ML17079A037
| ML17079A037 | |
| Person / Time | |
|---|---|
| Site: | Callaway  |
| Issue date: | 03/20/2017 |
| From: | Klos L Plant Licensing Branch IV |
| To: | Diya F Union Electric Co |
| Klos L | |
| References | |
| Download: ML17079A037 (26) | |
Text
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- H:~~~~:( 1--lf--.-r---1 A tOitW) 000.000 GALLONS}
0* I L..,_~--.---4:-~ h_AUNOR'f ANO HJT SHJWER lHSJ 0M(NEAALt7~ I WATER STJR~GE I TAIIK (AN) f--..-- ISV * .)JJ GALLVNSJ O~SCHARGE\ MOMTOA TANK B , 1100,000 ' GALLONS I I I l&HS L&HS I I Tank A Filter Tank B Filter I I I I
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- ~~~~(IUf{~M)-...\!!WJ.!__ _ _ _ _ _ _ _ --t--t--=.L---t __ "'T_l....-_t r-........, CONOENSATE I I StORAGE rAIII<.
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- ---------~-
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___ I IJQRON THERMAl REG£NRATION 1-------i S'T'S fW lSGI I HISTORICAL I I I I CALLAWAY PLANT l--------- 0----.--r '--~--1 FIGURE 11.1A-1 I
;~;~:::!;;cr!u _J:'---+G'\~;~H----<<h~!!~~~~**u t-(1 (Ow) \J.Y LIQUID WASTE TREATMENT SYSTEMS BLOCK DIAGRAM
(7.5 gpm) Divert to Boron Re cycle System (1, 840 gpd@ 1.0 PCA)
~ 2 ~
,.. Ve nt to letdown I Ga seous Radwaste System Return to (75 gpm @ 1.0 PCA) 1 3 4 Reactor Coolant System DECONTAMINATION FACTORS Cesium & Other Iodine Rubidium Nuclides
- 1. Mixed Bed Demineralizers 10 2 10
- 2. Cation Bed Demineralizer 1 10 10
- 3. Reactor Coolant Filter 1 1 1
- 4. Volume Control Tank (a)
System DF 10 20 102 (a) For noble gases, a value of 0.25 is built into the GALE code for they parameter for the case of continuous VCT purging. Chemical and Volume Control System CALLAWAY PLANT Figure 11.1A-2 (Sheet 1) System Decontamination Factors HISTORICAL
Plant Discharge R. C. Dr Tank (300 gpd@ 1.0 PCA) Vent to Gaseous Radwaste .* J u ........ Via Liquid Radwaste System (Equipment Drains) .-* Letdown ,.. 1 2 3 4 5 6 ~ (1,840 gpd- shim bleed) 1
*------------* I DECONTAMINATION FACTORS Cesium & Other Iodine Rubidium Nuclides
- 1. Recycle Evaporator Demineralizer (a) 10 2 10
- 2. Recycle Evaporator Feed Filter 1 1 1
- 3. Recycle Holdup Tank
- 4. Recycle Evaporator 102 103 1Q3
- 5. Recycle Evaporator Condensate Demineralizer (b)
Anion Bed 10 2 1 1 Mixed Bed 10 10 10
- 6. Recycle Evaporator Condensate Filter 1 1 1 System OF (with anion bed in item 5) 105 2 X 103 104 (with mixed bed in item 6) 104 2 X 104 105 Decay Time Boron Recycle Holdup Tank #2, Collection Time Recycle Process Time Boron Recycle System T = 0.8 x 56 000 = 20 _9 days T = 0.8 x 56,000 = 2 days CALLAWAY PLANT c 2,140 p 21.600 Figure 11.1A-2 (Sheet 2)
- a. Mixed Bed
- b. Anion Bed or Mixed Bed Optional. See System Decontamination Factors Chapter 11.0 of Each Site Addendum.
