BVY 04-081, Vermont Yankee Nuclear Power Station, Technical Specification Proposed Change No. 263 - Supplement No. 11 Extended Power Uprate - Response to Request for Additional Information
| ML042320080 | |
| Person / Time | |
|---|---|
| Site: | Vermont Yankee  |
| Issue date: | 08/12/2004 |
| From: | Thayer J Entergy Nuclear Northeast, Entergy Nuclear Operations |
| To: | Document Control Desk, Office of Nuclear Reactor Regulation |
| References | |
| BVY 04-081, TAC MC0761 | |
| Download: ML042320080 (131) | |
Text
Entergy Nuclear Northeast Entergy Nuclear Operations, Inc.
Vermont Yankee 185 Old Ferry Rd.
a_,Brattleboro, VT 05302 Tel 802-257-5271 August 12, 2004 Docket No. 50-271 BVY 04-081 TAC No. MC0761 ATTN: Document Control Desk U.S. Nuclear Regulatory Commission Washington, DC 20555-0001
Subject:
Vermont Yankee Nuclear Power Station Technical Specification Proposed Change No. 263 - Supplement No. 11 Extended Power Uprate - Response to Request for Additional Information
Reference:
- 1) U.S. Nuclear Regulatory Commission (Richard B. Ennis) letter to Entergy Nuclear Operations, Inc. (Michael Kansler), "Request for Additional Information - Extended Power Uprate, Vermont Yankee Nuclear Power Station (TAC No. MC076 1), NW 04-057, July 6, 2004
- 2) Entergy Nuclear. Operations, Inc. (Jay K. Thayer) letter to U.S. Nuclear Regulatory Commission, "Vermont Yankee Nuclear Power Station, Technical Specification Proposed Change No. 263 - Supplement 10, Extended Power Uprate - Response to Request for Additional Information, BVY 04-074, July 30, 2004 This letter responds to NRC's request for additional information (RAI) of July 6, 2004 regarding the application by Entergy Nuclear Vermont Yankee, LLC and Entergy Nuclear Operations, Inc.
(Entergy) for a license amendment to increase the maximum authorized power level of the Vermont Yankee Nuclear Power Station (VYNPS) from 1593 megawatts thermal (MWt) to 1912 MWt. By letter dated July 30, 2004 (Reference 2), Entergy had provided a partial response to the NRC's RAI. Attached are responses to the two RAls (designated as SPSB-C-32 and SPSB-C-33) that were not addressed in Reference 2. to this letter provides Entergy's response to the two RAls. Because each RAI response contains proprietary information as defined by 10CFR2.390, Attachment 1 has been designated in its entirety as proprietary information. A non-proprietary version, suitable for public disclosure, is provided as Attachment 2 to this letter with the proprietary information redacted. An affidavit that constitutes a request for withholding of the proprietary information in from public disclosure in accordance with NRC regulations is provided by the owner of the proprietary information (General Electric Company (GE)) as Attachment 3. The proprietary information in Attachment 1 is designated by double underline within double square brackets. In each case, the superscript notation, "{3)", refers to paragraph (3) of the affidavit, which provides the basis for the proprietary determination. The proprietary information has 1b
BVY 04-081 Docket No. 50-271 Page 2 of 3 been handled and classified as proprietary, customarily held in confidence, and withheld from public disclosure. The proprietary information contained in the responses to the RAls was provided to Entergy in a GE transmittal that is referenced by the affidavit. The proprietary information has been faithfully reproduced in the enclosed RAI responses such that the affidavit remains applicable. GE requests that the enclosed proprietary information be withheld from public disclosure in accordance with the provisions of 10CFR2.390 and 10CFR9.17.
There are no new regulatory commitments contained in the responses to the RAls.
This supplement to the license amendment request provides additional information to clarify Entergy's application for a license amendment and does not change the scope or conclusions in the original application, nor does it change Entergy's determination of no significant hazards consideration.
If you have any questions or require additional Information, please contact Mr. James DeVincentis at (802) 258-4236.
I declare under penalty of perjury that the foregoing Istrue and correct.
Executed on August /2 , 2004.
Sincerely, (Jay/K. Thayer Site Vice President Vermont Yankee Nuclear Power Station Attachments (3) cc: (see next page)
BVY 04-081 Docket No. 50-271 Page 3 of 3 cc: Mr. Richard B. Ennis, Project Manager Project Directorate I Division of Licensing Project Management Office of Nuclear Reactor Regulation Mail Stop 0 8 B1 Washington, DC 20555 Mr. Samuel J. Collins Regional Administrator, Region I U.S. Nuclear Regulatory Commission 475 Allendale Road King of Prussia, PA 19406-1415 USNRC Resident Inspector Entergy Nuclear Vermont Yankee, LLC P.O. Box 157 Vemon, Vermont 05354 Mr. David O'Brien, Commissioner VT Department of Public Service 112 State Street - Drawer 20 Montpelier, Vermont 05620-2601
BVY 04-081 Docket No. 50-271 Attachment 2 Vermont Yankee Nuclear Power Station Proposed Technical Specification Change No. 263 - Supplement No. 11 Extended Power Uprate Response to Request for Additional Information REDACTED AND NON-PROPRIETARY INFORMATION Total number of pages In Attachment 2 l (exciudina this cover sheet) is 123. '
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 1 of 123 NON-PROPRIETARY INFORMATION RESPONSE TO REQUEST FOR ADDITIONAL INFORMATION RELATED TO EXTENDED POWER UPRATE REQUEST VERMONT YANKEE NUCLEAR POWER STATION PREFACE The following information is provided in response to NRC's request for additional information (RAI) dated July 6, 2004, regarding the application by Entergy Nuclear Vermont Yankee, LLC and Entergy Nuclear Operations, Inc. (Entergy) for a license amendment to increase the authorized thermal power level of the Vermont Yankee Nuclear Power Station. By letter dated July 30, 2004 (BVY 04-074), Entergy had provided a partial response to the NRC's RAI. This Attachment contains responses to the two RAls (designated as SPSB-C-32 and SPSB-C-33) that were not addressed in the July 30, 2004 response.
The individual RAls are repeated as provided in NRC's letter of July 6, 2004.
The subject RAls have been discussed during conference calls held between the staffs of the NRC and Entergy to further clarify the information needs of the NRC staff. In certain instances the RAls may have been modified based on clarifications and understandings reached during the telecons. The information provided herein is consistent with those understandings.
PROPRIETARY INFORMATION This Attachment 2 is identical to Attachment 1 of Entergy letter BVY 04-081, except it has been edited to remove Proprietary Information. The removed information has been deemed to be proprietary to the General Electric Company. Instances where proprietary information was deleted from the text are identified by double square brackets. The basis for the proprietary information is contained within the affidavit provided as .
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 2 of 123 NON-PROPRIETARY INFORMATION Probabilistic Safety Assessment Branch (SPSB)
Containment and Accident Dose Assessment Section (SPSB-C)
RAI SPSB-C-32 Please provide input to the computer calculation (data in ASCII format) of the minimum containment accident pressure used for ECCS pump NPSH calculations for the double ended guillotine break of a recirculation line. Please verify that the input is consistent with the VYNPS emergency operating procedures. In addition, provide a schematic of containment with dimensions and ECCS schematic for this analysis. The input parameters needed are included in Attachment 1. [Attachment 1 is not repeated here.]
Response to RAI SPSB-C-32 Table SPSB-C-32-1 contains inputs used for the M3CPT/LAMB DBA-LOCA short-term analyses used to determine the peak DBA-LOCA drywell pressure. Table SPSB-C-32-1 also provides the inputs used for the DBA-LOCA short-term (600 second) and long-term (10 day) SHEX analyses used to calculate the containment response for NPSH evaluations. These inputs are consistent with the VYNPS emergency operating procedures.
Table SPSB-C-32-2A provides the core shutdown power used in the M3CPT/LAMB DBA-LOCA analyses for peak drywell pressure. Table SPSB-C-32-2B provides the core shutdown power used in the SHEX containment analyses. The values shown are normalized to the initial reactor power. The core shutdown power used in the M3CPT/LAMB calculation is that used for the LAMB break flow calculations which are performed in accordance with 10CRF50 Appendix K. The core shutdown power used in the LAMB break flow calculations includes fission power, fuel relaxation energy and decay heat based on the ANS 5-1971 decay heat model + 20 %. The shutdown power used in the SHEX analyses include fission power, fuel relaxation energy, metal-water reaction and decay heat based on ANS 5.1-1979 + 2 sigma with additional actinides and reactive products per SIL 636 Revision 1. The containment codes calculate the core shutdown power at each time step by multiplying the initial reactor power by the normalized core shutdown power obtained by interpolation of the tabular values. The initial core thermal power used in the analysis is assumed to be 2%higher than the rated core thermal power per Reg. Guide 1.49 (see response to RAI SPSB-C-4). For information, the core power calculated by the SHEX code at each time step (in Btu/sec) using Table SPSB-C-32-2B has been provided in Tables SPSB-C-32-5 and SPSB-C 6 (see Column labeled mCore Thermal Power").
Tables SPSB-C-32-3A and SPSB-C-32-3B provide ECCS and RHR pump heat vs. time for the SHEX short-term (600 second) and long-term (10 day runs) analyses.
Table SPSB-C-32-4 (M3CPT for peak drywell pressure), Table SPSB-C-32-5 (SHEX 600 second analysis for NPSH) and Table SPSB-C-32-6 (SHEX 10 day analysis for
Attachment 2 to BVY 04081 Docket No. 50-271 Page 3 of 123 NON-PROPRIETARY INFORMATION NPSH) provide time depended data requested by the RAI and referred to in Table SPSB-C-32-1 except for the data in Tables SPSB-C-32-2A and SPSB-C-32-2B which provide the normalized core shutdown curves. The data provided in Tables SPSB-C 4, SPSB-C-32-5 and SPSB-C-32-6 are obtained from the computer run output.
Figure SPSB-C-32-1 shows a schematic of the SHEX containment model.
Attachment 2 to BW 04-081 Docket No. 50-271 Page 4 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-1 Innuts to Containment Analyses for Peak Drvwell Pressure and for Evaluation of NPSH Parameter \ Case Unit Short-Term Short-Term Long-Term DBA-DBA-LOCA for (600 s) DBA- LOCA for NPSH Peak Drywell LOCA for NPSH Pressure GE Computer Code used M3CPT SHEX SHEX Containment Geometr Parameters See Note 3 See Note 3 See Note 3 Drywell (including free volume of ft3 128,370 128,370 128,370 vents at low suppression pool water level)
Drywell hold up volume (i.e. pool ft3 Not Modeled Not Modeled Not Modeled volume prior to falling into the vents)
Wetwell Airspace ft3 103,932 105,900 105,900 Suppression Pool ft3 70,000 68,000 68,000 Initial Suppression pool depth ft T/S HWL TIS LWL T/S LWL 11.27 11.03 11.03 No. of Downcomers 96 96 96 Downcomer Diameter ft 1.958 1.958 1.958 Loss coefficient for vent system 5.17 5.17 5.17 including entrance and exit losses based on vent exit (total downcomer) flow area(S)
Downcomer Submergence (Vents) ft 4.54 (TS-HWL) 4.05 (TS-LWL) 4.05 (TS-LWL)
Vent Lengths See Note 5 See Note 5 See Note 5 Initial Conditions Initial Drywell Pressure psig 1.92 1.7 1.7 Initial Wetwell Pressure psig 0.0 0.0 0.0 Initial Drywell Temperature OF 135 170 170 Initial Wetwell Temperature OF 90 90 90 Initial Drywell Relative Humidity % 20 100 100 Initial Relative Humidity % 100 100 100
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 5 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-1 Inputs to Containment Analyses for Peak Drvwell Pressure and for Evaluation of NPSH Parameter I Case Unit Short-Term Short-Term Long-Term DBA-DBA-LOCA for (600 s) DBA- LOCA for NPSH Peak Drywell LOCA for NPSH Pressure Heat Structure Properties Drywell Heat Sink for Internal Metal Not Modeled Structures and Vents (Steel)
Surface Area (facing drywell air) ft2 NA 19,405 19,405 Mass Ibm NA 637,000 637,000 Thickness ft NA 0.067 0.067 Specific Heat Btu/Ibm- 0F NA 0.11 0.11 Thermal Conductivity Btu/hr-ft-OF NA 26 26 Drywell Heat Sink for Internal Not Modeled Concrete Structures Surface Area (facing drywell airspace) ft2 NA 2068 2068 Mass Ibm NA 1,004,995 1,004,995 Thickness ft NA 4 4 Specific Heat Btu/Ibm- 0 F NA 0.2 0.2 Thermal Conductivity Btu/hr-ft-0 F NA 0.54 0.54 Wetwell Airspace Heat Sink for Not Modeled Torus Steel Shell Surface Area (facing wetwell ft2 NA 14,596 14,596 airspace)
Mass Ibm NA 479,176 479,176 Thickness ft NA 0.067 0.067 Specific Heat Btullbm-PF NA 0.11 0.11 Thermal Conductivity Btulhr-ft-OF NA 26 26 Suppression Pool Heat Sink for Not Modeled Torus Steel Shell Surface Area (facing suppression ft2 NA 12,136 12,136 pool water)
Mass Ibm NA 398,436 398,436
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 6 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-1 Inputs to Containment Analyses for Peak Drvwell Pressure and for Evaluation of NPSH Parameter I Case Unit Short-Term Short-Term Long-Term DBA DBA-LOCA for (600 s) DBA- LOCA for NPSH Peak Drywell LOCA for NPSH Pressure Thickness ft NA 0.067 0.067 Specific Heat Btu/Ibm- 0 F NA 0.11 0.11 Thermal Conductivity Btu/hr-ft-OF NA 26 26 Wetwell-to-Drywell Vacuum Not Modeled Modeled Modeled Breakers Number (Number of multiple valve NA 2(M) 2 (M) systems (M) with 2 valves per line, 6 (S) 6 (S) number of single valve systems (S) with I valve per line Flow Area (per Vacuum Breaker ft2 NA 2.95 (M) 2.95 (M)
System) 1.62 (S) 1.62 (S)
Differential Pressure Setpoint psid NA 0.5 0.5 Opening Time sec NA 1 1 Loss Coefficient (per Vacuum Breaker NA 1.67 (M) 1.67 (M)
System) 2.69 (S) 2.69 (S)
RX BuildinB-to-Wetwell Vacuum Not Modeled Not Modeled Not Modeled Breakers Number NA NA NA Flow Area (per Vacuum Breaker ft2 NA NA NA System)
Differential Pressure Setpoint psid NA NA NA Opening Time sec NA NA NA Loss Coefficient (per Vacuum NA NA NA Breaker)
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 7of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-1 Inputs to Containment Analyses for Peak Drywell Pressure and for Evaluation of NPSH Parameter \ Case Unit Short-Term Short-Term Long-Term DBA DBA-LOCA for (600 s) DBA- LOCA for NPSH Peak Drywell LOCA for NPSH Pressure Containment Leakage %by weight Not Modeled 1.5 1.5 of initial See Response to See Response to containment RAI SPSB-C30 RAI SPSB-C30 mass per for description of for description of day containment containment leakage modeling leakage modeling Drywell to Reactor Building, Area and Not Modeled Not used. Not used Loss Coefficient See Response to See Response to RAI SPSB-C30 RAI SPSB-C30 for description of for description of containment containment leakage modeling leakage modeling Drywell to Reactor Building, Area and Not Modeled Not used. Not used.
