ML19224B425
| ML19224B425 | |
| Person / Time | |
|---|---|
| Site: | Crane  |
| Issue date: | 12/13/1977 |
| From: | Metropolitan Edison Co |
| To: | Mullinix W NRC/IE |
| References | |
| 1800.3, TM-0181, TM-181, NUDOCS 7906150086 | |
| Download: ML19224B425 (27) | |
Text
6',
,.r s'
4 TMI DOCUMENTS voCauruO.TM-0/1/
METROPOLITAN EDISON COMPANY.
e t.
Wilda R. Mullinix, NRC F
7906150086 4.i s..
.l '.
204 017 P
m
1800.3 Revision 0 h
12/13/77 THREE MILE ISLAND NUCLEAR STATjOAI I CTZ?
> U t ' tr
/
i o-
'< ~i STATI0t1 CHEMISTRY PROCEDURE 1800.3 {\\}
\\
" n Ad e dVV,(
f O [- n.i n g / -
WATER CHEMISTRY MAtiUAL (UtilT 2 OtiLY)
Jd Table of Effective Pages
[
{}
)
Page Date Revision Pace Date Revision Page Date_
Re sion 1.0 12/13/77 0
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41.0 66.0 l
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_ _ _ _ _ __ _ _ ___. 67.0
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47.0 72.0 23.0 12/13/77 0
48.0 73.0 0
49.0 74.0
[;. 24.0 12/13/77, 25.0
_12/13/77 0
50.0
-- 7 5.0
~
Unit 1 Staff Recommends Approval Unit 2 Staff Recommends Approval
~
Y-
~ ' Date !M 71 M
Date Approval Approval
~
Cognizant Dept. Head Cognizant Dept. Head Unit 1 PORC Recommends Approval Unit 2 PORC Recommends Approval A/
Date Date Cha : man of PORC Chairrnan of PORC a'
Unit 1 Superintendent Approval Unit 2 Superintendent Approval h
Date
,)
}
Lf Date 9
/
Manager Generation Quality Assurance Approval
/f/
Date -
204 018
" " ^ " ' ' " " '
1800.3 Revision 0
- r..
12/13/77 THREE MILE ISLAfiD fiUCLEAR STATION STAT 10l1 CHEMISTRY PROCEDURE 1800.3 WATER CHEMISTRY MAfiUAL (UNIT 2 ONLY) t SAMPLE LOCATIONS 1.0 WATER TRE_A_TMENT 1.1 Make-up Pretreatment a.
Floctreator Effluent b.
Floctreator Sludge Header c.
Floctreator Reaction Cone 1.2 Make-up Demineralizers a.
Carbon Filter Effluent
- b.
Cation Unit Effluent c.
Anion Unit Effluent d.
Mix Bed Unit Effluent
- e.
Vacuum Degasifier Effluent f.
Deminera'ized Water Storage Tank g.
Neutralizing Tank
- No Established Analysis Requirements l.3 Raw Water Systems a.
River Water Influent b.
Cooling water chlorination c.
Condenser Circulating Water d.
Circulating water chlorination e.
River Water Discharge
_ _. 43 f.,
i i
k 1.4 Potable Water a.
Domestic Water (Unit 1) 204 019 3.0
1800.3 Revision 0 12/13/77 2.0 SECONDARY PLANT 2.1 Feedwater Train a.
Condenser Hotwell i
b.
Condensate Pump Discharge
-+
Condensate Polisher Effluent d.
Condensate Booster Pump Discharge e.
Steam Generator Feedwater Inlet f.
Condensate Storage Tank 2.2 OTSG Secondary Side a.
Wet Layup b.
< 15% Power 2.3 Steam Train a.
thin Steam b.
Moisture Separater Drains c.
Heater Dra.in Tank d.
Heater Drain Cooler
~
7-3.0 AUXILLIARY SYSTEMS 3.1 Closed Cooling Systems
-~
-- ' ' ;~
' - ~ ~ ~ ~ ~ ~ ~ ~
SecondarySerEiceClosedCooling a.
s b.