HISTORICAL
1.11~ Plant Discharge
~=:t:s (400 gpd @ 0.5 PCA) 1111!. . . . l
--tL--1___.l-----tL..-2__.1---IL..-3---'I-----t..._4__.1--....L.._5___.t--..... 6 I~
- Reactor Makeup Water Tank (400 gpd)
DECONTAMINATION FACTORS Cesium & Other Iodine Rubidium Nuclides
- 1. Waste Holdup Tank
- 2. Waste Evaporator Feed Filter
- 3. Waste Evaporator
- 4. Liquid Waste Charcoal Adsorber 1 1 1
- 5. Waste Evaporator Condensate Demineralizer 10 10 10
- 6. Waste Evaporator Condensate Filter 1 1 1 System DF 104 Decay Time Waste Holdup Tank #1 Waste Process Collection Time Time Liquid Radwaste
_ 0.4 10,000 _ Train "A"- Clear Waste T c-X
- 10 days T = 0.4 X 10,000 = O 185 da 400 p 21 600 . y CALLAWAY PLANT Figure 11.1 A-2 (Sheet 3)
System Decontamination Factors HISTORICAL
,... 3 4 ~
Discharge Dirty Waste (1, 140 gpd
@ 0.058 PCA) -- 1 2 5 6 7 8 - Reactor Makeup Water System DECONTAMINATION FACTORS Cesium & Other Rubidium Nuclides
- 1. Floor Drain Tank
- 2. Floor Drain Tank Filter 1 1 1
- 3. Waste Monitor Tank Demineralizer (a)
- 4. Waste Monitor Tank Filter (a)
- 5. Waste Evaporator (b)
- 6. Liquid Waste Charcoal Adsorber 1 1 1
- 7. Waste Evaporator Condensate Demineralizer 10 10 10
- 8. Waste Evaporator Condensate Filter 1 1 1 System OF (c)
Decay Times Liquid Radwaste Train "B" - Dirty Waste Floor Drain Tank#2, Waste Processing Time Collection Time CALLAWAY PLANT
= 0.8 x 10,000 = 7 da s Figure 11.1 A-2 T T = 0.8 x 10,000 0 _37 day (Sheet 4) c 1,140 y p 21,600 a) Used only when influent activity< 1o-5.,u Ci/cc System Decontamination Factors b) Used when influent activity~ 10-~Ci/cc c) Assumes evaporator path HISTORICAL
CALLAWAY - SP Figure ll.lA-2 Sheet 5 is deleted. HISTORICAL
Ventto#5 Feedwater Heater 25% flash Steam Generator Recycled to Blowdown --.. 1 2 3 4 5 . Secondary Cycle Max. 4.2 X 106 lb/d ay Min. 0.7 x 106 lb/day DECONTAMINATION FACTORS Cesium & Other Iodine Rubidium Nuclides
- 1. Steam Generator Blowdown Flashtank
- 2. Steam Generator Blowdown Regenerative Heat Exchanger
- 3. S.G. Blowdown Nonregenerative Heat Exchanger
- 4. S.G. Blowdown Filters 1 1 1
- 5. S.G. Blowdown Demineralizers 102(10) 10(10) 102(10)
System OF 103 102 103 Steam Generator Blowdown CALLAWAY PLANT Figure 11.1 A-2 (Sheet 6) System Decontamination Factors HISTORICAL
low TDS 1 2 (12,857 gpd) 1-..... Secondary Cycle High TDS (4.286 gpd) 3 7 9
-...... 10
