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Harry G. W oo, .
- Executive Vice President ,=...- ./ 1DOCKETE
Consolidated Edison Company of New York. 1 8 1972 5 4 Irving Place. New York, N Y 10003 REGULATORY Telephone (212) 460-6001 MAIL SECTION ~DOCKET CLERK
0) ebruary 16,
Regul~ator e .0y. Dr. Lester R. Rogers, Director Division of Radiological and Environmental Protection
U.S. Atomic Energy Commission 01
Washington, D. C. 20545
Re: Indian Point Unit No. 2 .r-.
Docket No. 50-247
Dear Sir:
Enclosed herewith are copies of the following documents which have been requested by your consultants at the Oak Ridge National Laboratories:
1. Statement of Method of Determining Residual Chlorine in Chlorinated Condenser Water.
2.- Explanation of Manner of Operation of Chlcrination System.
3. Calculated Chlorine Residuals for the Combined Operation of Indian Point 1 and 2.
4. Cooling Water Data Sheets for the Indian Point Station for the-Period November 1968 toNOvember 1971 Showing, Among Other Things,
orine Demand.
5. Information on Peak Temperatures Within the Condensers for Unit No. 1 and Unit No. 2.
6. Status Report on the Installation of Gates on the Outfall Structure.
7. Data on Consolidated Edison Company of New York's Planned Capacity, Load and Reserve for the Summers of 1971 and 1972 and New York Power Pool's Capability, Peak Loads and Margins for the Summers of 1971 and 1972 and Winter of 1972-1973.
PiiD09066D9 720216 PDR ADOCK 05000247 P PDR I
:- /.. A
OATE OF DOCUMENT:
2.16-72IDA
MEMO:
jORIG.: CC:
.I slgfted
ACTION NECESSARY E] NO ACTION NECESSARY [
EPOPT:
'.jTHER:
CONCURRENCE COMMENT
NO.:
aOrnR
E I DATE ANSWERED:
SIBY:
POST OFFICE FILE CODE:
REG. NO: '" " _
Ltv trans tle f#ollo1ing: •REFERRED TO DATE RECEIVED,13Y".
Muller 2-28J72 1/'3eyA for AIN.
DATE
ENCLOSURES: JJb eg 10Nes -0-feg Fies Documents which have been requested AC PM by 0M at Oak I dge Nat nal Laboratories consisting of 8
-- documents as stated.
I c~e Of ene, ra d REARKS:~sc ~a)_________
meat fez' M. J* Qetfaz i cy LoPcal. FP)RJ 1montp, W. Y.) ACKNQWLEAB
U.S. ATMIC ENRGYCOMMSSION ACNRLFR OMAC36" i. U.S. ATOMIC ENEPE,4COMMISSION
* U.S. GOVERNMEN-T PRINTING OFF ICE:'-1971-424-062 "
1
MAIL CONTROL FORM FORM AEC'326S 48-60) ':
Dr. Lester R. Rogers -2- February 16, 1972
8. Summary of Dissolved Oxygen Measurements at Indian Point Unit No. 1 Intake and Discharge.
Very truly yours,
Harry/G. Woodbury -f Executive Vice President
Enc.
cc: Dr. William Yee (with enc.)
A -
,~
0/
1. The method for analyzing chlorine in the discharge canal is a variation
of ASIH method, D 1427-68, "Nonreferee Method A- Starch-Iodine Titration
Method". A -py of the method used by the station "Determination of Residual
orine in Chlorinated Condenser Water" is attahed. This is the same
method as is used in analyzing for chlorine in the discharge canal.
Code No. B-7-60 10-13
-DETERMINATION OF RESIDUAL CHLORITE IN CHLORINATED COTIDENSER WATER
Starch-iodide Method
Scope and Summary
This. method is based on the liberation of free iodine from potassium iodide by waters containing chlorine. The liberated iodine is titrated with a standard solution of sodium thlosulfate using a starch solution as indicator.
This method is suitable for determination of residual chlorine in condenser water and certain industrial process waters. It is not suitable for highly polluted waters.
Apparatus
Sampling bottle: 125-ml capacity, calibrated at lO-ml and 110-ml mark Casserole: Approximately 300-ml capacity Buret: 50-ml Capacity Water sampler: Varies slightly with different stations but basically
similar to attached sketch (Figure 1)
Reagents Chemical laboratory No.
Potassium iodide, 7.5 per cent solution 108-B Platner's starch solution -237-C Sodium thiosulfate, O.lN 61 -A Sodium thiosulfate, 0.0028N..
Note: This reagent must be prepared fresh daily by measuring exactly 28 ml of 0.1N sodium thiosulfate into a 1,000-ml,
. volumetric flask and filling to the mark with distilled water. The solution should then be mixed thoroughly.
Procedure
1. Connect the sample bottle to the water sample connection located at the.tail pipe of the condenser.
2. Open inlet and outlet valves and allow water to circulate until sampling lines are purged.
3. Shut off valves and discard water in test bottle.
.... .: Add10ml of potassium iodide solution to the sample, bottle and reconnect the sample bottle to the water sampler, open valves and admit water to the 110-ml mark. Close valves.
5. Mix sample. transfer to a 300-ml casserole and add 1 or 2 ml of starch solution.
* . Titza-z'i" o.... zc: u ....ulat until ... blue color ust " disappears:.,
- 7.' , Recordthe ml of 0.0028N sodium thioshlfate used.
A
I t
,.Code. No. B-7-60
Calculation
Residual chlorine, ppm ml of 0.002811 sodium thiosulfate.
CONDENSER TAILPIPE
,FGURE I
010-14
, Z.; The chlorination system is designed to be automatic but will be operated
manually. A 24 hour timer is provided that can autcvtically start a
preselected chlorination puMp and open an automatic valve that will supply
sodium hypochlorite to three of the six circulating water purp bays. After
one half hour the automatic valve would close and the second automatic valve
would open allowin the ran three bays to be chlorinated. After
chlorination of the circulating water bays, the service water bay would be
.,..,chlorimated for ne half. hour-,by- the,,automatic valve -to -the circulating
water bays closing and the valve for the service bay opening. Upon
completion, the pup would shut off, and all autoatic valves would close.
The cycle would again begin in 24 hours or less.
However, since it is planned to chlorinate less frequently then every 24
hours, the automatic timer will not be used. It will then be necessary
for the operator to manually initiate the cycle whenever it is desired to
chlorinate. The cycle will then proceed as described in the preceding
paragraph.
3. Since the flows at Indian Point 2 will be faster than at
Indian Point 1, will the chlorine residuals be greater?
The rate of flow of the condenser cooling water at
Indian Point 2 will be faster than the rate of flow of
condenser cooling water at Indian Point 1. The data on
chlorine concentrations in the outfall from Indian Point 1
indicates a residual at the point of discharge into the
river of less than 0.1 ppm. The data is inadequate for
the purpose of calculating chlorine residuals at the point
of discharge into the river from Indian Point 2 because of
the complexity of the time/concentration relationship. Con
Edison will obtain the necessary data in the next few weeks
in order to respond to this question. Although we expect
that the calculation will indicate a somewhat greater
chlorine residual if Unit 2 is operating alone than is the
case if Unit 1 is operating alone, we do not expect that
the difference will be substantial and in any case will be
substantially less than 0.5 ppm.
4 Attached are the Cooling Water Data Sheets for Indian Point Station for
the period Nmoveitr 1968 to Novenber 1971. The Hudson River chlorine A
de--nd, in pp, is tabulated under the headinq "Demand".
.,'.' . Nov.
' ~C. ("' '~"'':A'' COLINGWATER'DATA
" " : " 'I " ! :'. . "
___•______._.______.____.. ..__,_.____ 1
2
7
1. S13
1ii15
I r7
18
20 21
22
23
24
JN
NaOC I. js e I in Cl ()r i n:i t i iln
UN IT I/1 NiT #I P Feed Rate ' . Feed Rate
Gals." gpm Gals. .pm
:7=-.
75 1.2'
- I I iI
75
100
100.
125
75
50
50
.50
50
1.1
1 .5
1.5
1 9'
1.2
0.75
0. 75
0.75
1.0
I L..1 T
River
Temp. F
65
Demand
W) SChLI tu rn a
Temp. F .
