ML18009A681

Transmits Application for Renewal of Plant NPDES Permit

ML18009A681
Person / Time
Site:	Harris
Issue date:	09/28/1990
From:	Loflin L CAROLINA POWER & LIGHT CO.
To:	NRC OFFICE OF INFORMATION RESOURCES MANAGEMENT (IRM)
References
NLS-90-178, NUDOCS 9010110272
Download: ML18009A681 (74)

Text

ACCELERATED DISTRIBUTION DEMONSTRATION SYSTEM gl 1 tv REGULATORY INFORMATION DISTRIBUTION SYSTEM (RIDS)

ACCESSION NBR:9010110272 DOC.DATE: 90/09/28

. NOTARIZED: NO FACIL:50-400 Shearon Harris Nuclear Power Plant, Unit 1, Carolina AUTH.NAME AUTHOR AFFILIATION LOFLIN,L.I.

Carolina Power

& Light Co.

RECIP.NAME RECIPIENT AFFILIATION Document Control Branch (Document Control Desk)

DOCKET, 4 05000400

SUBJECT:

Transmits application for renewal of plant NPDES permit.

I DISTRIBUTION CODE:

COOID COPIES RECEIVED:LTR J ENCL 3 SIZE:

IP' TITLE: Licensing Submittal: Environmental Rept Amdt 6 Related Correspondence NOTES:Application for permit renewal filed.

05000400

/

RECIPIENT ID CODE/NAME PD2-1 LA BECKER,D COPIES LTTR ENCL 3

3 1

1 RECIPIENT ID CODE/NAME PD2-1 PD COPIES LTTR ENCL 1

1 A

D INTERNAL: ACRS NRR/DET/ESGB 8D OGC/HDS 1 RGN2 DRSS/RPB 6

6 AEOD/DSP/TPAB 1

1 OC/LFMB 1

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NOTE TO ALL"RIDS" RECIPIENTS:

PLEASE HELP US TO REDUCE WASTE! CONTACT THE DOCUMENT CONTROL DESK, ROOM Pl-37 (EXT. 20079) TO ELIMINATEYOUR NAME FROM DISTRIBUTION LISTS FOR DOCUMENTS YOU DON'T NEED!

TOTAL NUMBER OF COPIES REQUIRED:

LTTR 21 ENCL 19 D

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Carolina Power 8 Light Company SERIAL:

NLS-90-178 SEP 38 1990 United States Nuclear Regulatory Commission ATTENTION:

Document Control Desk Washington, DC 20555 SHEARON HARRIS NUCLEAR POWER PLANT DOCKET NO. 50-400/LICENSE NO. NPF-63 NPDES PERMIT RENEWAL Gentlemen:

Carolina Power

& Light Company (CP&L) hereby transmits a copy of the application for renewal of the Shearon Harris Nuclear Power Plant (SHNPP)

Nat:ional Pollutant Discharge Elimination System (NPDES) Permit.

A copy of the new permit will be transmitted to the NRC within 30 days of the renewal being approved in accordance with Section 3.2 of Appendix B of the License.

If you have any questions regarding this submittal, please contact me at (919) 546-6242.

Yours very truly, L. I. Lofli Manager Nuclear Licensing Section SDC/ecc (801HNP)

Enclosure cc:

Mr. R. A. Becker Mr. S.

D. Ebneter Mr. J.

E. Tedrow 411 Fayettevilte Street o P. O. Box 1551 o Raleigh. N. C. 27602 9020i 20272 %00928 PDR ADOCK 05000400 PDC C'oo l Il)

0 1

COAL Carolina Power & Light Company SEP 27 l990 SERIAL NO.:

ESS-90-975 Dr. George T. Everett, Director N.C. Division of Environmental Management P.O.

Box 27687

Raleigh, NC 27611-7687 RE:

Shearon Harris Nuclear Power Plan5 NPDES Permit No.

NC0039586 Request for Renewal Dear Dr. Everettt The current NPDES permit for Carolina Power

& Light Company's (CP&L)

Shearon Harris Nuclear Power Plant (SHNPP) near New Hill in Wake County expires on March 31, 1991.

CP&L respectfully requests that the N.C. Division of Environmental Management (DEM) renew the SHNPP NPDES permit in accordance with 15NCAC 2H.0100.

Enclosed are a check for the

$200 application fee and the Application for Permit to Discharge Wastewater (Standard Form C).

As

required, the application is being submitted in triplicate.

Should you have any questions or require further information, please contact Mr. M.

R. Greeson at 5ll6-7902.

Yours very truly, G. J. Oliver, Ph.D.

Manager Environmental Services BWS: des (90>>157BWS )

Enclosures bcc: Mr. C.

S. Hinnant Mr. D.

E. Hollar Mr. L. I. Loflin Mr. J.

M. McDowell Mr. J.

R. Sipp 411 Payettevilte Street

~ P. O. Box 1551

~ Rateign. N. C. 27502

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I N. C.

DEPT.

OF NATURAL RESOURCES AND COMMUHZTY D~,

ENVIRONMENTAL MANAGEMENT COMMISSION NATIONALPOLLUTANTDISCHARGE ELIMINATIONSYSTEM APPLICATION FOR PERMIT TO DISCHARGE WASTEWATER FOR AOKNCVUSK STANDARD FORM C MANUFACTURINGAND COMMKRQQLt SECTION I. APPLICANTAND FACILITYDESCRIPTION Unless otherwise specified on tnis form all Items are to be comDNted. Ifen Item d nol ap pl feeble Indicate 'NA ~

AOOITIONAt INSTRUCTIONS FOR SELKCTKO ITEMS APPEAR IASKI'ARATKINSTIIUCTIONbOCFCLKT AS IN~1'EO, REfjsllTO 8OOKLET 8KFORK FILLING OUT THESE ITEMS.

Pleepp Rrfnt or Type Leeal frame of Applicant Isee Instructions) 1 ~ 1 wer & Li ht Com an Malllne Address of Appllcarit Isee lrrstwctlorrs)

Number S Street City State Zip Code Applkant's Authorised Aeent (see Instructions)

Name and Title Number 4 Street Address City lbpe teeb North Carolina t82e lepd G. J. Oliver, Ph.D.

Hana er - 'Environmental Services P.O.

Box 1551 Ral'ei h State 2lp Code Telephone previous AD p liest i en If ~ prevlOua apolication for ~

Nauona< or Federal dlscnaree per-mit hat been made, elva tne date of application.

Use numeric deslpnallon for date.

18Se IOSf Area Code Number 86 12 29 VR MO OAV N rt Carolina I certify that I am familiar with the Information contained In this aDpllcatlon end that to the best of my knowtedpe end belief ouch Information Is 'true complete and accurate See Attachment 7

for Signature Authorization G. J. Oliver, Ph.D printed Name of Person SIenlnp Sipnature of Applicant or Authorized Apens

~

Hanager

- Environmental Services TNe VO

~~

VR Mo OAV

Ãorth Carolina General Statute 143-215.6(b)(2) rovidcs that:

hny person <<ho knoviagy aakes eny false statemeat representat oa, or ccrc cat on M any application, record, report, plan, or other document files or required to bc maiataincd under article 21 or regulations of the Environmental Management Comnission impleaeatiag that'reicle f or %81o falsifiese tempers Srith, or kaottly readers inaccurate any recording or monitoring device or method required to be opcratcd cr maintained under Article 21 or regulations of the Eaviroamental Management Commissic imolementing that Article, shell be guilty of a misdemeanor ~ahable by a fine not to czcced

$10,000, or by imprisonmert not to exceed six monthsa or by both.

(18 U.S.C. Sectioa 1001 prtrtri a punishment by e fine of not more than

$10s000 or imprisonment not rlorc than 5 years, br bothj for a similar cffense.)

