ML19224B424
| ML19224B424 | |
| Person / Time | |
|---|---|
| Site: | Crane |
| Issue date: | 11/29/1976 |
| From: | Metropolitan Edison Co |
| To: | Mullinix W NRC/IE |
| References | |
| 1800.2, TM-0180, TM-180, NUDOCS 7906150084 | |
| Download: ML19224B424 (36) | |
Text
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TMI DOCUMENTS DOCUMENT NO:_
~
Colt MADE ON OF DOCUMENT PROVIDED BY L
METROPOLITAN EDISON COMPMIY.
h$ W t
7 Wilde.R. Mullinix, NRC O
7 9 0 c i s o o r(
I 8
?
4 203 340 5
e
1800.2 Revision 3
- I
... *5.1.E, F EVAPORATOR FEED Afl0 BOTTOMS 11/10/76 a
Analysis Frsouency Limits Desirable Demarks Shows need for dumping B, ppm R
I
<17000 ppm B concentrates Gross By, uCi/ml R
I J
I....
5.1.G RAD WASE CATI 0ft DEMIfl. If1 & OUT (CE-127,128, l_29,13Q}
PH R
I i
Cond, umho/cm R
I Indi_ates need for Cl, ppm R
I
<0.02 OUT Resin replacement t
Indicates need for :-
. F, ppm R
I
<0.02 OUT Resin replacement -
c ~
~
B, ppm R
I Gross Indicates need for By, uCi/ml P
I Resin replacement Y
~
~~
N
. :... t
--e f
^
~
.s
... ~.. - -. _ _., =. - _ -.,..... _ - _
~
O e+<
[
3tI 35.0 e
+-.
eh.
1800.2 l..
Revision 4
ro g d'
COPY THREE MILE ISLAND NUCLE AR STATIOb CHFMISTRY PROCEDURE 1800.2 V ASTE R CO STATION SAMP' LING SCHEDULE (UNIT #1) 30 NO__,REN OVEe, Table of Effective Pages Pay Date Revision Page Date Revision Pg Date Re
$on 1.0 11/29/76 4
26.0 11/10/76 3
51.0 2.0 11/10/76 3
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52.0 3.0 11/10/76 3
28.0 11'10/76 3
53.0 4.0 11/10/76 3
29.0.11/10/76 3
54.0 5.0 11/10/76 3
30.0 11/10/76 3
55.0 6.0 11/10/76 3
31.0 11/10/76 3
56.0 7.0 11/10/76 3
32.0 11/10/76 3
57.0 8.0 11/10/76 3
33.0 11/10/76 3
58.0 9.0 11/10/76 3
34.0 11/10/76 3
59.0 10.0 11/10/76 3
35.0 11/10/76 3
60.0 11.0 11/10/76 3
36.0 61.0 12.0 11/10/76 3
37.0 62.0 13.0 11/10/76 3
38.0 63.0 14.0 11/10/76 3
39.0 64.0 15 0 11/10/76 3
40.0 65.0 16.0 11/10/76 3
41.0 66.0 17.0 11/10/76 3
42.0 67.0 r
18.0 11/10/76 3
43.0 68.0 19.0 11/10/76 3
44.0 69.0 20.0 11/10/76 3
45.0 70.0 21.0 11/10/76 3
46.0 71.0 22.0 11/10/76 3
47.0 72.0 23.0 11/10/76 3
48.0 75.0 24.0 11/10/76
,3 49.0 74.0 25.0 11/10/76 '
3 50.0 75 0
- ~
Unit 1 Staff Recommends Approval Unit 2 Staff Reco men s
\\pproval
' Approval S 6fA %
Date U
, Approval _.
I\\ lI Date Cohnizant Dept. Head Cognfanye[. iead i-pproval Unit 2 PORC R ommend wovai Unit 1 PORC Rei )mmefds Date Date Chairrna of 0F Cj Chairr an fPOR
[ inciuded PORC comment-of included PORC commer is o 4
date)
( te)
M~
~
i j,
Date By By y
L_ Date N
Date
// J1-7d Approval S[/ticl/Superint ent/
n2 03 31'l 2
~ ' "~^ " 'I' Unit Superinten
7
,a 1800.2 Revision 4 11/29/76 Section 2, Sampling and Analysis Schedules The following analysis requirements are a reasonable frequency of analysis for routine, steady-state operation.
The frequencies of various hf J
analyses may be changed based on plant operations.
For example, more C
, 6 frequent analyses should be made during a start-up or major load change when there is a reasonable chance that limits may be exceeded.
- Analyses, not required by Technical Specifications, may be deleted by the Chemistry Supervisor / Foreman if unit conditions or department workload are restrictive.
Such deletion shall be reported to the Supervisor of Radiation Protection and Chemistry.
The analyses required by this procedure will be ' scheduled by the'. ~
~~~
~~
Technical Specificatica Surveillance Procedure Schedule and the Chemistry
~
t l - -- __. - - Schedul i ng Program. ---.-- - - -
___ -i
_ _.~
~.- - :._. -.. -
e.
i
" ^ ' ~
=
._ u
.e.
e.
gM.
@4.
. ~
._ - ?
.-. _..j. :.
g _
g.
.g
~~ ~~
4,
~
.g. 9.,_
u.
. ~.
.u
- h. :-.._
1.0 t _
, j,;.
a.m.
9_
... _. - -.=
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_- =
... _. ~. _ -_.
. z.
m
.e e
~ '
- =.n.
3sca,2
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e.
Rwision 3 11/10/76 Legend Frequency Kg f
D - Daily g
W - Weekly 3/W - 3 analyses / week, assumed to be Mon., Wed., Fri.
5/W - Analysis to be performed each working day.
M - Monthly Y - Yearly Q - Quarterly R - As nquired C - Continuous Monitor NOTE:
The maximum allowable time interval _for any giver. _._ __.. _ _ _ _ _ _
analysis is that specified +25%.
~~
~~
1.imits I-Nc limit set by manufacturer or tech specs.
Analysis
" Made to obtain necessary information.
