ML20096E972
| ML20096E972 | |
| Person / Time | |
|---|---|
| Site: | LaSalle  |
| Issue date: | 05/11/1992 |
| From: | Landry A COMMONWEALTH EDISON CO. |
| To: | |
| Shared Package | |
| ML20096E925 | List: |
| References | |
| ATD-0117, ATD-0117-R00, ATD-117, ATD-117-R, NUDOCS 9205200119 | |
| Download: ML20096E972 (55) | |
Text
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l Calculation No. ATD-0117 Prop.ct No. 9012-26 Revision 0. Page 1
- Date: May 11, 1992 Evhluation'of.NPSH requirements for-HPCS, RHR, and RCIC i
. pumps and backpressure limitations of RCIC turbine following station blackout COMMONWEALTE EDISON COMPANY LASALLE COUNTY STATION UNITS 1 &-2' WIN.1218-SAFETY BEf2TED.
Prepared ~By:- N # M Date: I//'/TL Prepared By: NP lee h/, > > Date.. Y ^//- 2.'
Reviewed By: --
_,_, Date: -'*D Date: ~~ / '
Approved By: ./ . - -/M
~
9205200119-920515 .
. P D"t ADOCK 05000373
.P PDR'
Calculation No. ATD-0117 Project No. 9012-26 Revision 0- Page 2 TAELE OY CONTENTS i.C Title / Signature . . . . . . . . . . . . . . . . 1 2.0 Table of Contents . . . . . . . . . . . . . . . 2 3.0 Purpose & Scope . . . . . . . . . . . . . . . . 3 4.0 Design Input . . . . . . . . . . . . . . . . . . 4 I
- 5 . 10 .nssumptions . . . . .. . . . . . . . . . . . . 6 6.0 Approach . .. . . .. . . . . . . . . . . . . . . 7 7.0 Calculations .-. . . . . . . . . . . . . . . . . 9 8.0 Results . . . . . . . . . . . . . .. . . .. .- 11 9.0 Referonces . . .. . . . . . . . . . . . . . . . 12 10LO Attachments / Appendices . . . . . . . . . . -. . . 15 e
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Calculation 1No. ATD-011*/ - Project No. 9012-26 Revision Page 3 3.0 Purpose & Scope The purpose of this: calculation is to verify that following station blackout, NPSH requirements for RCIC, HPCS, and RHR-pumps are satisfied, and that the RCIC turbine backpressure does not exceed thu turbine trip limit.
To determine if the WPSH requirements of the pumps will-be
. met,-the highest-possible suppression. pool temperature, the lowest possible chamber _ pressure, and the lowest possible-pool- level following the station blackout cre considered.
l To determine if the RCIC turbine will trip due to high 7 ~
backpressure, the highest-possible chamber pressure, the-L highest possible pool level, and the highest.possible RCIC
~
L turbine exhaust-flow following:the station blackout are L. considered.
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b Calculation 2o. ATD-0117 Project No. 9012-26 Revision 0 Page 4 4.0 Desion Input
- 1. The-initial conditions of the suppression rool are taken from Reference 7.
- 2. Conservative conditions of the suppression pool following station blackout are taken from Reference la.
- 3. Conservativo conditions of the drywell following station blackout are taken from Reference Ib.
- 4. Minimum suppression pool water levels following station blackout are taken fron Reference id.
- 5. Required not positive-suction head values of 1.5 feet for the HPCS pump at a flow of 6250 RPM, 11.5 feet for cha RHR pump at a flow of 7200 GPM, 15 feet for the RCIC puup at a ficw of 600 GPM, and the limiting conditions.to meet these NPSH requirements are taken from Reference ic.
-6. The layout of the RCIC turbine exhaust piping is provided in Reference 2.
- 7. Pipe size and schedule for the RCIC turbine exhaust piping are taken from References 4 and 5.
