ML19260A719
| ML19260A719 | |
| Person / Time | |
|---|---|
| Site: | Midland |
| Issue date: | 11/29/1979 |
| From: | Howell S CONSUMERS ENERGY CO. (FORMERLY CONSUMERS POWER CO.) |
| To: | Sells D Office of Nuclear Reactor Regulation |
| Shared Package | |
| ML19260A720 | List: |
| References | |
| HOWE-300-79, NUDOCS 7912030155 | |
| Download: ML19260A719 (100) | |
Text
Stephen H. Howell m
Senior Vice Presuient General offices: 1945 West Parnall Road, Jackson. Michigan 49201 * (517) 788 4 453 80E0113 RFG 1179-4 HOWE 300-79 November 29, 1979 Mr Donald E Sells, Acting Chief Environmental Projects Branch 2 D; vision of Site Safety & Environmental Analysis US Nuclear Regulatory Commission Washington, DC 20555 MIDLAND PROJECT - DOCKET NO 50-329, 50-330 -
ENVIRONMENTAL REPORT (OLS) -
REQUEST FOR ADDITIONAL INFORMATION -
FILE:
0505.5 - UFI:
1141-71*20*02*03 r
1141-72*10*14 - SERIAL:
7959 In partial response to your request for additional information dated October 11, 1978, enclosed are six copies each of the requested documents listed below:
State of Michigan, Department of Natural Resources, Water Resources Commission, Discharge Permit Application, Consumers Power Company revised submittal of June 1, 1979.
National Pollutant Discharge Elimination System Application for Permit To Discharge Wastewater, Standard Form C - Manufacturing and Co-eu iol, Consumers Power Company revised submittal of June 1, 1979.
Additionally, enclosed for your information are six copies of the report:
Report of a Preliminary Archaeological Survey of a Transmission Right of Wav.From the Midland Plant to the Tittabawassee Substation for Consumers
_Power Company, July 1979, Report Prepared by Museum of Anthropology, University of Michigan.
"m A
'{iTT -"
.y.
M Ccro l E.s 7912030/ 6
//I oc1179-0419a-46 1456 048
9*
t i CONSUMERS POWER COI'PANY MIDLAND PLANT UNITS 1 & 2 FEDERAL STANDARD FORM C APPLICATION FOR PERMIT TO DISCHARGE WASTEWATER MAY 16, 1978 SUPPLEMENT AMEULMENT NO 1 NOVDBER 22, 1978 l1 MSIGrEIT NO 2 JUNE 1, 1979 l2 AMENEMENT 2 JUNE 1, 1979 1456 049
OSB No. !$5 ~R0iOO FOR ACLNCY USE i
NATIONAL POLLUTANT OlSCHARGE ELIMINATION SYSTEM APPLICATION FOR PERMIT TO DISCHARGE WASTEWATER STANDARD FORM C - MANUFACTURING AND COMMERCIAL SECTION 1. APPLICANT AND FACILITY DESCRIPTION Unless otherwise specified on this form allitems are to be completed. If are item is not applicanse Indicate 'N A.*
ACOITIONAL INSTRUCTIONS FOR SELECTED ITEMS APPEAR IN SEPARATE INSTRUCTION BOOKLET AS INDICATEO. REFER TO BOOKLET BEFORE FILLING OUT THESE ITEMS.
Please Print or Type Consumers Power Compan'/
1.
Lagal Name of Applicant tog (see instructions) 2.
Malling Address of Appilcant
**j"'N,**' Stit 212 West Michiean Avenue Nm
- ior, Jackson City
.som.
State
'some Mihigan M201 zio Code 1ozd 3.
Applicant's Authorized Agent (see instructions)
P c Hit +1e Name and Title 103a Director of Environmental Activities Department loI45 West Parnall Fnad Numcor & Street Address 103b Jackson City to3e Michigan State to34
!&9201 Zip Code 103e 517 788-1930 Telephone 103f Area NumOer 4.
Previous Application epoe if a previous application for a National or FeGeral disCnarge per-mit has Deen made, give the date E
of application. Use numeric designation for date.
104 YR MO CAY l Certify that I am famillar with the information CCntained in this application and that to the best of my knowledge and belief such information ls true complete, and accurate.
Stephen H Howell Senior Vice President of Projects, io,,
Printed Name of Person Signing Engineering and Construction 70 6 1 WL W4
& - /- 77 *" "
^*
gnature of Applicant or Autnorized Agent
~~
Oate Application Signed 13 U.S.C Section 1001provides that:
Whoever. in any matter wsthin thejurisJiction of any dcpartment or agency of the United States knowingly and wilfully falsifies, conceals or covers up by any inck. scheme, or device a materialfact, or makes any false. fictitious or frcudulent statement or representation. or makes or uses any false writmt or Jocument kuomng same to contain any false. fictitwus or f:raudulent statement or entry. shall be fined not more than 310.000 or impnsoned not more than fire years. or both.
FOR AGCtaCY USE OFF f CE:
EPA Region Nummer Received -
YR MO DAY C ate 1456 050 m. mo_
_m
=
FOR AGENCY USE a
NATIONAL POLLUTANT DISCHARGE ELIMINATION SYSTEM APPLICATION FOR PERMIT TO DISCHARGE WASTEWATER
.. s STANDARD FORM C - MANUFACTURING AND COMMERCIAL SECTION l. APPLICANT AND FACILITY DESCRIPTION Unless otherwise specified on this form all items are to be completed. If are item is not applicaole Indicate 'N A.'
A000TIONAL INSTRUCTIONS FOR SELECTED ITEMS APPEAR IN SEPARATE INSTRUCTION BCCKLET AS INDICATED. REFER TO BOOKLET BEFORE FILLING OUT THESE ITEMS.
Please Print or Type 1.
Legal Name of Applicant 101 (see instructions) 2.
Malting Address of Applicant (see instructions)
Number & Street 102a City 102b State 102c Zip Code
.1024 3.
Appt6 cant's Authorized Agent (sue instructions)
Name and Title 1024 Number & Street Address 103b City 103c 5 tate 1034 Zfo Code 103e Teleonone 103f Area Nu mber 4.
Previous Application Code if a Jrevious application for a National or Federal discnar9e per.
mit has noen made, give the date of application. Use numeric designation for date.
104 YR MO OAY I certify that I am famillar wfth the information contained in this appilcation and that to the best of my knowledge and Delief sucn information is true, complete, and acc Jrate.
102e Printed Name of Person Signing Title YR MO DAY 102f
^'
Signature of Applicant or Autnorised Agent Cate Application Signed 18 U.S.C Section 1001 provides that.-
Whoe:er, in any matter within thejurisdiction ofany department or agency of the United States knowingly and will:dly falsifes, conceals or covers up by any inck. scheme, or device a materialfact or makes any false. Bctitious tv frcudulent statement or representation. or makes or uses any false writmg or document knousng same to contam any false, fictatious or fraudulent statement or entry, shall be fincJ no more than
$10.000 or impnsoned not more risan fire years, or both.
FOR AGCNCY USE OFFICE:
EPA Region Numtwr Received YR MO DAY State
"# 3 P"U#*
E P A Form 7350.23 C-73) 1456 051
4
~
Passaity/ Activity (see instructions)
FOR AGEPwGY OSE s.
c.. ine name, ownmnio, and 7
pavsicas location of tne plant or oiner operating racuity wnere di, e
cnargo(s) does or wtle occur, Consumers Power Company Narne tosa Midland Nuclear Plant Ownersnio (Pubiic Private or sotn Pubiac and Privatel tash O PUB
@ PRV O ePP Cneck block if Federal Facility 105C O FED and give GSA Inventory Control Number 105d Location 3500 East Miner Road sireet a Number iose Midland City
- ios, Midland County go,,
Michigan state i.3, Generation of Electrical Energy and Process Steam s.
Nature of eusiness state ene tosa nature of tne DLllness Conducted at tne plant or operatang faClilty, lo4D AGENCY USE 7.
Facility intake Water (see inst ruc-tions) indicate water intawe volume per day by sources. Estimate average volume per day in enousand ganors per d:y.
1 Municipat or private water system to7a anousand gations per day 2l!
(Tittabawassee River) 28,000 inoo,,nd,anons,e, d,y surrace water toro 0
croundwater to7e
,n o,,,,,,,,,,n,,,,,, y 13s740 otne,'
se76 inousand,3,,onspe,da,
41.000 tnouund gaisons per day Total item 7 1J7e ol Stner.N' e"c <*yln*e's*Er'c'..*
Precipitation: 20h0 tho': sand callons ner day fallin;: on o
t o 7, cooling pond and storm water. collection areas (based On average annual rainfaH).
s.
Faculty water Use Estimate avera,e voeume per day in enouund Dow Chemical Co 11700 thousand gallons per day as feed-ganons per day for tne fonowing 8
types of water usage at the f aculty.
water to prOCCSS Steam evaporators.
(see instructions) 20.000 l
Noncontact cooHng water 1o8a in,,,,,,,non,,e, a,y 11.810 (See item 12) 2l sone, veed water too.
tnouund ganons per day i
Precess water (including contact g
cooseng water) 1.Se tnouund gallons per day
$anitary water 9.old tnousand gallons per day 50 oin.,*
iese k1'900 2l Tot 4. item a ioef
- tr iner re di cnarges to Precipitation included in item 107d which is discharged to
,otner, specity, togg ne:::alnGer 01 Feel liar,lon I h a La cool-Storm GralnS.13 included in ltem Oda.
ing nd and if tnere is Sanitary' water use, give
,no n.meer o, oeoose s.,,e.
, o,,,
peon.e s.,v..
1456 052 m
E P A Form 7550 23 (7.73)
AMENDMiCT2 2 JUHE 1, 1979
FORM Ar*PROVD
~
QMB No. U8-30100 l rom AGENcv ust l s.
An Fusney Olsenaries ano einw t.assena Numsw ane cistnerge <see instructions) Voeurne Soecify 'ne numoet of oisenarne coints ano tne vosume of water otscnargea or sost from sne facielty accoroing to tne categones oesow. Escre are 3,,,,,
y,g y,,,,,, y,,,
averso voeume ser say 1 thousame cascnarge or Olsenargeo, gassent ser any.
c,,n,y Q
g 3
surface Water toSet 1csaa 14 Sanstary wastewater transport 103t&
.10182 system 2
50 f' ]
Storm water transoort system
. 199e5 10$eJt i)l I :, l *,,, ',
Camoened sanitary and storm 0
0 UJb l
' l,,,
[ '
i
'i.
,l#
w;.
'l ',j,
4 water trandort system
'10948 1034T l
a i
n
~
0 DL 0
Sur..ca Arneaunament wtta no
.101e2' s
effluent
.10$at 12 't Uncergroung percosation ISSf?
101ff West insection 10Sgt 1091 1 0
0 ( s e * ** es *' 2 )
Weste accootance firm
- 1999e, 1994t2 18'000 2l Evaporation toSIF-10942 Capsumodon 109W
,10912 2
11'7CO Ctner*
T Ostt-losser wacairy casenarges ana,oeurne 6
?
W 41+900 rr ;
totas item s.
tosit-reser
.it enore are essenerges to otner.'
Ocv Chemical Cc prccess stea= and creeess ste u avgrera-ter 1::1cvdown
' +
- 10. Permets. n censes ane Aeoelsations i st ass esisting, concing or conses permits, licensee ano acoHcations rotated to cisa sarges from tfiis raculty (see instructionst.
Cate Cate Cate Emoiration Tm of %q issuing Agency For Agency Use 10 P8umper 8'iled issued Oenied Cate M Ucense V 4/MC/CA YR/MC/C A 1 v4/MO/CA Y4 MO/CA i
titr (a)
I (3n m(
ter.
(
tat j
(et
)
(n j
(gr.
l (ng j
- l C C" S *O.U.c*" $ CDrece_ o, II 6c/1/11 i ~g/ig/icl l
I l
l n-1*
AEC i
^
i L
a i
i i
l l
l l
l (Amended 73/5/23)l l
2.
[
lCCC8tTlCO'enm-=_cej60/_/13 l72/12/Ml I
1 e.
a.
!T ~ '< ~L
' ~.l l
l (A= ended 73/5/23)l l
l.: m m, l ' " ; l upe
- - l l 77/8/31 l l
l r,leeEn 2.
p r-
...i i
~~ <
I '
'l (Continu4d in Item il2. Pare II M l
l
- 11. Mass ane crewengs Attacn asl recuiree maos anc orawngs tr tne cacx of tfus anonication.ases instructionst (3ee at* ached 71g*lres A, 3, In C)
- 12. Aealttenes informaden 11 3 iter'9 Nurneer i nf'"r**" af Mn 2
3 l 11.700.000 rpd frem Cow to tracess stem evatorators,- 112,000 gpd rake up to condensate feedvater and main cteam systers.
9 I No preepera*d-aa' etal cleanin: is currentiv clanned.
Shculi
! netal cleanine be recuired in-in: the life cf the t' a-
- it aculd i involve the shitment of chemicals to the site by ank tr ck and Il rencval of all stent cleanine solutions snd rinses frc: the site t.= ape = mo-a a.m ey : ant trucx to an apprevec waste acceptance firm.
s
..,s......
14 5 6 0 5 3 = 1,1979 u-m 2
- tes 10 - centinued U***
U***
U***
D
- tic"
- yp of Permit Jssuing Agency Tor Agency Use D:Tumber Filed
- ssued
- enied Oate U /?O/*A G/w3/SA U /?C /"A U /w]/DA 4
S$ @ b OIE-05Ei$nSEhit69-23-2 69/7/2 69/8/5 72/12/31 C
a C n-Drads ien Fe-1:60-23-2 72/8/22 73/1/18 76/12/31 c ?r.a-fs rs oM s92es 5.
6.
53C CN*-Ei*!:r FP-55 69/5/29 69/6/25 Constructi:n I(A=ende: 69/6/:.3 :
7.
%7c 95dH-S iSC 1h26 70/6/9 70/10/15 ra1 a,stevater (A=endet 70/7/15 s
lPIPPApproval 7h/1/23 74/8/30 S.
m?c I
9.
_%7C
)
NPDES Permit 78/3/1 nazer sus :;7 10.
L 7.C c. -- d "i c st i c e.
71/1/12 71/3/12 g 4C
' dater Qual:ty
~~
e
,*Js4.o*4--
71/2/g@
12.
MDE I@E.'s5'?!f5 3) 77/1/17 l
13.
MDn Dredge Per=1-69-8-2L 69/8/5 77/12/31 (F. wised Dredge 69-8-2hA 77/5/2h 77/12/31
.=.
14
'r' W Per=ission 76/3/18 76/h/3,
- <**schstge t
ndl ster: atbr e
Micane creer an,d 69/7,f,
- 9/7/ _,.
15.
c 2 card
- 3. - 4. -.
construe:1cn l
16.
%u gg=ird
=g u < -
' E.eEFI?si, h68 l
73/1/22, so Fer=1;
@r HN-a 35$ks[55k l787L278 l77/12/.9i C
7.
l
?'# 108 l
l l
l
,--. sr -
- f. '.' e ' s s <.*
e..
4.0 l ! < 3
'r; f :.; *_4
- a..
"?m'* *~**...t.
1
- 3. C ard. C f l l00cs*,000
{c.,.g 4,.,,.
.,,,,. 9, l
.~.
M,i C ind...
l Crier.30.0.J l.1.~//6 \\ 7. k/ e /'C l
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~
Scisd. f
- struct l
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1456 054
4 4
FORM APPROVED CMB No. H:-R0100 FOR AGENCY USE STANDARD FORM C-MANUFACTURING AND COMMERCIAL SECTIONII. BASIC DISCHARGE DESCRIPTION t
Corno.ete tnis section for eacn aescnarse inoicated an Sec*.lon I. Item 9. tMet is to surface waters Tnes enesuces cancnarges to munecioas sewerage systems in wn.cn tne wastewater coes not go inraugn a treatment worms prior to Deing oiscnarged to surface waters Cascnarges to wesas must be descreDed wnere there are asso nascnarges to surf ace waters from tnis f acility. SEPAR ATE DESCRIPTIONS OF EACH OISCHARGE ARE REQUIRED EVEN IF SEVER AL. DISCHARGES ORIG 8. GATE IN THE SAME FACiL37Y All values for an existing sisenarge snould De repre=
sentateve of the tweeve provsoua montne of operation. If inst is a proposed descnarge. wasues snould reflect Dest enganeering estimates.
ADO:TIONAL. INSTRUCTICNS FOR SELECTED ITEMS APPEAR IN SEFARATE INSTRUCTION SCOKLET AS INQlCATED. REFER TO UCOKLET BEFORE Fil.WNQ CUT THESE ITEMS.
1.
Dessaarge Sersaa No.and Name
~ 'oTa' QQL.
a
- a. cescaar,e series No.
(se. enstructionsi
~,
Cc=bined Plar.t Discharge ca.. nun. of aiunuge, if any.
(see 6nstructionst s
- c. F=ce.s oisans,e sena. N If prevsous oct Ast aoot4Catson N
was mece for snis desenarge (see tota 11sen 4. Section O. orovide prov>
ous dJacharge sersas numoor.
2.
ovan.rg. Oeeraung oaws
- a. Disenarge Segan Data iftne aiscnu,a eeunoea oei w.s in 3,1 ooeration.,ve tne aate (w.cnin 202.
Dest estimate) the oisenarge YR MO og negan.
D D
oin u ' \\!
i
!ii [ j' ll lh h'- U E
a
_r u o s.nar,e to.e,m oate
.f tne
. o >
65Cnarge nas'never occurred Dut
] $
is planned for some future date.
2024 gewe the care (witnen test esth YR MO mate) tne essenarge weta megen.
- c. Dissnarge to End Date if dis.
cnarge es schecuied to De descork N
tinued witnen tne next 5 years.
202e gwe the date (wetnan cost esti.
YR MC
- atet tne cisenarge well end.
3.
Engineering Report Availante Cnecas if an enginesting recort is arattaDee to rev ewing agency upon request. (see anstructions) 203 C
4 Olscnstge t.asatsen Nametne positical Doundaries watnin wneen Agency use the point of desenarge is located.
Michigan State
'204e 20A4 County toda 204e
>!ii' 5'Ud 204#
(if sootscansel C:tv or Town 1044 S.
Olsenar,e Pesnt cessnetlen Otscnarge es anto (cneck oner, tsee instructions)
Strsam tincruces cittnese arroyos.
and other intermettent watercourses 3 2DSa 35TR c-une ctKE l
Ocean COCC 1
Mun*cipas sanitary wastewater Teansoort System OMTs Munscroat Comeined Sanitary and Storm Transoort System CMCS 111 EP A Form 7550.23 (7.73)
This acerfort contanns 9 su. :es.
a I
s i
OsSCHARGE SER8 A4. fduMSCR Col FOR AGENCY USE Munacasal Storm Wat.r Transoort System CSTS W.ss (ini.ctioni C WEl.
Ot n.r COTH I
if 'other*.s checked. specify 2ess 6.
Ostenary. P.4nt.= Lat/Lang civ.
(n. precas. location or tn. goant
- o. enscnarg. to tn. n.arest s.cona.
k3 cza
_3f,,,u,u 13.cc Laur,a.
ans.
Longnva.
seen
% oca U utN
- <ac 7.
Ode. marg. R.c.tv6ng Wate? Nam.
Nam. in..a.
av at ta. po.nt zota 71 33.avassee River et oisenar... instrucuens
,s an Anneyuw war a**cv uw
.tf to. destnerg. es tnrougn an out.
Mae i ulaer i.u.i I
3o3.
fait tnat estenas o.yo-a tn.snor 207s 287 un. or is o.so. tn. m.an io g
l
....e 1.n com...t. t.,n e.
cresner, o.unun
- t-~
0
- a. cianup oistanse er.m sner.
- osa rt 6 o.sau,.o..o s.. Wewe (depende'nt upon river vater surface elevatien}
su ren.
' mosis.
ft 9.
oisenary Typ. ane occurr nce
- a. Tys..f Dissaart. Cnecu
.n.tnu tn. oinnu,..s e.n.
- osa C (coni coaunuous Discharge '.ype and occurrence deperds en
""""',U,*,'s*'"*"'
O cino intum.iteat Tittabavassee River flow. The estimated st c 1
ncnthly average diccharge flowrates are:
A Dessnarg. occurrene. Days per ween Enter tn. av. rag. num.
2ost Days per. a her of days p.r weeis (curin, (Average, c,.s) puiacs av assenupi sn.: ass.
J F M A
M J
J A S 0 :I D 2) lo 13 41 79 36 15 5 2 h 3 h 6
- c. oescauw es. mne..-ventn.
If tnes o scnarg. normany 200s CJAN Orts CuAR OAast During =cnths of March, April oonatu t tnu.ntermittenuv.
oe continuousayl on lesa (Ran CMAY CJuN OJut caua and Ma."r
- the discharge is most a y.ac.uound pases (sucaucens likely to be Continuous. For 1
sauteo.no ear route,. ma nw.
Osta O oct C Nov Ccec
+he remainia8 =0nths, the' dis-
- n. aces. cn.cli (n. montns du,.
ice tne y.u.a.n in. eise""
charge may be intermittent. At any given instant is operat,ng. (sa. instructsons the blevdown flow vill be zero or between ; an3 r-2l Ca*S '"' 'd** io.no ir mater-220 ers. For a description of the metaods used mittent is en.cuea in nem u.
oin-wis.. orocua to n.m :2.
to ectablish the allovable blevdown flovrate see 1
Exhibit V Appendices 3 and C of the " Discharge io.,ina-utent cis nu,. auaniny ta,e tn e -.r.
....m...e _
,,o
-,A
.,_s.n.
..ons -r.is.n.r
_rrenc Permit Applic at ion. "
cnaro. occurrenc..n tnous.nas of Sa68anh
... Interm.t,.n, ana,e.
...n
.n..r
..n.y i n.f m.t,. n,.i..n.r,..,.
t..n
-e..y
.n_,_rs -may
~rno..., stat.,n....ra,.
n
.....,, n.
atscnare..s oceratins i456 056 m.n.erm.t.e nt....n a r,.
Pro.uency Stat. tn. avera9 21la
.m.assenarge occurrences per day numou os esenara. occur.
t.nces per oay durmg aays wnen aianarg.ng.
- 42. Mamemum ri.. eere.q
- 0..tn.
tema o.,. w m wn.cn ene mas.nium f 25*
From _ Marc *"10 _Jn=0
' low of an.s a.sse:ar, occurs mon.n m ntn ena r= ns:-:s a m g
AME:lDME:IT 2 JU:E 1,1979
g FcR.*.! APPROVED s
001 OMB.No. US R0100 FOR AGENCY VSE
,e aEso'iion o$u'.ty S e preposed entererise is a tvc = it nuclean pcver 2:sa narr producarig this alscnarge.(seg inat,ucuans, plant.
Each unit censists of a pressuriced water re-acter, a turbine generatcr, and assceiated aux
'd d es.
d The facility has a total ec=bined nacerlate rating of 1,360 MWe plus k x 105 lb/hr of process stess. ":te electricity will be supplied to the applicant's electri-cal distribution systes a.'.i the process steam vill be supplied to The Dev Chemical Cc=pany.
2 This discharge vill consist of apprevd-ately 11.7 FDD (annual average) cccling pend b1cvdevn and 0.1 MGD (annual averase) of treated lov volu=e vastes.
14 Activity caustry Disenarge For each SIC Coce wnich cascriDes the activity Causing this discharge, suppey tRe tyDe and maatmum arnount of either the raw matcrial Consumed (Item 144) er tne OrcGuCt produced (item 140) in tne unsts specified in Taste t of the testruc-Uon Gooulet. For sic Coces not listed in Taose 8, use raw matereal or production units nC rmally used for measuring procuction.(see
&#sstructiofis) 4.
Raw Matersals Masamum Unit Sharma Olscharges s:C Coa.
Name Amountfoav see Taoie o (senal numoer) 2144-(1)
L
'21 i
13) ten a
(S)
Net kncvn l
l l
l l
l l
1
- h. Proeucts Maximum Unit Shared cisenarges sic Code nam.
Amount / Cay (See Taose O (Serial Numcert 2144 01 (2) sin a
ta)
- 51 i
Ele l
I lse ctr:.c.:ver I 1.e4 i
49,.
rices w~
2061 lStes: Supply l
07 2 l :-2 l
- ene 1
I I
I I
I I
i 1456 057 EP A Farm 7550 23 U.73)
U-3 AIE.IDENT 2 JUHE 1, 1979
o olSCMARGE SERI A4. NUM8ER 001 FOR AGENCY 1.SE is, wate Amatement EnnetU*w*a eS*o* ate,"ent CCndenser ?Oolin: Vater vill be ??Oir0uleted in zisa Narratives OraCtlCes usea on Inis alsenerge witn a orief narratw (see the ecolin: nendt b1:vdovn vill be discharOed fres -he instructions:
ecclest toint in the syster.
? heck 91eri_stic-cf acn-denser and service vater v411 et re st'lt 4-a se wrible discharme of residual chlorine due to
- a 4 4~u: of 3 days residence 1: the eccling pend. '4astes havin extreme s.
u pH values vill be ad*usted to within the ranze of 6.5 to 9 5 prior to discharge. Lev volu=e vastes havin hizh
- ?
-. suspended solids eencentrations vill be routed to ecolin6 pend for settling prior to discharge. Lov volu=e vastes
- n... vnich may be centa=1:ated by oil cr grease vill be processed
$ ~-
through oil M-'e a n
?""""
"' " i t6 wasta Abstement Ceaes 215>
(1)
(2)
(3)
,r,, U:GS RECYC1
, removal equid-t.mns tne coaes sistea in vaoia gg3gg 11 of the lastruction soomiet.
(4)
(5)
(6)
- =,ent prior to assence the waste amatement qgy 3e- -
---_y x,,
(s)
(3) processes for this oisenarge in (7)
EC ge.
tne oraer in wnica tney occur T
(111 PN#
(12)
If possiDie-(10)
(15)
(13)
(14)
(16)
(17)
(18)
(19)
(20)
(21)
(22)
(23)
(24) m)._
1456 059 u
m
..r- ~..:w.n,
FORM APPROVED e
Ol5C)4ARGE SERI AL. NUMeER ogs No.153-R0100 001 FOR AGre'4CY USE 8
ts, wastewater charactersstics I
Chects the Dom Desado eacn constituent wnica is cresent an the ef fluent (cascnarge water). This determenation is to be based on actual analysts Q >(
et Dost estimate.tsee instructions)
Co y
ae f
3 2
.L oo Parameter x
Parameter x
- c
$4 c 216 1:
216.
=
d ~~ 3
~ v o.to a.
a.
L L
.d,4e4 ou1 Color Copper a.= v pa jdj od 00080 X
01042 y
Ammonia tron "32 0
00610 X
01045 X
E ~~
op Organmc mtrogen 1
Lead "5
C3 0 00605 1
01051 (b)
X 4d N
wvo C
O Nitrate Magnestum l
0 > 0 00620 twi y
00927 (b1 IX 3Em 4.r4 Yo U
~*
Nitrite Manganese y
00615 01055 (a)
X
-c
m 0 m o
Phosphorus Mercury amo k
00665 I
71900 (b) v 5 +3
>> : o o
Sulfate Molybdenum
-cL
.c 00945 X
01062 C 'O
_2 C 2 Sulfide Nickel
- ' C 00745
/qi y
01067 X
$da N
Sulfit.
- D$
00740 X
01147 o
~
' gr o b a.
m Bromide Silver a.r4 71870 01077 (b)
X 0
9.'.
O
.J
,g g Chloride Potasnum
- 0
>o
~f " d 4o 00940 X
00937 fwi y
Cyanide Sodium T$$
0 00720 (a)
X 00929 X
va o 3
C.C
. 2 m.
g+3 Fluoride Thallium x
Jr 00951 01059 o
t e
e Aluminum l
Titamum
,0 d
4 **4 01105 (a) ly 01152 3*3 Antimony i
Tin i
n j ~g, 3.s f 01097 l
01102 l
4 o a to Arsensc Zinc hO
.h o h 01002 01092 X
MC :
H C,c r4 o 2 m **
o
"'3 Beryllium Algicides
- O 2
31012 (b)
X 74051 X-0 ~
0
<t>
to o t.r4 o
- r4 0
0 Barium Chlortnated organic compounds
- e $, U M
01007 (a)
X 74052 (c)
X o
e h&M Boron P:sucides*
3
~MM d
0102 y
74053 3 d _ *d h D +'
Cadmium Oil and grease i
hdC J.c,4 U
d*
01027 (b)
X 00550 ly x 2, a s oo o <t) e Calcium Phenols fa O m% - 5 s (H 2.H 00916 (b)
X 32730 (b)
X
~0 e
o s 09 d Cobalt Surfactants l
L > L 2 3~"j@@ay 01037 38260 ly 8
G "
r4 43 2 ~d ~" "$ $.@
Chromir Chionne 1
~
01034 X
$0060 (c)IX Fecal coliform bactern Radioacuvity*
l Y
3s M, g 74055 74050 l7 3y
- s.
7
[... O o,o
.f %j
- Specify substances, compounds and/or elements :n item 26.
.J
- o Pesticides (insecticides, funcie: des. and roden.icides) must be reported in terms on' the acceptable common
~ " U4 oe names spectsied in Acceptacte Common Namer and Csemical Names for rne Incredient Statement on
$ E ~ ~ M 43 o Pesticade Labels. 2nd Edition. Environmenul Protection Acency. Wasiunuton. D.C. 20:50. J une 1972, as 3 V t 8ej required by subsection 162.7(b) et the Regulations for the Entorcement at ths FederalInsestic:dc.
20
- ,c o
Fungicide, and Rouentic:de Act.
5I3 g r.ra p
, =
w, w
1456 059 u.s m.-. m n.m P00R ORB Ay
t 4
OISCHARGE SE Al AL NUMBER OCl FOR AGENCY USE
- 17. Descristien of Intate ane DisCnarse For eaCn of the parameters insted Delow. enter in the approorlate Don the value or code letter answer Called for.(see instructions)
In sod 4 tion, enter tne Garameter name and Code and all required values for any of tne following parameters if tney were CneCited in item 16 ammo.144. Cyanede. aluminum, arsensC. Dery'llum. Cadmium. Chromium. CoGDet. lead, mercury, naChel, seteneum, ainC. Onenois, oal and grease, and Cnlorine tresiduao.
Enluent influent m
P y
Fi!
-i ~ji m ti re 3
re EE E
>30
>33<
[
s!"
Paramercr and Code 3
h,353
'S '2hl"h_
!i 5 $.
E N
!_3"3k_b
_21N "3
= x o-c
.x v
E E =,
3: t a.,
P.
's o.17_ 3
.= 17_
77 E3 s
x.
x o
=-
o 4
o myc 42e c
rowa<
sow =
w<
=<
a I
(1)
(2)
(3)
(4)
(5).
(6)
(7)
(8)
Flow
- 2l m pa.hr MGD 30.0 0.141 ! 11.8 3.2 142.0 50050 See Isen 26 pH" ' '
1l 8.0 95 6.5 95 00400 Temperature (wmter) i 3
I3 74028 Tempersture (summer)
- F 60 (a) 98 67 103 74027 BioChenues10xygen Demand t
(BO D 5-day) l mg/l (b)
(b) l (c)
(c)
(c) 00310 l
Chemical Oxygen Demand (COD) l mg/l (D)
(D)
(C)
(C)
(C) 00340 Total Suspended (nonfilterable)
Solids 1l
- [30 15 CO (d)
(d) 100 0
Specific Conductance i
micromhos/cm at 25* C l I 00095 610 150 l
TCO 3400 Settlesbie Matter (rendue) ml/l I
00545 (b) 41
' (d)
(i)
(d)
(Continued in Ites 26) 80ther discharges shanng :ntske flow (scrisi numbers).(see instrucuens) 0 0
(1) Se average tempersture is 4807 and rsnges frc= 2h F to 66 7.