654
I ' I _____ .L........A
92 65 - 64
9. 2
9.1
9.1
15.6
I 5
15.4
15 A.
63
62
60
58
58
59
59
57 56
1)4
54
53
52
50 50
49
50
*
Residuti I
0.8 •65 <O.I
3
- 70 - I - < -
0. 8
0.8
0.8
0.8
0.8
0.8
74
62
65
64
65
65g
< 0.1
<0'1
65-
64 63
62
60
,61
56
56
54 53
60
61
<O.i1 <0. 1
<.1
<O0
o26 50 .75 - - 15.3 50 0.8 (4 0.1
2 " 50 - 61 -" 1127 "5
28 " - -..... - . -50
50 .75 , -. Y5.3 49 0.8 67 0.1
30 - - 567 30_
* Chlor iiL (ppm)
2<.-, -.
• .'. • ' " ',""t " . . , .7,1.777-.
t
. 1-0 8
7nT
-- V
~O~iAL %.1 U lZ.A
COOL INGI WATER DATA
NnOC I. used in Cii rin:;inn er ,
)at t UNIT / UNIT #i P cone. *..
Feed Rate Feed . Rate . Temp. Demand. Temp. Residu .
Gals. gpm Gals. gpm F F
1. _ ' - - 65 - 65 65. - 65 - -5
2 5 o - 9.2 65 0.8 65 -0.1
:-- 64 - 70
- 9.2 63 0,8 75 < 0.1 > 75 i 6., "- . 62 - 74
7_- .- 60 - .62 '
8 00 1.5 - -. 9.1 58 0.8 65 < 0.1 "--. 58 - 64
T'10 100. 1.5 - - 9.1 59 0.8 65 . .
.. .. . . ,- . - 5- 6 5
o _1 125
13. -.. .". . 58 - 65
•h- _ . . . -57 - 64 15. . 1.2 -15.6 56 0.8 63 <0.1 .... _ 5 1.2
16 - 6.2
.50 .0.75 _ - • - 62
--- - ". -460
i 075 - - 5.5 54 0.8. 61 <-.o
20 - -..- '53 -56
21 - - 52 - 56 .
22 50: 0.75 . • . 15.4 50 0.8 54 23 -. .. - 50 - 53
50 1.; 0 _ - • 15.4 49 0.8. 60 < 0.1
- - ~50 - 6 2
W26 50 0.75 - - 15.31 5)0 08 6
'. - 50 - 61 28 ... 49 -50
28. . r' • . 1 . .08 1 - O l
S50 .0.75 - - 0.8 6 0 3- -. 50 - 671
*.C ori1w (ppin) . .,- .. ':,,
,~ C h o . . .. ... ., . . . . . . .,,, ...... . . . -- -.. ", .! ,m- 'r £'~ L1l'::7:
:,-.t -?
Nov.
' i . . 4
£' COOLINC WATER DATA
NaOCL used in C .1(1 ri n::tIi6n Riv
IDatt UN ITI 1 UNIT / 2 Cone.
Feed 'Rate Feed Rate % Temp.
Gals. .as. gpm F .
2 " . _5
5 1 2 2. - .G .-- 65
" -- - - 64 75.1.1 - 9.2 63 ':!';'75i i
- - - - 62
:i7:¢i 7 - .... 60 9.1 58
10 100 1.5 - . . 59
125 - -9-8
• _ . . '" . : 58 13 '~ i ._ ._ 57
15 .75 1.2 - - 15.6 56
6 - .
', b50 0.75 8- . . . . .."... -.. 1)4
-50 o.75 - -. 5 54
20 21 -
- 52
.22 50 o.75 - 5 0.4 50 - 50
23
24 50 15.4 49
- ... . .. .... ... 50
26 50 0.75 1 _. 5.' 50
- 50
28
50 " .75 "- 49
30 - ,i.,.
* Chlori.rne (ppin)
3'::; : ~ ~ ~~~~~~~~- !7. . .... ..... •......
r
Demand
0.8
0.8
0.8
0-8
Nov. 19
1)i Sel:tr e rlnal, ffll-' !
* "J) ly Ave-
Temp. Residuut I'low Rat
F Mgpm
65 3 30.5
65 - 330 . .
L65 . 0.1' 330.5
70 - .330.
75 .1?,.
74 1 330. .7
'62 - 330.5
65 < 0.1 750.5
64 - 750-5
65 < 0.1, 605.5
65 6
_ ,6ar
" - 1 65 . . ..
0.8
0.8
0.8
64 63
62 62
60 61
56
56
54 53
60
61
<0.1
< 0.1
0. 1
•<0 .1
:745...
.745. -5
745. 5
745.
745 5
745.5
745.5
745. "
7 745.5.. 325.
175.5
175.5
0.8 ' 1 0.1 - 61 ,- '.175-.
• 50 1-7D.5
0.8 67 . 01 175.5
67 " 175.5
.." - .A. ".,-"
October , 107L
COOT,TNG WATI 'R DATA
NaOCl used in Chlorination River Discha al Effluent
:",:'.Date U N IT /i . -. 2 . Conc. Dai ly Av
...-. .. " Feed Rate " Feed Rate Temp. Demand P esidua Flow R:
Gals. .Pm Gals gpm FF
1
I ....
7- 1 7 - 320. 5
-- - .7. 0- 7 6 2 0.
100 i.;- 10' C 0 . 0 - '-6- -- 0. . ~ "P~
6 00. 1.h 70 0.7 78 0 . 5
7 -670.5
8 100 1. 5 . .10. 68 0.7 78 0.1 170.5
- 6B 78 -1.
10 .- 68
O078 .7 170.5
S 100 150.? 68 0.7 77 0.1 170.5
1 2 " i.6 7 _ 7 1 0.5
100 1.5 -- 10.1 66 0.7 76 0170-5
14- 66.- 767 6182.0 :. 10
....... ... 20.7
0.5 1-0 .i 6 o .7 68_.
1:' . .. 0 .7 7 67 i 170 .5
- 66 '.,66 --- 320.5
3 65 600 6 68 388.
2 - - -- 65 .. .. -18,9 o
<'p -]..-"65-- .7.
.8 0 0'.70 .2 5
27 . ... 6.. . .. -- 70
..20 1 7 65 - 320.5
21 - 66 320.5
22 - -6- 320.5
... 65 " 20 .9
- - 65 320.
... ........ -320
, 31~i 626 320 .5
..... :i -- "W 1
Li~' . Consolidated Edison Co. of N.Y
." , ;' . . . .
! ; ... .. . .
NaOCl: used in Chlorination
:)ate UNIT # 1 UNIT
Feed Rate
Gals. gpm' Gals.
250 3. ,2 -._ _ __- _
250 3.9 .
.
Feed Rate % Temp. D
gpm -F
... .5
£ - I - I i~) I - I
temp., Residual Flowat F . Mgpm
86 0.1. 205.0
81 - _ 30.57 55 ,u. I . '-,. .
I. ~ I I I I
10.5- ... 86 -. 213.0
-4 . - .~ . - ~
* __
_jt4.f__ __11
7
- - -4 - I t t T87
'1 ~
10.. 100
I :
13
14
15 .175
, i .... .
7 25-.10.1 (f
6.o 0
83
- 4-----4 t-h~i . 1Z71 .. I- 4 1 T1 -- 1
±-.0ulL2.5_ , ,
76 76 .-77
- 1 1 1-i-z-- r (0 '-'C.
______________ 9. r--2.7: 14. b)
760.8
76 77.
82
<0.1
1 581 6- --
213.0 .213.0
325.5
325.5
i86L. 5 186 5
186.5
325.5
325.5
325.5 -_
. . ' 74 80 - 325.5
-18 """-" - ''-"": " JIL"" .. " .. z 2.
18
20 175 2.7, - 13.0 71 • . 80 <0.1 325.5
-1L - ...... - - 74 . 80 - 325.5
21 • <0-...
22 1 2.7 L.. 12.8 72 . :.78 <0.1 325.5
23. .. ' - 72 - 78 . 325.5 23 - -25
24 175 2.7 . - 12.6 71 0.7 77 <0.1 325.5
25 ..__ . , - 71 - 77 - 325.5
.26 -7I
-2- -- -5
27 325 2.7 , - 12.3 .70 0.7 76 .<0.1 325.5 - -
2 8 3 0 0 2_ _ _ _ _ L3_2 .2_7 0.7_6_ _3
5_ _.
1.9.._. 12.1 7O 76< 325.5 -L .. .--
71 - 77 - 325.5 L' i B -- . .. -- - •
39(
.3 1..
<F
.77
_
- , . _ | • ,
Inc.. '.. :Indian Point -Station
September " 1971
COOLING WATER DATA'
River Dischar e Canal Effluent
2 - Conc. Daily Averi 2-~ ~~ ~~~mn Temp...-': h/:ii'L " I/e>"" a r'"U
emnd.
