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REGUL'A»TORY INFORMA»TION» D»ISTR»I BUT»IO SYSTEM» (RIDS)
DOCKE»T< 005%RZ2~0509052905090530
ACCESSIO»VI NBR ~ 8110300289 DOC ~ DA»TE1:'1/10'/28 NOTARIZED!: NO
FACIlr:STN 50 528 Pa»1 or Ve'rdei Nucl ear» Statiloni, Uhit» 1P Ar»izone Publ iSTN 50 529 Palo; Ve'rdeI Nucle'eri StationP Unit" 2'P Arizona PubliSTN"50', 530 Palo Vei der iVucl ebr< Statlioni Und t" 3P Ar lizone Publ i
AUTH!,NAMEI AUTHORr AFFIL»I'ATIION-VAN'RUV!T'EEI,E!~ Arizonei Publ i c; S'ervi c,et C'o,
RECIP' VAMEI RKCIIPZENTI AFFIL»IA!T'ION»TEDESCO»P R "B L!B" AssistantB Dir e'ctor» for» I.rlcehsing
SUB'JECIl"t: Forwards dr af t» FSAR" cl er»if i cathons'er fecil i ty sampling,par amet'ers" (T'ah»le 9.3 3) Pse'condary sys drain» sampling,(Se'ctioni 9;3~,2 2D3') EreVise'd» Pages 1 1.2!-20. through, 2?l 1 Page's»11,4 1 iI ff.4 2'.Ihfo will bel included» in FSAR'mehd."
O'ISTRXBUTEONi CODE»: BDDIS'OPIEB RECEEVED:.LITR''NCL» J"SIZE'!ITLEI::PSARr/FSAR AMDTS and Reil ated Cbr re'spondence
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4DZKDEMSTA.
Ãult&IICIKSIEPllt5lltl CKSKMEFP.o. BOX 21666 PHOENIX, ARIZONA85036
October 28, 1981ANPP-19292 — JMA/WFQ
Mr. R. L. TedescoAssistant Director for LicensingDivision of LicensingOffice of Nuclear Reactor RegulationU.S. Nuclear Regulatory CommissionWashington, D.C. 20555
~~)
p
g4( (')
Subject: Palo Verde Nuclear Generating Station(PVNGS) Units 1, 2 and 3Docket Nos. STN-50-528/529/530File: 81-056-026; G.1.10
Dear Mr. Tedesco:
Attached please find draft FSAR clarifications regarding PVNGS samplingparameters (Table 9.3-3), secondary systems drain sampling (Section9.3.2.2.3), revised pages 11.2-20 thru 22 and pages 11.4-1, 11.4-2.
This information is provided in response to telephone requests forclarification from the NRC's Effluent Treatment Systems Branch and willbe included in a future FSAR amendment.
Very truly yours,
EEVBJr/WFQ/avAttachment
cc: J. Kerrigan (w/a)P. Hourihan (w/a)A. C. Gehr (w/a)T. Chandrasekaran (w/a)
E. E. Van Brun Jr.APS Vice Presi ent,
Nuclear ProjectsANPP Project Director
p~c 1
(/i
8||0300289 8110&8 ~
PDR ADDCK 05000528 I
q A PDRy
~ ~
STATE OF ARIZONA )) ss.
COUNTY OF MARICOPA)
lf
I, John M. Allen, represent that I am Nuclear Engineering Manager ofArizona Public Service Company, that the foregoing document has been signedby me for Edwin E. Van Brunt, Jr., Vice President Nuclear Projects, onbehalf of Arizona Public Service Company with full authority so to do, thatI have read such document and know its contents, and that to the best of myknowledge and belief, the statements made therein are true.
hn M. Alle
Sworn to before me thisg9 day of 1981.
Notary Public
My Commission expires:
V~ ~
f"~ ~
J
'fj
Table 9.3-3SAMPZING SYSTEM DESIGN PARAMETERS (Sheet 2 of 13)
/
Sample OriginType ofSamplecooler
TypicalDiscrete Sample
Analysis(b)
PressurizedSample
Capability
'ontinuousOn LineAnalysisProvided
Mode of SampleRemoval and
Location
Nominal
Pressure(psig)
Tempera-ture ('F) Figure No. )7
Primar Sam linS stem Cont'd
'Pressurizer SurgeLine
Reactor Drain PumpDischarge BeforeFilter
Reactor Drain PumpDischarge AfterFilter
Rough
None
None
Boron
ConductivitypH, Cl Boron
ConductivitypI), Cl Boron
No
No
No
None
None
None
RemoteAux BldgE1-140'ocal
Aux BldgEl-120'ocal
'Aux Bldg
El-120'500
.
65
65
700
120
120
5. 1-19.3-2
9.3-13
9.3-13
Q C)
4) 4)Q II
00 ~
Pre-holdup IonExchanger Outlet
None
Holdup Tank Inlet None
Boric Acid Conden- Nonesate,Ion ExchangerInlet
ConductivitypH
.Conductivity .
pH, Boron, Cl
ConductivitypH, Boron
No
No
No
None
None
None
Local~ Aux BldgEl
120'ocal
Aux BldgEl-120'
k
LocalAux BldgEl-120'5
60
60
120
130
140
9.3-13
9.3»13
9.3-13
Boric Acid Conden-sate Ion ExchangerOutlet
None ConductivitypH, Boron
No None LocalAux BldgEl-120'0
140 9.3-13
Reactor Makeup Water NonePump Discharge
Reactor Makeup Water NonePump Recirculation.