(b) :Ic k.ncvn.
'c) "nable to predict.
(d) 'Jnable to predict, settling vill Occur in the cccling pend.
1456 060 E P A F., 7350 23 (7.;;)
IId AMF"IDMEIT 2 JE 1, UW
f FORht APPROVED OMB No.158-R0lC0 OISCH ARCE SERIAL. NUMBER 001 FOR AGENCY '8$E I
l
- 17. (Cont'd.)
Innuent (ng/1)l Efnuent (ng/1) l 4
e i
- I J Ii esy ;
a 2
s y
i a
>3=
> 3 =s u 1,
y Parameter and Code s.g
=,,.
o S<
4 s,,s.ed 1A i.i <,.
=e e
=s
_e.
=~s x
z
=;
2 mm os
-=
=_
5-d' <., !,
= o - 3. 4
- x1
= a. 0i a
- m. a =s p=
aE-
=3 a'
e o
- 2O
=
2Cuc<
33 2Cw w<
n<
w i
(1)
C)
(3)
(4)
(5)
(6)
(7)
(8)
A==enia 00610 0.1 f
1.67 0.04 20.4 l 3er7111um 01012 (0.003 (a)
<0.004 (a)
~
2 Cad =ium 01027 (n.onh I
(a)
(O.OCh (a)
Chremium 0103h (0.006 I
(a)
(o.ook (a)
Nickel 01067 (0.01 l
(a)
<n.n2 (a) 1 Ccener 010h2 0.008' O.02
<0.01 l
l (Continued in Ite 26)!
l l
l (a) Unable to predict. This =aterial has been detected in the plant's pr0 posed cooling water supply (Tittabavassee River), and therefore expected to be present in the
=
ec=bined plant discharge.
mm ts. Mant Contraes check if the foi-27sc lowing plant controis are availaDie for tnts disc!large.
Alternate power source for major O APs pumpene facility.
. =
Alarm of eme*genCY Drocedure for 3 AL.M power or equipment failure Complete item 19 ff discnarge is from Cocaing and/or steam water generation and water treatment additives are used.
- 19. Water Treatment Additives if the discflarge is treated watn any cor>
ditioner, inneDator, of aJgscade, answer the followmg
- a. Name of Material (s) 2fSa NOUO
- b. Name and address of manu.
g facturer 219th c.
Quantity (pounds 440e4 Der 2198 million gallons of water treated).
1456 061 u'
m ae-n,..n a.n, teEnDMENT 2 JUE 1,1979
t s
DISCHARGE SERI AL. NUMBER 001
Q R AGENCY WSE e
/
- b
- d. Cnem6 cal composition of these 213e adatt'ves (see instructions).
Comosets items 20 25 If tnere is a enormas disenarse (e.o., associated witn a steam and/or power generation paant, steet melt, petroleum refinery, or any otner manufactueing process) and one total discnarge flow is lo m4340s gations per day or more. (see enstructions) n.-
to. Thermas Desenarge Source Checis 220-the acoroortate item (s) inalcating tne source of the disenarge. (see Instructions)
Boiler Blowdown
'],
CBLSO Soner Cnemical Ceaning C SCCt.
Aan Pond Cverflow
[$.}
CAPCF Sotier Water Treatment - Evapora-O EPSD
$.4 tor Stowcown Cie or Coal Fired Piants - Effluent CoCFP
.y froen Air Postution Control Cevices Concense Coosing Water
,j
@COND Cooding Tower Stowdown O CTSO Manufacturing Process
'- Q
- C MPPR Cther i
CoTHR r
y
- 21. Otsanarge/Receeving Water Temper.
ature Difference Give the mamimum temperature elfference between tne cisenarge anc receeving waters for surnmer and wtnter coerating conditions.
('**'""'
30 op, Sumener 221e hO
'F.
Winter 221b
- 22. 04senarge Temperature, Mate of Change per Hour 222-
'F./ neur (See hem M )
Give the maximum poss4We rate of temperature cnange per nour of discharge under ocerating con-altions. (see lastructions)
- 23. Water Temperature. Percentile Report (Frequency of Qecurrence) en the tante netow enter the te+noerature wnicn is exceeced 10%
of the year,5% of the year 1% of the year and not at alt (marimum yearry temperature). (see instructions)
Freauency of occurrence 10%
1 5%
i 1%
i varsmum
~ ~" O' l
"'CO'l 3-oel Q~om a.
Intake Water Temperature gns
,= p-74
- * ~ "
(Suotect to natural enanges)
- 97o, 9 Co, 1;go.g ;gy, g
t.
Cischarge Water Temperature 222a
<r 24 water antame veiocity 224
- eet/sec.
Iwe snitructions 2s. astenu.n Time ci e ine i.n,tn ot 22s 3 h-tee See M re anaeed u ne E he d.
?
urne, in minutes, from start or
.. t t.m.... r. r. s... -.,.
os cocieng water. (see instructions) 300R ORGINAL 1456 062 me.m,,,.,, g.,,,
"-8
f n
~
FORM APPROVED CMB No.138-R0100 ciscNARGE SERI AL. NuMaER PCM AGENCY USS j w
j.-
- s. Aseseeass envermauea 20s-itam I
informacon 16 lAlricides?h05'.
lShouldalgaecrevthevercreatenuisanceconditiensintheecclin l pend, sodius hytechicrite vculd be used as an algicide. See chlorine 50060 for further discussion, item 16, p II-5 I
16 Radicactivity Th050 The felleving radienuclides, in addition to those already present in the Tittabavassee River, =st be present in the discharre. All radionuclides are estimated to be less than 0.035 cf 10 CFR 20 li=its entering the river except tritius which is estimated to be 0.2% of 10 CFR 20 limits.
3r-83 Fe-55 Te-12cn I-130 Fe-Sc Te-127=
I-131 Cc 48 Te-12c
lI-132 C0-60 Te-131s lI-133 Sr-80 Te-132=
I-13h Sr c0 Ba-lho l -135 Sr-91 Ce-141 lRb-86 Y-91 Ce-lh3 1 Cs-13h Y c3 Ce-1kh 1
Cs-136 Zr c5 pr-lit 1 Cs-137 7b c5 7r-21c Cr-51 Mc co Ar-116 Mn-Sh 9u-101 01 p.,-i n4 17 l Influent: Untreated !ntake Water-(11 Makeur frc-Tii shavissaa Siger -
2l l
28.0 MGD l
? cipi*,ation falling upcn or roucea oc cae ccc-ng ;cc -
g l
1.99 MG:
l 2-?lant Treated Intake Water:
1 (2) Mid' and ity water for crecesa.use
.125 LUD 2
datestic use -.015 MGD 1456 063 1ederatm use
.*1 son t? A 7.,= 753c-:s a-m AEiLisIT 2 JUE 1,1979
I a
FCP.4 otPPROVED OMB.Va.138-it0100 ctSCHARGE SERI At. NuusER l PCR AGENCY WSE l Col L:
... '. [' ;.
1l e%
- 28. Aseinenas informanen 2=E, item I
incomenon 17 l
.nauent(_-gl.d Effluent (ng/1) w k
? ? l E $
_E $
~EE['
h N35 S 35k E
5 [
Parame:er and Code g
I
! ??Ew
!?? E M.:
-g
'"?
IMa 3 4 U$4 -
cete=
ctUs ya
.M,
- w
==w l
nsi c i %,.
E, i s L 5. 4 2 3 L3 p
5 ~2
?.
e=
i
-a w
a.a m -
m a
o k =,
"2=
=
nouc<
sowc w<
=<
n (1)
C) l (3)
(4)
(5)
(6)
(7)
(8)
I I
lead 01051 0.02 l
l0.04 l<0.01 l
0.17 2
y,reur.,71900 o.001 jo, cog l4.0004 0.02 l
l* I 2ine 010c2 0.022
! 0.05 0.02 0.22 Oil '. Grease 00550 1
2 l1 4
l l
l l
a...
4 4 snven 4 0.005 l l
foi l
foi r,)
1l O.1
) (a)
(a) l (a) l A.luminu= 01105 l0.03 l 0.002 0.05 l
Phencls 32730 0.01 Chlorinated crganic h
f C0= cunds 7h052 Chlor =-'es=avbesult fresshock$hicrinatken l
l (a) fJnable to dater-:ine.
Material is er ected to be tresent in main clant laborater r.
22 Under eterating conditiens the iischarre te-:erature chancas according to metecrelerical cenditien uctuations. and the estimated is0.5F[ hour.
C maximum rossible rate of chance in the discharge te=rers
--a 23 Intake water te=perature equals natural river temperature near the Midland Plant. Eased en daily average river te=peratures for water l7 ears 1976 and 1977. the f0110ving frequency of occurrence can be l calculated as foll:vs:
l 105 55 15 Maxi =um 7
7Q0; Ap?.
. Cv.
--C.
ss ii v.
l I
I Pa Pen M30 :3 g..m II-10 14 56 %2f,1979 AIE:DEIIT 2
FCR4 APPROVED 6
Q*f9 No. 2%20200 ciscuanos sanias.auussa l FOR AGENCY USE i col
[ - t g,t
], q..;
+
r.. \\
ms. Asesa.aas inv.,menen M
item l
informacon lDischarre vater terrersti-. de-.-As ~~c'e-o-
-2
' e a.t iced e
~e ---d 1-d I:stecrclecical ccediticas.
Ass 4 2 ene meeth - fuelin; ried e--
.,eg lunitduri:2 Acril and Ma r
=ad
.~ ele dne dail r 1 r - e r. -...,. -,, -
l conditions at Flint, Michigan "cr water years 1976 and 1977
-he I frequency c' cecur ence 'er discharre vater secterature is ce.lculatei.as Ifollows:
10%
35 15 Maximm l
97 ?
990F 102cy to-cy 1
I I
1 I
I I
I l
l l
1 I
I I
I I
I I
i l
i l
I I
l I
en.e-= tuo-:: (7.. :1 II-il 1456 065
TE VIPER / CURE R!SE AFTER ll.'7A K E > IN F
- c..-.
N k
2 (e h in O
5 y
9 w tn tr1 s
" i 'm I
I I
I i
i t i
?. :$ C f
I I
l l".
- O2 l
2L' 5 -
j p-k + T.
U<D-l l
g < E. g - - - -
l I
8, 1"
5,23- - _-
i n
Z,.*N
=
i
(<
- 0 Z
fe Z
e N,:
% Ae 6 9 >9 C
, m T
4 ::: o v-Y' Wg Y*
'm C,
X 2
I n
m 3
i
- *p g
Q l
LS 9
~
v a
l fa I
h C
2, l
D
-4 l
m
=
'.,)
??
M l
fe lI DTr D
'r]ffBQ6Bf}
l 9.f\\ blnbkk j
i.
k g
me
- R f
=->w
% 7 >O 7" 5 H56 066 n, e
?
e 0
e
FORW APPROVED OMB No.133-R0100 FOR AGENCY USE STANDARD FORM C - MANUFACTJRING AND COMMERCIAL SECTION III. WASTE ABATEMENT REQUIREMENTS & IMPLEMENTATION (CONSTRUCTION) SCHEDULE - :iA This section recutres information on any uncornoisted'lmosomentation scredule wnsen may nave Oc.en imoosed for construction of waste amate-ment factinties. Sucn recuirerrants and imosomentation senedules may nave seen estaotianed Dy local. State,or Federas agencies or my court action. In addition to comoteting trie fostowing items a copy of an officias (mosomentation senedule snould De attactied to this apolocation.
IF YOU ARE SUBJECT TO SEvERAL DIFFERENT IMPLEMENTATION SCHEQULES EITHER BECAUSE OF OlFFERENT LEVELS OF AUTHORITY IMPCSING OlFFERENT SCHECULES (item la.) ANO/CR STAGED CONSTRUCTICN OF SEPARATE OPERATICN UNITS (item Ic). SUBMIT A SEPA RATE SECTION 144 FOR EACH CNE.
FOR AGENCY USE 3.
tmorevements 300-
$CNED. f40.
~
a.
Otsanarse Serial Number Affested Let trie disenarge sota sertaa numbers. assigned in Section 11. tnat are covered ny thesJmovementation scnecute.
tn. Autneetty smoesing Require.
ments chects the accrooriate item inc.catsnq the authonty for imolementation schedule, if the identicas imoternentation scnedule nas been ordered ny rnare tnan one autnanty. cneck
']-
\\
(
F '
tne approodate items. (see q
D a
D tristructiom)
Locally deveicoed plan 301b CLCC g
.J dM g
Areaw6de Plan CARE UO CSAS Basse Pian State approved ima,iementa-05a3 tion scnedule v
Federal approved water cuality standards implementa-tion plan.
CWQS Federal enforcement proced.
- J ure or action
- ra CENF State court order CCRT 7l CFED Federal court order
- c. Facality Requirement. Soecify the 3-cnaracter code of those 3 cnaracter itsted Delow that Dest descr: Des (general) in general terms tne require-ment of the implementation
- ggg, scheduce and the appticasse six.
character acatament code (s) from TaDie 14 of tne instruction booklet. If more than one 3014 6-criaracter scfiedule acosies to the f acility e
(toecific) because of a staged construction (see Taose att senedule state tne stage of con-struction being described here with the aooroortate gener s8 action cooe. Suomit a secariere Section lit for each stage of construction osanned.
^h New Facility NEW Modification (no increase in capacity or treatment)
MCO increase in capacity INC Increase in Treatment Levee INT Sotn increase in Treatment Lovel and Capacity ICT Process C.nange PRO Elimination of Discnarge ELI 111-1 P P A Fw,7330.;3 (7 73I 77ds secflon conrJins 2 pagoa.
a I
e POft AGEP4CY USE 3.
Implemeetatied SCnedule and
- 3. Aetuas Compaction Oatei Provede dates imposed by serieduie and any actuas dates at cornotetson for sino:ementation steos sisted nosow.
Inescate dates as accaratety as possele. (see instructions),
tenecementation Stepe
- 2. Scneouse (Yr,/Mo./Cavl
- 3. Actuas Comoserton (Yr./Mo./ Cay) ww.
m
- a. Preatmanary paaes complete 302S r
i 303a-i i
- n. Finas pian supmession "302D r
i
^ 303h i
i
- e. F:neJ ptan corroseto 302 s e
i 303e r
i
'303e
- d. Financing car *ipsete & contract awarded
'302a r
i e
i w.,=
y,;
- e. Site acquired
'302e i
i 7303e i
r
- ..q-j -:.
6
- f. Begin action (ab constwton) 002t*
i r
303f+
r r_
$.A ;
- . a
- P30Sy i
i
- g. End act!on (e.% constructioni r 3023, e
i
.;.~
/3429 e
r 303>
r i
- h. Olsenarge Sagan m..
-4..
-?
L Coerstionailevet attained 302tt i
r-
'303r-i e
h h
e t
4 Ill '-
- u s ":
E P A r.r 7sse-33 (7-m
FORM APPROVED CMB No.138 R0200
""^
STANDARD FORM C - MANUFACTudlNG AND COMMERCIAL SECTIONII. BASIC DISCHARGE DESCRIPTION t
Caspeceste Jus section for saan Castnarge endlCatee in Section s. Itens 9. tnat is to surface waters. Tnes inctuaes oisenarges to munecJoas sewerage systents in seneCft *ne wastewater coes not to tnrougn a treatrnent worma prior to Desttg alscnarged to surtaca waters Olscnarges to weets must De gescrtDed where tMere are also Gisenarges to surf aCS waters from tais fac118ty. SEPARATE CESCRIPTIONS OF EACM 015 CHARGE ARE REQUIRED EVEN tF SEVERAL Ot$ CHARGES CRIGINATE IN THE SAME P AC28.17Y. All values for an emsting Olscnarve snouse De recre-sentauve of the twelve preveaua monLas of ooeratsom If taas la a proposed 46senarge. vaaues snouad reflect Dest engineering estimates.
ACOtTIONAt.INSTRUCTICNS POR $ ELECTED ITEMS AP9 EAR IN SEPARATE INSTRUCTION BCQKLET AS INotCATED. REFER TO SCOKLET BEPQRE PILLING QUT TNP.SE ITEMS.
1.
Odsanarse Sertas Ne. anet Nanus tex 002
- a. Osscnar,e sanas No.
(see instructionsi
- h. 04samarge Name 20f Give nasne of casenarge, if any.
(see instructions) iM
- c. Prestems Olssnarge Sartas No.
5-if Drestous permet ago6& cation was enace for tnes essenarge (see 2 ate 9
stens 4. Sectlan it. provede prov6 oue aiscnarge eersea nartnoer.
~
cF It >
b4
~
l,]
1 2.
Olssfiarge Coersting Dates
(
a
- a. Casenarge Segan Date aftne r
asscnarge cescnneo Oesow is in y lQ operation. give the cate (witnen 202a Dost estimatet tne cascnarge YR Mc D*9aA I.d.
- m. Casenarse to sesin Date if tne casenarge nas never occurved out 7^.
as gaanned for some future date.
201D geve tne cate (wetnen Dest esth YR MO mate) the esognarge wits negen.
- c. Dissnarge to End Date If d6J.
charge is senecuseO to De discorp g
unuea witrun tne next 3 years.
202e gree the date (wetnsa Oest esth YR MO matet tne eMcnar,e was eaa.
-l*
3.
En,4peonn, R acert Avs.iamie checa 6f an engeneering recort is avsatapes ta reviewing agency upon reauest. (see instructiom 20s C
,.?
4 Dessnarge L.asades Name the posettai Douncartes wethan wasca Agaricy use the poent et alscnarge as located.
'""r"'
- o44 state
-204 d1Ed 204e County 2048 N d1Ed 264f (if soottcaciel C:ty or Town
'204e S.
Dessnarge Point cessnetten Ciscnarge e ento (enecu oner.
(sae instructionst stream <,_,...s
.tnes.a,r _ s.
and otMer intermettent watercourses $
tosa CSTR m.
cme 1456 069 c"=
Murhcioas Sanitary wastewater Transoort Srstem C MTS Munecicas Camoined $4mtary ano storm reansoort system CMCS 11-1 EP A Fece 7350.*3 (7. 73)
TMs section containe 9 pos es.
e e
DISCHARGE SERI AL NUMSER mo POR AGENCY tJ3E adunecJoas 5torm water Trarmoort
.c system QSTS wess (InMction)
C WE1.
Otner QOTH i
Sanitar_r vastes are discharred to the *:cv Chemical et otner is caseteo. speefy sos.
C =pany which win treat these vastes and discharge s.
chaaarw r**a-Lat/L*as G3'a the= to the Tittatavassee Riter the preCase toCatton of the notat of elesnarge to tne nee est seconch h1 Laatuae sess oga 1c,,y 20 gg O
b lN 7 *EC Lan,tude a.
cEm 7.
Dessaarve Reestvtag wasee Name Name tne waterway at tn co.n:
.2ota Tittabavassee Ri rer by Dev Chemical Cc=:any (HPDIS es disenarge.(see instrucuansi
,.c.
Discharge Permit No MI 0000668) m
.or.s. _ y es.
.or._cy s.
. tne.t.cna,,e ts er_,n an ou,.
Adaeerl utaer8 Sus 4 Jose fast tnat extenas Devone tne snore.
- i2273, 207e f6w or is Desow tne mean love water tane, cornesete item a.
733
_f
.l
.. w W^
4.
Offsmeee Casazarga 3.eh a
y-
- a. oascan,,e oistanes trem sner.
ss.
re e
tb Desaharge Desta Sesew water 34
...w-Serrase
- 20$2h.
feet
- ?'y 3.
Diasaarse Type ane ossurrense
[L
- a. Type of Dessnarge Ciecs T
wnetner tDe alscnarge is con.
- 108a, C (coni Continuous.
. ' ] l ; ' I ", '. ' 'r",
tenuous or intee mittent.
yg (see lastrucconal C (int) Interme. teat f
/4 t
..e Ie /d
- m. cascnarge casurrence Days per T eays per wese sp"' -
ween Enter ene avera,e nutn.
- ssty, Der of days per weeis (during periods of eksc.dtget tn.s ota=
I'r~
I cnarge occurs.
..e~q
- e. Casanarge Occurrence-Montas if this eksenarge normaaty 20s hJAN $FEB G AAR QApR operates (estner intermettently, or continuouseyl on sesa tman
$MAY QJUN QJUL QAUG a year.eround eases (anctuaang snuteowns fer routsne mannte.
CSEP GCCT C NOV CCEC nance), cnocu tne montns eur.
ing the year wnen tne essenarve is operaung. (see instructions)
~.
Comosete stems 10 ane 11 If "fnter*
snittent" ts cpeczee en a tem ga.
Otherwess, process to atom 12.
iv, W{
- 10. Intermettant 01sanarte Quantity State tne average veaume cor 413 210.
,b,
"*eusand gastons per ciscnarge occurrenca, cnaege occurrence in tnousanos of gasons.
- 11. tenermettent ciscnarge Questien one Frequency
- a. Intermettant Casanarge Cursesen
^
PerDay State tne average 211e
' sours per day numoer of nuurs ser Gay tne elsenerge es ooerating.
B.
Intermettent Olsamarge Presuener State ene average 211a anscnarge occurrences car day numoer os aescnarea occur.
rences per oav eunng cays Wnen 41scnarging, t2. Masemune piew peries 0.we the y-
. ume peceed on wneen ene man 6 mum 21:
. rom " E",,
to "
now of thes ensnares occurs, montn montn t.. p._,,1..
n.:
1456 070
~
FCRM APPROVED 002 CMB No. LZ2J0100 FOR AGENCY USE
~
l ss. Asisat, omenstesa owa mw,3 aa^ ~ s a k a- ~ =~ =' =~ s u '
- s '* " *' k a~ s er* * 's-r va a-3-
narrauve ancnouen av acuvetY 2134
~~
~~~
.r
_t.... - r n.
recuire=emse eer ass reem e emee,-d
, s.
r-e---
_t.
en *he clant si*e. and *Ma sir _k dred 9 4-
-ka e'tatorster buildia.z isberaec-r.
.. A._t
- n, C
.,e For esca SIC Code wnaca essences
,, _,..aus.n, t.
._a_
succey the type and mazamum am _ to,..t.or,.er.. m. _ a.
. _.me..t.m m,.ct.eoro _ t pr._
.. tern m,. t...n.
n,, )
ll ![
4 specified in Tacle 6 of tas instrue.
tasted in Tan 6e 1. use raw maternae
- ',,,i ;, ;n j',t j
Uon Secesset. For SIC Co.es not
~
u i'
~~^*'"U--'
or production unsts normassy usee for measuring production.gsee
-,r
- a...
t_
Identneum Unit Shared Ciscriarges ssC Code Name Amoum/ Day (See Tacle I)
(Sertae Numeerl
{h (1) 4 (21 (3) 6 ee3-(5) 3A I
I I
I i
1 I
I I
,r
..t.
Maximum Unit Shared Ciscnarges Sic Code Name Amount / Cay (See Taose 11 (Sertas Numoet) 21449 (1)
(2) 6 r31 (a) f*)
i I
i i
i l
I I
I I
I I
I I
I I
1456 071 m, _. n.., <,.,,
n.3
r DISCH ARGE SERI Al. NUMBER 002 FOR AGENCY USE i
- 14. Wasta Amatement
' $$nNe*7.$!a7"ats7 eat Sa=ita 1nd eVEucr2tcr bUi1diUE 1SbcrIYcII e
zisa Nuradvm eracuces uses on tnis aiscan,e vastes are collec*ed secarstel-r from
_1 other vaste-witn a ories n= rate.e. (see instucuens water strect=s snd dischsreed *e *ke Ocv &_e-'icei 00=pany I,$_ ~.
for trastrac*.
m
%F a - e-7.V W::
' e::
- N..D....
4=w
.Tu
, - ~
- hJ.
. ~ - <
- =7 a
'W$.
E9#C""
(3)
=37"33 (2)
' HSE (1) in, wasse Asatement cases Using the coces ustee in Tan 64 c-
- e of the instruction soomiet.
(4)
(3)
(s) eescrine tne waste acatament processes for tnes assenarge in (7)
(s)
(31 tne oreer in wnmn tney occur if pasmosa.
(10)
. (11)
(12)
(13)
(14)
(13)
(14)
(17)
(1s)
(201 (21)
(19)
.)
m,
(..,
.)
m,.
s pn -
u
,,,.-,,,.. n,,
1456 072
FORM APPROVED OtSCH ARGE SERI At. NUM85R CMS No.153 R0f 00 002 FOR AGENCY USE
~
O IS. wastewater Charactertstsaa Cheets the Dom Deside eacn consutuent watch is present in the effluent (alsenarve water). Thas determ6naston is to te cased on actuai analysis er east estimate. nee instructions 4 e
li li Parameter
=
Parameter x
216; 2
216i 2
a.
a.
/ o 1 lv Color l
Copper 5
00080 Iy 01042
- I
=v eo Ammonsa from 6
00610 X
01045 (a)
X d y Organic natsogen Lsad
- 2 00605 X
01051
$a Nittste Magnesmm
$ "=
I 00620 X
00927 La Nitrite Manganess
-o (E) I d4 006t5 01055 o-c Mercury
- 1) 1
@j Phospnorus ll X 71900 00665 Sulfate Molybdenum l
I 01062 I
a C V C0945 Sulfide Nicket i
D$
00745 X
01067 I
o=
Setenmm l
YS Sulfite 00740 (a)
X 01147 i
L*oe Bromde Silver
,o 71870 01077 d m Chlormie Potanmm 00940 X
00937 X
9 *'
lX 3*
Cysnde Sodium 00720 (a)
X 00929 l
Fluorde Thallium 3
"2 00951 v
01059
.a g Aluminum Titamum l
L5 01105 (a)
X 01152 l
3*
Antsmony l Tla l
4 0 01097 I 01102 i
"3 b:
Arseme Zhic 01002 01092 (a)
X
$Y Beryllium Algic2 des
- l 3
01012 74051 l
=v
-t (a)
X Chlormated orgazuc compounds
- Barium 74052 j]
01007 Boros Pesuades*
l 3 0 01022 (1)
X 74053 l
$3 Cadmium Oil and grease lX Ot027 00550 i
h Calcium Phenols s.5 y
32730 009L6 hh Cobalt l Surfactants z'
a-01037 1 38260 g
c Chromium l
l Chlonne I.,
OE 01034 I
l 50060 li.
.2.;
hdioacuvity*
l l X ll 74050 l
tp Fecalcoliform bac:eria 74055 l
.=
- !pecty substances. :ompounds and/or elements in item 25.
]'
Pesticdes(insecucdes, funeicdes. :nd rodensteides) must be reported in terms ot the acceptsoie common d
names spectiled an Acceptacte Cammon Names,nud Gemical Names for the inerettaent Statecnent on
/estacale LJactr. nd Editton. Environmental Protecnon Acency. Wasmnetun. 0.C. 23250. J une 1972, as required by Subsceuon 162.7(b) ot' the Regulations tar ute Enlacement ut the I ederd Ins:cac:de.
Fungscade,and Rodenue:de Act.
II-5 EP A F orm 7310 -23 (7./3) 1456 073
ey[g, g a D" cg$
f ga>R ga o
or n
s 3-g,R i
B~
ga;" 1 i: ! o:
, f *;g tg~E.$ al. 3g g s:IlE a ! s* ;h t !* Et.5 g,2 R ! e~
5*
nlg{ -
ig01 l?
sI*
,g g? ti: I lI *1.&.ga I.I
%' gI !2f.8 2a'. jg3b!ggr 1
{,!8 a
,!E3ah 1 I3gp !2M$gg7 at i aleIE g
E n~
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ty gi g
s n v e
n u
I i e
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u i
la u
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c c
o e
s VrDA y
k
)
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e la u
y t
c g
g a
o s
a s a V0l s dd g ns c
a e
c T
n a
c e a
i s
e l en ic ad d e
-hen r
e u i
g e
Ta v r
s e e rai u vt ty u e e t
y p
d v
WA uv a
u y A
c b s e a
ql "t
m e
A ms c h. i 3*. R ta y
la s
v e ct a
n e y n
a px e n e
m s y
d s yut t t ia
- k d 0
ibOEDA bOED 1's. A A
s c s i b k ic ab mi isl a a 4
l I
t l
naD neD D
mdw E'
- gF gw 3
B UW(
il (
Qo 3
t f.
f;I;4<:8 o o[
O *
- 6 "
O Ooi g'OgO v
VI
$,y h.
^fv 2v ww c
{i ^$E f"
aF 2v s
^pv
(
t r*
a f3i ^
a-
-pv
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^'o v 2v s
i*
"[E 9g
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^fv 2v G!h3
^ov c
t
{
ha (ef e "
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f*
^fv 2v s
^t c
c QP
)
I-F YE ifa Po f*
^*o v 9v t
{ s nEfa 54o<><DnMn pvO
^fv 9v i
x2E~k
$qE-e
(
,f*
^tv 2-(
t ugInkhfeh~
de nj 5' g. 24 -
, o
,/
, r
)*. go 3,"
e.
4$
I'*,l}
n s
uj 1's 'N
' n,n'I esr Ild 'y t 3
t 3
h'r)1<> w4!m
=
a bwp?0 e b;C 7
u ;s p"e *' 8 N!.N J
[;:oo p5N D
D i
E
[
c 5
Q~D
.a i.ah Ie
- HN egw d
Q*5p "
g g
s FORM APPROVCD ChtB No. !$8.-R0800 CISCHARGE SE RI AL. NUMBER p
002 Fon Acency use
- n. a:
.a e
rococat ( =g/11 zm== (=g/1) t m
a aa
$ =$
=
$ ?
$ 2 E $
1 w
3
= 3 5
so 3
o 2
- ~
a l
Parameter and Code m,3,c.
>3<
g 5
x n
> S <-
4 3 : s if b armi
- 1 Us r.
E,=
a Wi 2
q il a d a*#
ji - 335
.5 g s n=
f2 32 E
=4 12 1
.s 3 ".a 7 m
a3 2 ?
i
" o r.
mS C SJe i c
zowc<
sown w<
z<
n (1)
C) l (3)
(4)
(5)
(6)
(7)
(8)
A=menia 00610 (a)
(b)
(b)
(b1 Cyanide 00720 (a)
(c)
(el (c1 Alu=inus 01105 (a) l (e)
(e)
(c)
Copper OlCh2 (a)
(c)
(c)
(c)
I Mercur r 71900 (a)
Y (c) lei (ci l
l (ci l
Zine 91002 (al (el (c)
(bT (b1
/bi !
Oil 7, 0rease 00540 (s)
I Chlorine 50060 (a)
I (a) 0.2 05 (a) Not knwn (b) Unable to predict but scr ally present in sanitary is, piant eentres. eneca st ene fe 23:2 ioweng osant controns are avassao
vastes t
a er source for maior AP5 Dumosng factilty.
L {;,
Alarm or emergency procoodre for
@ AtJA Dower or seuloment faalute Comosete item 19 ff dtscaarge la from confirag and/or staam water OO generation and water treatment D
D D
?! li'1 acolttves are used.
si fj
J' oc a
- 2 J W e a,
- 19. Water Treatment Additives iftne chenerge is treated witn any cor>
ditlener, tantostor, or asgicide.
, ]'
answer tne fostowing:
- a. Name of Materlad(sl 2f ta'.
30"*
_ ; s.~
fL Name and andress of manu=
fas wret 219 s J^
- c. Cuantity (pou..*e acced per 219e meglion gations of water treated).
