosphorus (osPJ,'otal

.P723-14 0)f.Radloactlvlty I))Alpha, Total.'2)8ata.Total"A I3)Rac))un';Totai 1 I" (4)Radium 220, Total r'I X X 0 0.01 212 110.8 0 08 3.2.Z 10~QL 3.2 Z 1 168 100 2 2 mglL lhs pCi/L pCi/L mgLI lhs mg/L.lhs Q.Ql 234 67 1-6 X 1Q.3 2 2.X.10 3 2 14 Ou ata rtrr, (os d04J~~1 4808.7941 I.Sutfkl~ada)IJ';m, u'to.(os g(73J;A'..f)4288~n.)guh actanti'usrpt I{7Q))4194);~

wrote)l".<.-~5l'Ott Total':1 th!N I7 r;Total s'.P44048.4)~.Iron, Total f743949 8)X 2910 C O.l<95 3800 4 23 6.2 X 10 2880 0.1 495 8.2 X 10 3595 C 23 1.4 X 10 1.8 X 10 mg/L mg/L ug/L UR/L ug/L lbs lbs lbs lbs lbs 2800 0.1 (95 3660 (23 87 X lO 1.1 X 10 6 2 0-2 t.Mapnaslum, Total (7439.95.4)

.Mohrbdanum, Total P 439-98.$)16~~-9>~}3.6 X 10 84 QC2 XDO.1 X 10 2 Ug/lr uggL lbs Ibs 771 11.3 2.4 X 10~3.5 X 10 P%NW l~.P~~P~10 I Ib324))".$

i~~~~1 lrlIEI IVDE r EPA Form 3610-2C tRev.2-86)ttl:.irtl OWa PAGE'V-2 u/L lbs<4 CONTINUE ON PAGE V-3 p~~CONTINUED FROM PAGE 3 OF FORM 2-C spA I.o.NUM acR (co<>y from Item I of Form Il PLD000807461 OUT<<A<.L r<>~'.001',<H~Hl<I!i<YI~.">II><I l.'..IIII<<f IAII V~<III<'l/,<I~~~PART C-If you are a primary industry and this outfall contains process wastewater.

refer to Table 2c-2 in the instr<<imns io<I<><<<<i Ire wliicli of Ihu Gc/MS I<actions yo<>><<us<<Io:.I II>r II]!irk-x-i<i<<I<<<annul:, II y<<II i>>e not ru)u<red to mark coliunn 2.n f I<coi<liu>i<i I'us(ri.i.n i<>pi>I<s'asiaweter ou(falls.and nonrarfuired GCIMS free(fons J, mark-X-in column 2b for each pollutant you know or Ii,.v>i..is<Xi to l>l>lieve is present.Murk-X" in>n>lunin 2 c loi e icli l>oil<>to It y<ii believe is absent.If you mark column 2a for any pollutant, you must provide the results of at least one aria lysis for t ti.lt I,alt iiwi>tlf yoii mark cohi<un 21>f<>r aiiy p<<ll<>I J>II, yG>i ill>>a<pio vide I I>I!i<4 of at least one analysis for that pollutant)f you know or have reason to believe it will be discharged in I o>><:en<roti.>na

<>I 10 pi>b or greater If yui<inaik colunin 2li f<ir o<;rnlei>i.

ac<yl<>nitiilo.

2.1 dlnitrophenol, or 2.methyl-4, B dinitrophenol, you must provide the results of at least one analysis lor>.a<:I<of thus<.I.<<I<<i<ants which you hnow or have runs<>i>to believe<Iiut yoi<disci<<<<II,i in concentrations of)00ppbor greater.Otherwise, for pollutants for which you mark column 2b, you most oi<tlcr subni t.<II.,>: I ono analysis or briefly ilnsciibo tliuio I ons ihe I>ollutunt is exi>octad I<>be discharged.

Note that there are 7 pages to this part;please review each carefully.

Complete one table fall 2(>i>ga>;.<

Ictions foi a<lditional details and requirenienls

)I PQLIQUTANT

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-BASE/NEUTRAL COMPOUNDS (continued}

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NO STING RE IRED PAGE V-9

'-l C X 1 I Ak V~'g , r'e J l'C%~g C~<t'+>w as TURKEY POINT PLANT GENERAL PLANT DESCRIPTION AND DISCUSSION OF MAJOR PROCESSES AND ASSOCIATED WASTE STREAMS Florida Power&, Light Company's Turkey Plaint Plant is located at latitude 25 26'09"N and longitude 80 19'52"W, on Biscayne Bay, approximately nine miles east of Florida City, Florida.The plant and its surrounding area covers approximately 12,700 acres (See Attachment 1).The plant consists of two fossil fuel units (Units 1 and 2)and two nuclear units (Units 3 and 4).Units 1 and 2 each have 402 megawatt net continuous capability.