ConductivitypH, Boron, Cl
ConductivitypH, Boron
No
No
None
None
LocalAux BldgEl-120'ocal
Aux BldgEl-120'30130
120
120
9.3-13
9.3-13
Boric Acid MakeupPump Recircula-tion
None Boron No None t,ocalAux BldgEl-120'30 120 9.3-13 M
M
SHAFT~ ~
Table 9.3-3SAMPLING. SYSTEM DESIGN PARAMETERS (Sheet 1 of 13)
C
Sample Origin
Type ofSampleCooler
TypicalDiscrete Sample
Analysis(b)
PressurizedSample
Capability
ContinuousOn LineAnalysisProvided
Node of SampleRemoval and
Location
Nominal
Pressure(psig)
Tempera-ture ('F) Figure No.
IoeI
o (.
Primar Sam lin~sstem
Hot Leg Loop 1
Pressuriier SteamSpace
Shutdown CoolingSuction Lines 1& 2
ESF A&B Train SafetyInjection PumpMini Flow Line
Purification FilterInlet
Purification FilterOutlet, IonExchanger Inlet
Purification IonExchanger Outlet
Rough
Rough
Rough
Rough
None
None
None
pH ~ 02'2'otalDissolved
Gas, NH3,Lithium, Boron,Cl , F , Radio-activity
82
Boron, Radio-activity
Boron, Radio-activity
pH, NH3,Lithium, Boron,Cl , F , Radio-activitySuspendedSolids
pH, Lithium,Boron Cl , F ,Radioactivity
Yes
Yes
No
No
No
No
No
None
None
None
None
None
Radio-activ-ity«)
None
RemoteAux Bldg
El-140'emote
Aux BldgE1-140
'emote
Aux BldgEl-140'emote
Aux Bldg
El-140'emote
Aux BldgEl
140'emote
Aux BldgEl-140 s
RemoteAux Bldg
E1-140'485
2500
435
2050
60
50
50
621
700
350
350
120
120
120
5.1-19.3-2
5.1-19.3-2
6.3-19.3-2
6.3-19.3-2/, ~
9.3-139.3 2
9.3-139.3-2
9.3-139.3 2
Q
M
a. Pressure value in PSIA.b. Radioactivity samples can be analyzed for gross activity, isotopic composition, tritium or alpha activity.c. Refer to section 11.5 for detailed descriptions of process and effluent radiation monitors.d. Refer to section 11.3 for a description of the explosive mixtures monitoring.
Table 9.3-3SAMPZING SYSTEM DESIGN PARAMETERS (Sheet 3 of 13)
r
Sample OriginType ofSampleCooler
TypicalDiscrete Sample
Analysis(b)
PressurizedSample
Capability
ContinuousOn LineAnalysisProvided
Node of SampleRemoval and
Location
Nominal
Pressure(psig)
Tempera-ture (4F) Figure No.
Ol ~
W 4lO I(m CO
Primar Sam linS stem Cont'd
Boric Acid MakeupPump Discharge
Boric Acid BatchingTank
Reactor Makeup Waterto Volume ControlTank
Volume Control TankDrain to RecycleDrain Header
CVCS Letdown
Shutdown CoolingHeat ExchangerOutlet
Safety injectionTanks 1,2,3,4
Secondar Sam lePo ill'ts
Hotwell 1A, 2A, 18,2B, lC, and 2C
None
Portable
None
None
None
Portable
None
Fine
Boron
Boron
conductivitypH, Boron Cl
ConductivitypH, Boron
Boron
Boron, Radio-activity
Conductivity,pH, Boron
YesCationConductivitySodium
No
No
No
No
No
No
No
No
None
None
None
None
YesBoron
None
None
YesCationConduc-tivitysodium
Local Aux BldgE1-120'ocal
Aux BldgEl
120'ocal
Aux Bldg
E1-120'ocal
Aux Bldg
El-120'emote
Aux BldgEl-120'ocal
Aux BldgE1-120'ocal
Containment
El-80'emote
HotwellAnalysis Sta-tion TurbineBldg El
100'30
130
50
50
650
610
2(a)
120
160
120
120
120
160
120
121
9.3-13
9.3-13
9.3-13
9.3-13
9.3-13
6.3-1
6.3-1
10.4-99.3-3
MLM
a(0n(090'-(0
Table 9.3-3SAMPLING SYSTEM DESIGN PARAMETERS (Sheet 4 of 13)
Sample Origin
Secondar Sam lePoints cont'
Type ofSampleCooler
TypicalDiscrete Sample
Analysis(b)
PressurizedSample
Capability
ContinuousOn LineAnalysisProvided
Mode of SampleRemoval and
Location
Nominal
Pressure(psig)
Tempera-ture (4F) Figure No.
S/G 1 and 2 HotlegBlowdown
S/G 1 and 2 ColdlegBlowdown
Rough &Fine .
