rev 1 to calculation nesp032395jjs, 'bat pump npshr vs bast … · 2018. 5. 31. · calc. no.:...

gE-ON(OBY95)

NUGAE@~ R ENGINEERING OEPARTj@gNTCalculation Cover Sheet

Cook Nuclear Plant

SECTION SHEET 1 OF

CALCULATION No. C.SP ~7. 5 MS, INDIANA MICHIGAN POWER COMPANY

SAFETY RELATED

SYSTEH CucS-

TITLE

RFC/HH/PM/PR/CR/TH No.

FILE LOCATION C.

C'ALCULATION

DESCRIPTION:

oÃa x o. X4 a,

S

YES ~ NO UNIT No.

CALCULATED BY: 3~ K. Crci ha

Lcm'.<VERIFIED BY:

APPROVED BY:

oretc r

sc

DATE

DATE

dr~ FsDATE

D OF VERIFICATION: ALTERNATE CALCULATION v DESIGN REVIEW

REVISION

NO. REASON FOR CHANGE

VS ~c. Vroko- Who +ac + m ~ e ~C.mr~

CJOY

Calculated8 Oate

(./z

Ver)fled8 Oate

Approved8 Date

>z~/(~i

9808%00'f09 9808iTPDR AnaCX 0S00OSXS

PDR

7

~,,rNE&15(oz/9s)

DONALD C. COOK NUCLEAR PLANT

Section

DESIGN VERIFICATION CHECKLIST - CALCULATIONS

Calculation Number AC P 4>~~RS MS

Signature of Verifier Date

1.0 Were the inputs correctly selected, incorporated anddocumented into the calculation? Yes ~ N/A

Basis ~ M>vw~ ~~c t-awe . Pmcrvna~ ~~a ~ +~e ~~ 'so~t-~tc.tcwco + Qv ~ P CvcLAcx'- Qa ~vcc. W~c~ . A ~c ~\ tc— Ww~ok

2.0 Are assumptions necessary to perform the calculationadequately described and reasonable? Yes ~ N/A

Basis: i~~~ ~c .o~s. Gts~~~ a~~ ~wc ~~~K<~ s e'- 4

P~m~'MAC—C %Caccia%' aL wc'+wAMcou

3.0

Basis:

Are the app'iicablerequirementsmet?

Wa ~e As

codes, standards and regulatoryidentified and requirements for design

Yes N/A ~S~l4&AC W~m C Ct ~KCsOC M~CC

tXw5. MLc v~mac

4.0 Was an appropriate design method used? Yes v N/ABasis: ~~ ~~~~ m~ v PCZWWS M~ Ww~As

0'.0

Is the output reasonable compared to input? Yes ~ N/ABa s 1 s: U~~ ~vatic.eu ca~ wc-

~'v~~ ~~~ ~~cc- ~ 40 Cc

t~a Cu14C~atd g St %@AC

6.0 Are the results numerically correct?Basis: ~~~ Q~C .cc~p'tD& c o~v~~~~

Yes ~ N/A

Qc.V W~ut C4 WW~t ~tK

Page 1 of 1

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11:32

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She.e. e l c 4PROTP~LO201by PROTO-POWER COrgpRATION

Utility- D:VROTOFLOUIM.PDB- VersionPlant - System

Combined Summary ReportConvergence: Pressure=1.0E-S Sum Q"-1.0E-2 Friction=1.0'CV=1.0'CV=1.0'emperature=5.0'age

1

Pipe: 1.00 ID = 2.067 Flow = 75.00 Vel = ?.172Turbulent f = 0.0200 Reynold's Number = 3.2281E+05

N1'ODE1 ** Press= 14.84 Elev= 589.43 .- Flow= 0.00 Temp= 180.00N2: NODE2 Press= 12.98 Elev= 588 53~low= 0.00 Temp= 180.00

x Z ~ >'tWW 4; ~ ~ W~OPipe: 2.00 ID = 2.067 Flow= 75.00 +Vel = 7.172

Turbulent f= 0.0200 Reynold's Number = 3.2281240N1: NODE2 Press= 12.98 Elev= 588.53 Flow=-0:00 Temp= 180.00N2'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= 180.00N2: 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= 180.00N2: NODE5 Press= 110.67 Elev= 588.53 Flow= 0.00 Temp= 180.00