Following a limit indicates technical specification.
limit. The frequencies given meet or exceed requirements...
for normal operating conditions.
See tech specs for
~
(
further information.
' - ~ -
~
..m.
. - _ _ _ _. _.. = - = -
p
. DM - Daily Maximum
~~
r WA - Weekly Average MA - Monthly Average
..e..
4 j;
r.
2.0 03 J'
?-
1800.2 R:-/ision 3 11/10/76 SAMPLE LOCATIONS PRIMARY PLANT R f F
1.1 REACTOR COOLANT SYSTEMS a
Q A.
R. C. Letdown B.
R. C. Decay Heat C.
Pressurizer H O Space 2
D.
Pressurizer Steam Space 1.2 MAKE-UP AND PURIFICATION SYSTEMS A.
Purification Demin. Outlet km B.
Make-up Tank Liquid t
C.
Make-up Tank Gas D.
-Bleed Tanks l,
E.
Deborating Demins.
L :;.
F 4
m a
6 o
e
- m e
4 gei se e -
3.0 1 ;', C
.h J 't 3 r
1800.2 Revision 3 11/10/76 PRIMARY PLANT (continued) 1.3 MISCELLANEOUS PRIMARY SYSTEMS jj A.
BWST
/
B.
Core Flood Tanks C.
Na b 0 Tank 2 2 3 D.
Na OH Tank E.
Reclaimed Boric Acid Tank F.
Reclaimed Water Storage Tank G.
4% Boric Acid Mix Tank H.
Boric Acio Mix Tank I.
Spent Fuel Pool
- J.
R. D. Drain Tank
- No established analysis requirements p
4 e-
-mem 4
~
~
I, ame
.e.
gm a
e S 1
~
e
@^-
a.
g
~-
-e 4'
e.
.-.ee*m.m.
e w "
4.0
'((j j J$
1800.2
- . ' ~..
Revision 3 11/10/76 SEC0f4DARY PLAtiT 2.1 FEEDWATER TRAIN 4 j A.
Condenser Hotwell
[
B.
Condensate Pump Discharge (CE-2,3)
C.
Powdex Effluent (CE-4)
D.
Condensate Booster Pump Discharge (CE-5)
E.
Steam Generator Inlet (CE-6)
F.
Condensate Storage Tank
}.._
2.2 OTSG WATER t
I A.
Wet Leyup B.
<15% Power
~
{
2.3 STEAM TRAIN A.
Main '.iteam
___m.
B.
Moisture Separator Drains I-C.
6th Stage Heater Drains r
h_
D.
H. P. Heater Drains 5.0 203 347
.sa
< T.
1800.2
~
Revision 3
11/1C/76 3.
AUXILIARY SYSTEMS 3.1 CLOSED COOLING SYSTEMS A.
Intermediate Closed Cooling
%j B.
Nuclear Services Closed Cooling
~ 3 a
h C.
Secondary Services Closed Cooling D.
Decay Heat Cooling E.
Chilled Water Closed Cooling Systems F.
Diesel Cooling G.
Stator Cooling t
~ ~
3.2 AUXILIARY BOILER A.
Auxiliary Boiler Feedwater B.
Auxiliary Boiler Drum i
C.
Auxiliary Boiler Steam
~ - -
D.
Auxiliary Condenser ___
f.
L. -
c-3.3 MISCELLANEOUS
- A.
Fluid Block t.
- No established analysis requirements m.
m a
-D
~
.e. -
.41 e
203-348
~
i --
=
, g m
1800.2
'J '
Revision 3 11/10/76 4.
WATER TREATMEf4T 4.1 CYCLE MAKE-UP PRETR.ATMENT A.
Clarifier Effluent 4
~
7
- y
( N 4.2 CYCLE MAKE-UP DEMIN A.
Carbon Filter Effluent
- B.
Cation Demin. Effluent
- C.
Vacuum Degasifier Effluent
- D.
Anion Demin. Effluent
- E.
Mixed Bed Demin. Effluent F.
Make-up Demin. Effluent
~ ~
G.
Demineralized Water Storage Tank
- No established analysis require.nents i
4.3 RAW WATER SYSTEMS c
A.
River Water
~
B.
-Cooling Water Chlorinatur g.
- -. --. ~ q C.
Circulating Water Chlcrinator
,E D.
Makeup Demin. Neutralizing Tank an.
E.
River Water Discharge
~
x f.
Main Condenser Circulating Water (Excluding Water Treatment)
~
, Sewage Treatment Plant..._
--; - =.
G.
p, _. _
4.4 POTABLE WATER A.
Domestic Water
- B.
Softened Water a r
- No established analysis requirements
)
_7 20)
J m
7.0 T
e 3
=
1800.2
~~
Revision 3 11/10/76 5.
WASTE SYSTEMS 5.1 LIQUID WASTE SYSTEM A.
Miscellaneous Waste Storage Tank j
B.
Laundry Waste Storage Tank n
- C.
Concentrateu Waste Storage Jank E
D.
Evaporator Condensate Demineralizer Effluent E.
Evaporator Bottoms F.
Waste Evaporator Feed G.
Rad Waste Demineralizers
- I.
Neutralizing Feed Tank
- I.
Neutralizing Mix Tank
- J.
Neutralizing Storage Tank I
- No established analysis requirements
~
. :~
~
5.2 GASE0US WASTE SYSTEMS e
e w
+.*A.
9e
- A.
Waste Gas Decay Tanks
~
W
- No established analysis requirements t
- 1..
~
jU-a4 t,.