5 Faedhy/Actlvlfy (soo lgjgglcflohsl Olve the name, owns~end phydcal loc4tloh of trl

. ht of OthV OOOratlne facllltywhere all.

chafeoIII dov ot willoccuf, Hams I054 e r Power Plant I

Foh AOCHCy tf 0 l

'1'

~

1 Ownership IpublH, private or bOth PuNIC 4nd Ptlvatel

~00b Q I UB 5g/hV QBPP Check @loch lf Federal Faclllty and elve OSA Inventory Control Humps r l050 QFaO NA LOC4tloh 5tteet 0 Humber City 1054 lbef 1050 State Road 1134 New Hill Wake Stat>>

de Hahlfe Ot blttlheSS State tne nature of 'lhe business conduc'lsd at the plant or opefatlhe fscnlly.

'teSII Electric Power Generation f000 ACErtcv UsE Te I adll'ly Intone Wafat ISO>> Ihltnfc tlonst Indicate water Intone volume per day by sources.

Bst Imate

~verses volume per dsy In thousand

~aliens por day.

Munldpal or private water system Surface water Oroundwatsr Other 1074

~ 0ye teyd NA NA NA thousand 0allons per day thousand 0sllons per day PIOI>>ahd psllens paf day theutand Salient Pof d4y TOtal Item 7 soya 28,657 thousand eellons por day Ifthere ls Intake water ftem

~Other,e SPOClfy tne Seurse.

lbyf NA

~.

Faotdty Water LHe Kstlmate

~verses volume pet day In thousand 0allons pot day for tho followlne types of water usaeo at tho taclllty.

(seo hlsttuctlons)

Honcontact coollne waist boiler food water

~rococo water {Indudlne contact co>>line water)

Sanitary water Other Total Item ~

~Ifther>>ere ~Ischafpaa to Otheraa SP>>dfy.

Ifthere H Sahlt ~Iy walef User elva

'tho number of peopl~ served f004 1004 5000 f

'I'e

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eraumne aaaeec aer eer 28 405

~4 thputend 0sllons per day IIINweaaeael>> aer eelr e re%ca aeaeec sw eea ca~~ area

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FOh AGENCY USE S'DARD FORM C MANUFACTURING ND COMMERCIAL SECTIONK BASIC DISCHARGE DESCRIPTION complete triis section foi each odchai9t indicattdrn Section I, lltni 9, that is lo surface waters.

This iilcludts disctlartts Io niunicioal sewer ~ 9C systtrns in wnicn thc wastewaltr aots not to throutn ~ Irealmenl works prior lo otin9 oischartea lo surface wattrL oischartts lo wells must bc otscribeo wnero tntre are also discharocs ln surface waters trnni this facility. SEFARATE OEScRI ~TIDNs DF EAcH otscHARGK ARE REQUIRED EvEN IF sEvERAI. OlscHARGES ORIGINATE IN THE SAME FACILITY. Allvaiuts Ior an ~irrstint oischarte stipula bt rturt sentalive of tne twelve previous months of operation.

It this Is ~ proposed dischartt, values should rtflect bast entinetrin9 esllmattL AOOITIONAL INSTRUCTIONS fOR SEI ECTEO ITKMS AOPEAR IN SEPARATK INSTRUCTION BOOKLKTAS INDICATKD. RKFKR TO BOOKLET BEFORE Fll LING OUT THESE ITEMS.

1.

Oischartt Serial No. and Name a

Dischartt Serial No.

)see instructions) 20Ia

b. Dischartt Name Givt name of dilcharte, if any,

)see instructions>

tBIO Common Outfall Line to Harris Lake c.

previous Oischart ~ Serial No.

If previouS Permit appiiCatiOn was made for this oiscnaitt face Item 4.Section I), prOvide previ oul discnarte seri ~ I number 20Ic

001, 002, 003s 004s 005 Oilchartt Ootratiiit Da'Its a.

Dischartt Betan Date Il inc dischai9t otsciibco btiow is in ootration, tive tne date Iwitnin best estimate) Inc ancnartt Cia 9aii, 202a 85 11 YR Mo b.

Oischarte to Bttin Date ir Inc oisshar9t has riever nccuired but is oiannea for some future aalt.

tive lht date Iwilhinbell csli niatt) the oischartt willbocin tata YR MO c

Dischaitt to Eno Oalt tt dis cnari)o is scheduled In bo oiscnn tinued within Iho ntkt b Voais, tive Ine date fwilhinbvst cs:i i>>alt) tnc discnarto wiri i no tote NA VII MO Entinttrint Report Avaiisoir ChOCk if an tn9inttrin9 rtooit is avaiiaoie lo revitwinc acency unon ftoutsl. Istt instruclioris) 202 4.

Dischartt Location Name the Ooldical OounOaiieS witnin which Ihe ooint ot discharte is localto Stale Cnunly Iit aOniil abic) City Or tOwn 5.

Discharte point Otscriotion Discharpe n into (check one):

Isee instructions)

Stream IinCiudes dilChel, ~ rrayOS.

and other intermittent walorcoursts)

Lakt Octan Mumcioat Samlary waste>>attr Transport System Municipal Combinto Sanil ~iy and Slorm Transport System 2044 204O 204c tote North Carolina Wake NA OSTR QLKE OOCE OMTS OMCS 2BBB KBdf Atency Ult Thlt taction oonfalna 9 pagea.

DISCHARGE SERIAL NVMBER Municipal Storm water Transport System Well fin)ection)

Other It 'other's checked, specify ttyb QSTS QWCL QOTH fOR AISENgy VSE f

I" y.

Dlscharye point-Lat/Lony Give the precise IOCation of tnt point of dlschlf9t to tht ntlfeit second.

Latitude Lonyitudt 2yya toyb MOEG MIN SEC 34 47

~OEG

~MIN Q7 SEC y.'lschafye Realvlny Water Nlmt Namt the waterway ~I tht point of dlscharye.f set Instructions)

Harris Lake If the dischlfyt ls throuyh an oui follthlt attends btyond Iht shoi ~.

line or is below tne mean iow water fine. complete Iltm y.

toyb Foi A nc Vst Maror Minor Sub toyt I For A ncy Vse i

303e DffihtrtOischafst

a. Dischlrtt Distinct from short 20ya 500 Ital b.

Olscharyt Depth belOw Water SUfflCt 20th 40 y.

Discharye Typt and occurrence a

Tyot Of OISCharyt ChtCk wnetner the discnaiye is con.

tlnuous or intermittent.

istt Inslruclions) 20ya

+Icon) Continuous O lint) Inltrnullcnt b.

Dischafyt Occurrence Days per Week Enter lht averlyt num btr of day'I pet wetk ldiifiny periods of discnaryt) this dis.

Chlfyt OCCurS.

20yb dlys ptr wttk 7

c.

Oischlryt Occurrence Montns

~

It this dischlryt normlfiy operlies I~ilhtr intermitttntiy, or continuously) on fess thin

~ yell around basis Iexcludiny shutdowns for routine mainle.

nance), check the months dur Iny tht year whtn tritdiscnlryt H operatiny.

fice Inslruclions) tote NA QJAN Qf EB OMAR QAp

\\

OMAV O JUN Q JVL OA G

OSEo OOCT QNOv ODEC

omplete tlems 10 and llIf "Infer.

alttent" ls checked In Item 9A.

)therwlse, proceed to Item 32.

0. Intermittent Olscharye Quantity State the averayt volume per dis.

chlrye occUfrtrict In Ihousands ol ye IIoils tlb NA thousand ylilofiipef dlschafye occUrrence.

11. Inttrmlffent Olscharye Duration and Frtyutncy a.

Intermittent OHchafye Duration

~ef Oly Stale the aveflyt number of hours per dly tne dHCharye IS Operatlny.