Loss Coefficient See Response to See Response to RAI SPSB-C30 RAI SPSB-C30 for description of for description of containment containment leakage modeling leakage modeling Containment Snravs Drywell Spray Flow rate Ibm/sec Not Modeled Not Modeled 924.35 (Constant value starting at 600 seconds)
Drywell Spray Enthalpy Btu/lbm Not Modeled Not Modeled See Table SPSB-C-32-6 Column Labeled 'Drywell and Wetwell Spray Enthalpy" (See Note 10)
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 8 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-1 Inputs to Containment Analyses for Peak Drwell Pressure and for Evaluation of NPSH Parameter I Case Unit Short-Term Short-Term Long-Term DBA-DBA-LOCA for (600 s) DBA- LOCA for NPSH Peak Drywell LOCA for NPSH Pressure Initial Spray Droplet Size ft Not Modeled Not Modeled 0.002625 Wetwell Spray Flow Rate Ibm/sec Not Modeled Not Modeled 48.65 (constant flow rate starting at 600 seconds) (constant flow rate starting at 600 seconds)
Wetwell Spray Enthalpy Btullbm Not Modeled Not Modeled See Table SPSB-C-32-6 Column Labeled ODrywell and Wetwell Spray Enthalpy' See Note 10 Initial Spray Droplet Size ft Not Modeled Not Modeled 0.0039 Initial RPV Water Level Inches 504 (2) 504(2) 504(2)
Above Vessel Zero Break Area Data Break Size 7.327(1) 4.16(1) 4.16(')
Recirc Suction Pipe Inside in 25.917 See Note I See Note 1 Diameter at Break Location Vessel Nozzle Inside Diameter in 25.75 See Note I See Note I Jet Pump Nozzle Inside Diameter in 3.115 See Note I See Note 1 Number of Jet pumps per loop in 10 See Note I See Note 1 Number of nozzles per jet pump in I See Note I See Note 1 SRV Performance Not Modeled Not Modeled Not Modeled SRV Discharge flow mass and NA NA NA energy vs. time Number NA NA NA
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 9 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-1 Innuts to Containment Analyses for Peak Drywell Pressure and for Evaluation of NPSH Parameter Case Unit Short-Term Short-Term Long-Term DBA DBA-LOCA for (600 s) DBA- LOCA for NPSH Peak Drywell LOCA for NPSH Pressure Diameter In. NA NA NA Differential pressure setpoint psid NA NA NA Opening time sec NA NA NA Loss Coefficient NA NA NA Break Critical Flow Model"2) Moody SLIP HEM HEM Break Flow Rates See Table SPSB- See Table SPSB- See Table SPSB-C-324(6) C-32-507) C-32-4)
Decay Heat vs. Time Initial Reactor Power MWt 1950 (102% of 1950 (102% of 1950 (102% of EPU Reactor EPU Reactor EPU Reactor Thermal Power) Thermal Power) Thermal Power)
Normalized Core Shutdown See Table See Table See Table Power vs. Time SPSB-C-32-2A SPSB-C-32-2B SPSB-C-32-2B Pump Heat vs. Time HP Not Modeled See Table SPSB- See Table SPSB-C-32-3A C-32-3B ECCS Injection Flow Rates and Enthal__
LPCI Pumps Not Modeled
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 10 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-1 Inputs to Containment Analyses for Peak Drvwell Pressure and for Evaluation of NPSH Parameter \ Case Unit Short-Term Short-Term Long-Term DBA-DBA-LOCA for (600 s) DBA- LOCA for NPSH Peak Drywell LOCA for NPSH Pressure Number of Operating LPCI Pumps NA 4 pumps In LPCI 4 in LPCI vessel vessel injection injection mode mode before 600 sec (See discussion 2 pumps in LPCI in note 7 mode. I LPCI regarding LPCI pump turned off.
njection modeling Remaining LPCI to intact and pump aligned in broken RHR containment recirculation spray mode after loops) 600 sec Pump Heat (per LPCI Pump) hp NA 1001.6 1001.6 Core Spray (CS) Pumps Not Modeled Number of Operating Pumps NA 2 2 Pump Heat (per CS Pump) hp NA 562.2 562.2 ECCS Flow Rate and Enthalpy See Note 9 See Note 9 Total ECCS - LPCI plus CS Pump Ibm/sec Not Modeled See Table SPSB- See Table SPSB-Flow Rate to RPV from suppression C-32-5 C-32-6 pool See Column See Column labeled "ECCS labeled ECCS flow to RPV" flow to RPV" Enthalpy of ECCS (LPCI and CS) Btu/Ib Not Modeled See Table SPSB- See Table SPSB-flow to RPV from suppression pool C-32-5 C-32-6 See Column See Column labeled NECCS labeled 'ECCS flow enthalpy flow enthalpy from suppression from suppression
_ pool. pool' RHR Heat Exchanaer Performance Heat Exchanger K-factor (per HX) Btu/sec-OF NA NA 179.375 (See Note 11)
RHR Service Water Temperature OF NA NA 85
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 11 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-1 Inputs to Containment Analyses for Peak Drvwell Pressure and for Evaluation of NPSH Parameter Case Unit Short-Term Short-Term Long-Term DBA DBA-LOCA for (600 s) DBA- LOCA for NPSH Peak Drywell LOCA for NPSH Pressure Number of RHR Loops (1 HX per Not Modeled Not Modeled 1 loo p) _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _
Number of RHR pumps per RHR loop NA NA I Pump Heat per RHR pump hp NA NA 1001.6
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 12 of 123 NON-PROPRIETARY INFORMATION Notes for Table SPSB-C-32-1:
(1) The break area shown for the LAMB analysis corresponds to the sum of the two sides of the broken recirculation suction line pipe at the break location. Note that shortly after the DBA-LOCA occurs, the LAMB break flow is limited by the choked flow which exists at the locations with minimum flow area upstream of the break.
The break area shown for the SHEX analysis is the sum of the minimum flow area upstream of the vessel side of the break (vessel safe end nozzle) and minimum flow area upstream of the pipe side of the break get pump nozzles).
(2) The RPV water level shown corresponds to the water level outside the core shroud. This value is used to calculate the liquid volumes within the LAMB vessel model and also to calculate the liquid volume in the VYNPS SHEX vessel model.
(3) The containment geometry parameters given for the M3CPT analyses correspond to conditions associated with the Technical Specification Suppression pool High Water Level (TS-HWL). The values given for the SHEX analyses correspond to conditions associated with the Technical Specification Suppression pool Low Water Level (TS-LWL).
(4) Not used.
(5) ((
(6) The break flow rate shown for the M3CPT/LAMB analysis for peak drywell pressure is calculated by the LAMB code based on the Moody SLIP critical break flow model. The values to 20 seconds have been provided which covers the time period past the time of the peak drywell pressure.
(7) The break flow for the "short-term" (600 second) SHEX analyses for evaluating NPSH includes two components. These components include; 1) break flow to the drywell from the vessel 2) direct LPCI break flow to the drywell which originates at the suppression pool.
The first component is the vessel break flow. The vessel break flow to the drywell is calculated using conditions in the vessel and the break area. The break flow rate for this component has an enthalpy corresponding to enthalpy of the vessel liquid.
See Table SPSB-C-32-5 for time varying vessel break flow data. The data in the columns labeled: "Vessel Liquid Break Flow Rate,' "Vessel Liquid Break Enthalpy,"
'Vessel Vapor Break Flow Rate," and WVessel Vapor Break Enthalpy' provide time histories of the vessel break flow and enthalpy.
The second component is the direct LPCI flow to the drywell. For this analysis it is assumed that 2 LPCI pumps inject into the broken recirculation loop. The LPCI
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 13 of 123 NON-PROPRIETARY INFORMATION flow to the broken loop is assumed to flow directly to the drywell. This break flow has an enthalpy corresponding to the enthalpy of the suppression pool water (plus additional energy added by the LPCI pumps). The LPCI break flow rate equals the LPCI pump flow rate into the broken recirculation loop. Table SPSB-C-32-5 contains the LPCI break flow data. The LPCI break flow rate and break flow enthalpy is provided by the data in the columns labeled: "Direct LPCI Break Flow to Drywell" and "Enthalpy of Direct LPCI Break Flow to Drywell."
(8) The break flow for the "long-term" (10 day) SHEX analyses for evaluating NPSH includes only includes break flow to the drywell from the vessel. It is assumed for this analysis that all LPCI flow is injected to the vessel. See Table SPSB-C-32-6 for time varying vessel break flow data for this analysis. The data in the columns labeled: "Vessel Liquid Break Flow Rate," WVessel Liquid Break Enthalpy," "Vessel Vapor Break Flow Rate," and "Vessel Vapor Break Enthalpy" provide time histories of the vessel break flow and enthalpy.
(9) Note, the ECCS flow rates shown In Tables SPSB-C-32-5 and SPSB-C-32-6 (column labeled "ECCS flow to RPV") are the combined LPCI plus CS flow to the vessel. The flow enthalpy (Column labeled "ECCS flow enthalpy from suppression pool") is the enthalpy of the flow from the suppression pool not including the energy added by the pump heat.
(10) Note the containment spray flow enthalpy in Table SPSB-C-32-6 (Column labeled "Drywell and Wetwell Spray Enthalpy") is the enthalpy of the flow into the drywell and wetwell airspace and includes the RHR pump heat.
(11) The heat removal rate is calculated in SHEX with the following relationship:
Q = K x(T 1,-Tw) Btu/sec Where:
Q = Rate of heat removal per heat exchanger (Btu/sec)
T= RHR shell side inlet temperature (= suppression pool temperature)
T= Service water inlet temperature (12) The Moody Slip critical break flow model is used for the LAMB break flow calculations which are subsequently input to M3CPT peak drywell pressure calculation. The Moody Slip critical break flow is the same as used in the Appendix K ECCS/LOCA analyses and is conservative relative to the HEM model. The SHEX analyses use the HEM critical break flow model which is consistent with the critical break flow model identified for use during the Mark I Long-term Containment Program (NEDO-21888, NUREG-0661). Additionally, the key parameters obtained from the long-term containment response analysis (e.g., peak suppression pool temperature) occur well after the end of the vessel blowdown.
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 14 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-2A Normalized Core Shutdown Power for VYNPS Extended Power Uorate LAMBIM3CPT Peak Drvwell Pressure (Sum of Fission Power. Decay Heat and Fuel Relaxation Enerav)
(Decay Heat based on ANS 5 -1971 decay heat + 20%)
Time (sec) Normalized Shutdown Power 0.0 1.000 1.0 0.938 2.0 0.826 3.2 0.711 4.0 0.647 5.2 0.551 6.0 0.500 7.2 0.440 8.0 0.402 9.2 0.353 10.0 0.322 11.2 0.284 12.0 0.260 14.0 0.212 16.0 0.172 25.0 0.131 50.0 0.049
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 15 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-2B Normalized Core Shutdown Power for VYNPS Extended Power Uprate SHEX - Short-tern & Long-Term NPSH (Sum of Fission Power. Decay Heat and Fuel Relaxation Energy)
(Decav Heat based on ANS 5.1 -1979 decav heat (incorporating the requirements of SIL 636 Revision 1) + 2 Sinma Uncertainty Adder)
Normalized Time (sec)Shutdown Power 0 1.00823 2 0.5545 4 0.5796 10 0.3803 20 0.1201 60 0.04512 100 0.04144 120 0.04045 120 0.03222 200 0.02909 400 0.0255 1000 0.02079 2000 0.01707 4000 0.0137 6000 0.01209 8000 0.01114 10000 0.01047 15000 0.00986 20000 0.009184 40000 0.007752 60000 0.006989 100000 0.00608 200000 0.004916 400000 0.00384 1.OOE+06 0.002649 3.46E+06 0.001545
Attachment 2 to BVY 04081 Docket No. 50-271 Page 16 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-3A ECCS and RHR Pump Heat for VYNPS Extended Power Uprate SHEX - Short-Term NPSH Time LPCI Pump LPCS Pump RHR Pump (sec) Heat (HP) Heat (HP) Heat (HP) 0-27.2* 0. 0. 0.
27.2*- 4006.4 1124.4 0.
600 _ _ _
Table SPSB-C-32-3B ECCS and RHR Pump Heat for VYNPS Extended Power Uprate SHEX - Long-Term NPSH Time LPCI Pump LPCS Pump RHR Pump (sHeat (HP) Heat (HP) Heat (HP) 0-27.2* 0. 0. 0.
27.2*-600. 4006.4 1124.4 0.
> 600** 2003.2 1124.4 1001.6
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 17 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpy for Peak Drvwell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy (Ibm/s) (Btullbm) 0 0.OOE+00 5.26E+02 0.000488 3.28E+04 5.26E+02 0.000977 6.30E+04 5.26E+02 0.001465 5.98E+04 5.25E+02 0.001709 5.58E+04 5.25E+02 0.001953 5.47E+04 5.25E+02 0.002197 5.47E+04 5.25E+02 0.002686 5.47E+04 5.25E+02 0.003662 5.46E+04 5.25E+02 0.005615 5.46E+04 5.25E+02 0.009522 5.46E+04 5.25E+02 0.013428 5.45E+04 5.25E+02 0.017334 5.45E+04 5.25E+02 0.02124 5.44E+04 5.25E+02 0.025147 5.44E+04 5.25E+02 0.029053 5.43E+04 5.25E+02 0.032959 5.43E+04 5.25E+02 0.036865 5.42E+04 5.25E+02 0.044678 5.42E+04 5.25E+02 0.05249 5.41 E+04 5.25E+02 0.060303 5.40E+04 5.25E+02 0.068115 5.40E+04 5.25E+02 0.075928 5.39E+04 5.25E+02 0.08374 5.38E+04 5.25E+02 0.091553 5.38E+04 5.25E+02 0.099365 5.37E+04 5.25E+02 0.107178 5.36E+04 5.25E+02 0.11499 5.36E+04 5.25E+02 0.122803 5.35E+04 5.25E+02 0.130615 5.34E+04 5.25E+02 0.138428 5.34E+04 5.25E+02 0.14624 5.33E+04 5.25E+02 0.161865 5.32E+04 5.25E+02 0.17749 5.31 E+04 5.25E+02 0.193115 5.29E+04 5.25E+02 DBA-LOCA break flow data provided for 20 seconds. This extends the DBA-LOCA break flow data past the time of the peak drywell pressure which occurs at approximately 5 seconds.
