ML19325E048
| ML19325E048 | |
| Person / Time | |
|---|---|
| Site: | Mcguire, McGuire  |
| Issue date: | 10/24/1989 |
| From: | Tucker H DUKE POWER CO. |
| To: | Overcash D, Wilms R NORTH CAROLINA, STATE OF |
| References | |
| NUDOCS 8911010070 | |
| Download: ML19325E048 (11) | |
Text
'
gh ' . e b Jt ,;
s
][;M,%)
y ,
s s
,v
. f f '. ' , ;. ~, '
'o _
r y 'E', m Duxz POWER GexpAny .
.s , <
P.O. NOX 33489 U ' '
s/ OMARLOTTE. N.C. 98249 9
, c-y . , , , HAL B'. TUCKER ; , ni,,mo,,,
- 59. *>c= *= *=asari '
. . m u.. :eno.
, , ng onmi n
m, c .
6i N <- 3! ,
i ..s
. 4 ,
' LOctober124, '.1989 '
L ,
s s . ,
y;, : Mr.' R; Paul Wilr.s, Director s 'Div.isionlof Environmental Management.
F", ' Department of Environment, Health, and Natural Resources.
P.O. Box 27687' Raleigh, NC 27611
[f_ ~ .
Attn; Mr. Dale Overcash
Subject:
- McGuire Nuclear Station 'k
- NPDES Permit Modification o . - Adding-. Inputs to Treatment Facilities .
File: MC-702.13 ]
Dear Mr. Wilms:
Duke Power Company is constructing a new vehicle maintenance f acility at the McGuire Nuclear Station site and desires to route the wash water from ;
- the' vehicle wash pit to . the McGuire domestic. wastewater treatment (WT)
J .
. system. In discussing the proposal with your staff, we were informed, that since the WT system 'is permitted to treat only domestic waste, an- :
< application for an NPDES permit modification would need to be submitted. l
. In reviewing the application for modification, several additional small inputs were discovered and ' ire included in the application. Additionally, a : '
now landfill is being proposed to be constructed in 1992. It is desirable
[ '
'to route any leachate from the landfill to the conventional wastewater treatment (WC) system. This proposed input is included in the modification application.
Please find enclosed triplicate copies of the application to modify the HPDES permit and a check (no. 244050) for $400.00 for the permit i
COC'I
,i' l(
8911010070 891024 '
3r' ', .- -
a, El y,.
ij f , ,; II.. e -#
o' , . g 4
+.
.m'w
'#k?, j) c
, p ,, $y -
. , h *= ' I 1 -
g m,-----
-it : .
%r'hw,Kr, t ,w a i .,,,",4c t - oT s' .y;N W, W. -
A ~~d4;
,l . ,
>, '4 7-n'Q,s , , , <a .v,,~<- a gsgi.'u ; h m .;-@y..
b I, . ,3 me .
'i t ,
a, <
,i ,i g ', f \7,..- t J. . .
- L .
.'I'
,k' f
(
~
. . , .t.=
.', ' y' '[,
1 .
h [ 4', ' ( ,'
m :,f
- ' j '
f
'&. = $ s,y 4N
' hj f.- N ,.f Vi' i
- m't. , ,'$:j.1 u . t t
i ,,' -E ,
m ' ,
+ '
@fl}$r; f{f[. ' i. j' u '(- .pJ q Sl
. c
'y ' ', ., ,
,f ,
t ,
'.h L;
m' o. ; .x b,,[
, c ,
, ,,. i , a g
.m e: ~;.
s o
n
,g 4 i
%, - s m .
.v o +o ,s ,
s m . .
g$.. Q. %g:.S *
' g 1NrXR.4 Paul WilmsE ' '
'.1 ,r <
W gq '
y .
c
'.d.- w' d , LOctoberl24 F 1989 o
"- 4 W+m '
1 wa;4
,m,- .
t.q .- -
0 s: Page:Two;.
e '
. o ,
4, (c A. ' i, p r .4 , ~ a y ;y- ,
- , , y ,
, r n
- y. .
sgff k f , ...r ; y -
zo u ,
, /
9i g*
- : n a. ,3
- . J. '
, , . I
,,,., i s i
W,45: ? / , i ,,;' , ' p'O'rocessingO f'ee. LSh'uld?"you: o havo : any e quostions ; or , desire ad'd'itional' ' -!