211 ~

Kh hOuri per day b

Ihtefiiillltn'IDischafye FreduenCy State the arerayt numbtr of discharye occur.

fences ptf dly durlny days when dhchlryiny.

t11 ~

NA dlSCharyt occUfftnCti Pef day 12.

Maalmum Flow parlors Give tne time period In which tht maximum flow of this dlschlfyt occUrL From lo JAN DEC

, month month ll.0

OISCHARQE SERIAI NUMbER POR AISENCV uSEl

13. ActivllyOescttolion Give a nartahve desctiotlon of activity producrne this dischafoe )see Instructions)

(

S e Attachment 1 for narrative description of 212 each dischar e contributing to the common outfall.

Ie. *<<IINlyCauslna ollcharee r ot eaCh SIC COde whiCh deacrioel the achvily causlne lhis dischatoe, supply lne type and maalmum

~mount ol elthet the raw matcher consumed litem )aa) or the oroduct produced )item ) eo) In the units Ioecitied in Topic I of the Insttuc.

liOn BOOu rat.

S Or SIC Cpdet nOt hslcd in 1 aole I. use raw materi ~ t ot otoduclion units normally used for measutine production.tree irisftuctions)

~.

Raw Materials NA SIC Code 2140 I

Name Maximum Uml Amount/oay

)see Taole I)

Shared Olsctla toes

{Sell~ I Numoer) products SIC Code 2)do

)

4911 Nalrie Electric Power Services Mealmum Unit Amount/Oay

)See Yaose I) 0.9 Shared Osscharoes

)serial Number)

niSCsfnstrr SE.I<<nl NuMIII.a 001 FOR AGENCY USE, IS.

Waste Abatement a,

wasle Abaltmtnt Flactlces oescribe lnc wast t abet ~ment oracticts usto on lnd discnarte wills a brier narlatwt. (Iet In<<ructlons) 2IS ~

abatement practices b, Waste Abatemtnt codes tfstn9 tht codes listed In Table Il of the fnstruction sooi itt, descnbt tnt walla abalemenl Droctssts for this discher9t in tht order in which the Y occur If OONiblt.

2 tab (I) ~UQDZ BACTIV

()) ~KLLG1

() 2)

POTHER (16) f)9)

(22)

(2$ )

CCLDIS I PSEDDI t

()a) POTHERI

()7)

(20)

(2$ )

l

~

(2) ZSZZJZl

6) CPHADJ (9 I QgCQAgg

~

(12) PSEPAR (1$ )

()d)

(21)

(2 ~ )

15b Items 1-2 Items 3-6 Cooling Tower Blow(town nt atment Pla ning Waste aste Sewage are Items 7-9I Eietal Clea Items 10-)2ILow-Volume Items 13-14(Radwaste

tslgCHAAOKSKAIAI rcUsanKtt 10% AOKSSCY USK I

1 ~. wastewater chsrecterhllca See Item 26 check the box besrde <<ach cohsntuent which ls present In the affluent'tducharea water). This deterrnlhallon ls to be based on actual analysis or best estlrnate.tree Inffruetlons)

Color 00080 Ammonia 00610 Organic nitrogen 00605 Nllrale 00620 Nialtc 00615 Phosphorus 00665 Sulfate 00945 Sulfxlc 00745 Sulfite 00740 Bromale 71870 Chloride 00940 Cyanide 00720 Fluoride 0095 I Alununum 01105 Antimon>

01097 Arsemc 01002 BeryUium 01012 Parameter r216 X

X X

Cotlper Iron 0104S Lead 01051 Magnesium 00927 Manganese Mercury 71900 Molybdenum 01062 Nickel 01067 Sclcnium 01147 Silver 01077 Potaaium 0093'I Sodium 00929 Thallium 01059 Titanium 01152 Tln 01102 Zinc 01092 Algiades'4051 Parameter

~0 Se X

X X

X Balrum OIOV7 Boron 01022 Cadmium 01027 Calcium 00916 Cobalt 01037 Chromium 01034 Fecal coliform bacteria 74055 X

Chlormated orgardc compounds'4052 Festiades'4053 Oiland grease 00550 Phcnols.

32730 Surfaaants 38260 Chlorine 50060 Radioacthrity'4OSO X

'Specify substances, compounds and/or e)crnents in item 26.

Pesticides llnactiadcs, fungicidcs, and rodcntiddcs) must bc reported ln terms ofthe acceptable common names speafied in Acceptable Common Hemcscnrf ChcmicalHcmcs forrkclngrerfirnrSrcrcmcnr on Pc!rfridcLabels, 2nd Edhion, Errrironmcntal Protection Agency,%as)dngton. DC. 20250, Junc 1912, as required by Subsection 162.7fb) of thc Regulations for the Enforcement of thc Federal fnscctiddc, Fungicide, and Rodenticide Act.

DISCHAROE SERIAI rIUMEER 001 I Dh ACSEIICY USE'y+

Desertea en et Intelle end Dhens tee f

he r

rs listed OV or ecch or I Oe smete ow, enter In the eOOroorlete eon the value or code letter answer cVIed fergtee Instructl~st In eddltlon, enter the parameter nsme end code end ell redulred rSWes ror any or the rollowlne oeremeters If they were checued In Item ter

~mmonls, cyanide. ~Iumlnum, arsenic, Oerylllum, cadmium, chromium coOOW lead, mercury, niner, selenium, Slnc, OhenVI, ou sne Creese.

~nd chlorine Iresutusl)

~

tntluent Emucnt parameter and Code QRyj!

8~e irk (2)

C (3)

(4) 4 gk x8u (5) 0 j

C (6) 0 QQ 2 C Il CLc EVl (7I Illa'OWe Gclbas per day MGD 00056 50050 pH Ualts 00400 30 NA NA

10. 38 7.93 I

NA I 1

G Terapcrature (wbtter)

'F 74028 39 NA NA Temperature (ammcr)

~ F 74027 82 NA 84 1

G Ihchetakal Oayyen Demand (GOD &day) mg/I 00310 NA NA C10 C24 (bemkal Oaygea Demand (COD) mg/l 00340 NA NA 5Q C24 Total guspselded (noe5ltcsabk) 505ds mg/1 00530 42 NA 120 C24 SpecNc Coaductance sakrornllos/cm at 25' 00(65 60-80 Scttleabk )getter (res&!ue) ml/1 00545 NA NA NA 1

NA

~Otbcr discharges sharbtg htaltc Aow (scrhl aumbcrsgme (astructkca)

+24-ur co o

1 t thi

'c. fic cation c

bined ou a

ho mp sate samp ing a s

spe i lo

(

om tf ll line) was done for purposes of this application and the Annual Pollutant Analysis require-ment.

Normally, only toxicity monitoring is conducted at this location.

These values may not represent maximum values expected but are believed to be representative of typical at the combined outfall line, effluent characteristics.

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DI5CHAROE 5ERIALNUMSEA I

FOII AOENCv~USS d, Chemksl conlposltlon of th<<e addltlves (see Instructions).

See Attachment 1

ICha rye yeneratio 0th ~ r ye flow tructlon Is I)

Complete Itenls 50.55 If there ls ~ therrrNI dl (ao., assocktad with ~ steam and/or power plant, steel mill, petroleum refln<<y, or eny manufacturlny process) ehd the total dlschar 10 mullon yallons per day or more.

(Iea Ins

50. Thermal Odcharye 5eurce Checx the appropriate Item(s) Indlcatlny the source of the dlscrlarye, (see Instructions) boiler biowdown

~oiler Chemkal Cleanlny Ash Pond Overllow boiler Water Treatment Evapora.

tor Slowdown Oll or Coal Fired PlantS Effluent from Alr Pollution Control Oevkes Condense Coollny Water Corulny Tower Slowdown Manufacturlny Process Oth<<

Qv

" (r 0

,.l P BLSD PSCCL PAPOF PEPSD POCFP pcorrD Q CTbD P MFPA P OTHA 5t. Dkehalye/Raalvlny water Tamper.