Rough 6Fine
YesConductivitypH & Radio-activity
YesConductivitypH & Radio-activity
No Yes, Con-ductivitypH, Radio-activ-ity(c)Yes, Con-ductivitypH, Radio-activ-i,ty (c)
'emoteCold
Lab Aux Bldg
E1-140'emote
ColdIab Aux BldgEl-140'1791179
554
450
10.3-19.3-3
10.3-19.3-3
S/G 1 and 2Downcomer Blow-down
Condensate LP HeaterTrain A, B, and COutlet
FW Pump A and BSuction
HP Heater TrainA and B Outlet
Rough 6Fine
YesConductivitypH 6 Radio-activity
Portable YesConductivity
Portable YesConductivity
Portable YesConductivity
No
No
No
No
Yes, Con-ductivitypH &Radio-activ-ity(c)
\None
None
None
RemoteCold LabAux Bldg
E1-140'ocal
TurbineBldg,
El-140'ocal
TurbineBldg
El-140'ocal
TurbineBldg
E1-140'179
400
400
1225
554
396
396
450
10.3 19.3-3:
10.4-9
10.4-10
10.4-10
MSR A, B, C and DDrain
Portable YesConductivityIron, Copper
No None Local TurbineBldg El 140'02(') 383 10.2 2
First Stage RHTRDrain Tank A, B,C and D
Portable YesConductivityIron, Copper
No None Local TurbineBldg El-140'32(') 452 10.2 2
Second Stage RHTRDrain Tank A, B,C and D
Portable YesConductivityIron, Copper
No None Local TurbineBldg E1-140'85( ) 543 10.2 2
0
Table 9.3-3SAMPLING SYSTEM DESIGN PARAMETERS (Sheet 5 of 13)
Sample Origin
Type ofsamplecooler
TypicalDiscrete Sample
Analysis(>>
PressurizedSample
Capability
ContinuousOn LineAnalysisProvided
NominalNode of Sample
Removal and PressureLocation (psrg)
Tempera-ture (4F) Figure No.
IOe~ lAO)co O
Seconda Sam lePornts
Cont'tr
Drain Tank Aand B Drain
Htr Drain Pump Aand B Discharge
Spray Pond Water
Circulating WaterOutlets
Condensate TankSample
Portable
Portable
None
Fine
None
ConductivityIron, Copper
ConductivityIron, Copper
Hardness~ Alkalinity
pH, TDSConductivity
ConductivitypH, Chlorine
ConductivitypH, ChloridesFluorides,DissolvedSolids.Silica
No
No
No
No
No
None
None
YesConduc-tivity
YesConduc-tivity pHChlorine
None
Local TurbBldg El
100'ocal
Turb BldgEl
100'emote
YarYa Area
Remote ColdLab Aux Bldg140'is
Sta Tur-bine Bldg
100'ocal
Yard Area
433( )
202«)
15(a)
30
371
383
97
108
Ambient
10.2-2
10.2-2
9.2-1
10.4-49.3-3
9.2-8
U(8n(0
Essential chillerA and B Outlets
Essential coolingWater Pumps Aand B Discharge
None
None
Normal Chillers NoneA, B, and C OutletHeaders
pH,Chromate
pH,Chromate
pH,Chromate
No
No
No
None
Radio-activ-ity(c)None
Local ControlBldg El 74'5
Local Aux Bldg 45RoofEl 15'»
Local Aux Bldg 105El 70'9 9.2-11
9.2 4
9.2 10
M
M
0
Table 9.3-3SAMPLING SYSTEM DESIGN PARAMETERS (Sheet 6 of 13)
4
Sample Origin
Secondar Sam lePornts Cont'd
Type ofSampleCooler
TypicalDiscrete Sample
Analysis (b)
PressurizedSample
Capability
ContinuousOn LineAnalysisProvided
NominalMode of Sample
Removal and PressureLocation (psig)
Tempera-ture ('F) Figure No. f7
Nuclear CoolingHater PumpDischarge Header
None pH,Chromate
No Radio-actjv-ity(c)
Local Aux BldgEl-88'0 105 9.2-5
shutdown CoolingHeat ExchangerRoom A and BDrain
None pH Ho Hone Local Radwaste Atmos.Bldg El-88'20 9 '-7
LRS Hold-Up TankLeak Drain
None Radio-activity
No None Local LRSHold-up TankArea
El-100'tmos.120 9.3-7
LRS Recycle MonitorTank Leak Drain
None Radio-activity
No None Local LRSHold-up TankArea
El-100'tmos.120 9.3-7
Main Turbine LubeOil CentrifugeOutlet
None SuspendedSolids
No None Local TurbineBldg El-100'5 120
FWPT Lube OilCentrifuge Outlet
Cooling H20 Hold-upTank
None
Hone
SuspendedSolids
RadioactivitypH, Chromate
No
Hone
None
Local TurbineBldg
El-100'ocal
Aux BldgEl-40'0 75
52 120
9.3-10f7
I
C)I
Chemical wasteNeutralizer Tank(1 Sample Pointat Each Tank)
None
Condensate Polishing NoneDemineralizer(LO-TDS) Sump(2 Sample Points)
RadioactivitypH, Chromate
Radioactivity
No None
None
Local YardArea
E1-100'V088-V195)
Local YardArea
El-100'V028,
V031)
10
60
75
100
9.3-10
9.3-10
0O
Ul
M
0
l
Table 9.3-3SAMPLING SYSTEM DESIGN PARAMETERS (Sheet 7 of 13)
Sample Origin
Secondar Sam lePornts Cont'd
Type ofSampleCooler
TypicalDiscrete Sample
Analysis(b)
PressurizedSample
capability
ContinuousOn LineAnalysisProvided
Mode of SampleRemoval and
Location
Nominal
Pressure(psig)
Tempera-ture ('F) Figure No.