9
213.0U<U. ±
r w i
w
U., 0". •
_8. . , 82
.77-9_=;
7n. C. N Indian Point Station • '"' Cnsol1idated.Edisofl Co.
N..
c . . 1 71 ::I......
COOLING WATER DATA.
':; -- e-- Dischre Canl Ef fluien
NaOC1 used in Chlorination ies Daily Avo
#T 1 IrNIT -2 Conc. .a... -. .. ed Patte Feed i
•e TDn . Thmand rpom.) RcsidUa1 Flow R:2t ,
G,. .8. Feed p t I U M pm ":'.1 n .. y I- IM - -
8182.5 :-::;:.--------- t 182 5
2. --'-'--
77 77- 1
73 - . 778 82.5
78--78 -182.5
-8.
6 .-
0 - 78 - 182.5 - -78 177 .5
, 77 -77 -177.5
.7:7 -77 25.5
10. 0 .7
..
78. 112.0
........ . 7- " 7313.5
S- 77 77 92.25
13 - - - . 77 "77 -177.5
13'"77 77 177.5
4 - 177 5 15 .. 77 - 77
2 -7 7 177.5
15% 3 - 7 R
- ,7 ,,- 32-775.5 - ----
5---5
20 150:2.5i-1- 11.3 78 0.7, 86 <0. 1 .17325
']52(1) 278 325.5 278. 5 - 325.5
23/017-- 1. 8 7 15 <01 325.5
- ' -- -- 5-- " 325.5
2i: 10 l') -I !
7G 0.7 :83 <0.i 325.5
.2 02 76 81 - 325.5 76.8 - 173.
.. 58 3255
--78-- --- -3---
..j.-7 0.
.2i. 78-. :. 0 . I 9
1 I
1! 7i: -- ---- 32 .
, . 2 3" , 1 .0 0 ' " " " " " " :. . . ' "
Qonsolidated Edison Co. of N.Y., Inc. Lnc an
K.:.-. "0"July , 19 71
COOLNG WAT.ER DATA
"::1i aal EFffluentL i . ; River D s h r
NaOCl-used in Chlorination vesh-CnEf t
ii.%:¢ Diand ' nDa i:ly Av(,,
,Date' UNIT # 1 UNIT //2 Conc..
" -eed ate Feed Rate % Temp. Demand Temp.l Rei.diul ,'w I):,t Feed ppm F- F M i',n
• --. :< n. s .I, iln Cal. .1S . "
2100, 1.8 " _ 3 3 7. 0.9- 84 0.1 33 . -,73 . 4- 7 - 330.5
'K -"- - 72 - 73330.5. 12'1.9~ -~-12. 7 1.0 84 0 330.5 i'" 2100 .8 3,_ " " -
6 " " 73 74 - 330.5
873 7330.5
15 .3-12.4 74 1.0 01 335.5
10'' = - - "- 74 - 798 0 I 33 5.5
1 2 5............. 1173 8 -3
1[I .' : I 10 1. 1 . 74' 1.0 80 0.1 335.5
13"----74 - 75 . 330.5
1. 74 " 75 0 335.5 . 15-- 74 - 75 - 3355
-* :, . -6
7- 8 .
o " -76 1 77 0 8335.5
1 o .- - . . .. 7 1 7 .
__ - 76 "77 - 1765
200 33 .
21 .- -- - 76... -6 - 176. 5
22 --- 6" .76 -, 3.55"
23 _ 77 77 3074.5
2,[!:- 4 . --.- 7777 - . ] 30.5
. 2 .. .. _ 77 - 77 - 30.5 26- --- "----7 - 78 - 3 .5
2_ __ __ __ __ - 77 - . 7 7 . . 32.0
28!4 - .7 -177.0.32.
-;in' 2'';- - .78. - 78 - 32"17 .0
0. -• - - - 78 78 - 35.5
74. 75
14
1 .. - i - -- 7 - - 32.
I76
... . . . . . . . 7 7.. . . ... . ...
[ I i::!; ' ".. . ... . . . . . ... . . . .. . . . . . . .. . . .. . . . '..:. - ".U ." ."'. "..• ... •". • ... ... .. ....... -7
"".'!, ,.. ;=:.. .... :...:... :,:..¢i.. ..... ...,..i.:.:: ..,, .,_ ,_ .?.:{ -: -t.'<.t. '..!-,:-: "'..,' ' : :;7.6: :. -
0" 'June 19
COOLING WATER DATA
NaOC1 used in ChIorination River Dischar e. a EffIuer a AIT # 1 Conc. Daily Al->
Da 'TL -- NI -. UNIT 2 -. .. C n.... .," R s ua F ow l:t
Feed Rate Feed Rate • Temp. Demand Temp. Resid31 Gals. 1m1i Pm F F. M lm
_s.. | "*) m ' ,1.0 ) <0.1m0.'
6 . - - . o 6 60.o 170.5 :3 ._. - - , -60 -, 60 . -•_0 .
4 - • _ 61 . 61 -. 30.5 - - - - 61 - 61 - 10.5
,6 . .. ." - 62 -62 . 330.5
7 100 1.55 - 1 . 4.7 63 "!0 71 <0.1 347.5
8- - • - " - '63 - 71 - 424.O
9 75 1.15 14.6 63 1.0 ' 73 <0. -377.25
10 6 : - 33-i,-0
100 1.55 - 1!15 64 1.0 75 '<0.1 . 330.5
" . . _ - - 65 " 7' - 330
13"65 76, 330.5
10 1.55 _ - .66 1.0 2 <0.1 05
i~~ i{ 15 - . . . - - ' '" " 71 " ' 14 .61015 -," 14.3 6, .0 72 <0.100 330.5
1 5 " , i1 -17 - " ' - -1 100 1.55 l- 14.1 • 1.0 78 <0. 1 330.5
- - - - 6. -. 77•8 330.5
20 - . -6 - ' _ - - .5
2 1 0 14o '7o o1.0 80- <0.1 "0
22 -J " "424.0
23 _ 0 0- ) -3 70 o.9. 80 <0.1 '-. 5
24 - . - 71 - 81 - 330.5
100 1.55 ' - 13.7 7. 0.9 81 ' O.1 330.5
26.7 1 ' . 7 - 82 - 330.5
7 7-- 1
28 100 3.6 .72 0.8 82 <0.1 330.5
S-' .7. - 82 - 35.7
30 100 2.? - -73 o 9 83 <0.1 335.5
31. ..
I .L " -~ ,".: ..... , ,
Consolidated Edison.:Co. 01 N ... . - 0
. Y. , Inc.,
May
COOLING WATER DATA,
f T"
, 19 71 -I
NaOC1 used in Chlorinaton 'River Discharge Canal Effluent Conc.' Da Ily A- e ra;
-tte UNIT # 1 UNIT # 2 Cone. .. D ly...
Feed Rate . FeedRate % Temp. :Demand Temp. Residua Flow Ravi
. Gals. gpm Gals. gpm F F M gpm
.___ - 46 5 s
z 46 . 54 1 330.5
50:1. 0 -6 <01. -
50 1.0 - "1 h6 0.8 57 <o. 1 406.5
- -- - 48 - 5s8 -402.5
• _ _ _x T
50 ... 11.0 47 0.8 57 <0.1 106.5
- . . . - - 5 544.o
S- 9 - 448.5
50 0.9 _ "11.0 4- 0.8 57 <0.1 482.0
S 50 59i 458.5
20 50 0.9 - - 11. 0.8 57 <.1 566.0
i3 - - - . - 5 _ L - 58.9
:50 0.9 '" 10.9 52- -0.8 50 <0.1 570.5
1 L5 -5 -58
L63 53 - 59 - 570.5
15 -1" 10.9 4 0.8 60 <0.1 570.5
L4.~56 500957 ..
L9 - _ .2- 1 - - 61'....I 70.
- - - - 56 , - 62 - 570.5
75. 1.2 - - 10.8 56 " 0.8 62 <0.1 " 570.5
2 7 ; - - o 57 - 61 . 570.5 3"-62 . ...6 • 570.5
"-4i::'O 1 . ...- , "- 0.7 56 .. -j< . . ~ .
-3 -5-7
I 501.1 0. 5 0.8S 63 <0.1 257.5 75 1.2 ."57
6 1 330.5
0-..9" " 59 j.- 59 330.5
". -. . 7- 330.5
: ,,;-"---
. J1"(118/' rai n" o~a~i~On
0C()MTN rWATI13AI
14Cod Hate Feed, a te Deem 1mand Tom) ei(~ IO
Cal s. . Pm ~ I~um F FMr.