~tete Difference OWe the max lmum tern peralure difference between the dlscharye and recelvlny wat<> Temperature (5ublect to natural chahyes)

Dkcharye Wat<<Temperature Se. Wat>> intone Ye(catty (ae Instructions)

55. Retention Thne Olve the Ienyth Of time, In minutes, from start of water temperature rise to dlscharye of coollny water. (See Instructlona) oF OF

~~feet/sec.

~rA i~i.a oF oF oF

Oi5CHAROE SERIAL NUMBER 001 CrOR AOENCY UBE

24. A44uroner Inlormo iron 224 Rom 16 lnlormoson ~ O' Chemical constituents contained in this discharge will in part be re rese t t ve of the naturall occurin chemical uality of the chemical constituents of such quality and quantity associated with similar discharges for nuclear generating facilities of this size,

type, and in this geographical location that may be conveyed to Harris Lake.

Either all or part of the elements enumerated in the Periodic Table, either sin ularl or in an combination, may from time to time be char e.

either 1) resent in the common outfall ollutants monitorin for this ermit a lication, 2) known to be present in the specific wake..s R dioactive corn onents of releases are regulated by the Nuclear 17 17 plication,...gadj.g~yj.Q'.

measured at the combined outfall line

.Sgnv~~~a~priori~t Pollutants data inAttach.

planned for use is the biodi~sersant "ACTI-BROM II u e ll 1990 b

the N. C.

Division of Environmental Management.

The Influent data requested is variable in nature and not normally under the control of the applicant.

Effluent data is available in the Dischar e Monitoring Reports previously submit'.ted to DEM.

e ts are incor orated b

reference in this submittal.

this a

lication is from Convention/

Priority Pollutants monitoring conducted at the common outfall.

EPA - approved procedures are used for all NPDES"required analyses.

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~ Oi ll NPDES APPLICATION FOR PERMIT TO DISCHARGE'WASTEWATER List of Attachments Attachment 1 - Narrative Attachment 2 - Permits,

Licenses, and Applications Attachment 3 - Maps Attachment 4 - Water Use Diagram and Approximate Flows Attachment 5 - Conventional and Priority Pollutants Data Attachment 6 Possible Chemical Waste Attachment 7 Signature Authorization (9O-82BWS)

l

ATTACHMENT 1

DESCRIPTION OF WASTE STREAMS CPA SHEARON HARRIS NUCLEAR POWER PLANT Introduction The Shearon Harris Nuclear power Plant (SHNPP) consists of a

900 MW generating unit.

The facilities include a

Westinghouse pressurized water

reactor, three recirculating steam generators, a turbine generator, a one-pass condenser, an open recirculating (cooling Cower) cooling water system, and a

lake to makeup water loss by evaporation.

In a pressurized water reactor

design, steam is produced in bhe secondary system steam generators using hob water from the reactor core.

The primary system does not come into contact, with any other part of bhe generab1ng

system, such as the steam cycle which includes the turbine and bhe condenser.

Combined Outfall to Harris Lake The SHNPP operates on an open recirculating cooling system using a

natural draft cooling bower and 4100 acre makeup water storage reservoir.

All five ma)or wastewater discharges ab the SHNPP are combined in a

36-inch diameter common pipe which discharges bo the Harris Lake 500 feet offshore at 40 feet below the surface (Discharge 001 in this applicab1on.)

The individual waste streams contributing bo bhe common outfall pipe are:

cooling tower blowdown, sanitary waste treatment facil1ty effluent, metal cleaning

waste, low-volume waste, and radwaste.

(These waste streams are enumerated in bhe present permit as serial numbers

001, 002,

003, 004, and 005, respectively.)

Monthly toxicity testing has been conducted on the combined outfall line s1nce February 1990.

Each of the waste

streams, as well as m1scellaneous discharge points, will be described in this narrative.

Also included is a list of chemicals which are expected to be in waste streams from the SHNPP (Attachment 6).

Cooling Tower Blowdown to Harris Lake The cooling tower provides the condenser with a supply of water for removing bhe heat re)ected by the condensation of steam.

(The recirculating water temperature rise across bhe condenser is 25 F. )

This heat is dissipated primarily by evaporation as bhe water falls through the tower.

, This evaporation is essentially pure water vapor, with bhe dissolved and suspended solids remaining bo concentrate.

To prevent the solids from causing scale and corrosion problems, some of bhe concentrated cooling water 1s discharged from bhe cooling tower basin, i.e.,

blowdown.

During plant operation, the cooling tower basin continuously d1scharges for optimum performance.

Blowdown currently averages approximately 10 MGD.

Makeup water for cooling tower evaporative losses and cooling tower blowdown 1s provided from the main reservoir.

The cooling tower also serves as a partial source of ser vice water, which is used for non-contact cooling of auxiliary equipment throughout the plant.

The cooling tower is infrequently drained for maintenance.

The normal operating procedure includes draining bhe residual water to the lake and disposing of any sed1menbs in bhe SHNPP landfill (Permit No. 92-A).

(90-76BWS)

I l b l

Occasionally, the condenser is drained for maintenance and repairs.

When bhe condenser is

drained, ib is necessary to route bhe residual water (approximately 60,000 gallons per event) to area storm drains.

This water is monitored for appropriate parameters required for cooling bower blowdown in accordance with bhe NPDES permit.

Presently, condenser draining events are reported bo DEM, including monitoring data.

Several chemicals are used (or planned for use) in bhe treatment of the circulating water.

Information concern1ng these chemicals and approximate dosages are provided below.

(The chem1cal supplier is subject to change ab any time.)

Chemical Descri tion A

roximabe Dosa e

Nalco Sure-Cool 1321 An aqueous solution of zinc, phosphoric 100 lbs/million gallons and sulfuric acid (Approximately 7.2'$

as Zn and 43.6$ as P04)

Nalco Dyna-Cool 1328 Aqueous solution of an acrylic polymer and a sulfonated car boxylated polymer 85 lbs/million gallons Nalco 86UJ183 Aqueous solution of approximately 40$

sodium tolylbriazole 40 1bs/million gallons Nalco ACTI-BROM 1338 Aqueous solution of sodium bromide and a biodispersant amount var1es depend1ng on biological activity and temperature of makeup water)

Sodium Hypochlorite 15$ Solution (amount varies depending on biological activ1ty and temperature of makeup water)

Sewage Treatment Facility A

0.05 MGD extended aeration sewage treatment facility st ves the plant.

The plant consists of dual-path equalizabion

tanks, aer at1on

banks, sludge holding tanks, clarifiers, and chlorine contact tanks.

Disinfected effluent is pumped bo the common outfall line.

Sludge is disposed of off site by a contract disposal firm.

The contractor adds lime to bhe sludge for sbabilizabion.

In addition to sandbar y waste, HVAC condensate and organic developers from the microfilm pr ocessing laboratory (approximately 52 gallons/year) are discharged to the sewage treatment facility.

(Hazardous and ammonia-conbaining components of developing waste are disposed of as hazardous waste and low-volume waste, respectively.)

(90-76BWS)

>, ~

I l

Chemicals used (and approximate quantities) in bhe sewage tr eabment facility are described below.

The chemical supplier 1s subject to change at any time.

Chemical composition of bhe Betz products is proprietar y informabion.

Chemical A

roximate Quantity Sodium Hypochloribe 15$

Betz Foam Trol 144 Sodium hydroxide 50$

Bebz Polymer 1192 Liquid Alum 50$

2000 gallons/year 75-')00 gallons/year 2500 gallons/year 130 gallons/year 50 gallons/year Metal Cleaning Waste Infrequently, cleaning of heat exchanger equipment by chemical solutions may be necessary.