Nuclear Service Closed Cooling c.
Decay Heat Closed Cooling d.
Intermediate Closed Cooling e.
Diesel Cooling f.
Service Bldg. Chilled Water g.
R.B. Evaporator Cooling Water gj.
qe h.'
Control Bldg. Chilled Water
. f..
I 1
A; 204 020 2.0
1800.3 Revision 0 12/13/77 4.0 PRIMARY PLANT 4.1 Reactor Coolant Systems i
a.
R.C. Letdown i
b.
Decay Heat c.
Pressurizer Water Space d.
Pressurizer Steam Space 4.2 Make-up And Purification Systems a.
Purification Demin Outlet b.
Purification Demin Inlet c.
Make-Up Tank Liquid d.
Make-Up Tank Gas e.
R.C. Bleed Tanks f.
Deborating Demins f
4.3 Miscellaneous. Primary Systems a.
BWST b.
Core Flood Tanks t-c:
Na0H Tank b
d.
Reclaimed Boric Acid Tank i
e.
Boric Acid Mix Tank f.
Spent Fuel Demin Outlet 5.0 WASTE SYSTEMS 5.1 Liquid Waste
-l
~
a.
Miscellaneous Waste Holdup Tank b.
Contaminated Drains Tank 1 1
- c. ' Concentrated Waste Storage Tank.
if 1
~
- d.
Evaporator Condensate Demineralizer Outlet 3o 204 021
180P 3 Revision 0 12/13/77 e.
Evaporative Condensate Test Tank f.
R.C. Evaporator Feed Tank g.
R.C. Evaporator Outlet i.
h.
Cleanup Demineralizer Outlet
~1,
- i.
Neutralizer Tank
- j.
Auxiliary Bldg. Sump Tank
- No Established Analysis Requirements 5.2 Gaseous Waste
- a.
Waste Gas Decay Tanks b.
Vent Header
- No Established Analysis Requirements 6.0 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 analyses may be increased (up to 25% of the sample period) 3 according to plant operations.
For example more 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 U
required by icchnical Specifications, may be deleted, on an intermittent basis upon approval of the Chemistry Supervisor if unit conditions or department workload are' restrictive.
Such deletion choli be I
reported to the Technical Engineer and the Unit Superintendent.
The report should indicate when it is expected that the analyses shall be next performed.
'i 4
b.'
h 4.0 204 022
1800.3
/
Revision 0 12/13/77 Legend Frequency 4
0 - Daily W - Weekly 3/W - 3 analyses / week, assuned to be Mon., Wed., Fri.
5.W - Analysis to be performed each working day.
M - Monthly Y - Yearly Q - Quarterly R - As required C - Continuous Monitor NOTE:
The maximum
.lowable time interval for any given
~
analysis is that specified +25%.
L Limits
~ - - '
I - No limit set by manufacturer or tech specs.
Analysis made to obtain necessary information.
~
./
^
i
- - Following a limit indicates technical specification or permit limit.
The frequencies given meet or exceed requirements.
for normal operating conditions.
See Tech. Specs., NPDES or Ind. Wst. Permits for further information.
~7 Y-'~~
p-4' r.
204 023 5.0
to00.3 73713)99 1800.3 1.1.A FLOCTREATOR EFFLUENT analysis freq.
limit desirable remarks PH 3/W I
Used for Determining Pred atment Chem. Feed.
Cond. pmho/cm 3/W I
Used for Determining Pre eatment Chem. Feed.
Turbidity NTU 3/W I
Used for Determining Pretreatment Chem. Feed.
Alkalinity PPM 3/W I
Used for Determining Pretreatment Chem. Feed.
Fe PPM W
I
!ia rdness PPM W
I Cl-PPM R
I Na*
PPM R
I Sus. Solids PPM R
I
-~
. Dis. Solids FPM R-I 1.1.B FLOCTREATOR SLUDGE HEADER Settleable Used for Determining Pretreatment Solids 3/W I
70 - 90%
Chem. Feed. _.