Pipe: 5.00 ID = 2.067 Flow = 75.00 Vel = 7.172Turbulent f = 0.0200 Reynold's Number = 3.2281E+05

N1: NODE5 Press= 110.67 Elev= 588.53 Flow= 0.00N2: NODE6 Press= 110.28 Elev= 588.53 Flow= 0.00

Temp= 180.00Temp= 180.00

Pipe: 10.00 ID = 2.067 Flow= 75.00 Vel = 7.172Turbulent f = 0.0200 Reynold's Number = 3.2281E+05

N1: NODE6 Press= 110.28 Elev= 588.53 Flow= 0.00N2: NODE6.5 '* Press= 33.70 Elev= 592.50 Flow= 0.00

Temp= 180.00Temp= 180.00

P~~4@~4~

" Fixed Pressure%% Pressure Below Vapor Pressure¹¹ NPSHA lass than NPSHR

II Reverse Flow Thru Check Valve++ Section Was BalancedM Flow Past End of Pump Curve

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CALC. NO. : NESP032395JJSREV. 1SHEET: ~ OF lRDATE: 6/2/95COMPANY: I&MPLANT: DCCNP

SUBJECT: BAT PUMP NPSHR vs BAST LEVEL

DESCRIPTIONModel the boric acid tank to the boric acid transfer pump usingproto-flo, placing a valve at the end of the model to throttle thepump to 75 GPM. Then changing the atmospheric pressure at the baseof the tank until the NSPH available is as close as possible to theNPSH required. This will give the lowest pressure at the base ofthe tank before the pumps can no longer be supplied with the boricacid solution to maintain 75 GPM out of the transfer pumps. Thepressure then can be converted to show the lowest level required tothe pumps and have a 75 GPM out put.

PURPOSEThe result of the calculation will be used in the development of

H HEW Severe Accident Management Guidelines. In the event that anaccident progresses to core melt, where emergency operatingprocedures are no longer valid, these guidelines would be used.

ASSUMPTION & LIMITATIONS1) BORIC ACID SOLUTION TEMPERATURE = 180 F2) BORIC ACID SOLUTION HAS SAME VAPOR PRESSURE AS WATER(=,)3) BORIC ACID SPECIFIC GRAVITY EQUAL TO WATER4) TANK AT ATMOSPHERIC PRESSURE5) BORIC ACID TRANSFER PUMP OPERATING AT 75 GPM

RESULTS1) 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 it equals .3328'r =3 15/16" from the bottom ofthe tank.

CONCLUSIONSThe minimum'AST tank level that is acceptable to operate the BATpumps while still having adequate NPSH and supplying 75 GPM is3 15/16" of boric acid solution f m the bottom of the tank.

4 I

04

CALC. NO. : NESP032395JJSREV. 1SHEET 3 OFDATE: 6/2/95COMPANY: IBMPLANT: DCCNP

SUBJECT: BAT PUMP NPSHR vs BAST LEVEL

REFERENCES1) CAMERON HYDRAULIC DATA: PROPERTIES OF WATER AT VARIOUS TEMP.

(CONVERSXON FACTOR FT/LB/IN"2)2) AEPSC ISOMETRIC DWG. O-CS-539L1.43) AEPSC VALVE DWG W-200D42ZGO FOR 2" DIAPHRAGM VALVE4) AEPSC FLOW DIAGRAM ED 12-51315) PUMP CURVE FOR PP-466) 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

NX%1ELEV. 38$

.423'ABLE'i SO a.S

Qa 3aas 3.3. SS -reQS 2- Oi~ Vmve gCV Vgg

0 l4%4 ~ 3,300 f&N

3'-W V1S-

SMY. 3$

8.33'~

0

10 V2"

HOOCS

01 PPAS 1

CLCV SS1 ~ '3'COCS,S

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06-02-1 995 11:32 PROTO-FLO 2.01 by PROTO-POWER CORPORATIONUtility- DAPROTOFLOUIM.PD8 - Version