Cleaning solutions would be routed bo the waste neutralization basin for pH adgusbmenb (or other chemical neutralization) prior to discharge to the settling basin where further treatment by sedimentation occurs.

To

date, bhe only metal cleaning which has been conducted was a preoperabional flush. If a new system is added in the future, flush1ng could be necessary again.

Also, metal cleaning may be needed in bhe future for the steam generators or auxiliary boilers.

Chemical solutions used may include phosphates, organic cleaners, citric acid, or oxalic acid.

Radwaste Treatment System The radwaste system is designed to collect, store,

process, and release any radioactive or potentially rad1oacbive liquids assoc1abed with operation of bhe nuclear power plant.

The waste streams are collected in tanks and sampled for conventional pollutants and radioacbiviby.

The specific batch treatment is selected based on these analytical results.

This allows for selection of the proper treatment processes for each individual batch.

Most radwaste streams are treated by the Modular Fluidized Transfer Demineralization System (MFTDS) that uses filtration and ion exchange in a manner that minimizes the production of solid wastes.

Boric acid is recycled.

The secondary waste system (SWS) is for treating radioactively-contaminated water from the secondary steam cycle system;

however, since that system is not normally contaminated, bhe SWS is usually shut down and those flows are routed bo bhe normal low-volume waste treatment system after radiological monitoring.

After treatment, bhe radwaste flows are stored in one of four banks:

bhe secondary waste sample

tank, the treated laundry and hot shower

tank, bhe waste monitor tank, or bhe waste evaporator condensate tank.

After monitoring bo verify adequate treatment, bhe tanks are discharged to the common outfall line.

The recently installed cooling tower bypass line provides a flow of lake water for radwaste releases, as regulated by the NRC.

Radwaste dilution may also be provided from cooling tower blowdown.

(90-76BWS)

J

Low-Volume Waste Xn the operation of the

SHNPP, there are many processes which result in intermittent low volumes of various waste streams.

Low-volume waste is treated by neutralization (for pH ad)ustment),

sedimentation, and separation.

These wastes may be treated 1n the oily waste separator and/or neutralization basin as needed prior to routing to the sedimentation

basin, which ultimately dischar ges to the common outfall line.

Chemicals present in these systems may include corrosion products (such as copper and iron) corrosion 1nhibitors (such as chromates or molybdates,

ammonia, and hydrazine),

acids and bases from water treatment processes, and wastewater from ion exchange processes.

Low-volume waste flow from the settling basin averages approximately 0.2 MGD.

Sediment which collects in the sedimentation basin is disposed of periodically in the SHNPP sanitary landfill.

The various low-volume waste sources are described below:

a)

Water treatment system wastes from processing of demineralized water and potable water (The water treatment system includes coagulat1on, filtration, disinfection, and ion exchange.

Wastes from treatment include filter backwash and deminerali,zer regeneration wastes.)

b)

Non-radioactive oily

waste, floor

drains, and chemical tank containment drains (Turbine building wastes which could contain oil are routed to the oily waste separator for treatment prior to routing to the neutralization basin.

Waste oil is collected by a contractor for reclamation.)

c)

Steam generator and aux111ary boiler draining following wet layup d)

Non-radioactive secondary waste from condensate polishers e)

Miscellaneous drains/leaks from condenser, steam generator, and secondary components f)

Ammonia-containing wastes from microfilm processing laboratories g)

Auxiliary boiler system blowdown h)

Miscellaneous waste streams not otherwise identified elsewhere in this applicat1on (90-76BWS)

)

,1

Other Dischar es 1.

Storm Drains Runoff from parking lots, outside storage

areas, roof drains, and other areas on the plant site are collected in storm drains and ultimately routed to six release points wh1ch discharge to Harris Lake.

Flow contributed from those areas 1s estimated at 8.8 million gallons per

month, based on average rainfall of 43" per year and a runoff assumption factor of 0.7.

Further description of the storm drain system will be provided to DEM in the storm drain application to be submitted in accordance w1th the EPA final stormwater regulations.

In addition to stormwater, there are a few miscellaneous sources of water which are also intermittently routed to the storm drains.

These sources that have a

minor contribution to overall storm drain flows are as follows:

a)

Upflow filter clear well drains The upflow filter clearwell stores filtered lake water which is used in the potable water treatment system.

Periodically, some of the water from this tank is drained to the storm drains.

This water may contain low concentrations of chlorine because sodium hypochlorite is added to control biological growth in the tank prior to treatment through the upflow filter.

b)

Heat exchanger on the demineralizer feedwater During the cold months, it is necessary to heat the source water to the demineralized water treatment system to achieve.

opt1mum degassification.

To accomplish

this, steam is used to heat the demineralizer feedwater.

The condensed steam is discharged to the storm drains at approximately 5-10 gallons per minute.

This steam could contain trace amounts of hydrazine and ammonia used for chemistry control in the auxiliary boiler steam system.

Due to the low flow rate and the long retention

t1me, the temperature of the condensed steam should be at ambient temperature upon reaching the lake.

c)

Condenser water box drains Prior to condenser maintenance or repairs it is sometimes (approximately twice/year) necessary to drain circulating water to the storm drains (approximately 60,000 gallons per event).

This water is monitored for selected cooling tower blowdown parameters.

d)

Filtered water storage tank Water from the upflow filter clearwell is treated with carbon filters for turbid1ty control and then stored in a tank prior to subsequent filtration and disinfection.

Occasionally, some water from this tank may be drained to the storm drains.

This water may (90-76BWS)

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contain trace amounts of chlorine.

)

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Approximately 5000 gallons of lake water used for annual testing of bhe fire protection system is routed bo the storm drains.

In bhe event of a fire, additional water could be discharged bo storm bhe drains.

lj Emergenc Service Water S stem This system primarily provides non-contact cooling water for nuclear safety-related equipmenb systems and during emergency conditions.

The emergency service water system discharges to the auxiliary reservoir which is used as bhe plant's heat sink during emergency conditions, a

feature required by Nuclear Regulatory Commission regulab1ons bo provide a reliable supply of cooling water.

Under normal operab1ng conditions, bhe auxiliary and the main reservoirs are isolated from each other;

however, bhe reservoirs may be connected as necessary.

In addition bo emergency situations, this system is used periodically for testing purposes or for containment cooling as needed.

This water may contain braces of chemicals identified for the cooling bower blowdown.

(90-76BWS ),

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SXZHHI, HBII). 10 PHHIXS~ IZ(ZRKS, M) JBPfZGKIBG DXK DLvLsicn of Heelth ServLces DivLsicn of Health Services DivLsicn of Ehv. ~.

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Eke County P1anning fhke County P1anning Nuclear Regu1atcry Gcamhsicn acne SpecifLed (90-8186)

AuxLliaryResavcdr Well Ccnstru ticn Well Ccnstzucticn Well Ccnstructicn Well Ccnstneticn 401 Grtllficaticn 401 Certificaticn land Use land Re Facility Operating License 633 633 1145 K}C-1198 MZ-214 NC0039586 13383

%F63 2/11/74 2/11/74 7/11/73 7/11/73 11/2/72 3/7/83 12/29/86 4/11/74 12/22/81 11/5/80 9/5/79 7/14/77 7/16/73 4/17/73 11/13/72 9/4/77 2/1/90 4/11/74 3/20/78 10/24/86 (1'cs'perating license) 1/12/87 (high pcwer opaating license) 3/31/90 10/24/2026

1. MANIOA'M MAINOAMSYILLWAY S. AUXILIARYDAM

~. AUXILIARYOAMStlLLWAY

t. AUXILIARYhttthVOlh SEPARATING DIKE AUXILIARYRE TER VOVICHANNEL

l. EMERGfNCYSERVICE WATER INTAKtCHANNEL k fMERGENCY SERVICE WATER DISCHARGE CHANNEL

h. COOLING TOWER MAXEMWATER INTAKECHAHHEL IO. YIANTISLAND.