A -
~
8.0
.m 203 350 e
9
~ ~ '
Revision 3 1800.2 (CF-1041 11/10/76 1.1.A R C Letdown Tav. > 2000 Analysis Frequency Limits Desirable Rema rk_s Hot Calculated Can show Need for pH 5/W 4.8 - 8.F
> Neutral other analyses Can show need for"f Cond, umho/cm 5/W I
other analyses
~ (
Cl, ppm 5/W*
0.100, 0.150*
<0.02
-F, ppm 5/W*
C.100*
<0.02 0.1-1.0 (Hot Shut Must not be adde'd during N H, ppm R1 24 down if H2 n t in spec.
power operation Crud, ppb W
<100 ppb Also af ter deliberate B, ppm 5/W, 2/W*
0-2285 change in Conc Li, ppm 5/W
- 0. 5 - 2. ')
~~ = --" r ~ '~
[
Pb, ppb W
< l.0 Not Detectable
' ' ~ _ -
Should.
allowed to drop H, cc/t H 0 3/W 15-4C 30-40 to sl6 prior to sched. shu 2
p 00wn.
Radio Fuel pin leakage
_ Icd _ine,_uCi/ml '
W*2.
I
~~
~~ ~
monitorina
~
. ~~
Gamma
~
Used in complete Radiochemi Scan, uti/ml W *, M* '
I cal _ Analysis '
Total Activity Y
2/Y*
<130/E uCi/ml
~,
Necessary for -
E calculation Gross
~ ~o
~ ~ U -" ~
k By, uCi/ml 5d!*
I-
~~ ~
~ ~ ~ ~ ~ ~ " ~
~
15 min."decassad
~ ~ ~ "
L.
Used in comp.ete Radio-Tritium, uCi/ml W, M*
I chemical Analysis Should not be_ _ _j__ Z G oss a, uCi/ml 6/Y I
detectable Dissolved
[
! [
f
' j ~ ~~...-~
Oxygen, ppb 5/W ~
100* ~
<5
~
~~
Total Gas v
~ " ~ ~ ' ' ' ' "
. ' ~.
cc/l W
<100
~
" ~#
1* Daily if H2 not in spec during hot shutdown 7 r-I ~ ~ ' ' '
dQ)
J J.t 2 Performed when power level changes greater 9.0 than 15%/Hr.
'~
..m._.
Revision 3 1.1.A (cont'd.)
RC LETDOWN - Tav. >2000 (CE-104 ) 11/10/76 Analysis Frecuency Limits Desirable Remarks Used in Radiochem Sr89 - Sr90, uCi/ml M*
I Analysis
~ f P
S s
l.1.8 DH COOLER OUTLET - COLD SHUTDOWN (CE-119)
Can show need for other pH 5/W 4.8 - 8.5 analyses Can show need for other Cond, umho/cm 5/W I
analyses - -
Tech Spec. applies when C1,, ppm 5/W 0.100, 0.150*
< 0.02 '
TAVG >2000F.
Tech Spec. applies when I
F, ppm 5/W 0.100*
< 0.02 TAVG >2000F
~
f H H, ppm 5/W 0.1 - 1.0 5[.
_. T_.
11 _
p4 Also after deliberate B, ppm 2/W*
0-2285 change in conc
,. : Pb, ppb W
(1.0 Not detectable Gama Can show migration of _;
Scan, uCi/ml W, M*
I corrosion & Act. Prod.
Is lsed in Radiochem Analysis s, _,. _
2/Y*
<130/T pCi/ml E cticulation Total Activity tiecessary for dc.-
p k
h; Gross By,
~
J.:T. -
~~~
. uti/ml 5/W I
15 min degassed Tech Spec. applies Tritium, uCi/ml W, M*
I when TAVG >200 F i
~~~~
- Gross a, uCi/ml I
6/Y I
should not be dettctable '-
Sr89,Sr90, uCi/ml 5
I
.r i
-m 10.0 b
h c
sevision 3 11/10/76 (CE-105) 1800.2
.l.l.C PRESS H-_0 SPACE Analysis Frequency Limits l Casirable Remarks pH R
4.8 - 8.5
~
g Cond, umho/cm R
I
$I Should be = to R Cl, ppm R
0.100, 0.120*
letdown Should be = to RC F, ppm R
0.100*
letdown Check for conc of B in B, ppm R
0-2285 Press Dissolved Oxygen, ppb R
I Check for 0,3 buildup l:
=..
1.1.D PRESS STEAM SPACE - POWER OPERATI0t (CE-106)
~
l Gama Can show need for.__-..
Scan, uti/ml.
R I
deqassing press
'.d
~
Gaseous Can give warning of H,, & 0,,, %
R I
"hard bubble" g
LE
~
PURIFICATION DEMIN OUT - POWER OPERATION & HOT SHUTDOWl1 (CE-123) 1.2.A
~
Can show need fog Cl, ppm R
I
<0.02 Resin replacement
~
Canshowneedfoh
F, ppm R
I
<0.02 Resin replacement Can show need for Li, ppm W
I Resin replacement 11.0 3 7L j e
g
Mevision 3 1800.2 11/10/76
.l.2.A (cond't) PURIFICATION DEMIN OUT powrp nDFDaTinr1 g unT cunTDnby (f k 1'2 O Analysis Frecuency Limits Desirable Remarks Gama Scan, uCi/ml R
I Gross Compare with 'RC'Lttjown Gross BY to detet e/ne By, uCi/ml W
I Demin DF.
. b e
Determines Borond Boron,(ppm)
R I
sa tu ra tion
,1.2.B MU TANK LIQUID - OPERATION & HOT SH' TDOWN (CE-120)
J Li, ppm R
I Dissolved Oxygen, ppb R
I
~~
~
~ ~ ~ ' ~ ~
~
I B (ppm)
R I
Crud (ppm)
W
<D.1
~~
~~
f*'
~
s;
....._s
.}.,
^
~
.y
- 1. 2. C MU TANK GAS - POWER OPERATION & fiOT SHUTDOWN (CE-120)
Gama
~
' ~ '
Can indicatd need fo'r._ [.
p-Scan, uCi/ml~
~W
'~
..7I~'~
' - ~ - - ' ~~~"- ~
deyassing RC System.~2 C F
Gaseous Prevents buildup of explo Hg & 0, %
W I.
sive mixture in MU Tank 7
_.....i.-.
4 4
-1 t -
z.
'+:_ -i
=.