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 18 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPTILAMB DBA-LOCA Break Mass Flow Rate and Enthalpv for Peak Drvwell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy
.(Ibm/s) (Btulibm) 0.20874 5.28E+04 5.25E+02 0.224365 5.26E+04 5.26E+02 0.23999 5.25E+04 5.26E+02 0.255615 5.23E+04 5.26E+02 0.27124 5.22E+04 5.26E+02 0.286865 5.20E+04 5.26E+02 0.30249 5.19E+04 5.26E+02 0.318115 5.17E+04 5.26E+02 0.33374 5.16E+04 5.26E+02 0.36499 5.14E+04 5.26E+02 0.39624 5.11 E+04 5.26E+02 0.411865 5.07E+04 5.26E+02 0.419678 5.06E+04 5.26E+02 0.42749 5.05E+04 5.26E+02 0.435303 5.04E+04 5.26E+02 0.443115 5.03E+04 5.26E+02 0.450928 5.02E+04 5.26E+02 0.45874 5.01 E+04 5.26E+02 0.466553 5.OOE+04 5.26E+02 0.474365 5.OOE+04 5.26E+02 0.482178 4.99E+04 5.26E+02 0.48999 4.98E+04 5.26E+02 0.497803 4.97E+04 5.27E+02 0.505615 4.96E+04 5.27E+02 0.513428 4.95E+04 5.27E+02 0.52124 4.94E+04 5.27E+02 0.536865 4.93E+04 5.27E+02 0.55249 4.91 E+04 5.27E+02 0.568115 4.89E+04 5.27E+02 0.58374 4.87E+04 5.27E+02 0.599365 4.85E+04 5.27E+02 0.61499 4.83E+04 5.27E+02 0.64624 4.81 E+04 5.27E+02 0.67749 4.77E+04 5.28E+02 0.70874 4.72E+04 5.28E+02 0.73999 4.68E+04 5.28E+02 0.77124 4.63E+04 5.28E+02 0.80249 4.59E+04 5.28E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 19 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpy for Peak Drywell Pressure Calculation (0-20 seconds)'
Time (sec) Break Flow Break Flow Enthalpy (Ibmfs) (Btulibm) 0.83374 4.54E+04 5.28E+02 0.86499 4.50E+04 5.29E+02 0.89624 4.45E+04 5.29E+02 0.92749 4.41 E+04 5.29E+02 0.95874 4.36E+04 5.29E+02 0.98999 4.31 E+04 5.29E+02 1.02124 4.26E+04 5.30E+02 1.05249 4.21 E+04 5.30E+02 1.08374 4.16E+04 5.30E+02 1.11499 4.11 E+04 5.30E+02 1.14624 4.07E+04 5.31 E+02 1.17749 4.02E+04 5.31 E+02 1.20874 3.98E+04 5.31 E+02 1.23999 3.93E+04 5.31 E+02 1.27124 3.89E+04 5.31 E+02 1.30249 3.85E+04 5.32E+02 1.33374 3.81 E+04 5.32E+02 1.36499 3.77E+04 5.32E+02 1.380615 3.74E+04 5.32E+02 1.39624 3.72E+04 5.32E+02 1.411865 3.71 E+04 5.32E+02 1.42749 3.69E+04 5.32E+02 1.443115 3.67E+04 5.32E+02 1.45874 3.66E+04 5.32E+02 1.474365 3.64E+04 5.33E+02 1.48999 3.63E+04 5.33E+02 1.505615 3.62E+04 5.33E+02 1.52124 3.60E+04 5.33E+02 1.536865 3.59E+04 5.33E+02 1.55249 3.57E+04 5.33E+02 1.568115 3.56E+04 5.33E+02 1.58374 3.55E+04 5.33E+02 1.599365 3.54E+04 5.33E+02 1.61499 3.52E+04 5.33E+02 1.630615 3.51 E+04 5.33E+02 1.64624 3.50E+04 5.33E+02 1.661865 3.49E+04 5.34E+02 1.67749 3.48E+04 5.34E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 20 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpy for Peak Drywell Pressure Calculation (0-20 seconds)'
Time (sec) Break Flow Break Flow Enthalpy (lbmls) (Btullbm) 1.693115 3.47E+04 5.34E+02 1.70874 3.46E+04 5.34E+02 1.724365 3.45E+04 5.34E+02 1.73999 3.44E+04 5.34E+02 1.755615 3.43E+04 5.34E+02 1.77124 3.43E+04 5.34E+02 1.779053 3.42E+04 5.34E+02 1.786865 3.41 E+04 5.34E+02 1.794678 3.41 E+04 5.34E+02 1.80249 3.41 E+04 5.34E+02 1.810303 3.40E+04 5.34E+02 1.818115 3.40E+04 5.34E+02 1.825928 3.39E+04 5.34E+02 1.83374 3.39E+04 5.34E+02 1.841553 3,39E+04 5.34E+02 1.849365 3.38E+04 5.34E+02 1.857178 3.38E+04 5.34E+02 1.86499 3.38E+04 5.34E+02 1.872803 3.37E+04 5.34E+02 1.880615 3.37E+04 5.34E+02 1.888428 3.37E+04 5.34E+02 1.89624 3.37E+04 5.35E+02 1.904053 3.36E+04 5.35E+02 1.911865 3.36E+04 5.35E+02 1.919678 3.36E+04 5.35E+02 1.92749 3.35E+04 5.35E+02 1.935303 3.35E+04 5.35E+02 1.943115 3.35E+04 5.35E+02 1.950928 3.34E+04 5.35E+02 1.95874 3.34E+04 5.35E+02 1.966553 3.34E+04 5.35E+02 1.974365 3.34E+04 5.35E+02 1.982178 3.33E+04 5.35E+02 1.98999 3.33E+04 5.35E+02 1.997803 3.33E+04 5.35E+02 2.005615 3.33E+04 5.35E+02 2.013428 3.32E+04 5.35E+02 2.02124 3.32E+04 5.35E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 21 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and EnthalDy for Peak Drvwell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy (Ibmis) (Btullbm) 2.025147 3.32E+04 5.35E+02 2.029053 3.32E+04 5.35E+02 2.032959 3.32E+04 5.35E+02 2.036865 3.32E+04 5.35E+02 2.040772 3.32E+04 5.35E+02 2.044678 3.31 E+04 5.35E+02 2.048584 3.31 E+04 5.35E+02 2.05249 3.31 E+04 5.35E+02 2.056397 3.31 E+04 5.35E+02 2.056519 3.31 E+04 5.35E+02 2.056641 3.31 E+04 5.35E+02 2.056885 3.31 E+04 5.35E+02 2.057373 3.31 E+04 5.35E+02 2.05835 3.31 E+04 5.35E+02 2.060303 3.31 E+04 5.35E+02 2.064209 3.31 E+04 5.35E+02 2.072022 3.31 E+04 5.35E+02 2.087647 3.30E+04 5.35E+02 2.118897 3.30E+04 5.35E+02 2.150147 3.29E+04 5.36E+02 2.181397 3.28E+04 5.36E+02 2.212647 3.28E+04 5.36E+02 2.243897 3.27E+04 5.36E+02 2.275147 3.26E+04 5.36E+02 2.337647 3.26E+04 5.36E+02 2.400147 3.25E+04 5.35E+02 2.462647 3.24E+04 5.35E+02 2.525147 3.23E+04 5.35E+02 2.587647 3.23E+04 5.35E+02 2.650147 3.22E+04 5.35E+02 2.712647 3.22E+04 5.34E+02 2.775147 3.22E+04 5.34E+02 2.837647 3.21 E+04 5.34E+02 2.900147 3.21 E+04 5.34E+02 2.962647 3.21 E+04 5.34E+02 3.025147 3.21 E+04 5.34E+02 3.087647 3.20E+04 5.33E+02 3.118897 3.20E+04 5.33E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 22 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPTILAMB DBA-LOCA Break Mass Flow Rate and Enthalpy for Peak Drvwell Pressure Calculation (0-20 seconds)'
Time (sec) Break Flow Break Flow Enthalpy (Ibmrs) (Btullbm) 3.134522 3.20E+04 5.33E+02 3.142334 3.20E+04 5.33E+02 3.150147 3.20E+04 5.33E+02 3.157959 3.20E+04 5.33E+02 3.165772 3.20E+04 5.34E+02 3.173584 3.20E+04 5.34E+02 3.181397 3.20E+04 5.34E+02 3.189209 3.20E+04 5.34E+02 3.204834 3.19E+04 5.35E+02 3.20874 3.20E+04 5.35E+02 3.212647 3.20E+04 5.35E+02 3.220459 3.19E+04 5.35E+02 3.228272 3.19E+04 5.36E+02 3.236084 3.19E+04 5.36E+02 3.23999 3.19E+04 5.36E+02 3.243897 3.19E+04 5.36E+02 3.251709 3.19E+04 5.36E+02 3.259522 3.19E+04 5.36E+02 3.267334 3.19E+04 5.37E+02 3.275147 3.19E+04 5.37E+02 3.282959 3.18E+04 5.37E+02 3.286865 3.18E+04 5.37E+02 3.290772 3.18E+04 5.37E+02 3.294678 3.18E+04 5.37E+02 3.298584 3.18E+04 5.37E+02 3.30249 3.18E+04 5.37E+02 3.306397 3.18E+04 5.37E+02 3.310303 3.18E+04 5.37E+02 3.314209 3.18E+04 5.37E+02 3.318115 3.18E+04 5.37E+02 3.322022 3.18E+04 5.37E+02 3.325928 3.18E+04 5.37E+02 3.329834 3.17E+04 5.37E+02 3.33374 3.17E+04 5.37E+02 3.337647 3.17E+04 5.37E+02 3.341553 3.17E+04 5.37E+02 3.345459 3.17E+04 5.37E+02 3.349365 3.17E+04 5.37E+02
Attachment 2 to BW 04-081 Docket No. 50-271 Page 23 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpv for Peak Drvwell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy (Ibmls) (Btu/lbm) 3.353272 3.17E+04 5.37E+02 3.357178 3.17E+04 5.37E+02 3.361084 3.17E+04 5.37E+02 3.36499 3.17E+04 5.38E+02 3.368897 3.17E+04 5.38E+02 3.372803 3.16E+04 5.38E+02 3.376709 3.16E+04 5.38E+02 3.380615 3.16E+04 5.38E+02 3.384522 3.16E+04 5.38E+02 3.388428 3.16E+04 5.38E+02 3.392334 3.16E+04 5.38E+02 3.39624 3.16E+04 5.38E+02 3.400147 3.16E+04 5.38E+02 3.404053 3.16E+04 5.38E+02 3.407959 3.16E+04 5.38E+02 3.411865 3.16E+04 5.38E+02 3.415772 3.16E+04 5.38E+02 3.419678 3.15E+04 5.38E+02 3.42749 3.15E+04 5.38E+02 3.431397 3.15E+04 5.38E+02 3.435303 3.15E+04 5.38E+02 3.443115 3.15E+04 5.38E+02 3.450928 3.15E+04 5.38E+02 3.45874 3.15E+04 5.38E+02 3.466553 3.15E+04 5.38E+02 3.474365 3.14E+04 5.38E+02 3.482178 3.14E+04 5.38E+02 3.48999 3.14E+04 5.38E+02 3.497803 3.14E+04 5.38E+02 3.513428 3.14E+04 5.38E+02 3.517334 3.14E+04 5.38E+02 3.52124 3.14E+04 5.38E+02 3.529053 3.14E+04 5.38E+02 3.536865 3.13E+04 5.38E+02 3.544678 3.13E+04 5.38E+02 3.55249 3.13E+04 5.38E+02 3.560303 3.13E+04 5.38E+02 3.568115 3.13E+04 5.38E+02
Attachment 2 to BW 04-081 Docket No. 50-271 Page 24 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPTILAMB DBA-LOCA Break Mass Flow Rate and Enthalpy for Peak Drvwell Pressure Calculation (0-20 seconds)*
Time (sec) Break Flow Break Flow Enthalpy (Ibm/s) (Btullbm) 3.575928 3.13E+04 5.38E+02 3.58374 3.13E+04 5.38E+02 3.591553 3.13E+04 5.38E+02 3.599365 3.13E+04 5.38E+02 3.607178 3.12E+04 5.38E+02 3.61499 3.12E+04 5.38E+02 3.622803 3.12E+04 5.38E+02 3.630615 3.12E+04 5.38E+02 3.638428 3.12E+04 5.38E+02 3.64624 3.12E+04 5.38E+02 3.654053 3.12E+04 5.38E+02 3.661865 3.12E+04 5.38E+02 3.669678 3.12E+04 5.38E+02 3.67749 3.12E+04 5.38E+02 3.685303 3.11 E+04 5.38E+02 3.693115 3.11 E+04 5.38E+02 3.700928 3.11 E+04 5.38E+02 3.70874 3.11 E+04 5.38E+02 3.716553 3.11 E+04 5.38E+02 3.724365 3.1 E+04 5.38E+02 3.732178 3.1 E+04 5.38E+02 3.73999 3.1 E+04 5.39E+02 3.747803 3.11 E+04 5.39E+02 3.755615 3.1 E+04 5.39E+02 3.763428 3.11 E+04 5.39E+02 3.77124 3.1OE+04 5.39E+02 3.779053 3.10E+04 5.39E+02 3.794678 3.1OE+04 5.39E+02 3.80249 3.10E+04 5.39E+02 3.810303 3.10E+04 5.39E+02 3.818115 3.1OE+04 5.39E+02 3.825928 3.10E+04 5.39E+02 3.83374 3.10E+04 5.39E+02 3.849365 3.10E+04 5.39E+02 3.86499 3.1OE+04 5.39E+02 3.872803 3.09E+04 5.39E+02 3.880615 3.09E+04 5.39E+02 3.888428 3.09E+04 5.39E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 25 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpy for Peak Drvwell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy (Ibm/s) (Btu/lbm) 3.89624 3.09E+04 5.39E+02 3.904053 3.09E+04 5.39E+02 3.911865 3.09E+04 5.39E+02 3.919678 3.09E+04 5.39E+02 3.92749 3.09E+04 5.39E+02 3.935303 3.09E+04 5.39E+02 3.943115 3.09E+04 5.39E+02 3.950928 3.09E+04 5.39E+02 3.95874 3.09E+04 5.39E+02 3.966553 3.09E+04 5.39E+02 3.974365 3.09E+04 5.39E+02 3.982178 3.09E+04 5.39E+02 3.98999 3.08E+04 5.39E+02 3.997803 3.08E+04 5.39E+02 4.005615 3.08E+04 5.39E+02 4.013428 3.08E+04 5.39E+02 4.02124 3.08E+04 5.39E+02 4.029053 3.08E+04 5.39E+02 4.036865 3.08E+04 5.39E+02 4.044678 3.08E+04 5.39E+02 4.05249 3.08E+04 5.39E+02 4.060303 3.08E+04 5.39E+02 4.068115 3.08E+04 5.39E+02 4.075928 3.08E+04 5.39E+02 4.08374 3.08E+04 5.39E+02 4.091553 3.08E+04 5.39E+02 4.099365 3.08E+04 5.39E+02 4.107178 3.08E+04 5.39E+02 4.11499 3.08E+04 5.39E+02 4.122803 3.08E+04 5.39E+02 4.130615 3.08E+04 5.39E+02 4.138428 3.08E+04 5.39E+02 4.134624 3.07E+04 5.39E+02 4.154053 3.07E+04 5.39E+02 4.161865 3.07E+04 5.39E+02 4.169678 3.07E+04 5.39E+02 4.17749 3.07E+04 5.39E+02 4.193115 3.07E+04 5.39E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 26 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpv for Peak Drvwell Pressure Calculation (0-20 seconds)*
Time (sec) Break Flow Break Flow Enthalpy (Ibmns) (Btulibm) 4.20874 3.07E+04 5.39E+02 4.216553 3.07E+04 5.39E+02 4.224365 3.07E+04 5.39E+02 4.232178 3.07E+04 5.39E+02 4.23999 3.07E+04 5.39E+02 4.247803 3.07E+04 5.39E+02 4.255615 3.07E+04 5.39E+02 4.263428 3.07E+04 5.39E+02 4.27124 3.07E+04 5.39E+02 4.279053 3.07E+04 5.39E+02 4.286865 3.07E+04 5.39E+02 4.294678 3.07E+04 5.39E+02 4.30249 3.07E+04 5.39E+02 4.310303 3.07E+04 5.39E+02 4.318115 3.07E+04 5.39E+02 4.325928 3.06E+04 5.39E+02 4.33374 3.06E+04 5.39E+02 4.341553 3.06E+04 5.39E+02 4.349365 3.06E+04 5.39E+02 4.357178 3.06E+04 5.39E+02 4.36499 3.06E+04 5.39E+02 4.372803 3.06E+04 5.39E+02 4.380615 3.06E+04 5.39E+02 4.388428 3.06E+04 5.39E+02 4.39624 3.06E+04 5.39E+02 4.404053 3.06E+04 5.39E+02 4.411865 3.06E+04 5.39E+02 4.419678 3.06E+04 5.39E+02 4.42749 3.06E+04 5.39E+02 4.435303 3.06E+04 5.39E+02 4.443115 3.06E+04 5.39E+02 4.450928 3.06E+04 5.39E+02 4.45874 3.06E+04 5.39E+02 4.466553 3.06E+04 5.39E+02 4.474365 3.06E+04 5.39E+02 4.482178 3.06E+04 5.39E+02 4.48999 3.06E+04 5.39E+02 4.497803 3.06E+04 5.39E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 27 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPTILAMB DBA-LOCA Break Mass Flow Rate and Enthalpy for Peak Drvwell Pressure Calculation (0-20 seconds)'