--- A 1456 075 EP A Fe<= 7550-23 (7-731
OtSCHARGE SERIAL. NUMBER PonAGsNCvuss CC2
/
- {^
- d. Chem 4cas csmoosation of tnese 2194 adottives (see leistruClional.
w; be -sadf comosete items 20 23 If enere is a tnormas cincnarge (awe assessated wetn a steam and/or oower generauon paans, stees mesa, cetsoseum refinery, or any otner manufacturing process) and tne totas etscnarge flow is 10 maison gassona ser say or more. (see 6nstructiones
- 29. Thermat Olsenarge Seurse Caecat 22t>-
h n
/
f9q f 7,_
the amoroortate itemtsi lacicating m / lf)[f {;
U
~
tne source of tne alscfiarge. (see q
J
.y westa.cuome 9
b bY. 4 C St.80 l
Boner Snowdown t%
C 8CCI.
,.f, Boder Cnernacal Cleanang AsJs pond Cverflow hdi CAPCF Bouer Water Treatment - Evapore.
CEPSO i.
ter Sloansown
. -n u'
""Y CCCFP Ois or Cosa Fired Plants = Ernuent from Air Pottudon Control Devices Condense Coosing water b
CCCNQ h
CCT80
~ [k Coosing Tower Sloweown C MPPR SAanufacturing Procass ws Otner f _? %
C OTHR
- vA.-
- 21. Otsanarge/meceeveng water Temper.
?
seure 04fferense
. r'Q Give the maximum temperature y.,
difference Detween tne discharge l :.
and receretng waters for rummer
.g and wenter coeraung concitions.
Summer 221s 1*P.
s 9
'P.
winter 1221m
$?O
- 22. Otsasarge Temperature, mate of y 'F.#out Change Per Hour 22 7 ca Oswe the mamemum possan4e rate of temoerature enange ser noiar of
, a..
eiscAarge under operaung Con.
altions. (see lastructionsi y
- 22. Water Tamperature. Percentue Regers ;Preguency of occurrenset la the tasse netow. enter the temoerature we een is excessed 10%
of the year. 5% 9 tne year.1% of tne year ano not at are (mamsmum
~
yearty temperatures. (see instructional Pfeeuency of occurrence 10%
4 S%
i 1%
I Maximum
,,; f
- a. Intase water Temoerature
-i25 (3} D {E) ** Il 3 )
- ! N **
(Suotect to naturas enanges 8 ** I1) I &I **
'? I **
th Ctsenarge water Tornoerature 222h
( & )
- .C *.
'.CC 'aT.
28 Water intase veseesty 224 reet/sec.
(m onstrucuenst
.Ia.
- 23. Recentlen Time Cave tne lengtn of 223 minutes tiene. Ws minutes, from start of water temoerature rise to disenarge of coosing water. (see instructionst 1456 076 u-a m
..r.,e... n.n,
FOR5t APPROVCD OMO No.1384100 DISCHARGE SERI AL NUMBER FOR AGENCY USE 002 I
I A..
1 223 stern l
faf0'madon I
I 1456 077 m,._,m.m,_n,
b FORbt APPROVED OMB No.13%R0100 roR AGENCv usE 1
STANDARD FORM C -MANUFACTURING AND COMMERCIAL.*
SECTION III. WASTE ABATEMENT REQUIREMENTS & IMPt.EMENTATION (CONSTRUCTION) SCHEDULE TNs section reoutres information on any uncomoteted implementation scBe@use wneca may nave Deen im,oosed for construction of waste acate.
ment facauties Suc9 recuarements and smosomentation seneouses may nave been estanaisnea ey sacaa. State, or Federas aeoncies or Oy court acuen. In adottlon to comoseting tne fossowmg items. a rooy of an officias unosomentation scnecute snouac ce attacned to (nes apostcation.
IF YOU ARE SUSJECT TO SEVERAL OlFFERENT IMptEMENTATION SCNEQULES EITNER SECAUSE CF CIFFERENT LEVELS CF AUTHORITV tMoCSING QiFFERENT SCHEQULES (Item 14.) ANQ/CR STAGEQ CCNSTRUCTICN CF SEPARATE CPERATION UNITS (item 1c). SUBMIT A SEPA RATE SECTION lla FOR EACH CNC.
FOR AGENCY USE 1.
Imoreeements 30 s-SCHED.NC. -
- a. Discnarse sertal Numeer Affsetee List the alscnarge Sete serial numbers. Assigned in Section 81 tnat are covered my this4mosomentation seneouse.
D. Aetnerity 1moesang Requsto.
meets Check the aooroorlate item Indicating the authortty for imoeementation schecuse, if
- p pg tfie identicas lmosomentation i
scnosuse nas Deen orcerod by more tnan one autnonty, cnecat the accroortateitems. (see
. f instrucuonal Q/
1 Locatty eswescoed osan
'341b CLOC i
Arsewide Plan Gig 7
[Agg g
~
m e-
~*
State sooroved imosernenta.
.9 Csas uon sen.co Federal aooroved water
' ~. ' '
eua44ty stanssarcs amotementa.
~
tion ptan.
CwCS Federal enforcement proceo.
C' ' <
ure or action
[a b CENF
-[,(
CCRT State court oveer C FED Qy=
Pederas court order
- c. Familty Recuerernent. Specify listed betow tnat Dast describes "f
3.cnaracter the 3<natacter code of tnose (genered) in generas terme tne square.
ment of tne imosomentation gggge seneouse and tne acostcaese sta=
cnatacter acetement code (s) from TaDie il of tne instruction Doostlet. If more tfgan one
, Wet 6 cnaracter (l#8C8flCI scheouse acceles to the fscility
,s.
because of a staged construction
]_
(see Taste it) s.
schasule. state tne stage of con.
,.4,
struCllon being descrtDed nere.
_r wet!s the aooropr6 ate general C
actlon code. Suomat a separate Section all for eacn stage of construction osanned.
New Facility NEW Moolftcation (no increase in capacity or treatment)
McQ increase in capacity INC increase an Treatment Lewee INT Botn increase en Treatment Laves and Caoacsty ICT 1456 078
-c-
. Eilanination of Cascnarge Et.1 111-1 E P A Fw,7333.;3 g7.73)
This section contauns 2 pages.
D D
D I
^
- f. U 'GT'e pp
/
r i
O frost AGEPeCY USE 2.
Imp ***atation senecem ane
- 3. Astmas comoestion catee Provule datee imposed by scaecule arte any actual dates of comotetion for imosomentation steos sisted besow.
Inescate dates as accuratasy as possem. (see instructionst, impeamentation Stess
- 2. Schectu8e(Yr h h )
- 3. m Montion (YrWWOad
- a. Predienanary osan comptete 302h r
5 -__
' 303e, e
i nR
'Sesta.
r i
- h. Mnel stan summession
[3023e a
y*j-v;
- Q
- e. Mnes otan comosete
~ 202a, e
i 1303e-
,}
[D;
- _3028, i
a
- 303
- r i
- d. Mnancing compsete & centract awarded yh:
hMI'
- e. Samaceutred etaae 5343e=
r i
r i
y;:.R C. * ' Q -
- f. sogari actie e (as, construction sa2e a
e
'l303r' r
, aM ll*:
- s. Ens action (e.s Construcuent 302s.
r i
303e r
i 20tc
-.1.p. C
! so3:e A casenerve segna
,302m r
i i
i WI.
WCh 73 ass-i r
L operosiones sevet attaines
. son-r i
G e
S e
IU'2 en r
- sso :s a tsi 1456 079
FCRSt APPROVED OnfB No.138-R0100 FOR AGENCY USE STANDARD FORM C-MANUFACTURING AND COMMERCIAL l
SECT 10NII. BASIC DISCHARGE DESCRIPTION 1
Casnosets taas secuen for naea casenarge enescated in Section t. Itens g. triat is to surface waters Tnes 6ncsuces asscnarges to munacJose sewerage systems in weten the wastewater sees not go tartmagn a treatment worms orter 14 Deang elssnargets to surface waters CisCnerges to weds must De eescrtoed where there are also esscnarges to surface waters froen tnes facility. sEPAR ATE DESCRIPTIONS OF CACM QBSCHARCE ARE mEOutREO EVEN IF SEVE3tAL DISCMARCES ORIG 8 MATE IN THE SAME PAC 38.37Y. Ala va6ues for an eassting assenarge snouse De recre=
sentatsve of the tweeve preveaus montas of operatson. 4f taas is a secoceed sucnarge wasues snouse reflect Dest engsneering estimates.
AOctTIONAL INSTRUCTIONS FOR SELECTED ITEMS APWEAR IN SEPARATE INSTRUCTION SCOKLET AS INotCATED. REFER TO SOCKl.ET SEFORE FILL.JNQ OUT THESE ITEMS.
1.
f,asemasTe Sartal No.and Nanse 003
-~~
- a. 04senasgo Sartal No.
.2913 (see instrucuens A ct d%
%,s h ceess Stean Bratorster 31ewies.n
- o. Dessaarve Name Give name of shenarge. Af arry.
(noe instructions) r
- k f.T:
- s. Prevesse Otssaarge Sertat No.
.M[.
if provsous permit acosacaden 3A wee enaos for tais alscharge (see 20te stens 4. Sectioss II, provide prove.
ous elecnarge senas nuancer.
~
$ 13 2.
Ossese,,e Oseraang Cases
- a. Desenarge segas Cate Ifthe
-E:
r
]
eisenerge descnoes oesow is in NA Uoo D
D,
,@o k[j jj J
J u( h
_ J(
operation. give the este (witnen 202a.
n J
eest estimatet the etscnarge YR MO wc began.
th. 04sensage to segia Cate if tne
"*O
- 0 castnarge has risver occurrett Dut is osannes for some fun.re cate.
. 202a-geve tne cate (witnen oest este.
YR MO matop the oesenarse wot bettn.
- q
- c. Olsenerve to End Oate if ato.
enarge e seneouses to be elecor>
w.
tanues watm tue next 5 years.
202e, QL grre tne case tuttnen Dest esta=
VR immu matel the CtsCastge wdt ens 1.
<" I 3.
Entneering neoert Ave 48anse Cnects of an engsneereng recort is avestaose to rev eweng agency upon reevest. (see instructions 3 20 1 C
.:n 4
Olssparge t.eastden Name the posttica8 Ocunear6es witnen wasca Agency use the peere of aasenarge is located.
Y '"
m-State
- 204e 2044 41d' md County 204a 204e
~
\\{"4 A ig4 (If sooelcancel C:*r or Town 20se 2044 S.
Ossannege poent Oeservet.m Ohcnargo e into (cneca o-M' (see anstructions)
Stream tericsuces esteries, arrow; and otner intermattent watercoursest 205a CSTR l.ame Ct.KE Ocean CCCE Munectoas Sanatary wastewater Transoort System CMTS r
Muntesoat Cornoined Sanitary ano Storm Transoort System CMC 5 11-1 EPA Fene 7333.33 (7.73)
This section contains 9 pa.:es.
s os5CNAACE SERI Al. NUMSER CO3 Foft AGENCY US newnecisas Storm watee Transonrt
/
System Q $T3 west (Insection)
C WEL oiner corw e
- his vaste is discharred to the %v Chemi ni
.e, tny it otrier es crisened. tosety 2es.
which vi'1 treat this vaste and discharge it to the s.
caener,s eeant - tavo ag csv.
Tittabavassee River tne efectae locauen of the ootnt et eascnarge to tne nearest second, massa h3 -Ea
.25, MIN d 5EC taatwe tangstume
-seen.
% :Ea I? uiN LEc
%9 7.
cassnarge messeeeng Water Name Titta'cavassee River by the Dev Chemical Cc=pany Name tne waterway at tne sota 2ota et eascaargeJane erstructions m,_
f (NPDM dis 0ha rre ?"'""it 'IO M 0000 I
n att tne oescnarge es mrougn an out.
P*# # **'"'Y D
"'**"""*8"'
I
~
303' faa taat estenas oeyone tne snore-
..asim tino or is oesow ine mean sow
-L e
20Ts 2_5.. 0.. ".l
-l J. s weter one comosete stam s.
9.n.7 s.
offsne,e ossenerge gh 3A
- a. omenarge Distanes trens snere Zoso
'est
- }!I
(
]DiQ 'g l i i i < > > :; ;,' < > > ![; i t,
3si M D Disanarge Desta seeew water 32 "c
.j'Ji a se, vise rest
- 2,oam d
[=
1 n
y s.
Dassnaege Tyse ane ossumnoe
- a. Tyos of osasaarge Cneca
'm
41) 6 061 htes Supply l
2 l 2-2 l :Icne 7-l l
l l
1 I
I I
I I
I 1456 082 m,_ mo m g_m u.3
a a
9 JesCHAACE SERI AL NuM8ER 001 ronAaE:sev usE
/
- 15. Weste Anatoment a waste Anatoment Peseth Process SteS3 eV3DCratOr D1CVdOVn 'dll De Desertes tne waste amatement
- ' Sa, Narrattwee e
collected Separate frOS Other W3Ste StreBOS 1Ed dis-tn et ar at
(
instrues.no
-~
charred to the CoV Chemical Cc=ranv for treatment-
,z y
4:;ym
-re
$'Y!$
TW a7:6.%
P'- U *.:
26'48' 7.:::::
WCg
~$-DAI:
ie!I9 3CT:
- "Y T.*
DME
- a. weste Amstemoet comes
- itsm.'
(1)
(2)
(3)
Using tne codes insted in Tasle h
(3)
(s) is of tne instruction soomist.
(4) cemettee tne weste seatement processes for tnes essenarge 6n (7)
(s)
(1) tne oreer in wnica sney occur (12) if passalue.
(10)
(11)
(12)
(14)
(13)
(1s)
(17)
(13)
(21)
(13)
(20) m,
(.,
(25)
DD e.
1
..(!
EO d d
\\l 1456 083 m,_, -
-n)
FORM APPROVED Ot3 CHARGE 3ERI As.NUMSER OMB No,15340f 00 003 FOR ACCNCY USE t S. Wastewater Characteristles CheCM the Dos Des &de eaCR Constituent wn4Cn 65 present in the t*ftuent (dtscnarse water). This ostermination is to os maaea on actua4 analys&&
et Oest estimate.tsee instructions)
Parame se Parameter 216i e
2161 e
n.
e.
Color Copper 00080 01042 Ammoan Iron l
00610 01045 i X Orpaac mtzogsn
- 1. cad 00605 01051 Nitrate Magnenum 00620 00927 Nitrite Manganese 00615 01055 lX Mercury Phosphorus i
71900 00665 Sulfate Molyedenum 00945 01062 sulfide Nictet 00745 01067
'uffits Selenum l
1 01147 i
00740 1
Bromide Silver e
71870 1
01077 I
Chlords Potamnum l
00940 X
00937 I
Cmese Sedium l
00720 00929 l X Fluords Thaihum l
00951 01059 I
pummam TItantum l
01105 1 01152 l
Antimony T.n 01097 01102 Arsemc Zinc
{
01002 01092 i
Beryllium Ahucdes*
1 01012 74051 l
Bartum Chlormated orgmc compounds
- l 01007 74052 l
Boros Pesticides
- l 01022 74053 l
Cadmium 00 and grease 1
01027 00550 I
Caktum Phenots 00916 32730 Cobalt Surfactants l
01037 38260 1
Chromium i Chionne l
l 01034 l 50060 l
l Fecalcoliform bacterza Radioacuviry*
74055 74050
- Specfy substances. compounds and/or elements a item 26.
Pesticides (insecticxies, f*Jocicdes and rodenuedes) must be recorted in terms ot the accrotable common names spectkd in Acceptacte Common Names and Ocmscal Names for the Intmisent Statement on festicate Labets. 2nd Edtuon. Environmental Protec: tun Aguncy. Wmunytun. D.C. 20250. J une 1972. as required by Suowction 162.7(b) os the Reguaationa l'or tile Entorcement ut the 1 eder L inwunc:de.
Fungscide.and Rugenuc:de Act.
1456 084 EPA Feene 7550.2t (7.7)
P00R D E R
O4SCNARGE SERI AL. NUMBER 003 FOR AGENCY USE I
- 17. Desertossen ed totsas see Cascaeree For eeen of tne paeameters tested esow. enter in the sooroortate con tne veaue or coes setter anseer castee for.(see instructions 3
=
fn aesttion. enter tne saremeter name and code ane aas rooueree vaaues for any of tne fosloweng parameters if tney were eneckee in stem 16:
asnmonsa cyanese, asumanum arsen.c. perytisum. aamium, caromeuen. coooer. lees. mercury, neckes. seien, urn. vae. one. oss, oss one grease.
irus snforene tresaeuaak laihtent i
F.!Duent A
1 8 E 1 E$
} }3 5 N}I li 3E -$
k b
Farsmatcr and Code
!Ef h
s3 3
2E.
li dil 5
!IIII 3m d11 i
j 2 N.11
- M X. w 8' ~i 51 a
$$a8 236 l d
28554 3855 C4 J
(1)
(2) 0)
(4)
(5).
(6)
(7)
(8)
Flow *
, -- MGD 0.058 0.058 (a) 0.115 5C050 1
pH l
Units a
j 95 1o,5 00***
l Temperature (water) l 105 L30 60 155 7 02s I
Temperaaus (rummer)
'F
! Lk0 70 155 74027 lh0 i
I Biochsmica10xygen Demand (BCD 54ay) 0 0
0 0
mg/l 0o31o QemicalOxvgen Demand (COD)
I O
l (a)
(a)
(a) co34o Total!aspendad (nonditarabis)
Soma
<1 t30 (a) 150 me j
oosso i
Spectt!c conductance rmcrombos/cm at 25* C i
5 (a) 4000 00095 Settleable Matter (rendue)
"V1
. (0.1 40.1
( 0.1 (0.1 00545 l
- Other dischr.rges sharing intsze now (scrui sumbetslisce instruccons)
{ a) *'nable
,0 p:'edi:*
t P A Poem 7333 3 (7,7 II-6 1456 08,-3
TCRMAPPROVED CNB No. US-R0!OO DISCHARGE $( Af AL, Nyugga OC3 ran AacNCy vss o
- 17. (Cent's.)
Induent f
Emuent f
r l
m y
13 m
!Eh h
ha}
S*3})
i[
3= 3 1' 2 1.s i s, ;[.
Puameter and code
- m i3 t ii l,
3
- 1. 3 h. Ine
'1~2 a
C man
- +
e
-s.
u a.&.y =.
M 7
a 4
a.3 g
a ae3 I
g
."...O l
Q 3Gwa<
2Gm~
Z<
vi D ip.
(1)
(2)
(3)
(4)
(3)
(O (7)
(3)
NA l
l l
l l
I I-I l
I I
l i
I I
l I
I l
l l
I m-1s. Maat Caan.-:a CDecas if tne fos.
215 lowmg prant contross are avassacee for tnis assenerge, y.a Alturnate power source for maior C AP5 pumosne facality.
- a.,
Alarm or emergency orocsours for 3Aw power er equeornent f adute
.v-Comosete item 19 ff atsenarge is from caostng and/or stnam water generation ame water treattnant asettkes are used.
e
- 19. Wster Treatmoet Adeltives if tree eisenarse is treated witn any con, attsoner. Innanitor, or assscsae.
answer tne tonowmg
- a. Name of Material (s) 2134
,. q' w..e
.ff"l
- h. Narne and accress of manu.
gg faClurer 219b M
- c. Cuantity (counos acaea per 21se meillon gations of water treatea).
1456 086 u-'
m ae m..n.m
e e
OtSCNARGE SERI A4.NIJMSER 0 0 *t PCR AGENCY VSE
- 4. Cnemecas composetten of triese 510E
.t e aeosteves (see hatructions3.
6*
Comosete stems 20 25 it tnere is a thermas essenarge tae. associated watn a steam ane/or power generauen paant. saees meal, petroseum refinery. or any etner manufacturene processe and tne totas eManarg6 Flow se le amuseen Sassens per day or more. (see enstructionsi
- 29. Thermas 04senarge Seures Cnec38 221P tne aes.cortate itemiss ano6cating rne esurce of sne eisenarse. (see in, sn.ctie=
Qc
]p C st.s0 5 ier eiewe wn em Cnemicas ca.ning
- 4.J,'
C eCC1.
A.= pone 0,ernow
,PJJ CArce Sesec water Tres ernent - Evapore.
CEPSD ter Stoweown gg
'.*~*2 C CCPp 014 et Coas Piree plants = Effluent f
frans Air Poilutson Contros Deveces (yi cancense Ccosang water
,d CCOND Coestag Tower sloweewn
(
CCT80
' d.
C MPom Manufacturing pmess w
Ctner
?~.9 COTHm 7:
w St. Casonsreepneceivtag Water Tom.,er.
attre r;ifference c-.
cave ene manmum temperature offf'srence between the elsenerge
- .-o and retarvang waters for earnmer ans$ winter coerating coftettions.
W (see tasaructions)
'JA
'
- w c4 ib.21E NA 'F.
Winter a
+3 r
- 22. ossamarse remoorsture. nate of
'.i.
.TA 8 '.Acur Change per Heesr J22X 1
Give the mansmum passande rate of temperature enange per nour of enacnarge under coerating con.
estions. (see instructions) 9' 7
~.M s
- 23. Water Temeersters. Percentile neeert (Frequency of casurrensel in the tasee sesow, enter tne temcorature weteca is excessed 10%
of the year 5% of the year.1% of the year and not at att (mantenum yearty temoenture). (see lastructions)
-'~
P-~-
of occurrence T....~~
m i 5%
I is ivusmum
_r NA ow l NA o.1 NA cel :TA o.
- a. Intsee Water Tameeratura
' 223a-( uwt to naturas enanM 7A ce l 7A,el ?7A,, l. A,, l S.
Casanarge Water Taeneerature 223as le. water intase vesec8tv 224 beet /sec.
Isee anstructions 74
- 28. mesension Time Gave tne sengtn of 2:S miteutes time, in minutes. ' rem start of water temperature rise 10 eistflarge et coesang water. (see instructionst 1456 087 na m,e m.m
FCRM APPRCVCD CMB No. U8.R0100 OsSCHARGE SERT AL. NUMBER FOR AGENCY USE 003 II u
f 1456 088 m.
n,..u,,_m, u-9
i e
FORM APPROVED CnfB No.133-R0100 FOR AGENCY ust II I
STANDARD FORM C -MANUFACTURING AND COMMERCIAL SECTICN III. WASTE ABATEMENT REQUIREMENTS & IMPt.EMENTATION (CCNSTRUCTION) SCHEDULE Tats section recuares inforenation on any uncornesetse lensternentation scpeouse wnecn may nave Deen innoosee for construction of waste amate.
ment facalettes. Sucn recuarewnes ane tenosernentation scrieeum may nave Oeen estassesnee my tocas. State. or Feeeras agencies or ey court acuon. In asettien to completing tne rollowing stems, a cooy of an offictas ernosementation seneouse snouse De attacties to tms acosecation.
IP VCU ARE SUSJECT TO SEVERAL CIFFERENT IMPt.EMENTATION SCNEQuLES. EITNER sECAUSE CF OIFFEftENT L.EVELS CF AUTHORITY IMPCSANG CIFFERENT SCHEQut.ES (stem la.) ANQ/OR STAGED CONSTRUCTION OF SEPARATE CPERATION UNITS (1 tens 1c3. $USMIT A SEPA RATE SECTION lie FOR EACM CNE.
FOR AGENCY USE 9.
lenocevements 30 0 SCFIED.740.
~
- a. Casemerge Sertal Numeer Affected Last tne eiscnarge Sete sortai numbers assagnee in Section a1. mat are coverse my tfusJmo#ementation seneevea.
- t. Amtmerity Imeesang Reguare.
meets Cnecas tne aoo.sortate atom snescaung the ausnority for isneaumentation serieause. af tne teenticas imosementation
~.
scnesuas nas esen creates my more tnan one autnonty caecas the soproortate 6tems. (ees instructions)
Y, J 2 LOCaely oevelopes otan 34kb CLCC Areewees Pian CARE Q
CsAS sasse 'ua state soorovee amosementa.
, M.. -
C5Q3 uon seneouse Feeeral soorovee water egality starNaares emolementa.
CWQS tfort otan.
Federad enforcement procoe.
Isre or action h ',.
CENF CCRT state court ores, Federad court ortser p
CFED
- c. Pseellty Recuarement. Soedfy
.y tne 3.cnaracter coes of tnose i
3.cftaracter listee Desow tnat nest descrtese r.. -
(generast in generst terms tne reoudre.
enent of tfle imoternentation ggg g, sCneeune and tne sootlCaole stX.
crtaracter acatement cocets) from Taese 11 of tne instruction Docasiet. If more tnan one Ste 4.cnaracter (888CIII8I sCneouse apotles to tne faCality
~
(see Taose 111 because of a stages construction seneoute, state the stage of con =
x struction Doing descrtose mere
- 31 wetre the apocoortate generad action coes. Suomat a seoarate Section III for eacn stage of P00R ORBiMq construction osannes.
-*-a.
Neur Faculty NEW Mestrication (no increase in capacity or treatment)
MCO 1456 089
,_ cao.tv
'~=
facrosse in Trestrnent Laves INT Scan Lncrease an Treatment Levee ane capacity ICT t
Process Change psto Ellmanation of Olsenarge Ekl 111-1 E F A P* 1550=.3 (7.731 TMs section contarns 3 pagea.
F FCit AGEFGCY USE '
2.
luestesseentation Saneente and
- 3. Astmas Cseesserfee Caesi prow 6de dates smoosed by seneouse and any actual estos of comoeoties for imodamentaden stess insteg besow.
Ineicate dates as accurate'y as oesnese. (see 6nstructionsg, imosomentation Stoos
- 2. Schecuse (YrA/Cav)
- 3. Actuas comotetson (Yr./Mo./ Cay)
P wu=====
- =====m as NWW 9444 COrnoem 20h i
r
' 303a-r i
ch i 7m i
i i
- h. N pian maernession
,342 3 S.? I
- ? ' h*'
- saae, i
i
'sose.
- e. Maas psan sannosete Lii.s 24r;'
O. maancine somosete a centros awarded soze r
i
- aosee i
- ?2 N'TQ J ose.
r i
3
- e. Site acou 6ted
!sede r
i
?!?.
{k.k i
e c 3nse r
i
- f. esean action (s% constistront
.sc2e M T; Af;f I.h >
r i_
- 3. End action (th sonstnictlent
'302s; e
i
' Li'
(
??M r
i
- n. Casenerge regen soms i
i
+ soars.
g ~s i Cj'4 3
i i
Isospe i
i
$ 02tx L Coorstaenaalevas attained h
h e
$P' '
+
a IU"3 sPo ses. rat IP A F.r. 7553= t3 CA 1456 090
FOR.4 APPROVED QM8 No. LJ8-R0200
~.
l FOR AGENCY USE l STANDARD FORM C -MANUFACTURING AND COMMERCIAL.
ll SECT 10 NIL BASIC DISCHARGE DESCRIPT1CN t
e no.ete inas action f or =e= esenar,e enecatoe in s.cuan s. itom g. tnet is is surm, wsteri. Tnes inctuca ancna,g. ta neuruenue aw. go systems in wnsen the westewater goes not go tnrougn a treaunent worus ortar to oeing cassnarM to surface watert Olscnarges to wesis must the aestrioeg wnere there are asso discnarges to surf ace waters from tnes facJilty. SEPARATE CESCRIPTIONS QF CACM QlSCNARGE ARE REQUIRED EVEN IF SEVERA6 OtSCHARGES QRIGINATE IN TME SAME FAC3LITY A:t values f or an enasting gescnarge snou64 oe r*2re=
sentauve of the twave crewoous montns of eserasson. If tnis la a proposed decriarge, raaves snound reflect Dest esigsneering astarnates.
ACOsTIONAl. INSTRUCTICNS FOR SELECTED ITEMS APPEAR IN SEPARATE INSTRUCTION SCQKLET AS sfvDICATEC. REFER 70 SOCKLET SEFO RE Fit.LJNG CUT THESE ITEMS.
3.
rh*==ge sertas No and Nanus LT
_22h-
- a. o.senar,e seNai N (see irtstruCtional ww Rai:: fall Ru::0ff tc Bull:ek C:eek
- m. ossenarge Na=.
- om Give name of essenerge,if any.
( 3 ec"~'ui*a )
(see instruct 44ns) yf TO C.
Prov6ees Olsenerte Serfad Me.
af orsv6eus permet aoosecation was made for tnis alscaarge (see ES1s 1
Itern 4. SeCtlen th provsde provt=
ous dissnarge sertaa nutnoer.
2.
Desenerge OperatAng Cates
- a. 0+senarse Segan Cate afthe ehenarge oescreoed oeaow is an operation. give the date (wetturt 202.a.
nest estimates the etscnarge YR Mo engan.
D. Discnarse to sesse cate of tne docnarge nas ne=er occurred out es paanned for some future care.
202b
'M yve tne cate (witnen nest estk YR MO matel the cascnarge west oogen.
p.
- c. Disenerve to End cate if dis.
cRatge te sCneouted to os obscorm 3
unued wetfun tne next 5 years.
202s yve ene cate twetnen oest esth YR MO matal tne cascnarge wete one, 3.
Engineersag Resort Avaeaaste Check of an engineering resort is avastante to reveewing ageracy ucon r=tuat. cue utruct.ons:
2cs.
C.
4.
oeuna,,e i eaa Narn. tne godaticas bouncartes witnen wesen Agency use tfle podret of destnarge as located.
Michigan state 2o4.
- pe County 204o 204e wew of moneicanies C:ty or Town 2o4 2ose s.
oisenar,e ee.nt cesenecen o,s r,e.s.nto.,.c. one,..
(see enstructionst l
Strearn (tricsuces altcfies arroves j
ana ener intermittent watercourws:
2nsa 3sTR I
m.
cm Ocean CCC::
Munecioa Sanetary wastewater 1456 091 1r.nse.rt s.sr.-
c
%s nacloas Carneined Sanitary and u
Storm Transoort System CMCS E P A f orm 7530.'3 (7-m 7'his section contains 9 paaus.
4 e
osSCHARGE SERI AL NUMSER ofjh POR AGENCY USE Munessoaf Storm water Transport System CSTS wese (Iniectient CWEL oiner CoTw e
if 'ottier" is cnectati, specify 2054 6.
Oteenares e M = bel /Leng Olve tne precase locanen of tne oosnt 98 elscnerte le f ne nearest seCone.
k3 "Ea 12 MtN E!5EC Laatuee 2es.
O =Em
'.l_u i m
'" *EC Lon tuoe sm 7.
oesenerg Reese,ent Wwer Name Name tne wateSep at tne poent 207s of eascnarge.(see instructions)
~'
..- s
- ~g:
Pop Agency Uge
+4f tne essanarge is threven an ous.
For Aeoney (Jte 203e fail inat estenes De/ene tne snors=
.2079L l
Mne er is Desow tRe mean iow i
water eine. comotete item 8.
~
L
'1 s.
oefsn.re oi.ener,e 7;9 0
4.
04ssnarse Destaess frem Snore -
20sa.
'est
- h. Dissaarge Lesta Beiew water root 2cem.
DV*
Sertase l2 9.
06sanerte Type ane Ossurrense
- a. Type of D6senarge Cneck wnetner tne eisenarge is con-2trea.
C (coni continuous etnuous or intermettent.
(see instructionst C (latl antermsttent i r.' ;
b.
Ossenarse caeurrones cays per ween Enter tne average nu.n.
20s>
bays per woest Der of asys per ween tourtag perseas of oisenarvet taas ela.
snerge occurs
ing tne year wnen ene assenarse is ooerating. (see instrucuanst Carno#ete items 10 and 11 If Mater.
motste.h-is snecmee la item ga.
C*nerwese, oroceee to 8 em 12.