....... Discharge Monitor Tanks Secondary Ski~ Floo' Drams (7,200 gpd) 1 4 ~~~----**--------------------~*~ Dh~u~M~~r n.___:j Tanks DECONTAMINATION FACTORS Cesium & Other Iodine Rubidium Nuclides
- 1. Low TDS Collector Tank
- 2. Low TDS Filter 1 1
- 3. High TDS Collector Tank
- 4. Oil Interceptor
- 5. SLW Drain Collector Tank
- 6. SLW Filter 1 1
- 7. SLW Evaporator (available only for high TDS) 103 104
- 8. SLW Charcoal Adsorber
- 9. SLW Demineralizer (C)* 10{102 ) 10(2)
- 10. SLW Monitor Tank (Low TDS)
System OF* High TDS 10 4 105 Low TDS 102 2 Secondary Liquid Waste System (a) Processing will be subject to chemistry requirements. CALLAWAY PLANT (b) No credit is taken for collection and processing times. (c) Second number indicates Low TDS DF. Figure 11.1 A*2 (Sheet 7) System Decontamination Factors HISTORICAL
UNIT VtNT AUX. BLDG. DRAIN TANK TOP OF CONTAINMENT EL. 2:200'-0" AUX. BLDG. SUMP
*I I
PRIMARY SAMPLING lAUNDRY & HOT SHOWER TANK I REACTOR COOlANT IHOTI REACTOR BUILDING
@1
~ AUXILIARY BUILDING I I L-@@@~
RADIOACTIVE LIO. LEAKAGE IHOTI CONDENSER AIR REMOVAL SYSTEM FUEL STEAM PACKING EXHAUSTER BUILDING SECONDARY LEAKAGE TURBINE BUILDING TURBINE BLDG. VENTilATION FUEL BLDG. DRAIN TliNK El. 2137'-0" RADWASTE BLDG. DMIN TANK iTYP. OF 101 WASTE HOlD-UP TANK - -~M~a~k::e:_-u~p~A~ir_ _ __,-.JH""G;;;;;:dr;;o~;;;;l Laundry Dryers 1--+----~ Laundry Dryer Exhaust P Hr----------.. WASTE EVAPORATOR !'KG. Laundry Decon FLOOR DRAIN TANK Facility VENT COLLECTION HEADER WASTE MONITOR TANK CHEMICAL DRAIN TANK NON PRIMARY SAMPLING SYS. WASTE GIIS SYSTEM LEAKAGE RAOWASTE BlDG. VENT EL. 20'55'*6" SPENT RESIN STORAGE TANKS RADWASTE BUILDING RADIOACTIVE UO. LEAKAGE !HOT) BLOWOOWN SURGE TANK EVAPORATOR BOTIOMS TANKS LEGEND r;;'1 PRE FILTER OR L:.J ROUGHING FILTER CALLAWAY PLANT ED HEPA FILTEA
@] CHJ>RCOAL ADSORBER FIGURE 11.1A-3 01\SHEO LINES FOR INTERMITIENT SOURCES POTENTIAL GASEOUS RELEASE HISTORICAL
8 7 6 5 4 3 2 1 ( 0) ~08HZZ-~
,-----------------l~ I~ i _____________ j41~21 NOTES:
I. THE FOLLOWING WESTINGHOUSE STANDARD EQUIPMENT IS SUPPLIED
~--8 <?- t---~ <?- TO A HIGHER QUALITY GROUP/SEISMIC CLASSIFICATION AND 021 PRINCIPAL CONSTRUCTION CODE THAN IS REQUIRED BASED ON 1 I J CIS-A
-, CLOSES I ~ I -(' CCLIOSs-ts WASTE HOLDUP TANK ITS SAFETY RELATED IMPORTANCE AS DICTATED BY SERVICE AND FUNCTIONAL REQUIREMENTS AND BY THE CONSEQUENCE OF THEIR R.C. PUMP "A" ~ I HBB HBD r--~~r-------------~~M~2~2~H~B0~2~
SEALS FAILURE. EQUIPMENT CLASSIFICATION SHOWN IS FOR INTERFACE