- g. , M y ' m ;3 nformation,' please. contact J. S. ' Carter - [ (704) 373-2310) . *
-o "Q w: t g ag- s s
- t i
' ,q i
4,1, . .,, p t ,
,.,s3y s s i. c. . .
g-Pe=!' L a i. > i .I..
,4 Y
.,2
+ 4, q . . . ~)
4 3
c.
, =
r >.
$,v;Sincerelyg ,j ,
+,.
g, ,-[
m;y ~ . ~ WG 1., , w
-, m v , ..
. w; , ' . > ,
, ,' <;- p a
ay ;! w ,
h.'> 5 hc .,.
/ f ._ .>-
6 , - 'l a. ,
l ww , ,
- q. ,. , .
R/ o .sa. ..
Hal BF. T.uckerk.ViceLPresident
.f.0 M,
m,e,s.g' M ./.r. f. ,". l Nuclear Production Department g
. r-
/a, j
. . v*:
, ;n , , - ,
v : p-s. 's s
-, ..1 a > ; -
M,,f:. 7.? '
u , m, LWTG/rmb:0420i , e s
- M 4.3 H._m, . g .,
.y* -s v a
i q, ,,. Igg i( P
, g
',' y'. ;iW 4. < > En' cl' 'o'sure' s" , , , ,
.f;J, . . .
+
7
.r; -
. 1
()
m2 . .ry ON. :. g /cci INRC Document Control. Desk y~ . - as-y;[ , w y . g ,
(
s
,...O., t q. ,
q #' ' b 3 NI g,, t-4 ,.1 .[F +, i,y,., (
. . ,1 l \ j ! ' ' k
..s
- i. ', , , ,, gy Q , .'O , , , > i
'g p.69<
.f { * <n '
y L m. ,;, , , ,
3c
.: 1 <;
._v , ..
i, %
r s '
6 /-
y
- i, ' i3 - ,
sg y
l 5,1 .E; -
t- ' {' f >
' ,[ - #1 a
, , a{
': s ;
<, 4, "h ; ,
< I
/,
.4? l4 i
, 't Y,'
=j,,['%
, 1
, [
m, 3lv i
s' , t i A0 e ,
\(,o.' sL , , ,"
, .{ j, , l %' N us a- ,
L M, h8,*
q I 's ' , fI 1- , ' 1 a :. > t
- Q. i, [l : ' . .,* .k u ,9 ,
j.,<g,
- (' r . _,
r'a i
- '.., i g
, , .'l i '.,
i
't y,.bai.'.
t , ', :'b -
i lb ,
4 i .t'E,
4i p
t i
L ? N,l \
- _ . .
MLi si 9 (;
6 J
, , 6 1 1
)*
g,
~t, ,, i '[
..:fr;.Jr W 4
+w 3
, .i
.( .
3 ,i, , f 'c,. \ b
.m
[ (. % g g, .- ss
, i 16
-. ? sIi.t, )
y E 4, ' ;i
, 1b i .' s, . .W N3,,.
t ry .
-1. , . [.) <r. o . -
e ' Eph . -P ea ,i, , f, n i i
' s.q: ;
y .'m ,- a
[ ,,.