,j h?xu
- 18. setennettent Cessnarge Quantity
'fariable State the average voeurne per ots.
21tr
+nousane gassons rer ciscnarge occurrence.
cnarge accurrence en tnousanos of
$444 ens,
- 15. interniettent Casst.arge Questeen ame Presueney
- a. entermettent Ossanarge curassen
'/ariable Per Day State ins average 211e
=ours por eay memoor of nours per say tne a
eencnarge as operatang.
j 0.
latermettent cessname
- /gyigbig Freemenev State ine average 211a
=essnarge occurrences per aay numoer of descnarse occur.
rentes per day Gunnq cays wnen chcnagging.
- 12. Masamune Stew poeie. Gwetne tense corone in wn=cn ene mamemum 232 From v U to e, 1
4 00
' tow es ines ensnarea occurs montn montn l
V V/
rna www nso.n a in g g,3
FORM APPROVED CCh oug ya. ng_,aagno FOst AGENCY USE l t
7"IU Y111 ~1EO YI-OOl*i?OI*d Y IOOf dIIiUS "IId oc st on o sty 213e proeucang tnis eisc.narwsae instructaonst
'7tri irging, '#,,11 be dischspred 'ris 3 O!==; gngars to Bullock Creek
~
14 Aetenty causasig 06sasha#Te For esca SIC Case wnsen cesences the acuvaty causang this eiscnarge.
suspey the type and maximum amount of et;ner tne rsw matenas consumee (4 tem 14ap er tne erseuct peoeuced (stem 1400 in tne unats specified in Taose I of tne instruc=
tion Goossaet. For Sic Codes not 1&sted in Taom I. use raw maternas or peoiduction units normassy used for measursag preauction.(see lastfuCtions)
- a. Raw castennes IAamarnum Unit Shared Otscnarges Sic Code Name h / Cay (See Taose O (Senas Nummert 214eI (1)
<2) 4 (3)
- 46-
+
(S)
NA l
l l
l I
I I
I I
1 I
I I
I S. ~ ts saamamum unet Snared Cesenarges
$4C Case Name Amount / Cay (See Taose si f5ertas Numoert 21e 1) i
<71 e
en
- a) es)
SA l
l l
I i
l l
I I
l l
l l
i P00g0ii3}!h gg erAr-nso.:w.m II.3 1456 093'
a essexAncs sens AL.Nuusan OCh a3mAosNcvuss l
s is, waste Aaatement
- a. weste anewn.ene pruuse.
cancrine ine wmee. etement a s sa.
Naname
^'##"[
7""
- '^"'
"*'" '*" ~~'*""
s
["n"**,*,,",,"*,*",,'"1 '(*,e,"#"*
of runoff and near devaterinz opersti:ns to centrol instruca ass s11tation.
Rio-rse apelied at chances of e-ade
['Ac and chanzes of direction to siev vater velecitr, f.,Z.;
minimitinz erosien and siltation. bbankments (I
seeded, fe n tli:ed sad -"' ^=d
- ^
- ^a**^'
sail h i!
q,-
erasion.
T,4 3t
-pa;
-t*,-*
e; s
-% rr 9 m.:.4 kS~E Wd*
-A,. %
a,
PSEDDf
- a. Weste Anetement Ceees 2YTSk (1)
(2)
(3)
Using the codes listee in Tanae (3)
(1)
H et the Instruction Boomset.
(4) eescrime tne waste seesoment processes for tais essenarge en (7)
(s)
(3) the steer in wanca tney occur w possas (10)
. (11)
(12)
(13)
(14)
(IS)
(16)
(17)
(18)
(21)
(19)
(20)
(22)
(23)
(24)
.)
e u"
1456 094 m,e.m,us u.n,
FORM APPROVED CISCHARGE SERI A4.NUMSER OMS No.153-R0100 00h POR AGENCY USE U"able ta esti::". ate.*
Is. wastewatee Caaracterestles Chesu tne som besaae eeca conststuent wnsen as oresent in the eartuent tatscnar9e water). This ceterrnanation is to ce nas.as on actuae anasysea es ness entsenate.tsee anstructionsa Parameter k
f Psramoto 2162 2%
a.
a.
C "or Cooper 00080 01042 Ammonu troa 00610 01045 Orgatus natmgen Lead 00605 01051 Nitrato Mags m un 00620 00927 Nitrite Manganese 00615 OtM5 Phosphorus Mercury 00645 71900 Sulfate Molybdenum 00945 01062 Sulfide Nickei 00745 01067 Suff1te Scienmm 00740 01147 i
Bromide
$dver e
71870 01077 I
Chlornia Potasnum l
00940 00937 l
Cyanuts i
Soamm l
00120 1
00929 i
Fluorzie Thallium 00951 01059
/ tummum Titamum l
0a'05 011J2 l
Antimvay Tin 01097 01102 Arsenac Zinc
{
01002 01092 I
Bery!!!um Algte: des
- 01012 74051 Barm m Chlormated orgasue compounds
- l 01007 74052 l
Boron Festledes*
(, a022 74053 Cadmium 00 and g: case 1
01027 00550 1
Calcium Phenots l
009t6 32730 l
Cobalt surfactants l
01037 33260 l
Chromtum l Chionne 1
01034 I 50060 i
Fecalcaliform bactern Radioscovsty*
74055 74050
'Specfy substances, compourdis and/or elements in Item 25.
Festtexics(insecticxies, functc: des. and rodentic: des) must be reported in terms of the acceptaole common names spec 1 tied in Accrotnote Cammon Namer and Ocmical Names for rne intredient Statement on
/carrale 4detr. :nd Edition. Environmentas Protection Agency Wumnyton. D.C. 20:50. J une 1972, as requurd by Subsection 162.7(b) os the Regulattuna tot the Entorcement os ths Feder21InsectN:dc.
I Fungicide,and Rodenue:de Act.
11-5 EPA Fwa 7550.:3 (7 73) 1456 095
e i
OtSCN ARGE SERF AL. NUM8ER 00h Folt AGENCY USE
- 17. Deserts Jee of Intaae see Cissnarge For eacn of the parameters stated Deew. enter in tne soproortate nos tne value or co6e letter answer called forJtee testructions) in acettion, enter tne parameter name and coae and all required vasuca for any of tne foHowing parameters if tney were enecmed in stem 16s ammensa, cyaneae, asununum arsemc. corytilum, caem>m. cnromium. cooper. Isas, mercury, necmas. sesemum. zinc. openois, one and grease, ans cneertne (resleua4.
MW1 IAduest
.2 2 ; I
- s
= sm s
3 I
!E$ I b
$Ed s355 1
E Faramettr an4 Code
^
3 i ti4 2
!?? u, 122a a s
- w
=
3j 3: 33 I=
42 i I
I Js 1J 2
f" j= a=
3.x ML4 T'
3
$8054 5805 C <]
$ <2 a
=
E
m
j
$5E 23B ;
' 0)
(2) l 0)
(4)
(5).
(6)
(7)
(3)
Flow
- I I
G=8*** tad *r MD 0.0h09
[ 0.Ch09
- 0. Col 2.13 5C050 e
pH j
Units (a) j (a)
(a) mg Tenperature (wmter)
'F (a)
{
(a) 32 (a) 740:3 l
Temperature (summer)
(a)
(a)
(a)
(a)
Blochemica! Oxygen Demand (BOD 5 day)
=5/3 (a)
(a)
(a)
(a) 00310 l
CremscalOxygen Demand (CDD) met (a)"
(a)
(a)
(a) 0034o Tot 215aspended (nooditerable) 8" (a)
(a)
(a)
(a) miti 00530 Specific Conductance I
micrombos/cm at *.5* C 00095 (a)
(a)
(a)
Settkable Matter (resdos) i
(*
("
(*)
45 9ther discharges sharu g intake flow (scrul numbersMses insuucuons)
(a) "nable t0 p:'edi ct.
e t P4 Fen. 733g.g (7,q ll-6
/ n L
/
FORM APPROVED CMB No. !$3-R0100 CISCNA ACE SEMIA4. NuusEA ggh PCR ACENCY USE
- 17. (Cast's )
Inauen Emuen i
=
0 1 I I I?
Parameter :c:t Code I
!E E,
h
=3cN.
[-
Ss,3 c 1
=
x s-r a=mye a
,Fi s <
8<
,e
" -2 3x 4
S a
e
!k E
k s
(
DD C 23=
a sowa<
sown w<
2<
n i
(1)
(2) l (L
(4)
(3)
(6)
(7)
(3)
I y3 i
t i
i I
I i
1 S. Mant Centrees Check if the foe.
aft doeng plant contross are ava6140se i_7.,_
for this discharge.
=..?*,
Alternate power sourts for mator O APS pumoing faculty.
17
}{A C
C AWA Alarm or emergency procedure for power or equipment f adure pf,
Complete item 19 ff discRatge is
~jf.
from cooient and/3r steam weter generation and water treatmeit additives am usets.
- 19. Water Treatment Additives if the diaCnerge 6s trasted weth any Cof>
4.'iloner. Inaugeter. or algacice.
answer QS following*
- 4. '.'
None
- a. Name of Matertad(s)
~2194,
's*.
s
- {' Ts.
- n. Name ano aaoress of mano.
3; rar.turee use I^'
C.
Quantity (Dounds acced per 21Ss fntillon SMions of water treated).
~~
'1456 097 na m..- m.-
-n,
e e
DISCH ARGE SERI A&. NUMBER COh FOR AGENCY USE "3
d elemical composillon of these Se ae644 eves (see isttruct!ons),
w Carnesete items 20 25 If there 14 a thermal cassnarge
(&&. a**ard a*ae witn a stearn ane/or power generation osant, stees nues. petrosevne refinery, or any otner manufacturing process) ate tne totas discnarge flow is le maisson gastons per say or morew (see 6nstrucconst r-
- 28. Tnerreas 06senerge Seures Checas 221h the aeoroortate item (s3 Ino6cating the source of tne elsenerge. (see Z,,, g lastructions) j soser afowdown C St.80 soon Cnemma c.an*g R
C sCCs.
Asa pone c,=ne.
Ei$
CAFoF SoNet Water Treatment = Erapore.
M CEP90
~
ter Dtoweown syf,*},'
011 or Coas Fires mants -Etnuent M^%
CCCFP.
frone Air Poslution Contros Cevices r .c, Candense Coos 6ng Water
-3 CCCNO Coeung Tower Sloweown f 15.$
CCTBD
- _r Manufacturing Precass C MPpst M, -.c-C OTHR Other e
f%
- 21. Descharge/messevens Water Temper.
..e.
asure Ottfevense rQ Cave ene manimum temonacune elf forence thetween tne alscriarge and recoven, waters for summer
.; 3,
and wanter coerating conestions.
.,y, (see instrucuanni (a) og, IS (a) op.
- winte,
- 22=
j.!N
- 22. Casanarge Temperature. Rate of Change Per Heest pg
'F./hout Cave the mam6 mum posseele rate of temperature criange per hour of
'A acnar,e unew ooeraung coa.
',. ~ (a) Unable to p: edict attions. (see instructions)
- 7..,.,n
- 22. Water Temperature. PereentHe mooert (Freemeney of Oesverensel la tne taose oesow, entar the temocrature wesen is excessee 10%
et the year. 3% of the yest.1% of the year one not at an (manianum yearfy temocrature). (see instructions)
Freevancy of occurrence i.@'
tog 6
5%
1%
' Mantmum
/. i e, l /. i c -
- a. Intame water Temoerature
- 222a, o
t)
- w f,i *sr
<=e=t to aaiuria enen*==>
( a ) e,, l ( a ) o,,
( a ) o. ; ( a ) o,,
115 Otscharge water Temoerature 2221s 24 Water intasc veseesty 224.
A
'est/ loc.
(see instructions:
7A
- 25. Notensten Time Give the lengtn of 228 minutes time. In minutes. from start or water temoseature rise to alscnarge of coesang water. (see 6nstructional t9k Fem 1~.%23 0.731 11-8 1456 098
FORSt APPROVED QMB No.138-R0100 CISCHAAGE SERIAL.NUM8E A POR ACEMCY USE l
- 28. Assamenes soformecea 223 item information e
t e
__6 6
9 e
e e
e m'
W tra r.,a 75:o-:2 a-in 11-9 1456 099
e FORW APPROVED e
QMB No. US R0100 FOR AGENCY USS
^
.e 4
STANDARD FORM C-MANUFACTURING AND COMMERCIAL SECTICN III. WASTE ABATEMENT HEQUIREMENTS & IMPt.EMENTATION (CCNSTRUCTICN) SCHECULE 7tus section reeutres information on any uncomotetee'Imotementation scneouse wnsen may nave seen imoosed for constructlen of waste amate.
rnent facasettes Sucn recuarements ano irnosementauon seneouses may nave Deen estansinnee ey tocas. State.or Feeeras agencies or ey court acuoes In acoltion to comosetsng tne fossoweeg stems. a cooy of an offic.as imosomentation seneouse snouse ce attacned to (nes acoucatson.
P YOU ARE $USJECT TO F.VERAL CIFFERENT IMPLEMENTATICN SCHEQULES. EITHER SECAUSE CP QlPPERENT LEVE1.$ CF AUTHORITY IMPOS6NG P: FERENT SCHECULES (item 14.) ANQtCR STAGEO CONSTRUCTICN OF SEPARATE QPERAT!CN UNITS (item Ic3. SUSMit A SE'
'.TE SECTICN lil FOR EACM CNE.
FOR AGENCY USE
~
1.
Isnoreeements 344-SCHED.NO; '
- a. Cassearge Sartaa 'aummet Affected t.at toe etscnarge 301e eerses numoers, assagnee in Section 11. tnat are coveress Oy 2-trusJmosomentation seneouse.
b AetAerity Imeeting Reeutre=
monts Cnecis the sooroonate Itern (noscaung the autnority for imoeementation seneouse, if tne seentaCal Irnsiementation seneoute na$ seen oreerest Oy
'J more tnan one autnestty, cnecM fo ine.co,oon ii.,n (se.
y instr==onc
,, ~ ~
mm a@
J 10. @j_ )(
"A fl i.c ody es.a. coed,uss
- ain, CLeC D
D 1
J Ar=-wa =
c CAaC
,o o J
o y
- CsA, soie,un sim acom.e i,no.ementa.
tion SCAesiu6e u* b CSQ3 C
red.e,. aooro.ee.w.t.
ou. y stanea,e. mo,e.nonta.
CWQS tioso plan.
rede,. enfo,eement omese.
oraeuen g.
CENe stata court orew J
CCRT i
CrEo reens cou,t oren n
- c. Feettity Rosettement. Soecify me unmer., coes of inose unusetw
~
(generall floted below tnat Dest descritpos 2.,f in generas terms tne recuare.
,nent of in. in,oi.,n.nauon seneeuie and tn. aoo.caos. sa.
cnaracter anatoment coce(s3 from Ta.3de 88 of tne anstruction necesset. if more inan one 1331e Maracter scneeule apotles to tne fatality
~=-4 (spectffel because of a stagea construction (W T2888 383 scnedusa, state tne stage of con.
w struction noeng desertons nere watn the sooroortate generas action code. Suomit a seoarate sectson ses for esca stage of construction osanned.
Peeur Facsilty NEW Massification (no increase in capacity of treatmenti MCO lacrease in Caoacity INC increase in Treatment Levee INT Botte increase an Treattnant t. eves and Caoacity ICT 1456 100 process Change 8840
_ natl of
.m.go m
1111 I? P & Pens ;550.23 (7 73)
TNs section containe : pages.
e NA AGENCY USE l 2.
Imosomentaesen Saeeemse and
- 3. Asasas Comeestsom Oased preside setee smoosed Dy scneouse and any actuas dates of Comosetten for imolementaden steos itstee Detow.
Insecate estes as assuratesy as ocamene. (see lastrusuenas, 2a (YF N /08vl
- 3. Actuad Cornesetsese (vrsw%gm
& M % D6antemseeen r*~.',
730m i
i
- b. Final paae suesnession "3423s Wk' T* q
- e. Finas piancampeete 4302er 303e5 s
i
<e-G *,
,",~n s; T
{303e.
r_
s
- d. Finanssng somptete 6. contract awensed 302a e
r
$Rg
- f.O
' 30 s
- e. sie acesseed
- seas, e
e NfrC; it *O2 ISO 3re i
f i
i
- f. Setan estien (awk tonstruction) 3029" 3 S**
'r-Q:
~
I303a.
r i
- g. End actiese (e.h constrhtlan) 302 3 i
i
@4 r,5463
- m. einenarve senn so3m 3eam
- h. hi%
'ASA i
s er302 e
i k Operationalleyes attained name.am h
o
/
J I
(({.2 GPO t o S.7 at EPA Pere 7330 23 (7,ygg 1456 101
E e
FCRM APPROVED ChiB No. 2Jt-ROL00
^
FOR AGENCY USE STANDARD FORM C-MANUFACTURING AND COMMERCIAL l
SECTIONIL BASIC DISCHARGE DESCRIPT1CN t
Comosete tnes nestsen for saca esscnarge enescatee in Section t. Item 9. tnet is to surface waters. Tnts inctuaes anscnarges to munissoas sewerage systems in efteen tne wastewater goes not to Intougn a treatmart wortas prtor to Deeng 4,scharged to surrace watert CasCaarges to wests must lie eescasDeq where tflere are 48so Giscnarges to surrace waters,com tries fac134ty. SEPARATE DESCRIFTIONS OF EACM QlSCHARCE ARE REQUIRED EVEN IF SEVERA4. 04SCHARCES OFIGIN'.TE IN THE SAME FACIL37Y. Alt vsiues for an enasting gescnarge shouad De reore-sentatJoe of tne tweste preveous montas of escret104 If 'Jnas as a presosed esscharge, easues snoued reflect Dest engineering estirnates.
ACOsTIONAl. INSTRUCTtCNS PCR SELECTED ITEMS APeEAR IN SEFARATE INSTRUCTION SCQK1.ET AS INCICATED. REFER TO SCCKt.ET 3EFORE FILL.ING CtJT THESE ITEMS.
5.
Dessaaste Sartal No. and Name
~~~
Mc
- a. 04senarge Sartas No.
291m (see instructions)
';c M.
i*7??
g,;
Rainfall Dumff te TitttMvss9aa **-a=
,,m,,,,,,,,,
Gave name of etscnarge. If any.
(see enetructional
'd
..:=:.
- c. Presseue Otsanarge $esta4 No.
~. W.
If preveous permet apos6 cation
]A was maae for tais discriarge (see Zala stone 4. Sectson 13. ocoruse preve=
eess etscnarge sersas numeer.
s f?$
z.
casseorge o mets.e case.
O
- a. Desenstee Sagan Date iftne descnarge gescribed Detow rs in g
operation, gave the date (witn6n 202a
{} g,I,, }
g t>est estimate) the etscnarge YR MO f.
D'
\\ \\) \\&
3 t
U:g i
s D. Dhtmarge to Segen Date if tne eiunar,e mae ne.er o-.,re..ut 78 3 es paanned for sorne future cate.
202h goes tne date (witnen Best esth YR MO rnate) the descnarge wsil cogst
_ m-
- c. Olsenerge to End Date if dis-cnarge e scnocused to De encart-HA isnuee witnan tne ne=t s years.
2o2.
gewe the date twetnen Dest esth YR MO matal tne distnarge well erMt.
2.
Engsneering Reeert Arsuanie Cneck sf an engineering recort is avestanse to reveeming agency uoan reevest. (seeinstrucucas 202 C
.. u 4
Desenarge Losatsee Name the ossaticas ticunearies inen wn.cn Agency use the point of distAarge is locatesh MiO D E 50U State
-204e Minand 2o4 Co,e,,
2,u.
Midisnd zose of sonescacies C:tv or Town
'2o**
s.
oeunstge point cesenett.n Casenarge einto (eneca oner.
(see instructions) stream unciuges artenes, arrovet "g" TR are otner tntermittent watercourses zosa La..
cuK Ccean CCC Mun csoas Sanitary Wastewater Transoort srstem CMTS 1456 102'
-n.c.c. C.mo.r mtar -
storm Transoort srstem CMCS 11-1 EP A Persi 7330 3 (7.m This accfion conraans 9.cevos.
e OtSCHARGE SERT AL. NUMBER C05 POR AGENCY USE neanscapaa Storni water Transoort syneen a sTs wees (Intectioni C WEL.
Otner COTw 8
ff *0ther" is chectatf. specfy 2934 6.
06ssaarge Poems-Lat/Leeg alve tne precame tocamen of the pot.n
.f cocan,e to tne nearon second.
3 3 "EG
,5 19 *EC
~
LAutuee 2064 MIN 8h EG 13 19*E2 Lanctude
[2 f
J IN 3
- e 7.
Ossenerge Rese#veng water Name Name ins waterway at tne poent 207a Tittakava33ee 3iver et alacnarge.(see lnstructionst W;
-.4
[
Por Ageracy use Per Aeenev Use
=4f tfte cessnarge is througn an oute
'P g g,,
g 30Je fadt inat estenas Devono the snore-
.207D water tene, comosets (tern 4.
- .{
,j
'e
-- [
line or is De6ew tne mean low e
F
'*'f-d
~.r.v"
([<
8.
Offsmers Olssaarge O
- a. Dessaarge Castanee frene Snere
=gsar
'est
?;>
-p
- m. Ossenerge Deets sesaw water Above servase zoam.
rest
\\
gi sl Q', r,. s
,(
ii i;(f
- -q O
9.
Otasmarge Type and Cesurrense g
h, - {u],
A
- a. Type of OlseAarge Cneca
'h D
weestner tne eissnarge es con =
~20Sas C { coni Continuous tenuous or intermettent.
(see 6nstructJonst
.'Il?
@lnt) InPermettent
- t. sg
- t. Otsanarse Oceerrense Days per Ween Enter the average num.
20 San mys per weses Der of days per weses (euring portoes of 41scaarget thas cas-
- "****W"
i
- s. Dassnarge oesurrense-Montas If tnes elsenarge normassy
-209e.
UJAM CFEB OMAR M APst operates (estner intermettently,
~
CMAY QJUN QUt.
[AUG or cont 6nuoussyt on sens Inan
.,e.r oune.aus i.eciusing snuteowns for routane maente-CSEP QOCT QNOV ECEC noncel, caeca tne anontns dur.
eng tne year wnen ene essenarge is ooeretsne. (see enetructionst ue Camosete etomt.10 ane 11 if intoe.
.C mettentIs caecues in ttem 9.a.
3:
Otawwese,proceenf to etem 12.
yJ g
is, sneernuttent Ossanarge Quantity
/E EMe 4
State tne average voeurne oer ats.
210
,nousand gassons per etscnarge occurrence.
anarse occurrence en tnousanos of gaa8ons.
11 laterneettent cesamarge Ceretten one Progeeney lariable latermettent Ca ansege Ouretsen a.
s per Oay State one average 211o.
' tours per gav numast of mours oor say tne elsenerge es operassng.
B. totermettent Distnaeve
'lariable Freemency State tne average 2113
- tscnarge er:currences per aay me.moet of erscnarea occur.
rences per day ownng aays wnen asscnargeng.
\\456'\\
- 12. wassmem Piew perees Give tne g, to ]qq time oerena an wnsen tne mansmuvn 212 From flow es ines encnaree occurs, monta montn e Pa Nw rsse-:2 a_rn gg.,
FCRM APPROVED e
5 w
cug u,, na_aogoo ron AczNCY ust 88^**'"'0"'***
G8"
- o c,,.,.. e b*r,.~., a,. sin s aanauw eescriouen et actNity atse
- 14
,e,,
.L s,
--. a
- - - - - - - ~---
eroeuen, inis essen4%ise v.d 'rsr4 drsins, vill be dischsreed ria ster:
anatructica*I savers to *he ficod 1 sin sheia the Tittsbavsssee River.
- 14. Asuvity Causasst Dessaarge For nach SIC code wasn concrteen the activety causing tnts discnarge.
supory tne type and mamarnung amount of either tne raw mater'as consumee (item leal er tne product J @ pl D produced (itern 14el in the unets r
Jiij,Mj flg,_s,e, p,m1 eeme.inra e..,ineia= =
uan eo.= set. re< sic Caan not s
{ d {J U.
A listed in Tanae 8, use raw materaad
, j 'k ;/}
e j
U <.
Ll er production units norma 68y used for measuring production.(see instructions)
- a. Raw htstersade 8Aasimum Unet Sharme Ciscnarges SIC Code Nome Amount / Day fSee Taade 1)
(Sortas Numoer) 21 (1)
I (2) 6 13) e est-
'S)
I M
1 l
~.os Adamarnum Unit Shared Olsenarges Sic Case Name Arnount/Cav (see Taose il (Sartat Numeer) e (2) e all I
(a) 85)
Sie (1)
'IA I
I I
I I
I I
I I
I I
1456 104 EPA Fe= 73%n (7.n]
Il-3
e e
CISCHARGE SER A4. i4WM cE R OCC POR AGEMcv USE
/
tS. weeas Anasement 8'
" * " * ^ * * ' ' * * * ' " " * *
- Holdin.1; pcnds in ditches near any source of r*Jr.-
Demente the waste amaternent 21Se Narrattwee oracticas uses on taas etecnarge off and near devatering crerstions to centrol silla-tn a oner narreties, (see i nr.:cami tien.
Rio-rte atelied at chances of direction and chanaes of artde *c siev vgter.f.,mei..f.
.4
.u
,.s<
Si3f 2 arSsien tnd silag. den, y, g, 9
[,
f*Mili2*d sad -'il?hed *S cc**rcl soil arcsiaa.
Tij f x.y
.~-.a A.
w
-ns TiW;
- -r.. -
~;.,
m%v;
- 'ra ESPAE ISEUI'd
- n. weses Amatement c ee.
'itsh' (13 (2)
(31 unene tne coees sistee in Taose it ofins Instruction soomies.
(4)
. (s)
(s) eessnee tne weste sostament
- for enes essenarge in (7)
(s)
(s) tne ocear in wnsen tney occur if *****e.
(10)
(11)
(12)
(13)
(14)
(ISI (171 (181 (le)
(20)
(21)
(19)
(23)
(24)
(22)
(25) 9*
M5 m e-m m -.,,
FcitM APPROVED OsSCHARGE SEAf At. NUMSER CWS No.153J0100 07 POR AGENCY USE ts. wastewater Caarsstartsstes Unable to eSti:: ate.
- Checss tne som nessee esca consatuent weten is present in the effluent tow.go waters. This caterminauon is to be cased on actuas anasyses se east osumana.4 sea sastructionst P:rameter Parameter f
216i 4
214i a.!
a.
Color Copper 00080 01042 Ammonn iroa 00610 01045 Organc natrogea Lead 00605 01051 Nitrate Magnesium 00620 00927 Nitrite Mangnesa 00615 01055 Phosphoras Meretary 00665 71900 Snifate MotytMenum 00945 01062 Solfide Nicket 00745 01067 Saffite Seteamm j
00740 01147 i
Bromsie Silver 71870 01077 r
Chloride Potassium 00940 00937 Cyannte Sodium 00720 00929 Fluotuis Dia111am 00951 01059 Alununum Titanium 01105 01152 Anumony Tla 01097 01102 Arznic Zinc 01002 01092 Berytilum Algicdes*
01012 74051 3armm Chlormated orpruc compounds
- 01007 74052 Borce Festtentes*
01022 74053 Cadmium 00 and greams 1
01027 03350 l
Caletum Phenots j
009I6 32730 t
Cobalt Surfactants 1
01037 38260 i
Chromsum l
Chlonne l
01034 1
50060 1
Fecalcaliform esctens ibdioscuvity' 74055 74050
- Specly substances, compounds ar.d/or tiements un Item 26.
Pesticides (insseticxies. funcic: des and rodentiedest mtist be reoorted in terms of the accret204 common names spcasied an Accestcole Cammon Namesand Ocmicst Names tor the increcient Surement on ferrarate L.thefs. 2rh1 Edition. Environmental Protecttun Agency. Wauiington. D.C. 20:50. J une 1972. as requurd by Subsecuan 162.71be os the Repalanons for uns Eruorcement us the Fvder::d Insecu b1 j"k p %
h)
Fungicide,and Rodenue:de Act.
i 1456 106 55 m,_ 7m.mr.,,
04SCHARGE SERF A4. P8UMSER FCM AGENCY USE
- 37. o neu
.# i.e. a. cinna,e.
c t,
t
.t
...w..m
,n(n.a.
t..o.en..
.,c
.n
,c.
e,_,n.t. vet.n.,
in assgat.n..nt., (n. pa fn.t., narn. and cod. and all. uw.J watu.s f e, any of tn. f.II.weng param.t. lf tney w.r. en.ca.d.n it.m 16s ammen a. cvan.a= sununum m.n.s. e.,ymum, ummeum, en onneum, coco i.
mercury. n. cam. = n.um, nnc. an.n s.. ana,,
and enf tne (r.saguask Infhaest i
E'Duent
=
4a 1 ;
1 I I Ii 1
s
-c 3
i s.5 w
>3c
$3 Farameter and Code 23 a
1 M
l*
$ k h, l!II jl
!i 5k i as Ess 33bt
- #E il 11 5
-3ge sse.
d now5<
2dwa w<
z<
a (1)
(2)
(3)
(4)
(5).
(6)
(7)
(3)
Flow
- l w r MOD 0.009h L 0.009h 0.0001 0.h9 50050 pII Units (a)
(a)
(a) 00400 Temp.raoue (water) l
- F (a)
I (a) 32 (a) 74023 l
Temp.ranne (sammer)
I
- F (a)
(a)
(a)
(a) 74027 BiochemicalOxypn Demand I
mod s-dar)
(a) 1 (a)
(a)
(a) ms/l l
00310 1
Cienuca10xygen Demand (CCD)
I mWI (a)
(a)
(1)
(a) 00340 Total Suspend.d (nonstarabl.)
N (a)
(a)
(a)
(1) mt/l 00530 I
Sp.cfic Conductance nucromhot/cm at15* C (a) l (a)
(a) 00095 Settleabis Matter (rendue)
(a)
(a)
(a)
(a) 00543
- 0ther dischstges snanng Latake dow (scrui numbers)4sce instmctions)
(a) i;nable to pret.:t e
,,,..n,,. n, as 56 \\9y
e FORM APPROVED CMB No. U8-RQl00 OtSCHAftGE 3EJt AL Nguaga 3C4 FOR AGENCY USE l
- 17. (Coas*e.)
e Influent Emuent r
7 3y l,
a se 1
w s
y a
>3m
>a a<
Paranwter and Cods x
3 g
IIIi N
!$5IE EEI
.5 5, 5
. s=
24-i = ts i
= = ta r
al i
sii 23$ '
s 58Q54 3805
- 1 a
l c)
(4)
(5)
(6)
(7)
(s)
(1) a)
l l
l Ud I
l l
I I
I l
l l
I l
u l
l l
l l
m-
- 13. Mant Centrols Cnecas if the fos-21 0 fewsmg plant controis are aweelande for ?Mes alscaarge.
Atter'iate power tource for maior CAM pumosag factilty.
- !(;
7A Alarm or emergency proceeure for QALM power or equiprnent f aalure
?
Comosete item 19 af stacnarge is from coosing and/or stears water gefterttlon and water treatrnent a4341tivet dre uses3.
- 19. Water Treatment Adestives if the essenarg is treated witn any con-ettlener, inntestor. or asgecace, f 'f answer tne fotiowent i r. '
,g y
a, Mame of MatertaiO) 2I L S
- e s.e h,
Name and 44Gre t of manu.
'JA facturer 219th
- c. Quantity (pounds accea car 213e mellion gassons of water treasee).