+. -
- 8
---W*.
a _e
_m,
,)
Revision 3
.l.2.0 RC BLEED TANKS (CE-132) 11/10/)u Analysis Freauency Limits Desirable Remarks pH R
4.8 - 8.5 Cond, umho/cm R
I
'4 4
Cl, ppm R
<0.100 F',
ppm R
<0.100 Crud,, ppb R
<0.100 B, ppm R
0-2205 Li, ppm R
I
~
Gross By, uCi/ml R
I
- Tritium, uCi/ml R
I
~ ~
^ ~
~~
I Dissolved Oxygen, ppb R
<0.100
~~
~
. ~~'---
L.,.
...' : 3 - +
~'
1.2.E DEBOR DEMIN IN & OU7
~
(CE-126 & CE-124) ~ ~ '--
Detects Resin k.
B, ppm R
I Exhaustion
~
.=
. 4 4
.p.
m -.
l
=
j L
13.0 7 r'
- ~ L. - - ^ -
7 D h J J gN.
g
?.evision 3
.l..~.A BORATED WATER STG. TANK 1800.2 11/10/76 bal. sis Froeunncv i imi n Dosi"ble Remarks pH M
4.5 - 8.5 4h-Cond, uaho/tn M
I "ust be same qual ty as SF pool water for'1 C1, ppm M
<0.100 g uelino z
"ast be same quality as SF pool water for F'.
con M
<0.100 r='velino Must be same quality W or
- as SF pool water for B. gom After MU
'2270*
refuelina Ganna Scan. uCi/al R
I g
Gross BT, uCi/ml M
I Personnel exposure
~
Tritit.a.
Parsonnel exposure....
uCi/mi M
I j
(
[
Turbidity, t
lisual M
Clear Si,e as SF pool
~-
t.
i,-
~_,
j'-
s ' 't..
('
_ t.
~ '(CE-121 & CE-122)
- ~.~
l.3.B CORE FLOOD TANKS
~~
pH M
-~
-I k.Cond, umho/cm M
I Fotential RC System C1, ppm M
I
< 0.10_0 contaminent Fotential T
RC Sys tem. :4. - ?.- -
F, opa M
I
<0.100 contaminent J_.
M or
- B, ppm after MU
>2270*
2300-2350 14.0 7
203 356E
'~
Revision 3 11/10/76
.l.3.3 (cont'd)
CORE FLOOD TANKS (CE-121 & CE-122)
A* a l y s i s Frequency Limits Desirabl e Remarks G.oss Check valve leakage B.,.uCi/ml M
I monitoring
- Tritium, Checkvalveleakfgp cCi/al R
I monitoring
- y 7
h 1.3.C SODIUM THIOSULFATE TANK cH Q*
9.0 - 10.0 s9.5
~~
'~
~ ~ ~ '
E, ppm Q*
I 1750 Also after each N: 5 0, W%
Q*
Nominal 30*
makeup
- 0 7
I
~
6 c-
' ; t.g. _
'~
-'~~..'_^1.'
. T ;.!i'~
1.3.0 SODIUM HYDR 0XIDE TANK c
.l
.u r... -
- .. - = _ 2 Nominal Also after each.-. f Na 0 H, W%
Q*
20*
20-22 Makeup *
" ~ ' -
--w
.;.s is.0 203 357 9
.=m6--m
--6eN.
.**.N*
- e_
Revision 3 1800.2 1.3;E,F RECLAIMED WATER STORAGE TA'lK 3 3 f,n ryg i
halysis Frequency
'imits Desirable Remarks Determines suitability Ci, ppm R
I for re-use a
Determines r-R I
Suitability-1
, ppm See Tech Specs. Ypr required soluble B, ppm R
I poison inventerv Gross Determine suitability Bv, 2Ci/ml i
R I __
fnr m-nw Detennine suitability Tritium i
R I
for re-use.
l.3.G,H B.A. MIX TANKS AND RECLAIMED BCRIC ACID TAf1K
~
~
See tech specs for required soluble poison B, ppm 2/W*
I*
inventorv
~
Determine suitability --
Gross B y uCi/ml R
I N-F
-R I
Determine suitability Cl-R I
Determine suitability i~
1.3.I SPENT FUEL POOLS
~
~
).
pH M
4.5 - 8.5 a.
1' I-
, 2 'Cond, umho/cm3 g
7 1E' "
2 Cl, ppm M, W
<0.100
~
2
~
F, ppm M, W
<0.100
-e-
=
3
...e
=
H I
_ __2H, ppm 4.-.- ~ ~ _R During refueling m_.m_
M or
- B, ppm After etU
>2270 2300 - 2350 nz 7cQ b
~
16.0
__1
Revision 3
.,1.3.1 (cont'd)
SPENT FUEL P0OL 11/10/76 inalv ie.
' Erenunncy
-i+
Desirable Remarks Li, ppm R
I Ganna Scan, uCi/ml R
I
- Y Of concern due t /
Gross personnel exposd"c 2
By, uCi/ml M, W I
near_nool Necessary to
- Tritium, calculate airborne 3
uCi/ml M. W I
tritium levels Necessary for observa-Turbidity, tion of refueling I
(Visual)
M, W I
operations.
I refreling i
2demin not in service
~
~
~
t.
j.
2.1.A MAIN & AdX CONDENSERS (CE-19 thru 37 CE-53 & 54) r R
~
I Check for
~. _
s.-
pH tube leaks Ic.-
Check for Cond, umho/cm R
I tube leaks
~,
~
r Check for c
tube leaks ~ " ~ ' _Y.
Cl, ppb R
I e
Check f
, g_.. _ _.
k Check for SiO, ppb R
I tube leaks 2
Check for._ _ _
Cat Cond. (umho/cm)
C I
<0.5 Tube leaks
~~
a A.