Unit 1 was put into commercial service in 1967 and Unit 2 was put into commercial service in 1968.Construction, design, and operational aspects are essentially the same for both units.Units 3 and 4 each have 693 megawatt net continuous capability.

Unit 3 was put into commercial service in 1972 and Unit 4 was put into commercial service in 1973.Construction, design, and operational aspects are essentially the same for both units.All four units obtain their once through condenser cooling water from and discharge to a closed cycle recirculating cooling canal system (cooling canals).There are no discharges to waters of the United States from the plant site.Major processes at the Turkey Point Plant which generate wastewater as a function of operating activities for the purpose of steam production to generate electricity are: Process Units 8.9.1.Boiler and Steam Generator Makeup Water Purification 2.Combustion Residue 3.Boiler Blowdown 4.Steam Generator Blowdown 5.Chemical Volume Control System 6.Once-Through Co'ndenser Cooling Water System 7.Auxiliary Equipment Cooling Water Systems Condensate Polisher Intake Screen Wash Fossil and Nuclear Fossil Only Fossil Only Nuclear Only Nuclear Only Fossil and Nuclear Fossil and Nuclear Nuclear Only Fossil and Nuclear Information concerning flow rates described below may be found in Tables for the various.processes 1, 2, and 3.1.Boiler and Steam Generator Makeu and Nuclear)Water Purification (Fossil Municipal water is passed through a coagulator and a fine sand filter to remove suspended solids and then passed through activated carbon filters for additional removal of organic and inorganic suspended solids.The softened, filtered water is further purified by gassing through a cation resin bed where cations such as Mg+and Ca++are removed, and through an anion resin bed where anions such as S04=and Cl are removed.Finally, it passes through a polishing mixed bed containing both cation and anion resins.After a period of use, the anion and cation resins become exhausted and must be returned to their original condition (regenerated).

Cation resins are regenerated with 5%H2S04 (sulfuric acid)where H+replaces the cations exchanged by the resin during the demineralization process.The anion resin bed is regenerated with 5%NaOH (Sodium hydroxide), where OH replaces anions exchanged by the resin during demineralization.

The sand and carbon filters are backwashed with municipal water to remove trapped suspended solids previously filtered from process water.Corrosive anion and cation regenerant waste (pH<2.0 SU or<12.5 SU)is sent to a totally enclosed treatment facility where the pH is adjusted to a range of>6.0 SU to<8.5 SU.This waste is then discharged directly to the cooling canals or routed with the remaining anion and cation regenerant waste and sand and carbon filter backwash waters to the lined concrete neutralization basin (B-1)(see Attachment 2 for location)for neutralization and dilution treatment.

Final effluent is discharged to the cooling canals.2.Combustion Residue (Fossil)A carbon reinjection system provides a means for collecting carbon and unburned by-products of combustion in the flue gases.This carbon residue is recycled back into the boiler fire to maximize the use of combustible material.The resulting fly ash and slag contain various non-combustible compounds, which are sluiced to one of two solids settling basins (B-2 or B-3)(see Attachment 2 for location).

Combustion residue is also accumulated during various maintenance f unctions.Supernatant f rom the solids settling basins is discharged to the cooling canals.Residue is chemically fixed on site or removed for vanadium reclamation.

3.Boiler Blowdown (Fossil)Three forms of sodium phosphate are added to the boiler water for control of calcium and magnesium scaling.Ammonia hydroxide is added for pH control.Hydrazine is added for

oxygen removal.Undesirable boiler water contaminants such as Cl and silica can be introduced from condenser tube leaks.The boiler blowdown is used to control and maintain desirable boiler water chemistry.

Boiler blowdown is taken from the bottom of the steam drum and contains such materials as silica (which can deposit on steam turbine blades), dissolved solids such as sodium phosphate mentioned above, and metals such as copper and iron.Some of the boiler blowdown flashes into steam and discharges into the atmosphere.

The remaining liquid portion of boiler blowdown not recovered and reused is routed into the cooling canals.4.Steam Generator Blowdown (Nuclear)High purity water is generated by the water treatment plant by way of carbon filtration and anion and cation exchange demineralization.