.y
.,,e 1 g
u 't -, n w
.g+ge ; .4
- q g;4,,@y-. , ' .
g\, ; Z' +!1 :.n. .
n' e
, 4 . , _.m. _
y >
&. y _.
l 1
i
\
'.i '
q
,4 w_ <
.4_=,,
c=..=,
.2. i. ps__ .
r=
. n R
- .,.=a, J cuAni;orrS;NORTE .a_ wn .DUE$u -QW+. ".; ER.. COMP 24 ANY
- m __
ox .n=- ,
d :, CAROLINA. totes t .1
...4050 l
. .=.,dg:.l .-.8.;:il._ll=!I'll=d.I; sir = j r= a -- a Mi
--i - -- - ,t i =ii=Il=li=JlsWilulF=ll.ll. ll=II.- = il...... -
l=1;,
ll=lf
~ . r. .
= - a =- = :=q=e',,
. ,i = i i =
,='F " V il :
lf= :- L- -
PAYi ,$ *,='G eom00!'7 1 w midl =llp.ll.=lff=ii' =li iW=li= =in=
c= =
- =
l =n itr= =!I:=li =lrllsim ..
- = m=J.n=w, = p.= = sn=s-ii i. c==.ii ,=;f=. .-.
=; .
ei=i =llilfNiiw = = a .-.;
=lN= q =e1=! =j =l" =lyl_f 11w, ,
' PAY m' "== 2 -- o a:ir -:-
oem,;=il
,, ,,= != ii n .- ;
S. .
endsO DEPl. G _ =; @. =IA h. . . .$8URCES- --
, - %. W W '. i. l **"'".'.'*. .""
.f , .-i: q -) . . g g --.
~
. ~ l i.g g Cl Muff 1TVil By TRI ALITY)- ;- '.
"pg. g ign i-i .c . ~~'.. " " " i
....i
. = " .: ! ,@ . ^ T'I . NC.276. '.
- }7, "=' i ;
- RALE. -
- i.- :.- a n - . - l. .
. .: ::..L = . = . ' .
.. t . . = ..,
e u*0000 2440 50A s:0 5 3 D O O n8 31:Q L &B E. 5 0 5 4 4 3 9u'"
-l
'l 4
i e
4
?
')
i s
6 I
.t i
h
, , .<-w--- - - - , . . . , . . . . - , - - - . . - - - . - - - . - - . , - . - - - . . . - - - - - . - . . - + - . . - - - - . - - . - _ _ _ . - - - - - - _ . - _ ------_.----------------+-=s
yW*% y L..',.
pg .
Xw i
- Supplemental Infomation
- McGuire Nuclear Station 3 System Description j
'i b [
I Additional Inputs to Conventional Wastewater Treatment (WC) System (Outfall
, 002)-
i L ~ >, Outfall 002 discharges treated wastewater from.the Conventional Wastewater 0 ' Treatment (WC) System through a Parshall flume to the' Catawba River below b ,
Cowans Ford Dan.. The 'WC' system consists of a concrete lined initial holdup
.,' pond (IHP, 200,000' gallons), two (2) parallel clay-lined settling . ponds i (2.5 million gallons each), and~ a concrete ' lined - final holdup pond (FHP, 'l
[~
million gallons). ' Normally, inputs are received 'in the IHP but can be routed directly to an in-service settling pond. The IHP. serves as a common mixing point for all wastewater, a surge-dampening function'.to the 3 remainder of the system, and allows the heavy solids to settle for periodic removal. Retention time in the IHP is ' 12 to 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />. Solids removed from
-the IHP . are dewatered ano disposed' of on a State licensed landfarm or i
landfill.-
! Flow is directed to the in-service settling pond through the chemical addition building where caustic, acid, and/or other chemicals may be injected ~ into ~ the water by a metering pump. Sulfuric acid and' sodium 3 hydroxide are added for pH control- or to precipitate verious chemical l
{~
compounds. Coagulants may be added to facilitate the settling of ' lighter !
solids. Additional treatment may include chemical oxidation with j hypochlorite (calcium or sodium) or catalyzed hydrogen peroxide. Retention time ' for each of the settling ponds range between 6 and 12 days. The .,
settling ponds can discharge to the PHP or directly to the Catawba River. !
Treatment and discharge are normally on a batch basis.
