ML17335A154
| ML17335A154 | |
| Person / Time | |
|---|---|
| Site: | Cook  |
| Issue date: | 06/29/1995 |
| From: | Creiglow J INDIANA MICHIGAN POWER CO. (FORMERLY INDIANA & MICHIG |
| To: | |
| Shared Package | |
| ML17335A147 | List: |
| References | |
| NESP032395JJS, NESP032395JJS-R01, NESP32395JJS, NESP32395JJS-R1, NUDOCS 9808100109 | |
| Download: ML17335A154 (59) | |
Text
gE-ON NUGAE@~ R ENGINEERING OEPARTj@gNT (OBY95) Calculation Cover Sheet Cook Nuclear Plant SECTION SHEET 1 OF CALCULATION No. C.SP ~7. 5 MS, INDIANA MICHIGAN POWER COMPANY SAFETY RELATED YES ~ NO UNIT No.
SYSTEH CucS- CALCULATED BY: 3~ K. Crci ha DATE TITLE Lcm'.<
VERIFIED BY:
RFC/HH/PM/PR/CR/TH No. DATE FILE LOCATION C. APPROVED BY: dr~ Fs DATE C'ALCULATION DESCRIPTION:
oÃa x o. X4 a, oretc r S
sc D OF VERIFICATION: ALTERNATE CALCULATION v DESIGN REVIEW REVISION Calculated Ver)fled Approved NO. REASON FOR CHANGE 8 Oate 8 Oate 8 Date VS ~c. Vroko- Who +a (./z >z~/(~i c + m ~ e ~C.mr~
CJOY 9808%00'f09 9808iT PDR AnaCX 0S00OSXS PDR
7
~,,r NE&15 DONALD C. COOK NUCLEAR PLANT (oz/9s)
Section DESIGN VERIFICATION CHECKLIST - CALCULATIONS Calculation Number AC P 4>~~RS MS Signature of Verifier Date 1.0 Basis ~
wco +
Were the inputs correctly selected, incorporated and documented into the calculation?
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~~ 'so~t-~tc.tc N/A 2.0 Are assumptions necessary to perform the calculation adequately described and reasonable? Yes ~ N/A Basis: i~~~ ~c .o~s. Gts~~~ a~~ ~wc ~~~K<~ s e'- 4 P~m~'MACC %Caccia%' aL wc'+wAMcou 3.0 Are the app'iicable codes, standards and regulatory Basis: Wa requirements met?
~e As identified S~l4&A C and requirements for design W~m C Ct ~KCsOC M~CC Yes N/A ~
tXw 5. MLc v~mac 4.0 Was an appropriate design method used? Yes v N/A Basis: ~~ ~~~~ m~ v PCZWWS M~ Ww~As 0'.0 Ba s 1 s:
Is the output reasonable U ~~ ~vatic.eu compared ca~ wc-to input? Yes ~ N/A
~'v ~~ ~~~ ~~cc- ~ 40 Cc t~a Cu14C~atd g St %@AC
6.0 Basis
~~~
Are the results numerically correct? Yes ~ N/A Q~C .cc~p'tD& c o~v~~~~
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Re.g. 5 She.e. e l c4 66-0:2-1 995 11:32 PROTP~LO201by PROTO-POWER COrgpRATION 1 Utility- D:VROTOFLOUIM.PDB - Version i ~
Plant - System Combined Summary Report Convergence: Pressure=1.0E-S Sum Q"-1.0E-2 Friction=1.0'CV=1.0'CV=1.0'emperature=5.0'age Pipe: 1.00 ID = 2.067 Flow = 75.00 Vel = ?.172 Turbulent f = 0.0200 Reynold's Number = 3.2281E+05 N1'ODE1 ** Press= 14.84 Elev= 589.43 .- Flow= 0.00 Temp= 180.00 N2: NODE2 Pipe: 2.00 ID = 2.067 Press= 12.98 Flow= 75.00 x Z Elev= 588 53~low= 0.00
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+Vel = 7.172
~ ~ W~O Temp= 180.00 Turbulent f = 0.0200 Reynold's Number = 3.2281240 N1: NODE2 Press= 12.98 Elev= 588.53 Flow=-0:00 Temp= 180.00 N2'ODE3 Press= 11.52 Elev= 588.53m Flow= 0.00 Temp= 180.00 w.'59W (= > 4-W %+ ~