~HBB (~6 (~0 , PURPOSES ONLY I I.e. WELD END PREPS I. ACTUAL CLASSIFICATION H ) M 22BB03A DOl HCD 1" I HBO \1 s I INDTE 14)
\1 s 7 ~13~ IH-Bl OF THE EQUIPMENT IS THE LOWER CLASSIFICATION AS INDICATED FOR THE ASSOCIATED PIPING. H
,---\~NOTE 22 0
~VLh-5"-;;, ~VLf-7:;:<-;;,
IE 5 l u 2"x 1" II AS II AS T FUEL POOL A. WASTE HOLDUP TANK B. WASTE EVAP FEED PUMP R.C. PUMP "B m0 ~--,-_J~~S£~~--~C:LE~A~N~-~U~P~F~IL~TtE)RS II 020 HCD 3"
~ F.o~ :::, ~ F.o'\
l /~ C. WASTE EVAP FEED FILTER SEALS D02HCD1" I Cs\ I,- zs M 22EC02 D. REACTOR COOLANT DRAIN TANK HEAT
) M 22BB03B ~:~ 44 7150r-~~~J 1{1s.s) 020
~--.....~**. .- - - - _j EXCHANGER !SHELL SIDEl
~15~1 7126 P / WASTE GAS 1"1Dl ID 6l E. FL DRAIN TANK FILTER IE 5 l INSIDE LouTS IDE / ./ Q COMPRESSOR V382 r- -:t F. WASTE EVAP CONDENSATE DEMINERALIZER r \_--r---~~M~2~2H~A~O~I~
1 - r--t><~----~~~~~~~~~Of2~5~H~B~B~3~/4!:"-G~~--~0~2~6~HB~D~3~/~4~"-r--{~
~
G. WASTE MONITOR TANK DEMINERALIZER R.C. PUMP SEALS "c" 003 HCD 1 II I 1058 115
- h. rx F. C. VOI8(1 ,ir
~voif 'o 8' P I PE TUNNEL L _j RECYCLE HOLDUP TANK H.
I. WASTE MONITOR TANK FILTER LAUNDRY AND HOT SHOWER TANK FILTER
) M 22BB03C ~
I 016 HCD 3" 2. PORTIONS OF THIS SYSTEM THAT CONTAIN RADIOACTIVE FLUIDS
--l lr M 22HEOI IE -5 l 115 ~y 0
m I I ~ 1---l...f---J TEST 3~'t," l"x3/4.{ ""' ~ 029-HBD-3/4" 030-HBD-3/4" ~
'~
I IA 8 l AND ARE IDENTIFIED BY QUALITY CLASSIFICATION "D" SHALL MEET THE AUGMENTING REQUIREMENTS.
~
C 0 R.C. PUMP 11 0 11 1058 u INOTE 15l 3. THIS DRAWINGS BASED ON WESTINGHOUSE DRAWINGS 1145E06.
~t-8 ~VOl ~017 SEALS 0 L..:.J n
I II 5
) M 22BB03D 004 HCD 1 II CONN.
m I TEST \ ~£~~~~{ o~i8K & 7 vo26 <0 I NUCLEAR SAMPLING 1145E07, SHEETS I ,2 AND 3. IE -5 l 'N L..:.J 3;{ CONN.
~\ CONNECT I~ ~ 0 018 HCD 3/4" ~!!_B..!.ti-9-j M-ZZSJ0 3
~-'S'-"YC'S_,T-cE,.,M~
- 4. MAKE CONNECTIONS TO SIDE OR BOTTOM OF TANK.
- 5. SPOOL PIECE NORMALLY REMOVED. TO BE INSTALLED ONLY AFTER I 227-HCD-3/4" L----L}"~-L~ LOCAL SAMPLE ~~~~~r---~
0 u T.C.
~ - I H-7l DEPRESSURIZATION FOR DRAINING.
~~4 I
I 023-HCD-3/4" V022 0 I 7147 6. VENT LINES TO EXTEND WITHIN 12 INCHES OF FLOOR. G (Pi\ --,--- 1 m ,- 021-HCD-2" C ::;-- m PC 3/8 II G
~5 0 ,------17155 NOTE 22 I
0 ------~-------------_ 'f 7. OVERFLOW LOOP SEAL TO EXTEND 12 INCHES BELOW TANK ro 017-HCD-1" .:-:::. CONNECTION AND TO TOP OF TANK WITH SIPHON BREAK ON I I N 0 Q V0 24 Q fPcV\
~L ~IS~)
HYDROGEN V012 TOP OF LOOP SEAL.