~
1.1.C FLOCTREATOR REACTION CONE Used for Determining Pretreatment Settleable 50 - 70%
Chem. Feed.
Solids 3/W I
e
.~
o 204 024 6.0
1800.3 Revision 0 12/13/77 1.2.A MAKEUP DEMIN. CARBON FILTER EFFLUENT analysis freq.
limits desirable remarks chlorine PPM W
0.0 Indicates Need for Replatelbat or Cleaning.
a 1.2.C MAKEUP DEMIN. ANION UNIT EFFLUENT PH I
' Cond. umho/cm I
Cl-PPM I
F~
PPM I
S0 PPM I
52 Na PPM I
Fe PPM I
- SAMPLED NEAR END OF RUN (WITHIN 10% OF TOTAL THRUPUT).
1.2.D MAKEUP DE'4IN. MIX BED UNIT EFFLUENT Y
PH 6.0 - 8.0 Cond.hmho/cm
~
~ ~
~
I
<0.1
~
Cl-PPM 0.100 F-PPM 0.100 S0 PPM 0.020
<0.005
$2 Na PPM I
Fe PPM
<0.010
" ~ ~
- SAMPLED NEAR END OF RUN (WITHIN 10% OF TOTAL THRUPUT).
<(
. ?..
4' i
f L
m.
7.0 204 025
1800.3 Revision 0 1.2.F DEMIT 1ERALIZED WATER STORAGE TANK analysis freq.
limits desirable remarks PH W
I 6.0 - 8.0 Cond. umho/cm W
I
<0.50 i-Cl-PPM W
I
<0.020 F-PPM W
I
<0.020 Fe PPM M
I
<0.100 Na*
PPM R
I l.2.G MAKEUP DEMIN. NEUTRALIZING TANK PH R
6.0 - 9.0 6.5 - 8.5 Fe PPM R
I Sus.
Solids PPM R
I Diss.
Solids PPM R
I
- ~ - - ~ ~ ~
~
1.3.A RIVER WATER INFLUENT PH 3/W I
Used for Determining Pretreatment Chem. Feed.
L Cond.' pmho/cm 3/W I
Used for Determining Pretreatment Chem. Feed.
.x s.
Turbidity NTU 3/W I
Used for Determining Pretreatment Chem. Feed.
Al ka.
PPM 3/W I
Used for Determining Pretreatment Chem. Feed.
Fe PPM W
I In Conjunction with Neut. TK.
Discharge.
Hardness PPM W
I Cl-PPM R
I Na*
~
PPM R
I 4
Sus.
In Conjunction with Neut TK Solids PPM R
I Discharge.
Diss.
In Conjunction with Neut. TK Solids PPM R
I Discharge.
OnA n74
{ U t}
U L_ u 8.0
1800.3 Pevision 0 12/13/77 1.3.B COOLING WATER CHLORINATION analysis freq.
limits desirable remarks free
<0.1 max
0.2 max. total
<0.1 Chlorination.
- REQUIRED DAILY WHEN CHLORINE MONITOR IS NOT IN SERVICE.
1.3.C CONDENSER CIRCULATING WATER PH W
I Depends on Langelier Index Cond. umho/cm W
I Depends on Langelier Index Na*
PPM R
I Indicates Number of Concentration Cycles.
Langelier Index W SI = +0.5
'.3.D CIRCULATING WATER CPLORINATION
~
Free 10,30,50 Min. After Start of l.0 Max.
0.c -__1.0 Chlarination.
1.3.E RIVER WATER DISCHARGE I
PH W
6.0 - 9.0*
I b-Cond. Omho/cm W
I y
I Fe PPM W
7.0(Diss.*)
l 4
Sus.
I L'
Solids PPM W
560*
~
~
Diss.
~
~
j Solids PPM W
700*
Monthly Avg. <500 Al ka.
PPM W
I
<100 PPM as CaC03 I DURING EACH NEUT. TANK DISCHARGE.