?00R j3hlI8 1456 10B 117 EP A Pene 7330.*3 a.73)
e-0 OISCH A AGE SE A 8 A4. NUM SEA 005 Poa ^****v USS I
/
W
- 4. Cnemesas comoseedon of tnee 219e adottives (See lastructionsl.
w Comosete stems 2C 25 If tnere is a enormas distnarse (e66. assassated weta a steam ane/or power generatson osant. stees mast. petsoseum refinery. or any etner manutettureng process 3 and the totas alscnarge flow as le mslien gassons per say or more. (see instructional
- 29. Thorinas Olsenerve seures Check 22F tne aeoreertate stemts: Inetcating the source of the etscaarge. (see
,.(
lastructienst
}','Q
[ ag.go Seder Sloweown esser Cnemetad Cesn6ag a..,
C BCG Aan Ponse Overflow N*
CePOP Somer water Trestrnent = Evasors=
C EFSO tar esowsown
,-g,
Ost or Case Fired Plants = Effluent CCCFD froro Aar postuuon Contros Coveces Caneense Coeseng water C COND Coosing Tower esowdowat OCTED 7.'-~
C MPrat taanufacturing process
~t Otner M '.
COTHA
- m.w -.
- 21. Otsenargernessevent water Tee pet.
sture Otfferenes
.(f Give the massmum temocrature a.
olfforence netween tne eissnerge j
and receiv6ng watert for sumener and winter ooeraung renettions.
(see instruct'onst Ia)
,22 4 op,
^
\\ S ) 'F.
l.:.* 4 winter l221h
,Qv
- 22. Olsenarve Temperature. Rate of a
oF hout Change Per Hour 222"*
1 Give the mamemum sonstede rate of temaerature cnange per nour of s'
assenarge unser oceraung eon.
Q (g) {I:11 Die to p2"Sdict attlens. (see instructheist y
Q
- 22.
- vater Tameerature. Pereentile neoert (Preemeney of Oceurrensel la ene tasse sesow, enter tne temeerature wasca is escaeeed 10%
et the year. 5% of tne year.1% of the year ane not at a41(maatmum yearry 'emperaturel. (3*e Instructional Presuenry of oceanece
~4 pyg i sg i
1%
i wassmum=
ze,.' -
/ g ) se l [ g ' ear l IgI oel l 1 I #e
& latame water Temoerature 222mi (Sectoct to natural snangest
{ T ITI ** I I**
I
- 1 b Olstaarse water Tomoerature 222h 24 Water tntame veteesty 224
'est/sec.
(see anstrucuanst
.dA
- 28. notenelen 7tme Clwe the tengtn of 225
"nutes e
time. In minutes. rront st t ' of
- ~
water temocrature rise to eisenarge Of teeting water. (See instructionst 1456 109 1I-8 tPA tem ps30 23 W-73)
. =
FORM APPROVI?D CMS No.138 R0100 OssCHAnct SERI A4. NUMSER FOR AGEreCY USE 005 as. me. e ine.cm.u.=
228 st-n l
rnform uon e
t w
e e
w e
e I
l EPs F-= 755e.: g-m 11-9 1456 110
. =
FORM APPRQVED CMB N 138 R0100 rCR AaENcv uSE l STANDARD FORM C-MANUFACTURING AND COMMERCIAL SECTICN III. WASTE ABATEMENT RECUIREMENT3 & IMPi.EMENTATICN (CCNSTRUCTICN) SCHEDUL.E rnee.=n reew,= intarmau.c on any unc aw'im..em nu.a un. awe nia may am n im ror construcu.a av wate a.t
,nent vuusu.a. suca re
.,emana ane. em.ntae.n un.e may nm seen nu.isa ny i.cu.staie.., F.e.ru non...t av.cau.rt cou nu.n. in aceinen i commenne ene va.
- n. to.
e a.v., an aerium im.iemenau.a un we snome ne anacned t (n......
a.
IF YOU ARE SUSJECT TO SEVER AI. 34FFERENT IMPt.EMENTAf tCN $CNECQt.13. CITHER SECAU$E CF Cf# PERE.NT t.EVEL3 CF AUTHORITY IMPCSING OlFPERENT SCNEOut.13 (itern la.) ANC/CR STAGED CCNSTRUCTICN OF SEPARATE CPERATICN UNITS (ttom Icl. $USMIT A SEPARATE SECTtCN let PCR EACH CNE.
FOR AGENCY USE
~I 30e r- -
t.
- 2 I;;rtur. raw -
- a. casenarve senos Nesn or Arvatee uit tne eium,,e ut.
enia.noort. nu,nw in sece
- n. mat ar.coverse my twm entauen uneau.a.
f
~
- m. Aeta.ity im. awn, Re.wre.
Itent inescating the autn.nty for men. Cn.c= tn. aor..mto len.serpentatl.sg senes%de, if tne esentscas ten.sementatten T
uneewe am no.n er. ores av O
D g1 t
t q
.nore in-on. a tnonty, gn-=
x' W[
8 O. {
s r"7 tne teor etate eten.s. (see
(
>u -
i g,
t esvo.
.un son C CC 9q CARE A,se. se Pian
{pf CSAS alas. Ptaa State as.rowse imoeementa.
.]
C5CS ts.n senaeus.
- -c ;-.
Federes apor. wee water Guas6ty stancaros orn.eernenta.
CwCS U.n psan, f ;,,,,
'S' Federas enforcament prosse.
ute er acitoa 7.6 C ENF CCRT State court er.or
.jl C FED Pe.ored cosart aroer
>a-
- e. Foestty Reeseresseet. S.ecify the 3 snaracter cou. of tnose 7, '~ '
3.cnarest ar instee.es.w tnat Sest generi.es (generest la generas terme tn. reautre.
rnese.f the om.s.m.ntation
- sete, sca.euse and tne a. saca.e. saa.
cnatacter anatoment e eet:3 frene Ts.s. el.d tne instruction
'301 s 6 cnaracter Deesset. If more tnan one (s.ecaml a e., eles to tfw f acility
'.,; 1 scneouse a
<- T e...
a sta,.e c.r,et,u
.n tcneente, state tfte stage of can.
y' t.T struct).rt Deang eescrt e nere t,ea r r,at.,er,.
t.
- e..
m.t.s at.
. -~
ts
.....r.4 st.,s.,
7 corestructs.n peannee.
NE9t teser Fecality Mesification (ft. Increate en ca.acity or treatment) 44C 0 trasresse in Caoestty INC
- ncrease wa Treatment t.awee INT Satn increase en Treatment Leves ares Ca.acity fCT 1456
- ,1 Ra
- c~
l E!Imenetson.d Ciscnarge ELA 1111
'"' lS*W M1 T? sis aneti.. cantanne : pag a.
E A
==
FOR AGEftCY USE I I
__..... _. _._,_.m._. _....... _.
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- 2. sensensee (Yvede.,Cari
- 2. Actuas comeneuen (vt.swasc.yp
- e. Pressmanary paan semesew
'sosa e
i
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a
- 3. Phnas os.m x:- ~
',3029 8
s'as,
- e. Pines pee esmos.m
- 342e r
i gese.
i f;"C a~r
- 4. Finanssne esmodate & sentrast sweros.
302a.
s
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C'N e g PpQC flau sysrEM WATER D
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goiLER CLE AN,=j nxtuREs i
y l e
MsTC MA% PLANT
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LABORATORY Q
UMTs L&2 z
C
./3 mruREs CONDENSATE %jj V
i FEEDwATER e m STEAM Ctry wartR systems
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-35 7,p 7
3 s r.w teras _ -
T20M MAGNE FIL ( A $yS ' t T
C l _,
twy WASTE mNT RE ACTOR E
uhTs iS2 LAJPCRV mP FACUTv ss_2%
PLANT sYs7EMw-e SYs7EM Floc 17[a ss-NUCLEAR SYSTE I
I w ATER USA Node I i 2 1 3 l 4 l 5 i 6 i7 l 8 9 t to I
't
{ I? I 13 I Escocted Monimum Flow e iso l sec l rse fios ooof rmpeo'es soc 4arn)\\ 32s d ses '
ss soo h I
asax f 323 'twch o h3poh h
Expected Average Flow
+ 0. 9 34 5t3 itse o
i 'Oc 53Aco h
y Node 31 1 32 33 1 34 I 35 1 36 t 37 38 I 39 I 40 l 41 l 42 1 43 l Espected Maximum Flow l <e nal l
l is c ooobs ooo! 4 4 I 44.scol e.sool.so l e
e ss 4900l Empected Averege Flow os o
.i t
os o
opoci3000 C.4 4 i,3 7
(
6 1
5 1456 112
+ 4 1
3 1
2 1
1 F
ASSEE river l
Dow CO DI SCM AR GE wa,%g s't 31UCTURE ST RUCTURE CHEMICAL USACf I
J hoes Chen= car l Lil/Ve e
A he 0CI 69(NYh I
5
%Ce 6230 :
li 0
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sf w **4mA4e a.su _m q.
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- 5%
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N"s sysrE u NOTES
,, g
_ _ ae gar aat'.o= wAmLq g,,,,,,c,,,ng,,,,n,, and optional fiow s are
~
C08M8nAC l I_
included m fotol f?ow totes.
md'Cof ed by dashed imes Ond are not i
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Y IJ) g
,g yq 4
T C r A$
A$
2 Flow rates are 1000 s of gollons per day.
2
- AS'E WAS TE
_ k( dT 3 Monimurn flows may not occur SWTiuttorneously.
L MP SLAdP
'.O_ C.ooLe4 N 4 See phibos for further description of flows.
{
' ' - ~
5 These chemico's are present m vbe Conto,nrnent
_J
{
spray systems Af ter tre milici Chorgmg of
__I a
these systems,no odditional Consumpteaes e
orifecipoted I
6 Discharges f rom the liquid radwaste
--M L O.J 'O
!?
M C s'j system well be in botches of up to mW45 tE RADwAstE mgorrs+tt 20000 gallons. A batch well aC Cumula t e 9
systlu
-H$ t svT'Ek D'1'058' at a rate of about E00 gallons per day, LOO # _ommet g
peqq.
i A L POOL
,$g a
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---_---_--_-n-3 L-
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g OR gioOybf@n 4 l l$
16 l 17 18 1 19 j 201 21 1 22 1 23 J 24 ? 25 1 26 i 27 28 l 29 30 30 A d3 1.s.w
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.I neI 70 i
SCHE Tic OF WA R FLOW l05 ol0 0
Wu up aa 1.
15 $
e 40 6
6 CS 10 0
L(2'[
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C045vuCR!, POwEs COna* ANT 4
wiDon%D muCLEAR PLAMT 4
45 l 46147 l 48 I 49 I 50 l Si i 52 i S3)i 54 3 55i 56I 57 1 58 1 59 i 60 f
m,ot %n,. ogago vicMi,AN lhl ee I ne l.oo.l758 k5 I h er I.N,! to I a4 O.! 7 o km T,,
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3
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i 1456 113
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LO CATION M AP - G ENER AL ti j j a"
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5 MAP OF MIDLAND MICHIGAN
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CONSUMERS POWER COMPANY I
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N, y
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MIDLAND NUCLEAR PLANT N
G E R S 'O L /L}.u.,~ s A{\\\\
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MARCH 31,1978
'H!A l t i
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La por te.
F%GE 2 OF 3 PAGES mio
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SCALE IN MILES 1
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ei i t s !.' i~ 3-i- -hE 0
1 2
3 4
5
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s CCIISUMERS PC'4ER CO:GA'iY MIDLAIiD PLA:i? U:!ITS 1 & 2 STATE DISCHARGE PERMIT AFPLICATIO:!
FIERUARY 28, 1978 SUPPLE:E C MEID:EC :IO 1 CCTC3ER 20, 1978 i
MCC:EC :iG 2 JUIi2 1, 1979 2
A:EC:Ei"' 2 JU:1E 1, 1979 1456 117
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STATE C P MICHIGAN 4 4450 DEPARTMENT CP NATURAL RESQURCZs 2/74 WATER REECL'RCES COMMISSICN l '.*e V e." * **' 2 DISCHARGE PERMIT APPLICATION 6
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1 (al TYPE CP LEGAL ENTITY (Ch.ek one6:
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A. Muness.es Wow.sw.cw, sen.os, fr.d.c p.r.
C. Mansacturing an. Mlaieg
- e. Aert.vetusse. 'asiu.ing Pien Perm.
O. W'i.re.e.. en. m et.. Te.. c enee camm.reise E st.o.asnmats f et CESCRIPTION CP #9CPCSIO ENTERPRISE: ( **-*bi; I.)
The pre;csed enter;;ise is a two unit ::uelear ;cwer plant. Each unit ::sists of a pres-stri:ed water reacter, a turbine generater, and associated a"-r'-tes.
The facility 1
has a total c =bined ca=eplate rati:g of 1,360 lSe plus 4 :c 1C 1b/hr cf ; recess b
stes=. The electricitf vill be supplied to the applica::'s electrical distributies systes a:d the process stess vill be supplied to The Dev Che:ical CO:parf.
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- 8. t.) BRIEF DESORIPION OF PROPOSED TREATMENT OR CONTROL PAOILITIES (IrhiDiI
?-Ocess Water: Cil separatics, pH af.Justment, settlics and re. dica:tive vaste treat =e :
00:11:r Water: Debris re=cval, recirculating syste= fer heat dissipatics, and blevdow:
flow rate and velocity control.
D =eSti: WestevF.ter: Sanite_y vastes vill be treated and discharged by the DOw Che:ical CO=pa=y, Laundry water vill be filtered.
Lol CES::RIPTION OF EXPE;TEQ OHARACTERISTICS OF WASTE AFTER TREATMENT (B e m.I, onymcsi, en.m.csi,ornert:
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COOLING AND Li.t All AddMw.e (Exhibit V and Figure 1)
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t AFFE:iDIX A A'TALYSIS OF MIDLAND PC'4ER PLMIT C00LI:!G POND OPERATION Introduction The cooling pond has been designed to adequately dissipate the vaste heat re-sulting from the generation of approximately 1300 M'4e of electricity and four
=illion pounds per hour of steam. The pond will effectively transfer vaste heat to the at=osphere through evaporation, back radiation and conduction processes.
The cooling pond =akeup and blevdown operation is designed to centrol the pend Total Dissolved Solids (TDS) concentratiens which originate from use cf Tittabayassee River water. TDS input from the plant operation, circulating water acid and hypochlorite addition and the possible discharge of condensate demineralizer regeneration vaste are not significant. As evaporation losses of pond water resulting from the heat dissipation process will result in total dissolved solids accumulation, the cooling pond blevdown and takeup process will allow for TDS control within the pond o,perating requirements.
1 A description of the basic regulations, assu=ptions and data utilized in this analysis folicva:
1.
Rezulations Discharging cooling pond blowdown into the Tittabavassee River hac two primary effects: Creating a thermal plume, and adding TDS to the river.
To protect the water quality of the river, the folleving rules of the Michigan '4ater Resources Cc mission (L?.C) must be maintained:
a.
Heat load to the river shall nct vars the receiving water at the edge of the mixing =cne to te=peratures greater than the folleving men:hly
=aximum temperatures:
Month:
J F
M A
M J
J A
S 0
3 3
0F:
hl ho 50 63 76 SL 85 85 79 68 55 h3 b.
Heat lead to the river shall not vars the receiving water at the edge of the mixing tone more than 5 F.
c.
The size of the mixing zone is limited such that it does not contain more than 255 of the cross-sectional area and velure of flew of the river at any river transect.
d.
The controllable addition of TDS to the river shall not increase the river TDS concentratien beycnd 500 pp as a conthly average nor scre than 750 pp: at any time.
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ww9 1f4V 1456 120
- i g
a Dow Chemical Company discharges its tertiary pond effluent into the Tittabawassee River about 300 ft upstres= frc= the location of the cool-ing pond blowdown discharge. Both discharges are at the south bank of the river. Dov's effluent also adds heat and TOS to the river.
2.
Physical Assumptions Si=alation of the daily operation and the TDS concentration levels of the cooling pond are based on the following physical assumptions:
a.
Total dissolved solids in the cooling pond come from the Tittabavassee River only. TDS input from plant operation, circulating water acid and hypochlorite addition and the possible discharge of condensate de-
=ineralizer regeneration waste, is not significant and is not censidered.
1 b.
Cooling pond volu=e gain by precipitation is assumed to be equal to the volume loss by seepage. This is a conservative assumption since an annual average precipitation of 30 inches over the pond surface of SSO acres is equivalent to 3 cfs which is larger than the estimated pond seepage loss of 0 5 cfs.
c.
Zio credit is taken for TDS loss from the cooling pond via seepage.
d.
pond TDS is uniformly distributed throughout the pond volume.
e.
The effluent of Dow Chemical Company's tertiary pond is asst =ed to be a continuous discharge having a flowrate of 67 cfs with an excess tem-perature of 5*F and a TDS concentration of 2500 pp=.
f.
2l Average daily Tittabawassee River flows for water years 1937 to 1977 are i
ured in the operation study.
(This assumption was utilized for analytical purposes only. River flow may vary widely over a day due to operation of Sanford Da=.
Operating controls will assure continuous cculiance with the withdrawal schedule set forth in Exhibit II. )
1 g.
The assumptions that the cooling pond is full and that pond TDS is at a concentration of 500 pp= are used as initial conditions for the si=ula-tion of the pond operation.
3 0;eratien Assumptions In this study, the operation
' the cooling pond (timing and amount of
=akeup and blowdown), is governed by the following assumptions:
2I a.
The annual refueling period for each unit is assumed to be one =onth.
Re-fueling occurs in September for Unit 1 and in April for Unit 2.
Se heat D
6 1
load to the cooling pond is 3370 x 10 Btu /hr for April, 5c80 x 10 Etu/hr for Septe=ber, and 9050 x 10o 3tu/hr for the re=aining =enths of the year.
AME:iDME:T" 2 A-2 JUNE 1, 1979
'456 121
b.
Maxi =um allowable blowdown flowrates as determined from the Alden Research Laboratory ( ARL) test program are a function of the river flow and blowdown excess te=perature (blowdown te=perature less natural river temperature). Blowdown flowrates used in the pond operation study were kept below a set of mw'-"- allowable values shown in Figure A-1 derived from the K.lL test program and consider-2 ation of thermal constraints in the Tittabawassee River.
Makeup flowrates are kept as hi h as possible without filling the pond c.
S above elevation 627 ft.
The constraints on =akeup flowrates are listed in Subsection 3.4 of the Environ = ental Report. The =axi=um makeup flow utilized in the pond operation simulation is 270 cfs correspondicg to the makeup pu=ps runout conditions.
d.
In order to simulate pond operation under the =ost stringent conditions, Dow effluent discharge into the Tittabawassee River is given priority 1
over the Midland Plant cooling pond blowdown discharge. The Midland Plant blowdown flow will be controlled so that it will not cause the river TDS to exceed 500 pps.
2 e.
The mav4 m - blowdown flowrate is limited to 220 cfs because of hydraulic characteristics of the gravity fed blowdown sche =e.
The mini =us flow-1 rate is 5 cfs due to difficulty in throttling for flows below 5 cfs.
f.
The pond water surface elevation i= poses the following limits on the takeup and blowdown flowrates:
1.
When pond level is above 627 ft., no makeup is permitted and blow-down may be discharged at its -av4 m - allowable flowr.te.
2.* When pond level is 626.5 ft., no blowdown is per=itted and makeup withdrawal may be made at its caxi=um allowable flowrate.
2 3
When pond level is between 627 ft. and 626.75 ft., both =akeup withdrawal and blowdown discharge may be =ade at their =r.W.u allowable flowrates.
4.
Khen pond level is between 626.75 ft. and 626.5 ft., ma>eup flow-rate =ay be set at its maxi =um allowable value and the blowdown flowrate is limited so that the pond level is not lowered because of the blowdown discharge.
Pond blowdown discharge 1 ter inated when daily average natural river g.
temperatures are within 5( of the =onthly max 1=us te=peratures.
4 Data 1
a.
The US Geological Survey gaging station on the Tittabawassee River is located so=e 4700 ft. upstreas from the Midland Plant river intake structure. Daily average river flows published by the USGS from water 2l years 1937 to 1977 were used in the cooling pend operation si=ulation.
1456 122 McE2:;T 2 A-3 JU::E 1, 1979
a f
a b.
Natural river te=peratures on a daily average basis from October 1, 1975 to Septe=ber 30, 1978 as recorded by the Dow chemical co=pany at the Dow dam were extracted and used to develop a model relating long term daily natural river te=peratures and daily dry bulb te=peratures.
From dry bulb temperatures recorded at the Bishop Airport of Flint, Michigan, natural river temperatures were generated fres March 1,1949 to September 30, 1978 and were used in the pond operation si=ulation.
2 c.
Daily natural river TDS concentrations were either directly obtained or estimated from the natural river conductivities contained in the monthly Operating Report of Dow Chemical Company frem October,1975 to Septe=ber, 1977. conservatively, the hisher 1976 TDS concentrations were used re-peatedly in the study.
d.
A transient cooling pond =athematical model was used to estimate daily average bisdown te=peratures and pond evaporative losses.
e.
A physical codel was utilized to determine the quantity of blevdown that could be discharged into the Tittabawassee without resulting in a mixing zone more than 1700 feet long and not exceeding the 255 cross-secticnal limits for the thermal mixing zone.
Both the Dow tertiary pond discharge and the cooling pond blowdown were si=ulated in the physical model. A = atrix of 275 thermocouples, posi-tiened throughout the model, were used to determine the =aximum allow-able blowdown flowrate for a given blowdown excess temperature and 1
river flow. For all data provgded, the edge of the ther=al plume is based on the location of the 5 F excess temperature isotherm as deter-mined by the average te=peratures obtained from 25 scans of each of the ther=occuples.
5.
Simulation of Pond Oceration A computer program was written for the daily si=ulation of the cooling pond operation. For each day, the =akeup and blowdown flowrates (if any),
pond volume and pond TDS concentration are calculated from known blowdown excess temperatures (blowdown te=perature less natural river temperature) and natural river TDS concentrations. The logic of the program incorpor-ates all assu=ptions and operation rules previously outlined.
6.
conclusions The following conclusions resulted from the sl=ulation of the cooling pond 2
operation based on the assumptions presented previously. Fond blowdown will be controlled by measuring the actual river flow, upstream river temperature, excess temperature of blowdown, upstream river TDS and Dow discharge condi-
- tions, a.
It is feasible to control the pond TDS level by a takeup-blowtown sche =e.
1 Eased on the available data, the operational assu=ptions set forth re-sult in pond TDS concer.trations that are acceptable for the circulating water and service water system hardware.
A>CIDFEIT 2 A4 JUn3 1, 1979 1456 123
I b.
On an average temperature basis, the thermal plu=e shall not cover more than 25% of cross-sectional area or volu=e of river flow at any 1
transect of the river, and its length shall not exceed 1700 feet.
h c.
On a long tern basis, cooling pond blowdown and the resulting thermal plu=es will exist in the Tittabawassee River about 27% of the ti=e.
Fifty percent of the ti=e, blowdown is withheld because Dow effluent uses the whole TDS capacity of the river. Eight percent of the time, i
blowdown cannot be discharged because natural river temperatures are 2
within 5 F of the monthly maxi =us temperatures set by MGC. The pond water level was below 626.5 ft. 2% of the ti=e and no blowdown was discharged. The calculated blowdowr flowrates are below the present minimum blowdown flowrate of 5 cfs 13% of the ti=e, so that no blev-down takes place.
Variations between actual values of the pa a:eters which will control pond blow-down and assu=ptions used in the study =ay result in increased frequency and blowdown rates. The combin'ed effects of the cocling pond blowdown and the Dow 1
Chemical Co=pany discharge shall comply with Michigan Water Quality Standards regarding te=peratures, TDS, mixing zone length and width.
1456 124 ALEGEiT 2 A-5 JUIE 1,1979
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APPI:! DIX 3 Blowdown and Makeup Control System An automatic cancrol system is provided to minimize the TOS concentration in the cooling pond 'oy maximizing blowdown and makeup flowrates.
The frequent changes in the variables, particularly river flow, dictate the need for an automatic rather than a manual system.
The combined effects of the cooling pond blowdown and the Dow Chemical Company discharge shall comply with Michigan Water Quality Standards regarding temperatures, TDS, mixing zone length, and width.
The cooling pond is generally kept full when possible and therefore blowdown will usually be voluntarily restricted when makeup cannot keep up with pond losses.
Blowdown Contral 1)
Blowdown flowrate is determined by calculating the flowrate that satisfies the TOS requirements and separately calculating the flowrate that catisfies the thermal requirements. The lower of the two flowrates is selected and is then checked to verify that it is within the physical range of the blowdown system. Pond level and makeup rate are also checked to make certain that blowing down will not decrease the pond level.
The calculated blowdown rate is then set by an automatic adjusteent c' the three blowdown control valves.
Flow measurement is provided in each blowdown line. Periodically the flowrate is recalculated and reset as required.
1 2)
The blowdown flewrate to satisfy thermal requirements is calculated from the Alden Research Laboratory modi' testing program results.
Calculations can be done for all river flowrates up to the maximum rate tested by interpolation. For hignar river flowrates, extapolation of the test data and proportioning are used to calculate blowdown flowrates.
The measured parameters required for this calculation of blowdown are river flowrate the cooling pond blowdown temperature and the natural river temperature.
If the natural river temperature exceeds the monthly maximums stated in the water quality standards, no blowdown is allowed.
3)
The blowdown flowrate to satisfy river TDS requirements is calculated by dcing a fully aixed = ass balance using seasured values cf river fiev and TOS cencentration, the Dew discharge ficw and TOS concentration, and the blowdewn IDS concentration.
The allcwable TOS river ecncentratiens are 500 ppm as a daily average and 750 pp: as an instantanecus naximum.
River TOS is-=easured dcwnstream at Freeland to verify ec=pliance.
x.Est:.et 1 3
-1 OCT;3ER 20, 1978 1456 126
,i Makeup Control
- 1) The =casured river flovrate is used to select a takeup flovrate that conplies with both the makeup withdrawal schedule and ti maxi =um 1 ft/see velocity in front of the intake structure traveling sc -
.:s requirement.
- 2) The calculated flovrate is established by starting the required number of pumps and adjusting the control valve in the recirculation line to bypass 1
the excess flow. Flov =3asurement is provided to determine both net makeup and bypass.
- 3) Makeup is automatically terninated when the pond is full.
Radvaste Discharge Dilution
- 1) Pond blevdown is used for radvaste dilution when the blevdown flow is adequate.
- 2) Eadvaste dilution flow from the discharge of the makeup pumps will be used when pond blowdown flow is insufficient. Fond blevdown vill be temporarily suspended when radvaste dilution flow is in operation.
AEiDE!T 1 3-2 CCT0351 20, 1978 1456 127
APPE: DIX C ANALYSIS 07 "'ur '"u" MAL PLUME A'O DCW CE4ICAL CCMPANY DISCHARGE INTEoACTION In response to Staff's request of July 28, 1978 for an analysis of the inter-action of the ther=al discharge frc= the Midland Plant with the critice.1
=aterials discharged by the Dow Chemical Cc=pany, the following has been pro-vided by the Dev Staff:
A.
The listing of critical =aterials to be analyzed forwarded to Consu=ers on September 13, 1978 by Mr Robert Basch (letter attached) originated frc=
the Dow Chemical Cc=pany's annual vastewater report to the DUR of critical
=aterials discharged for 1977 Upon review of this listing, the Dev Chemical Cc=pany Staff has infor=ed Consu=ers that the list includes some materials disposed of via deep well injection. Further, the Dov Staff is unable to identify a river discharge (date, quantity or source) for =any =aterials listed in the Septe=ber 13 letter frc= Mr Easch. These =aterials on the list which cannot be identi-fied as discharged to the river ani are not, therefore, reasonably expected to be normally present in the Tittabavassee River are assu=ed to be present on an infrequent basis. If present, the anticipated =inimal amounts of 1
these =aterials should be unaffected by the ther=al discharge frc= the Midland Pcver Plant cooling pond.
Additionally, the Dev Staff indicates that only two of the =aterials, a==cnia and cine, listed in the Septe=ter 13, 1978 letter can reasonably be expected to be discharged during the su==er period. Under vinter con-ditions, havever, the listing may include ten substances as listed belev:
Benzene A==onia Pentachicrophenol Dichlorophenol Class 2, h, 5-T Trichlorophenol Class Styrene Tetrachlorophenol Class Hexachlorobenzene Zine 3.
Review cf scientific literature regarding the potential interaction of thermal adaition to those =aterials listed in the D:iR September 13, 1973 letter has been undertaken.
In researching the effect of temperature on chemical tcxicity to aquatic organisms, it is apparent that past studies have dealt largely with in-organic =aterials. Literature concerning the effects of temperature en the toxicity of a==onia, :ine and phenolic cc=pcunds in general was accu =ulated and reviewed.
The data reviewed generally indicates increased temperature produces in-creased toxicity (Cairns et al. 1976, Cairns et al. 1975, I:FAC 1973, Llcyd 1960, Cairns et al. 1971, 3urten et s1. 1972, L1cyd 1961, Skid =cre 196k, Wuhrmann et al. 1953), however, contradictory information is cer:cn AME3D ERT 1 C-1 CCTCEER 20, 1978 1456 128
(Cairns et al. 1976, Lloyd et al. 1962, Lloyd 1961, Hazel et al. 1971, Sprague 19,'01 In an IPA publication (1975), it is stated that no assump-tions should be made about temperature effects on toxicity.
At the present time, based on the contradictory nature of the available literature, it is not possible to specifically predict the effcets of temperature on tnose listed materials which may be present in Dov's dis-charge. Consumers Power Cc=pany cannot identify the source, nature, quantity or time period of Dov's efflu"nt thereby ec= plicating the diffi-culty of predicting the possible intel :tions of temperature and discharge materials.
In general, by assuming that Dov's discharge meets applicable regulations, and by taking into account the total volume of heated water ec= pared to the volume of available river water, the limited length of the mixing zone and dispersion of organic cc= pounds, no additive effects are anticipated.
In regard to the thermal discharge enhancing chemical activity of Dov's probable discharge materials, a review of pertinent literature (~4est 1970) indicates the thermal discharge should have no effect on decomposition or reaction enhancement of zinc, pentachlorophenol, 2.h. 5-T, hexachloroben-zene, and phenolic, compounds (dichlorophencl, trichlorophenol and tetra-chlorophenol class). However, it is anticipated that some loss of these materials would occur due to evaporation frc= vater to air. No deco = position for benzene, phenol, 'a==onia and styrene would take place.
AMENDMENT 1 C-2 CCTC3ER 20, 1973 b
f2h
Burton, D.T. et al. 1972. Mortality curves of bluegills si=ultaneously exposed to temperature and zine stress. Trans. A=er. Fish. Soc. 101, 435.
Cairns, J. Jr. et al. 1971. The effects of pH, solubility and te=perature upon the acute toxicity of zine to the bluegill sunfish. Trans. Kansas Acad.
Sci. 74, 81.
Cairns, J. Jr. et al. 1975. Te=perature influence on chemical toxicity to to aquatic orgsnis=s. Jour. Water Poll. Control Fed., Vol. 47, No. 2, pp 267-280.
Cairns, J. Jr. et al. 1976 Effects of te=perature on aquatic organiss sensitivity to selected che=icals. Virginia Water Resources Research Center, Bulletin 106, 98 pp.
Enviro::= ental Protection Agency,1975 mthods for acute toxicity test with 660/3-750c9
~
Zeological Research Services. IPA-fish, =acroinvertebrates and a=phibians.
European Inland Fisheries Advisory Co==ission, 1973 Water quality criteria for European freshwater fish, Report en =eno-hydric phencls and inland fisheries. Water Res. 7:929 Ha:el, C.R. et al. 1971. Sensitivity of striped bass and stickelback to a==ccia
~
in relation to temperature and salinity. Calif. Fish and Game, 57, 154.