6 m,
b 17.0
~
~
203 359
,m,
11/10/76 Revision 3 CONDENSATE PUMP DISCHARGE (CE-2 & CE-3)
.2.1.8 Analysis Frecuency Limits Desirable Remarks PH W
I Indication of %/
Cond, umho/cm W
I denser tube se Indication of tsff-Cl, ppb W
I donsor tub,lo=Lann Cation Cond, Indication of condenser umho/cm C
<l.0 tube leakage Fe,. ppb W
I Indication.of con-Na, pob C
I denser tube leckage Indication of con-SiO, ppb W
I
~
denser tube leakage ~'- '
9 Dissolves Oxygen (ppb).
W
<20 2.1.C,
POWDEX EFFLUENT ~ ~ ~
' ~ ~~' ~ - ~ ' ~~(C E-4)~ ' ~~~" " '
Cat.Cond, umho/cm C-
<0.5
<0.100
~' ~ - "
- :... ;=:
,. g:m C1, ppb W
I C
<20
. J _.e.
".1-l p-Fe, @
~
W~
'~
l~
< 5 ~ ~~ ~
~
~ ~ ~" 5
~ ~.t~. --~~
Na, ppb W
I
<10 Si0,, ppb W
I
<5 j~~~- ~~
g
~..
.m..
._me.6-
,} --
203 Sbu 18.0
~
c)
A>C#
.:, c. v>e 0,
%>b 49' l,,l//
,Q
//// .
%)/
NN [$)'$$f x
'tkc/
(3
\\
IMAGE EVALUATION NN TEST TARGET (MT-3) 1.0 lU2A Si a "? p"22
- 39 b ?:2 lulpl2.0 llll l.l 3"
m llE -
l i.e i
1.25 1.4 Il I.6 li h
m, 8e,>,,
- a&s a
v.g
//
e v.a y
o
+ r y g.
Oy Q' f y
(
&> 'd 0
' D @ a "' A)y; /
A o
,s. or 9
\\y////
h
/,!YtfN V
N
'4N/ @
(4 /kf#
\\
IMAGE EVALUATION TEST TARGET (MT-3) 1.0 lP 02 lm
[h[jff [!!1 li l.l
$@,==
'I '2 i
lles.8 1
i, e
l.2 5 ll ! A 1.6 4
6" 1
A,%,/
/+
^ ///,,\\\\
4 + A f'
@,w,gs#cs& f 6
v
\\
/
x ge 7
o,s *y e,
t*
- g
.:gse
(
A> ',6 s.9 'de i..
- $M+$> $ h %df7
- ' lb p.
g k
IMAGE EVALUATION NNNN TEST TARGET (MT-3) 10 lSla BA i2 22 s]=2.2 igg n,e b rt; Llj2.0 l.I t..
=.
!!i1.8 ill I.25 M IA 1.6 nn- -
6" i
+ sh' xi%vi
- 4 Qste s
n e_=.
o "a 9
/
(fb Q
%f
-r O
&W ge
(
hb>
l u,*'s
/ /g s
"Ihhk Ig}9 k
\\\\ 9/ v q 4[g4 <p 9
%9,
/g /%% ga v
4pff F
IMAGE EVALUATION TEST TARGET (MT-3) 1.0 F E24 m
-[f[ fell
'lI.i
[*LM I
!!!!B 1.25 1.4 "i l
== liil.6 6 %.
/p su kg
%h
'h
/
ulcu? S'?////.
<3 4?//,K ob,%,., *
"6,f.
8 s
0 j,
~
\\
-N L\\
QQ f
+
t
1800.2 Revision 3 11/10/76 2.1.D CONDENSATE B0OSTER PUMP DISCHARGE (CE-5)
Analysis Frecuency Limits Desirable Remarks Check on ammonia Cond, umho/cm C
I 5.7 - 8.4 feed system Sufficient to ad pst i
NH, ppb W
0.7
'1.5 pH to 9.3 -9.5 HW 3
Valu%
N Ha, ppb C
20-100 300 /.of 02 e
9 Dissolved Oxyaen (ppb)
C
<7 2.1.E STEAM GENERATOR INLET (CE-6) pH C
9.3 - 9.5
~ ~
~ ~
, Cation Cond, umho/cm C
.<0.5
~
'~
~ ~ ~
~
-~
I NH, ppb R
I 3
N H, ppb D
20-100
.t 300 /, ot' 09 Value
[.
p4
~
^
~ ' ' '
f Fe, ppb D
10
~
~ - - - - - -
p...'..
~ '
Cu, ppb W
2 l
,2 t
Na, ppb C
<20 i
g'_ :'SiO, ppb
~
D
- ~ < 20
~'
~ ~!c;b.-~ -
~~~
2 i
Dissolved
' ~'
~
Oxygen, ppo~
D,C
<7 F-
~
~~ ~~
h -- l-y I
4 q
-=
Cl, ppb
~
~~
~~
I
~
~
~ '~
1 " '
~
w
_m.-
Pb, ppb W
0.0
') []
(', () ]
~ ~. ~
~
19.0
,,m gg e p
..-.mwwe.
Revis' ion '3
.2.1.F CONDENSATE STORAGE TANKS 11/10/76 Analysis Frequency Limits Desirable Remarks pH W
I 9.3 - 9.5
'1 Cat. Cond, umho/cm W
I
]
Q N H, ppb W
I Slight residual 9 a Indication of failure Fe, ppb Q
I
<20 of epoxy lining Dissolved Should be run if Oxyggn, ppb W
I no hydrazine present I
2.2.A STEAM GEN. SHELL SIDE - WET LAYUP (CF-R & FF ol pH DI 9.5 - 10.5
-~
~ ~
Cat. Cond, umho/cm DI
<10
~'
~
CIT, ppm I
- ~~
~~
~~
' ~ '
~~-
D
<1.0
+
I NH, ppm D
2-20 z
g I
N H, ppm D
<50 s200 p4
~
L ~ Na, ppm
~~
DI
<l.0
~ ~ ~ ' ~
~~
~ ~~ ' ' '~~
~
- 1. Frequency reducec to weekly after cheinistry stabilizes
~
~
mm.
b ee,e-e+
e
. w_s
-o_m
_~ - _** * *
=
20.0
- ~
204 002
~
u i.c
~
11/10/76 Revision 3
-2. 2. Q _
STEAM GEN. SHELL SIDE - OPERATING CONDIT'ONS <l5% POWER (CE-8 & CE-9)
Analysis Frequency Limits Desirable Remarks pH 3/D I
Cation Cond, umho/cm 3/D
<10.0
~(<
7 Cl, ppm 3/D
<l.0 Daily at less Na, ppm 3/D
<2.0 than 15% power Gross RCS >300 psig or By,,uCi/ml W*
<2.0 x10-8*
Tav >200 F only*
0 Radio-I Iodine, uCi/ml R'
I 1.