,y A
i
{.
9.0 204 027
1800.3 8evision 0 12/13/77 1.3.F SEWAGE TREATMENT PLANT analysis freq.
limits desi rable remarks PH W
I Raw Influent D
6.0 - 9.0*
Final Effluent 1-Total mg/L W
I Raw Influent Phosphorus W
2*
Final Effluent Dissolved D
I 2-5 Aeration Tanks Oxygen Mg/L D
>5 Final Effluent Settleable D
I Aeration Tanks Solids %
D I
Primary Clarifier Suspended 2/W I
1000-4500 Aeration Tanks Solids Mg/L 1/W
< 30
- Final Effluent FREG 2/W I
1-2 Chlorine Contact Tk.
Final Effluent B0D Mg/L W
I 150-400 Raw Influent W
< 30*
Final Effluent Turb.
NTU D
I Secondary Clarifier Total
. Solids Mg/L
~W -
I Aerobic Digester Fecal Coliform W
200/100Ml*
Final Effluent 1.4.A DOMESTIC WATER Bacteria Count M
0 6--
i t
1 a
.b' h.
204 028 10.0
1800.3 Revision 0 12/13/77 2.1.A CONDENSER HOTWELL analysis freq.
limits desirable remarks PH R
I Check for Tube Leaks.
Cond. umho R
I Check for Tube Leaks Cl -
ppb R
I Check for Tube Leaks.
Na+
ppb R
I Check for Tube Leaks.
S0 ppb R
I Check for Tube Leaks.
52 CAT.Cond. umho C
<0.5 Check for Tube Leaks.
2.1.B CONDENSATE PUMP DISCHARGE PH C
I Cond. umho W
I Cl-ppb W
I Indication of Tube Leaks.
Fe ppb W
I
- - ~ ~
- - ~ - -
S0 ppb W
I Indication of Tube Leaks.
j2 D.0.
ppb W
<20 Na+
ppb W
I Indication of Tube Leaks.
~
Cat.Cond. pmho C
<l.0 Indication of Tube Leaks.
~~
2.1.C.
CONDENSATE POLISHER EFFLUENT f
CAT.Cond. pmho C
<0.5
<0.3 PH C
I l
Na+
ppb C
<20
<5 Indication of Polisher Breakthrough
..l Cl-ppb W
I Fe ppb W
I
<10 012 ppb W
I
<5 f-k 204 029 11.0
1800.3 Revision 0 12/13/77 2.1.D CONDENSATE B0OSTER PUMP DISCHARGE analysis freq.
limits desirable remarks i-Cond. umho C
I 5.0 - 8.5 Anmonia Control CAT.Cond. umho C
I NH ppb C
20 - 100 50 3x0 V lue 24 2
0 ppb C
I
<7 2
Nii ppb W
- 0. 7 - 1. 5 To Adjust PH 9.3 - 9.5 3
2.1.E STEAM GENERATOR FEEDWATER INLET PH C
9.3 - 9.5 CAT.Cond. umho C
<0.5 0
ppb C,D
<7 2
Na*
ppb C
<20
<5
~
~
[
NH ppb C
I 20 - 100 To Control 0 Below ppb.
2z 2
NH ppb R
I j
3 Fe ppb D
<10 Cu ppb W
<2 s
S0 ppb D
<20 g2 Cl-ppb W
I
~
Pb ppb M
0.0 t
I.
4:
?.
1 4
104 030 12.0
1800.3 Revision 0 2.1.F CONDENSATE STORAGE TANKS 12/13/77 analysis freq.
limits desirable remarks PH W
I 9.3 - 9.5 i,
Fe FPb W
I
<20 4
NH PFb W
I Some Present 24 CAT.Cond. umho W
I 2.2.A OTSG IN WET LAY UP I
PH D
9.5 - 10.5 I
CAT.Cond. umho D
<10.0 I
Cl-PPM D
<l.0 I
NH PPM D
2 - 20 3
I NH PPM D
50 - 200 200 24 I
Na*
PPM D
<l. 0 2.2.B OTSG AT <l5% POWER PH 3/D I
CAT.Cond.