'L Pipe: 3.00 ID = 2.067 Flow= 75.00 Vel = 7.172 Turbulent f 0.0200
= Reynold's Number = 3.2281E+05 N1: NODE3 Press= 11.52 Elev= 588.53 Flow= 0.00 Temp= 180.00 N2: NODE4 Y W ~ %+~
Pipe: 4.00 ID = 2.067 Flow= 75.00 NPSHA =5:97 -- NPSHR = 5.90 N1: NODE4 Press= 10.14 Elev= 588.53 Flow= 0.00 Temp= 180.00 N2: NODE5 Press= 110.67 Elev= 588.53 Flow= 0.00 Temp= 180.00 Pipe: 5.00 ID = 2.067 Flow = 75.00 Vel = 7.172 Turbulent f = 0.0200 Reynold's Number = 3.2281E+05 N1: NODE5 Press= 110.67 Elev= 588.53 Flow= 0.00 Temp= 180.00 N2: NODE6 Press= 110.28 Elev= 588.53 Flow= 0.00 Temp= 180.00 Pipe: 10.00 ID = 2.067 Flow= 75.00 Vel = 7.172 Turbulent f = 0.0200 Reynold's Number = 3.2281E+05 N1: NODE6 Press= 110.28 Elev= 588.53 Flow= 0.00 Temp= 180.00 N2: NODE6.5 '* Press= 33.70 Elev= 592.50 Flow= 0.00 Temp= 180.00 P~~
4@~4~
" Fixed Pressure II Reverse Flow Thru Check Valve
%% Pressure Below Vapor Pressure ++ Section Was Balanced
¹¹ NPSHA lass than NPSHR M Flow Past End of Pump Curve
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CALC. NO. : NESP032395JJS REV. 1 SHEET: ~ OF lR DATE: 6/2/95 COMPANY: I&M PLANT: DCCNP
SUBJECT:
BAT PUMP NPSHR vs BAST LEVEL DESCRIPTION Model the boric acid tank to the boric acid transfer pump using proto-flo, placing a valve at the end of the model to throttle the pump to 75 GPM. Then changing the atmospheric pressure at the base of the tank until the NSPH available is as close as possible to the NPSH required. This will give the lowest pressure at the base of the tank before the pumps can no longer be supplied with the boric acid solution to maintain 75 GPM out of the transfer pumps. The pressure then can be converted to show the lowest level required to the pumps and have a 75 GPM out put.
PURPOSE The result of the calculation will be used in the development of H HEW Severe Accident Management Guidelines. In the event that an accident progresses to core melt, where emergency operating procedures are no longer valid, these guidelines would be used.
ASSUMPTION & LIMITATIONS
- 1) BORIC ACID SOLUTION TEMPERATURE = 180 F
- 2) BORIC ACID SOLUTION HAS SAME VAPOR PRESSURE AS WATER(=,)
- 3) BORIC ACID SPECIFIC GRAVITY EQUAL TO WATER
- 4) TANK AT ATMOSPHERIC PRESSURE
- 5) BORIC ACID TRANSFER PUMP OPERATING AT 75 GPM RESULTS
- 1) NSPH required to supply 75 GPM = 5.90 ft.
- 2) Pressure at the bottom of tank is 14.84 psia, when converted to a tank level the tank.
it equals .3328'r =3 15/16" from the bottom of CONCLUSIONS The minimum'AST tank level that is acceptable to operate the BAT pumps while still having adequate NPSH and supplying 75 GPM is 3 15/16" of boric acid solution f m the bottom of the tank.
4 I 4
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CALC. NO. : NESP032395JJS REV. 1 SHEET 3 OF DATE: 6/2/95 COMPANY: IBM PLANT: DCCNP
SUBJECT:
BAT PUMP NPSHR vs BAST LEVEL REFERENCES
- 1) CAMERON HYDRAULIC DATA: PROPERTIES OF WATER AT VARIOUS TEMP.