Lloyd, R., 1960. The toxicity of Z SCg to rainbow trout. Ann. Appl. Biol. 48, 84.
n Lloyd, R. 1961. The toxicity of a==enia to rainbow trout. Water and Waste Trt.
Jour. 8, 278.
Lloyd, R. et al. 1962. The effect of the enviro::=ent on the toxicity of poisens to fish. Jour. Inst. Pub. Ingr., 61, 132.
Skid = ore, J,F. 1964 Toxicity of zi. ; ec= pounds to aquatic an*C s, with special reference to fish. C.uarterly Rev. of Biology,39-227.
Sprague, J.B. 1970 W asure=ents of pollutant toxicity to fish, II, utilizing and applying bicassay results. Water Res. 4, 3.
Weast, R.C. (ed), 1970 Handbook of Chemistry and Ihysics. 51st Iditien.
Chemical Rubber Company, Chio.
Wuhr= ann, K et al. 1953. Contributions to fish tericity, In, cencerning the toxicity to fishes of a-mnium and cyanide solutions with variable cr/ gen tensions and temperature. Schweiz.
Zeitsche Hydrol. (G6r.), 15, 235. Taken frc= Cairns, J. Jr et al. 1975 (previcus reference).
1456 130 AECC'T 1 C-3 CCC03IR 20, 1973
STATE OF MICHIGAN NATunAt nasouacas comuission CAAL T. JCHN$CN L M. LAITALA WILUAM G. MILUKEN, Governor CY," $Ett DEPARTMENT OF NATURAL RESOURCES MAARY M WHITELEY STEVENS 7. MASON GurLQiNG Box 3CO28. LANSING. VicHIGAN 489C9 JCAN L WOL7E HowARO A. TANNER. Director CHAatES CL YOUNGLOVE September 13, 1978 Mr. Michael Putnam Consumers Power Company 212 West Michigan Avenue Jackson, MI Dcar Mr. Putnam:
Attached is the list cf critical materials discharged during 1977 as reported by Dow Chemical Company for the Midland p? int.
As we have discussed in the past, we would like you to analyze the interaction of the thermal discharge from the Midland nuclear plant with these materials so that we might better evaluate the environmental effects of your discharge and prepare the NPDES permit. If you need further clarification, please contact me.
Very truly yours, WATER QUALITY DIVISION Robert 3asch Aquatic Biologist Biology Section RB:cip cc:
D. Ticeney K. Zollner 6-MICHiG
t
- . ( 'a 1456 131
'" /
/
AME:o:.2:c ;
Ch CCTC3Ea 20, 1973
a e
t Critical Materials Discharged by Dow Chemical Company, Midland 1977 Critical Material Quantity (lbs.)
Aniline
<ll Benzene 1,001-10,000 Hexachlorobutadiene
<ll Pentachlorophenol
>100,000 2,4,5-T 101-500 Styrene 1,001-10,000 Butyric Acid 501-1,000 1
Phenol 10,001-100,000 Hexachlorobenzene 11-100 Ethyl Acrylate
<ll Ammonia
>100,000 radmium
<ll Antimony
<11 Chromium 1,001-10,000 Copper 501-1,000 Phenolic Compound Class
>100,000 Dichlorophenol Class
>100,000 Trichlorophenol Class
>100,000 Tetrachlorophenol Class 10,001-100,000 Zinc
>100,000 PCB
<ll Dichlorobenzenes 1,001-10,000 1456 132 A'CC'CT 1 C-5' OCTC ER 20, ~_975
APPENDIX D THERMAL PLUME EFFECT ON DISSOLVED OXYGE'I LEVE*S In response to Staff's July 28, 1978 request for an assessment of the effect of the Midland Plant's ther=al discharge on dissolved oxygen levels in the Tittabavassee River, the following is provided:
Under certain conditions the cooling pond discharge =ay reduce dissolved oxygen levels in the river as a result of the limited solubility of oxygen in heated vater and the potentially high biological oxygen demand of the Midland effluent.
It is the Company's understanding that Dov's current NPDES Permit requires the assurance of a daily =inimu= D0 level of 5 pp= measured at the Freeland
=onitoring station. A review of Dav Freeland monitoring data vill be under-taken to identify the occurrence and frequency of potentially lov DO levels.
As discussed in the Preliminary Analysis of Midland Power Plant Cooling Pend Operation (Append *x A), various constraints on pond blowdown include: river TDS levels, river temperature, river flow, blovdown temperature and blevdown flovrate.
If the preliminary river D0 review indicates levels of D0 approach-ing 5 pp= can be anticipated during allovable blevdown periods, the Co=pany's preoperational and postoperational aquatic studies will be modified to assess the timing and extent of the proble= as well as reco==end appropriate corrective alternatives.
1 The Midland cooling pond was initially filled during 1978, therefore, limited data are available concerning its aquatic ecosyste=.
Pre-and postoperational data collections will evaluate cooling pond biota and predict 3CD effluent limits.
A preliminary mathematical assessment was made concerning the mixing of watera of various D0's to provide a hypothetical prediction of DO change. This assessment is meant for general use and is based on several assumptions.
It is by no means complete or inclusive.
The dissolved oxygen concentration found in a body of water is a function of several variables:
1.
d [0g] = (OD T,V,3) dt where CD = 0xygen Demand T = Temperature V = Volume 9 = Diffusivity of oxygen into water Assumptiens A.
The dissolved oxygen levels within the mixing zone are not significantly effected by tha oxygen demand of either the pond or the river based on the ratio of volumes and the residence time in the mixing zone.
AMENDMINT 1 D-1 CCTOBER 20, 1973 1456 133
3.
The diffusic: rate of exyge: 1:to the river 'd***=
-S e dvd g_:c=e is expected to change sc=ewhat as a result of the fluett:sticus is river te=;erature due to ;c=d blevdown but this change is =ct expected to te significa:t.
1 C.
Assu e the eccli=g pond discharge is 5 cfs (2ased c= verse case 47 derived frem the ther=al== deli =g studies at river fievrate of 770 cis).
D.
The -avd ta=;erature expected inte eccling ;c d discharge is m
C approx 1=atelyigi?. Assu=e a -
v' = aT of kS~?, a:d a river te:-
perature of 60 F.
2 I.
Assu=e the DO cf the plant discharge i.o be a =ind=us of 5 p;s and the river to be at 100% saturatic: (9.8 pp=).
F.
Ass =e ec=plete =ixing within a -d vd g =cre vhich is 1700 ft ic=g by 255 of the river vol=e a:d the average velocitf of the river is 94 ft/sec.
Calculate the disselved crfge: ec=ce:tratics is the -dvd 2 =cce based c the above ass =ptic:s:
1.
Calculate residence ti=e is -dvd g =c==
17CO ft -;.9h ft/sec = 1808.5 see Ti=e in -dvd
=cce 1
2.
Calcula.e the volu=e of water in the dvd g =cce 3
770 ft /see x 18c8.5 see x.25 = 3k8,138 ft3 3;y,,yo;=, yt 313
-dvd g =cce 3
3 5 ft /see x 18C8 5 see S.ch3 ft 313c337g, ye;=,
s 3
357,181 ft 7;;3; ye;=,
3 Calculate the exygen ccatest of the river and discharge vc1=es *rithis the ther=al p1=e area.
3 3
3ha,138 ft x 28.316 1/ft x 9.8 =g/l 02 - 96.6 Ig 0 i: St* Eiv'# 7*1=*
2 3
sch3 ft x 28.316 1/ft3
- 5*0 28/l 0 1.28 rs 0 i 218Ch2#E' 7*1=*
=
2 2
2 97.88 Kg 0 20**1 i "i*i 8 2* '
2 1
h.
Calculate dissolved exygen ec= tent in
- d g :cce 97.88 I Cg 2 1068/Es
, = 9.67 =g/l ca th' M' E 20:'
1 357,:.31 ft3 x 29.3:.61/ft; 2
?is is a 107 cf.13 =g/' in the =ixing :::e.
D P
D "3lfD d
oJ3M1A ld
_a Aus::MIr 2 D-2 JUIE 1,1979 1456 134
A ore realistic situation would be to choose a su==er month where the river flowrate is at a level where discharge would occur and where both the pond and river te=peratures are high.
A.
Assu=e that the month is August and the te=perature of the river is at a =aximus (80 F) and the flovrate is 770 cfs.
B.
Assu=e an average discharge rate of 9 efs and a te=perature of 105 F in the cooling pond discharge.
C.
Assu=e the D0 of the plant discharge to be a =inimum of 5 pp= and the DO in the river to be approximately 85% saturated (6.8 pp=).
Making these assumptions, the dissolved oxygen contcnt would drop fro 6.8 pp= to 6.67 pp=, which is probably more representative.
1 The relatively short residence time in the mixing zone should not result in a significant effect upon DO levels in this restricted area of the river. However, a possible reduction in downstream D0 levels may occur as a result of cooling pond and river 30D conditions.
A literature search to identify the potential effects of the Midland Plant's thermal discharge on the dissolved oxygen levels in the Tittabavassee River is continuing. '4here =any variables are synergetically contributing to a single effect, it is very difficult and perhaps not possible to fully express the proble: =athematically. The feasibility of future mathematical assessments will be determined by the results of the literature search.
The pre-and postoperational monitoring studies will include the results of the Company's investigation into this issue. If conditions exist which would result in the potential depression of the DC level in the river be-lov the daily average limit of 5 pp= as a result of pond operation, correct-ive =easures vill be implemented. Potential corrective =easures may include aeration of the pond blevdown, control of 303 levels in the blevdown or additional ILnitations to restrict when pond blevdown can occur.
1456 13e3 A>E32:E C: 1 D-3 COT 03ER 20, 1978
- 1. INORGANIC NAME AMOUNT Obs/yr) j NAME AMOUNT (Ibs/yr) l MATE RI A LS A ntirnony i
Mercury Iiote 1 l
Arsenic l
Nickel Note 1 Cadmeum I
Se'enium 2l Chromium (30) i Silver Note 1 Ccoper 7600 l
Sulfides Cyances
]
Thaihum Leed Note 1 I
Zinc Note 1
- 11. ORGANIC NAME AMOUNT Ubs/yr) l NAME AMOUN T Obs,yr) l MARRIAM Act' dine I
Hexachlorobenzene (HCS) i Acrotein l
Hexachlorobutadiene (HC80)
Aldrin
' Hydroquinone Ammonia 120.000 88corone Amyl Acetate l
Lactonitrile Anilines (inct. S enzidines)
Mesirviene 8 enzaldehyde Mesityt O x es B enzene (Solvents i
Naothol l
Benzvt Bromide 1
Naanthenic Acid (Naotnaienes 1
Beta Proariolactre Il Nitrobenzenes l
Butyl Alconol l Phenotic Compounds l
B utyraloanydes jl Phenanthrone l
Butyric Acid ll Phthalates Carbon Disultice t
i Picramates (n rtro.omenoist l
Chlorinated Benzene Compounds 4 Polychlorinated Dichenvis (PCB'S) l Crotonaldehyde i
Pyridines l
[ Cumene i
Quinonne I
wus Quinone l
Oichloroorocane Styrene O seldrin l
Tordon Note 2 0:etny: benzene Tomachene i
E ndren i
i vinyl Toluene I
i Ethyl Acrytate Xylenes l
l i
Hectacnsor 2 4 5 T tand its formutations) l Note 2 i
Submitted in accordance with Section 8 lbl, Act 245, Pubiic Acts of 1929, as amended.
l 3.ea.e
- r. of A cos.c.at Dat.
j if Partn.esnio, signature of CoCwn.r O ate 1 c__
6 - i-? t :
Prin. or
. A ocu. 3t a c.am. ano T sti.
Print or T vo. Co4*n.r's N.m.
Stephen H Hewell, Senior Vice hesident Of I
hojects, Engineeri::g &
Construction NOTE: If sanetary sewage is to be discharged from hcusing develoements. acartment buil:*ings. shooping centers. cr other commercial developments into a system dther than an accroved municipal sanitary waste coilection systern. the following should be ccm;leted and signed by an authonzed municipal efficial or townsnio efficer.
It is the policy of the Commission to recuest that acclications involving the disocsal cf sewage of human crigin from any entity other than iocal governrnent include the local government as a co-sigrer of the statement. and that all proceedings and hearings against the said entity weil include the local unit cf govemrrent as a party Oy accropnate notice. and all permits issued as a resait of suen nearings ar's proceecings wist te jointly against the said unit and entity.
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14 5 6 13 6= 1> 1979 MEasm 2
State of Michigan Department of Natural Resources Water Roscurces Commission thSCHARGE PERMIT APPLICATION This permit application is required by the Michigan Water Resources Commission Act. Act 245. Public Acts of 1929, as amended. A cornpleted apphcation should be submitted at least 130 days pnor to imtiation of a new or increased use of waters of the state for waste dispsal purpsses.
INSTRUCTIONS FOR COMPLETING THE APPLICATION The foRowing instructions are listed in the :Jrder in which the items to be comOcteJ appear on the application. Please read carefully and c omplete the entire application. Pnnt or type ah informa~ ion except for required signatures. Partially comple ed applications will be returned eo the app!icant for completion. Upon complenon, retain ene (17 copy of the application for your files and send three (3) applications to:
Water Resources Commission Department of Natural Resources Stevens T. Mason Building Lansing Michigan 48926 You will be nonfied by letter that yoe.r application has been received, and you will be contacted by a district representative or notded of action taken by the Water Resources Commiss on. If the proeosed discharge is to surface waters, you will receive additional forms to be completed in accordance with the National Pollutant Discharge Elimination System Permit Program.
I. Check whether discharge is an existing discharge. to be a new discharge, or to be an increase in an existing discharge.
- 2. Name. Maihng Address and.TeLphone Number of Applicant:~
Give the name of the person propasing to make the new or increased use of the waters of the state for waste disgosal purposes. An agent may sign the applicauon if authonzauon to act for u.a discharger accompanies the application. If the application is subnutted by a corpcrauen or a company, it should be signed n an ofUcer of that organization i.e. president, vice president, etc.
Give the mading address and telephone number where the person proposing to make the new or increased use c?v be contacted.
- 3. (al Check whett.cr the preon proposing to make the new or increased use is doing so as an individual, partnership, corporst:os spublic or pnvate), governmeriW board or agency or other legal entity.
If the person proposing to make the new or incrrased use is a pablic or pnvate corporation name the state in which the articles of incorporatica are filed.
(b) Check the box which best corresponds to the proposed en.erpnse.
(c) Characterize proposed enterpnse on the basis of its pnneipal function. E e.nes: cannery, oil refinery, chemical manufacturing, metal platmg. or car wash. Then give narrative description of the proposed enterpnse mciuGing types and volume of material produced or processed.
(d) Desenbe location of proposed enterprise. Be specific. Whenever possible use street or road names and numbers, narre of political subdivision (city village, township). Attach a sketch or map showing location.
J.
Desenbe water supply source f well or we!!s. surface water, public supply), If source is surface water. give name oflake or stream invohed; if source is public supply, give name of owner (city, village, township, etc.).
Give separate estimates of the amounts of water to be used for various purposes as indicated. Amounts should be expressed in terms of gaI!ons per day.
$. Desenbe the proposed location of the waste discharge tgroundwater. public sew r. county drain, nyer. lake). Give proper name where applicable.
If discharge is to a public sewer, gne name of owner and state whether sewer is of the storm, sanitary or combined type. If d scharge is to a county or inter-county drain, give name of drain and uste w hether it is ogn or closed. (Informauon on drains may be obtained f:om appropriate county draan commissioner).
Give separate estimates of the daily volume of waste to be discharged in gallons per day. Indicate whether discharge is over I shift (8 hour9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br />si. :
shifts (16 hours1.851852e-4 days <br />0.00444 hours <br />2.645503e-5 weeks <br />6.088e-6 months <br />). or 3 shifts C4 hours). With respect to periodic batch discharges, indicate volume and frequency.
- 6. (a) Indicate the typ of treatment expected to be used to provide adequare control of the wastes.
(b) List signancant bactenal, physical or chemical waste charactenstics. Example: color, tureidity, temperature. biochersical oxygen demand.
chemical oxygen demand, toxic components, alkalimty or acidity, taste and odor producing components, radio-ac tvit), etc.
- 7. Distance private and murucipal wells are from proposed waste treatment fac.!ines.
- g. Distance surface watercourse is from proposed waste treatment facilities if sub-surface disposal or oxidation pond is proposed.
- 9. Ifinsection well is proposed give a narranve description of the method and manner to be followed in the construccon of fie weu. Any above ground treatment needed prior to injection also should be desenbed.
- 10. Either draw in the space provided or enclose a USGS or county map with appropriate markings showing each proposed pet of discharge as indicated in item 5.
II. List names and addresses of property owners adjacent tc propcsed enterprise.
- 12. Act 200. Public Acts of 1970. requires every industry and commencal entity which discharges wastes to the waters of the state to file an annual report with the Commission listmg materials used or incidental to its manufacturing oprations, including by-products and was.e products, which appar on the register of cntical materials compiled by the Commission. Indicate the amount of each matenal listed which is tsed er is proposed to be used. in or inexfental to, your opera' ices.
NO TE: Sec' ion 6 (a) of Act :45. Public Act cf 19 9. requires that every industrial or commercial enoty which discharges liquid wastes into any surface water or groundwater shall have waste treatment facilities under the s;ecific supervision and control of persons who have been certded as prowly quaided to operate the facilities. Pnor to start-up of your proposed operation, you wdl be required to submit an applicauon for the persones) for ceru5 canon under the Act.
The township supervisor. village presider.t. or city supenntendent must sign the statement if sanitary waste is to be disciarged into a system other than an approved municipal sanitary waste coilection system. The appropriate of!Icial should sigr. in th: space labe!ed " Signature of Authorized Local Government Representauve'* and complete other spaces at the end of the statement.
APPLICATIONS WITH PARTIALLY COMPT.KTED STATEMENTS wit.L BE RETURNED TO APP 1! CANT.
P00R D M 1
e
_e Ca.v,Im. r DESCRIP*IO:I CF FR0pCSED ENTERPRISE The Midland Plant Units 1 and 2, owned and to be operated by the Censu=ers Fover C0=pany of Michigan, is sited partially within the southern limits of the City of Midland, Michigan. Cc==ercial operation of Unit 2 is planned for March, 1981, and cc==ercial operation of Unit 1 is planned for March,1982. The 1235-acre plant site is en the south shore of the Tittabavassee River i==ediately across frc= the Dow Chemical Cc=pany's =ain industrial ec= plex.
The Midland Ant will generate approximately 1,300 =egawatts of electricity for distributica to the applicant's syste= and that of the Michigan ?cver Pool of which the applicant and Detroit Edison Cc=pany are the principal partners.
In addition, up to L,050,000 pounds per hour of stes= will be delivered to the Dow Che=ical Plant across the river for use in chemical processes and heating.
The two reactors for the Midland Plant are pressurized-water type supplied by the Sabcock and Wilcox Company. Each reactor vill cperate initially at a ther=al power level of 2k63 MWt and vill be capable of an ultimate cutput of 2563 MWt.
Unit 1 vill have a gross electrical nameplate rating of 505 MWe, and in addition vill generate up to 3,670,000 pcunds per hcur of 175 psig stea: and up to 500,000 pounds per hcur of 600 psig sceau for sale to Oov Chemical Cc=-
pany. The gross electrical nameplate rating of Unit 2 vill be S55 MWe.
In normal operation, Unit 1 vill generate eisctricity and stes: while Unit 2 vill generate electricity. Unit 2 can provide steam when Unit 1 is shut devn. The n0=inal operating pressure and temperature for both reactors is 2200 psig and 0
579 ?.
The units are designed for a pressure of 2500 psis and a temperature of 6500F. An exception is the pressuricer which is designed for a temperature of
- 670cy, The steam and power conversion system is designed to accept steam frc= the nuclear stea= system. Cne portion of this heat energy is converted to electri-cal energy by the turbine generators. A second portien of the "est energy is used in the process steam evapcrators to generate pr cess stes: for Ocv.
The circulating water syste=, utilizing cooling pond vater, vill dissipete the balance of the heat energy which is rejected by the turbine ccndenser.
Steam frc= the steam and power conversion systems is used in the process steam evaporators to generate process steam in a tertiary syste for Ocv.
The function of the process stes: evaporators is to provide physical separation betseen the turbine plant cycle and the process stea= deli ~ered to Dov.
5tes: frc= the Unit 1 stes: generators vill pass through a two-flev. 1300 rp=,
tande:-ec= pound, high-pressure turbine and then through =01sture separater re-heaters and cc=bined intercept and stop valves to one double-ficv lev-pressure turbine which exhausts to the main ecndenser. Steam frc= Unit 2 vill pass through a similar syste=, except that final f1:v vill be to tvc icuble-flow, lev-pressure turbines which exhaust to a dual pressure ecndenser.
\\k e
e
The Midland Plant Units 1 and 2 vill generate electrie,#cVer a*~ 22 k"' a "4
2h kV, respectively. Tnis pove" vill be
- ad---.h*ough separate isolated phase
+
uses.c the unit main transfor:ers where it will be stepped un to 3h5 k7 w
o
,ransmiss.cn voltage and delivered to **he sv4 c#a* d "-" aeparate overhead lines.
1456 139 I-2
..m... r._
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3CURCI CF *JA"'Z3 Figre 1 sche =atics:._2. inustrates the ser:es Of vater and the =a :er is whi:h each scu e vin be used.
?-eeess Vater All vater for use as process vater vill be provided as follevs:
1.
"'he ::cv Chemical Cc=;any vin previde feedvater to the eva;crsters (30de 20, Figre 1) in the pr: cess stes= system. The stes: thus pr:duced is ret =:ed (Iode 21, Firre 1) to the ::cv Chemi:21 Cc=pany for use is their process syste=s. This fiev is expected to be cc ti ucus.
2.
Duri:g the first year of Unit 2 c;erstic the Midland Municipal *iater "lis-trict vin supply the Midland Plant -
- eup da-4 erali:er syste: (2cde 29, Fig re 1) which in turn vin supply process vater to the Midla:d Plant.
This flev is expected to be ec:tinueus. After the first year of cperatice the Plant win have the Opti:= cf using either Midla:d Muni:1;al vater er Ocv de=isersli ed vater for =aken; ;= poses.
i Coolier and Cendensier Water
- 4ater for use as :aling and ccedensing vater ill be withirsv: fr = the Citta-bavassee River and pu=;ed to the SSc acre re:Ren'.r.ti:s : eling pend ' cde 5, 1
Firare 1).
he istake stractre== the river <in e tai: travsi-ing screens, screen vash pu=;s, a:1 trash rschs. Orsveling screen vash vater vill be strain to retai: debris prier 0 returning vash vater :: the 1:take str20ture. Oebris ac:2=ulating c trssh.rseks vill be za:"C'y re=0ved.
All c Re ted debris vin te trs:s;crte:i effsite fer disposal.
"'he desis: Of the intake str cture has been f:und tentatively acceptable by the State Of Mi:higs:
Depar =ent of "atrsl Rescur:es pending ; cst c;erstic:a1 studies of the i:take's efficiency and : -site velocity =easure=ents (letter fr:= Mr Rebe.- J 0: rchaire.
ONR, to Mr Pau'. C Zittle. 0 :su=ers ?:ver Oc=pacy, dated Ja:uary 17, 1977).
Fre11=icary design rating of the =akeup pu=;s was 200 cfs.
'te W u; pu=;s as built vill be espable of withdrawing vater fr0= the !ittabavassee River for :: cling peni =akeup at a mad =u capacity of 270 cfs sub,Je: to the f:lleving:
River Flev, cfs Maxi =u= Pend Makeup Fate, efs 4350 0
350-650 Excess over 350 up :: a
=axi=u= cf LO 650 and Ixcess over 650 plus.0 above but Oct =cre than 270 1456 140 M
2
^C ":-r: - -, ~ ^ -
Agg ; y,g3- ;
-n
8 Ix;ected =akeu; vater appr:ach vel: ities sre presented in '"stle 1.
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(b) Mes: surface level.
(~) Recirculatic 1
- river for radvaste dilutic ::17
]
("') Recirculste :: =akeup pu=p inlet.
".ne re:irculsting water 1 :ake structure en the 380 acre recirculsting coeling pend vill ecstain circulating vater pumps, trssh racks sed fixed screens. Cebris sceu=ulating On the trash rseks and fixed screens vill be anually re ved sad transper:ed.cff-site f r dispesal.
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heat re: ved by plant coeling sud :: densing systers and vill be used t: pr:vd.de water for the plant fire prote :10: system. C: ling pend Operstic is discussed in Exhibi*. 17.
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P ecipitatien Precipitation falling en the plant site vill 'ce transported via roof drains and site ster: drains to 3411cek Creek, Tittabavassee ?.iver, and the 380 acre re-circulating eccling pend (3cdes 1, 2 and 3, Figures 1 and Figure 3).
Precipita-tien falling en areas where oil centoninatica nay occur such as transfer:er areas, cil storage areas, and oil transfer areas (3cde hS, Figure 1) is routed to the cily vaste ecliection r*stes.
Precipitatien falling on the 330 acre f
recirculating eccling pond (3cde h, Figure 1) slightly decreases eccling pond nakeup water requirements.
The =axi=== precipita ice rate is based en the naxi=u: 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> rainfall since 1932 which vas 4 31 inches. Precipi*stien f*cvs are expected to be inter =ittent.
about 30 inches.
The average annual precipitation is
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i456 142
EXHIBIT II ATTACEMENT A IR VAL A*TD ADULT FISH MONITORING PRCOEDURES FOR THE INITIAL FILLING CF THE MIDLAND PLAUT COOLING FOND Entrainment Monitorinz for Larval Fishes Fish larvae sampling at Midland ec :enced with the initial filling of the cooling pond during April 1978. Sampling frequency is weekly during pumping 1
periods. Velocity ceasurements will also be recorded at this ti=e (at the intake structure and in the river) to correlate changes in velocity and current direction with makeup pump operation.
A 0 5 = diameter, No 2 plankten net (351 x mesh) with a flov meter vill be used to collect sa:ples from the Tittabavassee River in front of the river intake trash racks or at the discharge into the cooling pond.
Integrated
~
vertical sa ples frc= surface to botto= vill be used for sa ples collected at the river intake structure. The final location of sampling vill be deter-mined after analyses of initial data. At least 10 =inute replicate sa=ples vill be collected day and night and preserved in 10% formalin. Rose-bengal dye vill be added to stain the larvae to facilitate sorting. Larvae vill be 1l counted and =easured (nearest==)
and identified to the icvest practical taxonc=le level.
Entrain =ent results vill be expressed on a 12 hour1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br /> diel basis as nu=ber of larvae and/cr fry (over 25 3==) of each taxonomic category per 1000 =3 cf water. Potential number of larvae entrained vill be estimated by simple pre-portion to the total makeup flow per week.
Essential plant operating data vill include:
Intake water temperature ( C);
makeup water pu=p capacities; number of takeup water pumps in Operation; and duration of pumping cperations.
Impineement Monitorine
=pingement of adult and juvenile fishes is anticipated to be lov, therefore, it will be attempted to collect all impinged fish. The screen washing is normally done on a daily basis and =ay vary depending on the incunt of fish and/or debris accumulated on the traveling screens. Screens should be washed until clean, and time of vashing recorded. Fish vashed frc: the screens vill be collected by a basket (3/8" voven wire mesh) in the sluiceway, emptied into labeled plastic bags and frozen.
All fish vill be sorted and identified to species level. The total nu=ber, total veight (kg), and size range (==) vill be obtained for each species.
Tctal length (==) and weight (g) =easurements vill be made f0r not 20re than 25 individuals of each species category. Subs 1=pling may be imple ented during periods of heavy fish runs and shculd include at least 105 by weight of the total amount impinged.
I:pingement results will be expressed as total nu=ber of fish i= pinged per week and per million gallons.
- pingement and entrainment =enitoring frequency is sub'ect to change up n re-view of initial filling results.
xcccxzNT 1 II _ u 1456 143 CCT0 sat 20. lars
EXHIBIT !!!
pROPCSED LOCATION OF WASTE DISCV.AECE Figure i sche =stically illustrates the =anner in which vastewater strea=s vill te discharged and their crigins. The location of the discharge structure for these strea=s is shown on Figure 3 The Dow Che=ical C0=pany receives, treats and discharges process stea= evaporator blevdown and sanitary vastes. The Dov Chemical Cc=pany is authorized to discharge vastewater to the Tittabavassee River in accordance with NFDES Discharge Fer=it No MI 0000868.
Process Water Slowdown frc= the evaporators which supply process sten: to the Dov Chemical Cc=pany (Node 22, Figure 1) vill be pu= ped to the Dow Che=ical Cc=pany for treat-
=ent and discharga. This evaporater blevdown is expected to be con-tinuous.
Plant floor drainage (except drainage frc= chemical storage, che=ical treat =ent and potentially radioactive areas) vill be treated to re=0ve oil, gresse and suspended sclids (Nedes 49 and 51, Figure 1) prior to being discharged to the Tittabavassee River via the cooling pend bl0vdevn line. This treated cily vaste is extected to be.di.scharged.continueusly.
~~
Makeup de=ineralizer and condensate polisher regeneration vastes and associ-ated che=ical stcrage and treat =ent area irainage and auxiliary boiler blev-down are collected in neutrali:ing su=ps.
After pH adjust =ent, the contents of these su=ps (Nodes L5 and k7, Figure 1) vill be discharged to the Tittabavassee River via the treated oily vaste and cooling pond blevdown lines (Nodes 7 and 51, Figure 1).
The evaporator building neutralizing su=p vill nor= ally discharge at 9,000 gallons of =akeup de=ineralizer systeu re-2 generation vastes per day. The maxi =u: expected discharge rate is 74,000 gallons per day. The =akeup de=in storage tank overflov/ drain line has been rercuted Lu that portion of the site ster = drainage syste which discharges to the Tittabavassee River (Node 2, Figure 1).
In addition, blevdown frc= the two auxiliary boilers vill alco be routed to the evaporator building neutralizing su=ps at a =axi=u: of 9, 00 g;allons per day per boiler for a =axi=us of 35 days per year per boiler.
ins Units 1 and 2 turbine building neutrali:ing su=ps vill nor= ally discharge at 16,000 2
gallons every day. The =axi=u= expected discharge is 53,000 gallons per day.
AME';DME"T 2
- -1 JU:G 1, 1979 1456 144
1 Condensate polisher backvash and rinse water vill te eclie: tea by the Units 1 and 2 elean vaste sumps. The centents of these su=ps vill be routed (Ucde -,
Figure 1) to the SSO acre recirculatin ecoling pend. These su=ps vill ner: ally discharge at 29,000 gallons per day. The --vd-"
expected discharge is 97,c00 gallens per day.
2 Backvash frc: the magnetic filters (Ucde ho, Figure 1) vill occur in 1,500 gallen and 2,900 gallen tatches. One 1,5c0 gallen tatch and ene 2,9c0 gallen 1l tatch are expected to normally occur every seven to 1L days.
The maximum ex-2l pected rate is :ne 1,500 gallen batch and ene 2,9:0 gallen batch per day.
Liquid radvaste and irainage frc potentially radicactive areas vill be treated in the liquid radvaste systen to reduce the a: cunt of radioactivity and will be recycled to the plant nuclear systems. Ecvever, a pcrtion of this vaste may be occasionally discharged (Nede 59, Figure 1) in accordance with the Code of Federal Regulations, Title 10, Parts 20 and 50, (10 CFR 20 and 50).