- 8. The equations for velocity in a pipe and for Reynold's number are taken from Reference 10.
- 9. The equations for ideal gases and celative humidity and the values for the gas constants are taken from Reference 10.
- 10. Values for the losses associated with valves and fittings located in the RCIC turbine exhaust piping are provided in Reference 6b and Reference 8.
- 11. The valuer of temperature, pressure, and specific volume for saturated liquid water and saturated water vapor are taken from Reference 9. Where necessary, the values have been determined by linearly interpolating betwean the values in the table.
l'2. The valtes of internal energy for saturated liquid water and saturated water vapor are taken from Reference 11.
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Calculation No.1 ATD-0117 Project No. 9012-26 Revision 0 Page 5
- 13. The values for the viscosity of water and the friction factor, f, ..re taken from Reference 3.
14 . - The equation .'or frictional losses is taken from Reference 6a.
- 15. The setpoint for RCIC turbine trip.dte to high backpressure is 25 psig and is taken ' rom Reference 13.
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Calculacion No. ATD-0117 Project No. 9012-26 Revision 0 Page 6 5.0 $ssumpilons
- 1. Both the-drywell and the suppression chamber are assumed to be leak-tight.
- 2. The temperature of the suppression chamber is assumed to be the same as the pool temperature, and no credit is taken for heat transfer to the concrete and steel structures in the airspace.
- 3. To determine a low suppression chamber pressure for the -
evaluation of the pumps' NPSH requirements, pressure increases due to pool evaporation and drywell venting 3 are not considered.
4._ To determine a high suppression chamber pressure for the RCIC turbine backpressure analysis, 100% relative e
humidity is assumed.
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- 5. To determine an increase in pressure of the suppression chamber due to the venting from the drywell, an
.instanteous mass transfer of a homogeneous mixture of air and water vapor is acsumed to occur to balance the
_ pressure between the dryvell and the suppression chamber.
- 6. In the RCIC turbine backpressure analysis, all steam vented from the drywell to the suppression pool is
- assumed to condense.
- 7. In the RCIC backpressure analysis, it is aasumed that after the_RFV has been depressurized to 165 psia,_the RPV pressure will be maintained between 165 psia and 200 psia. Also, since RCIC turbine flow decreases as RPV pressure decreases, an exhaust flow is determined at an RPV pressure of 200 psia by linear interpolation of the exhaust flow versus RPV pressure data in Reference la.
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Calculation No. ATD-0117 Project No. 9012-26 Revision 0 Page 7 6.0 ADoroagh To determine if the net positive suction head requirements for the HFCS, RHR, and PClC pulps will be met following a station blackout, the worst case values of temperature and water level in the suppression pool and pr essuru in the suppression chamber are determined. Thir includes the lowest water level the pool would be expected to reach, the highest possible pool temperature, and the lowest possible suppression chamber pressure. The limiting conditior of these parameters such that the NPSH requirements of the pumps are met and that flashing does not occur in the suction piping are provided in Reference ic. Flashing occurs in the suction piping when the pressure of the water dropa below its vapor pressure.
Worst case conditions for NPSH of the RCIC pump are taken L four (4) hours and fifteen (15) minutes following station l blackout with the RCIC system used for decay heat removal.
l After this time, RPV pressure in decreased, and steam flow to the RCIC turbine is stopped, thus shutting off the RCIC pump. Worst case conditions for the HPCS and RHR pumps are taken four (4) hours and fifteen (15) minutes-following station blackout with the HPCS system used for decay heat removal (Reference la). At this time, pool cooling becomes available and the RHR pumps are started.
Reference la provides the maximum pool temperatures, and Reference 1d provides the low water levels. The pressure in the suppression chamber is calculated based on the temperature in the pool and air behaving as an ideal gas.
To be conservative, an increase in suppression chamber pressure caused by pool evaporation and drywell venting is not considered. If the suppression chamner pressure is less than the vapor pressure corresponding to the pool temperature, boiling has occurred. The conditions in the pool are then balanced to create thermodynamic equilibrium.