Time (sec) Break Flow Break Flow Enthalpy (Ibmls) (Btu/lbm) 4.505615 3.06E+04 5.39E+02 4.513428 3.06E+04 5.39E+02 4.52124 3.06E+04 5.39E+02 4.529053 3.06E+04 5.39E+02 4.536865 3.06E+04 5.39E+02 4.544678 3.05E+04 5.39E+02 4.55249 3.05E+04 5.39E+02 4.560303 3.05E+04 5.39E+02 4.568115 3.05E+04 5.39E+02 4.575928 3.05E+04 5.39E+02 4.58374 3.05E+04 5.39E+02 4.591553 3.05E+04 5.39E+02 4.599365 3.05E+04 5.39E+02 4.607178 3.05E+04 5.39E+02 4.61499 3.05E+04 5.39E+02 4.622803 3.05E+04 5.39E+02 4.630615 3.05E+04 5.39E+02 4.638428 3.05E+04 5.39E+02 4.64624 3.05E+04 5.38E+02 4.654053 3.05E+04 5.38E+02 4.661865 3.05E+04 5.38E+02 4.669678 3.05E+04 5.38E+02 4.67749 3.05E+04 5.38E+02 4.685303 3.05E+04 5.38E+02 4.693115 3.05E+04 5.38E+02 4.700928 3.05E+04 5.38E+02 4.70874 3.05E+04 5.38E+02 4.716553 3.05E+04 5.38E+02 4.724365 3.05E+04 5.38E+02 4.732178 3.05E+04 5.38E+02 4.73999 3.05E+04 5.38E+02 4.747803 3.05E+04 5.38E+02 4.755615 3.05E+04 5.38E+02 4.763428 3.05E+04 5.38E+02 4.77124 3.05E+04 5.38E+02 4.779053 3.05E+04 5.38E+02 4.786865 3.05E+04 5.39E+02 4.794678 3.05E+04 5.39E+02
Attachment 2 to BW 04-081 Docket No. 50-271 Page 28 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpv for Peak Drywell Pressure Calculation (0-20 seconds)*
Time (sec) Break Flow Break Flow Enthalpy (Ibnlms) (Btullbm) 4.80249 3.05E+04 5.39E+02 4.810303 3.05E+04 5.39E+02 4.818115 3.05E+04 5.39E+02 4.825928 3.05E+04 5.39E+02 4.83374 3.05E+04 5.39E+02 4.841553 3.05E+04 5.39E+02 4.849365 3.05E+04 5.39E+02 4.857178 3.05E+04 5.39E+02 4.86499 3.05E+04 5.39E+02 4.872803 3.05E+04 5.39E+02 4.880615 3.05E+04 5.39E+02 4.888428 3.05E+04 5.39E+02 4.89624 3.05E+04 5.39E+02 4.904053 3.05E+04 5.39E+02 4.911865 3.05E+04 5.39E+02 4.919678 3.05E+04 5.39E+02 4.92749 3.05E+04 5.39E+02 4.935303 3.05E+04 5.39E+02 4.943115 3.05E+04 5.39E+02 4.950928 3.05E+04 5.39E+02 4.95874 3.05E+04 5.39E+02 4.966553 3.05E+04 5.39E+02 4.974365 3.05E+04 5.39E+02 4.982178 3.05E+04 5.39E+02 4.98999 3.05E+04 5.39E+02 4.997803 3.05E+04 5.39E+02 5.005615 3.05E+04 5.39E+02 5.013428 3.05E+04 5.39E+02 5.02124 3.05E+04 5.39E+02 5.025147 3.05E+04 5.39E+02 5.0271 3.05E+04 5.39E+02 5.029053 3.05E+04 5.39E+02 5.031006 3.05E+04 5.40E+02 5.032959 3.05E+04 5.40E+02 5.034912 3.05E+04 5.41 E+02 5.036865 3.05E+04 5.41 E+02 5.038818 3.04E+04 5.42E+02 5.040772 3.04E+04 5.43E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 29 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpy for Peak Drvwell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy (Ibmls) (Btullbm) 5.042725 3.04E+04 5.44E+02 5.044678 3.04E+04 5.45E+02 5.046631 3.03E+04 5.46E+02 5.048584 3.03E+04 5.47E+02 5.050537 3.03E+04 5.49E+02 5.05249 3.02E+04 5.50E+02 5.054443 3.02E+04 5.52E+02 5.056397 3.01 E+04 5.54E+02 5.05835 3.01 E+04 5.56E+02 5.060303 3.OOE+04 5.57E+02 5.062256 2.99E+04 5.59E+02 5.064209 2.99E+04 5.61 E+02 5.066162 2.98E+04 5.63E+02 5.068115 2.97E+04 5.65E+02 5.070068 2.96E+04 5.67E+02 5.072022 2.95E+04 5.69E+02 5.075928 2.91 E+04 5.74E+02 5.079834 2.89E+04 5.78E+02 5.087647 2.82E+04 5.88E+02 5.095459 2.79E+04 5.96E+02 5.103272 2.75E+04 6.05E+02 5.111084 2.70E+04 6.13E+02 5.118897 2.66E+04 6.21 E+02 5.126709 2.62E+04 6.29E+02 5.134522 2.58E+04 6.37E+02 5.142334 2.53E+04 6.44E+02 5.150147 2.48E+04 6.52E+02 5.157959 2.43E+04 6.59E+02 5.165772 2.38E+04 6.67E+02 5.173584 2.34E+04 6.74E+02 5.181397 2.29E+04 6.81 E+02 5.189209 2.24E+04 6.87E+02 5.197022 2.19E+04 6.94E+02 5.204834 2.15E+04 7.01 E+02 5.212647 2.11 E+04 7.07E+02 5.220459 2.06E+04 7.13E+02 5.228272 2.02E+04 7.19E+02 5.236084 1.98E+04 7.25E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 30 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and EnthalDy for Peak Drywell Pressure Calculation (0-20 seconds)-
Time (sec) Break Flow Break Flow Enthalpy (Ibm/s) (Btullbm) 5.243897 1.94E+04 7.31 E+02 5.251709 1.90E+04 7.37E+02 5.259522 1.87E+04 7.42E+02 5.267334 1.83E+04 7.47E+02 5.275147 1.80E+04 7.52E+02 5.282959 1.77E+04 7.57E+02 5.290772 1.73E+04 7.62E+02 5.298584 1.71 E+04 7.66E+02 5.306397 1.68E+04 7.70E+02 5.314209 1.66E+04 7.74E+02 5.322022 1.63E+04 7.77E+02 5.329834 1.61 E+04 7.81 E+02 5.337647 1.59E+04 7.84E+02 5.345459 1.57E+04 7.87E+02 5.353272 1.55E+04 7.90E+02 5.361084 1.53E+04 7.92E+02 5.368897 1.51 E+04 7.94E+02 5.376709 1.50E+04 7.96E+02 5.384522 1.49E+04 7.98E+02 5.392334 1.47E+04 8.OOE+02 5.400147 1.46E+04 8.02E+02 5.407959 1.45E+04 8.03E+02 5.415772 1.44E+04 8.04E+02 5.423584 1.43E+04 8.05E+02 5.431397 1.42E+04 8.06E+02 5.439209 1.41 E+04 8.07E+02 5.447022 1.41 E+04 8.08E+02 5.454834 1.40E+04 8.08E+02 5.462647 1.39E+04 8.08E+02 5.470459 1.39E+04 8.09E+02 5.478272 1.38E+04 8.09E+02 5.486084 1.38E+04 8.09E+02 5.493897 1.37E+04 8.09E+02 5.501709 1.37E+04 8.09E+02 5.509522 1.37E+04 8.09E+02 5.517334 1.36E+04 8.09E+02 5.525147 1.36E+04 8.09E+02 5.532959 1.36E+04 8.08E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 31 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpy for Peak Drvwell Pressure Calculation (0-20 seconds)*
Time (sec) Break Flow Break Flow Enthalpy (Ibm/s) (Btullbm) 5.540772 1.36E+04 8.08E+02 5.548584 1.35E+04 8.08E+02 5.556397 1.35E+04 8.07E+02 5.564209 1.35E+04 8.07E+02 5.579834 1.35E+04 8.06E+02 5.595459 1.35E+04 8.04E+02 5.611084 1.35E+04 8.03E+02 5.626709 1.35E+04 8.01 E+02 5.642334 1.35E+04 8.OOE+02 5.657959 1.35E+04 7.98E+02 5.673584 1.35E+04 7.96E+02 5.689209 1.35E+04 7.95E+02 5.704834 1.35E+04 7.93E+02 5.720459 1.35E+04 7.91 E+02 5.736084 1.35E+04 7.90E+02 5.751709 1.36E+04 7.88E+02 5.767334 1.36E+04 7.86E+02 5.782959 1.36E+04 7.84E+02 5.798584 1.37E+04 7.82E+02 5.814209 1.37E+04 7.81 E+02 5.829834 1.37E+04 7.79E+02 5.845459 1.38E+04 7.77E+02 5.861084 1.38E+04 7.75E+02 5.876709 1.38E+04 7.73E+02 5.892334 1.39E+04 7.71 E+02 5.907959 1.39E+04 7.70E+02 5.923584 1.39E+04 7.68E+02 5.939209 1.40E+04 7.66E+02 5.954834 1.40E+04 7.64E+02 5.970459 1.41 E+04 7.62E+02 5.986084 1.41 E+04 7.60E+02 6.001709 1.41 E+04 7.59E+02 6.017334 1.42E+04 7.57E+02 6.032959 1.42E+04 7.55E+02 6.048584 1.42E+04 7.53E+02 6.064209 1.43E+04 7.51 E+02 6.079834 1.43E+04 7.50E+02 6.095459 1.44E+04 7.48E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 32 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalfv for Peak Drvwell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy (lbmls) (Btullbm) 6.111084 1.44E+04 7.46E+02 6.126709 1.45E+04 7.44E+02 6.142334 1.45E+04 7.43E+02 6.157959 1.45E+04 7.41 E+02 6.173584 1.46E+04 7.39E+02 6.189209 1.46E+04 7.37E+02 6.204834 1.47E+04 7.36E+02 6.220459 1.47E+04 7.34E+02 6.236084 1.48E+04 7.32E+02 6.251709 1.48E+04 7.31 E+02 6.267334 1.49E+04 7.29E+02 6.282959 1.49E+04 7.27E+02 6.298584 1.49E+04 7.26E+02 6.314209 1.50E+04 7.24E+02 6.329834 1.50E+04 7.23E+02 6.345459 1.51 E+04 7.21 E+02 6.361084 1.51 E+04 7.20E+02 6.376709 1.52E+04 7.18E+02 6.392334 1.52E+04 7.16E+02 6.407959 1.52E+04 7.15E+02 6.423584 1.53E+04 7.13E+02 6.439209 1.53E+04 7.12E+02 6.454834 1.54E+04 7.11 E+02 6.470459 1.54E+04 7.09E+02 6.486084 1.54E+04 7.08E+02 6.501709 1.55E+04 7.06E+02 6.517334 1.55E+04 7.05E+02 6.532959 1.56E+04 7.03E+02 6.548584 1.56E+04 7.02E+02 6.564209 1.57E+04 7.01 E+02 6.579834 1.57E+04 6.99E+02 6.595459 1.58E+04 6.98E+02 6.611084 1.58E+04 6.97E+02 6.626709 1.58E+04 6.95E+02 6.642334 1.59E+04 6.94E+02 6.657959 1.59E+04 6.93E+02 6.673584 1.60E+04 6.92E+02 6.689209 1.60E+04 6.90E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 33 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPTILAMB DBA-LOCA Break Mass Flow Rate and Enthalnv for Peak Drvwill Pressure Calculation (0-20
__ seconds)*
I Time (sec) Break Flow Break Flow Enthalpy (Ibm/s) (Btulibm) 6.704834 1.60E+04 6.89E+02 6.712647 1.60E+04 6.89E+02 6.720459 1.61 E+04 6.88E+02 6.728272 1.61 E+04 6.88E+02 6.743897 1.61 E+04 6.86E+02 6.759522 1.62E+04 6.85E+02 6.790772 1.63E+04 6.82E+02 6.822022 1.63E+04 6.80E+02 6.853272 1.64E+04 6.78E+02 6.884522 1.64E+04 6.76E+02 6.915772 1.65E+04 6.74E+02 6.947022 1.65E+04 6.73E+02 6.978272 1.66E+04 6.71 E+02 7.009522 1.66E+04 6.70E+02 7.040772 1.67E+04 6.68E+02 7.072022 1.68E+04 6.67E+02 7.103272 1.68E+04 6.65E+02 7.134522 1.69E+04 6.64E+02 7.165772 1.69E+04 6.62E+02 7.197022 1.69E+04 6.61 E+02 7.228272 1.70E+04 6.60E+02 7.259522 1.70E+04 6.58E+02 7.290772 1.71 E+04 6.57E+02 7.322022 1.71 E+04 6.56E+02 7.353272 1.71 E+04 6.55E+02 7.384522 1.71 E+04 6.53E+02 7.415772 1.72E+04 6.52E+02 7.447022 1.72E+04 6.51 E+02 7.478272 1.72E+04 6.50E+02 7.509522 1.73E+04 6.49E+02 7.540772 1.73E+04 6.48E+02 7.572022 1.73E+04 6.46E+02 7.603272 1.74E+04 6.45E+02 7.634522 1.74E+04 6.44E+02 7.665772 1.74E+04 6.43E+02 7.697022 1.74E+04 6.42E+02 7.728272 1.74E+04 6.42E+02 7.759522 1.74E+04 6.41 E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 34 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPTILAMB DBA-LOCA Break Mass Flow Rate and Enthalpv for Peak Drvwell Pressure Calculation (0-20 seconds; Time (sec) Break Flow Break Flow Enthalpy (Ibms) (Btullbm) 7.790772 1.75E+04 6.40E+02 7.822022 1.75E+04 6.39E+02 7.853272 1.75E+04 6.38E+02 7.884522 1.75E+04 6.37E+02 7.947022 1.75E+04 6.35E+02 7.978272 1.75E+04 6.35E+02 8.009522 1.75E+04 6.34E+02 8.040772 1.75E+04 6.34E+02 8.103272 1.75E+04 6.32E+02 8.165772 1.75E+04 6.31 E+02 8.228272 1.75E+04 6.30E+02 8.290772 1.75E+04 6.29E+02 8.353272 1.74E+04 6.28E+02 8.415772 1.74E+04 6.27E+02 8.478272 1.74E+04 6.26E+02 8.540772 1.73E+04 6.25E+02 8.603272 1.73E+04 6.25E+02 8.665772 1.72E+04 6.24E+02 8.728272 1.72E+04 6.23E+02 8.790772 1.71 E+04 6.23E+02 8.915772 1.71 E+04 6.21 E+02 8.947022 1.69E+04 6.21 E+02 8.978272 1.69E+04 6.21 E+02 9.009522 1.69E+04 6.21 E+02 9.040772 1.68E+04 6.21 E+02 9.103272 1.68E+04 6.20E+02 9.165772 1.68E+04 6.19E+02 9.228272 1.67E+04 6.19E+02 9.353272 1.67E+04 6.17E+02 9.384522 1.64E+04 6.17E+02 9.415772 1.64E+04 6.17E+02 9.447022 1.64E+04 6.17E+02 9.478272 1.64E+04 6.17E+02 9.540772 1.64E+04 6.16E+02 9.603272 1.63E+04 6.16E+02 9.665772 1.63E+04 6.15E+02 9.728272 1.62E+04 6.15E+02 9.790772 1.61 E+04 6.14E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 35 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpv for Peak Drvwell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy (Ibm/s) (Btulibm) 9.853272 1.61 E+04 6.14E+02 9.978272 1.61 E+04 6.13E+02 10.00952 1.58E+04 6.13E+02 10.04077 1.58E+04 6.13E+02 10.07202 1.58E+04 6.13E+02 10.10327 1.67E+04 6.13E+02 10.13452 1.57E+04 6.12E+02 10.19702 1.57E+04 6.12E+02 10.25952 1.56E+04 6.12E+02 10.32202 1.56E+04 6.11 E+02 10.44702 1.55E+04 6.1OE+02 10.50952 1.53E+04 6.1OE+02 10.57202 1.53E+04 6.10E+02 10.63452 1.52E+04 6.1OE+02 10.69702 1.51 E+04 6.09E+02 10.75952 1.50E+04 6.09E+02 10.82202 1.50E+04 6.09E+02 10.88452 1.49E+04 6.09E+02 10.94702 1.48E+04 6.08E+02 11.00952 1.47E+04 6.08E+02 11.07202 1.46E+04 6.08E+02 11.13452 1.46E+04 6.07E+02 11.19702 1.45E+04 6.07E+02 11.25952 1.44E+04 6.07E+02 11.32202 1.43E+04 6.07E+02 11.38452 1.42E+04 6.07E+02 11.44702 