EMERGENCY SERVICE WATER ANDCOOLING TOWER MAKEMINTAKESTRUCTUht EMERGENCY SERVICE WATER SCREENUIG S'IRUCIURE tMERGENCY St'RVICE WATER DISCHARGE ST ROCIURE TURSXIE EUiLDING ADMNIISTRATIONANO SERV ICE SUILDING COOLING TOWER DIESELtUfLOILSTORAGE TANKSUILOING DIE St LGEN ERATDh BUILDING fUELHANDUNGtlXLOING RfACTOR AUXIUARY SUILOUK1 CONTNMKNTSIXLOING WASTE EROCE STING EIXLOIN0 TANKXUILENNO li. SUCKHORNDAMIEXISTINGI IT. EL~EITEUNE IS EXCLIRHNIEOUNDARY lt. UQUID RELEASt EOINT l1DOKT EROM EXCLUSION

~OIXIDARYVIA CLONOODH PIPELINE LETTERa TttrrTtg ta CAID C

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SIHLEK HAIIKSNHIZIR H%KR PORC ARSGXBCK MSGR USE MER VMLQS SZCHBi GSGIXIWS HEM-0 MAX. HREP KlÃ6 'le. SHUZIXMP 1

2 3

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10 11 12 13 14 15 16 17 18 19 21 23 24 c5 26 27 28 29 30 31 32 33 34 35 36 37 38 I

21,000 gpn 510 M8 864 KN 648 Nm 0-5000 gm 500,000 gm 500,000 gpn 300 gpn 20,800 300 gpn 1.2 KN 24,000 gpn 24,000 gm 315,900 gpn 315g900 gpn 6~

208,300 0

666,600 500 50,000 gm 1,220,800 0

0-1 M8 7,645,000 4,000,000 300 its/rncnth 3>033 11,000 8,786,3$

1.2 KM 2,445,000 39,000 1,3$,000 500 11,000 1,167 693,000 21,000 gm 0-5 NZ 9 KM 4M8

-; 0-5000 gpn 0-284,000 gpn 0-284,000 gm 0-176 gpn 0-10,000 0-176 gm 210,000 0-16,500 gpn 0-16,500 gpn 0-185,000 gm 0-185,000 gpn 5 NR 208,300 0

666,600 500 50,000 gpn 220,000 0

7,645,000 4,000,000 300 lbs/ixnth 3>033 11,000 8,786,3$

1.2 KM 2,445,000 39,000 1,200,000 500 11~000 1,167 693,000 Bna gency/Testing'Intend.ttanb Use Varies with dissolved solids Cooiling tower rnsIQMp Average NstcnQogioal Ccnditicns CociUng tcwev bye line Intennittant Opraticn Ccndensate polisher regenaaticns ard rinse (Interrnittant Opaation)

Vay infract operaticn ArncUiary Bailer Drains Revioe Rrter System Seocndary %ste (Nomad. ) A14xmte Rcute

~ary Nebe (Rad. ), not nonrally used Eke-up as needed Settling Basin~

Treated mrna. Tank Drains Bra Punp Test Stcrm drains inoluhs rairMrter and fire wabr Potable %ter Rantor GxQmt System Danineralized Rrter Daubmalized Rrta to Arndliary Boilers Fire Bxp Test Hydrant and Drain Tests plant and HHK &hx'sage page 3 of 4

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SraZm Zm 0 mx.~

H.m 0 me. SHUrZOm 39 41 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 0.2 MK 8,340,000 10,000 33/ 300 1,220,800 0.2 KM 413,000 10,000 67,000 30 75,000 316,000 7,000 6,000 4, 100 5-10 gpn 10,000 6,950,700 0.2 MZ 8,340,000 10,000 33'00 220,000 0.2 KM 413,0O0 10,000 gpn 67,000 gm 30 75,000 316,000 7,000 6,000 4,100 5-10 gm 10,000 6,950,700 3rnitary Rmte Sludge reanml as necessary Yard and Roof Drains Mmp as requrled Bkey fcr 9 and 11 Sanitary Waste Raheste Boron Recycle Rrcn Recycle/CVCS Letdown Rate Qil Equipnent Drains.

Floor Drains Decontamfrated 1hste Laboratory ate (Chmfstry)

Varies with nunber of Alter baahashes

&ter Treatment Steam Heater Drains Cordenser mter box (apprac.

two drains/year)

Lcw-Valune Rmte

+Units:

Gallons per math unless ot erwhe noted NK = million gQlcns per mcnth gm = gQ.lens per~

Page 4 of 4

4

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1

NOTES:

1. SEE ATTACHEDPAGES Sh FOR TAIEOF FLOWRATES

2. SEE NARRATIVEFOR DESCRIPTION OF MAIORWASTE STREAMS UTWVOUJMEWASTE SETTUNG BASIi WAlER PRETREATllENT POTABLE WATER SAJITARYWASTE.

WATERTREATMENT SERVICE WATER SG BUJWDOWN MAGJKllC F%1ERS 12 1h NONCONTAM.OI.Y WASTEa FLOOR OIYWASTE SEPARATOR 17 19 WASTEIKEK BASIlS LIETAL CLEAIING WASTE MAIQMPAND POUSHI&

DELIRKRAUZERS h7 10 REN TOR SECOII)ARYWASTE HOIDNGTAlKS SHEARON HARRIS NJCLEAR POWER PlANT STATTONWATERUSE DIAGRAM PAGE 1 OFh SEPTEMBER 1h, 1990

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29 TREATEDWATERTANKDRAINS YARD8 ROOF DRAlHS WATERTREATMENTSTEAMHEATER DRNNS CONDENSER WATERBOXDRAINS RRE PROTECTTON SYSTEM DETAILA SECONDARYWASTE SAMPIETANK TREATEDHOTSHOWER TANK WASTE LIOHITOR TANK CO C9K CO LCCDO CC 0

COOLANTSYSTELI BORON RECYCIE EQUIPMENT DRY 2S SECONDARYWASTE FLOOR DRA9I WASTE EVAPORATOR.

CONDENSATE TANK BORON RECYCIETO CHEMICALIL VOLULIECONTROLSYSTEM DETAILB SHEARON HARRIS NUCIEARPOWER PLANT STATIONWATERUSE DIAGRALI PAGE2OFh SEPTELITER 1h, 1990

P

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ATTACHMENT 5

Sample No.90-4254 HARRIS PP&APA, MIKE MCDOWELL Environmental Compliance Unit CPB 4C3

Raleigh, NC 27602 Date Sampled:

6/13/90 Date Received:

6/13/90 Date Completed:

8/ 2/90 REGULATORY HARRIS COOLING TOWER DISCHARGE CCc w a<al&O ourFA4~ un')

Approved bf PO Number:

Sample Analysis Results Test Name Aluminum, Total Ammonia (as N)

Antimony, Total Arsenic, Total Barium, Total Beryllium, Total Boron, Total Bromide Cadmium, Total Carbon, Total Organic Chloride Chromium, Total Cobalt, Total Coliform, Fecal Color (Chloroplat. Units)

Copper, Total Fluoride Gross Alpha Gross Beta 110 8.7 ug/l mg/l

< 0.05 mg/l 0.001 mg/l 10 ug/l

< 0.01 mg/l 50 ug/l mg/l

0. 12 ug/l 15.

22.

2.8 mg/l mg/1 ug/l 0.05 mg/l Analyst GFD 563-49 JJ 589/21 SKM 587/7 JVW 580-53 SKM 587/8 SKM

. 587/13 SKM 587/7 JEZ 586/40 GFD LMP 585/26 JEJ 586/45 GFD 563-52 SKM

< 5 col./100ml MMW 70.