2 75 1. 25 -- 1 .) 1 <- 20.t 7
4 - -12 -62 - 207.2r
-575 1.25 - 35 )13 1.0 <3 0. 1 205.7
6 ----- 11- 1-191. or
1750. 0.8r3 - .1 10..j 1?030
), --- o OT 18) t
-- 13. 1 o.0 !,L2 < 0.1 1 02
~10 ----- i . - 177, 5C
11------ 3 -175.5C
12 50 0.85 h ?~)i 0.9 6h1 < 0.1 170.5,
13 - - -- )? - l.68. n(
1~; 0 (.8. ~ - -I?. o. 030.2 L).7L
is----- )t2 -. ()2),7
iv .i 6 50 0 .85 .-12.1 6~ 0. 3 01 j j
-~1) 6 -- 0~ 1Q3. 5(
- -- )15 - ,7 182.0
20. ) -- 5 5 L9 -235 0(
21 c0 0.8 )1 .2( ~0. B9 <..95.0'C,
2285 12 ---It
23 ~ 08 -.- 11. )17 06.7 60 <0.1 325-5C
214 A - C 25.5C
- - - ~ - 1 - 25.9-,
26 0 0.85.- 1( )17 7 8 <0.1 325.5C
27 -- - - 17 -or3 325-5(
28. 50 0.85 -- 11. 3 6 0.8 57 <0.1 325. 5C
29 ----- 46 -5- 25.5
300 c. 85 - 116 08 57' <0.1 325. -C 3 ___________ ______________ ____
y~ .. rfiq ~ ~ '~COO (~0JI'J WATER DATA
Nai lu sed in' Clrnto'River Disc. Caa F~
ate #U -1# . UNIT # 2 Conc. Dil
- ~ Feed Rate- FeedRate % Temp. Demand Temp. iwsidual F1 ow
al.Gals .al.m F M s"
- - - - 32 -53 -170.
2 100 1.2 o 14 .8 54~ <0.1 182.
~ d - -- -207
14 75 1.1 - 1)4. 33 0.M2 KO120
- - -- 314 -514 -243.
8 50 1 .0 .14.ih 33 0.9 55 <0.1 1 209.
33 56 --- 217.
1050 0.9 - 14., 33 0. 0 <. 44o.
- -- 3 -51 - 482,_
12 50 0).9. 0.914: &~'7
13 - -- 33 -55 -231
- r)5 -236.
14 ----- 3), _ __ _ _
75 12--14. 30. 56 <o.1 2141.
- - -- - 14 - ~ 4 -207.
1750 0.9 -- 14.- 3)4 .0.9 51'- <D.1 420
19 50 0. 0.9T~ 3 52, <0.1 L.1-9
20~1 0 35 - - p
220 7 .5 1. 354 0. 51 0142
- 0~9 - - 14. 3 0.9 50 <0.1 7
......- 26 75 1-.15 -1.0 38).0 6 < .
- - - - - 35 -50 . 7
~ 28 -- - - 36 59I
27f~.~ 1 7 12 3. 35 58 WE 1 0 I
2&
ITr,.c1 I -d ija Clilorl-nn.Linl________ -___ ~
I TTT I Conc. It e ~~T Temp. n em
V r at, Fee d 1C. I. T');Kfd 1 n p c
Gal. r, rq:~ gpvv r
Ad - - - 33.
333 447.- -3
-6. 3 -o. 33 - -.
7 100 1.5 - I -61 3 . _ 01T1
0.8~I 32 Zo.6 .. 10 152153
0.__0.1h01
-33 - 158 _ - 7
1.6
33 5 c
7_ . 1QL3 08 ~ .
1,. 2 O
lit 4132 5
20 i5. 2
1 COOLING WATEP DATA
,AvorLla I
Of 4~1T0c1Used DI. hag
IIt - 1g pin
Of) 0. 2 10.
.. . . . .. .. .. f _ _ _
.10'
'K
... ...
0_ 1 0 1.3. 2L ....3
...... .. .. . ._ _ _ _ _ _ _ _ _ ......
7T 32
COOLING WATEB TA
* Avo rtgo. Chx irm.n -P ~ Ieoc1 lned Dischargo. Te
Fl rw -Ra to
..onth Fee c d4gr
IJ -lato L -1 -ll
4',o
1. 1. 100v2I ~ .
.... ......... '4
4'
'47
.. .... .. 44. , 2 .
- - -------3
2QO..5q
"A'
0. C,, c ul '2u0.5
onoldtdE inon Co. of' N.Y., Inc. .n l uli i1 .x1kL~ .juAkA
Vi;COOLING W ___DAT
AvorLa go
1.18y o eimu Chlorine (pm) jj80C1 Uced . Dischargo TE~n -03 Y of mm ppFlo-4 Rato
~c~c1 * Mgpm 1
FResiduoi DO-mCxkd G9B cn
-~ ~ G 10 L 10(
- - 5.0 5
h -- -5.0 5 9
----5.0 56
- - 5 -0 57
- 0 5(- L <0.1 __0.3,
9 5::0 . L (
5.04 50 52
5.0 50
5 50
5. 5
*~:. ,3c3.t~
C srdtdEcilfoo ku.
* M ~ ~~. ~.ndian PoY
COOLTUG A
Of1 Mo ~ xitrum. Chlorine (ppm)
nmth Fc^-d
Peoldu1Dmon
-e
.. ... ..
e7L~
**. Ii. ...........
_ _ _ _ _ _
.... n c l t d
IAT M-, MTA
* - .... *~ .;L.
-A .~.
,.,. *~~j,$
3
~1
V 4
I * *,
I
4
I-.
r onoolide ted :Edison Co of N.Y., Inc.
~iK *~,Unit
0't
Ilo. 2
CO0O0L N'! WATER lATA
Maximi. Chl hrine (ppm) WsOC1 Used Avehragel e
________________- -Flow. Ra to Feed gn
Rsidual Dem~and Gal1. (cone.)_______ In
2)-- 5.0 yo(
4 -- _ _ _ _ _ _ 5.069
5.0 (9
_____5 - -50 69
-__ _---50 68
5__ - 50 68
5L__ - . 67
5__ 5 0 66
- 50 65
- - - 50 (
_____ -
______- - 50 5.0 64.
<..1 121.7 5 1.99.2 ____
7 ____ ____ - 50 64
________5 _ _ _---50 64
___ - - 50 _ _
________~ _____ ____ -- 0 64
_ _ _ _ _ _ _---5.0 -2
5.0 62
_____- -0. 62
~XL1.3 0. ~5.06
4 _ __ ___ __ ___ _ __ ___ _____ __ - .0 61
Calculated .
mWin~WP~
19-:
Indian Point Station
u n s~ i~ated+ Edison CO.. 01 14.1.,-L .Lt,.
++ ' "1"' "
COOLING WATER. MTA
sximul Ch1flrie (ppm) ne -,1
)py 0 j,,,.
,onth
4
12
Ii
22
Demand
I . I
Feed "R"ote
I~~~:~~i
14sOC1 Used
Gels. (cone..
I I
I_- 4
- 1-4-I---].1 - -9- 1
Average Discharge Flow Ra t.
gpm
P-0.5
20.5
20.5
20.5
)O. 5 20.5
20.5 20.5 .... .
20.5 ++
2O. 5"
2().5
20.5 •
I.
Temp. (OF)
72
____________ I
I - I
')rl
~y1. ~
7:2
I1
I - __
..-. _'"-- • '+,. -...... 74
73
7z
I.
''5
7)4
__.__,__. ___ _ _. - 20.5 71;
Tf A ... _.
_ __.. ._ _ _ _ ___._._ _._. --- - (/, , " ( +
. .,. . • ___________
.. +.;.H .. A . ______-_•_" -"__,_., __ -
* Colculated
I -~1
:1
. .. . ... . ( "" L -,. f " , - -
+"' ]+ ... ' ..... ,t;'19 T )
In
77
77
7(
75
S74
74
(.
.3
73 -73
!
on- 5
Out
77
77
77
7i' 76.
76
75
75 75
7)
.73
rn
. cons6i dated Edison Co. of N.Y., Inc.
AA
inalan iOLIGnATE @t -,19 70
COOLING WATER DA TA ......--
IOiL
12
7-
i: n ,
Maximum Chlorine (ppm) M" i (P
Residual
-- -- -- -- --
Domand
-----
Fced
Rate-
-I
1jOC1 Used
Gels. (conc.)