C cline and Ccndensing Water The blowdown frc: the SSC-acre recirculating ccling pend (3cde 7, Figure 1) vill be routed to the discharge structure. Cooling pend Operation is discussed in Exhibit IV.
Dcmestic Wastevater Ocnestic water vill be distributed throughout the plant to sanitary fixtures, laboratory fixtures, drinking fountains, safety shevers, etc, and vill be col-le:ted by the sanitary vaste ecliection syste: (Nodes 23 and 31, Figure 1).
The sanitary vaate collection syste pumps the collected vastes to the Ocv Chemical C:=pany (3cde 24, Figure 1) for treatment and discharge.
Sink irainage frc: the main plant laboratory vill be routec to the Unit i neu-tralizing su=p where it vill be ec bined with Ocndensate polisher regenerati:n vastes for neutrali:stion and discharge (3:de -5, Figure 1) as described in the Prccess Water section of this Exhibit.
Ocmestic vater vill be supplied to the laundry f1cility. Wastewater frc this facility will be treated to remove suspended solids (3: des 52 and 53, Figure 1) prior to being discharged to the Tictabavassee River via the treatei 0117 vaste sad cooling pond bicvdevn lines (Modes 7 and 51, Figure 1).
- f levels of radio-acoive caterial in this vastewater exceed permissible levels of radicactivity as specified in 10 CFR 23 and 53, the stres: vill be diverted to the liquid raivaste syste: f:r further processing (3cce 53, Figure 1). Treated laundry varte vill be discharged in,000 gallen batches. Ucr: ally, cne such batch vill be discharged every seven days. At maximum usage of the launiry facility, cne such batch will 2l be discharged every one and one-helf lays.
Painfall Runoff Fre:1pitation falling :n the site vill be 2011ected and discharged via gravity ficv conduits to Su11cek Creek, Tittatavassee River and the eccling pend (Figure 3).
The cily vaste 2011ecticn syste: routes precipitation falling on areas which may be cen
- -=*ei by 011 to the oily vaste storage and treatment syste: (2cde L9, Figure 1) to be treated and discharged with the plant ficer drainage.
1456 145 1
AECE"" 2 I:: -2 o'Jnz 1, 1979
Plant Discharres Pricr to Connercial Cteration Prior to cen=ercial operation, the plant vill use veil vater, City of Midland vater and demineralized water for purposes of performing hydrestatic tests and water flushes on various plant systems during construction and testing y
phases as described below:
1.
Hydrostatic Tests - These tests are used to ensure integrity of welds and connections within a system. This test censists of holding pressurized test water within the syste: to be tested for given ti=es and pressures.
1 l The water dces not becc e chemically contaminated in any way and present plans call for the discharge of such waters into either the ecoling pond or the Tittabavassee River dependent upon the physical location of the hydrostatic testing activities.
(However, no discharge vill be =ade to 1
the Tittabavassee without appropriate approvals.)
Condenser hydrostatic tests will be conducted using Flucrescein dye.
2 Fluorescein dye vill be used for the initial condenser hydr: static test and for routine condenser tube leak inspections associated with the an-nual refueling outages for each unit.
2.
ylushes
- ater Flushes
~4 ster flushes differ frc: hydrostatic tests in that the 4
a.
purpose of the flush is to ensure proper functioning of a systen and to remove any obstructions that =ay somehow have gotten into a system.
These flushes vill also utilize well water, City of Midland water or demineralized water.
All the piping is delivered to the plant site with end caps installed.
The only contamination that the flush water could pick up would be minute a=ounts of rust, dust or oil in the for: of thin res44"=' #41:
areund pipe ends resulting frc: pipe beveling or preparati n rcr veld-ing. Minor flushes and hydrostatic t ests, performed en Ocnponents cr small systems, vill be carried cu*
4"*d ag the construction period. This test water vill be drained to varicus building suspe which diJeharge to the ecoling pond.
The first =ajor flush will be in April 1979 on the condensate system.
Other major flushes er hydros vill be performed en all er parts of the folleving systems:
feedvater, part Of main steam, bleed stea: condenser and possibly part of piping to Ocv.
All major flushes vill te drained to the cooling pond. Varicus stainless steel systems will be flushed with demineralized water which will also be drained to the ecoling pond.
b.
Chemical Flushes - The use of chemical flushes at the Midland site is presently only a contingency plan. Since there is no planned usage of a chemical flush, the corresp;nding procedures have not been devel: ped.
If such flushes should be used, they have historically involved shipment Of the c"a d-a'
- ka site in tank trucks by an outside supplier, usage in the flush and return directly fr : the systens being flushed to the tank trucks for removal fr : site.
Such flushing materials v ald, therefore, nct te discharged into either the pond Or the river.
4 A f.{
- * !m
.U!EiDME C 111 - 3 JUE 1,1979
3.
ccustruction chemistry Lab Trailer Wastes - Small a=ounts of waste chem-icals resultant from vet chemistr/ analysis perfor=ed in the temporar/ lab 2
trailer during construction will be discharged to the eccling pond. Use of the temporar/ lab trailer is expected to terminate with the cc=pletion of the per=anent laboratory facilities currently scheduled for early 1980.
s 1456 147
/dS: DICT 2 III h
JUIE 1,1979
EXHIBIT IV DESCRIPTICN OF PROPOSED TREA NE'IT OR CO:ITRCL FACILITIES Figure 1 sche =atically illustrates the segregatien of vastevater stres:s and the proposed treatment facilities. Process steam systes evaporator blevdevn and sanitary vastes vill be treated by the Dev Chemical Cetpany. Metal clean-ing vastes and debris removed from both makeup and circulating water intake structures vill be transported off-site for disposal.
Process Water Plant ficor drainage and precipitation falling on areas which may be centaminated by oil vill be collected and pu= ped to the oily vaste st orage and treatment systen as described in ite: 1, 011 Separation. Drainage from caenical storage and chemi-cal treatment areas vill be routed to neutralizing sumps for treatment as de-scribed in item 2, eH Adiustment. Drainage free potentially radioactive areas vill be routed to the liquid radvacte syste= as described in ite L, Radicactive Waste Treatment.
1.
Oil Separatien The cily waste treatment system vill consist of an cily vaste stcrage tank, a vaste oil storage tank, and oil removal' equipment.
The oily vaste storage tank vill be located outdoors and attached to the building centaining the oil removal eqaipment and vaste oil storage tank.
The oily vaste storage tank vill be fabricated with internal underficv and everflov veirs (analogous to an API separat0r) to allev free oil and suspended solids to be retained in *ka *aak.
Cil and suspended solids retained in the tank vill be manually removed as required to avoid carry over into the tank effluent line. The active capacity (above the overfl0V veir) cf the oily vaste storage tank is sufficient to retain 3 inches of rainfall on cutdecr collection areas plus the maxi =u: firevater usage event.
If an additional event occurs simultanecusly, ed the storage tank capacity is exceeded, the overflow will be routed to the cooling pond via the stor= drainage system.
Tank overficv vill be taken frc= the effluent side of the underfiev and overf10v veirs.
The oily vaste storage tank effluent vill be routed to an oily vaste treat-cent syste= for removal of any oil which may not have been retained in the oily vaste stcrage tank (such as emulsified and dispersed oils). The essential-ly 011 free effluent (.'!cde 51, Figure 1) vill be discharged to the Tittabavasee River via the cooling blevdown line.
Waste 011 separated frcm the vaste stres: vill be transferred to the vaste oil storage tank.
Waste oil accumulated in this tank vill be trucked off-site for disposal or refining.
2.
pH Ai?ustnent The evaporater building neutrali:ing sump and the Unit i and Unit 2 neutral-1:ing sumps vill receive process va'tes and ficer drainage frc= chemica.1 storage and checical treatment areas which are expected to have extruae pH 1456 148 n-1
values.
In addition the Unit 1 neutralizing su=p receives irainage frc the main plant laboratory. These sumps vill be equipped with air mixers, acid and caustic injection equipment and pump recirculation to allev pH adjustment of the sump contents. The pH adjustment vill be a batch Operation; when the desired pH is achieved, the surp contents vill be discharged to the Tittabavassee River (Hodes k5 and k7, Figure 1) via the treated cily vaste and cooling pond blevdown lines (Nodes 7 and 51, Figure 1).
Should either the Unit 1 or Unit 2 neutralizing sump contain condensate polisher regeneration vastes which exceed allevable levels of radicactivity (as set forth in 10 CFR 20 and 50), the vastes vill be transferred to the liquid radvaste syste for processing.
3 Settling a.
Magnetic Filter 3ackwash Main steam frc either Unit 1 or Unit 2 vill be supplied 50 the process steam evaporators. The evapora:Or condensate return vill be passed through magnetic filters (N0 des 3S and 39, Figure 1) for suspended iron oxide removal. Periodically these filters vill recuire backvashing. This backvash water (Ucde h0, Figure 1) vill be routed via the plant stern drainage system to the ecoling pend where the suspended iron exides will be assimilated in *he cooling pend sediment.
b.
Unit 1 and Unit 2 Clean Waste Sumps Condensate polisher backwash water and rinse water vill be collected by these sumps. Because this vastevater vill be very Icv in total diss0lved solids, it will be routed to the 380 acre recirculating c0 cling pend (3cde 4h, Figure 1).
Suspended sclids in this vastewater vill consist of icn exchange resin fines and corrosion pr0 ducts such as ir0n and 00pper oxides which vill be assimilated by the cooling pend sediment.
Radica:tive contaminants which may be present on 20ndensate polisher ion exchange resin are expected to be removed by regeneration chemicals (these vastes are routed to the Units 1 and 2 neutralizing sumps, as described in ite: 2 above). 3ackvash water and rinse water are not expected to exceed discharge limitations for radicactivity as set forth in 10 CFE 2C and 50.
The Unit 2 an=0nia and hydrazine storage and transfer area irainage is not expected to contribute measurable concentrations cf these chemicals to the contents of the Unit 2 elean vaste surp.
h.
Radioective Waste Treatment Radicactive process vastevater and potentially e- 'a-4-ated radicactive drainage vill be treated in the raivaste treatment systems. These systers consist of filters, icn exchangers, evaporators, and sclid vaste packaging equipment.
Solids rencved frc: the influent liquid radvastes vill be packaged and transported to a licensed burial site fer disposal. The purified water vill be recycled to the reactor plant systers. Occasionally this purified 1456 149 1v a
water =ay be discharged (Hede 59, Figure 1) to the Tittabavassee River via the treated oily vaste and cooling pend blevdev= lines (3: des 7 and 51, Figure
- 1) in a 00rdance with 10 CFR 20 and 50.
Ccoling Water The 880 acre recirculating ecoling pond vill provide ecoling vater f r the Units 1 and 2 condensers (Nede 11, Figure 1) and for varicus plant cooling require =ents via the Units 1 and 2 service water syste=s (Mode 13, Figure 1).
Service water vill provide cooling for varicus plant syste=s and cc=ponents other than the Units 1 and 2 condenser..
In order for this syste= to perfor= its cooling functions, the service water entering the plant cust not exceed its design temperature li=it.
The service water cooling tower (Nodes ih-18, Figure 1) will be put into operation as needed to =aintain the service water intake temperature below its design limit. 31ovdown frc= the service water cooling tower vill be re-turned to the cooling pond (Ncde 18, Figure 1).
No che=ical treatment is planned except as follows.
Sodit: hypochlorite vill be generated onsite for use in centrolling biological growths en heat transfer surfaces exposed to cooling pond water. It is expected to be injected twice daily for a period of one half hour each into the Units 1 and 2 condenser cocling water and service vater syste=s. Use of sodiu= hypo-chlorite vill be li=ited as deter =ined by operatica require =ents.
A chlorine residual as a result of this operation is not expected to persist in the pond for a sufficient ti=e to circulate to the point fr = vhich pond blevdown is withdrawn.
Sulfuric acid vill be injected into the pond via the service water syste= and
^
the cooling water inlet to reduce the tendency for eccling pond water to for=
carbonata scale en heat transfer surfaces. This vill slightly increase the sulfate concentrition that would otherwise be present in the pond.
Sc=e sodiu= chicride vill be present in the solution produced by the ensite sediu=
hypochlorite generation syste=.
This soluti0n is expected to have negligible effect on the pond sodium and chieride concentraticns.
The 00=bined plant discharge to the Tittabavassee River vill be through three 2-1/2 f ct dia=eter valved pipes Oriented perpendicularly to the river fi:v. This arrange =ent vill provide, by valve throttling and closure, both centrol of the i
cooling pond blevdevn flow rate and a discharge velceity up to 15 feet per second. This discharge velocity coupled with injecti:n of :ne fischarge per-pendicular to river ficv vill provide enhanced =ixing with the river.
Radioactive centa=ination of the ecoling pond or the vaters of the State are not expected to occur due to the precautions taken to prevent such centaminatien.
These precautions are described in detail in the Applicant's " Midland Plant -
Units 1 and 2 Final Safety Analysis Ecport" sub=itted to the United States Huclear Regulatory C:==ission, Oc:ket Hu=bers 50-329 and 50-330.
Ocrestic Wastevater Ocn-phosphate detergent vill be used in the laundry facility. Wastewater fr:=
the laundry facility vi Sa
*a-ad
-- -a-ave suspended solids (Nedes 52 and 53, Figure 1) prier to being discharged via the treated 0117 vaste and : cling pond blevdevn lines to the Tittabavassee River (Ucdes 7 and 51, Figure 11 Should this vaste stra=- av eed all:vable 1e'.je 75P6 ='f4313 7 i' "*
m.L,.M'... 2 1/ _,
CCTC3ER 20, 1973
.. e.
s
diverted to the liquid radvaste system for treatment to reduce the radicactivi;y level prior to release (Hodes 58 and 59, Figure 1).
The radvaste dilution flow supply frcm the cooling pond rakeup pu=ps (3cde 6, Figure 1) vill be utilized to ensure a mini =un of 43 efs for dilution of radionucleids in the radvaste prior to discharge to the Tittabavassee River 1
to comply with 10 CFR 20 and 50 limitations. During periods of pond blevdown when the blevdown flow is adequate, the pond blevdevn vill be utili:ed for radvaste dilution. Radvaste dilution flov frcm the discharge of the makeup pumps vill be used when pond bicvdown is insufficient.
Precipitation In addition to the ecnstruction impact control =easures specified in the Company's Supple = ental Environmental Report ani the AIC's Final Inv* *^--- *al Statement,
several additional measures are also being implemented for the centrol of sur-face runoff. These additional constructicn impact centrol measures include:
Ccnstruction of holding ponds in ditches near any source of runoff and near devatering operations to control siltations..
Rip-rap applied to 'iaite and Debolt Drain, 3 ranch #1 Drain and Su110ck Creek at changes of grade and at changes of direction to sicv vater velo-city, minimizing erosion and siltation.
Enbankments seeded, fertilized and mulched to centrol soil ercsion.
The construction impact control program fc11cvs standard practices presented in the folicving publications:
Michigan Soil Erosion and Sedimentation Centrol Guidebeck, prepared for Michigan 2epartment of Natural Rescurces, et al. by Beckett Jackson Raeder, Inc, February 1975 Soil Erosien and Sediment Control: Standards and Specifications for Eay, Midland and Sarinaw Counties, US Department of Agriculture, Soil Ccnservation Service, December 1974 En2ineering Field Manual for Conservation practices. US Department of Agriculture, Soil Conservction Service, 1969
\\456 \\c\\
3 AMIUDMINT 1 IV i
CCTC3ER 20, 1973
EXRI3IT 7 1
DESCRIPTION CF EUECTED CRARAC"' ERISTICS OF WASTEWATERS Process Waste Table 1 of this exhibit presents the expected characteristics of precess vaste-waters. Radioactive vaste discharges vill be in accordance with the Ccie of Federal Regulations, Title 10, Parts 20 and 50.
The discharge of demineralized water via the takeup desin storage tank over-flow / drain line (Figure 1) would be extremely infraquent, cecurring enly when the water level in the storage tank exceeds normal or when the tank is required to be drained. The tank is equipped with a high level alarm and a high level switch which aute=atically shuts down the makeup demin system. This instru-mentation is designed to preclude or prevent overflev cccurrences. The storage tank will not be routinely drained for maintenance On any sakad"l ad basis. It is expected the tank may require maintenance less than ence per year. The rated tank capacity is 50,000 gallons of de=ineralized water. The =akeup de-
=ineralized water chemistry is also presented in Table 1.
Cooling and Condeising Vater Table 2 of this ;xhibit presents the expected characteristics of the cooling pond blevdown tef re and after being ec=bined with prccess vastevaters for dis-charge to the Iittabavassee River. The total dissolved solids concentration in the Tittabavat ;s River at Freeland Road is not expected to exceed a monthly average of 500 mg/l nor an instantaneous zaximu= cf 750 mg/l as a result of this discharge. The ec tined plant discharge (Nede 60, Figure 1) vill not ex-ceed phosphate limits as set forth in the agreement reached between Consumers Power CO:pany and AEC Regulatory Staff Counsel, Thcmas ? Englehardt, whereby the 0.05 pps in river concentration of phosphorus was rescinded in favor of a ::tal discharge limitatien of phosphates not to exceed an average af 35 p02nd3 per day, exclusive of pond reconcentratien of existing levels in the river.
0 Table 3 of this exhibit presents the surface area and length of the 5 F iso-ther for varicus river flows.
Physical Model Testing at Alden Research Labcratories was used in deriving Table 3 River ficvs used in preparing these temperature distributions were based en long range average values. River water 1
temperatures devnstream of the mixing :ene are not expected to exceed the values given in Rule 1075 (2) and (3b) of the Michigan ' Administrative Code, Part h, Michigan Water Quality Standards, as a result of the cc=bined Plant discharge (Ucde 60, Figure 1).
C Estimated distances for closure of the I F isother:c are given in Table L.
14 5 6 15 2
,w.v-3==..
=
1,
.,0 i w Ns
.m er.4 6
...r s,
w' e -
- Attach =ents A and 3 of this exhibit provide an overview of the si=ulation models used as well as the effects of the Plant's thermal plume on the Tittabavassee Rivar. Attach =ent A provides a detailed description of the field survey, phy-sical =cdel and =athematical model used in the Plant ther=al plu=e si=ulation.
Attach =ent 3 provides a general discussion of the plu=e in terms of its effects in the near field and far field based on preli=1:ary =cdeling results.
Plant Discharres Prior to Co==ercial Operati'n e
1 Table 5 of this exhibit presents the expected characterisites of the preoperation-al wastewater expected to be discharged to the cooling pond prior to cc==ercial operatien. Also included in this table is a sm-m y of the ic=ical dischargos 2
fro: the construction che istry lab trailer to the eccling pond for the period Septe=ber 5, 1978 through April 20, 1979 As noted p evicusly on page III - 3 hydrostatic test water will be discharged to either tae Tittabawassee River or the cooling pond; the characteristics of this waste water are also included in Table S.
The frequency of flush water, hydrostatic test water, and layup dis-charges is listed in Table 5 as " varies". This =ay be construed as several tir::es a week for flush water, approxi=ately once per week for hydrostatic test water, and perhaps a few times each =onth for syste: layup dischartes. It should be noted that these frequencies are only approximations. Under field conditions, there =ay be weeks without discharges. As construction progresses towards co=-
pletion, there may be an increase of activity which =ay result in discharges
= ore frequent than presented above.
1 The ecoling pond holds approxi=ately seven billicn gallons of water when full.
~'he total esti=ated discharge of flush water and hydrostatic test water for 1979, 1980 and 1981 is approxi=ately 15 =illien gallons. To illustrate the effect on pcnd che=1stry, even if the total volume of both these vastevater stres=s for all three years were discharged all at once to the full pond, the dilution factor vould be five hundred to cne.
There would be no effect on pond pH.
Pend T::S vould be increased by only 0.k pp: and TSS vould be increased by 0.2 pp=.
Si=ilarly, the effect on pond chemistry of the other preoperational discharges vould be very slight because the dilution becc=es =uch larger as s= aller volu=es are discharged. Hydrazine (:T H nitrogea gas when exposed to air and,2 k) rapidly disassceiates into vater and so, can be disregarded.
AE:CMDT 2
'l - la JUI!2: 1, 1979 1456
'.53
I'GI3IT V TEE 1 EXPEC"'E3 CHD!ICAL CHARACTERISTICS OF PROCESS WASTE'4ATERS Evaporator Building :Teutralizing Su=p, Nede 47, Figure 1 Parameter Value Average Daily Volu=e, gals 9,000 Max 1=um Daily Volu=e, gals 74,000 pH 6.5-9 5 TSS, =g/l
< 30 TDS, =g/l 5,200 2
Ca,,=g/l 19o Mg, =g/l 100
- Ta, =g/l 1,300 S0, =g/l 3,100 3
C1, =c/1 260 g,=g/l trace Units 1 & 2 Neutralizing Su=ps(al, :Tode L5, Figure 1
}
Pars =eter Value 2
Average Daily volume, gals 16,000 Maxi =ur. Daily Volume, gals 53,000 pH 6.5-9 5 TSS, =g/l 4 30 TDS, =g/l 14,300 Ca, =g/l 200
- IH, =g/l 1,200 3
- Ta, =g/l 3,000 S0, =g/l 9,700 3
Laundry 'inste Treatment, :I:de 53, Figure 1 Aver 36e/ID:i 0=
value (b)
Pars =eter 2
Daily Volume, gals 600/3,000 pH 9 3/9 7 TSS, =g/l 430 Conductivity, ;=20/c= 1,LC0/2,000 PC, =g/l as P 0 9/3 3
1456 154 A.NENDMEIiT 2 7-2 JUIE 1, 1979
E'GI3IT V TA3I.E 1 (eent)
Oily '4aste Treatment, :Iode 51, Figure 1 Average / Maxi =
Parameter Value 2
Caily Volume, gals 64,000/288,000 pH 6.5-9 5 TSS, mg/l
<30/<100 011 and Grease, =g/l <15/<20 Magnetic Filter Backvash (Prior to Settling),:Icde LO, Figure 1 Value(d)
Parameter Average Daily Volume, gals 600 2
Maxi== Daily Vol=e, gals 4,400 pH 6.5-9 5 TDS, =g/l
< 50 TS3, =g/l
< 1,500 011 and Grease, eg/l
( 15 Auxiliary 3 oiler 3 lowdown,:!cde 37, Figure 1 d)
Parameter Value Frequency, days per y 35 AverageDailyVol=e,g/ boiler
) gals 1,900 Maxi = Daily V 1=e,
gals 19, coo 2
PH 6.5-9.5 T:S, =g/l 4 20 TSS, eg/l
<30(C Fe, =g/l 41(
Cu, eg/l 41 Oil and Grease, 26/1
<,15 2
33,=g/l
<2 Units 1 and 2 Clean Waste Sumps, :Tode ik, Figure 1 Value(k)
Para eter Average Daily Vol=e, gals 29,cco 2
Maximum raily Volume, gals 97,000 pH 6.5-9.5
. - e,
._v. /.-
e, : v-55 TSS, 26/1
<100 s
011 and Grease, ng/l 4.15 l
A?S:GIM 2 V-3 JU:2 1,1979
EXHIBIT V TABLE I ( Cq3 '_],
Makeup Ce in Storage Tank Overflev/ Drain, Figure i Parameter Value (Maximum Desien) 1 Frequency of Discharge 4cnce/yr test)
Maxi =um Daily Volume, gals 50,000 Conductivity 40 50 n=he/cm 3 25 C Silica, SiO2 (soluble) 4 0.01 pp=
pH 6.5 - 8.0 Chlorides, C1 40.05 pp=
Footnotes See attached sheet (b) Makeup Demineralizer and condensate polisher regeneration vastes cre 2
not expected to vary significantly from the average values given.
(a) Ouring the startup of the auxiliary toiler, total iren and copper cencen-traticas in the boiler blevdown may exceed 1 mg/l for a few hcurs.
(*4) Values for concei.craticn parameters are estimated maximuns.
2 (e) Both auxillary boilers in operation.
1456 156
!JEC.'EC 2 Vh JE E 1, 1979
The folloving reagents are expected to be used in the main plant laboratory. Occasionally trace amounts of these re. ;ents may be present in the main plant laboratory drainage to the Unit 1 neutralizing sump.
ItEAGErlT AllALYSIS IIFAGEllT ANALYSIS REAGENT AtlALYSIS Nitric Acid Phosphate. funcanous Sulfate Oxygen 1, 2 Hapthoquinone Morpholine Ferric Altra Chloride Potas9ium Iodide Oxygen Chromate 14 Sulfonic Acid Mercuric Thiocyanate Chloride Saalum Thioselfate Oxygen Mopholine Standard Morpholine Methanol Chloride Stabilized Starch Oxygen Chromate Ammonium Molybdate Phosphate, Silica liydrazine Sulfuric Acid Oxygen, Fluoride Oxalle Acid Silica Glycerol (Clycerin)
Oxygen I
l-Amin 2-Napthol Silica, Phosphate A
u n
Ac M llydrochloric Acid Chromate, Fluoride Indigo Carmine Oxygen Silica, flydrazine Sodium Sulfite Silica Phosphate Dex t. rose Oxygen Paradimethylamino-Ilydrazine Manganese Standard Manganese enza ehyde Potassium flydroxide Oxygen Boric Acid Ammonia
^** " "
Sodium Standard Sodium Sodium Metabisulfite Phosphate
^ * " " ' "
pil linf rer.s Various Sodium Bisulfite Silica
^ " " " "
Fluoride Fluoride Barium Cnloride Sulfate
^ " " " " "
Lithium Standard Lithium Sodium Chloride Sulfate Alizarin ited S Fluoride Phenolphthalein Alkalinity Calcium Stanlard Calcium Zirconyl Chloride -
Fluoride "E"**'""
" 0 " " **
Octahydrate Methyl Orange indicator Alkalinity Copper Standard Copper MeM Pgk MMu mdMy Iron Standard Iron L.J1 CA N
EXHIEIT V TABLE 2 IXPECTED CHE!! CAL CHARACTERISTICS OF OCCLING PC:D 3LC'a'DC'4N NC CCM3I:!D PLA'IT DISCHARGE Cooling Pend Slowdown Cc=bined Plant Discharge
(?!cde 7, Figure 1)
(:Icde 60, Figure 1)
Average / Maxi ="-
Average / Maximum (c) 2l Parameter Concentration (
Concentration (a) i pH 6.5-9 5 6.5-9 5 1I TSS, =g/l I:ct Available/(lCO Not Available/CCC TDS, =g/l 880 2200 900/2500 Ca, =g/l 15 540 150/520 Mg, =g/l 40 130 40/120 h, =g/l 60 210 70/270 So, =g/l 120 150 140/660 a
C1, =g/l 130 410 130/400 2
Poh, =g/1 0.18/0.84 0,18/0,31
- TH, =g/l 0.20/1.5 1.67/20.4 3
Ag, =s/l]
0.006/0.04 0.006/0.04 Eg, =ge 0.003/0.02-0.003/0.02 Pb, =g/l (b) 0.04/0.18 0.04/0.17 Ni, =g/l 0.03/0.11 0.03/0.11 2n, =g/1 0.05/0.22 c.05/0.22
('ag.
Chlorination of water syste=s and ecoling pond acid treat =ent are esti=ated to increase the valurs given as follcws:
avg.
=ax.
Na,=g/1
+5 vis C1,=g/l
+8
+22 S0g,cg/l
+200
+1100 2
Assu=ing the cooling pond blowdevn vill be terminated and the avaporator building and Unit 1 & 2 neutralizing sumps (nodes 47 & 45) vil' be routed to the cooling pond when discharge to the Tittabawassee River 3uld cause the River to exceed permit limitations, then the following incree.se in chemical concentrations are expected in the coolirg pend:
Para =eter Maxi =u= Increase ILS, =g/l 70 NA, =g/l 15
=g /l ko 23,=g/l h
y (b) Concentrations listed for these =aterials result frc= pond evaporative cen-centration of a=bient levels of these =aterials, see Exhibit VIII, : Tote 1.
1 (c)
.Vaxi=u concentrations were ce=puted using the =ini== blevdown flev (5 cfs )
and the maxi =um instaneous vaste discharge rates.
}$Q MENmE:.'I 2 7-6 J mz 1, 1979
EX'4IBIT V TA3LE 3 Area and lenzth of the 5 ? : other from Alden Research laboratorv Test Daca Q
Laboratory Q3 dT3 Area Length (cfs)
Test No.
(efs)
( F)
(aeres)
X (ft.)
835 292 25 15 0 0.18 Sho 288 13 19 5 0.32 860 290 9
25 1 0.17 600 1,305 329 73 12.2 0.h0 1,210 336 23 22.6 0 39 1,090 331 130 10.0 0.17 210 333 11 35 3 0 37 1,100 I
2.065 355 137 12 3 0.21 200 35h 73 13 9 0.29 320 3h3 73 13 3 0.29 830 3h2 73 2h.2 0 71
. 350 3k5 35 23.8 0 51 1,230 298 20 29 5 0.27 800 301 15 39 5 0.27 810 3,015 307 73 19 5 0.32 830 311 25 h2.3 0.50 1,260 350 100 18.1 0 30 720 305 73 29 7 0 51 1,200 3,515 322 1h3 17.8 0.63 1,010 320 73 28.5 0 58 Tho 278 L5 h0.0 0.37 Tho 317 77 35 9 0.37 550
'a nere,
Q = River flev rate directly upstrea= of the bicvdown (including plant makeup and Dev discharge).
Q3 = 31cvdown Flevrate AT3 = Te=perature of the blevdcun minus ambient river temperature.
X = Distance frc= bicvdown discharge structure to point of isether closure.
AEIDEIT 1
'l - 7 L 7 - 3 00:03IR 20, 1973 1456 l59
EX'4I3IT V TABLE h Estimated Distance for Closure of 1 F Isotherm f:r the Laboratory Tests with the Longest Isother in each River Flev.
4 3 Length Q
Laboratory QB (efs)
Test No.
(cfs)
( F)
X (ft.)
835 292 25 15 0 11,000 1,305 329 73 12.o 13,000 2,065 3k2 73 2h.2 L2,000 3,015 305 73 29 7 21,000 1
3,515 322 1h3 17.S L2,000
'4here, Q = River fievrate directly upstream of the blevdown (including Flant makeup and Dev fischarge).
^ 3 = 310Vdown flovrate.
AT3 - Temperature of the blcvdcvn minus s bient river te=perature.
X = Distance fre blovdown discharge stru::ure to point of is0thern closure.
1456 160
..'a.
tb'*L.4
< = 0,
, L. 0 2.~.
cJ,.yiO
I EXHI3IT V TABLE 5 EXPECTED CHDf! CAL CHARACTERISTICS CF PLA'IT DISCHARGES PRICR TO CC:"ERCIAL OPE?ATION l
1.
Flush '4ater (vaste water frc flushing syste=s after constructien)
Parameter Expected Value Frequency of Discharge Varies Volume of Discharge h,000,000 gal /yr for 1979, 1930 L 1981 pH o-8 TDS, =g/l
<200 l
TSS, =g/l (100 1
Effect of discharge to pond No measurable effect 2.
Hydrestatic Test ~4ater (vaste water frc hydrostatic testing of systems)
Parameter Expected Value Frequency of Discharge Varies Volume of Discharge 1,000,000 gal /yr for 1979, 1980 & 1931 pH o-3 TDS, =g/l 4 200 TSS, ng/l 4 100 2
FluoresceinDye,=g/l(condenserhydroonly)
(0.4 No nessurable effect Effect if discharged to pond 3
Syste lav-Un Discharres (as necessary to drain systems fer reverk after chemical lay-up)
Parameter Extected Value Frequency of Discharge Varies Volume of Discharge 1,000,C00 gal /yr fcr 1980 1 1981 pH 93-95 "TS, ng/l
< 50 TSS, =g/l
< 10 1
NEa, g/l 2 - 20 N N, =g/l 200 - 500 2k Effect of discharge to pond All chemicals vould be diluted approximately 10,0C0 tc 1 AME:C:-E:C 2 V - 9a JC a 1, 1979 1456 161
EXHI3IT V TABLE 5 (Cont'd) k.