(CONVERSXON FACTOR FT/LB/IN"2)
- 2) AEPSC ISOMETRIC DWG. O-CS-539L1.4
- 3) AEPSC VALVE DWG W-200D42ZGO FOR 2" DIAPHRAGM VALVE
- 4) AEPSC FLOW DIAGRAM ED 12-5131
- 5) PUMP CURVE FOR PP-46
- 6) PROTO-FLO SOFTWARE FOR WINDOWS VERSION 2.01 (DATE AND TIME OF RUNS SHOWN ON OUT PUT DATA SHEETS)
- 7) IBM PERSONAL SYSTEM/2 MODEL 77 486DX2 COMPUTER WITH OS2 SYSTEM (PROTO-FLO OPERATES UNDER"OS2 WINDOWS APPLXCATION)
SKETCH
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3'-W V1S-SMY. 3$
8.33'~
10 V2" HOOCS CLCV SS1 ~ '3 0 S 'COCS, 0 1 PPAS 1
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06-02-1 995 11:32 PROTO-FLO 2.01 by PROTO-POWER CORPORATION Page 1 Utility- DAPROTOFLOUIM.PD8 - Version Plant - System Hydraulic Resistance Report Convergence: Pressure=1.0E-5 Sum Q=t.OE-2 Frtction=1.0E-6 FCV=1.0E-4 PCV=1.0E-3 Temperature=5.0'-
ID Flow DZ Velocity Reynolds Pressure Drop Hydraulic Resistance Pi e FromNode To Node (Inches f//g m"2 ~si/g m"2 1.00 NOD E1 NODE2 2.067 75.00 1.85 7.172 3.2281 E+05 5.314 2.235 9.4470 E-04 3.9739E-04 2.00 NOD E2 NODE3 2.067 75.00 1A6 7.172 3.2281E+05 3.476 1.462 6.1800E-04 2.5996E-04 3.00 NOD E3 NODE4 2.067 75.00 1.38 7.172 3.2281E+05 3.290 1.384 5.8494 E-04 2.4606E-04 5.00 NOD E5 NODE6 2.067 75.00 0.38 7.172 3.2281 E+05 0.926 0.389 1.6470 E-04 6.9281 E-O 10.00 NOD E6 NOD E6.5 2.067 75.00 76.58 7.172 3.2281 E+05 178.083 74.911 3.1657 E-02 1.3317E-02
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06-02-1 995 11:32 PROTO-kO 2.01 by PROTO-POWER CORP@RATION
~
R<<. 5 5hech 5 oW h l Page 1 Utility- D:PROTOFLOUIM.PDB - Version Plant - System Pump Status Report Pump Name: 1-PP-46-1 Manufacturer Drawings:
Pump Status: BAST Speed (RPM): 3,500 Flow (gpm): 75.00 Head (ft): 239.00 Hydraulic Horsepower: 4.40 Pump Impeller Elevation (ft): Inlet Node Elevation (ft): 588.53 Pump Suction Temperature ('F) 180.00 NPSH Curve: BAST NPSH NPSH Available: 5.97 NPSH Required: 5.90 Pump Name 1-PP-46-2 Manufacturer Model:
Drawings:
Pump Status: OFF Speed (RPM): 3,500 Flow (gpm): Head (ft):
Hydraulic Horsepower:
Pump Impeller Elevation (ft): Inlet Node Elevation (ft): 588.53 Pump Suction Temperature ('F)
NPSH Curve: BAST NPSH NPSH Available: NPSH Required:
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'I c~ 4 07 06-02-1 995 11:32 PROT - LO 2.0'I by PROTO-POWER CO ~ RATION Page1 Utility- D:PROTOFLOUIM.PDB - Version Plant- System Boundary Condition Report Node Name Bounda T e 8ounda Parameters NODE1 Pressure Suction Pressure 14.84 psia Elevation 589.43 tt S ecifiedTem erature 180.00 'F NOD E10 Pressure Discharge Pressure 33.70 psia Elevation 592.50 ft S ecifiedTem erature 180.00 'F NODE6.5 Pressure Discharge Pressure 33.70 psia Elevation 592.50 tt Specified Temperature 180.00 'F
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~~,;, hec.+ l c V lL 06-02-1995 11:32 PROT'O 2.01 by PROTO-POWER CO~~RATION Page 1 Utility- D:<PROTOFLOUIM.PDB - Version Plant - System Combined Summary Report Convergence: Pressure=1.0E-S Sum Q=1.0E-2 Friction=1.0E4 FCV=1.0'CV=1.0E-3 Temperature=5.0'ipe:
1.00 ID = 2.067 Flow = 75.00 Vel = 7.172 Turbulent f = 0.0200 Reynold's Number = 3.2281E+05 N1: NODE1 ** Press= 14.84 Elev= 589.43 Flow= 0.00 Temp= 180.00 N2'ODE2 Press= 12.98 Elev= 588.53 Flow= 0.00 Temp= 180.00 Pipe: 2.00 ID = 2.067 Flow= 75.00 Vel = 7.172 Turbulent f = 0.0200 Reynold's Number = 3.2281E+05 N1: NODE2 Press= 12.98 Elev.= 588.53 Flow= 0.00 Temp= 180.00 N2: NODE3 Press= 11.52 Elev= 588.53 Flow= 0.00 Temp= 180.00 Pipe: 3.00 ID = 2.067 Flow= 75.00 Vel = 7.172 Turbulent f = 0.0200 Reynold's Number = 3.2281E+05 N1: NODE3 Press= 11.52 Elev= 588.53 Flow= 0.00 Temp= 180'.00 N2: NODE4 Press= 10.14 Elev= 588.53 Flow= .0.00 Temp= 180.00 Pipe: 4.00 ID = 2.067 Flow = 75.00 NPSHA =5.97 NPSHR = 5.90 N1'ODE4 Press= 10.14 Elev= 588.53 Flow= 0.00 Temp= 180.00 N2: NODE5 Press= 110.67 Elev= 588.53 Flow= 0.00 .Temp= 180.00 Pipe: 5.00 ID = 2.067 Flow= 75.00 Vel = 7.172 Turbulent f = 0.0200 Reynold's Number = 3.2281E+05 N1: NODE5 Press= 110.67 Elev= 588.53 Flow= 0.00 Temp= 180.00 N2: NODE6 Press= 110.28 Elev= 588.53 Flow= 0.00 Temp= 180.00 Pipe: 10.00 ID = 2.067 Flow = 75.00 Vel = 7.172 Turbulent f = 0.0200 Reynold's Number = 3.2281E+05 N1: NODE6 Press= 110.28 Elev= 588.53 Flow= 0.00 Temp= 180.00 N2: NODE6.5 ** Press= 33.70 Elev= 592.50 Flow= 0.00 Temp= 180.00
- Fixed Pressure II Reverse Flow Thru Check Valve
%% Pressure Below Vapor Pressure ++ Section Was Balanced
¹0 NPSHA less than NPSHR && Flow Past End of Pump Curve
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'/2/95 11:36:05 AM PROTERO 2.01 by PROTO-POWER COk~%RATION Pipe 1.00
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~ p Utility- D:PROTOFLOUIM.PDB - Version Plant- System System Pipe Section Data Sheet From: NODE1 Elev: 589.43 To: NODE2 Elev: 588.53
Description:
Drawings:
Fluid: Fresh Water Material Roughness: 0.000150 Carbon Steel 2.000 inch Schedule: STD 40 - Inside Diameter: 2.067 Length: 16.58 Misc L/D: Misc K Fixed:
Valves: 1-CS437N I I Pipe Flow Summary
Title:
Tees: 1 Run; Branch Only; Branch Elbows: Welded -, 2 90s, 45s; Threaded- 90s, 45s Bends: with angle = ,rid=
with angle = ,rid=
Entrances: Abrupt Reductions from d =
Exits: Abrupt Expansions to d =
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Description:
Drawings:
Fluid: Fresh Water Material Roughness: 0.000150 Carbon Steel 2.000 inch Schedule: STD 40- Inside Diameter: 2.067 Length: 4.00 Misc L/D: Misc K Fixed:
Valves: 1-CS410/ I Pipe Flow Summary
Title:
Tees: Run; 1 Branch Only; Branch Elbows: Welded- 90s, 45s; Threaded- 90s, 45s Bends: with angle = ,rid=
with angle = , r/d =
Entrances: Abrupt Reductions from d =
Exits: Abrupt Expansions to d =
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'Rc.w. X l\ 4c~W 50 oV 6/2/90 11:36:05 AM PROTMLO 2.01 by PROTO-POWER COi'-~%) RATION -
Pipe 3.00 Utility- D:PROTOFLOUIM.PDB - Version Plant - System System Pipe Section Data Sheet From: NODE3 Elev: 588.53 To'ODE4 Elev: 588.53
Description:
Drawings:
Fluid: Fresh Water Material Roughness: 0.000150 Carbon Steel 2.000 inch Schedule: STD 40 - Inside Diameter: 2.067 Length: 3.63 Misc L/D: Misc K Fixed:
Valves: 1-CS412-1 / I Pipe Flow Summary
Title:
Tees: 1 Run; Branch Only; Branch Elbows: Welded- 90s, 45s; Threaded- 90s, 45s Bends: with angle = ,rid =
with angle = ,r/d=
Entrances: Abrupt Reductions from d =
Exits: Abrupt Expansions to d =