1.42E+04 6.06E+02 11.50952 1.41 E+04 6.06E+02 11.57202 1.40E+04 6.06E+02 11.63452 1.39E+04 6.06E+02 11.69702 1.38E+04 6.05E+02 11.75952 1.37E+04 6.05E+02 11.82202 1.37E+04 6.05E+02 11.88452 1.36E+04 6.05E+02 11.94702 1.35E+04 6.05E+02 12.00952 1.34E+04 6.05E+02 12.07202 1.33E+04 6.04E+02 12.13452 1.32E+04 6.04E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 36 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpv for Peak Drywell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy (Ibmfs) (Btullbm) 12.19702 1.32E+04 6.04E+02 12.25952 1.31 E+04 6.04E+02 12.32202 1.30E+04 6.04E+02 12.38452 1.29E+04 6.04E+02 12.44702 1.28E+04 6.03E+02 12.50952 1.27E+04 6.03E+02 12.57202 1.26E+04 6.03E+02 12.63452 1.25E+04 6.03E+02 12.69702 1.25E+04 6.03E+02 12.75952 1.24E+04 6.03E+02 12.82202 1.23E+04 6.03E+02 12.88452 1.22E+04 6.03E+02 12.94702 1.21 E+04 6.02E+02 13.00952 1.20E+04 6.02E+02 13.07202 1.19E+04 6.02E+02 13.13452 1.18E+04 6.02E+02 13.19702 1.18E+04 6.02E+02 13.25952 1.17E+04 6.02E+02 13.32202 1.16E+04 6.02E+02 13.38452 1.15E+04 6.02E+02 13.44702 1.14E+04 6.02E+02 13.50952 1.13E+04 6.02E+02 13.57202 1.12E+04 6.02E+02 13.63452 1.11 E+04 6.01 E+02 13.69702 1.11 E+04 6.01 E+02 13.75952 1.10E+04 6.01E+02 13.82202 1.09E+04 6.01 E+02 13.88452 1.08E+04 6.01 E+02 13.94702 1.07E+04 6.01 E+02 14.00952 1.06E+04 6.01 E+02 14.07202 1.05E+04 6.01 E+02 14.13452 1.05E+04 6.01E+02 14.19702 1.04E+04 6.01 E+02 14.25952 1.03E+04 6.01 E+02 14.32202 1.02E+04 6.01 E+02 14.38452 1.01 E+04 6.01 E+02 14.44702 1.OOE+04 6.01 E+02 14.50952 9.92E+03 6.01 E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 37 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpv for Peak Drvwell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy (Ibm/s) (Btulibm) 14.57202 9.83E+03 6.01 E+02 14.63452 9.75E+03 6.01 E+02 14.69702 9.66E+03 6.01 E+02 14.75952 9.57E+03 6.01 E+02 14.82202 9.48E+03 6.OOE+02 14.88452 9.40E+03 6.01 E+02 14.94702 9.31 E+03 6.OOE+02 15.00952 9.22E+03 6.OOE+02 15.07202 9.14E+03 6.OOE+02 15.13452 9.05E+03 6.00E+02 15.19702 8.96E+03 6.OOE+02 15.25952 8.88E+03 6.00E+02 15.32202 8.79E+03 6.OOE+02 15.38452 8.71 E+03 6.OOE+02 15.44702 8.63E+03 6.OOE+02 15.50952 8.55E+03 6.01 E+02 15.57202 8.47E+03 6.OOE+02 15.63452 8.39E+03 6.01 E+02 15.69702 8.31 E+03 6.01 E+02 15.75952 8.23E+03 6.01 E+02 15.82202 8.15E+03 6.01 E+02 15.88452 8.07E+03 6.01 E+02 15.94702 7.99E+03 6.01 E+02 16.00952 7.91 E+03 6.01 E+02 16.07202 7.84E+03 6.01 E+02 16.13452 7.76E+03 6.01 E+02 16.19702 7.69E+03 6.01 E+02 16.25952 7.61 E+03 6.01 E+02 16.32202 7.53E+03 6.01 E+02 16.38452 7.45E+03 6.01 E+02 16.44702 7.38E+03 6.01 E+02 16.50952 7.31 E+03 6.01 E+02 16.57202 7.23E+03 6.01 E+02 16.63452 7.16E+03 6.01 E+02 16.69702 7.08E+03 6.01 E+02 16.75952 7.01 E+03 6.02E+02 16.82202 6.93E+03 6.02E+02 16.88452 6.86E+03 6.02E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 38 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPTILAMB DBA-LOCA Break Mass Flow Rate and Enthalmy for Peak Drvwell Pressure Calculation (0-20 seconds)*
Time (sec) Break Flow Break Flow Enthalpy (Ibm/s) (Btullbm) 16.94702 6.79E+03 6.02E+02 17.00952 6.71 E+03 6.02E+02 17.07202 6.64E+03 6.02E+02 17.13452 6.57E+03 6.02E+02 17.19702 6.50E+03 6.02E+02 17.25952 6.43E+03 6.02E+02 17.32202 6.35E+03 6.03E+02 17.38452 6.28E+03 6.03E+02 17.41577 6.22E+03 6.03E+02 17.44702 6.18E+03 6.03E+02 17.47827 6.15E+03 6.03E+02 17.50952 6.11 E+03 6.03E+02 17.54077 6.08E+03 6.03E+02 17.57202 6.04E+03 6.03E+02 17.60327 6.01 E+03 6.03E+02 17.63452 5.97E+03 6.03E+02 17.66577 5.94E+03 6.03E+02 17.69702 5.91 E+03 6.03E+02 17.72827 5.87E+03 6.04E+02 17.75952 5.84E+03 6.04E+02 17.79077 5.80E+03 6.04E+02 17.82202 5.77E+03 6.04E+02 17.85327 5.74E+03 6.04E+02 17.88452 5.70E+03 6.04E+02 17.91577 5.67E+03 6.04E+02 17.94702 5.64E+03 6.04E+02 17.97827 5.60E+03 6.04E+02 18.00952 5.57E+03 6.04E+02 18.04077 5.54E+03 6.04E+02 18.07202 5.50E+03 6.04E+02 18.13452 5.47E+03 6.04E+02 18.19702 5.40E+03 6.05E+02 18.25952 5.33E+03 6.05E+02 18.32202 5.27E+03 6.05E+02 18.35327 5.21 E+03 6.05E+02 18.38452 5.18E+03 6.05E+02 18.40015 5.15E+03 6.05E+02 18.41577 6.13E+03 6.05E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 39 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpy for Peak Drvwell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy (Ibmls) (Btulibm) 18.4314 5.12E+03 6.05E+02 18.46265 5.10E+03 6.06E+02 18.4939 5.07E+03 6.06E+02 18.52515 5.04E+03 6.06E+02 18.5564 5.01 E+03 6.06E+02 18.58765 4.98E+03 6.06E+02 18.6189 4.95E+03 6.06E+02 18.65015 4.92E+03 6.06E+02 18.6814 4.90E+03 6.06E+02 18.71265 4.87E+03 6.06E+02 18.7439 4.84E+03 6.06E+02 18.77515 4.81 E+03 6.06E+02 18.8064 4.78E+03 6.06E+02 18.83765 4.76E+03 6.06E+02 18.8689 4.73E+03 6.06E+02 18.90015 4.70E+03 6.06E+02 18.9314 4.67E+03 6.06E+02 18.96265 4.64E+03 6.06E+02 18.9939 4.62E+03 6.06E+02 19.00952 4.59E+03 6.06E+02 19.02515 4.57E+03 6.06E+02 19.04077 4.56E+03 6.06E+02 19.04858 4.54E+03 6.06E+02 19.0564 4.54E+03 6.06E+02 19.06421 4.53E+03 6.06E+02 19.07202 4.52E+03 6.06E+02 19.08765 4.51 E+03 6.06E+02 19.10327 4.50E+03 6.06E+02 19.1189 4.49E+03 6.07E+02 19.13452 4.47E+03 6.07E.02 19.15015 4.46E+03 6.07E+02 19.16577 4.44E+03 6.07E+02 19.1814 4.43E+03 6.07E+02 19.19702 4.41E+03 6.07E+02 19.21265 4.40E+03 6.07E+02 19.22827 4.39E+03 6.07E+02 19.2439 4.37E+03 6.07E+02 19.25952 4.36E+03 6.07E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 40 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpv for Peak Drywell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy (Ibm/s) (Btu/lbm) 19.27515 4.34E+03 6.07E+02 19.29077 4.33E+03 6.07E+02 19.3064 4.32E+03 6.07E+02 19.32202 4.30E+03 6.07E+02 19.33765 4.29E+03 6.07E+02 19.35327 4.28E+03 6.07E+02 19.3689 4.26E+03 6.07E+02 19.38452 4.25E+03 6.07E+02 19.40015 4.23E+03 6.07E+02 19.41577 4.22E+03 6.07E+02 19.4314 4.21 E+03 6.07E+02 19.44702 4.19E+03 6.07E+02 19.46265 4.18E+03 6.07E+02 19.47827 4.17E+03 6.07E+02 19.4939 4.15E+03 6.07E+02 19.50952 4.14E+03 6.07E+02 19.52515 4.13E+03 6.07E+02 19.54077 4.11 E+03 6.07E+02 19.5564 4.10E+03 6.07E+02 19.57202 4.09E+03 6.07E+02 19.58765 4.07E+03 6.07E+02 19.60327 4.06E+03 6.07E+02 19.6189 4.05E+03 6.07E+02 19.63452 4.03E+03 6.07E+02 19.65015 4.02E+03 6.07E+02 19.66577 4.01 E+03 6.07E+02 19.6814 3.99E+03 6.07E+02 19.69702 3.98E+03 6.07E+02 19.71265 3.97E+03 6.07E+02 19.72827 3.96E+03 6.07E+02 19.7439 3.94E+03 6.07E+02 19.75952 3.93E+03 6.07E+02 19.77515 3.92E+03 6.07E+02 19.78296 3.91 E+03 6.07E+02 19.79077 3.90E+03 6.07E+02 19.79858 3.89E+03 6.07E+02 19.8064 3.89E+03 6.07E+02 19.81421 3.88E+03 6.07E+02
Attachment 2 to BW 04-081 Docket No. 50-271 Page 41 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-4 M3CPT/LAMB DBA-LOCA Break Mass Flow Rate and Enthalpv for Peak Drywell Pressure Calculation (0-20 seconds)
Time (sec) Break Flow Break Flow Enthalpy (Ibm/s) (Btullbm) 19.82202 3.87E+03 6.07E+02 19.82983 3.87E+03 6.07E+02 19.84546 3.86E+03 6.07E+02 19.86108 3.85E+03 6.07E+02 19.8689 3.83E+03 6.07E+02 19.87671 3.83E+03 6.07E+02 19.88452 3.82E+03 6.07E+02 19.89233 3.81 E+03 6.07E+02 19.90015 3.81 E+03 6.07E+02 19.90796 3.80E+03 6.07E+02 19.91577 3.80E+03 6.07E+02 19.92358 3.79E+03 6.07E+02 19.9314 3.78E+03 6.07E+02 19.93921 3.78E+03 6.07E+02 19.94702 3.77E+03 6.07E+02 19.95483 3.76E+03 6.07E+02 19.96265 3.76E+03 6.07E+02 19.97046 3.75E+03 6.07E+02 19.97827 3.74E+03 6.07E+02 19.98608 3.74E+03 6.07E+02 19.9939 3.73E+03 6.07E+02 20.00171 3.73E+03 6.07E+02
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 42 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-5 Mass and Energy Data from SHEX Short-Term (600 sec)
DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Direct LPCI Enthalpy of ECCS flow ECCS flow Core (s) Liquid Break Llquid Break Vapor Break Vapor Break Break Flow Direct LPCI from enthalpy Thermal Flow Rate Enthalpy Flow Rate Enthalpy to Drywell Break flow to suppression from Power (Ibm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) (Ibm/s) Drywell pool (lbm/s) Suppression (Btu/s)
(Bbulbm) Pool (Btu/lbm) 0 2.491E+04 5.531E+02 0.OOOE+00 1.190E+03 O.OOOE+00 O.OOOE+00 O.OOOE+00 5.805E+01 1.863E+06 0.674805 2.473E+04 5.513E+02 O.OOOE+00 1.191E+03 O.OOOE+00 O.OOOE+00 O.OOOE+00 5.873E+01 1.580E+06 3.487305 2.407E+04 5.452E+02 O.OOOE+00 1.192E+03 O.OOOE+00 O.OOOE+00 0.000E+00 6.503E+01 1.059E+06 12.11231 2.142E+04 5.338E+02 O.OOOE+00 1.195E+03 O.OOOE+00 O.OOOE+00 0.000E+00 8.561E+01 6.013E+05 20.98731 0.0006+00 4.132E+02 3.014E+03 1.204E+03 O.OOOE+00 O.OOOE+00 O.OOOE+00 9.809E+01 2.185E+05 28.75293 0.000E+00 3.491 E+02 1.569E+03 1.197E+03 1.974E+03 1.031E+02 1.822E+03 1.024E+02 1.916E+05 32.12793 5.603+03 3.314E+02 O.OOOE+00 1.194E+03 1.974E+03 1.041E+02 2.224E+03 1.034E+02 1.800E+05 35.40918 5.368E+03 3.264E+02 O.OOOE+00 1.193E+03 1.974E+03 1.048E+02 2.309E+03 1.041 E+02 1.686E+05 39.65918 5.120'+03 3.201 E+02 O.OOOE+00 1.192E+03 1.974E+03 1.056E+02 2.413E+03 1.049E+02 1.539E+05 56.22168 4.663E+03 2.975E+02 O.OOOE+00 1.187E+03 1.974E+03 1.081 E+02 2.708E+03 1.074E+02 9.648E+04 72.56543 4.690E+03 2.724E+02 0.0002+00 1.180E+03 1.974E+03 1.091 E+02 2.943E+03 1.084E+02 8.125E+04 95.09668 6.701 +03 2.485E+02 O.OOOE+00 1.174E+03 1.974E+03 1.109E+02 3.096E+03 1.102E+02 7.742E+04 106.1592 6.809E+03 2.353E+02 0.0002+00 1.169E+03 1.974E+03 1.128E+02 3.162E+03 1.121E+02 7.603E+04 116.7217 6.871 +03 2.255E+02 O.OOOE+00 1.166E+03 1.974E+03 1.147E+02 3.204E+03 1.140E+02 7.506E+04 127.2842 6.054E+03 2.164E+02 O.OOOE+00 1.163E+03 1.974E+03 1.165E+02 3.238E+03 1.158E+02 5.902E+04 136.8467 5.298E+03 2.074E+02 O.OOOE+00 1.160E+03 1.974E+03 1.180E+02 3.268E+03 1.172E+02 5.833E+04 147.7529 5.690'+03 1.998E+02 O.OOOE+00 1.158E+03 1.974E+03 1.195E+02 3.291E+03 1.188E+02 5.754E+04 161.2842 3.889e+03 1.929E+02 0.0002+00 1.155E+03 1.974E+03 1.213E+02 3.309E+03 1.205E+02 5.656E+04 176.5654 3.027E+03 1.864E+02 0.0002+00 1.153E+03 1.974E+03 1.227E+02 3.325E+03 1.220E+02 5.546E+04 190.3154 3.0606+03 1.816E+02 O.OOOE+00 1.151E+03 1.974E+03 1.237E+02 3.335E+03 1.230E+02 5.446E+04 207.1279 3.094 +03 1.767E+02 O.OOOE+00 1.149E+03 1.974E+03 1.248E+02 3.336E+03 1.241E+02 5.353E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 43 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-5 Mass and Energy Data from SHEX Short-Term (600 sec)
.DBA-LOCA Containment Analsis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Direct LPCI Enthalpy of ECCS flow ECCS flow Core (s) Liquid Break Liquid Break Vapor Break Vapor Break Break Flow Direct LPCI from enthalpy Thermal Flow Rate Enthalpy Flow Rate Enthalpy to Drywell Break flow to suppression from Power (Ibm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) (Ibm/s) Drywell pool (Ibm/s) Suppression (Btu/s)