Reference Ic provides the limiting conditions of pool level and temperature and chamber pressure. The worst case values are then compared with the limiting conditions to determine in NPSH requirements are met.
To determine if the RCIC turbine will trip due to high backpressure, the pressure in the suppression chamber and the pressure-drop of the exhaust through the pipe and the rparger must be determined. To be conservative, the maximum possible suppression chamber pressure is calculated, the maximum water level is' determined, and the maximum RCIC I
turbine exhaust flow based on the pressure in the. reactor pressure vessel is used to calculate the pressure drop.
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Calculation No. ATD-0117 Project No. 9012-26 Revision 0 Page 8 The suppression chamber pressure is maximized by conservatively assuming the drywel: vents to the suppression chamber, and tnat a minimum pressure differential will exist. The pressure differential is based on the hydrostatic pressure that has to be overcome before the drywell can vent into the wetwell.
The maximum water level is calculated by using the conservative results of Reference la which maximizes steam and leakage flow into the suppression pool.
If the suppression chamber pressure and the pressure drop of the exhaust through the pipe and sparger are less than RCIC turbine backpressure trip setpoint, the turbine will not trip during the station blackout due to high backpressure.
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Calculation No. ATD-0117 Project No. 9012-26 Revision 0 Page 9 7.0 palculations-For details, see Attachment - 10.1 - Hand Calculations Evaluation of the RCIC Pump NPSH requirements:
NPSH g -(Pump Inlet Centerline) = 15 Feet Flow Rate- = 600 GPM Maximum Pool Temperature = 217.1'T Minimum Pool Level = 695'-0" Minimum Chamber Pressure = 19.1 psia NPSH g (Pump Inlet Centerline) = 22.6 Feet Minimum Water Pressuro - Vapor Pressure = 9.8 Feet
' Evaluation of the HPCS Pump NPSH Requirements:
1 NPSH g (Pump Inlet Centerline) = .'.5 Feet Flow Rate = 6250 GPM Maximum Pool Temperature = 234.2'F Minimum Pool Level = 695'-0" Minimum Chamber Pressure .
= 22.5 psia NPSH g (Pump Inlet Centerl.ine) = 16.5 Feet Minimum Water Pressure - VP.por Pressure = 9.2 Feet Evaluation of the RHR Pump NPSH Requiremente:
NPSH R (Pump Inlet Centerline) = 11.5 Feet
. Flow Rate- = 7200 GPM
. Maximum Pool Temperature = 234.2'F' Minimum Pool Lt. vel = 695'-0" Minimur Chamber Pressure .
= 22.5. psia NPSHg (Pump Inlet Centerline) = 16.2' Feet
. Minimum Water Pressure - Vapor Pressure = 9.2 Feet Evaluation of the RCIC Turbine Backpressure:
4 Hours Following Station Blackout RCIC Turbine Backpressure Trip Setpoint = 25 psig
-Maximum Chamber Pressure = 19.9 psig Maximum Water Level = 700'-2"
.RCIC' Turbine Exhaust Flow = 8910 lb/hr Friction Losses.Through Exhaust Pipe = 0.21 psi Pressure Drop Through Sparger = 2.95 psi Maximum RCIC Turbine Backpressure = 23.1 psig
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l calculation No. ATD-0117 Project No. 9012-26 I Revision 0 Page 10
, 4 Hours and 15 Minuta; Following Station Blackout RCIC Turuine Backpressure Trip Setpoint = 25 psig Maximum Chamber Pressure = 21.3-psig Maximum Water Level = 700'-4" RCIC Turbine Exhaust Flow = 8910 lb/hr Friction Losses Through Exhaust Pipe = 0.21 psi Pressure Drop Through Sparger = 3.02 psi Maximum RCIC Turbine Backpressure = 24.5 psig l
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= Calculation No. ATD-0117 Project No. 9012-26 Revision 0 Page 11 8.0 ,Results NPSH requirements for the RCIC, HPCS, and RHR pumps will be met following a station blackout. The required NPSH for the RCIC pump at 600 GPM is 15 feet, and the available NPSH is 22.6 feet. The required NPSH for the HPCS pump at 5250 GPM is 1.5 feet, and the available NPSH is 16.5 feet. The required NPSH for the RHR pump at 7200 GPM is 11.5 feet, and the available NPSH is 16.2 feet.