3/D
<10. 0 Cl -
PPM 3/D
<l.0
.. ' - ~
Na*
PPM 3/D
<2.0 i
1.
Frequency reduced to weekly after chemistry stabilizes.
I
~
4: ~
k 13.0 204 031
1800.3 Revision 0 12/13/77 2.3.A MAIN STEAM analysis freq.
limits desirable remarks i-PH W
I CAT.Cond. umho C
0.3 To maintain W Turbine.
Na*
ppb C
5 To maintain W Turbine.
S0 PPM W
I 52 f.{f1 Tritium g
Cl-ppb C
5 To Maintain ti Turbine.
2.3.B MOISTURE SEPARATER DRAINS PH W
I CAT.Cond. umho C
I Fe ppb W
I Dissolved 0xygen ppb W.
I Na+
ppb W
I
~
S0 ppb W
I j2 2.3.C IIEATER ORAIN TANK i
PH W
I s
CAT.Cond. pmho C
I Fe ppb W
I Na+
ppb W
I S0 ppb W
I j2 2.3.0 HEATER DRAINS COOLER PH R
I 4: -
k-CAT.Cond. umho R
I Fe ppb R
I 204 032 Na+
ppb R
I S0 ppb R
I j2 14.0
1800.3 Revision 0 12/13/77 3.1.A SECONDARY SERVICE CLOSED COOLING analysis freq.
limits desirable remarks b'
PH W
8.7-9.3 Cond. umho W
I Fe PPM W
I Corrosion Indication NH PPM W
I 3.1.B NUCLEAR SERVICE CLOSED COOLING PH W
8.7-9.0 Cond. umho W
I NH PPM W
I 24 Fe PPM W
I Corrosion Indication Dissolved i
I Cl-PPM W
<l.0 l
F-PPM W
<l.0 Gross pCi BG fit W
I 4
3 H
Ci MT W
I 3.1.C DECAY HEAT CLOSED COOLING PH W
8.7-9.0
~
~
T-j-
Cond. pmho W
I NH PPM W
I 24 Fe PPM W
I dj ~
~
4 Dissolved i
e*.
I Cl-PPM W
<l.0 F-PPM W
<l.0 15.0
1800.3 Revision 0 12/13/77 3.1.C DECAY HEAT CLOSED COOLING (cont'dj analysis freq.
limits desinble remarks Gross uCi BG M1 W
I i
"I 3
H Ml W
I 3.1.D INTERMEIDAlt CLOSED COOLING PH W
8.7-9.0 Cond umho W
I NH PPM W
I 24 Fe PPM W
I Cl-PPM W
I t
F-PPM W
I t
Gross pCi I
~T-W M
Bt3 3
H uCi HT-W I
[
3.1.E DIESEL COOLING PH Q
I Cond. umho Q
I I
Corrosion Inhibitor Q
I 3.1.F SERVICE BLDG. CHILLED WATER PH Q
I Cond. umho Q
I 4
Corrosioh
. f.
Inhibitor Q
I 1
4 Fe PPM Q
I 204 034 16.0
1800.3 Revision 0 12/13/77 3.1.G REACTOR BUILDIfiG EVAPORATIVE COOLER analysis freq.
limits desiraale remarks PH W
I i.
Cond. smho W
I Langelier Index M
-:0.5 This is an Index of Corrosion /Scalino-3.1.H CO.'4 TROL BUILDII;G CHILLED WATER PH Q
I Cond. pmho Q
I Corrosion Inhibitor 0
I Fe PPM Q
I
____.-e,--m e-m.----
e e-+
f e
~
e A'
~.f
~
1 i.
204 035 17.0
1800.3 Revision 0 12/13/77 4.1.A R.C. LETDOWN (Tavg > 250 F.l __ _ ____ _
analysis freq.
limits desirable remarks t.