Condensate Polishing NoneDemineralizer(HI-TDS) Sump(2 Sample Points)
Radioactivity No None Local YardArea
El-100'V034,
V037)
60 100 9.3-10
O Qe
lV LOO II M
co MI
Retention Basin(Holdup Prior toEvaporation Pond)(2 Sample Points)
Spent RegenerationSump (WaterReclamationFacility)
TCW Heat ExchangerA and B Outlet
ESF Sump Pump Aand B Discharge
Non-ESF SumpDischarge
Blowdown Demineral-izer Effluent (1)
Blowdown Demineral-izer Effluent (2)
Blowdown Demineral-izer StrainerInfluent (1)
Blowdown Demineral-izer StrainerInfluent (2)
None
None
None
None
None
Rough
Rough
None
Hone
pH, ConductivitRadioactivity
pH
Chlorine
Chlorine
Chlorine
Na, Si, pH,ConductivityRadioactivity,
Na. Si, pHConductivityRadioactivity
Conductivity
conductivity
No
No
No
No
No
Yes
Yes
Yes
Yes
None
YespH
YesChlorine
None
None
Yes, Na,pH.Si,Con-ductivityYes, Na,Si,pH,Con-ductivityYesconduc-tivityYesConduc-tivity
South ofUnit 3
El-100'V089, V090)
water RecFacility
Remote YardArea
Local Aux Bldg
E1-40'ocal
Aux Bldg
El-40'emote
YardArea
Remote YardArea
Remote YardArea
Remote YardArea
Atmos
40
25
50
15
225
225
225
225
116
75
110
120
120
135
135
135
135
9.3-11
9.3-10
9.2-9
9.3-5
9.3-5
10.4-8
10.4-8
10.4 8
10.4 8
an(080
Table 9.3-3SAMPZING SYSTEM DESIGN PARAMETERS (Sheet. 8 of 13)
Sample Origin
Type ofSampleCooler
TypicalDiscrete Sample
Analysis (bI
Pressurizedsample
Capability
ContinuousOn LineAnalysisProvided
Mode of SampleRemoval and
Location
Nominal
Pressure(psig)
Tempera-ture (4F) Figure No.
Secondar Sam lin
rI
Ico LoI
Blowdown Demineral-izer Waste (HighTDS)
Blowdown Demineral-izer Waste (IowTDS)
Blowdown Demineral-izer Caustic DayTank Effluent
Blowdown Demineral-izer Acid Day TankEffluent
Diesel Fuel OilStorage Tank Aand B
Condenser Sump(North and South)Pump Discharges
Turbine BuildingSump
TCW Pump A and BDischarge
Auxiliary SteamCondensateReceiver Tank
Auxiliary Steam
None
None
None
None
None
Hone
None
None
Portable
Rough
ConductivityRadioactivity
ConductivityRadioactivity
Conductivity
Conductivity
Apjo,Viscosity,HVV, Sediment
pH,suspended
'olids,Radio-activitypH, SuspendedSolids, Radio-activitypH Chloride,ions
pH,Conductivity
pH,Conductivity
Yes
Yes
Yes
Yes
No
No
No
No
No
No
Yes .Conduc-tivityYesConduc-tivityYesConduc-tivityYesConduc-tivityNone
None
None
None
Radio-activ-ityIc)
None
Remote YardArea(V182, V204)
Remote YardArea(V172, V169)
Remote YardArea
RemoteYard Area
Local Outsideby D.G. BldgEl-100'ocal
TurbBldg
El-100'V075, V078)
Local TurbBldg
El-100'V076)
Local TurbBldg
E1-105'ocal
Turb.Bldg
El-100'ocal
YardArea
225
225
50
50
35
20
20
90
15
250
135
135
85
85
75
75
75
110
212
405
10.4-5
10.4-5
10.4-8
10.4-8
9> 5-7
9.3-11
- 9.3-11
9.2-9
13-M-ASP-001
AO-M-ASP-002
Table 9.3-3SAMPLING SYSTEM DESIGN PARAMETERS (Sheet: 9 of 13)
Sample OriginType ofSampleCooler
TypicalDiscrete Sample
Analysis(b)
PressurizedSample
Capability
ContinuousOn LineAnalysisProvided
Mode of SampleRemoval and
Location
Nominal
Pressure(psig)
Tempera-ture ('F) Figure No.
l7
IQSbJ 4)Q II
C0 +
Seconder Sam linPoints Cont d
Circulating WaterCooling Towers
Demineralized WaterSurge-Rinse Tank
Demineralized WaterStorage Tank
Fuel Pool Clean-upPump (1 & 2)Discharge (SpentFuel Pool orRefueling Pool)
Fuel Pool CleanupFilter 1 and 2Outlet (SpentFuel Pool orRefueling Pool)
Fuel Pool CleanupDemineralizer 12 Outlet (SpentFuel Pool orRefueling Pool)
Radwaste Sam linPoints
Evaporator Feed fromLRS Holdup Pumps
Chemical Drain PumpDischarge
None
None
None
None
None
None
None
None
Water Chemistry
Water Chemistry
pH, Chloride,ions, Fluorideions, Boric AcidHydrazine,Ammonia, Lithium
~ RadioactivityIConductivity,pH, Chlorideions, SuspendedSolids, Sodium,Radioactivity
Conductivity,pH, Chlorideions, SuspendedSolids, Sodium,Radioactivity
pH
pH,Conductivity
No
No
No
No
No
No
Yes
YesFoam
None
None
None
None
None
None
None
Local CoolingTower Area
Wtr TreatmentArea
Local YardArea
Local FuelBldg
El-100'ocal
Aux BldgEl-120s
Local Aux Bldg
E1-120'ocal
RadwasteBldg
El-100'ocal
RadwasteBldg
El-40'tmos.