Performed when t ross b: inc ease by a factor of 2 above backgrot nd.nd each 10f increase th( rea f tr.r.
l 2.3.A MAIN STEAM (CE-15 & CE-16)
~~
l
"~
pg y
y L
Cation Cond, umho/cm W
I s.
'i Check on SG Na, ppb W
I carryover l
~
Check on SG ~.
.1 1 s SiO2, ppb W
I carryover
"=
pC1 1
Tritium W W
I.
-.,,s 20/
003-21.0 1
eu
.c 11/10/76 Revision 3
,2.3.8 MOIST"RE ScDARATOR DRAINS (CE-13 A. B. C. O. F. F Analysis Frequency I Limits Desirable Remarks pH R
I Cation Cond, If umho/cm C
I if d r,.y Fe, ppb R
I Dissolved Oxygen,' ppb R
I Na, ppm R
I Silica ppm R
I 2.3.C
- 6T,H STAGE DRAINS TANK (CE-12)
~
7
. Cation Cond,
-s
.-~
~..
L
('
Fe, ppb z-W I
.).-'.
- c.: e..
u-Na W
I
. -a:... - - : y...
i D
t--
2.3.D H.P. HEATER DRAINS 2ND STAGE (CE-10 & CE-11)
~
~ pH W
I 9.3 - 9.5 Cation Cond, T
I umho/cm W
I
~
NH, ppb W
I 3
E04004 22.0
.m.
eme
11/10/76 Revision 3
.2.3.D (cont'd)
H.P. HEATER DRAINS 2ND STA3E (CE-f0 & CE 11) (enni 'dl Analysis Frequency Limits Desirable Romarks Indication of erro-Fe, ppb W
I sion an HP heater tubes 1l Na, ppb R
I f
g i.
3.1.A INTERMEDIATE COOLING CLOSED pH W
8.7-9.0
- Cond, Cl, ppm W
<1.0
~
f F',
ppm W
<l.0
~
~ ~ ~
300%
Dissolved
- -. ~.. !
1
-N H, ppm W
p4 0xvoen Content CROSS L~
Ey,.uCi/ml W
I
~
~ ~ ~
~
ti
- Tritium, z_
Y-u^i/ml R
I i
- y. -
Morpholine ppm R
.. I.
t
^
[~
Dissolved Oxygen
~ W
~~
I '-~ ~ ~ -
~-' ' ~
" - - ~ ~
~ ~ '-~
- -
- ~~
I:
l Aninonia (ppm)
W 0.1 -3.
' ' ~
3.1.B NUCLEAR SERVICES CLOSED pH W
8.7 - 9.0
~ ~.
- Cond,
-:=.
23.0 2 O k - U O
~
9 e
w
=
w==
w.
Revision 3
3.i.B(cont'd) NUC' r^R SERVICES CLOSED 11/10/76 Analysis Frequency
.ts Desirable Remarks Cl, ppm w
<l.0 x
it7 F, ppm W
<l.0 1
300%
Dissolvec Tg N Ha, ppm W
0xygen Content 9
Gross By, uCi/ml w
I
- Tritium, uCi/ml R
I Morpholine ppm R
I i
~-
3.1.C SECONDARY SERVICES CLOSED
~
' -~~
pg W
8.7 - 9.0
~~ ~
~~~ ' ~ '-
'-~~"
Cona,umho/cm W
I
+
300%.
Dissolved M H, ppb W
content.
%~E5 ""
- ~
74 _
Indicat. ion or effectiveness of
~ ~'
- i. '. Fe, ppb I
corrosion inhibitor N
y k..
Morpholine ppm p
y
~
4 o_
4'w
. :. - - ~ *'~~'
2U4 UUO
,4.0 9
9 e
.e
....e..
Ibuu.2 Revision 3 3.1.D DECAY HEAT CLOSED 11/10/76 Analysis Frequency Limits Desirable Remarks PH W
8.7-9.0 si Cond, umho/cm I
y y
'5 Cl, ppm
<l.0 y
F, ppm
<l.0 y
300%
Dissolved N "4' PP*
W 2
0xygen Content Gross By, uCi/ml I
y
- Tritium, uCi/ml R
I 1.
Morpholine ppm W
I l
h
..i
.., ~ -
.s
~
'. -4. ;. '
.-.:~.....,
3.1.E CHILt.ED WATER CLOSED SYSTEMS
,e.,. ' "
l g
pH M
I
?-
~
},:"~Cond,
~
j
~ ~ ~ ~ ~ ~
4-umho/cm M
I
~~
~
~
-~~'~
~ ~ T '"- -
Indication of effect-iveness of corrosion Fe, ppb Q
I inhibitor Corros.on Inhibitor, ppm M
I
~~~~2'~~~
~~
i 25.0
}g/
007 4
~
Revision 3
,,3.1.F DIESEL COOLING SYSTEM 11/10/76 Analysis Frecuency Limits
_ Desirable Po-u k t pH M
I l
j/
Cond, umbs/cm M
I Corrosion "1
Inhibitor, ppm M
>1500 1500-2500 Drewguard 3.1.G STATOR COOLING SYSTEM pH W
I
~
~
~
Shows need for Resin Cond, umho/cm W
< 9.9
<0.5 Replacement Can show resin J_
Nii,, ppb M
I degredation k '._
Can show errosion _.. _
Cu, ppt M
1 of conductors
~
3
~
3.2.A AUX. BOILER FEEDWATER
,w:.
j pH
~
DI 8.7 min.