~ .~
SUPPLY 8. LOOP SEAL TO EXTEND 12 INCHES BELOW NOZZLE AND TOP OF SEAL TO EXTEND 6 INCHES BELOW DIAPHRAGM FLANGE WITH rPAH\
~5 ~15 G* 7170 REACTOR COOLANT FOI SIPHON BREAKER LOCATED ON TOP OF LOOP.
I 01 4 o_rl"--"' C016" DRAIN TANK 9. LOOP SEAL TO EXTEND 12" ABOVE AND BELOW PIPE. I THB09I @ ~]
~ HBD HBD 017-HC0-1" .:-:::. ::-a;; 10. THE FOLLOWING EQUIPMENT IS SUPPLIED WITH EVAPORATOR PACKAGE BY VENDOR.
I 003B
'-r"115 LT :~~0~22~-~H~C~D~-2~'-'--~~ NOTE 29 NOTE 15 VOl I ~------ ~
1003 , V010 1[4] ~ A. Y-STRAINER-SHB14 I VD1S ~ "'f-+t+_;J TEST CONN. I 4 6 B. PCV-333
~-~--1 C~ CO I 7 ~
&1"(DJ 1 C. TCV-325 I
I 115 1003A
'-----'115 I I
--------.,.......,. L,..J-,-flf-r-3-"x-2-"
L,J-,.......,. 056-HCD-3 11
! zs F _______ L ~21 D.
E. F. PCV-337 FCV-329 WEV-21
,--<i\.--------~ I ~ --------~,,-------~~~~--------~--------, 0 -
D 7136 G. WEV-26 f.---Y-------1 I I C>, ';" NOTE 4 ~LF-770-HCD-4" u I Ay ) CIS-A 11. LOOP SEAL TO EXTEND 12 INCHES BELOW PIPE. I~~~~~ I ' ~ 8 REACTOR VESSEL -,CLOSES I I \OW I --t663J---I V449 1003C I FLANGE LEAK-OFF :042 F.C. 12. THE PORTION OF THIS SYSTEM THAT IS Q-LISTED INCLUDES I I '-----'115 I eL I
'-----'II 5 I I
* ~11~5 ~ 71 ~0- ' ) M-228B01 ) - - ~' ; sl ~~ PIPING AND VALVES ASSOCIATED WITH CONTAINMENT PENETRATIONS AND THE SHELL SIDE OF THE REACTOR COOLANT DRAIN TANK
'--7"-7;;L-.j~~
L..:.J
~ HEAT EXCHANGER AND ITS ASSOCIATED PIPING AND VALVES.
II TO II II 1 II D HV s HY '-""" 4-: <?-'?
":?
( G-5) 3 "{X 3"g" w F pr:_olr rL ~~ 7 I 27 7127 r.a, <?(--<" If-057-HCD-2"- i""J 6 0
- 13. MECHANICAL DESIGNATIONS PER M-2G001. F
.o~
1 /
'V
~Vl._. ~ :c'l------. '
1 6'_, OS ',' F FROM FB-1 008 TO PHB02A 1003 --1 115 I F.O. ';J ~"-7"',-j- AS EXCESS LETDOWN {V ~ ci, 6 I ~4~~ 14. THIS POINT DEFINES THE "Q" BOUNDARY FOR CONTAINMENT ISOLATION, FROM THIS POINT DOWNSTREAM PIPING IS ANALYZED IB-41 IC-61 ~ F. 0.. HEAT EXCHANGER " V458 .... ] I "TC. CONSIDERING A SINGLE DEGREE OF FREEDOM.
.,L m ~
I f.---e5 ) M-22BG01 )- ---------------L BG-190-HCD-1 ~ o _J L. C. LY-1TO003A (--- ~C _ _j I 7128 IE 2 l '-' 1" TEST CONN. 2 rx.;__
" I;;'
t-J ,---- w HCB HCD
- 15. INDICATED PORTIONS OF THIS SYSTEM IDENTIFIED BY THIS NOTE ARE NOT QUALITY GROUP "D" AUGMENTED. AUGMENTED REQUIREMENTS DO NOT APPLY TO INSTRUMENTATION AND SAMPLING PIPING DOWNSTREAM
~
IE-2l 1003 zs OF THE SYSTEM ROOT OR ISOLATION VALVE. 11 5 L--r--1 NOTE 4 SJV117ar V041-1 I 7176 <[ 16. DELETED 032-HCD-2" _ /
- r:
SJVI15\,. -j--- I" BCD HCD * ' I I
- " - _ D15-HC8-3"
- 17. CONTROLS FOR WASTE EVAPORATOR ARE ON PANEL HB135 0
I I I L-ffLLi f---_L_--fl'\, F
- C* !WASTE EVAPORATOR CONTROL PANEL).