The FHP is aerated and is used to remove any persistent oxygen demand or to ;
provide additional holdup capacity. The FHP retention time is 1 to 2 days.. j The capability is availablo for recirculation intra- or inter-basin. Flow }
to the- Catawba River may be by gravity at a rate of approximately 200 gpm )
or be pumped at a rate of approximately 500 gpm. The pH of the discharge l from the WC system is adjusted by the automatically controlled addition of 3 carbon dioxide.
The WC system accepts all nonradioactive plant waste except sanitary 1 sewage. The inputs can be contaminated with very low levels of radioactivity. Any discharges of radioactivity are monitored and accounted !
for, being regulated by the Nuclear Regulatory Commission (NRC). Inputs to \
the system were described in the renewal application submitted December 28, i 1988. An additional input being contemplated to begin in 1992 is the d landfill leachate, j Landfill Leachate The landfill will be constructed on Duke Power Company property across Highway 73 from the station in 1992. The maximum working (active) area -
of the landfill is currently estimated to be approximately 0.45 acres.
1 s
Wp g ---
~ . ..L ,
g . .
,t * ,
es .
nb; # -
s !
4r; g /
- ,[ ,
. i
~
At. this time, it is unknown how much leachate will be collected. The
. r, 'leachat_e_ collection system is being designed to collect 68,000 gallons
, (the rainf all from thel 25 year 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />. storm event, approximately 6 inches,ifalling on the active area of the landfill). The leachate"will' be tanked or piped to .the WC system. :The, content of .the leachate will v be unknown until some leachate is collected and sampled. The. estimated average flow will be, assuming all' rainfall on tho active area becomes ,
leachate, .1,446 gpd .based on 'an average annual rainfall of 43.2
'.' . .i nches .
Xy i
Additional' Inputs to Domestic Wastewater Treat! ment (WT) Pacility (Outfall .
'003) 7- 1
- $ outfall ' 003 discharges treated wastewater from the ' Sanitary -(Domestic) j Wastewater Treatment (WT) System to the Wastewater Collection Basin (WWCB). i The- Sanitary Wastewater Treatment System is- a four (4) cell aerated lagoon system. The lagoon provides a 5-day retentions time and will allow for variable level discharge. The wastewater effluent f rom the aerated lagoon flows through chlorinators, a chlorine contact chamber and'a Parshall flume before' discharging to the WWCB.
The lagoon is liried with a flexible syr.thetic material such as hypalon; it is divided into four (4) calls by a curtain material such as a polymer coated polyester with a' weighted chain ballast and floatation collar. The first cell provides for a two day retention cime and ^1s kept in complete
. suspension by surface mechanical aerators. The second and third cells are kept partially suspended providing for partial settling. Each of these two ,
cells has a retention time of one day. The final cell is the settling cell with a retention time of one day. The surface of this cell is kept slightly agitated to minimize algal growth. If it becomes necessary to control algae growth, an algicide, such as-CUTRINE-PLUS, may be 4.dded to the. lagoon. From the final cell, the wastewater discharges to a chlorination device. After passing through the chlorinators, a retention time in excess of 30 minutes is provided by a contact chamber before being discharged to the WWCB.
T The sewage lagoon has a multiple level discharge capability at 5, 6 1/2, and 8 feet. At each of these dif ferent levels of operation, the lagoon is able to provide a 5-day retention time for influent wastewater Clow rates of 40,000 gpd, 52,000 gpd, and 64,000 gpd, respectively.
Accumulated solids are removed from the lagoon approximately every 12 to 18 f months to f acilitato removal of non-biodegradable material and to optimize the treatment process. The sludge bottc,ms are dowatered utilizing a filter press or other suitable method. The solids are treated with ilme and disposed of in a State licensed landfill or landfarm. The filtrate is returned to the sewage lagoon or is treated by neutralization and carbon adsorption or other suitable methods when released directly to the WWCB. An alternative method of sludge disposal is to tank it to a municipal sewage treatment system.