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~C 6/2/95 11:36:05 AM PROTMLO 2.01 by PROTO-POWER CORFtlRATION Pipe 4.00 J Utility- D:PROTOFLOUIM.PDB - Version Plant - System System Pipe Section Data Sheet From: NODE4 Elev: 588.53 To'ODE5 Elev: 588.53
Description:
Drawings:
Fluid: Fresh Water Material Roughness: 0.000150 Carbon Steel 2.000 inch Schedule: STD 40- inside Diameter: 2.067 Length: 0.00 Misc L/D: Misc K Fixed:
Pump: 1-PP46-1 Pipe Flow Summary
Title:
Tees: Run; Branch Only; Branch Elbows: Welded- 90s, 45s; Threaded- 90s, Bends: with angle = , r/d=
with angle = , r/d =
Entrances: Abrupt Reductions from d =
Exits: Abrupt Expansions to d =
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~ >Z,oV 6/2/95 11:36:05 AM PROTS~~LO 2.01 by PROTO-POWER COP'O'ORATION Pipe 5.00 Utility- D:PROTOFLOUIM.PDB - Version Plant - System System Pipe Section Data Sheet h
From: NODE5 Elev: 588.53 To: NODE6 Elev: 588.53
Description:
Drawings:
Fluid: Fresh Water Material Roughness: 0.000150 Carbon Steel 2.000 inch Schedule: STD 40 - Inside Diameter: 2.067 Length: 10.00 Misc L/D: Misc K Fixed:
Pipe Flow Summary
Title:
Tees: Run; Branch Only; Branch Elbows: Welded- 90s, 45s; Threaded- 90s, 45s Bends: with angle = , r/d=
with angle = , r/d =
Entrances: Abrupt Reductions from d =
Exits: Abrupt Expansions to d =
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6/2/95 11:36:05 AM PROT'-r LO 2.01 by PROTO-POWER COPSQRATION Pipe 6.00
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Utility- DAPROTOFLOUIM.PDB - Version Plant - System System Pipe Section Data Sheet From: NODE2 Elev: 588.53 To: NODE7 Elev: 588.53
Description:
Drawings:
Fluid: Fresh Water Material Roughness: 0.000150 Carbon Steel 2.000 inch Schedule: STD 40- Inside Diameter: 2.067 Length: 3.63 Misc L/D: Misc K Fixed:
Valves: 1-CS412-2/
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Pipe Flow Summary
Title:
Tees: 1 Run; Branch Only; 1 Branch Elbows: Welded- 90s, 45s; Threaded- 90s, 45s Bends: with angle = , r/d =
with angle = , r/d =
Entrances: Abrupt Reductions from d =
Exits: Abrupt Expansions to d =
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~~'ic cVh R.c.<. 5 6/2/95 11:36:05 AM PROT LO 2.01 by PROTO-POWER CO RATION Pipe 7.00 Utility- D:PROTOFLOUIM.PDB - Version Plant - System System Pipe Section Data Sheet From: NODE7 Elev: 588.53 To: NODE8 Elev: 588.53
Description:
Drawings:
Fluid: Fresh Water Material Roughness: 0.000150 Carbon Steel 2.000 inch Schedule: STD 40 - inside Diameter: 2.067 Length: 0.00 Misc L/D: Misc K Fixed:
Pump: 1-PP-46-2 Pipe Flow Summary
Title:
Tees: Run; Branch Only; Branch Elbows: Welded- 90s, 45s; Threaded- 90s, 45s Bends: with angle = , r/d =
with angle = , r/d =
Entrances: Abrupt Reductions from d =
Exits: Abrupt Expansions to d =
6/2/95 11:36:05 AM PROTKCLO 2.01 by PROTO-POWER CO%5RATION Pipe 8.00 Utility- D:>PROTOFLOUIM.PDB - Version Plant - System System Pipe Section'Data Sheet From: NODE8 Elev: 588.53 To: NODE9 Elev: 588.53
Description:
Drawings:
Fluid: Fresh Water Material Roughness: 0.000150 Carbon Steel 2.000 inch Schedule: STD 40 - Inside Diameter: 2.067 Length: 20.00 Misc L/D: Misc K Fixed:
Pipe Flow Summary
Title:
Tees: Run; Branch Only; Branch Elbows: Welded- 90s, 45s; Threaded- 90s, 45s Bends: with angle = ,r/d =
with angle = , r/d=
Entrances: Abrupt Reductions from d =
Exits: Abrupt Expansions to d =