-I
Avorage Discharge Flow Rath
M
20. '
Temp.. (F)
In Out
78 79
'K) 80
S.- 79 b
19.0 79 80
75,25 80
.3) 80 !9 79 J8
I _______________ A 0
.0
- - r I
1.8- 2.2 700
- t r I --
I ~' -4
I - 4 1
... ... ... ". . I .lb .9
I.
rh.
7 ,)
'70.Tq
79 70
78
79
79
7 0
80
80
-- -- 7 ' '2 5_,. ,-7 .,
I__~11 5 .'..20.
0 - .1 20 5V
I - 4 - I
19,0
-lC C .
79 • 79 8o
I. 2 . .. *L .__-,,, --L -- .1 o 79 80
-'- - - ,-I _. 19.0 78 7C
- ... I - 20.5 78 7
.....- .. . _ 20.7 (.,) 7 20.5 77
... .. ,-20 5 79 20- 7 2b :r % !::- --- -- -- - 1 o . 81
- -2 . -20.5
77
Calculated q" ": ~ ~ ~ ~ ~ ~ ~ ~ ~ ~~' 'M. tj -;C: ' . .A,, . '" :' ":. .. u'.,. .
" ,.. .................. ,-, . .- - ",:, ',' : : ;: ':, . - ; :: , . .. t:. ..... ..
'0[
::-
I..1.7
1C) 32o
319
319 319 3 19 " "
319
39 .
79
78 78>
78
S79 .79
J4. 0
IP5
oCY .*,
fnslidateid Edison Co. 01' N.., Inc.
Sy of aximum Ch l o rine (ppm)
") 7ntReeidual
2
ii '.
Demand
July 12 70 *0COOLING WATER- MYTA
Feed"
L~tJNGOCl Used
Gals. " cn . )
---- ---- ---
Ave rage Discharge Fl w Rto
14 gpu
20.5
20.5
20. 5
67.2 29. 3
* 20.5
83.9
;20 53.
145.b
i~0.8
Temp. (.F)
S In " 71
72
72 72
72
.3
SOut
0
-)
74
73
-74
74
73 74.
. i - " 168.5 3 75
- " lu" .5 74 75
• - - lE .. .74 75
S ' " .1P ') 7 3 °'
103 5,. 7I 9 77 ,
:1 - - -(5.5 7
__•2- - . 168.5 75 , .
.20 - 2K.5 75
_ _ _ _ - -9
.20.5 .20.5 75
2¢ - - - -
-- - " :- 20.5 ( 70 ________ - -20.
7
______ --- 20.5 9 . ____
_ _ _._ _•_. - , - 2 0 .5 ' . . .7
-. ... .. .. " - 20.5 : 7 9).
. • _ 20.5 .0 0"_79 -0- -
- Calculated • -
____________________ Zr-, Zr -'r'.-r ..................................................................................................................-~,.r.. ~~rJmrC.Yfl *~**fl~~
4i4~4
cc'rs2iatea Edison Co. 0
r~ay oil. Max imum Chic
V ~ <0.1
r :
Calculated
f N--L Inc.*Tune , 19 70
COOLITIG wATER DATA
)rine.(ppm) Nso~l Useed "Volume Temp.(F) Vrpsted
Foed * (1.0 Gel1s)
Dtmnafnl rati Ge l. (conc2- In Out
1.2 1l2 li0 110. 76
- -110.7 67
110 C.(-1
--- 110.51 67
- -- oo 68
15 L1 - ri 00- 6 8o
- o (8'-C
- . -. - 20068. 6
..-- uo 68(
no -.
-~~~~ Q 075
':10
-~T - - -
-'Coni-Aidated Edison Co. of N.Y., Inc. Indian ot 3tat.on
9OOLING WATE , 197
' COOLING WATER 1YATA
: i?.:L.
-- 1 62 r, P1 7
- " , - - - 112 (0 -.
., - 112 61 -. -. . .- . . . .. • 122 63 (L
_ __ . -_ - .. - -0 ... 6
S - - 12.00 .- 2
11-0 -- _ . - 12 (0 1 • ' "- . - - -1-0 " a (
-/ -: ' "- - ... ' ; . (,2" ,
-..ia - - - - -'. .
... - 135 " 62 1
* Calculated
-. -. -. ,...ajq..t. ~' -- . -?1 ~~.f~.rmr2rv, rJ.. . .
AvGrage
• ximMx Chcl.-rine (ppm) NoOC1 Used DischargeI . Temp. 'kF) C) M I aFlow Rate
Feed * Mgpm L ,. . o ... . O ,
.... L i I D rI an G 0 113 G~B. %(conc,) IIn Olit . - • .d - , ___ _____ ____
- :- - -.. . . .17) ____9 _53_
- • - 19 53 5L 4- - - -9 .
,- -- - 1 '9
. . . . - - 1-. _ __-_ _'_,'
' . , _ - 1 .•
9 ' . _ . . ... i915 55; -9 55 5.;
19 55
- - - 19 757 .
-. 1 .- - 19 •6"
- - .... " .519
- - - - 9 '57 5
- - - - 19 57 ____
- - - -19 57 5____
1 - :19 58 59
'-.j -" - 300 59 0
2n - "- . ..... 25 " 2W -7<
,. .. Yq ,I) {-s .l. ""¢
hcn lidated Edison Co. of. N.Y., Inc.
-9 I . .. .
1. !I
ii .4
I ApULtLL rx.LLI U Q %
A-pr.il1 1970
COOLING WATER ITA
Average(
.4X Cl i (paeOC1 Used Dischargo Temp. •
Dty Chlorine ,__ - Flew Rat. _ont -- Foed. * Mgp
Pe•.dus- Dm"d Gale. t(cone ) In Out
' 280 37 3 2I
- -19 .
. _ 300 L0
. - 150 . 4 i
. - -. 225 0.
..- _ - 300 O"
8 _____________________ - -300 41i'
" - •306 41 41
•250 42 42
11- -250 )13 4j
I I - 266 I0 41
1 3,L 2 7 0 L
.4--4
- -I - 200 44 '4
]o5
I', ______I_____I__I__I________ - 0300: -34
J.- 2 - 2 45 45
-- - - '120 45 15 --- -- 120 06..
20 _____I_______ - 00 47 -7
21I I- I -I 1280 45 4 5
"- .-- - : 295 9
257 )19
: i J "] I I I120 50 46lz
-- 173 50 50
180 50 50
- - - 19 ~ l 5
- 2 - -- i r - 19I
19 j - 1' 52 _- -5 2
Calculated *xThe unit was shutdown for refueling.1
.- : ..... L---
~ 0 TK2 UA.. ..... .,
uned D:X Iz~ C .nr;;
, . .. .n .d ,. ,," =,, e-- i _- 0 -"--.7
7 ~. -- 00 0.00
-. -.87.--5
~II
-"i....." 'i-tl !:. ..... '1,59" - - _
7- I5
-
_ _ _ -. --o. .. -"; :, -: i .- -.. -- -:.
-, ..
___ ,-, 1 _.
" . -- - " - - --= = =-= ' ' = " % - -I . oi - - 3 51 ... 1-" " .. " " : .. .I_ ,"" " .:
, ,u .- • " . _ = -- " " • .. . ... . ,L -, : - •
,. i ,. 1 . ._ . & . O . . !.-. ! i
: .. . . '"" • I, - 't '~. " " -' "
tn... . - ... " .- ,. -4 . . . . . . .
February
COOLING-- WATER rATA
MCalcuJlated
Average
:rT- 'of' M,4aximum Chl1i r l ne (ppm) NeOC. Used Discharge Temp. (C
-'4inth Foed F low . t Fo. M, gPM
Residual De mand Gals. (conc. ) :_.... _______ In Out
0.____ 8___ 100 10 .6 300334 2 <0.1 •.9 1.65 100 110. 225 33 43
- 275 33 43 4 0109 165 100 10.3 27 33 43 - ,__ _ _ _ ____. -: -. 300 33 143
4, _ _ <0.1 0.9 1.2 75 15.3 30 33 - 23
-- - 3 00 33 4; 0.9 1.25 300 33 43
<0.1. 1.7~5 15.03034 4
_ _ - -,- -300 3
17 KO110 12 5 1. 30 3434
" - - 300 44
<0.1 1.0 1.85 150 .15.5 .300 34
]0- - 34 2.5.3.
Vi!i : , < . .. ~ - . 5.. 5 . . ,___. ....__'__ _3oo-• 27 33, : 4>, - •<0.1 1.0 100 14.2 300 44 .