The system was designed primarily to process domestic sewage from rest rooms, showers, and lab drains f rom all buildings on the site as well as 1
2
h ,
E. < ,
u a; , c.. , 9 3 ,,
g p o .H j
[d '
i L ,i' the. ' station cafeteria..' Additional inputs are -the Vehicle Maintenance H
~ Facility building. washdown IC "
sewer, .the Construction and Maintenance h',"
p'
- Department ' - ( CMD) building and. shop ~ drains, and ' the Quality ' Assurance Department photographic wastes.'
- Vehicle Maintenance' Facility The Vehicle Maintenance Facility building .washdown sewer. will convey
- .> . wastewater from the building floor drains and vehicle washpit' grit s K a
- chamber through an appropriately. designed 'oll-water separator to .the a g' ' building. sewer system. The peak flow is expected .to be 1,920 gpd. Due - ,
to' the ' intermittent. nature of the wash -water flows, the averagefdaily 4
~
ficw will be minimal. The wash water . is -in addition to the domestic wastewater'from the facility. ,
i Construction and Maintenance Department Complex ;
In , addition to domestic -sewage, the Construction and ' Maintenance 5 Department (CMD) building and shop drains discharge wastewater through '
an appropriately designad oil-water separator to' the building sewer. j Q The waste stream from the shop areas will contain water and milling / .
O machining oil. No emulsifiers are used in the wash water. The drains
' discharging to the separator are installed for emergency purposes only ,
and are not intended for routine washdowns. The maximum daily. flow is .!
150 gpd.' The average daily flow cannot be estimated due to the highly c" intermittent nature of the flow.
Quality Assurance Office Facility The . primary effluent from the Quality Assurance office facility is ;
domestic waste. However, the photographic waste is connected to the i domestic waste line. When operating, the photographic waste consists of.approximately 4 gpm water, 0.0059 gpm developer replenisher working ,
solution, and 0.0297 gpm fixer and replenisher working solution. The !
developer' replenisher working solution contains hydroquinone, glutaraldehyde, potassium sulfite, and potassium acetate. The fixer and replenisher working solution contains ammonium thiosulfate and sodium sulfate. Other developer replenisher working solutions and/or fixer and replenisher working colutions with other constituents may be substituted in the future. The developing process is operated a maximum of 30 hours3.472222e-4 days <br />0.00833 hours <br />4.960317e-5 weeks <br />1.1415e-5 months <br /> per week (4.3 hours3.472222e-5 days <br />8.333333e-4 hours <br />4.960317e-6 weeks <br />1.1415e-6 months <br /> / day) but averages 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> per week (1.2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br /> / day). Operation of the developing process results in a maximum of approximately 1041.2 gpd, with an average of 290.6 gpd, of photographic waste discharging to the V:T system.
i
'? Chemical Treatment in Radwaste Treatment System (Outfall 004) j' The NPDES permit renewal application submitted December 28, 1988 described l the Radwaste treatment system including the wastestream inputs to the i
! syctem. Included in the descripticn were the chemicals that could be in
, these inputs.
Occasionally it is desirable, and permission is requested, to oxidize sodium nitrite in the waste monitor tank using hypochlorite (calcium or o
3 3 i
m
% W Z ,,
~
' > :x, , ", < '
YJi .tc ,
..e :.. o.
vu, ,7.' , . , ,
\ ..
p y: :; i
. 1 1
' sodium) or' catalyzed hydrogen ' peroxide. When this treatment is ' performed, the waste monitor ' tank is isolated, recirculated, and mixed. The tank is
- i - sampled to ensure ~ that the ' nitrite has been oxidized. The'. addition of the
.' oxidation chemicals-' should .. result . in a small' residual of nitrite . in the .
tank since the oxidation chemicalslwill not be stoichiometrically added'.in -
fis" ,
. excess. Discharge 'is 'at a rate of '150 gpm into the condenser cooling water f(CCW) which typically has'a' flow.of 640,000 to'1,016,000 gpm per unit.
- r. Li g.
\
{N '
I' pr
.1..