(Btu/bm) Pool (BtuAbm) 226.4717 3.141 +03 I.722E+02 0.0002+00 1.148E+03 1.974E+03 1.258E+02 3.336E+03 1.250E+02 5.289E+04 246.3154 3.139E+03 1.685E+02 O.OOOE+00 1.146E+03 1.974E+03 1.266E+02 3.336E+03 1.259E+02 5.223E+04 273.8467 3.187E+03 1.646E+02 O.OOOE+00 1.145E+03 1.974E+03 1.275E+02 3.336E+03 1.268E+02 5.131E+04 301.4092 3.207E+0 3 1.618E+02 O.OOOE+00 1.144E+03 1.974E+03 1.283E+02 3.336E+03 1.276E+02 5.040E+04 332.7217 3.217E+03 1.594E+02 0.OOOE+00 1.143E+03 1.974E+03 1.292E+02 3.336E+03 1.284E+02 4.936E+04 367.6279 3.249+03 1.575E+02 O.OOOE+00 1.142E+03 1.974E+03 1.299E+02 3.336E+03 1.292E+02 4.820E+04 398.2529 3.278 +03 1.562E+02 O.OOOE+00 1.141E+03 1.974E+03 1.306E+02 3.336E+03 1.298E+02 4.719E+04 429.1904 3.297E+03 1.553E+02 O.OOOE+00 1.141 E+03 1.974E+03 1.311 E+02 3.336E+03 1.304E+02 4.671E+04 460.6904 3.302E+03 1.546E+02 O.OOOE+00 1.141 E+03 1.974E+03 1.317E+02 3.336E+03 1.310E+02 4.625E+04 491.6904 3.301E +03 1.541 E+02 O.OOOE+00 1.141E+03 1.974E+03 1.322E+02 3.336E+03 1.315E+02 4.580E+04 522.6904 3.309403 1.538E+02 0.0002+00 1.140E+03 1.974E+03 1.327E+02 3.336E+03 1.320E+02 4.535E+04 553.7529 3.3154+03 1.535E+02 O.OOOE+00 1.140E+03 1.974E+03 1.332E+02 3.336E+03 1.325E+02 4.490E+04 585.0029 3.322e+03 1.533E+02 O.OOOE+00 1.140E+03 1.974E+03 1.336E+02 3.336E+03 1.329E+02 4.445E+04 600.0654 3.318e+03 1.532E+02 O.OOOE+00 1.140E+03 0.0002+00 1.331E+02 3.336E+03 1.331E+02 4.423E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 44 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energv Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Liquid Break Liquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibmls) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btulbm)
(Btu/bm) 0 2.443E+04 5.531 E+02 O.OOOE+00 1.190E+03 O.OOOE+00 5.805E+01 1.863E+06 0.674805 2.424E+04 5.513E+02 O.OOOE+00 1.191E+03 0.OOOE+00 5.878E+01 1.580E+06 3.518555 2.355E+04 5.453E+02 0.000E+00 1.192E+03 0.OOOE+00 6.519E+01 1.060E+06 12.14356 2.145E+04 5.341 E+02 O.OOOE+00 1.195E+03 O.OOOE+00 8.560E+01 5.998E+05 20.26856 O.OOOE+00 4.235E+02 3.310E+03 1.205E+03 0.OOOE+00 9.773E+01 2.210E+05 29.75293 O.OOOE+00 3.392E+02 1.404E+03 1.196E+03 3.408E+03 1.029E+02 1.882E+05 32.30762 5.395E403 3.257E+02 O.OOOE+00 1.193E+03 3.790E+03 1.032E+02 1.793E+05 35.71387 5.082E+03 3.163E+02 O.OOOE+00 1.191E+03 4.025E+03 1.039E+02 1.675E+05 39.24512 4.888E.03 3.071E+02 O.OOOE+00 1.189E+03 4.229E+03 1.046E+02 1.553E+05 60.55762 7.195E+03 2.645E+02 O.OOOE+00 1.178E+03 4.862E+03 1.084E+02 8.330E+04 76.71387 8.864E.03 2.376E+02 O.OOOE+00 1.170E+03 5.100E+03 1.114E+02 8.055E+04 95.02637 5.345E+03 2.189E+02 O.OOOE+00 1.164E+03 5.224E+03 1.130E+02 7.744E+04 114.8545 8.002E+03 2.135E+02 O.OOOE+00 1.162E+03 5.254E+03 1.143E+02 7.523E+04 133.2295 6.415E+03 1.995E+02 0.000E+00 1.157E+03 5.323E+03 1.166E+02 5.859E+04 146.8545 6.580E.03 1.910E+02 O.OOOE+00 1.154E+03 5.358E+03 1.182E+02 5.761 E+04 157.8545 6.091 E+03 1.856E+02 0.OOOE+00 1.152E+03 5.377E+03 1.195E+02 5.681E+04 174.1357 5.022E+03 1.786E+02 O.OOOE+00 1.150E+03 5.393E+03 1.211E+02 5.563E+04 189.917 4.664E4+03 1.731E+02 O.OOOE+00 1.148E+03 5.393E+03 1.224E+02 5.449E+04 206.167 4.760E+03 1.686E+02 O.OOOE+00 1.146E+03 5.393E+03 1.235E+02 5.356E+04 222.7295 5.054E403 1.649E+02 O.OOOE+00 1.145E+03 5.393E+03 1.246E+02 5.301E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 45 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Enerqy Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btu/lbm) (Ibm/s) (Btullbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(Btufbm) 236.792 5.313E+03 1.623E+02 0.0002+00 1.144E+03 5.393E+03 1.254E+02 5.254E+04 251.167 5.550E+03 1.601E+02 O.OOOE+00 1.143E+03 5.393E+03 1.262E+02 5.207E+04 267.0107 5.736E+03 1.580E+02 O.OOOE+00 1.142E+03 5.393E+03 1.270E+02 5.154E+04 284.3857 5.887E+03 1.562E+02 0.0002+00 1.141E+03 5.393E+03 1.278E+02 5.096E+04 302.792 5.973E+03 1.546E+02 O.OOOE+00 1.141E+03 5.393E+03 1.286E+02 5.035E+04 321.167 5.990E+03 1.533E+02 O.OOOE+00 1.140E+03 5.393E+03 1.293E+02 4.974E+04 340.042 5.932E+03 1.523E+02 O.OOOE+00 1.140E+03 5.393E+03 1.300E+02 4.912E+04 360.3545 5.657E+03 1.514E+02 0.0002+00 1.140E+03 5.393E+03 1.307E+02 4.844E+04 384.292 5.543E+03 1.507E+02 O.OOOE+00 1.139E+03 5.393E+03 1.314E+02 4.765E+04 410.1045 5.527E+03 1.501E+02 O.OOOE+00 1.139E+03 5.393E+03 1.321E+02 4.698E+04 433.9482 5.495E+03 1.498E+02 O.OOOE+00 1.139E+03 5.393E+03 1.327E+02 4.664E+04 459.9482 5.472E+03 1.495E+02 O.OOOE+00 1.139£+03 5.393E+03 1.333E+02 4.626E+04 490.4482 5.455E+03 1.493E+02 O.OOOE+00 1.139E+03 5.393E+03 1.339E+02 4.582E+04 520.9795 5.436E+03 1.493E+02 O.OOOE+00 1.139E+03 5.393E+03 1.345E+02 4.537E+04 552.7295 5.424E+03 1.493E+02 O.OOOE+00 1.139E+03 5.393E+03 1.351E+02 4.491 E+04 584.042 5.406E+03 1.493E+02 O.OOOE+00 1.139E+03 5.393E+03 1.356E+02 4.446E+04 600.0107 5.412E+03 1.493E+02 O.OOOE+00 1.139E+03 3.336E+03 1.359E+02 1.212E+02 4.423E+04 785.6045 3.341 E+03 1.527E+02 O.OOOE+00 1.140E+03 3.336E+03 1.377E+02 1.227E+02 4.153E+04 1097.855 3.334E+03 1.536E+02 O.OOOE+00 1.140E+03 3.336E+03 1.398E+02 1.244E+02 3.775E+04 1410.355 3.336E+03 1.543E+02 O.OOOE+00 1.141E+03 3.336E+03 1.417E+02 1.259E+02 3.560E+04 1722.073 3.332E+03 1.551E+02 O.OOOE+00 1.141E+03 3.336E+03 1.433E+02 1.272E+02 3.346E+04 2033.355 3.333E+03 1.557E+02 O.OOOE+00 1.141E+03 3.336E+03 1.447E+02 1.283E+02 3.145E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 46 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Longi-Term DBA-LQCA Containment Analysis for Evaluation of NPSH rime Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquld Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btu/lbm) (Ibmls) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btulbm)
(BtufLbm) 2343.417 3.335E+03 1.565E+02 0.0002+00 1.141E+03 3.336E+03 1.459E+02 1.293E+02 3.048E+04 2653.073 3.332E+03 1.572E+02 O.OOOE+00 1.142E+03 3.336E+03 1.470E+02 1.303E+02 2.952E+04 2962.323 3.335E+03 1.579E+02 O.OOOE+00 1.142E+03 3.336E+03 1.481E+02 1.311E+02 2.855E+04 3270.355 3.333E+03 1.585E+02 0.0002+00 1.142E+03 3.336E+03 1.490E+02 1.319E+02 2.759E+04 3578.792 3.334E+03 1.590E+02 O.OOOE+00 1.142E+03 3.336E+03 1.499E+02 1.326E+02 2.663E+04 3887.23 3.333E+03 1.595E+02 O.OOOE+00 1.143E+03 3.336E+03 1.507E+02 1.332E+02 2.567E+04 4196.48 3.334E+03 1.599E+02 O.OOOE+00 1.143E+03 3.336E+03 1.514E+02 1.338E+02 2.503E+04 4506.136 3.331E+03 1.604E+02 O.OOOE+00 1.143E+03 3.336E+03 1.520E+02 1.343E+02 2.457E+04 4815.792 3.335E+03 1.609E+02 0.OOOE+00 1.143E+03 3.336E+03 1.527E+02 1.348E+02 2.411E+04 5125.042 3.335E+03 1.613E+02 O.OOOE+00 1.143E+03 3.336E+03 1.532E+02 1.353E+02 2.365E+04 5434.23 3.334E+03 1.617E+02 O.OOOE+00 1.144E+03 3.336E+03 1.538E+02 1.358E+02 2.319E+04 5736.948 3.337E+03 1.620E+02 0.OOOE+00 1.144E+03 3.336E+03 1.543E+02 1.362E+02 2.274E+04 6031.792 3.319E+03 1.623E+02 O.OOOE+00 1.144E+03 3.336E+03 1.547E+02 1.365E+02 2.232E+04 6275.292 3.336E+03 1.626E+02 O.OOOE+00 1.144E+03 3.336E+03 1.551E+02 1.368E+02 2.210E+04 6534.73 3.336E+03 1.629E+02 O.OOOE+00 1.144E+03 3.336E+03 1.554E+02 1.371E+02 2.188E+04 6814.355 3.321E+03 1.632E+02 O.OOOE+00 1.144E+03 3.336E+03 1.558E+02 1.374E+02 2.163E+04 7115.386 3.334E+03 1.634E+02 O.OOOE+00 1.144E+03 3.336E+03 1.562E+02 1.377E+02 2.137E+04 7420.605 3.331E+03 1.637E+02 O.OOOE+00 1.144E+03 3.336E+03 1.565E+02 1.380E+02 2.110E+04 7724.355 3.334E+03 1.640E+02 O.OOOE+00 1.144E+03 3.336E+03 1.569E+02 1.383E+02 2.083E+04 8035.636 3.336E+03 1.642E+02 O.OOOE+00 1.144E+03 3.336E+03 1.572E+02 1.385E+02 2.057E+04 8346.917 3.338E+03 1.645E+02 O.OOOE+00 1.145E+03 3.336E+03 1.575E+02 1.388E+02 2.037E+04 8659.011 3.337E+03 1.647E+02 0.000E+00 1.145E+03 3.336E+03 1.578E+02 1.390E+02 2.018E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 47 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Ener-y Data from SHEX Long-Term DBA-LOCA Containment Analvsis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Llquld Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (BtuAbm) (Ibm/s) (BtuAbm) suppression Enthalpy (Btu/s) pool (BtuAbm)
(BtuAbm) 8971.105 3.338E+03 1.650E+02 0.OOOE+00 1.145E+03 3.336E+03 1.581E+02 1.393E+02 1.999E+04 9282.792 3.338E+03 1.652E+02 O.OOOE+00 1.145E+03 3.336E+03 1.584E+02 1.395E+02 1.979E+04 9595.292 3.336E+03 1.654E+02 0.OOOE+00 1.145E+03 3.336E+03 1.586E+02 1.397E+02 1.960E+04 9907.386 3.337E+03 1.655E+02 O.OOOE+00 1.145E+03 3.336E+03 1.589E+02 1.399E+02 1.941E+04 10219.89 3.337E+03 1.657E+02 O.OOOE+00 1.145E+03 3.336E+03 1.591E+02 1.401E+02 1.930E+04 10531.98 3.337E+03 1.659E+02 O.OOOE+00 1.145E+03 3.336E+03 1.593E+02 1.402E+02 1.923E+04 10844.48 3.337E+03 1.661E+02 O.OOOE+00 1.145E+03 3.336E+03 1.595E+02 1.404E+02 1.916E+04 11469.07 3.337E+03 1.664E+02 0.OOOE+00 1.145E+03 3.336E+03 1.599E+02 1.407E+02 1.902E+04 12093.67 3.337E+03 1.668E+02 O.OOOE+00 1.145E+03 3.336E+03 1.603E+02 1.410E+02 1.888E+04 12718.67 3.337E+03 1.671E+02 O.OOOE+00 1.146E+03 3.336E+03 1.606E+02 1.413E+02 1.874E+04 13343.26 3.338E+03 1.673E+02 O.OOOE+00 1.146E+03 3.336E+03 1.609E+02 1.416E+02 1.860E+04 13968.26 3.337E+03 1.676E+02 O.OOOE+00 1.146E+03 3.336E+03 1.612E+02 1.418E+02 1.846E+04 14592.01 3.329E+03 1.678E+02 O.OOOE+00 1.146E+03 3.336E+03 1.615E+02 1.420E+02 1.832E+04 15169.6 3.334E+03 1.680E+02 O.OOOE+00 1.146E+03 3.336E+03 1.617E+02 1.422E+02 1.818E+04 15794.6 3.334E+03 1.681E+02 O.OOOE+00 1.146E+03 3.336E+03 1.619E+02 1.424E+02 1.802E+04 16419.61 3.333E+03 1.682E+02 O.OOOE+00 1.146E+03 3.336E+03 1.621E+02 1.425E+02 1.787E+04 17044.2 3.333E+03 1.684E+02 O.OOOE+00 1.146E+03 3.336E+03 1.622E+02 1.426E+02 1.771E+04 17669.2 3.335E+03 1.684E+02 O.OOOE+00 1.146E+03 3.336E+03 1.624E+02 1.427E+02 1.756E+04 18293.79 3.334E+03 1.685E+02 O.OOOE+00 1.146E+03 3.336E+03 1.625E+02 1.428E+02 1.740E+04 18906.76 3.335E+03 1.685E+02 O.OOOE+00 1.146E+03 3.336E+03 1.626E+02 1.429E+02 1.725E+04 19531.76 3.335E+03 1.686E+02 O.OOOE+00 1.146E+03 3.336E+03 1.626E+02 1.430E+02 1.709E+04 20156.36 3.336E+03 1.686E+02 O.OOOE+00 1.146E+03 3.336E+03 1.627E+02 1.430E+02 1.695E+04
Attachment 2 to BW 04-081 Docket No. 50-271 Page 48 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energv Data from SHEX Long-Term DBA-LOCA Containment Analvsis for Evaluation of NPSH
'Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) IUquld Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (lbm/s) from Spray Power (lbm/s) (Btu/ilbm) (lbm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btunbm)
(Btu/bm) 20781.36 3.334E+03 1.686E+02 0.000E+00 1.146E+03 3.336E+03 1.627E+02 1.430E+02 1.687E+04 21406.36 3.335E+03 1.686E+02 0.OOOE+00 1.146E+03 3.336E+03 1.627E+02 1.430E+02 1.679E+04 22030.95 3.335E+03 1.686E+02 0.000E+00 1.146E+03 3.336E+03 1.627E+02 1.430E+02 1.671E+04 22655.95 3.335E+03 1.685E+02 0.000E+00 1.146E+03 3.336E+03 1.627E+02 1.430E+02 1.662E+04 23244.98 3.336E+03 1.685E+02 0.000E+00 1.146E+03 3.336E+03 1.627E+02 1.430E+02 1.654E+04 23869.98 3.337E+03 1.685E+02 O.OOOE+00 1.146E+03 3.336E+03 1.627E+02 1.430E+02 1.646E+04 24494.98 3.337E+03 1.685E+02 0.000E+00 1.146E+03 3.336E+03 1.627E+02 1.430E+02 1.638E+04 25119.98 3.338E+03 1.685E+02 0.WOE+00 1.146E+03 3.336E+03 1.627E+02 1.430E+02 1.630E+04 25744.98 3.338E+03 1.684E+02 0.000E+00 1.146E+03 3.336E+03 1.627E+02 1.430E+02 1.621 E+04 26369.98 3.337E+03 1.684E+02 O.0WOE+00 1.146E+03 3.336E+03 1.627E+02 1.430E+02 1.613E+04 26994.98 3.336E+03 1.683E+02 0.000E+00 1.146E+03 3.336E+03 1.627E+02 1.430E+02 1.605E+04 27595.76 3.336E+03 1.683E+02 O.000E+00 1.146E+03 3.336E+03 1.626E+02 1.429E+02 1.597E+04 28220.36 3.335E+03 1.682E+02 0.000E+00 1.146E+03 3.336E+03 1.626E+02 1.429E+02 1.589E+04 28844.95 3.335E+03 1.681E+02 O.0OE+00 1.146E+03 3.336E+03 1..625E+02 1.429E+02 1.580E+04 29469.95 3.332E+03 1.681E+02 0.000E+00 1.146E+03 3.336E+03 1.625E+02 1.428E+02 1.572E+04 30094.54 3.336E+03 1.680E+02 0.000E+00 1.146E+03 3.336E+03 1.624E+02 1.428E+02 1.564E+04 30719.14 3.336E+03 1.679E+02 0.000E+00 1.146E+03 3.336E+03 1.624E+02 1.427E+02 1.556E+04 31343.73 3.336E+03 1.678E+02 O.000E+00 1.146E+03 3.336E+03 1.623E+02 1.427E+02 1.547E+04 31968.73 3.333E+03 1.677E+02 0.000E+00 1.146E+03 3.336E+03 1.622E+02 1.426E+02 1.539E+04 32592.92 3.334E+03 1.676E+02 O.000E+00 1.146E+03 3.336E+03 1.622E+02 1.426E+02 1.531E+04 33191.54 3.336E+03 1.675E+02 O.OOOE+00 1.146E+03 3.336E+03 1.621E+02 1.425E+02 1.523E+04 33815.73 3.337E+03 1.674E+02 O.0OE+00 1.146E+03 3.336E+03 1.620E+02 1.424E+02 1.515E+04