PH 6/W 4.8-8.5
-4 Cond. umho 6/W I
Cl-PPM
<0.15
<C.1 F-PPM
<0.ib
<0.10
<0.005 NH PPM R
I 3 times Not Used During Power 24 D.O. Conc.
Operation.
CRUD PPM W
0-22G; More Often While Making Changes.
L PPM 6/W 0.5-2.0 j
Pb PP;1 W
<0.001 H
cc/Kg 3/W 15-40 2
Total Gas cc/Xg 3/W
<100 Gross BG pCi/g 3
H Ci/g W I
Gross a pCi/g M I
None Detectable E
2/y Total Activity
<100/E pCi/g Total Activity
~
t r
Gamma Scan D
t Dose Equivalent
<l.0 pCi/g Iodine 89 90 Sr Sr Ci/g M I
~
- AT LEAST ONCE EACH 72 HOURS.
p 204 036
1800.3 Revision 0 12/13/77 4.1.B DECAY HEAT (Tavg < 250 F) analysis freq.
limits desirabl e remarks i-PH b/W 4.8-8.5 Cond. umho 5/W I
Cl-PPM 5/W
<0.15 Tecg. Spec.AppliesWhenTAVG 225 F.
- F-PPM 5/W
<0.15 Tecg. Spec. Applies When TAVG 225 F.
I Tecg. Spec Applies When TAVG 225 F.
NH PPM 5/W I
If Used.
24 Baron PPM 5/W 0-2285 Pb PPM W
<0.001 fione Detectable 3
l H
Ci/g W
I t
Gross a pCi/g M
I I
89,,90 pCi/g M
I 37 5
Gross BG pCi/g Gamma Scan W
I E
2/y Total Activity
<100/E pCi/g Total Activity 19.0
1800.3 Revision 0 12/13/77 4 1.C PRESSUR~7ER WATER SPACE nalysis limits desi ra ble remarks PH W
4.8-8.5 Cond. umho W
I Cl-PPM W
<0.15 F-PPM W
I 4.1.D PRESSURIZER STEAM SPACE Gamma Scan R
I Can Show Need for Degassing Pressurizer.
Gaseous H.0,N R
I Can Give Warning of "Hard 2
2 2
Bubbl e. " - - - - - - - - - - - -
g 4.2.A PURIFICATION DEMIN. OUTLET Cl-PPM W
I Can Show Need for Resin Replacement.
F-
' PPM W
I Can Show Need for Resin Replacement.
f Li PPM W
I
^
I
~
Gross BG pCi/g W
I Can Show Need for Resin Replacement.
Gamma Scan R
I M-
_4'
. k.
20.0 204 038
~
1800.3 Rev Nion 0 12/13/77 4.2.B PURIFICATION DEMIN. INLET analysis freq.
limits desirable remarks Cl-PPM W
I Can Show Need for Resin 1-Replacement.
4 F-PPM W
I Can Show Need for Resin Replacement.
Li PPM W
I Gross BG pCi/g W
I Can Show Need for Resin Replacement.
Gramma Scan R
I 4.2.C MAKE_UP TANK LIQUID CRUD PPM W
<0.1 10 Liter Baron PPM W
<0.025 Indication of Oxygenated Make Up.
4.2.0 MAKE UP TANK GAS Gamma Scan W
I Can Indicate Need for Degassing R.C. System.
Gaseous s
H,&0 W
I Prevent Explosive Mixture 2
2 from Building.
i
~
4' i
(.
204 039 21.0
1800.3 Revision 0 12/13/77 4.2.E R.C. BLEED TANKS analysis freq.
limits desirable remarks PH W
4.8-8,5 4Y Cond. umho W
I Cl-PPM W
<0.15 F-PPM W
<0.15 CRUD PPM W
I Li PPM W
<0.1 Gross BG pCi/g W
I 3
H Ci/g W
I f
4_.2.F DEBORATING DEMINS.
I Detects Resin Exhaustion.