~~
9.3 - 9.5
~
~~~ ~ ~ ~ ~
~~
i I
Cend, umho/cm D
1 max.
0.5 max Cation Cond Cl, ppb I
I 100 max
]
~
~
D
~
f g
NH, ppb DI
~ ~
3 I
700 - 1700 N li, ppb DI p4 20 min.
20 - 100 26.
204 008
~
~
Sb
~--.,_._.,_,_a
~- -~-
~
11/10/76 Hevision 3
' '3
,3.2.A (cond)
AUX. BOILER FEEDWATER Analysis Frcquency Limits Desirable Remarks Na, ppb DI I
200 max 4
I Si0, ppb D
7 500 max' 20 max
~
(7 3.2.8 AUX BOILER BLOWDOWN I
ph D
8.5 min 8.7 min I
Cond, umho/cm D
10 max 6 max ~
~~ Cation Cond.
~~~
~
Cl, ppb D)
I 1000 max I
~
Na, ppb D
I 2000 max
)
SiO, ppb
.D I
209'J max
~J T ~ ~~ '~
~'
2 S-"
1 g
.-.--.-------*-=**-*=--*=m 7
s c'.
r r _. _
- w.-.
n
_- bE I
3.2.0
~~~;~ AUX. BOILERS STEAM
' ~ ~ ~ ~ ~ ~ '
~ " -
t.
l 3
3; pH D
8.7 min 9.3 - 9.5 i
I
~
~
~
Cond, umho/cm D
I
<0.5 Ca tionio~n~d. [
~
n.. - -
=
am..~.
~
.v
,3 ~ _
3_
-*~*_~d=
~ * + ~
?7 0 zog-2(j9 ~ - ;
N
- -wA+e>=
--e.-
m_
O O.aw a
men.m
.Mhe
_-_4
'00.2 Revision 3
--4.1. A CLARIFIER EFFLUENT 11/10/76 Analysis
, Frequency Limits Desirable Remarks Will vary with pH 3/W I
river pH D
Cond, umho/cm 3/W I
1 Indication of need to Turbidity, JTU 3/W
<5.0 change chem. feed Free Insures oxidation of Chlorine, ppm i
3/W I
0.5 - 1.0 Fe and Mn 4.2.A CARBON FILTi EFFLUENT
~
l Free Indicates need for steam i
Chlorine, ppm W
0.0 ing or replacement
{
~
[
4.2.F CYCLE MAKE-UP DEMINERALIZER EFFLUENT
~
(CE-1)
J~
~' _
r,
-n
.. -.. ~ -
pH W**
6.0 - 8.0 I
I cond, umho/cm W**
I
- 0.100 Cl, ppb W**
100
<20
'~
~~
~ ~
1 F',
ppb W**
100
<20 ~
~
_.._..{_..a._.
._..u_._..
i E '~ ~
~ ET L'
~
Pb, ppb W**
<1 Cu, ppb W**
<2 r:-
1
~
Na, ppb
[
W**
I
~
- Sampled when demin. is in ser,vice.
70$
ih-
~
~
28.0
~
~
.8 m.
h as g
~
1800.2 Revision 3 11/10/76 3
'4.2.F (cont'd) CYCLE MAKE-UP DEMINERALIZEP, EFFLUENT (CE-1) f Ana lys_i s Frecuency Limits Desirable Retatis Si0p, ppb W**
20
,<5 Oxygen, ppb W**
<100 f
Dissolved g
w
- Sampled when demi n. is in ser vice.
C 43.G DEMIN. WATER STORAGE TANKS Cond. tanks will follow pH of cond. -~
pH W
~ I 6.0 - 8.0 system I
umho/cm W
I
<0.5
[
Cl, ppb W
I
<20
~
F', ppb W
I
<20 F,'
p.
f F2, ppb M
I
<100 E-After each mixed.._
P Na, ppb R
I bed regen.
I...
__.__.__.x
... _....__in-5 _m 2
[.
.~
4.3.A RIVER WATER Used for determining 3/W I
pretreatment chem -~~
pH 5
feed
- Cond,
~ ~ ~
~
~
~~
1 Used for determtn-
~~
ing pretreatment
.O umhofcm 3/W I
chem feed LU4 U.I 1.
' Cl, ppm R -
I
"' E 29.0 9
Revision 3 i
1800.2
4.3.A (cont'd)
RIVER WATER 11/1 n / 76
__ Analy_ sis Frenuencl _ _.___ Limits
___ Desirable Remarks In conjunction with discharae Fe, ppb W
I iron sample ~
Na, ppb R
I
.l Usedfordetermlih ing pretreatment Turbidity, JTU 3/W I
chem feed Hardness, ppm j
W I
Suspended Solids (ppm)
R I
Dissolved Solids (ppm)
R 1
4.3.D MAKE-UP DEMIfi. NEUTRALIZIt1G TANK
~
R*
or before pH each dump 6.0 - 9.&
R or before 7 --
Fe, ppm each dump I
L. -.
-(ppm) orbehore
_Disso_lved Solids each dump I
~
R s,
or before
..m
' ~ Total Solids, (opm) each dump I
L Suspenc'ed Solids or'before
_ I
_,[_ _ _ j (ppm) each dump P
~
d'_
___.w [-$t-
.:. =-
4.3.E RIVER WATER DI5udARGE 204 012-..
pH W,*
6.0 - 9.0 *
~ " -
~
T S
I Cond, umho/cm W
I
~ '
Industrial -
I Fe, ppm W
7.0 Waste Permit'
- ~
30.0
Revision 3
- '4.3.E (cont'd)
RIVER WATER DISCHARGE 18nn y 11/10/76 I
____/ma l ys i s Frequency Limits Desirable Remirks Total 0.2 max total
- 10,30 & 5') min af ter Chlotine, ppm C 2*
<0.1 max free
- start of :hlorination Suspended J
I Solids ppm W*
560
- Dissolved I
Solids ppm l
W*
700
- monthly average <500 Alkalinity, Caco-ppm as CaCoq W
I
<100 ppm as l.