1",: _______-.__ • - ." - - .:, - . *1732 31 0. 14. NQ 33
."i " .. . 1.0 1.: 5 1 13.9 " "275 33. 4 •~~2'( 1" 43i. i i..
- 1.0 - 14- 7300 33 L3
S. 1 - 300 33
*": -. •• . - - "- - 300.. _ _ _
<0. . 1.0 .65 100 3. 275 33
<0.1 1.0 10_ 300 33 4.
, . . - 10 33 41
- - --. . .... .:- ' " -300 33 4.k
<0.1 1.0 1.65 100 13.3 •.. }300 33 4
-. :i " " <O"il • !,0 . .. 1 65- i . 10 13.2 '300 3-3 "..
i [:[ "' ' i. " -- • : . 1914 33 " ,
..... 3L . " 1OO 6' :13.o 00 -33 4
S-~ '___ _ -, - - 39 33 34
*:'! . " 1 ' ' " .' ' • ::, " - -, -. l
44 :.
, '-'A-IS'J *JLtJ.t~&LJLj
9COOLING- WATER DATA
i , .. r.1mx im Cl:rine (ppm) ' NhoC l Used Dinchargo T Y-"
eed e tiiFlow Pto ~n'u1Demernd JRIt - /;o n (e *: * j r~s
- -'. , • - , - I - - .. :i 2.: 0 A. ______ n i < I. al 1 ) (_ _ - - K _ .5o_ _ I _
S -O. T-9 T . j1T O
,0. •.] .25 12." 0 32
_ _____._____ 9_ 1 --:_ 1 - 12>. J 25 _°_o _-_____ <0.1I 0.9 1.25 7. -250 ____ j1J 2.Y ____ -
-L~- j12." 250 32
! -. <, -<o- I. " -. "I- 1 .2.51 2.:!50 _ -,._ -_ <0.1 . ( 9 ._4 ~ j j j j J250 ~J _ _ _ _
1'.--. - '... ... - . : ,s ...... _ _ _
- -_ - , 250 . t _...,.-.. * 1 i
:! -- ': .- ].i. q 50 9.
.... . f -. I J. ..-_2.i '50 1.* . 9,
<- 0 . 0
_______ 50
C _ l-< ..1 I -.,.
~Lz
IFT
,,11"!
TI.o 1.. 0
.LO.
1010.,
~50250
2'. 0.).., I___ /
"'C, I -~ -'--- ~ I
2:'5
1) L .1 ~
....................................
k
iI
::5 .0
i.;,_<_O.orsolidsted Edison Co. of' N.Y., Inc. . n tiun ±r.Jifnu, ot uori 9 .I-. er .. e
I December
COOLING WATER DATA"":" " - -: '..'- "
Ave rage
.J.7 of' Maximum Chlorine (ppm) :NaOCi Used Dischargo " Temp (OF ,'., ... - - Flow Rate
. .. ... •. F e d . " . * M g p . , - I . " P I D(ma n d .n... . .. .
-..
'. _ _,_.-_._00______
I•.2 G. '00_h _ _ ,
-. . - - -300' 44 L
<O. 0.9 . 150 10.1 300 43
:. . . . . .. . . -.. .300 43 ... ___
. ....-". .... 300 43 __
<0.1 . . 2.5 150. 0.0 300 42 52
S- - - . 300 42. _
{n. <0.1 0I . 10 10.0 .0
. -_ • .. .. - 300 42 52
0.1 0.9 1.25 75 1 5.9 300 .43 5: ''::' .. ... ' " .. . - " I .. . .300 ' .4 5 1
(0.!. I 42
-- • ... . ..- ,.. -.
*. 0. . 1" 2 '( • -v2 -00 " 0I< "J"
"-.- - -- o ' 0 <0.1 0.9 1.25 T') i5. 0 _'00 . 9
2 0- "-. " . . 0 0 "3 9 L - -,- " . . 300 ... _"
<0. E 0.9 1.25 .75 '4' .300 3. b
Y "- .- ' . - . 00 37
- - - - ~300 3 _ _
<0.1 1.0 1.25. .75 14.1 300 35 _
- 00 35 Lc;
o_ - . .... .. , 300 4
. .__ _ __ _ __ . ,__ -I-. . ____
. . ... ( .. . 0 0 ..
i
a'
4.
.1
Ca1culated
.". COOLID
N~ov. 1~
NG WATER MlTA
.4 4
I I
C' . 1l.nted
y oox Nximum Chlorine (ppm) WeOCI Used Dichrge Temp.
Sonth Flow Rat
Residual. Dommnd G (con In Out
- - - - 300____
S, - -(o300 59 ____
..... 0;i '..... - .0 :1.9 125 11.)l 300 5G .6.
-4 300 57 b!
<0.1 1.0 , 7 125 11.2 300 57- 67
SI300
S - - ! 300 55
.- _ 300 55 , 5
<0.1 0.9 2.1 10.1 300
- 300 ..4 64 -±3'i:'--- .
. 0".9 2.1 125 10.7 . oo 10 .... . 6
.0. 8 21 Oi00 20"_____ _ " - ,3o00 : 51 : ____
<0.1 0.8 10025 ~30
- - - 300 562
20- 300 501 _ 0.8 2.1 125 10.5 300 -51 59
- _ - 300 50
24 <0.1 0.8 22.) 0. 300 49 5...9
•-
300 47 5 i
<0.1 -0.8 . ____ 125 3. 300 . 5
0 . 2.1 125
I -- " R 0 0 'c
., . - • - 300 -6)
- -_ 300 -" 5
19 E,,':
l Co uildtted Cdtsor Co. of N.Y, Inc
-4, . .. . .
:MaxiUnIm Chlorine (ppm)
<U . L
<0. 1
<0. 1
<0.1
<0.1
<0.1
<O.1
o(ctober
COOLING WATER IATA
<0.1
<o.
cc <0.1
• Cal3culated
t .l>;t.tTh,
19
- ept. 19 C(
* COOLING WATER DATA
11) 0*mximumn clorine (ppm) NaOCI Used volumie Tmp Trga ted
rate 01:.(oi. _______ nt___
~~~I_ __ _j_ _ <0. 2.±00.
<0.1 0. 2- 150 11.0 008
__________300 79
__ _ _ _ <0.1 0.______11 0 007
<0 300 79 .1 ___________ _____78
<0.1 0.9 2.3 150 11.5 300. 7988
~~0.9 1.9~ 100 Q563076___
-- -300 * ~8( - - 1 300
-. . -5 l- ** 30 __ _
_____ <011. j9300 -9
- -300 L-7
0c. .0 1. 10 15.7 300. 78
- 00. __ _7_ _
_____ <0.1 .9 . 1 . .100 lL.. -00' Jj
______~ :-___ 300I
<0. 1. 2. .Clc3atd 150, -:+ 1. ~ 300.
: ( or6 i~ . €Lcd xd]i.oon Co. of N.Y., IncIndian Point. StAtt6n
CO0LING WATER rATA
Chlorine (ppm)
__________________________________________ -p I I
d r
Feed rato
NaOCI Used
r'&1n .(cnne.~
Volume Tr sted
(10 Gals)
Temp. "
T0' no - "--i
Ian -" 00I. ,- L . ... . .,' -
---- '..-'..... '~ ~ .... , ~ ~ 9:1'. .. ~..
/"y or t .t
Mgx Lrum
1(,:ILILfl L ,. -uz.L' L ..LL u'- . . \ .... ,- - • . , ,________
1 -. 1 .L. ., t- (co0e
.- .. • - None .. 300
.. <0.11.0 .6 .300 300
.4___ <0. 1 0. .. b 300 -. 7 .30 7 ... None - 007
_- _ _ <0.1 .9 4.6 300 5.4 .oo
___-___.-_,_.___._" None 77 300 77
<0.1 0.9 4. 300 85.1 W 77
N I _ .one 0 77
<0.1 0.9 .5 100 10.5 30
- j2 None WO30 778
<0. 1 0.9 1.5 10 142 300
None -00
__ __ _ __ __ _ __ __ _ _ __ _ __ __~100 138 00
- " - " Tone - 300
_____ <0.1 0.9 1.9 125 -13.5 300 78 ___, __. _____ " •__ t - -- one - 0 .
0"9- 1.9 125 13.2 300 78
o - None - 300 7,
I Non e '00
<0.1 0.9 1.9 1-5 5 12.5 300 7__8_ _
______.- ___.- _.. - jNone~ - juo , • ____
<0100 :1 2. 00 78
• .0. . ) .9 131 . •
... - -. - None .- • 0 77
___, I " <ol ,, . 0.9 1.125 11.8 300" 78 __
_______._._._ A - iNove - -. 00 7
21 1 .. 78 39
.. . .. - . -- - .N ne o
0' ._- n--.. 0 o°
T'.7.-- i • .