Plant - SystemHydraulic 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'-

Page 1

Pi e FromNode

1.00 NODE1

2.00 NODE2

3.00 NODE3

5.00 NODE5

10.00 NODE6

To Node

NODE2

NODE3

NODE4

NODE6

NODE6.5

ID(Inches

2.067

2.067

2.067

2.067

2.067

Flow DZ Velocity Reynolds Pressure Drop Hydraulic Resistancef//g m"2 ~si/g m"2

75.00 1.85 7.172 3.2281 E+05 5.314 2.235 9.4470 E-04 3.9739E-04

75.00 1A6 7.172 3.2281E+05 3.476 1.462 6.1800E-04 2.5996E-04

75.00 1.38 7.172 3.2281E+05 3.290 1.384 5.8494 E-04 2.4606E-04

75.00 0.38 7.172 3.2281 E+05 0.926 0.389 1.6470 E-04 6.9281 E-O

75.00 76.58 7.172 3.2281 E+05 178.083 74.911 3.1657 E-02 1.3317E-02

06-02-1 995 11:32

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5hech 5 oW h lPROTO-kO 2.01 by PROTO-POWER CORP@RATION Page 1

Utility- D:PROTOFLOUIM.PDB - VersionPlant - System

Pump Status Report

Manufacturer

NPSH Required: 5.90

Pump Name: 1-PP-46-1Drawings:Pump Status: BASTSpeed (RPM): 3,500 Flow (gpm): 75.00 Head (ft): 239.00Hydraulic Horsepower: 4.40Pump Impeller Elevation (ft): Inlet Node Elevation (ft): 588.53Pump Suction Temperature ('F) 180.00NPSH Curve: BAST NPSHNPSH Available: 5.97

Pump Name Manufacturer Model:

Head (ft):

Inlet Node Elevation (ft): 588.53

NPSH Required:

1-PP-46-2Drawings:Pump Status: OFFSpeed (RPM): 3,500 Flow (gpm):Hydraulic Horsepower:Pump Impeller Elevation (ft):Pump Suction Temperature ('F)NPSH Curve: BAST NPSHNPSH Available:

Ih

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06-02-1 995 11:32

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c~ 4 07PROT - LO 2.0'I by PROTO-POWER CO ~ RATION Page1

Utility- D:PROTOFLOUIM.PDB - VersionPlant- System

Boundary Condition Report

Node Name

NODE1

Bounda T e

Pressure Suction

8ounda Parameters

Pressure

ElevationS ecifiedTem erature

14.84 psia

589.43 tt180.00 'F

NODE10

NODE6.5

Pressure Discharge Pressure

ElevationS ecifiedTem erature

Pressure Discharge Pressure

ElevationSpecified Temperature

33.70 psia

592.50 ft180.00 'F

33.70 psia

592.50 tt180.00 'F

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~~,„;, hec.+ l c V06-02-1995 11:32 PROT'O 2.01 by PROTO-POWER CO~~RATION Page 1

Utility- D:<PROTOFLOUIM.PDB - VersionPlant - System

Combined Summary ReportConvergence: 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 = 7.172Turbulent f = 0.0200 Reynold's Number = 3.2281E+05

N1: NODE1 ** Press= „14.84 Elev= 589.43 Flow= 0.00N2'ODE2 Press= 12.98 Elev= 588.53 Flow= 0.00

Temp= 180.00Temp= 180.00

Pipe: 2.00 ID = 2.067 Flow= 75.00 Vel = 7.172Turbulent f = 0.0200 Reynold's Number = 3.2281E+05

N1: NODE2 Press= 12.98 Elev.= 588.53 Flow= 0.00N2: NODE3 Press= 11.52 Elev= 588.53 Flow= 0.00

Temp= 180.00Temp= 180.00

Pipe: 3.00 ID = 2.067 Flow= 75.00 Vel = 7.172Turbulent f = 0.0200 Reynold's Number = 3.2281E+05

N1: NODE3 Press= 11.52 Elev= 588.53 Flow= 0.00N2: NODE4 Press= 10.14 Elev= 588.53 Flow= .0.00

Temp= 180'.00Temp= 180.00

Pipe: 4.00 ID = 2.067N1'ODE4N2: NODE5

Flow = 75.00 NPSHA =5.97 NPSHR = 5.90Press= 10.14 Elev= 588.53 Flow= 0.00 Temp= 180.00Press= 110.67 Elev= 588.53 Flow= 0.00 .Temp= 180.00

Pipe: 5.00 ID = 2.067 Flow= 75.00 Vel = 7.172Turbulent f = 0.0200 Reynold's Number = 3.2281E+05

N1: NODE5 Press= 110.67 Elev= 588.53 Flow= 0.00N2: NODE6 Press= 110.28 Elev= 588.53 Flow= 0.00