, I '. . if , ,
1 a
f r
\
l' l'
i i.
L:
P ll .
r 1
. j' S: )
I 4- !
I
+
b a- .
.I 4 J 2'
.. );
- o m er.... !
sea 4.o. Numes n.c.ex tram inom o ur ro m n o c. veno n ao w u n wease orce or tvo. in the uninroed eree-i oniv.
DMUM **'*' N"es M as )
pg v.s. sNvinomenaNT AL PaoTaction Aosmev ,l
, APPLICATION PC PEJIT TD CISCHA~nt CASTEWATE3 i EXISTING MANUFACTURING, COMMERCIAL, MINING AND SILVICULTURAL OPERATIONS
'upggge Consolidated Perrrtits Program l
For each outfall, het the latitudo end longstude of its location to the nearest 15 seconas and the name ce the receiving water.-
A e g gggL a e. L A T s TWWW C. LONGITWOE
- .L aaau ...... .... ...... ...... .. .... ......
Catawba River 1
[ 002- 35 25 59 80 56 55 003 35 25 59 80 56 55 Catawna River via Discharge 005 l
~
)
A. Attach a line drawing showing tne weter flow through the tecility, indicate sources of intake water, oparations contributing westeneter to the ef f4ent.
and treettnent units lebeled to correspond to the more detailed Osascriptions in item S. Construct a water belance on the line drawing by showing swesy C flows between intakes, operations, treatment units, and outf alls, if a water belence cannot be determined te g,, for cereeirt m/ning act/rities), prov'ce a i' pictorial description of the nature end emount of any sources of water and any collection or treatment measures.
B, Ftr eeen outfeil, provios e oescription of t (1) All operations contributing westewater to the ef fluent, including process westoweter. serutary westewater, n dit nel h :ifn Ce .
O OO l . CUT, s. OPE R 4TiONJS) CONTRieUTING FLOW 3. TREATMENT
^ " ' L' g a gg/ e. OPE R AtlON thall s ti[un te', a DESCMiPTION .'s Conventional Wastewater Treet- 0.41 MGD Sedimentation 1-U- .
l
,- 002 ment (WC) System which receivcs Skimming X-X input from the following: Precipitation 2-C _,
j turbine building sumps, Co-Precipitation X-X water treatment room sump, Neutralization 2-K l ._. -,
condensate demineralizer Chemical oxidation 2-B !w_.
backwash, lab drains, steam Mixing 1-D l generator blowdown,. wet lay- Flocculation / Coagulation l 1-G I 2-D up solut ions, floor wash, Discharge to surface water 4-A metals cleaning waste, land- .
fill leachate (estimated to -
I begin in 1992).
Sewage Treatment System 0.040 MGD Screening 1-T 1'
I 003 (Monitoring only; discharges Aerated lagoon 3-B through Discha.rge 005) Chlorination 2-F l
1 l Additional inputs include 1
I Vehicle Maintenance Facility 0.002 MGD l
(Peak Flow) .
CMD Building and Shop Draino 0.0002 MGD" l (Peak Flow) l QA Facility Photographic 0.0003 MGD Waste i
l
- i The Average daily flow will be minimal due to thc intermittent nature of the wash water flows _-- -l U F F 4CI A L ust O NLY igf[Jurtig guwghnes gu b.cg3rggygrtyg,
_ _._.. _ _ .__ _CO N T I Ny t ON H r. _1
4 ., _, __ .. - - .
} , .J,[' ,.9 '
.u > "8 c , '1
,2 1 ,
i enesfakuto petOM THE plIONT 4:
f i
C. Emespt for steem runoN, tsche, et asHHe, are any of the dioshorges described in iteme IbA of B intermittent or sessenet? , ,
} ' Q &311empJete the folimme teMn C")N18 res to seetisa Ill) .