1 L. C. u 1 " S* W* CAP~ <:-:-:., 360-HCD-1 " I I m 014-HCD-3" 18. LINES 014 & 015 TO BE SCH. 80S WITH SCH. 40S BORE I I TO MATCH VALVES 7168, 7135, LCV-1003 AND HV-7136. w A"' SJ-028-BCD-1 ,_] sJV112 m 0 I I I 0 u HV 7176 Q 7168
- 19. INDICATED PORTIONS OF THIS SYSTEM TO BE 316L SS.
- 20. INDICATED VALVES TO LOCATED CLOSE TOGETHER.
~-r---1 I
ECD HCD " I
@ ,---e .:-:::. I"T.C.
042-ECO~
- 21. LOCATE INDICATOR WITHIN VIEW PUMP THROTTLING VALVE.
1--lv~o""o~*g- ] 0 u I [-- & 10 1 co I 055 HCD 3" 22. PRESSURE CONTROLLER IS VALVE MOUNTED. SIS ACCUMULATOR/
-z" 0 [--
TANK "B" I 0 23. INSTRUMENTATION IDENTIFIED BY THIS NOTE IS SUPPLIED E > M 2 2 EPO 1 H f---1~-.... 294-HCD-2" f----'=~;;.:;_"-----, [-- FC BY THE SOLID RADWASTE PACKAGE VENDOR UNDER SPECIFICATION M-135. E
~15 I E-8) I NOTE 5) IV028 1----..,...:-:::.+---~ 1 "D 24. CONNECTIONS TO BE SEAL WELDED.
'\ /~
,---- w SIS ACCUMULATOR/ 043-ECD-2" V443 F . C. L.J)-f---fff--f--f--f--f--f--c__,
- 25. PIPING AND INSTRUMENTATION DIAGRAM FOR THE REVERSE
~
TANK "C" 1 OSMOSIS UNIT IS SHOWN ON BECHTEL DWG. M-136-00025.
> H 295-HCD-2" f--~~NIIII...,f-------'=...:.:.::.:;...,:;___-1
[-- 1003F I
~~~---@
M 2 2 Ep 0 1 1 y1 15 26. PIPING AND INSTRUMENTATION DIAGRAM FOR THE WASTE IC 8 l I NOTE 5 I V029 I c~ EVAPORATOR IS SHOWN ON WESTINGHOUSE DWG. 4669D04.
~~ Q I BG-LCV459 I 7135 SIS ACCUMULATOR/ 045-ECD-2" TANK "A" 1
> M-22BG01>------ [-- [--
I I 7167 LY 1003A
- 27. REMOVABLE SPOOL PROVIDED FOR START-UP.
> M 2 2 Ep 0 1 . 297-HCD-2" H I -.~14---r---';.;:.:....:.:.:;::;:....:;_....,:......., 1H 6 l I I
I
,.,;L-J_~ AS FT
,------i10D9~----,
115 I
- 28. LOCATE WASTE EVAPORATOR REAGENT TANK TO ALLOW GRAVITY DRAIN TO WASTE EVAPORATOR.