20
288" H20
90
50
50
107 psia
88 psia
108
Ambient
Ambient
125
125
125
60 to120
60 to120
10.4 4
9.2-6
"9.2-6
9.1-9
~9'1-9t
9. 1-9
11.2-2
11.2-2
)6
M
WM
IC
Table 9.3-3SAMPLING SYSTEM DESIGN PARAMETERS (Sheet: 10 of 13)
Sample Origin
Radwaste Sam linPornts Cont'd
Type ofSampleCooler
TypicalDiscrete Sample
Analysis (b)
PressurizedSample
Capability
ContinuousOn tine 'Mode of SampleAnalysis Removal andProvided Location
Nominal
Pressure(psig)
Tempera-ture ('F) Figure No.
Hi-Lo TDS HoldupPump Recycle
None pH, Conduc-tivity BoricAcidConcentration
Yes None Local RadwasteBldg El 100'i-TDS
55 psiaLO-TDS42 psia
eo-120
11.2 2
Evaporator Concen-trate PumpsRecycle to VaporBody
Portable Boric Acid Con-centration, pH,,, Wtg "Solids
Yes None Local RadwasteBldg El-120'24 11.2-2
Ioem LOO II
CO Ol
Cas Sam lin S stem
Gas Surge Tank
Gas Decay Tank
None
Hone
Radioactivity,H2, 02
Radioactivity,H2, 02
No
Yes
H2,02 (d)
H2,02 (d)
Remote Rad-waste Bldg
El-140'emote
Rad-waste BldgEl-140'80380
200
200
11.3»29.3-2
1'1'.3-29.3-2
Cas Stripper None Radioactivity,H2, 02
Yes H2,02 (d) Remote Rad-waste BldgEl-140'00 120 11.3 2
9.3-2
Volume Control Tank
Equipment Drain Tank
Reactor Drain Tank
None.
None
None
Radioactivity,ity, H2'2
Radioactivity,H2, 02
Radioactivity,H2, 02
No
No
No
H2,02 (d)
H 0 (d)2'
H2,02 (d)
Remote Rad-waste Bldg
El-140'emote
Rad-waste Bldg
El-140'emote
Rad-waste BldgE1-140'0
120
120
120
9.3-139.3-2
9.3-139.3-2
11.3-29.3-2
Table 9.3-3SAMPLING SYSTEM DESIGN PARAMETERS (Sheet 11 of 13)
Sample Origin
Holdup Tank
Type ofSampleCooler
None
TypicalDiscrete Sample
Analysis(b)
Radioactivity,H2, 02
PressurizedSample
Capability
No
ContinuousOn I.ineAnalysisProvided
H2,02 (d)
Mode of SampleRemoval and
Location
Remote Rad-waste Bldg
El-140'ominalPressure
(psig)Tempera-ture ('F)
Atmos. 120
Figure No.
9.3-139.3-2 (7
ContainmentAtmosphere
Containment PurgeExhaust
None
None
Radioactivity
Radioactivity
No
No
Radio-activ-ity(c)
Radio-actjv-ity(c)
Local AuxBldg
100'evel
NE Quad
Iocal Aux.Bldg
140'evel
NE Quad
Atmos.
122
120
9. 4-13
9.4-13
oe) ~
o )M
co Ql
Plant Vent
ContainmentAtmosphere
Control BuildingOutside AirIntake
Post-AccidentSam Inn S stem
None
None
None
Radioactivity
Moisture(4 points)
RadioactivitySmoke, C12,2 points each
No
No
No
Radio-activ-ity(c)
YesMoisture(4 points)
Radio-activ-ity (c)Smoke, C12,2 pointseach
Local TurbBldg160'evel
Local 1 at'El-104'-6" NW
Quad; 1 atEl 124>-9NW Quad;2 laterRemote Con-trol Bldg,140'evel inOutside AirChase
Atmos. 120
122
Atmos. 113
9.4-13
9.4-12
9.4-1
Hot Leg Loop 1 Rough Isotopic, GrossGamma, pH, Oxy-gen, Hydrogen,Chloride, Boron
Yes Isotopic,GrossGamma, pH,Oxygen,Hydrogen,Chloride,Boron
Remote AuxBldg, Eleva-tions 140'nd70'yringeGrab Sample
2485 621 9.3-2A
MtM
Table 9.3-3SAMPZING SYSTEM DESIGN PARAMETERS (Sheet 12 of 13)
Sample OriginType ofSampleCooler
TypicalDiscrete Sample
Analysis (b)
PressurizedSample
Capability
ContinuousOn t.ineAnalysisProvided
Mode of SampleRemoval and
Location
Nominal
Pressure(psig)
Tempera-ture ('F) Figure No.