,e.
i 3. F REGUENCY l 4. FLOW )
,3
~a l.CUTPALL NU'ISER ' 4
- 3. OMR ATION(s)
CONTRIBUTING FLOW -
- e. Dave b. MONTHe Fan waku PamvsAn r m l 't e e,"" l < g gg, ts9elfy tspecify t. &# me to su 4. waasswu 1. some vana &TSON . -
l
, [hgg) ' , [M8(/ everagej evemase passy .avsnese a. maa pai6iu,wm (en days) "
everseef
.U (See Renewal Application submitted December 28, 1988.) -
4
- , )
.I Il I
(i , I s
I l
.' l A. Does en et*iuent Guideline limitation promulgated by EPA undeer Section 304 of the Clean Noter Act apply to your feCihtyi 3 s~se teomplete item fil BI CNO ito to Settron AV) ,
. S. Are the limitellone m the opphCoble effluent gul*lelsne expressed in terms of production (or other rpessure of 4Woretionl? .f C Yse fromplete item Ill.C) ? ero tea to Stetton IVI
\'
', C. If you enewered "yes" to item ilb8, list the cuantity which represents en eCtual meesurement of your level of production, expressed in the terme end units C used in th4 applicable effluent guideline, and indeCete the effected outfelle.
6
.. 1,. AVERAGE DAILY PRODUCTION .
C. oes s avione. enoowc t. war e nia6. etc. OUTFALLs .
e, eventerv esa may b. wm's se measwee repecifyp thst outfall trum ssen, }
N/A i
h l
l ,5 '
', q.
m o ,
I 1 n
~
IV. IMPROVEME NTS] .
1 A. 'Are you now requir'ed by any Federal, State or local authority to meet any amolementetson schedule for the Construction, upgrading or ooerotion of a .
(e witer treatment equipment or practical or any other environmental programs Which may effect the discharges described m this application? This ine'-
U/ Dut il not hmited to, permit condition 6,4dministrative or gnforcement orders, enfortement CorMhence schedule letters, stipulations, Court orders, anc ;
or toen Conditions Qvse teomplete the followsne table) D N O (to to item IV.8)
. 1.IE3M FlC N OF CONotTIO98 e.AFFeCTeO QUTFALLe p a N
- e. mo. Ik sounts op oisewanes evid*o ,c.
oi
.N/A i e
ii
} l t .
Ie
' i i I l
B. OPTION ALi You may atteth additional sheets describing any additional water pnHuMn Control proges for other enetronmentalprojects whrer' may .s'
.t, ' your discharges) you now t ave underway or which you plan Indicate whatner vJCh program il MW underway or planned, and indicate your act'.
( . planeed schedules for construction. ]gggg ..g.. IF OtsCRIPTION OF ADDITION AL CONTROL PROGR AMs le ATTACMs0 P AGC 2 OF A CONTINUt ON PA"it .1
. ' EPA Form 3610 2C (Rev. 2 85)
P,'
~ .. - _.- ..-.-.-.-
.?* #
y..
) n. . . ,
p .' ,
form toproveg -
lt t A 9, & C See instructions tafore presseding - Complete one set of tables ior each outteil- Annotete the outfell number in the spese proinded, H'
NOTE: Tables V.A. V 8, and V C are ineluesd on separete sheets numbered V 1 through V.9, .l l
'. D. Use the esece below to list any of the pe64utente listed in Table 2c 3 of the instructions, whien you know or have reason to believe is discharged or may be
- discharged from any cutteil. Pos seery pollutant you list, briefly describe the reasons yt.; believe it to be present and report any onelytical date m your l a . possession, s.PoLoutAnt a.sounce t.coLLuvANT 3.sounca i fL , . . .
L !
! v L' .t l
- t. s a
t 1
l
.y s, \
i;
')
l rI l c.
l; i
' , e 1
,4.. ,
vi. POTENTI AL DI6 CHARGES reOT COVCRED BY ANALYSISM ,
is gnypollutant listed in item V C e subetence or a component of a substance wnicn you currently use or manutecture es en intermediate or final procuct or .
! byprodut,t?