71.

cpu ug/l

0. 17 mg/l

8. 19 pCi/1 8.45 pCi/1 MHR 570/32 GFD 563-46 JEJ 586/32 MHR 570/40 MHR 570/40 Results Units

l 4

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'G Sample Analysis Results Page:

2 Test Name Iron, Total Lead, Total Magnesium, Total Manganese, Total Mercury, Total Molybdenum, Total Nickel, Total Nitrate + Nitrite (as N)

Nitrogen, Total (as N)

Oil and Grease Results Units MWMMMMMMWWM 0.530 mg/l 4.9 ug/l 3.7 mg/l 0.85 mg/l 0.05 ug/l

< 0.1 mg/l 9.6 ug/l 0.31 mg/l 8.1 mg/l 1

mg/l Analyst WWWWWWM SKM 587/14

GFD, 563-43 SKM 587/14 SKM 587/14 GFD GFD JEJ 586/40 SKM 579-90 MMW Biochemical Oxygen Demand

< 10 mg/l Chemical Oxygen Demand Phosphorus, Total Selenium, Total Si3.ver, Total Solids, Tot. Susp.

9 103C Sulfate (as SO4)

Sulfide Sulfite Surfactants Thallium, Total Tin, Total Titanium, Total Zinc, Total

.59.00 mg/l 1.5 mg/l

< 0.001 mg/l

< 0.05 mg/l 120 mg/l 59.

mg/l 0.9 mg/1 2.8 mg/1

< 0.1 mg/l 0.01 mg/l

< 0.5 mg/1

< 10 ug/l

0. 550 mg/l MMW 58 1/92 DCB 582-13 JVW SKM 587/12 MMW 58 1/64 JEJ 586/47 MHR 570/3 1 MHR 570/30 DCB SKM 587/7 SKM SKM 587/14

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Annual Pollutant Analysis lirionltorlng Requirement Reporting Form A

l. Facility Information:

NPDES Pepnjt No NC0039586 C~d0 Facility Name P6L SUPP Class:

W k Person(s)

Collecting Samples:

> ~ H" s "

Analytical Laboratory Webb I~ Technical GrouP CP&L GC/MS Library Size (number of chemicals catalogued):

Ii. Sampling:

24 hr composite for main sample I grab sample for purgeable fraction Page t of 6 Date Sampled: (composite sample)

Sampling begun (date, time):

Sampling finished (date, time):

Date and time sampled (grab sample):

Instructions The purpose of this document is to standardize the sampling, analysis and reporting procedures to be used for the Annual Pollutant Analysis Monitoring Requirement as described in the permit. In addition to the monitor-ing and reporting requirements described herein, the permitee willmeet all other relevant monitoring and repor-ting requirements as described in the North Carolina Administrative Code Section 15 NCAC 2B.0500

~ Surface Water Monitoring: Reporting. The permitee should use copies of this Annual Pollutant Analysis (APA) Form A to report the results of the analysis. Completed forms shouid include the signatures of the analytical laboratory representative and the facilityoperator in responsible charge (see p.6). Malltwo completed copies to: ATT:Central Files, Division of Environmental Management, NC NRCD, P.O. Box 27687, Raleigh, NC, 27611.

A 24.hour composite sample must be taken from the final effluent during mid-week (Nednesday through Fri-day). A grab sample forthe volatile organic fraction must be taken when the 24-hour composite sample is completed.

The effluent must be analyzed for pollutants, including those to be identified and approximately quantified under the 10 significant peaks rule, using appropriate EPA approved methods for each of the analytic fractions to be analyzed, as listed on this APA Form A. Other analytical methods can be substituted only with prior, written ap-proval of the Director of the Division of Environmental Management (DEM).AIIchemicals (orelements) to be analyzed for are included in the attached tables (parts A through F of this APA Form A, each of which includes space for the chemicals to be identified under the 10 significant peaks rule), and organlcs should elute in the chemical frac.

tion as listed.

Detection LlmltTargets which'should be met are listed on this APA Reporting Form A. Use of any higher detec-tion limitfor the purpose of this Annual Pollutant Analysis Monltorlng Requirement must be reported along with the results of this analysis. An explanation as to why the listed detection limittarget could not be met must also be submitted, attached to this APA Form A. Examples of acceptable reasons for not meeting a detection limit target could be high background concentrations in a sample, or the necessity forsample fraction dilutionto bring a chemical to within a detectable concentration. Ifa chemical Is found to be below the detection limittarget, report the concentration detected as less than (or 'C') the detection limit target In the appropriate space. Chemicals listed on the attached tables that are detected In concentrations above the detection limittargets must be quan-tified. Allchemical concentrations should be reported in units of mlcrograms per liter(ugll).Allmetals concentra-tions should be reported as total recoverable metal (as ug/I). The total number of peaks detected In each analytic fraction must also be entered in the appropriate space on this APA Form A, Chemicals to be analyzed for according to the 10 significant peaks rule (as described in item 2 of the Annual Pollutant Analysis Monitoring Requirement In the permit) must be identified where possible using a GCIMS library search. An estimate should be given of their concentration based on an internal standardusing a known chemical having the closest retention tlmb. Quantitation should be approximate and willbe used by DEM for planning pur-poses. The size of the GC/MS library being utlllzied must also be reported in the appropriate space, along with other required information, at the top of this APA Form A.

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Q. Acid Extractable Fraclion

" Number of chemicals detected in Fraction Fraction STORET Number 45582 Page 3 ol 6 STORET Number Compound Detection Limit Target Concentration Detected GC/MS Conffrmatfonf Yes/No

1. Pollutants to be analyzed for:

(ug/1)

(ug/1) 34452 34586 34601 34606 34616 34657 34591 34646 39032 34694 34621 4.Chloro 3.methylphenol 2.Chlorophenol 2,4 Oichlorophenol 2.4.0imet hylphenol 2,4 Oinitrophenol 2.Methyl 4,6 dinitrophenol 2.Nitrophenol 4.Nitrophenol Pentachloro phenol Phenol 2,4,6 Trichlcrophenol 10 10 10 10 50 24 50 50 10 10

<20 Yes

2. Other acid extractables (up to 10 highest peaks):

C. Base/Neutral Fraction Number of chemicals detected ln Fraction Fraction STORET Number 45583 STORET Number Compound Detection Limit Target Concentration Detected GC/MS Conffrmatfon2 Yes/No

1. Pollutants to be analyzed for:

(ug/1)

(ug/1) 34205 34200 34220 39120 34526 34247 34230 34521 "4242 Acena thene Acena'th lene Anthracene Benzidine Benzo a anthracene Benzo a

rene Benzo b fluoranthene Ben zo hi e

lene Benzo k fluoranthene Bis(2 chloroethoxy) methane 10 10 10 44 10 10 10 10 10 10

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E. Herbicides Numoer of cnemicais detecteo in Fraction

', Fraction STORET Number 00148 Page 6 at 6 STORET Number Compound Detection Limit Target Concentration Detected GClMS Confirmation?

Yes/No

. Pollutants to o= ana vzeo io;.

tug/1}

<ug/1) 39730 39045 39740 2.4-D Silvex 2.4.5 T 50 50 5

( DL.

< DLT

( DLT NO ilO NO

2. Other herbicides iuo to 10 hi hest oeaks:

F. Metals and Other Chemicals Number of Metals and Other Chemicals (as listed below) detected in Sample Fraction STORET Number 78240 STO BET Number Compound Detection Umit Target Concentration Detected

1. Pollutants to be analyzed for:

(ug/1)

(ug/1) 01104 01097 01002 01012 01027 01034 01042 01051 71900 01067 01147 01077 01092 Aluminum Antimonv Arsenic Bervllium Cadmium Chromium Co er Lead Mercu Nickel Selenium Silver Zinc 50 50 10 10 0.2 10 10 110

( 1'0'"

0.12 2.8

/I. 9

< 0.05 9.6

~ ~:GER-c (10.