7
Post-AccidentSam lan S stem~CoC '
Hot I.eg Loop 2 Rough Isotopic. GrossGamma, pH, Oxy-gen, Hydrogen,Chloride, Boron
Yes Isotopic,GrossGamma, pH,Oxygen,Hydrogen,Chloride,Boron
Remote AuxBldg, Eleva-txons 140'nd70'yringeGrab Sample
2485 621 9.3-2A
ESF A&B SafetyInjection Sumps
ESF A&B SafetyInjection HiniFlow Line
ContainmentRadwaste.Sumps
Rough
Rough
Rough
Isotopic, GrossGamma, pH, Oxy-gen, Hydrogen,Chloride, Boron
Isotopic, GrossGamma, pH, Oxy-gen, Hydrogen.Chloride, Boron
Isotopic, GrossGamma, pH,- Oxy-gen, Hydrogen,Chloride, Boron
Yes
Yes
Yes
Isotopic,GrossGamma, pHOxygen,Hydrogen,Chloride,Boron
Isotopic,GrossGamma, pH,Oxygen,Hydrogen,Chloride,Boron
Isotopic,GrossGamma, pH,Oxygen,Hydrogen,Chloride,Boron
Remote AuxBldg, Eleva-tions 140'nd70'yringeGrab Sample—
Remote AuxBldg, Eleva-tions 140'nd70'yringeGrab Sample
Remote AuxBldg, Eleva-tions 140'nd70'yringeGrab Sample
60
2050
60
350
350
120
9.3-2A
r.~9.3 2A
9.3-2A
0AMN
CM
M
MW
Table 9.3-3SAMPE ING SYSTEM DESIGN PARAMETERS (Sheet 13.of 13)
Sample Origin
Post-Accident~sx s st.cont
Type ofSampleCooler
TypicalDiscrete Sample
"Analysis(>>
PressurizedSample
capability
ContinuousOn LineAnalysisProvided
Node of SampleRemoval and
Location
Nominal
Pressure(psig)
Tempera-ture ('F) Figure No.
O ~
bD
I
Auxiliary BuildingSumps
Containment Air
Rough
Rough
Isotopic, GrossGamma, pH, Oxy-gen, Hydrogen,Chloride, Boron
Isotopic, GrossGamma, Oxygen(Hydrogenprovided byContainmentHydrogen ControlSystem)
Yes
Yes
Isotopic,GrossGamma, pH,Oxygen,Hydrogen.Chloride,Boron
Isotopic,GrossGamma,Oxygen(Hydrogenprovidedby Con-tainmentHydrogencontrolSystem)
Remote AuxBldg, Eleva-tions 140'nd70'yringeGrab Sample
Remote AuxBldg, Eleva-tions 140'nd70'yringeGrab Sample
50
60
120
350
9.3-2A
9.3 2A
0nW
PVNGS FSAR
9.3.2.2.2 Post-AccidentPROCESS AUXILIARIES
Liquid samples are taken from both RCS hot legs, containmentsumps, auxiliary building sumps and the ESF A6B mini-flow line.All samples are routed to a liquid;input header. After sampleselection, isotopic analysis is performed. The sample is thendepressurized and cooled to allow chemical analyses to beperformed. At this point a syringe grab sample can be taken;or the sample can be discharged to the RDT or EDT. Uponcompletion of the analysis, the source is isolated, and thesystem is then purged with demineralized water, then nitrogengas.
Gas samples are taken from containment air via the containmenthydrogen control system. Samples are routed to a gas inputheader. Isotopic analysis is performed then the sample isdepressurized and cooled to STP conditions in order to perform02 analysis. A syringe grab sample can be taken or the sampleis returned to the containment. The. normal hot lab countingroom at the 140-foot elevation in the auxiliary building isshielded to provide low background post accident. The countingchamber can be purged with instrument air or bottled gas. When
the analysis is complete, the source is isolated, and the systemis purged with nitrogen gas.
Liquid samples will provide information on isotopic content,gross gamma, pH, chloride concentration, dissolved oxygen,dissolved hydrogen and boron. Gas samples will provideinformation on isotopic content, gross gamma, gaseous
oxygen,'nd
hydrogen (from hydrogen monitor of the containment hydrogencontrol system).
9.3.2.2.3 Secondary Systems Drain Sampling
There are eight sumps in or near Turbine Building Structureswith potential for transferring radioactivity to flow pathsleading to the retention basins/evaporation ponds. There are
Amendment 7 9. 3-31A10-20-81
December 1981
1
PVNGS FSAR
PROCESS AUXILIARIES
three drainage sumps in the turbine building: the north sump,the south sump, and the turbine, building sump. Each sump hasan analysis point on its discharge piping and can transferfluids to the liquid radwaste system (LRS), either of twochemical waste neutralizing tanks (CWNT), or to an oil/waterseparator. Each CWNT has separate analysis points,and can besampled prior to discharge. Each CWNT can discharge- to theLRS or the retention basins. The oil/water separator dis-charges to its sump (sump four), which in turn discharges to.the retention basins.
There is not a very great potential of introducing significantradioactivity to these sumps, and it, is not likely that thesumps would be aligned to „discharge radioactivity to theretention basins. The following are the sources to thesesumps:
North Sum
Battery room neutralizing pit (nonradioactive)Floor drains (equipment leakage and cleaning liquids)Feedwater heaters
Heater drain tank and pump
Instrument air compressor drains (nonradioactive)Air dryer/prefilter drains (nonradioactive)Blowdown flash tank liquid drainTurbine cooling water heat exchanger drain(nonradioactive)
Turbine cooling water surge tank drain(nonradioactive)
Heater blowdown stack
Condensate storage tank
December 1981 9.3-31B10-20-81
Amendment 7 4
PVNGS FSAR
PROCESS AUXILIARIES
Condenser drains
Generator stator cooler drain (nonradioactive)
'V
Floor drains (equipment leakage and cleaning liquids)Low pressure heaters and condenser drainsCondenser evacuation drainSteam seal exhauster drainIsophase bus cooler drain (nonradioactive)
H2 seal oil cooler (nonradioactive)Condensate pump drainage
Turbine Buildin Sum
Feedwater pump lube oil reservoir drains(nonradioactive)
Feedwater pump drainTurbine lube oil drains (nonradioactive)
Oil ater Se arator Sum
North, South, and turbine building sumps.