Attachment 2 to BVY 04.081 Docket No. 50-271 Page 49 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Lonc-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (lbm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btuls) pool (Btunbm)
(Btu/lbm) 34440.32 3.338E+03 1.673E+02 O.OOOE+00 1.146E+03 3.336E+03 1.619E+02 1.424E+02 1.506E+04 35064.51 3.338E+03 1.672E+02 0.OOOE+00 1.146E+03 3.336E+03 1.618E+02 1.423E+02 1.498E+04 35688.7 3.337E+03 1.671E+02 O.OOOE+00 1.146E+03 3.336E+03 1.617E+02 1.422E+02 1.490E+04 36312.89 3.338E+03 1.669E+02 O.OOOE+00 1.146E+03 3.336E+03 1.616E+02 1.421E+02 1.482E+04 36937.07 3.336E+03 1.668E+02 O.OOOE+00 1.145E+03 3.336E+03 1.615E+02 1.420E+02 1.473E+04 37561.26 3.337E+03 1.667E+02 O.OOOE+00 1.145E+03 3.336E+03 1.614E+02 1.419E+02 1.465E+04 38185.45 3.336E+03 1.665E+02 O.OOOE+00 1.145E+03 3.336E+03 1.613E+02 1.418E+02 1.457E+04 38809.64 3.337E+03 1.664E+02 0.0002+00 1.145E+03 3.336E+03 1.611E+02 1.417E+02 1.448E+04 39423.29 3.334E+03 1.662E+02 O.OOOE+00 1.145E+03 3.336E+03 1.610E+02 1.416E+02 1.440E+04 40020.36 3.335E+03 1.661E+02 0.0002+00 1.145E+03 3.336E+03 1.609E+02 1.415E+02 1.433E+04 40644.14 3.336E+03 1.659E+02 O.OOOE+00 1.145E+03 3.336E+03 1.607E+02 1.414E+02 1.428E+04 41267.92 3.334E+03 1.658E+02 0.0002+00 1.145E+03 3.336E+03 1.606E+02 1.413E+02 1.424E+04 41891.7 3.336E+03 1.656E+02 O.OOOE+00 1.145E+03 3.336E+03 1.604E+02 1.412E+02 1.419E+04 42515.48 3.334E+03 1.655E+02 O.OOOE+00 1.145E+03 3.336E+03 1.603E+02 1.410E+02 1.415E+04 43139.26 3.336E+03 1.653E+02 O.OOOE+00 1.145E+03 3.336E+03 1.601E+02 1.409E+02 1.411E+04 43763.45 3.334E+03 1.651E+02 O.OOOE+00 1.145E+03 3.336E+03 1.600E+02 1.408E+02 1.406E+04 44387.64 3.334E+03 1.650E+02 O.OOOE+00 1.145E+03 3.336E+03 1.598E+02 1.407E+02 1.402E+04 45012.23 3.335E+03 1.648E+02 O.OOOE+00 1.145E+03 3.336E+03 1.597E+02 1.406E+02 1.397E+04 45637.23 3.334E+03 1.647E+02 O.OOOE+00 1.145E+03 3.336E+03 1.595E+02 1.404E+02 1.393E+04 46189.45 3.335E+03 1.645E+02 0.0002+00 1.145E+03 3.336E+03 1.594E+02 1.403E+02 1.389E+04 46724.76 3.337E+03 1.643E+02 O.OOOE+00 1.145E+03 3.336E+03 1.593E+02 1.402E+02 1.385E+04 47260.45 3.336E+03 1.641E+02 O.OOOE+00 1.144E+03 3.336E+03 1.591E+02 1.401E+02 1.382E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 50 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Eneray Data from SHEX Lona-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Liquid Break Liquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) flom Spray Power (Ibm/s) (Btu/lbm) (Ibmrs) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btuibm)
(Btu/lbm) 47796.32 3.336E+03 1.640E+02 0.000E+00 1.144E+03 3.336E+03 1.589E+02 1.399E+02 1.378E+04 48331.95 3.334E+03 1.638E+02 O.OOOE+00 1.144E+03 3.336E+03 1.588E+02 1.398E+02 1.374E+04 48867.57 3.335E+03 1.636E+02 O.OOOE+00 1.144E+03 3.336E+03 1.586E+02 1.397E+02 1.370E+04 49406.11 3.336E+03 1.635E+02 O.OOOE+00 1.144E+03 3.336E+03 1.585E+02 1.396E+02 1.366E+04 50656.11 3.333E+03 1.631E+02 0.000E+00 1.144E+03 3.336E+03 1.581E+02 1.393E+02 1.358E+04 51906.11 3.333E+03 1.627E+02 0.0002+00 1.144E+03 3.336E+03 1.578E+02 1.390E+02 1.349E+04 53156.11 3.336E+03 1.624E+02 O.OOOE+00 1.144E+03 3.336E+03 1.574E+02 1.387E+02 1.340E+04 54406.11 3.333E+03 1.620E+02 O.OOOE+00 1.144E+03 3.336E+03 1.571 E+02 1.384E+02 1.331E+04 55555.17 3.332E+03 1.616E+02 0.0002+00 1.143E+03 3.336E+03 1.567E+02 1.382E+02 1.323E+04 56805.17 3.335E+03 1.612E+02 O.OOOE+00 1.143E+03 3.336E+03 1.564E+02 1.379E+02 1.314E+04 58055.17 3.334E+03 1.608E+02 O.OOOE+00 1.143E+03 3.336E+03 1.560E+02 1.376E+02 1.305E+04 59300.54 3.332E+03 1.605E+02 O.OOOE+00 1.143E+03 3.336E+03 1.556E+02 1.373E+02 1.297E+04 60550.54 3.334E+03 1.601E+02 0.0002+00 1.143E+03 3.336E+03 1.553E+02 1.370E+02 1.289E+04 61800.54 3.335E+03 1.597E+02 O.OOOE+00 1.143E+03 3.336E+03 1.549E+02 1.367E+02 1.284E+04 63050.54 3.333E+03 1.593E+02 O.OOOE+00 1.143E+03 3.336E+03 1.546E+02 1.364E+02 1.279E+04 64300.54 3.335E+03 1.590E+02 O.OOOE+00 1.142E+03 3.336E+03 1.542E+02 1.361E+02 1.274E+04 65550.54 3.336E+03 1.586E+02 0.0002+00 1.142E+03 3.336E+03 1.539E+02 1.358E+02 1.268E+04 66776.29 3.333E+03 1.582E+02 O.OOOE+00 1.142E+03 3.336E+03 1.535E+02 1.355E+02 1.263E+04 67847.79 3.336E+03 1.579E+02 0.0002+00 1.142E+03 3.336E+03 1.532E+02 1.353E+02 1.2592+04 69092.29 3.332E+03 1.575E+02 O.OOOE+00 1.142E+03 3.336E+03 1.528E+02 1.350E+02 1.254E+04 70342.29 3.334E+03 1.572E+02 O.OOOE+00 1.142E+03 3.336E+03 1.525E+02 1.347E+02 1.248E+04 71592.29 3.334E+03 1.568E+02 O.OOOE+00 1.142E+03 3.336E+03 1.521E+02 1.344E+02 1.243E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 51 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Ener Data from SHEX Lona-Term DBA-LOCA Containment Anal sis-for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquld Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibrn/s) (Btullbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(Btu/lbm) 72842.29 3.335E+03 1.565E+02 0.000E+00 1.141E+03 3.336E+03 1.518E+02 1.342E+02 1.238E+04 74092.29 3.334E+03 1.561E+02 O.OOOE+00 1.141E+03 3.336E+03 1.515E+02 1.339E+02 1.233E+04 75342.29 3.334E+03 1.558E+02 O.OOOE+00 1.141E+03 3.336E+03 1.511E+02 1.336E+02 1.227E+04 76592.29 3.335E+03 1.554E+02 O.OOOE+00 1.141E+03 3.336E+03 1.508E+02 1.333E+02 1.222E+04 77842.29 3.335E+03 1.551E+02 0.000E+00 1.141E+03 3.336E+03 1.505E+02 1.331 E+02 1.217E+04 79092.29 3.334E+03 1.547E+02 O.OOOE+00 1.141E+03 3.336E+03 1.502E+02 1.328E+02 1.212E+04 80342.29 3.335E+03 1.544E+02 O.OOOE+00 1.141E+03 3.336E+03 1.498E+02 1.325E+02 1.206E+04 81592.29 3.336E+03 1.541E+02 O.OOOE+00 1.141E+03 3.336E+03 1.495E+02 1.323E+02 1.201 E+04 82842.29 3.332E+03 1.537E+02 O.OOOE+00 1.140E+03 3.336E+03 1.492E+02 1.320E+02 1.196E+04 84089.91 3.336E+03 1.534E+02 O.OOOE+00 1.140E+03 3.336E+03 1.489E+02 1.318E+02 1.191E+04 85339.91 3.335E+03 1.531E+02 O.OOOE+00 1.140E+03 3.336E+03 1.486E+02 1.315E+02 1.185E+04 88589.91 3.335E+03 1.527E+02 O.OOOE+00 1.140E+03 3.336E+03 1.482E+02 1.312E+02 1.180E+04 87839.91 3.335E+03 1.524E+02 O.OOOE+00 1.140E+03 3.336E+03 1.479E+02 1.310E+02 1.175E+04 89089.91 3.335E+03 1.521E+02 O.OOOE+00 1.140E+03 3.336E+03 1.476E+02 1.307E+02 1.170E+04 90339.91 3.335E+03 1.517E+02 0.000E+00 1.140E+03 3.336E+03 1.473E+02 1.305E+02 1.164E+04 91589.91 3.336E+03 1.514E+02 0.0002+00 1.140E+03 3.336E+03 1.470E+02 1.302E+02 1.159E+04 92839.91 3.335E+03 1.511 E+02 O.OOOE+00 1.139E+03 3.336E+03 1.467E+02 1.300E+02 1.154E+04 94089.91 3.335E+03 1.508E+02 0.OOOE+00 1.139E+03 3.336E+03 1.464E+02 1.297E+02 1.149E+04 95339.91 3.334E+03 1.504E+02 O.OOOE+00 1.139E+03 3.336E+03 1.461 E+02 1.295E+02 1.143E+04 96589.91 3.336E+03 1.501 E+02 0.0002+00 1.139E+03 3.336E+03 1.457E+02 1.292E+02 1.138E+04 97839.91 3.333E+03 1.498E+02 O.OOOE+00 1.139E+03 3.336E+03 1.454E+02 1.290E+02 1.133E+04 99089.91 3.336E+03 1.495E+02 0.000E+00 1.139E+03 3.336E+03 1.451 E+02 1.287E+02 1.128E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 52 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Ener Data from SHEX Lon -Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywall and Core (s) Uquid Break Lquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (BtuAbm)
(Btu/lbm) 100339.9 3.333E+03 I1.491E+02 0.OOOE+00 1.139E+03 3.336E+03 1.448E+02 1.285E+02 1.123E+04 101589.9 3.335E+03 1.488E402 0.OOOE2+00 1.139E+03 3.336E+03 1.445E+02 1.282E+02 1.120E+04 102839.9 3.334E+03 1.485E+02 0.OOOE+00 1.138E+03 3.336E+03 1.442E+02 1.280E+02 1.118E+04 104089.7 3.337E+03 I1.483E+02 0.000E+00 1.138E+03 3.336E+03 1.440E+02 1.278E+02 1.115E+04 105339.7 3.338E+03 I1.480E+02 0.OOOE+00 1.138E+03 3.336E+03 1.437E+02 1.276E+02 1.112E+04 106589.7 3.337E+03 I1.477E+02 0.OOOE+00 1.138E+03 3.336E+03 1.434E+02 1.274E+02 1.110E+04 107839.7 3.336E+03 1.475E+02 0.OOOE+00 1.138E+03 3.336E+03 1.432E+02 1.272E+02 1.107E+04 109089.7 3.338E+03 I1.472E+02 0.0OE00E4O 1.138E+03 3.336E+03 1.430E+02 1.270E+02 1.104E+04 110339.7 3.338E+03 1.470E+02 0.OOOE+00 1.138E+03 3.336E+03 1.428E+02 1.268E+02 1.101E+04 111589.7 3.337E.03 I1.468E+02 0.OOOE+00 1.138E+03 3.336E+03 1.426E+02 1.266E+02 1.099E+04 112839.7 3.338E403 I1.466E+02 0.OOOEO00 1.138E+03 3.336E+03 1.424E+02 1.265E+02 1.096E+04 114089.7 3.338E403 1.464E402 0.OOOE+00 1.138E+03 3.336E+03 1.422E+02 1.263E+02 1.093E+04 115339.7 3.331E+03 I1.462E402 0.OOOE+00 1.137E+03 3.336E+03 1.420E+02 1.262E+02 1.091E+04 116589.7 3.336E+03 I1.460E+02 0.OOOE+00 1.137E+03 3.336E+03 1.418E+02 1.260E+02 1.088E+04 117839.7 3.337E+03 1.458E+02 0.OOOE+00 1.137E+03 3.336E+03 1.416E+02 1.258E+02 1.085E+04 119055.5 3.337E+03 1.456E+02 0.OOOE+00 1.137E+03 3.336E+03 1.414E+02 1.257E+02 1.083E+04 120305.5 3.337E4+03 1.454E402 0.OOOE+00 1.137E+03 3.336E+03 1.412E+02 1.255E+02 1.080E+04 121555.5 3.336E+03 I1.452E+02 0.OOOE+00 1.137E+03 3.336E+03 1.410E+02 1.254E+02 1.077E+04 122802 3.336E+03 I1.450E+02 0.000E.O0 1.137E+03 3.336E+03 1.408E+02 1.252E+02 1.075E+04 124052 3.336E+03 I1.448E402 0.OOOE+00 1.137E+03 3.336E+03 1.407E+02 1.251E+02 1.072E+04 125302 3.334E+03 I1.446E402 0.OOOE+00 1.137E+03 3.336E+03 1.405E+02 1.249E+02 1.069E+04 126552 3.336E+03 1.444E402 0.OOOE+00 1.137E+03 3.336E+03 1.403E+02 1.248E+02 1.067E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 53 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquld Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btu/lbm) (Ibm/s) (BtuLAbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(Btu/lbm) 127802 3.333E+03 1.443E+02 O.OOOE+00 1.137E+03 3.336E+03 1.401E+02 1.247E+02 1.064E+04 129052 3.334E+03 1.441E+02 O.OOOE+00 1.137E+03 3.336E+03 1.400E+02 1.245E+02 1.061E+04 130302 3.334E+03 1.439E+02 O.OOOE+00 1.137E+03 3.336E+03 1.398E+02 1.244E+02 1.059E+04 131552 3.336E+03 1.437E+02 O.OOOE+00 1.136E+03 3.336E+03 1.396E+02 1.242E+02 1.056E+04 132802 3.335E+03 1.435E+02 O.OOOE+00 1.136E+03 3.336E+03 1.394E+02 1.241E+02 1.053E+04 134052 3.336E+03 1.433E+02 O.OOOE+00 1.136E+03 3.336E+03 1.393E+02 1.239E+02 1.050E+04 135302 3.336E+03 1.432E+02 O.OOOE+00 1.136E+03 3.336E+03 1.391E+02 1.238E+02 1.048E+04 136552 3.339E+03 1.430E+02 O.OOOE+00 1.136E+03 3.336E+03 1.389E+02 1.237E+02 1.045E+04 137802 3.333E+03 1.428E+02 O.OOOE+00 1.136E+03 3.336E+03 1.388E+02 1.235E+02 1.042E+04 139052 3.333E+03 1.426E+02 0.OOOE+00 1.136E+03 3.336E+03 1.386E+02 1.234E+02 1.040E+04 140302 3.336E+03 1.425E+02 O.OOOE+00 1.136E+03 3.336E+03 1.384E+02 1.233E+02 1.037E+04 141552 3.336E+03 1.423E+02 0.OOOE+00 1.136E+03 3.336E+03 1.382E+02 1.231E+02 1.034E+04 142802 3.335E+03 1.421E+02 0.OOOE+00 1.136E+03 3.336E+03 1.381E+02 1.230E+02 1.032E+04 144052 3.335E+03 1.419E+02 O.OOOE+00 1.136E+03 3.336E+03 1.379E+02 1.229E+02 1.029E+04 145302 3.336E+03 1.418E+02 O.OOOE+00 1.136E+03 3.336E+03 1.378E+02 1.227E+02 1.026E+04 146552 3.336E+03 1.416E+02 O.OOOE+00 1.136E+03 3.336E+03 1.376E+02 1.226E+02 1.024E+04 147802 - 3.336E+03 1.414E+02 0.OOOE+00 1.136E+03 3.336E+03 1.374E+02 1.225E+02 1.021E+04 149052 3.335E+03 1.413E+02 O.OOOE+00 1.136E+03 3.336E+03 1.373E+02 1.223E+02 1.018E+04 150302 3.336E+03 1.411E+02 O.OOOE+00 1.135E+03 3.336E+03 1.371E+02 1.222E+02 1.015E+04 151552 3.335E+03 1.409E+02 O.OOOE+00 1.135E+03 3.336E+03 1.369E+02 1.221E+02 1.013E+04 152802 3.337E+03 1.408E+02 O.OOOE+00 1.135E+03 3.336E+03 1.368E+02 1.219E+02 1.010E+04 154052 3.335E+03 1.406E+02 O.OOOE+00 1.135E+03 3.336E+03 1.366E+02 1.218E+02 1.007E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 54 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Lona-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Liquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (BtuAbm)