Auxiliarv Boiler Cleaning (vastes generated during initial boiler toil out)
Parameter Expected Value Frequency of Discharge Once Volume of Discharge 10,000 gal pH 9 - 11 TDS, eg/l 10,000 TSS, mg/l 1,000 Fe, eg/l 1,000 F0, =s/l 5,000 h
1 Effect of discharge to pond All chemicals would be diluted by at least 100,000 to 1 5
Auxiliary Boiler 31cvdown (required during operation to maintain boiler water quality)
Earameter Expected Value Frequency of Discharge 2/vh Volume of Discharge 3,000 gal /vk or 150,000 gal /yr pH 93-95 TDS, =g/l 4 200 TSS, =g/l
< 10 Te p, "F 300 NH, eg/l 4 10 3
NgHL, eg/l
< 2 Effect of discharge ' o pend All chemicals vould be diluted by at least 20,000 to 1 AMEUD;E3D 1 V - 9b October 20, lo78 1456 162
EXHD1" V TA3LE 5 (Cont'd) 6.
Construction Chemistry Lab Trailer Wastes (wastes generated by wet chemistry perfor=ed in te=porary lab trailer).
Sumary of Chemical Discharge to cooling pond, Septe=ber 5,1978 through April 20, 1979 Total Amount Chemical Discharged in Kg Amino Napthol Sulfonic Acid 0.004 Ammonium Molybdate 0.008 Ascorbic Acid 0.980 Boric Acid 0.vy9 CDTA 0.008 Disodium EDIA 0.536 Ferrous A== onium Sulfate 0.110 Olacial Acetic Acid 0.069 Hydrochloric Acid 0.298 Lead Perchlorate 0.001 Nitric Acid 0.432 2
Oxalic Acio 0.080 Phenciphatelein 0.008 Potassium Biphthalate 0.057 Potassium Chloride 0.165 Potassium Chro= ate 0.400 Potassium Hydroxide 0.530 Potassium Phosphate 0.030 Silver Nitrate 0.040 Sodium Borate 0.010 Sodium Chloride 0.009 Sodium Fluor'ide 0.116 Sodium Hydrogen Sulfite 0.240 Sodium Hydroxide 0.924 Sodium Metasilicate 0.002 Sodium Phosphate 0.108 Sodium Sulfite 0.008 Sulfuric Acid 0.078 Zine Acetate 1.~60 Total.......
6.410 1456 163 A!ENDME:iT 2 V - 9e JUNE 1, 1979
EXHIBIT 7 N" TACH'E A Description of Field Survey Study Field surveys of the plume resulting frc= Ocv Chemical Cc=pany's tertiary pend effluent into Tittabavassee River were =ade in the conths of July and October of 1977, for a river flew of about 400 and 1100 ers respectively. The Dov discharge was located about 2000 feet upstrea of the Plant river intake structure during the field tests and has subsequently been relocated approxi-
~
=ately 200 feet downstres= of the Plant river intake structure. The cenductivi-ty of the tertiary pond effluent was used as a tracer.
Data was collected at 5 to 11 cross sectiens during each survey. The cross sections were spaced apprcxinately 1200 feet apart except in the vicinity of Dov's discharge where a few sections were spaced approximately 150 feet apart, and around bends where sections c00 feet apart were surveyed. The total length of the river reach surveyed was about 12,000 feet end the location of the cross sectiens is sh0Vn in Figure A2.
Measure =ents consisted of river depth, velocity, and conductivity readings taken in 20 to 30 vertical intervals of each cross section. A Price curr'nt =eter obtained frc= the US Geological Survey (USGS) was used for velc-e city measurements. A top-setting vading rod was used to positi:n the meter duringtheJulysarveyswhen{gyriverwasshallevandabeat,scuntedwiththe USGSprocedures(b)gequipment necessary =easurin
, was used during the October surveys. Standard were followed for the velocity measurements and subsequent discharge calculations. Cenductivity was measured si=ultanecusly with veiectty reasurements using a Yellow Springs conductivity =eter (ISI Medel 33).
Con-ductivities near the water surface and near the river bottc= vere measured to check the vertical variation of conductivity which was found to be substantially constant with depth, indicating that complete mixing cecurred in the vertical directien.
Analysis of the survey data began by pict ing the measured river depth. velccity, and conductivity versus transverse distance for each cross sectien.
Survey results for October 16, 1977 are shown in Figures A3 and AL.
Values of the dimensionless cumulative discharge frc the right bank icoking downstres: vere cceputed and conductivity versus dimensienless discharge profiles were c n-structed and are shcun in Figure AS.
The concentration profiles were develcred in this manner so that the strea:-tube =cdel described in the rathematical model section of this attachment can be applied. The conductivity of ambient river was either actually reasured or estimated frc= easured concentration pr: files.
The 1=bient value was subtracted fr0= the =easured conductivity level 30 that the " excess conductivity" could be defined and used in the stres:-tube =0 del.
The excess cenductivity profiles established stove were used in tha cathematical model as upstres: boundary conditions.
This requirei dividing each profile into 10 to 15 segments and determining an equivalent line scurce f:r each segment. Additional data censisted Of the :::a; river discharge, an estimated 1456 i64 7 - 10
value of the constant diffusien facter D for the river reach under consideratien, and the distance to the devnstrea= section where a conductivity profile was ceasured. The D value was then adjusted by making =ultiple runs of the mathematical model until a best fit of ec=puted excess conductivity profile to the measured devnstrea concentration profile vas obtained. The measured downstres: profile was then used as the upstrea= boundary condition for the adjacent downstres= reach. By repeating this procedure, D values for each river reach vere determined.
T_s constant diffusien facters which yield the best fit to the survey data are given in T3ble A2.
The transverse diffusion coefficient K and the dimensionless constant E, both defined in the cathematical section, wd,re computed frc= D and river flev characteristics and are also listed in Table A2.
The estimated E values vary " rom 0.2 to 2.7 for the various reaches of the Tittabavassee River that were studied. In crder to be conservative in modeling the physical effects of the Plant discharge (Reference ) and in =cdeling radicauclide transport p value of 0.23 was used.
Descrintion of The Physical Model A reach of the Tittabavassee River extending 100 feet upstres= te 2000 feet devn-ctres of the river intake structure is simulated in the physical =cdel (Figure A1) at a scale of 1:15 The =odel topegraphy is constructed en a wood fra=e consisting of templates cut to reproduce the river bottc= centeurs and is covered with plywood to ecnfor= to the topography determined frc= field surveys.
The plywood is sealed with a layer of polyester resin. The detailed features such as the river intake structure and the Dov Chemical 0 =;any and Midland Plant dis-charge cutfalle, shown in Figure A1, are also constructed in plyvood sealcd with a resin ccating. The flow field devnstres= frc= the Plant discharge struc-ture can te divided into two regicns; the near field, and the far field.
In the near field the dilution of effluent with the river is primarily iue to jet mixing.
Dilution in the far field is achieved mainly by transverse convection and turbulent diffusion processes. To =cdel the hydrodynamic mixing in the near field, it is essential to have undistorted ge =etry and to ensure the equivalence of the Froude numbers in both the prototype and the =0 del.
Tr.e Feynolds number la not medeled, but it must be kept high enousa to ensure turbulent flcw fr = the
=cdel diacharge structure.
Equating the prototype and =cdel Frau a -"-bers d
yields U
U 2
= y y
=
,=/gH
/gH (a)
=
p where the subscripts p and = denote prototype and model, U and H denote a char-acteristic velocity and depth, respectively and g is the gravitational accelera-tien. This equality ensures that phenc=ena influenced by the veight Of fluid vill be similar in both the =0 del and the prototype.
It is also necessary to equate the densi=etric 7rcude nu=bers in bcth the model and the prototype t0 ensure proper representation of bucyancy effects U
U e
(3) z 7 =
=
o
~~
@D./P)p$H, 3 D. /0 )m. H 2 =
1456 165 cr F = U. (4J1 H)r~
(c)
-F V.*u
where the subscript r density the ration between =0 del and prototype, and 4 p/p is the density difference which depends nn both temperature and Total Dissolved Solids (TDS) concentration. The selectic:. of a length scale ratio of 1:15 re-sulted in the scale ratios of Table Al which were calculated frc= the continuity equation and equations (a) and (b).
Tv0 =ethods of operation vere empicyed for modeling conveniences; ence-through cperation and recirculatien of the model river flow. For the once-through cperation, a constant-head reservoir supplied the flov via a supply line. F10v-rates were =easured by a Venturi meter in the line. The f10v was then introduced into the =odel at the upstrea: trough. Saffles were used to distribute the flew across the entire width of the model river. At the downstres: end the water fleved over a tailgate and was discarded. Air temperature inside the building housing the =odel was lowered to a level close to the model river water temperature so that undesirable heat transfer fr0: the air to the model was ~*a4-'~ed.
Fcr the recirculaticn operation, water flowed into a su=p after leaving the redel and was pumped back into the supply line. A small a=ount of water in the sump was replaced by cold fresh water fro: outside so the =odel river water temperature could be maintained at a constant level.
The Dow Chemical Cc=pany tertiary treatment pond discharge was simulated using a hot water boiler connected in parallel to a saturated brine storart tank.
The relative density of the discharge flow vaa maintatned by centrolling the te=perature and brine (TOS) eencentration in the flov. The discharge flav was continually =0nitored with an in-line crifice plate metering section. The Plant discharge was similarly =0 deled, alth0 ugh its relative density was raintained by ad*usting enly the water temperature which was achieved with a boiler and a sixing network. The cooling pond makeup water was withdrawn thrcush a ge0:etrically similar structure via a s=all p;=p.
The withdrawal flow as well as the discharge flow were 20nitored by in-line crifice plate =etering secti:ns.
Surface and near bott vater vel: city reasurements were made with a calibrated miniature propeller meter. Temperature measurements in the 20 del vere 2:00 p-lished using a matrix of about 230 copper /censtantan ther:0ccuples. These probes were used to reasure surface and vertical temperature profiles thr0 ugh-out the model, in addition to critical temperatures for model :peration such as air temperature, discharge temperatures, and river inflov temperatures.
The ambient river temperature was 20nitored by three probes located in the upstress ficv distrit ;ien trough. The thert couples 20uld be scanned at desired time
'. :ervals and the excess temperature (vater temperature less ambient river temper-
.ture) at various locations could be displayed a::Ording to ther=0:0uple positions.
Further details cf the model and its cperation are contained in Reference 1.
Descrittien of The Mathematical Model-?cr Transverse Mixing Of Sclutes in Natural Strea:s The mathematical :: del is basically the strea tube =0 del Originally prepcsed by Y0tsukura and Cobb (2) adopted by the U S Nuclear Regulatory C:::issionl0l.
The : del was developed for the transverse diffusion of solutes frc steady stur:es placed in a natural stream with steady discharge.
Censity of water is assumed t: be h:20geneous through:ut the systen. Vertical variations of solute 20ccentration, velocity, and diffusi:n ::efficie;t are negie:ted through the use of depth averaged values.
As a result of t' ese assumptiens, the predicted r
solute plume is two-iirensicnal. The applicability of the strea tube :: del to the Tittabavassee River was verified by a cutter of field surveys of a
- AC/
144 st t
7 - 12
cor.ductivity plu=e resulted fren Dov Chemical Cc=pany't tertiary pend effluent into the Tittabavassee River near the Plant. A description of the field surveys has been previously described.
The theoretical deselopment of the =cdel involves the derivation of a diffusion equatien by balancing inflov and outflow of solute mass in a control volume.
Tae dependent variable is the solute cencentration and the two independent variables are longitudinal distance alcng the river and transverse cu=ulative discharge, q, frc the river bank:
q=
ud dy (d) o where y = transverse distance from river bank u = local river velocity at y d = local river depth The use of the ca=ulative discharge instead of the transverse distance frc the river bank enables a closed fers solution to be found fer natural rivers with irregular channel cross-sections. Boundary conditions are :ero solute cen-centration gradient at both river banks and a known solute concentration profile at the upstream end of the river reach to be studied.
The strea=-tube model as originally formulated only applied to cituations where the upstream solute concentration profile resembles a point source or a constant strength line source perpendicular to the river flev. To treat variable solute concentration at the upstres= boundary, a collection of short ecnstant strength line sources was used to approximate the variable solute cen-centration profile. The stres=-tube model was applied repeatecly with each shcrt line source as the upstres boundary condition and the solutions were added.
The solution obtained by this superposition is valid since the diffusien equation is linear.
The only parameter appearing in the diffusion equation is the constant diffusion factor D.
The evaluation of D requires a separate estination of the diffusion coefficient y$1ng Elder's e=pirical equatien 'gd frcs the river properites and river flev [ which, in turn, can be deternin t
K = SU"3 (e) y where 3 = average rfver depth, it U* = shear velocity, ft/see E = a dine.asicaless constant Values of 3 and U" can be calculated frcm field seasurements of river cross section shape, Jepth, flow and vat.c surface slope. The value of 3 can be de-termined frcs the stres:-tube =0 del, field measured solute concentration prefiles, and the riv r data =entioned above. For straight rivers, 3 has a 7alue cf apprcxi-mately 0.23 31 For curved channels, )
transverse =ixing by secondary currents t,is) larger than 3.23 due to increased The constant diffusion facter D can be calculated utilizing the value of 5, Ob-tained frcs Iquatien (e):
1456 167 K7 2
3 = q' ud dq (f)
=
o 7-12
Where Q is the total river flev The values of E and D for the stretch of the Tittabavassee River adjacent to the Plant during July and October of 1977 vere estimated frc= field data and are tabulated in Table A2.
After finding D for a river reach and after defining the upstres: solute con-centration versus cunulative discharge, a profile of concentration versus cu=ulative discharge at the dovstrea= end of the reach can be co=puted fr0= the
=athe=atical model. For the next reach downstrea=, this profile is used as the upstrea= boundary condition together with a new value of D to compute the con-centration profile at the devnstrea= end of the reach. By repeating this pro-cedure the lateral transport of a solute over a large distance downstream can be evaluated. By knowing the solute concentration versus cu=ulative discharge pro-fi.les and the distribution of river flow vithin each river cross section, the transport of a solute in the river can be adequately described.
References 2
1.
Alden Research Laboratories, "Hydrother=al ttdel Studies, Coolirg Pond 31cvdown Discharge. Midland Nuclear Plent" Final Report 45-79/:a24AF, April,1979, 2.
Yotsukura, U. and E. D. Cobb, " Transverse Diffusion of Solutes in Natural Strea=s, " U.S. Geological Survey Professional Papar 582-C, 1972.
3 U.S. Nuclear Regulatory Cc==ission negulatory Guide 1.113, "Esti=ating Aquatic Dispersica cf Effluents fr0m Accidental and Ecutine Reactor Releases for the Purpose of I=ple=enting Appendix I", May, 1976.
h.
- n. der, J. W., "The Dispersion of Marked Fluid in Tarbulent Shear Flav,"
Journal of Fluid Me:hanics, No. 5, pp. Shh-560,1959 5
Yotsukura, 3. and W. W. Sayre, " Transverse Mixing in Natural Channels, Water Resources Research, Vol.12, No. h, August, 1976.
6.
U.S. Geological Survey, ' Discharge Measurements at Gaging Statiens,"
Chapter AS of Techniques of Water Resources Investigations of the U.S.3.5, 1969 1456 168 AENDE:TT 2 V - 14 JUNE 1, 1979
TABLE A1-MODEL SCALI' RATICS Model to Prototype Characteristics Dimension Scale Ratic Length L
L = 1:15 Area L
A = 1:225 Velocity L/t V = 1:3.37 Time t
t = 1: 3.87 3
Discharge L fg q
,1 371,3 Temperature o?
T = 1:1 r
TDS pt:
C = 1:1 r
1456 169 V - 15
TABLE A2 SlM!AltY 017 TI'PPAHAWASSEE RIVER FIELD STUDY RESl1UPS Measured River Average Average Cross Section Date of Discharge Velocity Depth Ambient River' Reach Length C_omputed Diffusion Parameters Number Survey (cfs)
(ft/s)
( t )
Conductivity (pmho/cm)
(ft)
Dtft>/s2) Ky(ft /s)
Il 2
'(
- ( 16 '(7 am 410 1.41 1.4 660 600 2.5 O. 31 1.6 8
'(-16-77 pm 390 1.h6 2.1 660 600 0.T 0.09 0.h 9
7-16 '('( pm 360 1.01 1.9 660 600 0.7 0.12 0.6 10
'(-16-77 pm 380 1.09 1.8 660 600 07 0 9h 0.5 11 7-16-77 pm 390 1.20 15 660 600 07 0.06 0.4 12
'(-17-77 pm 380 1.15 1.6 620 yggg.
0.2 0.02 0.2 13 7-16-77 pm 360 1.29 1.3 660 600
- 0. T 0.10 0.7 1h 7-l'l-77 pm 380 1.3h 15 620 600 07 0.09 0.6 15 7_j7-77 pm 380 0.99 1.3 620 a
1200 07 0.1h 1.0 16 7-17-77 um h10 1.12 1.h 620 1200
- 0. '(
0.13 0.8 l'(
'/-l'(-T( run 450 1.18 1.8 620
'(
10-8-T( pm 1150 1 72 2.1 h50 500 116 0.52 1.2 8
10-8-T( am 1160 1.54 4.0 450 1300 3
0.10 0.2 10 10-8 '(7 pm 1220 1.60 2.3 h50 4
1220' 8
0 38 1.1 m 12 10-9 '('( am 1180
- 1. '(0 3.0 450 lb 10-9-T( pm 12hD 1.53 2.1 h50 4
0.27 0.8 N 16 10-9-T( pm 12'(0 1.l b 3.0 la 50 1910 i
CD
TABLE A2 (cont)
Measured River Average Average Cross Section Date of Discharge Velocity Depth Ambient Riv.er Reach Length Computed Diffusion Parameters riamber Survey (e rs)
(ft/s)
(ft) conductivity (nmho/cm)
(ft)
D ft)/s2 Ky(ft /s) _J 2
41 0 3
30-15-77 am 1080 1 57 2.6 4
950 6
0.4h 1.6 7
10-15-77 pm 1050 1.62 1.9 440 1800 7
0.57 2.7 10 10-16-77 am 1050 1.66 1.9 440 4970 15 0.11 0.4 16 10-16-77 pm 1000 1.36 2.5 h40 4590 10 0.38 0.2 20 10-16-77 pm 950 0.64 6.2 4! 0 4
s M
Cn m
~
~
m G
e
c EXHIBIT V ATTACEMENT 3 THERMAL PLUME EFFICTS Operation of the cooling pond blevdown syste for:s a thermal plume in the Tittabavassee River. The thermal plu=e consists of two parts, the near field and the far field. In
+>e near id the blevdcyn discharge dilutes rapidly with river water through a jet =ixing process. Further =ixing in the far field is =ainly due to transverse convection and turbulent diffusion. The thermal plume is simulated by a physical river =edel for the near field and by a rathematical :odel for the far field as described in Attachment A.
Heat loss from the thermal plu=e into the atmosphere was not considered.
Dev Chemical Cc=pany discharges its tertiary pend effluent into the Tittabavassee River at about 300 feet upstream frc: the Plant blevdown structure. Both dis-charges are at the south bank of the river and are shown in Figure A1.
The excess temperature (temperature of the effluent less a=bient natural river temperature) of Dov's effluent is incorporated into the Plant thermal plu=e si=ulation.
Ph,ysical model test results (Reference 1) in the near field resulted to the 1~F isother s shown in Figures 31 to 35 To extend those isother s in the far field, the transverse convection-diffusion =athematical model of Yotsukura and Cobb (Reference 2) was used. Parameters needed in the mathematical medel include river cross-sections and their velocity distributien as well as diffusien factors.
The Tittabavassee River gec=etry, river flow distribution, and excess tempera-ture at the end of the near field (Section A shcvn in Figure 36) are used to initiate the far field thermal plume rathematical medeling. The linkage between near field and far field is based en an excess temperature versus dimension-less cumulative discharge profile at Section A which is used as the upstrea:
boundary condition in the mathematical medel.
Diffusion factors for the reach of the river extending frc: the near field to Section 3 (shown in Figure 36 at Gardenville Rcad) have been ec puted for a range of river discharges based en field data cellected during July and October of 1977 Although no detailed field data is available for the reach cf the river downstream of Section 3, the Corps of Engineers has made a survey at the
^
Smith's Crossing Read bridge which is shown as cross-sectica No.10 in Figure 2.h.19 of Reference 3 This cress-section is quite s*
- 'a- +- Section 3.
The river was also observed en several occasions at the Smith's Crossing and Freeland Road bridges (Sections C and 3 shown in Figure 37), approximately C.5 and L.5 mile downstream of Section 3, respectively. The river cress-sections at th se locations resemble that of Section 3, having steep banks, siev =cving current, and a deep channel. Based on these observations, it was assumed that the Tittabavassee River characteristics downstrea= cf Section 3 are similar to these of Section 3.
The diffusien factor for this part of the river was, therefore, determined frc the hydraulic preperties reasured at Section 3.
1456 172
_ m.
, e
___c_
- hdc80-be
- Y
- ev V w.,v $,b 6 ddy E l
After determining the diffusion factor for a river reach and after defining
,the excess te=perature versus cumulative discharge, a profile of excess te=pera-vire versus cumulative discharge at the downstrea= end of the reach was com-puted from the mathematical model. For the next reach downstrea=, this profile was used as an upstrea= boundary condition together with a new value of the diffusion factor to co=pute the excess temperature profile at the downstres:
1 end of the reach. By repeating this procedure, the lateral transport of the thermal discharge over a large distance downstrea= vas evaluated resulting to the lengths of the 1 F isotherms listed in Table h for each river discharge.
The distances should be conservative since the =athematical model does not account for surface heat transfer to the atmosphere. Due to the lack of in-formation on river cross-sectional shapes and velocity profiles dovr.strea=
from Section 3, isother=s could not be drawn for the far field.
References 2
1.
Alden Research Laberatories, "Hydrotherrd Model Studies; Cooling Pond 31ovdctm Discharge, Midland Huclear Plant" Final Report 45-79AD.24AF, April,1979 2.
N. Yotsukura and E. D. Cobb, Transverse Diffusion of Solutes in Natural Strears, Professicnal Paper 5'82-C (1972), U. S. Geological Survey.
1 3
Consumers Power Cc=pany, Final Safety Analysis Report. Midland Plant-Units 1 and 2.
MECEC 2 7 - 19 T 3 1, 1979 1456 173
THIS PAGE I: iter:CITALLY LEFT 3LA'IK 1
(As a result of the data obtained in the September,1978 studies the information previcusly presented in Table 31 is no lenger applicable.)
1456 174
~
,u e c:.e c 1
'l - 20 OCTCEER 20, 1978
1 GiIS PAGE I:iTEITIONALLY 1 EFT BLtdIK (As a result of the data cbtained in the September, 1978 studies the infornation previcusly presented in Table 32 is no longer applicable.)
j.l.Ein:.EIT 1 7 - 21 CCT03ER 20, 1978 1456 175
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K L
H 16ko 18+O I4 +0 N
L 10 +O F
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s RIVER 8+10 1
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i B
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\\
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A btO MIDLAND 8 LOWDOWN DOW OISCHARGE RIVER INTAKE STRUCTURE
' FLOW ET$R i
1456 176 FI GURE A1 PHYSICAL MODEL LAYOUT MIDLAND PLANT UNITS 1& 2 CONSUMERS POWER COMPANY
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~' +,,, - g g 4-LE@ 5 J 'RQ l=359 9% i go i BECHTEL -E o., .A= d 1 i MIDLAND POWER PLANT g LOCATION OF RIVEH CHOSS SECTIONS [I i iN COOttNG POND Bt OwoOWN STUDY i ~ _m ut AMENINENT I 7220 FIGURE h6 OCTOBER 20,197') i g g G L' - 4 'l.'3 D
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e,, EXHIBIT VI DISTANCE OF 3 EADIE'!T FACILITIES FROM NEAREST '4 ELL The plant site is located within the distribution system of the Midland Munici-pal '4ater District which draws its supply from Lake Huron. The nearest known private wells in Lae are located on the plant site. These tells supply non-potable water for construction activities, primarily the preparation of concrete, and for hydrostatic testing and flushing activities. 1456 188 '/I - 1
., i.* EX9IBIT VII PROPERTY C'4IIED.S ADJACEIT TO PROPOSED E'TTERPRISE "'he evners of property adjacent to the Midland Plant are listed belev. This information was ec= piled frc= the December 31, 1977, City Assessor and County Equali::stion platt caps. The Dow Chemical Cc=pany Mr Clayton Badgero Michigan Division 3248 Miller Read Midland, Michigan Midland, Michigan h86h0 Rullock Creek School Mr Arthur Fisher Poseyville Road 3239 E Rullock Creek Drive Midland, Michigan 486h0 Midland, Michigan h86k0 Consumers Power Cc=pany Fisher Contracting Ccepany 212 ' Jest Michigan Avenue 921 Jeffersen Avenue Jackson, Michigan k9201 Midland, Michigan 486h0 Mr '4m Linten Mr 'in Sasse Rt 10, 3156 E Gardenville Rd at 10 Midland, Michigan 486h0 Midland, Michigan h86h0 Francis Goulette Mr Daniel Hart hh39 :T East =an Read Rt 2 Midland, Michigan h86ho Freeland, Michigan 38623 Mr Jerry Rare E11sie Spangler 702 ' dest Ellsverth Rt 10 Midland, Michigan h86h0 Midland, Michigan h86h0 Mr Earl Roebuck Mr John Helmes Rt 10 Et 10, 3h22 E Gardenville 3d Midland, Michigan h86h0 Midland, Michigan h86LO Mr Roy Robertson Mr '4 alter Rennet Rt 10, 3hl2 E Gordenv111e Rd 1555 Sassee Road Midland, Michigan h86h0 Midland, Michigan h86ho Mr 'im '41neland Mr 'im Mergard 3632 E Gcrdenville Ecad 323 Potava cn Mid]and, Michigan h86h0 Royal Oak, Michigan L600 V!! - 1
= e,4 +, -.U. *T ' T* Tf? ?. *1 7Y. 34. v CRITICAL MATERIALS L!5T New critical materials were added to the Critic. _. Materials R?gister en October 1, 1977 Caly the following of these new critical =aterials are expected or proposed to be used, or are incidental to the plant's operation: Name A= cunt (1bs/yr) Hydrazine 25,000 2 Hypochlorite 693,0c0 Lithium 20 Dimethyl A=ine approx.10,000 Triaryl Phosphate Esters Not Available The reported critical =aterials are expected or proposed to be used in plant cperations as described belev. A==onia: A==onia vill be utilized in the plant stes: cycle and auxiliary steam syste for pH control. Chrc=iu=: Sodium dichrc= ate vill be used in the plant closed 100P cooling 2 syste=s. Equip =ent drains frc= these syste=s will be collected in-portable containers and returned to the systems. Copper: The plant main condensers are tubed with admiralty metal. The value reported is an estimate of the circulating water copper pick-up. Hydracine: Hydrazine vill be utilized in the plant ste1= cycle, auxiliary steam syste=, and reactor coolant syste (temporary shutdevn only) for oxygen scavenging. Eypochlorite: Sodiu= hypochlorite vill be used to control biological growth on the main ecndensers and service water heat transfer surfaces. Lithiu=: Lithiu: hydroxide vill be used for pH centrol in the reacter ecolant systems. Dimethyl A=ine: This chemical vill be used as a reagent in the on-line steam cycle sodium analyzers. Triaryl Phosphate Esters: A triaryl phosphate ester vill be used in the stes= turbine electro-hydraulic centrol s; stems. Istimated quantities ?.re not available because a vender for turbine oil has not been selected. Cther compounds listed on the Critical Materials Register, as revised en October 1,1977, may be included in c0==ercially obtained fer=ulations of varicus 301-vents, fluids, and solutions which are incidental to plant cperatien.
- EcVever, these ec==ercially obtained
'---"'a-icns will be used in acecriance with manu-fseturer's instructions and are not prcduced or altered On-site. }{ }hh Notes to Ite: 12 Note 1: This =aterial has been detected in the plant's proposed cooling water MCEElf 2 l'aa Jine 1' '97o
,,
- 6,e supply (Tittabavassee River) in the concentrati:ns lieted below.
As such it is incidental to the plant's operation and discharge. 2l Ag 0.007 =g/l I Hg 0.005 =g/l Pb 0.033 =r/l 2[ Ui 0 02 :6/1 Zn 0.033 =g/l (It is anticipated that these =aterials will te concentrated in the cooling pond blevdown to the same extent as pond cycles of concentra-tion, see Exhibit V, Table 2.) Note 2: This material may be used on-site for grounds =aintenance. Use vill be restricted to co==ercial applicators who are licensed by the State of Michigan and will be performed under direct supervisien of trained foresters. Only appropriate herbicides approved by the FDA and EPA for the intended use vill be applied, and they will be applied in strict ec=pliance with manufacturer's specified solution strengths and rates of application. AEDEC2 VIII - 2 JU:G 1, 1979
7 l 6 1 5 l e g ~ ~ F d TITTABA 1i esTAq -= FD.m.L E.A.f.5 os C k;y r_>_- d.) Q ,.o ...e. ,.o, o.a Q _ _ _ _ _ r,) Q __- 1 _ _ _ _ _ q _ EA_o **m_sur e _ _ _ _ _ _. _ o m...Y. i Au .. ri eve. u== r qr ,,,,T,. 9 ' _fj),antoue.- h DR A#4 AGE 8 Il w re esa SEEPast it petCIPrTAILou Q C00LJeG F IRE 27 --W@_____ Go enof fCTION sysTru $e _,,,,, --e O y in' &[ q . q_ ='. c. m=_ _ _ _ _ _ _, [U* TSSh?ic'd Conotusras 4 o fa = s<su-Ul IN r ___g_._________ ,,,,C, lJ q q _ EU'O'alige gy_,, ,aTER Y COOLDs0 ci dsl E"'II--- ~ ~ h - tower C6 A P g Ff ED-4 I Dow O PROCESS LNTS 682 0 Cabewif Mg pmoc sTEau ,ST,E AM CDf esCAL SERva ~ v y Tgu w&TE R tone g \\ g3 van atowoow= g m e2.o.. t~~- To siYg smst Tm ovEnstow Q *_'0" DRA'"3 ,_aphan_cuytag garts._,C7 Q pu ""'YT' .l Sa'!,nJv - "- -0 e-501W ~ ~ ~ ~ ~ ~ v eCILER + CoLLsn Fixtunts I i ' 3 79 i& 2 C.LOgED.6TpG o_-@ I R t_ i. ~ mG= i i_.__ wp i L_ 1 Floo# ORA DEhrti e h Don.f e CLE AN'he gangTAny W EM l p-- ymm c --."41 - ! -u T seu snTEu -45~ '^rmTunes 4 w,,i.,T emarmy t,,Ts v g i V t.___________ FEEDWATEM S t g sn m Lp 6 uAG%rTic F RTE R LfAf tw U I LAprwa l LAstav wTs ia2 B [i}-* FaCaJTY - \\5 M4 WASTE TmT f* r etacTom l svbrEM PLANT SY5 TEN. _ _ _ d h l e W FLoc ser=T F Pook 1, y NUCL,, EAR $YSTEM W ATER USAG f Node i 2 3 4 5 6 7 8 9 10 H 12 13 1 h.M ses
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