The high quality water is routed to the steam generator for makeup to the water/steam cycle.Ammonium hydroxide is added for pH control and Amerzine (hydrazine based)is added for oxygen removal.Undesirable contaminants such as Cl from condenser leaks can contaminate the steam generator water.Strict operating specifications require that suspended and dissolved solids be maintained at very low levels, therefore, when the level of these parameters increase, they must be reduced by steam generator blowdown.This blowdown is routed to the cooling canals.During overhauls (fossil and nuclear)and/or refueling outages (nuclear only)the boilers, steam generators, feedwater systems, and/or condensers may be placed in a static mode where the internal metal surfaces of these components must be protected from corrosion.

The typical method used is to fill the system with a hydrazine/ammonia/demineralized water solution.This solution must be drained and discharged to the cooling canals.The solution used to protect the steam generators and condensers in the nuclear plant, when discharged, has a pH of 10.5 standard units and contains 200-300 ppm of hydrazine.

Approximately 1,000,000 gallons of the solution is discharged following each overhaul or refueling.(Quantities and hydrazine concentrations discharged by the fossil.units are significantly lower than those discharged by the nuclear units.)5.Chemical Volume Control S stem (Nuclear)This waste stream originates from various maintenance and operational activities which take place in the reactor auxiliary building (RAB).Flow from the chemical volume control system is intermittent.

6.Once-Throu h Coolin Water S stem (Fossil and Nuclear)Water is withdrawn from the closed-loop cooling canal system through two intake canals on the east side of the plants to cool the system condensers.

The waste heat from the steam is transferred to the cooling water in the condensers, and the cooling water is discharged back into the cooling canal system on the west side of the plant.With all 12 circulating water pumps operating, the cooling water f low volume is approximately 1,800,000 gpm.At full load, the cooling water temperature rise is about 16oF.7.Auxiliar Equi ment Coolin Water S stem (Fossil and Nuclear)An additional 120,000 gpm of water from the cooling canal system is used to cool, via heat exchangers, the closed cooling water system.This water is pumped from the intake structures and is discharged into the discharge canal on the west side of the plant.8.Condensate Polisher (Nuclear)The condensate polishers are utilized during the startup of Units 3 and 4.Effluent from this system is discharged directly to the cooling canals.Flow from this system is intermittent.

This effluent may contain small amounts of powdered resin.9.Intake Screen Wash (Fossil and Nuclear)Intake traveling screens are used to prevent debris from reaching the condensers.

Cooling canal water is pumped through spray nozzles to clean these screens.This wash water is routed to a debris pit at the intake area or to the discharge canal.Plant maintenance is required to maintain the steam production process, to maximize combustion e f f iciency and to minimize air emissions.

Routine maintenance cleaning of key plant equipment is performed at scheduled intervals.

Maintenance cleaning operations generally result in the generation of wastewater.

Maintenance processes producing wastewater are: Process Units l.Economizer Hopper Wash 2.Air Preheater Wash 3.Stack Wash 4.Dust Collector Wash 5.Boiler Fireside Wash 6.Boiler Waterside Chemical Cleaning 7.Equipment Area Routine Cleaning 8.Miscellaneous Fossil Fossil Fossil Fossil Fossil Fossil Fossil Fossil and Nuclear

Information concerning flow rates for the various maintenance activities described below may be found in Tables 1, 2, and 3.Economizer Ho er Wash (Fossil)The economizer section of the boiler collects combustion by-products during plant operation resulting in slag formation.

Periodically, the interior surfaces of the economizer hoppers are washed.Water washing is performed approximately three times per day.The wash water is discharged to one of two onsite solid settling basins.The supernatant from these basins is discharged to the cooling canals.2.Air Preheater Wash (Fossil)Air preheaters operate in an atmosphere near the dewpoint of the exit gases.Since there is some deposition of sulfur compounds on the preheater surface, wash water is typically acidic.Air preheaters are water washed weekly followed by rinsing with a 15%soda ash and sodium tripolyphosphate solution wash.The air preheater wash effluent is routed to and treated in one of two solid settling basins.Supernatant from these basins is discharged to the cooling canals.3.Stack Wash, (Fossil)Each stack is washed approximately every five years to remove combustion products which have adhered to the interior stack surfaces.The stack wash water is discharged to one of the two solid settling basins.Supernatant from these basins is discharged to the cooling canals.4.Dust Collector (Fl Ash)and Dust Collector Ho er Cleanin (Fossil)Particulate

.materials collected by the dust collectors falls into dust collector hoppers and is either reinjected into the boiler for reburning, or is sluiced to one of the solids settling basins.At present, the collectors and hoppers are not routinely washed.However, if clogging occurs, the appropriate section may be taken apart and the loose ash removed.The ash i: s caught within a curbed area and is sluiced to one of two solids settling basins.The supernatant from these basins is discharged to the cooling canals.5.Boiler Fireside Wash (Fossil)Boiler fireside water wash is typically performed a minimum of once a year per unit.The high pressure water wash is performed to clean combustion products deposited on boiler tubes during boiler operation.