550

2. Other inor anics:

01007 00940 00720 00951 Barium Chloride G anide Fluoride 20 (10 ~

22,000 C DLT 1 0 Analytical Laboratory resentative:

Signe Facility Operator in Resoonslble Charge (ORC I certify that t is reoort is curate and compl'e to the best of my knowledge.

Signed:

Date:

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SHEARON HARRIS NUCLEAR POWER PLANT COMBINED OUTFALL LINE CONVENTIONAL PRIORITY POLLUTANTS FIELD MEASUREMENTS Date Time pH Temperature

( C)

Total Residual Chlorine (mg/1) 6-12-90 1330 7.73 27.7

<0.05 6-12-90 1730 7.93 28.9

<0.05 6-13-90 0830 7.66 25.8

<0.05 6-13-90 1100 7.54 28.3

<0.05 Average Flow for June 12-June 13 was 9.95 MGD.

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SHEARON HARRIS NUCLEAR POWER PLANT POSSIBLE CHEMICAL WASTE FROM SHNPP Chemical Source(s)

Discharge

~Fre uene Estimated Concentration Treated Waste (ppm)

Treatment S~stem

'lum Ammoni a Water Treatment Secondary System 1I Auxiliary Boilers Weekly Daily

<20

<50 Settling Basin Waste Neutralization System Ammonium Bisulfite Anti-foaming Agents Chlorine Removal Sewage Treatment

Plant, Waste Evaporators Continuous As Required

<5

<10 Cooling Tower Radwaste Processing or Sewage Treatment Plant Boron Waste Processing System (Reactor Coolant Waste)

Periodically 200 Radwate Processing System Chlorides Demineralizer Regeneration Periodically

<1,000 Waste Neutralization System Chromate>><<

Closed Cool ing Water Corrosion Inhibitor, Possible Leakage Occasionally

<5 Cooling 'lower Basin or Neutralizaton Basin Citric Acid Copper Chemical Cleaning Filter Flushing, System Maintenance, Chemical Cleaning Periodical ly Periodically

<5,000

<1.0 Radwaste or Waste Neutralization System Waste Neutralization Basin Detergent Waste and Dirt Detergent and Waxes Waste Processing System (Industrial Cleaning)

Janitorial Cleaning Periodically Daily 1,000 1,000-1,500 Radwaste Processing System Sewage Treatment Plant "Final discharge is through the combined outfall pipe to the Harris Lake.

""Chromate system is currently being taken out of service.

(90-155BWS)

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SHEARON HARRIS NUCLEAR POWER PLANT POSSIBLE CHEMICAL WASTE FROM SHNPP Chemical Hydrazine Source(s)

Secondary System 4

Auxiliary Boilers (Chemical Additive)

Discharge

~Fre cere Daily Estimated Concentration Treated Waste (ppm)

<0.06 (5

ppm after wet layup)

Treatment

~Setee Waste Neutralization Basin Iron Filter Flushing, System Maintenance, Chemical Cleaning Periodically

<'I.0 Waste Neutralization Basin Nickel Oil and Grease Filter Flushing, System Maintenance, Chemical Cleaning Waste Processing Systems Periodically Daily

<1.0

<20 Waste Neturalizaton Basin Radwaste Processing System Phosphates (Organic 4

Inorganic)

Cooling Tower Treatment, Potable Water, Industrial, 8,

Janitorial Cleaning Daily

<5 Cooling Tower Sewage Treatment System Phosphoric Acid Chemical Cleaning Periodically

<10,000 Radwaste or Waste Neutralization System Photographic Chemicals Polyacrylic Acid Polyelectrolytes Microfilm Processing Lab Cooling Tower Treatment Water Treatment, Sewage Treatment Plant, Chemical Cleaning STP, Radwaste Occassionally Dai ly Weekly Periodically

<5 ppm

<10

<1,000 Neutralization Basin Cooling Tower Settling Basin, Cooling Tower, Sewage Treatment Plant Sodium Bromide Biodispersant Daily 0-0.5 ppm Cooling Tower

" Final discharge is through the combined outfall pipe to the Harris Lake.

(90-155BWS)

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SHEARON HARRIS NUCLEAR POWER PLANT POSSIBLE CHEMICAL WASTE FROM SHNPP Chemical Sodium Carbonate or Bicarbonate Source(s)

Chemical Cleaning Discharge Frerrfuenc Occasionally Estimated Concentration Treated Waste (ppm)

<5,000 Treatment

~Sstem "

Radwaste Processing or Waste Neutralization Basin Sodium Hydroxide Demineralizer Regeneration pH, Adjustment (6-9)

Periodically

<1,000 Waste Neutralization System Sodium Hypochlorite

Biocide, Chemical

Cleaning, Sewage Treatment Daily Periodically Daily 0

Cooling Tower 4 Sewage Treatment Systems Sodium or Potassium Molybdate Closed Cooling Water Corrosion Inhibitor, Possible Leakage Occasionally

<500 ppm Cooling Tower or Neutralization Basin Sodium EDTA Chemical Cleaning Occasionally

<10,000 Radwaste or Waste Neutralization System Sodium or Potassium Nitrite Closed Cooling Water Corrosion Inhibitor, Possible Leakage Occasionally

<500 ppm Cooling Tower Basin or Neutralization Basin Sulfates Demineralizer Periodically

<1,000 Waste Neutralization System Sulfuric Acid Demineralizer Regeneration, pH Adjustment (6-9)

Periodically

<1,000 Waste Neutralization System Tolyltriazole Closed Cooling Water Corrosion Inhibitor Leakage and Cooling Tower Treatment Daily

<20 Cooling Tower Basin or Neutralization Basin Total Organic Carbons Demineralizer Regeneration Periodically

<2,000 Waste Neutralization System

" Final discharge is through the combined outfall pipe to the Harris Lake.

(90-155BWS)

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SHEARON HARRIS NUCLEAR POWER PLANT POSSIBLE CHEMICAL WASTE FROM SHNPP Chemical Zinc Source(s)

Cooling Tower Treatment Potable Water Discharge

~Fre uenc Dai I y Estimated Concentration Treated Waste (ppm) 1.0 Treatment

~Sstem Cooling Tower II Sewage Treatment System

'Final discharge is through the combined outfall pipe to the Harris Lake.

(90-155BWS)

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ATTACHMENT 7 Carolina Power 4 Ught Company P. O. Box 1551

~ Raleigh, N. C. 27602 5NR a3 tSSZ JAMES M. DAVIS. JR.

Senior Vice President Fossil Generation it Power Transmission Serial No.:

ESS-87-272 Mr. R.

Paul Wilms, Director N.

C. Division of Environmental Management P. 0.

Box 27687

Raleigh, N.

C.

27611-7687 RE:

NPDES PERMIT APPLICATIONS DELEGATION OF SIGNATURE AUTHORITY

Dear Mr. Wilms:

As allowed by the North Carolina Water Pollution Control Regulations, Section

.0106, "Filing Applications", I hereby designate the Manager of the Environmental Services Section (ESS) as my duly authorized representative for the purpose of signing Carolina Power

& Light Company's (CP&L) NPDES permit applications.

The ESS Manager coordinates CP&L's non-radiological environmental programs and directs regulatory, compliance, and monitoring activities.

Currently, Mr. G.

H. Warriner occupies this position.

This action is in concurrence with a telephone conversation with Mr. Arthur Mouber ry of the Permitting

& Engineering Unit in which Mr. Mouberry indicated that CP&L could assign this responsibility to the ESS manager.

Should you have any questions or need additional information, please contact Mr. Warriner at (919) 362-3235.

Yours very truly, E3;->P'inn>

S>~77. H Ly JAiVIES M. DAViB, JP~

J.

M. Davi s, Jr.

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