7 v se stat att mch em:rurme, n. t.,,w., X so <<a to Item VI as
1N/A.
5 1
l l
l l
+
1 1
C 2
, j l
l l
1 i
l 1
' j i
r.
. ),
s.
'j ,
-l P A G E 3 o F' 4 CONTINUE ON RE' t
,, ; EPA Form 3610 2C (Rev. 2 96)
, . . . . - _ . . - . ~ . . _ . _ . . - _ _ , . , - . . . . . _ . _ . - . . . . . . . . _ . . . . _ . . _ _ _ . _ _ _ _ . ~ _ _ . _ _ _ _ - _ _ _ _ __ _ _ __
c.
' ,, f '
I I j. & /, ,f g l [
Y
)
q1 2 . h, O
r
- r ,
s i s L Jageremoso pn0hl mg p*W
-y p . . . _ . . _ . , , _ ,
- 4 -
4 is' 0e you has any knessesses or ressen to tieteeve inet eny tuologieel test for acute or chronic tom:sity nei tieen moos on any of your o. norge,,, on e J
{3 ) tem 6veng guaget in relelsen to your checharge wethan the teet 3 years? .
\
- y. 8 , iT.% vee resonant, ese rettei ens sener,se' esete euron serows c.-'No toe to seetion r!!n 1 W. 1
' Fathead minnow acute 96-hourtflow-through test. .j
- 1. gU Ceriodaphnia 7-day: chronic- survival, and reproduction test. 4 i
l nThe purposeLof both tests was for in-house knowledge of whether:the discharges were- .
I fi t c toxit; n The results of the . tests indicate that there is no toxicity in the ' discharges .
]
0
- n. ,'c,i- r s
J
, )
- l. i" 3 ;
K ., <d y, s 11 ff 1
l
.)
i '
s 4 1
[.9 i i
i t
.J
.a e 1l l'
s
/ 'l i'
s
, 'l VillCONTRACT ANALYSIS INFORMATioN ' M' N
~ nr.;.,, '
Wera any of the analyses reported in item V mirurmeo W a :> v et '.:uomto y or consultir g f.rm?
T ' K~~ vt san'h'an'ua t n unc ruov sir. w n.e" m&'m ,ua , ~.:ur ec c . . . of
,i se.um.
m .ws wrutants -No tso to se<t,an in i 4 Nau
= ~ - ~
,, .oo,,,,, mrmo .t,N n so ;
.; c.v4 ;m - o x ,. , .
a : .
, Enwright Laboratories, Inc. P.O. Box 5287 (803)373-0707{ Part V-C parameters: i Greenville, SC 29607 and analysis of ,
- , t i
e
{ hamplesonDischargo J r
004'(Radwaste). '
i
- i. > ,
. i [ s (See Renewal Application submitted December 28, 1988 for data.)
i i !
i
^
ll l i [
f, '
k i i
l' ,
is y f c:rtofy underpenelty ollo w thet this document end elt attac hments were propered under my directic,.s or supervisoon in accordance wrth e s ystem c'es. ;
Casurs that quelofredpersonnelproperty gather and evaluete the Information submitted Based on myinquory of the person orpersons who m.snege the i o ~
this2persone defectfyresponsble forgathering the mformation, the information submortedis to the best of my knowledge endbeliet, true, accurete. anJ 'n
'I Cm Cware that there are significant penettoes for submotting false information. includong the possobiloty of fine and omprisonment for knowing vo? st v
y 4. N A M E er OF FICI A L TITLE f t)tir or pede rs is PH ON E N o f dtra rode %
11 ' H. B. Tucker, Vice President l .* ; Huclear Production Department (704) 373-4531
,ts o c. soo n o. o Ara seonso l, r W .- Qg /& $ f 1- me-1 P A G E .1 O F 4 EPA Form 3510 2C. .(Rev. 2 85.) .-.. - -...-. . . . _ . - . - . , - . . _ . . _ , ._.-- . . . - , . - . . . . . . - . - , _ _ _ _ _ _ . ,