Control bu"'lding sumps (nonradioactive)The only sources noted above that could contain any radioactiv-ity are secondary system component sources — condensate orblowdown. No regenerant chemicals are present. Thus, anyradioactivity which is present must be at least as dilute asthe secondary system.
The activity level in the secondary is monitored at two points.Steam generator blowdown monitors 13-J-SQN-RU-4 and RU-5 willdetect abnormal activity in the secondary as it is diverted tothe blowdown processing equipment. The condenser gland sealexhauster monitors 13-J-SQN-RU-141 and RU-142 (low and highrange) will detect abnormal activity in the condenser.
7l .Amendment 7 9.3-31C,10-20-81
December 1981
PVNGS FSAR
PROCESS AUXILIARIES
If abnormal activity levels are present, sump transfer pathswill be aligned to transfer to.the LRS or the CWNT's with sub-sequent alignment to the LRS. However, if it is determinedduring operating (by sampling or monitoring) that the sumps do
'
not contain significant radioactivity, they may be realignedto discharge to the CWNT's (aligned to the retention basins)or the oil water separator and thence to the retention basins.
The remaining four sumps are the high and low total dissolvedsolids (TDS sumps that receive regenerant wastes from the con-densate polishing demineralizers or the blowdown demineralizers,respectively each sump has local drains that will be used forgrab sampling. For either processing stream, initial regener-ant eluent is fed to the resin and subsequently directed tothe high TDS sumps. These discharge to the CWNT's. As notedpreviously, the CWNT's,can discharge to the LRS or retentionbasins and are sampled prior to discharge. Only after the TDS
level of the regenerant has drops (associated with activitylevels), as measured by on-line conductivity cells, would flowbe directed to the low TDS sumps, or the circulating watersystem (and thence to the evaporation ponds via blowdown).Thus, the systems are designed to send radioactive waste tothe LRS and yet recover clean liquid for recycle to thegreatest extent practical.To ensure that abnormal levels of activity are not sent toclean systems, design provisions for sampling are beingclarified. FSAR Table 9.3-3 is being revised to show thesampling capabilities at these sumps. Operationally, when
significant activity is present in the secondary (as detectedby the steam generator blowdown or condenser gland sealexhaust monitors) the low TDS sumps will be aligned to dis-charge to the high TDS sumps. A grab sample analysis forradioactivity will be required prior to changing this alignment,to allow discharge to the circulating water.
December 1981 9.3-31D10-20-81
Amendment 7 7
PVNGS FSAR
PROCESS AUXILIARIES
In summary, the secondary systems are continuously monitoredfor activity. If abnormal activity is present, this will leadto alignment of leakage and cleanup stream discharge to theLRS. If after grab sampling, no abnormal activity is presentin,effluents they can be directed to the circulating wateror retention basins.
9.3.2.2.4 Retention Basin Sampling
The divided retention basin is located south of the Unit 3
spray ponds. It has a one million gallon capacity and isdivided into identical compartments. The compartments havesloping sides and are approximately 172' 98't top and121' 47't. bottom. Nominal depth is 6-1/2 feet with2 feet freeboard; The top of the dikes are 4-1/2 feet abovegrade to provide flood protection.The basins act as storage in the event the effluent is notwithin the standards for pH, conductivity, and radioactivityprior to discharge to the evaporation pond. One retentionbasin can store the normal waste effluent of 800 gal/min fora 10-hour period. The offline basin is monitored, chemicallytreated (if necessary) and discharged to the evaporation pond.
Sampling can be conducted directly by dip grab sampling or bysampling retention basin sump discharge (Figure 9.3-11,valves V089 or V090).
If a portable ion exchanger is used to purify the retentionbasin, expended resins will be disp'osed of in one of two ways.If resins are radioactive, they will be transferred by truckor drum to the solid radwaste system of either Unit 1, 2, or 3.If resins are not radioactive but do not meet chemistrylimits (excess chromate or other ions), resins will be hauledto a licensed disposal site. Regeneration is not currentlycontemplated due to the low frequency projected for thisoperation.
Amendment 7'.3-31E10-20-81
December 1981
PVNGS FSAR
LIQUID WASTE MANAGEMENT SYSTEMS
Table 11.2-7FPCCS EXPECTED PROCESS POINT ACTIVITIES (pCi/g) (Sheet 3 of 3)
RadionuclideSpent
Fuel PoolRefueling
Pool
Fuel PoolIX No. 1Outlet(
Fuel PoolIX No. 2Outlet (a)
CE-144PR-143PR-144NP-239CR-51
MN-54
FE-55FE-59CO-58
CO-60
See table11.1-5 11.1-5 1.7E«7
S.SE-S1.5E-62.2E-7
8.8E-94.8E-90.06.9E-81.6E-7
See table 3.3E-S
1.2E-105.0E-110.02.1E-101.9E-91.9E-92.3E-91.1E-91.9E-S3.0E-9
~ 7
through the LRS than necessary, non-radioactive turbine build-ing drains are processed by the chemical waste system. Besidesthe low TDS tank, an additional holdup tank is provided toaccommodate overflow from either the low TDS or the high TDS
holdup tank and is normally isolated from the supply headers.If necessary, this tank can be used to collect either low TDS
or high TDS liquid waste. An internal mixing header uniformlymixes the contents of each holdup tank prior to and duringprocessing. Acidic or caustic agents may be added for pH
control, and anti-foaming agents may be added if surfactantsexist in the tank contents. Decontamination facility wastesfrom Unit 1 only (including laundry liquid waste) and radio-chemistry laboratory wastes are collected in the chemicaldrain tanks prior to processing. Refer to section 12.5.2for further details on laundry system wastes.