I G-8 l I NOTE 5 I VD31 I F .o~ 'V 29. PIPING DOWNSTREAM OF THIS POINT IS ANALYZED I V391 FROM CONSIDERING A SINGLE DEGREE OF FREEDOM. SIS ACCUMULATOR/ 044-ECD-2" I V039 V038 ' LC-1 003
~
TANK "D" 1 FE L IF -8 l 30. STAINLESS STEEL PT COUPLING HOSE FITTINGS AND ASSOCIATED
) M 2 2 Ep 0 1 H r--,~.........--:---'=-"-'""-"'----:--1 296-HCD-2" 1009 1 " I D l L.: ~-* .:---::.._-1
~ ~
013-HCD-3" PLUGS/CAPS MAY BE USED INSTEAD OF VENTS AND DRAINS CAPS PER RFR-13719 REV. A. IA 8 l I NOTE 5 l V030 ~ 31. FAUCET ASSEMBLIES MAY BE INSTALLED FOR SAMPLING AS 3 " x2" V390 3-{1 Vl
-r-'l_------------------------.1...-{::t*f--------1l~1-__!:0!§5~3.::tj_HC£!D:;_j2:_:':_'--{_,::1-_i__,.~o:;:5~2=H~C£!D~3:_:":....------------t--"!'::-!r--J NECESSARY ON VENTS, DRAINS AND TEST CONNECTIONS.
V445 ' :38~ WHEN NOT IN USE. THE FAUCET ASSEMBLIES SHOULD BE IN I NOTE 15 l * ~- 0~ V040 THE NORMALLY CLOSED POSITION.
'N D L..:.J 0
u I V389 D w
- 32. CONNECTIONS ARE FOR AUXILIARY PROCESSING I l.e.FILTERING AND/OR DEMINERALIZATION). D I
D D z
- 33. THE PORTIONS OF LINES 500 AND 501 BETWEEN VALVES V816 AND 1 II D
'"N m
I r:--1, N I L..:.J 1"(0) , m I
' '~
V817 AND THEIR RESPECTIVE IN-LINE MIXING SECTIONS ARE LINED PIPE SUPPLIED BY OTHERS.
~
0 D u I u u V336 m I 0 I
~
I 1 "D I I
- I D
u I u I I
..,.-4~1/
I N REV. DATE
"' 303-HBC-3/4" --1
""0 32 111105 hi ~""'
~
0 REFUELING DRAWN CHKD. SUPV. POOL DRAIN RLW EWM SKC 035 HCD 4 II 0 PRESSURIZER INCORPORATE
) M 22EC02 I RELIEF TANK MP 89-1035A
[-- w HBC HBB HBC I ~ BB-1 09-HCD-3"::, I PART I ALl
-----{::"',r---------7 M-22BBoz )
ID 6 l >- 0 333-HCD-3" ---.__. FLOOR & EQUIP. D z REV. DATE [-- aJ 33 030507
._ ~ DRAINS [-- I pp REACTOR 7140 BB-HV7141 I E-2 l DRAWN CHKD. SUPV.
'-----l~<ll~t------l-) M-22LF09 DRW > COOLANT
~ ~~~-------- --------1 NOTE 15 RLW EWM SKC V432 IF7l I "D ~--* .:-:::.*f---1 '"' DRAIN TANK INCORPORATE v456 MP 89-1 035A LF-A74-HCD-3" V034 HEAT I I PARTIAL)
EXCHANGER
~--
[-- COMPONENT ~ I REV. DATE COOL! NG WATER 0 m I 34 040401 DRAWN CHKD. SUPV.
~.::,
2'=~~~~)-------_i20!4~8jH~B~C~4~"~~ I I
~~E~~~R+f~~ ~
M 22EG03 RLW EWM TWS c > )- BB-11 0-HCC-4" ,c:' 034-HCD-4" u COl 8 CAL ORN VALVE IE 3 I NOTE 1 HBC HBD
~ V305 ~ , V306 I
I I INCORPORATE MP 89-1 035A c
~-2 2 BB02 - - - - - - - - - - - - - - - -~,..~1---L-...Li;:..;;_:....:.:;;.:;;....:., % ~ .. I PART I ALl r
I FROM HS/-1003A FLUSH I NOTE 15 l m REV. DATE ID 4 l 039 _BCD-2 " BB-HV8031 e-r I F-8 l
' V4 01 FLUSH fof)* CONNECTION 0 V03 7 1
COMPONENT COOLING WATER 35 082208 CONNECTIO~
& 1 "0 DRAWN CHKD. SUPV.