;f p l i (.o n c / : " . , : " " ! -"" - -"j, ' .. .. o u ' , 1 '
1.0 c. ... 9 ,3 1!(00'.' .'.
Iw;
. :,i,. : " ' 00 .. .
. Ii
-e- .. 300 T 6
! •i . F 2. ; : .! 'o . . , . 00 "_. _." _._______
-i-. .. , . . , . b To~mc , --=__ __ !0 ::. \ _ __- . _ _ --_
----- ---
.3, u2 j.. 2 2 .
<0 200" 30) r, .
<0 1 12 7- .I '-3.. 7
',T .. _ .. . . . . ". ,7 5
-:_. .__. _ " -." .. .- . ... . . - . .. .... .-. - -- . . .... . . ' - j .q--,-
I Ia
. -_ . 1.
D? .- ±iie-300 _ I a &. -- -' --V : -.. ... II l*. . . Y " -. r"; -r k • i' .I 7 -.
- _ ;; '. . . .. - -- ,,- t % - i - ' . - I "
a .... .,- . .
' ,: ' ,a~e':].2[;K
4at; B wrr f\F
iP~r '0
I~1 tff t
(:101
-~ eI
< _ __<0.1 0.9 9__9__30__65_
<' 0. . 0.. . 9 12-. 300 67 _ _ j on 300 657
15 8 .9 30 I 669. -_- - ----- ---
____ 0.1 10 1.9 1 _ _ 20 300
I___ -- None - 300U 70L
-- None 00 70.
- None 30
< 0.1 1.0 31~~ . 0
-9 None L 30 I 7
______ :300 _____ .. 0 .
_ _ _ _ _- None 30-7
< 0.1, 9 .. I r 1 - . -~ None. . 3 0
SI i~oi0.L1 i4.1i
-i I. - I - ~None -L00 1. I
2__7 __ _ _.1L 0. 1.09 125. 1450 3_ 00.... .... ______- IK J e 300_
- None__ 09 . ___ i . J a_ _ __ _A1__ L7 J
________T7___ F6777___ NonePT
Ma 19
COOLITIG WATER M'ITbI
~ Mxtrw C~crile(pm)i~1~ Used ic~g Tep. (F FciRto
Fccd *M~
* ?!f p-nrui (tl)qr'mnd Gn1A3. (conc. Tn Oi+
-- - . I~oe -00
A I
- -- None -30 0
<0. 1. 300 .1 7
3o0 N4o ne 3 00 ~6
<0. 1 j0.9 1 15 75 00
<0. 1 1.0 100jon
201 1 A_126_5
1.0 1.55 100 b.1. 005
Noe '00 '56
<- ~10, .1 A 00 * 6
* Caculaed ,:..:. -~~j~r"., *
............
:- Consolidated Edison Co.,of.N.Y., Inc.
V...,. . I. J G WATEM MlIT
April , 169
*i. ~.i.
51
~, .,~
v~. ~2
li
p
Avorage
MDYofximum, Chlorine (ppu), uaOCl -Used Discharge Temp.. y Of.;
Flow Rah
Peeidual Do dGae. (cone. In
8.Q 90 L____ 41
<0.1 1.0 1.0 25 8.9 300 41
<0.1 0.9 1005_ _
N one -0042
1J6 - - None -300 42
<01 0.9 1. 101. 00 42
--- INone -300 42
30, one_20042
1 i<0.1 0.9 1.5 100 V.2' 300 43 a. --
one - 300 44
_ _ _ - -None. L 30 _______ -01 .10 300* I 1I~ KO.1 1.0 1. 105_______
.7- None, -30 46 ,00 4 <0.1 1. 15 15.L ______
N one - 00 47
<0.1 1.0 -1..5 100 15.4 300 . 47
-~on .oo : ~ l ~ - ~48
20N- one, .3 48
-. 0 Noe 00_ 49,
PI<0.1 0.i.4 c)
- - None -300 49
<0.1 0.9 1.4 _50 34.8 30 49
-.- N one -- V 3095
<0.1 0.9 1.2 90 14.~ 300*5
- -- INone. I 00' 51
_________________None- 0
t~t
- *Calculated. ..
-IILrclo
.44
It
wi
---------------
C_ _ _ _ _ _ _ _ _ _ _ _
'35
I. - - I 0
-CulaLi;
ta ~ ~ a t-
' ons didated: Edison Co. of . Li,.'..
.- •CLNG WATER rATA
Indian Point Station
S .- :rim t v 19
_______ 1* r
Maxiimrl C'!ri ne (por)
Residug I r.:'n .i
S<0. a. 2 0 0 O <
Na0Cl Used
10()0 10.9 ] oo 1i o.
Volume Tr R ted
(10 Go.,
Temp. F)
I ____ _____
] &) ___________ I )
f io.'~ - _________ "I ______I 10. '~ -)
" " None~ I -' ' '
14-'- - 4
<0.1 0.'. ,) 10. '/ 1i. 5 -, . h
6 - - - one
0:-
I, ) ,
19.5- None C9).
" _ None 51
1 <0. 1 0..' .0 " iO 5 14.5 -. L
0 4 ..- 1-.11" . 0
None - - None 3*
15 - - • _None - 33
.. -.. None .
-- None '33 *
10 -_ __ _ __ _ __'- "_ None 33. , *'
_ _ _ - _- I -",.
- - ' None j 33 *
None _ _ -4
N one- ! --
- a-" l . - on *
; 4 None 33
21~~I' , " -j,.: . .. "
I -L
U I - . S
~2U - -~ __- -________ - I
- I
* Mai n. Circudator Shut Down -
None 33
None 34
.Noe I -- -
"w Calculated
Oay of 4onth
2-.'
& . --a I
I:w .:, . .,. . .. .. ... ..., _ . . w t...t , , I . . : ....-: -,.,. ",',
I
I-
-.. isolid1a.ted Edison Co.: of "N.Y. nc.
COO[TTNq WArIlc IY'.'A
I nd, n J' ii,[ 9 O ,T , unr v 9..<
.,of . Mximum Ci'Lorine (ppm) NeOC1 Used Volume" T .( "rith " .Treated.
(10. Gals) D's .. :. i 1 Bemnnd Gals. (conc. ) .. :1
. . 12. 19. .
- .'. - ... "- 12.3 None . ... . . .. 43 •2. None
.4. 0.1 0.4 75 12.2 19.5 413;. h.___ .
'-12.1 None -34 __. ___ " <0.1 ' .• 0.3 . "75 12.- 19.5: 'I "
- .-.. 12.0 None, 4
* <0.10.5 5 1.2,0 N)
-. - - • - 12.0 None 4 .4 4.5 <O.l 1 0.5 5 .9 io.5 30 501"
5 50
". 1 No 45
<0 .1 0.5 5 11.8 19. 4
•- .11.7 None 3 4 45
-H<0. 1 0.5 ' 75 11. .19.5 4 y____
- - 12. None , . 4t
<0.1 0.4 5 11.9 1.5! ,. 4. .
_.__-____"_._-_.. - 11. . None 4 45
....-] - .., . .... 1 1 .5 "'e ' . 4 4
____ <0.1 0.4 15 ' i~4
______ - 11.4None ~ 1__/.<0__ _ •0.1.0. " . 19.5 .o.. . 40
11. . 40 52
<0.1 . 5 1.8 . [19.5 .. ..
_ "- :" ". -- '.. '11.2 . !,one.
____<0. 0.,3 65 11. '0 .
<0.1 . 0.. 55 . 11.0 . 19.
:i ".... . . I ' . . - . n.. . . . "0 11.0 ..N n "..""____
•.. .0.1
SCalculated
Col teisdion Co. 'of T4Y jo1C. in ipoint Stat Ion
/ of MxiorjnmjnChlorine (p)rOC1 Us-ed. Volume- Temp. (F Treted . (100 Gels)
B~es idui1: -eanid Gfih3. 70(c onc) In Out
0,1 I . 2 4.1. 19. 44
I -~None 524
ox 14Q .5.5
--------- lone ) 51
___J .. - 1.8. icne.P. 5
q.<0.1 0_19__5__
- .- 13.6 None.. 147
0.1 0.3 01. 19.5 '41 50
-4 13.4 . ITne D'7 47
13- N~one. v 45
_____ <0______ 0.4 j 513.3 19.5- 5.4 I 1.2. -37
06
19 9* 74
0 l~ .3 0.935 120 -
47
0.2 0.5 .10 1~71..3
I. . .44
0.3 .4. 4
.. . .,~ 4 30 3
14J
9, 77"l
~~k.s~1daedEdison Co. r 01'. ., . s:
*I)~~'t V oL'
M~ 4rith
17
20
-A.