Amendment 7 11.2-2010-,20-81 December 1981
1~
PVNGS FSAR
LIQUID WASTE MANAGEMENT SYSTEMS
Table 11.2-8WASTE INPUTS TO THE LRS (Sheet 1 of 2)
LRS Inputs
Hi h TDS HolduTanks
Containment sump
Auxiliary build-ing floor drains
Condensatepolisherregenerants
Blowdowndemineralizerregenerants
Chemical draintank (includeslaundry inputs)
Laboratory drains
Miscellaneoussources
ExpectedFlow
(gal/d-unit)
40
200
12,000 gal/15 days
115
400
700
DesignFlow
(gal/d-unit)
40
200
20,000
12,000 gal/15 days
400
700
Activity
1 PCA(
0.1 PCA
100% ofregenerantwasteactzvxty
100% ofregenerantwasteactivitySee chemicaldrain tankinputs
0.002 PCA
0.01 PCA
Total 2,255 22,255
Low TDS HolduTank
Turbine buildingfloor drains
Secondary system
samples
7,200
300
, 7,200
300
100% of main,steamactivity
„„100% of main,'steam.activity
a. PCA = Primary Coolant Activity.
December 1981 11.2-2110-20-81 Amendment 7
PVNGS FSAR
LIQUID WASTE MANAGEMENT SYSTEMS
Table 11.2-8WASTE INPUTS TO THE LRS (Sheet 2 of 2)
4
LRS Inputs
Low TDS HolduTank (cont.)
Condensatepolisherregenerants
Expected DesignFlow ,. Flow
(gal/d-unit) (gal/d-unit)
36,000
Activity
100% ofregenerantwasteactivity
Blowdowndemineralizerregenerants
12,000 gal/15 days
12,000 gal/15 days
100% ofregenerantwasteactivity
Total 8,300 44,300
Chemical DrainTanks
Decon stationwaste plusshowers (includeslaundry waste)
Primary systemsamples
100
15
100 SeeNUREG 0017,Table 2-20
1 PCA
Total 115 115
Amendment 711.2-2210-20-81 December 1981
w
PVNGS FSAR
11.4 SOLID WASTE MANAGEMENT. SYSTEM
Solid waste management is provided by the .solid radwaste system(SRS) which is designed to provide'oldup, solidification, andpackaging of radioactive wastes generated by plant operation,and to store these wastes until they are shipped offsite forburial. The system is located in the radwaste building, whichis designed to withstand an operating basis earthquake.
11.4.1 DESIGN BASES
The design bases of the solid waste management system are:
A. The SRS provides the capability for solidifying andpackaging concentrated'waste solutions from themiscellaneous waste evaporator, spent resins from .
radioactive ion exchangers, and chemical drain tankwastes.
B. The SRS provides a means for packaging and disposal ofspent radioactive cartridge filters and solid wastesfrom the LRS, CVCS, and laundry (unit 1 only).
C. The SRS provides a means of compacting and packagingmiscellaneous dry radioactive materials, such as paper,rags, contaminated clothing, gloves, and shoe coverings,and a means for packaging contaminated metallic mater-ials and incompressible solid objects, such as smalltools and equipment parts.
D. The SRS provides an alternate method of disposal of theliquid and crud from the backflushable filter crud tank.
, Note that the crud is normally removed by a disposablefilter and the liquid is normally processed by thechemical and volume control system discussed insection 9.3.4.
December 1981 11.4-1,10-20-81
Amendment 7
e
I
c
PVNGS FSAR
SOLID WASTE, MANAGEMENT SYSTEM
E. The SRS provides a method of solidifying and packagingblowdown demineralizer "resin and condensate polishingresin in the event that they become contaminated.
The maximum and expected input volumes to the SRS from each'
source of solid waste material are presented in table 11.4-1.The SRS input activities associated with the expected inputvolumes are presented in table 11.4-2.
Codes and standards applicable to 0he solid radwaste system arelisted in table 3.2™1.
Collection, solidification, packaging, and storage of radio-active wastes will be performed so as to maintain any potentialradiation exposure to plant personnel to "as low as is reason-ably achievable" (ALARA) levels, consistent with the recommen-dations of Regulatory Guide 8.8 and within the dose limits of10CFR20. Some of the design features incorporated to maintainALARA criteria include remote system operation, remotely actu-ated flushing, quick disconnect, equipment layout permittingthe shielding of components containing radioactive materials,and use of shielded casks for in-plant movement of high activitywaste. Additional ALARA provisions of the SRS are described insection 12.1.
Packaging and transport of radioactive wastes will be in con-formance with 10CFR71. Packaged wastes will be shipped in con-formance with 49CFR170-178. Collection, solidification, packag-ing, and storage of radioactive wastes will be performed inconformance with 10CFR50.
Laundry is cleaned by a dry-cleaning system. Solid wastes aremanually transfered to the SRS for packaging. Refer tosection 12.5.2.
Amendment 7 11.4-210-20-81
December 1981
I 0