FE R. C. LOOP 4 DRAIN HCC HCD * '"' 1008 301-HCD-3/4"- @h I f----------~--~~--L-----~If--~-- --t***:J-~.J------1 > RLW EWM TWS j pp
) M 22BB01 __,~-- M-22EG03 t---j;".;;jj~n11=E=H=8=Q=1JI ~~,.,~3~o_2_-H_B_c-_l_"~ ~1_, LocAL INCORPORATE CR 1E 8 ) 0 3' X 2"' <[ 1 L..:.J 11 (0)
'"' fC 'I I c :o ~
Ill \__ IE-3l CAR 08-000218; CAR 200804353 R.C.LOOP 1 DRAIN
) M 22BB01 I NOTE 15 l V247
- V004 c V005 i
I 3" X V006 1 1/2" V248 V334 L-1 " 6 V£;4 V335 3/4"
- J DRAIN 049-HBC-4" EG-142-HBC-4" REV.
36 DATE I 02808 DRAWN CHKD. SUPV. IEZl_/1 ,-_.....168-1j....:..:.;_...l___:"-~,1f-...l.-+t "'K-"}----"T"-r-+----11 1 , 01 D-HCD-3" J-------1' RLW TJC LMR 036-BCD-2" _)
~
T Hr-~~.......~r-~0~41~-~H~C~D--3'-'-'----~~~=~-r-1
- V402 4';.._x 3'
~~';;3~
'L_-...L.....I'-----L----1'---+r'--;="
,r L 009-HCD-3
r 334-HCD-1"' r
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CHKD. SUPV. APPD. RAM TJM N/A H IC-61 4. THE FOLLOWING WESTINGHOUSE STANDARD EQUIPMENT IS SUPPLIED TO A HIGHER IN CORP. QUALITY GROUP/SEISMIC CLASSIFICATION AND PRINCIPLE CONSTRUCTION CODE THAN CMP 88-102S. IS REQUIRED BASED ON IT'S SAFETY RELATED IMPORTANCE AS DICTATED BY SERVICE REV. DATE DRAWN AND FUNCTIONAL REQUIREMENTS AND BY THE CONSEQUENCE OF THEIR FAILURE. 5 030397 RAM EQUIPMENT CLASSIFICATION SHOWN IS FOR INTERFACE PURPOSES ONLY I I.E. CHKD. SUPV. APPD. HYDROGEN WELD END PREPS!. ACTUAL CLASSIFICATION OF THE EQUIPMENT IS THE LOWER JHK AMR N/A 2"X3/4" RECOMBINER 'B' CLASSIFICATION AS INDICATED FOR THE ASSOCIATED PIPING. INCORP. 015-HCD-3/4" DEC #1 398 M-22HA02 A. GAS DECAY TANKS REV. DATE DRAWN I D-7 I B. WASTE GAS DRAIN FILTER 6 042897 RAM CHKD. SUPV. APPD. JHK AMR N/A
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OXYGEN CATALYTIC HEATER REACTOR FROM GAS COMPRESSOR TO GAS ANALYZER TO GAS ANALYZER PHASE SEPARATOR COOLER/CONDENSOR TO GAS DECAY TANK TO GAS TO GAS T - TEMPERATURE MEASUREMENT ANALYZER ANALYZER P - PRESSURE MEASUREMENT Rev. OL-0 F - FLOW MEASUREMENT 6/86 CALLAWAY PLANT FIGURE 11.3-4 HYDROGEN RECOMBINER INSTRUMENTS
8 7 6 5 4 3 2 1 RADWASTE BLDG VENTILATION 024-HCD-3" X BOILOUT LINE M-22GH02 V177 TO WASTE EVAP 332-HCD-1" E o o IF -5 I HB-331-HCD-1" ~ ) r - . . . , . . . f - - - - - - - - - - - - 7 M-22HB02 H RADWASTE BLDG VENTILATION M-22GH02 C C-7 I 028-HCD-3" 0 E o
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