Temp= 180.00Temp= 180.00

Pipe: 10.00 ID = 2.067 Flow = 75.00 Vel = 7.172Turbulent f = 0.0200 Reynold's Number = 3.2281E+05

N1: NODE6 Press= 110.28 Elev= 588.53 Flow= 0.00N2: NODE6.5 ** Press= 33.70 Elev= 592.50 Flow= 0.00

Temp= 180.00Temp= 180.00

- Fixed Pressure%% Pressure Below Vapor Pressure¹0 NPSHA less than NPSHR

II Reverse Flow Thru Check Valve++ Section Was Balanced&&Flow Past End of Pump Curve

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PROTERO 2.01 by PROTO-POWER COk~%RATION Pipe 1.00Utility- 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:

Valves: 1-CS437N I I

Misc K Fixed:

Pipe Flow Summary Title:

Tees: 1 Run; Branch Only; Branch

Elbows: Welded -, 2 90s, 45s; Threaded- 90s, 45s

Bends:

Entrances:Exits:

with angle =with angle =

,rid=,rid=

Abrupt Reductions from d =Abrupt Expansions to d =

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Utility- D:PROTOFLOUIM.PDB - VersionPlant - System

System Pipe Section Data Sheet

Pipe 2.00

From: NODE2 Elev: 588.53 To: NODE3 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: 4.00 Misc L/D:

Valves: 1-CS410/ I

Misc K Fixed:

Pipe Flow Summary Title:

Run;Tees:

Elbows: Welded- 90s,

1 Branch Only;

45s; Threaded-

Branch

90s, 45s

Bends:

Entrances:Exits:

with angle =

with angle =,rid=, r/d =

Abrupt Reductions from d =Abrupt Expansions to d =

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4c~W 50 oVPROTMLO 2.01 by PROTO-POWER COi'-~%) RATION - Pipe 3.00

Utility- D:PROTOFLOUIM.PDB - VersionPlant - 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:

Valves: 1-CS412-1 / I

Misc K Fixed:

Pipe Flow Summary Title:

Tees: 1 Run;

Elbows: Welded- 90s,

Branch Only;

45s; Threaded-

Branch

90s, 45s

Bends:

Entrances:Exits:

with angle =with angle =

,rid =,r/d=

Abrupt Reductions from d =Abrupt Expansions to d =

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PROTMLO 2.01 by PROTO-POWER CORFtlRATION Pipe 4.00

Utility- D:PROTOFLOUIM.PDB - VersionPlant - System

System Pipe Section Data Sheet

From: NODE4

Description:Drawings:

Elev: 588.53 To'ODE5

Fluid: Fresh Water

Elev: 588.53

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:

Elbows: Welded-

Run;

90s,

Branch Only;

45s; Threaded-

Branch

90s,

Bends:

Entrances:Exits:

with angle =with angle =

, r/d=, r/d =

Abrupt Reductions from d =

Abrupt Expansions to d =

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PROTS~~LO 2.01 by PROTO-POWER COP'O'ORATIONUtility- D:PROTOFLOUIM.PDB - Version

Plant - System

System Pipe Section Data Sheeth

Pipe 5.00

From: NODE5

Description:Drawings:

Elev: 588.53 To: NODE6

Fluid: Fresh Water

Elev: 588.53

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:

Elbows: Welded-

Run;

90s,

Branch Only;

45s; Threaded-

Branch

90s, 45s

Bends:

Entrances:Exits:

with angle =with angle =

, r/d=, r/d =

Abrupt Reductions from d =Abrupt Expansions to d =

\6/2/95 11:36:05 AM

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PROT'-r LO 2.01 by PROTO-POWER COPSQRATION Pipe 6.00Utility- 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:

Valves: 1-CS412-2/ /|

Misc K Fixed:

Pipe Flow Summary Title:

Tees: 1 Run; Branch Only; 1 Branch

Elbows: Welded- 90s, 45s; Threaded- 90s, 45s

Bends:

Entrances:Exits:

with angle =with angle =

, r/d =

, r/d =

Abrupt Reductions from d =

Abrupt Expansions to d =

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PROT LO 2.01 by PROTO-POWER CO " RATION Pipe 7.00Utility- 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:

Run;Tees:

Elbows: Welded- 90s,

Branch Only;