The RCIC turbine will not trip due to high back pressure following a station blackout. The backpressure trip setpoint is 25 psig, and the maximum calculated backpre.asure is 23.1 psig fours' hours following station blackout and 24.5 psig fours hours and 15 minutes following station blackout.
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calculati"a No. ATD-0117 Project No. 9012-26 Revision 0 Page 12 9.0 References
- 1. Sargent & Lundy Calculations:
- a. 3C7-0390-001, Revision 1, 5-11-92, Suppression Pool Temperature Transient Following Station "lackout L. 3C7-0390-002, Revision 1, 5-11-92, Drywell Temperature Transient Following Station Blackout
- c. ATD-0070, Revision 1, 3-25-92, Limiting Operating Conditions for Net Positive Suction Head (NPSH) for HPCS, LPCS, RCIC, and RHR Pumps l
l d. 3C7-0189-001, Revision 2, 5-21-90, LaSalle Station
- Blackout Condensate Inventory Copying Assessment
- 2. Sargent & Lundy Piping Drawings:
- a. M-844, Sheet 1, Revision AT, Reactor Core Isolation Coolant-Piping, LaSalle County Station, Unit 1
- b. M-844, Sheet 2, Revision AF, Reactor Core Isolation Coolant Piping, LaSalle County Station,
-Unit 1
- c. M-844, Sheet 3, Revision-AC, Reactor Core Isolation Coolant Piping, LaSalle County Station, Unit 1
- d. M-844, Sheet 4, Revision AK, Reactor Cure-Isolation Coolant Piping, LaSalle County Station, Unit 1
- e. M-844, Sheet 5, Revision AG, Reactor Core Isolation Coolant Piping, LaSalle County Statien, Uni". I
- f. M-944, Sheet 1, Revision W, Reactor Core Isolution Coolant Piping, LaSalle County-Station, Unit 2
- g. M-944, Sheet _2, Revisiorn P, Reactor Core Isolation Coolant Piping, LaSalle County Station, Unit 2 L h. M-944, Sheet 3, Revision R, Reactor Core Isolation Coolant Piping, LaSalle County Station, Unit 2
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t Calcul' ation"No.=ATD-0117. Project No. 9012-26 Revision 0- Page 13
(
i.- iM-944, Sheet 4, Revision V, Reactor Core Isolation: '
Coolant-Piping, LaSalle County Station, Unit 2 j., M-944, Sheet 5,7 Revision T, Reactor Core Isolation Coolant Piping,-LaSalle County Stction, Unit 2
- 3. LaSalle County-Station, Units 1 & 2, Sargent &-Lundy-
-Mechanical Drawing-List, 4-03-92
- 4. Sargent &:Lundy Line List Drawings:
- a. M-3101, Revision AL, Reactor Core Isolation Coolant: System Line List, LaSalle County Station, Unit 1-
- b. M-3147,IR evision AG, Reactor Core Isolation CoolantLSystem Line List, LaSalle County Station,-
Unit 2=
- 5. _ Pip'ing Design Table "105LS" Revision D, LaSalle County Station ,
- 6. . ;Sargent;& Lundy.-Mechanical. Standards:
a.- MES-2.10,-Revision =F, Pipe Sizing-Data
- b. MES-2.16, Revision E,' Pressure Dropt Fittings, Valves,:& Discontinuities.-
- c. MAS-22, ~ Revision E, _-.-Preparation,:- Review &- Approval of Mechanical Department Design Calculations
-7 1 LaSalle County Station'0FSAR,LVolume V, Chapter 6,.