This system is designed to pump the boiler fireside wash water to one of two solids settling basins.The supernatant from these basins is discharged to the cooling canals.6.Boiler Waterside Chemical Cleanin (Fossil)Boiler water tube internal surfaces are typically cleaned every three years.Cleaning is usually performed with a 5%HC1 (hydrochloric acid)solution with a copper complexer added.Acid washes of internal boiler surfaces are performed to remove inorganic scale and metal oxides from the boiler tube surfaces.The treated water is then discharged to one of two imperviously lined solids settling basins for precipitation of the metals.The supernatant from these basins is discharged to the cooling canals.7.E uioment Area Routine Cleanin (Fossil)Floor drains typically receive small amounts of ash and other particulate materials, detergents, and small amounts of lubricating and fuel oils from floor and equipment cleaning and stormwater run-of f.The drains are routed to the cooling canals after treatment via an oil separation device.8.Miscellaneous 1.Non-E ui ment Storm Water Runoff (Fossil and Nuclear)Storm Water (rainfall) within the plant operating area collects in floor drains and is routed directly to the cooling canals.2.Sanitar Sewer (Fossil and Nuclear)Sanitary'aste from showers, water closets, and other personnel-related water wastes are routed to a county-approved on-site septic tank system on the fossil side.On the nuclear side there is a sewage treatment plant which discharges to a well onsite.

Attachment 2 TURKEY POlNT PLANT SCALE FUEL.OIL STORAGE AREA 250 UNI UN z Q UNIT 3 00 t LEGENO Central Hazardous Waste Storage for Disposal Area Direction of Water Flow V k i.r%p' t Attachment 3 Turkey Point Plant-Haste fl(nf Oi~0CIS Hl HO t>>STSTCU VHITS S 4 all I tcaH ICNCKatOK/

I t C COWLICK SCSTCll!Tvwta s a~I I CLOWOOWN T'IOCLSK (VHTIS I~1 I(I I I CNCNICaL TOLVNSI CONfKOI.STSTCH BONITOS taNKS I (VHITS S~~)I l I scHCNcaauccas.CKSOH ALTCKH<<a SKKOSIT C<<astc NON COKKOSIYC<<astc I<<CKwasH CNCLOSCO I E*L I I 1 NCVTAaUTINO I I I HCHICaLS OAOVLATOIC/L

'aHO TILfttt I I HCVIKJUCatlOHI CNCMICAI CLCANINO I CCONOMIZCR NOICICCR WASH OV5T COLLCCTOIT CLEANINO<<I Vl MVNICIITAL WATCR 5VI I LYI AIR flRCN CATCTT WASH OOILCR FIRCSIDC WASH 5TACS(WASH 5OUO 5 CTTUHO sasHls C S ANO~Sl lO C H LI Ol C O O aa~I U LI I Cl<<I O VI NON COIRFMCNT AACA 0 RAINAOC OILY WAS TCS OIL, SCTTARATORS NON COIntMCNT*RCA 5TORMWATCR s lncludea Mater fros Equi(snenc Area Cleaning and Storssfater Run<<Off Attachment 4 DRINKING WELL INVENTORY WITHIN A ONE-QUARTER MILE RADIUS OP THE TURKEY POINT PLANT FPL is not aware of any drinking water wells located within one-quarter mile of the Turkey Point Plant.Drinking water for facilities located in this area, including the Turkey Point Plant is provided by Metro-Dade Water a Sewer Authority.