Also during eact re;t. rege 1. waste discharge 2.
Daily when moni' or is out o service r
1
~ - -
I 4.3.F MAIN CONDENSER CIRCULATING WATER p
l 3
Depends on pH W
I 6.5 - 7.0 Langelier Index Indication of nur$ber
~
Cond, umho/cm W
I of conc. cycles v.c..
i
+
i Indication of number
[ Na, ppb R
I of conc. cycles Measured during chlor-Free ination cycle at the Chlorine, ppm C 'l
- 1 max
- 0.5 - i.0 blowdown at 10, 30 and.
50 minutes after the
- m..
beginning of the cycle 1
_ Langelier Index W
-0.5 <SI <0.5 1.
Required daily i hen chlorin a monitor is not ir service.
~
F-
.., gg
... ~ _. -
r
'T 2z
= ss.s. - -- - --
-*m-sevm=P,c ersgat e
,mer aras ames a =. mar sw en- -
-7
_. ~.
[
31.0
~~
J
.a.
a
1800.2 Revision 3
=
11/10/76 4.3.G SEWAGE TREATMENT PLANT Analysis Frequency Limits Desirable Remarks W
I Raw Influent
~
PH D
6.0-9.0 Final Effluent '
~
(.
Total Phosphorus, W 2-WA Raw Influent 1
mg/l W*
4-DM Final Effluent M.
Dic,olved Oxygen, D I
Aeration Tanks PFM D
> 5-WA Final Ef fluent Settleable D
I Aeratico Tanks
._ Solids, %
D I
Primary Clarifier -_..:
I Suspended 2/W 30 - WA 1000-4500
- Aera tion Tanks
. _~G..--
Solids, mg/l W
60 - DM Final Effluent (Composite-8 Hours)
Free _.
2/W. _ _ _
._ I
I _ _. _ _.
.__ _ l-2
_ Chlorine Contact Tk _. _
L
.1 Final Effluent 1
8.0.D.,
W 30-WA 150-400 Raw Influent
' - - ~ ~' -
mg/l W
60-DM
-. 5 ; -~ -
- n. Final Effluent "rO.w.
, L __...
' (Composite-8 Hours) ~'
Plant Must Reduce BOD By 85% - - -
1--
wii.. l.. Turbidity, NTU D
I
.f f ~ =.
- Z..
l Secondary Clarifier".I..u. f
~
~~~~~(, Total Solids,
W
.I T ~~ ~
Aerobic Dig'este - ~
~
~ ' ~ ~
.. ~...
?ji.y...mg/1
-2..
1_-
~
g m.
2.;
.q,._...._ g __;..__;g g. _g.g, g Fecal
_W 2
-200/100 ml-MA Final Effluknt --i;ff-(' z. ;.t__ _...
' Coliform ' - ~ ~
. _.. _ "., ~ -7 400/100 ml-MA
._...._-.7.__=.._=~'.-
._=..,=....--_~.,-...=__N.,._'="~-
7
.s.
.c 4..
'y v.
. w s-
-a,.s..s.,.;.,....<e.. Fs e
- ~
~
s
... ~
........._.n:. - -.. _.:---__..
.r.
.. / a.. --.
.-*we e
a.-
er e
e
.7
_**y
.y #e
).
.g.
p.4 4
g.
.p " g '
,.g g
- -4 c.
.e a
e.'.
T.. - '.
Ls e 1
.e,.-
,,/y Ie-
~ ~ -
-._2.
C-- N.4 -A-
=
=
.~..
_.,. 7. 1.. _.3.._...
s..~.
32.0
" ~
Revision 3
4. 4. A POTABLE WATER 1800.2 11/10/76 g
Analysis lFrer. enc L Limits Desirable Rema rks pH W
I Cond, umho/cm W
I g
Hardness, ppm 4
I Hot water only Free Chlorine, ppm i
W
>0.2 0.2 - 0.5 Free of coliform Count r.ade by Certi-Bacteria count M
Bacteria fied off-site lab 5.1.A M I_ S_C. WASTE 9TG. TAN K (CF-1711 Used in determining
}
pH W
~
I treatment Used in
- Cond, determining ' ~ ~ C T umho/cm W
I treatment l.
Ganma Scan x
I Used in
.n_
z-Gross By, determining uCi/ml V
I treatment
%' Total Used in
~'
determining T_~
Solids,(ppm)
W I
trea tment
%.-.-d--f-'_
Boron, ppm W
I
~ ~
.. ~
~
V_
m S.1.B
~
LAUNDRY WASIE_SIORAGLIANK
=
(CF 1W I
Used in.
= -
determining
?-
JL
-_,,,, w AN._..
...~. l.
- -. =
t rN LC.CDt Used in Cond, umho/cm V
I determining. ~
~~ -..
trnatront 4
7,g4 g}$
~
33.0
Revision 3 11/10/76
~ i.
~.
LAUNDRY WASTE STORAGE TANK 1800.2 ) (cont'd)
.' 5.1.B (cont 'd)
(CE-135
(
nalyLis Fre_cuency Limits Desirable Remarks Gamma Scan R
I Used in Ci/ml W
I
<l.0x10- g he "9
I Used in g
- Tritium, determining uCi/ml W
I treatment Used in Total determining Solids, (ppm)
W I
treatment Boron (ppm)
U I
<25 5.1. 0 WASTE _ (VAPORATOR_C_DfjDENS ATE STORAGE TANK Show suitability for pH R
recycle. Can also sh w 4
I 6.0 - 9.0 need for resin replacem
- Cond,
~
umho/cm.
R I
a a
a Cl, ppm R
I a
a a
e F, ppm R
I a
a
=
E"
. 2 B, ppm R
I
<25 ppm
' Gross
~-
~ - M -
~.
- - -9 "
By, u.Ci/ml
~ R I
a a
f Limits as expressed Tritium R
I in HPP 1621 Gamma Scan (uci Limits as expressed '
ml R
I in HPP 1621 t
5
~
O Mm_ _ _
^""M h-
.~.
204-016 34.0 w.h-