Engineered Safety Features,ERevision:8,L4-17-92.-
- 8. Crane Technical Paper'410,-1988 Printing
- 9. ,ASME Steam Tables, 1967 Edition-
- 10. Marks' Standard Handbook.for Mechanical Engineers, Ninth Edition y _
11.1 Fundamentals"offClassical. Thermodynamics, 3rd Edition,
~
- Wylen &'Sonntag~-.1985
- 12. .Sargent.& Lundy Instrument Data' Sheet'PS00-C, Revision 1 X, LaSalle. County Station, Units.1 & 2 11 3 . . Sargent &.Lundy1 Instrument Data Sheet:PS248, Revision
- . A,' Pressure Switches' LaSalle County' Station, Units 1 &
V ~2 4
+ -w ., ., r
M Calculation No. ATD-0117 Project No. 9012-26 Revision 0 Page 14
- 14. User's Manual for Compare /MODT-PC Computer Program (03.7.322-1.0), 1-28-92
- 15. - Sargent-& Lundy Structure Drawing S-325, Revision P, Reactor Containment Liner Plate Cross Section, LaSalle County Station, Unit 1
- 16. LaSalle County Station, Units 1 & 2, Sargent & Lundy Structural Drawing List, 4-03-92
- 17. Mechanical Engineering Reference Manual, Michael R.
Lindeburg, 8th Edition, 1990.
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Calculation No.'ATD-0117 Project No. 9012-26 Revision 0 Pago 15 10.0-Attachmet.to 10.1 Hand Calculations (39 Pages) r
1 Cal . NO. ST C C "7 REV!?W METHOD SHEET Revisien a Fage !. ':.-y n Proj. No. 'fa2 -3 This calculation has been reviewed by me according to the method (s) checked below.
- 1. Computer Aided Calculations a Revie. te oete nine tnat tne compuse p ogramts) nas esen vaticateo ano oocumenteo, is suitat ie to tne p octee oeing analyseo, ano tnat tne cateviation contains ati necessary infernietion fo reconstruction at a inter cate.
-o .nevie. to oetermine snet tne inout cata as specifieo for program execution is consist-ent witn tne oesign inous, co-rectiy oef ices tne p-ooiem for tne comouter algo-itnm ano ib su* f ic ient l y accurate to croouce results witnin any numerical limitations of tne prog afr ,
c Revie. to ve-i*y tnat tne resuits cotaineo from tne progesm are correct anc witnin stateo assum.9tions ano limatations of the prog *am ano are consistent with the inout.
c Revie. valioation cocumentatio* for temporary changes to itsteo or oewelormentai, or unsoue singie acclicatica programs, to assure tnat metnoes useo aceountely velicate
!- tne p*oprae for tne intenceo application. .-
t-
- -- e -Gevie. of cooe inout ont>. since tne comouta program nas sufficient history of use li at Sa pe.i & t,uno, in simitar caiculations.
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- l. f- Revie. a-itnme* c necessa 3 te p-eosee coce incut cata.
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- 2. Hand Prepared Design Calculations a
[ Detailes revie. of the e-iginai calcJiations.
o noview ey a, atte-nate, e m.pisfies, e- aco-ori te . tnoo of emicuistion.
nevie ef a r o-esantative sampi of remetitive calcuistions, e
o Review of tne calculation ap.16st 2 similar Cal *vlation previously 94Pf0fmeo.
- 3. Revisions a Ecitorial enanges emiv.
~o E15minat'en of unacorovec input cata without altering calculateo results c Other; p
- 4. Other i-Revie.er; , [g Cate ~p V AM.* F ORV. e7[ V I E W. i C2#19!65 i
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