Attachment 5 TURKEY POINT 40 C F.R 117 12 (~)(2)DISCLOSURE IST NUMBER TYPICAL USE CHEMICAL L STORED ON SITE AVG.MAX.QUhNTITIES PURCHASED PHYSICAL STATE DISPOSAL METHOD Ammonium Hydroxide 28 Feedwater pH control 825 gal 1150 gal 55 gal drum liquid Boiler/Steam Generator Blowdown Disodium Phosphate 245 Boiler Water Treatment 625 lb.750 lb.50 lb.bag solid Boiler Blowdown Sodium Hydroxide 241 Anion Regenerant 5,000 gal.8,000 gal.3,000 gal.truckload liquid Neutralization Basin Sul furic Acid 251 Cation Regenerant 5,000 gal.8,000 ga.3,000 gal.truckload liquid Neutralization Basin Trisodium Phosphate 246 Boiler Water Treatment 625 lb.750 lb.50 lb.bag solid Boiler Blowdown Paint Thinners and Solvents ToToene 263 Xylene 277 Paint Thinners and Solvents 330 gal.440 gal.55 gal.drum liquid Approved Chem.Waste Disposer Potassium Bichromate Potassium Chromate 216 217 Corrosion Control Corrosion Control 50 lb.100 lb.10 lb.bag 50 lb.100 lb.10 lb.bag sol id sol id Approved Chem.Waste Disposer Approved Chem.Waste Dispoer CatecaCor r Coolin Water: i TABLE 1 TURKEY POINT PLANT UNITS 1&2 WATER DISCHARGE FLOWRATES Average Annual Flowrate (allons/r)-Main Condenser Cooling-Auxiliary Cooling Screen Wash 289,091 x 106 12,609 x 106 159 x 106 Sub-Total Cooling and Screen Wash Water Related Flows Blowdown: 301,859 x 106-Boiler Process/Maintenance:

-Boiler Chemical Cleaning-Air Preheater Stack Wash-Boiler Fireside Wash-Hopper&Drain Flush Dust Collector Wash Total To Solids Settling Basin Floor/E ui ment Area Draina e:-Equipment Area Drainage to Oily Water Separators (East&Dike Area)**-Non-Equipment Area Drainage Water Purification Plant Wastes: 210,000*4,257,000 53,000 1,104,000 3,627,000 3,522,000 2,733,000 12,563,000 2,891,000 11,773,000 Boiler Water Make-Up Pretreat: (Coagulator Blowdown)(Sandfilter Backwash).Make-up Treatment (Carbon Filter (Backwash)

Demineralizers (Cation/Anion/Mixed Bed)Sub-Total to Neutralization Basin 6,885,000 2,'943,000 631,000 9,145,,000 19,814,000

• Discharge to Neutralization Basin For Treatment**Discharged to Fuel Oil Tank Farm Diked Area

~a 1 TABLE 2 TURKEY POINT PLANT UNITS 3&4 WATER'DISCHARGE FLOWRATES cate caCoi r Coolin Water:-Main Condenser Cooling Water-Auxiliary Cooling Water Screen Wash Sub-Total Cooling and Screen Wash Water Related Flows Average Annual Flowrate (Gallons/Yr) 655,970 x 106 50,455 x 106 191 x 106 706,616 x 10 Blowdown: Steam Generator-Condensate Polisher 139,810,000 683,000 Process/Maintenance:

-Chemical Volume Control System Monitor Tanks 4,888,000 Floor/E ui ment Area Draina e:-Equipment Area Drainage to oily water Separator (West)-Non-Equipment Area Drainage 631,000 28,225,000 Water Purification Plant Wastes: Steam Generator Make-Up Pretreatment: (Coagulator Blowdown)(Sandfilter Backwash)-Make-up Treatment (Carbon filter Backwash)-Demineralizers (Cation/Anion/Mixed Bed)32,955,000 14,139,000 2,786,000 41,995,000 Sub-Total to Neutralization Basin 91,875,000 t T y~catecaoCrr Coolin Water:-Units 1&2 Units 3&4 TURKEY POINT PLANT WATER DISCHARGE FLOWRATE

SUMMARY

Av.Flowrates Gallons/Yr 301,859 x 106 706,616 x 106 Gallons/Da Total 1,008,475 x 106 2,763 x 106 Floor/E uioment Area Draina e (Units 1, 2, 3, 4):-Oily (To Oil/Water Separators)

Non-Oily Total 3,522,000 39i998,000 43,520,00 119,000 Chemical Waste Treatment Facilit (Units 1, 2, 3, 4): Solids Settling Basins (For Fossil Process/Maintenance Wastes)-Neutralization Basin (For Water Plant Wastes)12,563,000

],]lg689~000 Total 124,252,000 340,000 Blowdowns:

-Boiler (Units 1&2)-Steam Generator (Units 3&4)-Condensate Polishing (Units 3&4)Total 2,733,000 139,810,000 683,000 143,226i000 392,000 Chemical Volume Control S stem-Monitoring Tanks (Units 3&4): 4,888,000 13,000 f~.~~'