4.3.A B0 RATED WATER STORAGE TANK
~
PH '-
M 4.5-8,5 Cond. pmho M
I Cl-PPM M
<0.15 F-PPM M
<0.15,
Doron PPM W
>2270 Also After Each Makeup t
Turbidity M
Clear 3
H Ci/g M
I Gross BG pCi/g M
I Gamma Scan R
I 4-3 k
204 040 22.0
s 1800.3 Revision 0 12/13/77 4.3.B CORE FLOOD TANKS analysis freq.
limits desirable remarks PH M
I Cond. umho M
I
' 4 's s
D Cl-PPM M
<0.15 F-PPM M
>2270 Also Afte' Each Makeup Gross BG pCi/g M I
3 H
Ci/g M I
4.3.C S0DIUM HYDROXIDE TANK NaCH Q
Also After Each Makeup.
4.3.0 RECLAIMED BORIC ACID TANK Tech Spec. Boron Inventory Boron PPM W
Cl-PPM R
I Use for Makeup.
F-PPM R
I Use for Makeup.
Gross BG pCi/g R I
Use for Makeup.
t
_4.3.E BORIC ACID MIX TANK Boron PPM W
Tech. Spec. Boron Inventory.
4
_e
'I L\\
23.0
1800.3 Revision 0 12/13/77 4.3.F SPENT 70El. DEMIN. OUTLET analysis freq.
limits desirable remarks 1-PH M
4.5-8.5
'4 Cond. umho M
I Cl -
PPM M
<0.15 F-PPM M
<0.15 NH PFM R
When Used.
>2270 Li PPM R
I Gamma Scan M
I Gross BG pCi/g M
I 3
H Ci/g M
I Turbidity R
clear
.When Moving Fuel.
F 1
-.. =
i
~
8.'
.n t
204 042 24.
1800.3 Revision 0 12/13/77 5.1.A MISCELLANE0US WASTE HOLDUP TANK analysis freq.
limits desirable remarks PH W
I
-4 Cond. umho W
I Total Solids W
I Gross BG pCi/g W
I 5.1.B CONTAMINATED DRAIN TANK PH W
I Cond. umho W
I Gross BG pCi/g W
I Total Solids PPM W
I ~~
- '~~~~~~ ~
- ' ~ ~ ~ ~ - - - - ~ ~ - - - ~ ~ - ~ ~ - - ~ ' ~
~~
3 H
Ci/g W
I 5.1.E EVAPORATOR CONDENSATE TEST TANK 0
PH _
R I
6.0-9.0 Suitability for Reuse Indicate Resir Breakthrough.
Cond. umho R
I Suitability for Reuse Indicate Resir Breakthrough.
Cl-PPM R
I Suitability for Reuse Indicate Resi Breakthrough.
F PPM R
I Suitability for Reuse Indicate Resi Breakthrough.
<125 Gross BG pCi/g R
I 3
H Ci/g R
I LimitsasExpressedinSHPPy1621.
A Gamma Scan R
I T
l_imits as Expressed in SHP('1621.
204 043
~
25.0
1800.3 Revision 0 12/13/77 5.1.F R.C. EVAPORATOR FEED TANK analysis freq.
limits desirable remarks t
I Indicates Time to Dump to CWST.
Y' Gross BG pCi/g R I
5 1.G R.C. EVAPORATOR OUTLET Boron PPM R
I Indicates Evap. Efficiency.
Gross BG pCi/g R I
Indicates DF Across Evap.
5.1.H CLEANUP DEMINERALIZER OUTLET PH R
I Cond. umho R
I Cl-PPM R
I
<0.02 Out Indicator For Filter / Resin Replacement.
F-PPM R
I
<0.02 Out Indicator For Filter / Resin Replacement.
I Indicator For Filter / Resin Replacement.
Gross BG pCi/g R I
Indicator For Filter / Resin Replacement.
5.2.B VENT HEADER Gaseous H &O %
'W
<4% H To Avoid Explosive Mixture.
2 2 2
Gamma Scan R
I t-4,
.[.
e 204 044
=
26.0