45s; Threaded-

Branch

90s, 45s

Bends:

Entrances:Exits:

with angle =with angle =

, r/d =

, r/d =

Abrupt Reductions from d =

Abrupt Expansions to d =

6/2/95 11:36:05 AM PROTKCLO 2.01 by PROTO-POWER CO%5RATIONUtility- D:>PROTOFLOUIM.PDB - Version

Plant - System

System Pipe Section'Data Sheet

Pipe 8.00

From: NODE8

Description:Drawings:

Elev: 588.53 To: NODE9

Fluid: Fresh Water

Elev: 588.53

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:

Entrances:Exits:

with angle =with angle =

,r/d =

, r/d=

Abrupt Reductions from d =Abrupt Expansions to d =

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PROT%--LO 2.01 by PROTO-POWER COB~" QRATION Pipe 9.00Utility- D:IPROTOFLOUIM.PDB - Version

Plant - System

System Pipe Section Data Sheet

From: NODE9

Description:Drawings:

Elev: 588.53 "To: NODE10 Elev: 592.50

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:

Valves: test-1/ /

Misc K Fixed:

Pipe Flow Summary Title:

Tees:

Elbows: Welded-

Run;

90s,

Branch Only;

45s; Threaded-

Branch

90s, 45s

Bends;

Entrances:Exits:

with angle =with angle =

, r/d =

, r/d=

Abrupt Reductions from d =Abrupt Expansions to d =

P6/2/95 11:36:05 AM

I

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S&c& Cl oW h3PROT(-'..LO 2.01 by PROTO-POWER CObQRATlON Pipe 10.00

Utility- D:PROTOFLOUIM.PDB - VersionPlant- 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:

Valves: test-1/ I

Misc K Fixed:

Pipe Flow Summary Title:

Run;Tees:

Elbows: Welded- 90s,

Branch Only;

45s; Threaded-

Branch

90s, 45s

Bends:

Entrances:Exits:

with angle =with angle =

, r/d =

, r/d =

Abrupt Reductions from d =Abrupt Expansions to 'd =

.E.D. RECORD COVER SHEET

'COOK NUGAE.EPR Pf.AFJNEO RECORD-NEO COPY

SECTION

ENGINEER

ET

O TE

PLAN LIFET!V(EDATE TO PlAM5

Cl NON PERMANENTMlwlMUR5RET 5TlO!4 YRS

C~CUIJ tILIO+[ g g~~g~K8 3++~+MpgL.r: .CV'.C

SUB JECT TQ: N.E.P. 6.4 (CALCULATIONS)N.E,P, 17.0 |.'RECORD RETENTION)N.E.P. 17,2 (HICROFILHING)

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NE-015(02/95)

DONALD C. COOK NUCLEAR PLANT

Section

DESIGN VERIFICATION CHECKLIST — CALCULATIONS

Calcula n Number <~~v-~we awaits Rev. c

Signature of Verifier1.0 Were the inputs correctly selected, incorporated and

documented into the calculation?Basis: MF ~ ufI~~ ~>3 ~ C4-/c~ /+Pe A'PJ H

Date

Mal cs cOcw I%4 J4 J ~/ Qe~ hlC.q r c,~M

2.0 Are assumptions necessary to perform the calculationadequately 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 regulatoryrequirements identif ied and requirements for designmet?

Basis: Af~ a~Yes N/A

4.0 Was an appropriate design method used?Basis: +l krJ &PS'A' nJc ~+<~>~

Yes ~ N/A

5.0 Is the output reasonable compared to input?Basis: '3 -™/ A M > ~ -+ ~ ~ T>

~u/J+6/0 .

Yes ~N/A

6.0 Are thy results numerically correct?Basis: > / a M ~e ~et / KME

Yes ~N/A

Pope 1 of 1

J 4g)

5E-914(o2/9s)

NUCLEAR ENGINEERING DEPARTMENTCalculation 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

TITLE ~> e~~v- ~>>We. us. Baaw Levai

RFC/MM/PM/PR/CR/TM No. ~ l~FILE LOCATION

CALCULATED BY:

~ VERIFIED BY:

APPROVED BY:

DATE

DATE~ +'zi/galDATE

CALCULATION DESCRIPTION: ~~~~~ i~~ ~~ ~v-~~ maMvb

~~a ~Re

~+%4 Wo w + ~CK&c4 'IX

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