20a
sIns i ( poll
<0.1
.<0.1.
0.1
<0.1I
0.1
0.
0.4
0.1
I ____________
1'\ ~y "[1)1 V . , 19 tA
COO FA N(u', VA'171-4 TYA5I'A
c Ic
- LL.
11.0
lo (.1
cul )ated
'.4...-..
1965
NOne
1 15)
No I i
N ic
Io
1.1o no
No 11(
N o sI c
t It~
0
567
51
51
51 5 1
51
.51
C",
.4
('14
-14
51
51
5'
~1
I::-;
~1
51 51
'-4-.
I, .
5±
1,
I. 4~
5a When the e pumps are operating a e lowest
practicable rate, what is the peak temperature r-se
of the water passing through the hottest of the con
denser tubes.in a) Indian Point Unit No. i, b) Indian
Point Unit No. .2?
*-a)-- The peak temperature rise of water through the
,hottest of the ..condenser tubes, for lowest flow rate,
on Unit No. 1 is 29.30 F. This includes mean temperature
rise of 27.8 0F and an additional 1.50 rise in the
hottest tube.
b) The peak temperature rise of water through the
..hottest of the condenser tubes, for lowest flow rate,.
o~i uin- i. 2 is 34.V hs i c ludes a mean term-pera
-ture rise of 32.50F and an additional rise of 1.50 in
the -hottest tube..
I
I . . .
.4,l
* ' 5b When the intake pumps are -operating under normal
conditions, what is the peak temperature rise of the
water passing through •the. hottest of the condenser
tubes in a) Indian Point Unit No. 1, b) Indian Point
Unit No. 2?
a) The peak temperature rise of water through the
hottest of the condenser tubes, for maximum normal flow rate
on Unit No. l-is 13.9°F for 280,000 GPM, . This includes
a mean temperature rise of 12.40 F, and an additional
1.5 0 F rise in the hottest tube. The peak rise for
84,000 GPM is 29.3°F. This includes: 27.8° meantemp
0 erature rise and 1,5 additional rse in the hottest
b) The.peak temperature rise of water through the
hottest- of the condenser :;tubes, for maximum normal flow rate
on.Unit No. 2 is 16.4 0F for 840,000 GPM... This includes
a mean temperature rise 14.9°F and an additional 1.50
rise in, the hottest tube. The peak rise for 252,000
. - - GPMis 34.0°F. This includes a mean temperature rise
of 32.50 Fand an additional rise of 1.50 in the hottest
tube. .
9
6. What is the status of the gates on the ourfall structure?
Are. two gates open at all times? If so, which two are
they? When will gates be installed?
All field work preparatory to receipt of gates is complete.
,Fabrication of the gates is also complete. Installation will
commence after the river thaws with work to be completed
in early April, 1972.
The two most southerly gates can be either completely opened
or completely closed, they are not adjustable. Positioning
of these gates (opened or-closed) will be dependent on opera
tion of the units to maintain a discharge velocity of 10
feet per second.
t"/ ' ,. - . .<. ,
CONSOLIDATED EDISON OF N.Y.
PLANNED CAPACITY, IJAD AND RESERVE
SUi6i1R 1971 AND 1972
SUMTR (KW) 1971 1972
Existing Installed Capacity 8 909
New Capacity 624
Gowanus Gas Turbines.. 873 -.1nd ,n-iPin-t :No. -2 47
Bowline Point No. 1 (Con Ed Share) 348 Narrows Gas Turbines
-184 -325
Retirements
Total Installed Capacity 10'205
920 -Firm Purchases
Rochester Gas & Electric 270
Orange & Rockland (Bowline Point No. 1) " -" 52
Total Capacity Resources 9829 i060C
Resere-ii'M1 879
23.62 200 26,2
ss- 503Indian Point No. 2 at 50% Power e6 eY
Reserve-i.1
ithout indian Point No. 2
Reserve-MW
1 697 - 20.2
- - 370
1 327
158
Scheduled Service D es for New Units
Indian Point No. 2 (873 i".w) Bowline Point No;. (600 MW)
Narrows Gas Turbine -Barge No'
Narrows Gas. Turbine Barge No.
(174 N1W,) (174 ',1)
July.1, 1972 July J1, 1972 July 1, 1972 July 15, 1972
System Planning Department
February li4, 1972
~--.. ~
'V
~ 4Y~
- A'
)
)
u 445u
*~i ~.
- '.2
A'
Total Controlled Sources
Capacity Ptrchases*
Capacity Sales*
Total Capacity for Local Area
Coincident Area Load
ACTUAL SUMER 1971
22,000
523
423
22, 100
18,146
7/1/71
1-12N
PLAINED
1972
24,670
90
150
24,610 19,510
June-Seot.
Gross Margin - MW
Scheduled Maintenance
3,954
21.8
# 3,326
5,100
26.1
** 250
8,111 43.7
** 1,3CO
% 3.5 24.9 36.7
Without Indian Point o. 2 -873 -873
Gross Margin - Ml _4,227 7,23=
3,977Margin after Maint. - M
- /0 20.4
39.0
5,93-
+I Se Fack o 2.1. ni, .14 ~I.i'$ £ 9 d 1 Q~foc i ;ofe~Q44
NOTES: $ -}'4' ij1veJ.
Based on preliminary information available for Docket R-362 (Apri! 1972)
Information on actual peak winter 1971/72 is not yet available.
* Short term emercency and economy purchases and sales excluded.
** Estimated scheduled maintenance based on September 1971 update
R-362 (March 1971).
# Includes
Schcdued Maintenance Forced Maintenance Variation of hvdro from Median
unavailable for all other reason
of Docket
Sumer 1971
490 SQ0 (148) 2104
-3326
System Plannin- renartment FebruarYv14, 1q72
NEW YORk Pct FR POOL (.Y. STATE -RCO'- ,.7ECTED SYSTE S)
CAP., BIL:TY, PEAK LOADS A :D Mf..Z:;S
WIi,.TR 1972-%'3
1972/-3
26,715
150
26,651
18,540
Dec.
.4
5.S!l
21.7
32 .C
- I 0 .. 8.:
SUM-1ARY OF DISSOLVED OXYGEN MEASUREM.ENTS AT THE
INDIAN POINT, UNIT !# INTAKE AND DISCHARGE TAKEN -Y QUIRK, LAILER & MATUSIZY ENGINEERS, DECEMBER 1971
Intake Discharce
Avg. Avg. Avg. Avg.
Time* Temp. D.O. Temp. D.O. AD.Ot*
Hrs. "F PPM F PPM PPM
0 43.6 10.7 60.4 10.5 -0.2
2:13 45.0 10.3 61.5 10.1 -0.2
3:46 44.8 10.5 61.7 10.4 -0.1
* 5:09 44.8 10.5 61.5 10.2 -0.3
. 5:49 44.5 10.3 61.5 10.2 -0.1
7:38 44.2 10.5 60.9 10.2 -0.3
9:12 43.8 10.3 60.4 10.2 -0.1
10:05 43.7 10.4 60.5 10.2 -0.2
11:25 43.6 10.4 60.5 10.4 0.0
, 13.22 43.2 10.3 59.3 10.5 +0.2
14:10 42.9 10.5 59.5 10.4 -0.1
15:13 44.5 10.3 - -
16:19 44.2 10.4 60.9 10.3 -0.1
17:36 44.4 10.3 61.5 10.1 -0.2
18:41 45.5 10.4 61.3 10.3 -0.1
19:28 43.5 10.4 60.6 10.1 -0.3
20:33 43.8 10.3 60.7 10.1 -0.2,
21:49 43.2 10.4 60.3 10.2 -0.2
23:00 43.2 10.6 59.8 10.3 -0.3
24:08 42.4 10.5 53.4 10.7 +0.2
25:32 42.6 10.6 58.9 10.5 -0.1
26:30 42.6 10.7 59.8 10.4 -0.3 IT
* zero time is at the beginning of survey
** Difference between the intake and discharge
concentration of dissolved oxygen
Quirk, Law lor r iat usk y E,,ginc eers