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Re~. h 6/2/95,11:36:05 AM PROT%--LO 2.01 by PROTO-POWER COB~" QRATION Pipe 9.00 Utility- D:IPROTOFLOUIM.PDB - Version Plant - System System Pipe Section Data Sheet From: NODE9 Elev: 588.53 "To: NODE10 Elev: 592.50
Description:
Drawings:
Fluid: Fresh Water Material Roughness: 0.000150 Carbon Steel 2.000 inch Schedule: STD 40-Inside Diameter: 2.067 Length: 10.00 Misc L/D: Misc K Fixed:
Valves: test-1/ /
Pipe Flow Summary
Title:
Tees: Run; Branch Only; Branch Elbows: Welded- 90s, 45s; Threaded- 90s, 45s Bends; with angle = , r/d =
with angle = , r/d=
Entrances: Abrupt Reductions from d =
Exits: Abrupt Expansions to d =
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Rc~. h P S&c& Cl oW h3 6/2/95 11:36:05 AM PROT(-'..LO 2.01 by PROTO-POWER CObQRATlON Pipe 10.00 I Utility- D:PROTOFLOUIM.PDB - Version Plant- System System Pipe Section Data Sheet From: NODE6 Elev: 588.53 To: NODE6.5 Elev: 592.50
Description:
Drawings:
Fluid: Fresh Water Material Roughness: 0.000150 Carbon Steel 2.000 inch Schedule: STD 40 - Inside Diameter: 2.067 Length: 10.00 Misc L/D: Misc K Fixed:
Valves: test-1/ I Pipe Flow Summary
Title:
Tees: Run; Branch Only; Branch Elbows: Welded- 90s, 45s; Threaded- 90s, 45s Bends: with angle = , r/d =
with angle = , r/d =
Entrances: Abrupt Reductions from d =
Exits: Abrupt Expansions to 'd =
.E.D. RECORD COVER SHEET
'COOK NUGAE.EPR Pf.AFJ NEO RECORD-NEO COPY SECTION ENGINEER O TE PLAN LIFET!E T V(E DATE TO PlAM5 Cl NON PERMANENT MlwlMUR5 RET 5TlO!4 YRS C~CUIJ tILIO+[ g g~~g~K8 3 ++~+M pgL.r: .CV'.C SUB JECT TQ: N.E.P. 6.4 (CALCULATIONS)
N.E,P, 17.0 l.'RECORD RETENTION)
N.E.P. 17,2 (HICROFILHING)
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NE-015 DONALD C. COOK NUCLEAR PLANT (02/95)
Section DESIGN VERIFICATION CHECKLIST CALCULATIONS Calcula n Number <~~v-~we awaits Rev. c Signature of Verifier Date 1.0 Were the inputs correctly selected, incorporated and Basis: MF ~ uf I ~~ ~>3 ~
documented into the calculation?
C4-/c~
~/
/+Pe Qe~
A'PJ H Mal cs cOcw I%4 J4 J hlC.q r c,~M 2.0 Are assumptions necessary to perform the calculation adequately described and reasonable? Yes . N/A Basis: // ~cue.' c /C c 2 ~~g J r Wnlg&
4.&NJ //->>-Wi~ S?
3.0 Are the applicable codes, standards and regulatory requirements identif ied and requirements for design met? Yes N/A Basis: Af~ a~
4.0 Was
+l an appropriate design method used? Yes ~ N/A Basis: krJ &PS'A' nJc ~+<~>~
5.0 Basis
Is the output reasonable
'3 -'/ A M > ~ compared
-+
to input?
~ ~ T>
Yes ~N/A
~u/J+6/0 .
6.0 Are thy results numerically correct? ~N/A Basis: > / a M ~e ~et / KME Yes Pope 1 of 1
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5E-914 NUCLEAR ENGINEERING DEPARTMENT (o2/9s) Calculation Cover Sheet Cook Nuclear Plant SECTION SHEET I OF CALCULATION No. ~~~-. ~=~z~s ~a INDIANA MICHIGAN POWER COMPANY SAFETY RELATED YES ~ NO UNIT No.
SYSTEM CALCULATED BY:
DATE TITLE ~> e~~v- ~>>We. us. Baaw Levai VERIFIED BY:
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RFC/MM/PM/PR/CR/TM No. ~ l~ DATE FILE LOCATION APPROVED BY: +'zi /gal DATE CALCULATION DESCRIPTION: ~~~~~ i~~ ~~ ~v-~~ ma Mv b ~+%4 Wo + ~CK&c4 'IX
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