(Btu/lbm) 155302 3.336E+03 1.404E+02 O.OOOE+00 1.135E+03 3.336E+03 1.365E+02 1.217E+02 1.005E+04 156552 3.335E+03 1.402E+02 0.OOOE+00 1.135E+03 3.336E+03 1.363E+02 1.215E+02 1.002E+04 157802 3.335E+03 1.401E+02 O.OOOE+00 1.135E+03 3.336E+03 1.361E+02 1.214E+02 9.994E+03 159052 3.334E+03 1.399E+02 0.000E+00 1.135E+03 3.336E+03 1.360E+02 1.213E+02 9.967E+03 160302 3.334E+03 1.397E+02 0.OOOE+00 1.135E+03 3.336E+03 1.358E+02 1.212E+02 9.940E+03 161552 3.334E+03 1.396E+02 O.OOOE+00 1.135E+03 3.336E+03 1.357E+02 1.210E+02 9.913E+03 162802 3.335E+03 1.394E+02 O.OOOE+00 1.135E+03 3.336E+03 1.355E+02 1.209E+02 9.886E+03 164052 3.333E+03 1.392E+02 O.OOOE+00 1.135E+03 3.336E+03 1.354E+02 1.208E+02 9.859E+03 165302 3.334E+03 1.391E+02 0.000E+00 1.135E+03 3.336E+03 1.352E+02 1.206E+02 9.832E+03 166552 3.330E+03 1.389E+02 O.OOOE+00 1.135E+03 3.336E+03 1.350E+02 1.205E+02 9.805E+03 167802 3.333E+03 1.387E+02 O.OOOE+00 1.135E+03 3.336E+03 1.349E+02 1.204E+02 9.778E+03 169052 3.336E+03 1.386E+02 O.OOOE+00 1.134E+03 3.336E+03 1.347E+02 1.203E+02 9.752E+03 170302 3.336E+03 1.384E+02 O.OOOE+00 1.134E+03 3.336E+03 1.346E+02 1.201E+02 9.725E+03 171552 3.336E+03 1.383E+02 0.000E+00 1.134E+03 3.336E+03 1.344E+02 1.200E+02 9.698E+03 172802 3.333E+03 1.381E+02 O.OOOE+00 1.134E+03 3.336E+03 1.343E+02 1.199E+02 9.671E+03 174052 3.333E+03 1.379E+02 0.OOOE+00 1.134E+03 3.336E+03 1.341E+02 1.197E+02 9.644E+03 175302 3.336E+03 1.378E+02 O.OOOE+00 1.134E+03 3.336E+03 1.340E+02 1.196E+02 9.617E+03 176552 3.335E+03 1.376E+02 O.OOOE+00 1.134E+03 3.336E+03 1.338E+02 1.195E+02 9.590E+03 177802 3.336E+03 1.374E+02 O.OOOE+00 1.134E+03 3.336E+03 1.336E+02 1.194E+02 9.563E+03 179052 3.335E+03 1.373E+02 0.OOOE+00 1.134E+03 3.336E+03 1.335E+02 1.192E+02 9.536E+03 180302 3.331E+03 1.371E+02 O.OOOE+00 1.134E+03 3.336E+03 1.333E+02 1.191E+02 9.510E+03 181552 3.335E+03 1.370E+02 O.OOOE+00 1.134E+03 3.336E+03 1.332E+02 1.190E+02 9.483E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 55 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Liquid Break Liquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (lbm/s) from Spray Power (Ibm/s) (Btu/lbm) (Ibmls) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btufbm)
(Btufbm) 182802 3.336E+03 1.368E+02 O.OOOE+00 1.134E+03 3.336E+03 1.330E+02 1.189E+02 9.456E+03 184052 3.336E+03 1.366E+02 O.OOOE+00 1.134E+03 3.336E+03 1.329E+02 1.187E+02 9.429E+03 185302 3.336E+03 1.365E+02 0.0002+00 1.134E+03 3.336E+03 1.327E+02 1.186E+02 9.402E+03 186552 3.334E+03 1.363E+02 O.OOOE+00 1.134E+03 3.336E+03 1.326E+02 1.185E+02 9.375E+03 187802 3.332E+03 1.361E+02 0.OOOE+00 1.133E+03 3.336E+03 1.324E+02 1.184E+02 9.348E+03 189052 3.335E+03 1.360E+02 O.OOOE+00 1.133E+03 3.336E+03 1.323E+02 1.182E+02 9.321E+03 190302 3.336E+03 1.358E+02 O.OOOE+00 1.133E+03 3.336E+03 1.321E+02 1.181E+02 9.294E+03 191552 3.335E+03 1.357E+02 0.0002+00 1.133E+03 3.336E+03 1.319E+02 1.180E+02 9.268E+03 192802 3.336E+03 1.355E+02 O.OOOE+00 1.133E+03 3.336E+03 1.318E+02 1.179E+02 9.241E+03 194052 3.333E+03 1.353E+02 0.000E+00 1.133E+03 3.336E+03 1.316E+02 1.177E+02 9.214E+03 195302 3.335E+03 1.352E+02 O.OOOE+00 1.133E+03 3.336E+03 1.315E+02 1.176E+02 9.187E+03 196552 3.333E+03 1.350E+02 O.OOOE+00 1.133E+03 3.336E+03 1.313E+02 1.175E+02 9.160E+03 197802 3.332E+03 1.348E+02 0.0002+00 1.133E+03 3.336E+03 1.312E+02 1.174E+02 9.133E+03 199052 3.336E+03 1.347E+02 0.OOOE+00 1.133E+03 3.336E+03 1.310E+02 1.172E+02 9.106E+03 200302 3.338E+03 1.345E+02 O.OOOE+00 1.133E+03 3.336E+03 1.309E+02 1.171E+02 9.083E+03 201552 3.336E+03 1.344E+02 0.000E+00 1.133E+03 3.336E+03 1.307E+02 1.170E+02 9.070E+03 202802 3.335E+03 1.342E+02 O.OOOE+00 1.133E+03 3.336E+03 1.306E+02 1.169E+02 9.058E+03 204052 3.337E+03 1.341E+02 0.000E+00 1.133E+03 3.336E+03 1.304E+02 1.167E+02 9.046E+03 205302 3.333E+03 1.339E+02 O.OOOE+00 1.133E+03 3.336E+03 1.303E+02 1.166E+02 9.033E+03 206552 3.333E+03 1.338E+02 O.OOOE+00 1.133E+03 3.336E+03 1.301E+02 1.165E+02 9.021E+03 207802 3.336E+03 1.336E+02 O.OOOE+00 1.132E+03 3.336E+03 1.300E+02 1.164E+02 9.008E+03 209052 3.336E+03 1.335E+02 O.OOOE+00 1.132E+03 3.336E+03 1.299E+02 1.163E+02 8.996E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 56 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Enermy Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH lime Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquld Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(Btu/lbm) 210302 3.334E+03 1.334E+02 O.OOOE+00 1.132E+03 3.336E+03 1.297E+02 1.162E+02 8.983E+03 211552 3.334E+03 1.332E+02 O.OOOE+00 1.132E+03 3.336E+03 1.296E+02 1.161E+02 8.971E+03 212802 3.337E+03 1.331E+02 O.OOOE+00 1.132E+03 3.336E+03 1.295E+02 1.160E+02 8.959E+03 214052 3.336E+03 1.330E+02 0.000E+00 1.132E+03 3.336E+03 1.294E+02 1.159E+02 8.946E+03 215302 3.336E+03 1.328E+02 0.OOOE+00 1.132E+03 3.336E+03 1.292E+02 1.158E+02 8.934E+03 216552 3.335E+03 1.327E+02 O.OOOE+00 1.132E+03 3.336E+03 1.291E+02 1.157E+02 8.921 E+03 217802 3.335E+03 1.326E+02 O.OOOE+00 1.132E+03 3.336E+03 1.290E+02 1.156E+02 8.909E+03 219052 3.333E+03 1.325E+02 O.OOOE+00 1.132E+03 3.336E+03 1.289E+02 1.155E+02 8.896E+03 220302 3.336E+03 1.324E+02 O.OOOE+00 1.132E+03 3.336E+03 1.288E+02 1.154E+02 8.884E+03 221552 3.336E+03 1.323E+02 0.0002+00 1.132E+03 3.336E+03 1.287E+02 1.153E+02 8.872E+03 222802 3.337E+03 1.321 E+02 O.OOOE+00 1.132E+03 3.336E+03 1.286E+02 1.152E+02 8.859E+03 224052 3.334E+03 1.320E+02 O.OOOE+00 1.132E+03 3.336E+03 1.284E+02 1.151E+02 8.847E+03 225302 3.334E+03 1.319E+02 0.0002+00 1.132E+03 3.336E+03 1.283E+02 1.151E+02 8.834E+03 226552 3.335E+03 1.318E+02 0.0002+00 1.132E+03 3.336E+03 1.282E+02 1.150E+02 8.822E+03 227802 3.335E+03 1.317E+02 0.0002+00 1.132E+03 3.336E+03 1.281E+02 1.149E+02 8.809E+03 229052 3.340E+03 1.316E+02 0.000E+00 1.132E+03 3.336E+03 1.280E+02 1.148E+02 8.797E+03 230302 3.333E+03 1.315E+02 O.OOOE+00 1.132E+03 3.336E+03 1.279E+02 1.147E+02 8.784E+03 231552 3.333E+03 1.314E+02 O.OOOE+00 1.132E+03 3.336E+03 1.278E+02 1.146E+02 8.772E+03 232802 3.336E+03 1.313E+02 O.OOOE+00 1.132E+03 3.336E+03 1.277E+02 1.146E+02 8.760E+03 234047.9 3.337E+03 1.312E+02 0.000E+00 1.131E+03 3.336E+03 1.276E+02 1.145E+02 8.747E+03 235297.9 3.337E+03 1.311 E+02 0.0002+00 1.131E+03 3.336E+03 1.275E+02 1.144E+02 8.735E+03 236547.9 3.338E+03 1.310E+02 O.OOOE+00 1.131E+03 3.336E+03 1.274E+02 1.143E+02 8.722E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 57 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Long-Term DBA-LOCA Containment Anal sis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibmls) (Bullbm) (Ibm/s) (Btu /bm) suppression Enthalpy (Btu/s)
(Btulbm) 237797.9 3.338E+03 I1.309E+02 O.OOOE+00 1.131 E+03 3.336E+03 1.273E+02 - 1.142E.02 8.710E+03 239047.9 3.337Ee03 I1.308E+02 0.OOOE+00 1.131E+03 3.336E+03 I1.272E+02 I1.142E402 8.698E+03 240297.9 3.338E+03 I1.307E+02 0.OOOE+00 1.131E+03 3.336E+03 1.272E+02 1.141E+02 8.685E+03 241547.9 3.336E+03 1.306E+02 0.000E400 1.131E+03 3.336E+03 1.271 E402 I1.140E+02 8.673E+03 242797.9 3.338E+03 I1.305E.02 0.oOOE+00 1.131E+03 3.336E+03 1.270E402 I1.139E+02 8.660E+03 244047.9 3.337E+03 I1.304E+02 0.OOOE+00 1.131E+03 3.336E403 1.269E+02 1.139E+02 8.648E+03 245297.9 3.336E+03 I1.303E+02 0.OOOE+00 1.131E+03 3.336E+03 I1.268E+02 1.138E+02 8.635E403 246547.9 3.336E+03 1.302E+02 0.OOOE2+00 1.131E+03 3.336E+03 I1.267E+02 1.137E+02 8.623E+03 247797.9 3.335E.03 1.301E402 0.OOOE+00 1.131E+03 3.336E+03 ¶1.266E+02 1.137E+02 8.61 1E+03 249047.9 3.336E+03 I1.300E.02 0.OOOE2+00 1.131E+03 3.336E+03 I1.265E402 I1.136E+02 8.598E+03 250297.9 3.336E.03 I1.300E+02 0.000E400 1.131E+03 3.336E403 I1.265E402 1.135E402 8.586E+03 251547.9 3.336E+03 I1.299E402 0.000E400 1.131E+03 3.336E+03 I1.264E+02 1.134E+02 8.573E403 252797.9 3.338E.03 1.298E402 0.000E400 1.131E+03 3.336E.03 1.263E+02 I1.134E+02 8.561E.03 254047.9 3.337E+03 I1.297E+02 0.OOOE+00 1.131E+03 3.336E+03 1.262E+02 1.1 33E+02 8.548E403 255297.9 3.341E.03 1.296E+02 0.OOOE+00 1.131E.03 3.336E403 I1.261E+02 1.132E+02 8.536E+03 256547.9 3.336E+03 I .295E.02 0.OOOE2+00 I1.131E+03 3.336E+03 I1.260E+02 1.132E+02 8.524E+03 257797.9 3.336E+03 I1.294E+02 0.000E+00 1.131E+03 3.336E+03 ¶1.260E+02 I1.131E+02 8.51 1E+03 259047.9 3.334E+03 I1.293E.02 0.OOOE2+00 1.131E+03 3.336E+03 I1.258E+02 1.130E+02 8.499E+03 260297.9 3.337E+03 1.291 E+02 0.OOOE+00 I1.131E+03 3.336E+03 I1.256E+02 I1.129E+02 8.486E+03 261547.9 3.338E+03 1.290E+02 0.OOOE+00 1.131E+03 3.336E+03 1.255E+02 I1.127Ei02 8.474E+03 262797.8 3.333E+03 I1.288E+02 0.OOOE+O0 1.131E+03 3.336E+03 1.253E+02 1.126E+02 8.461E+03 264047.8 3.340E+03 I1.287E+02 0.OOOE+00 1.130E+03 3.336E403 I1.252E+02 1.125E.02 8.449E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 58 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Enerm Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btu/lbm) (lbm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/bm)
(Btu/lbm) 265297.8 3.335E+03 1.285E+02 0.OOOE+00 1.130E+03 3.336E+03 1.251E+02 1.124E+02 8.437E+03 266547.8 3.338E+03 1.284E+02 0.OOOE+00 1.130E+03 3.336E+03 1.249E+02 1.123E+02 8.424E+03 267797.8 3.336E+03 1.282E+02 O.OOOE+00 1.130E+03 3.336E+03 1.248E+02 1.122E+02 8.412E+03 269047.8 3.337E+03 1.281E+02 O.OOOE+00 1.130E+03 3.336E+03 1.247E+02 1.121E+02 8.399E+03 270297.8 3.338E+03 1.280E+02 O.OOOE+00 1.130E+03 3.336E+03 1.245E+02 1.120E+02 8.387E+03 271547.8 3.340E+03 1.278E+02 O.OOOE+00 1.130E+03 3.336E+03 1.244E+02 1.118E+02 8.374E+03 272797.8 3.337E+03 1.277E+02 O.OOOE+00 1.130E+03 3.336E+03 1.243E+02 1.117E+02 8.362E+03 274047.8 3.338E+03 1.276E+02 O.OOOE+00 1.130E+03 3.336E+03 1.242E+02 1.117E+02 8.350E+03 275297.8 3.337E+03 1.275E+02 O.OOOE+00 1.130E+03 3.336E+03 1.240E+02 1.116E+02 8.337E+03 276547.8 3.336E+03 1.274E+02 O.OOOE+00 1.130E+03 3.336E+03 1.239E+02 1.115E+02 8.325E+03 277797.8 3.335E+03 1.272E+02 O.OOOE+00 1.130E+03 3.336E+03 1.238E+02 1.114E+02 8.312E+03 279047.8 3.337E+03 1.271E+02 O.OOOE+00 1.130E+03 3.336E+03 1.237E+02 1.113E+02 8.300E+03 280297.8 3.334E+03 1.270E+02 0.000E+00 1.130E+03 3.336E+03 1.236E+02 1.112E+02 8.287E+03 281547.8 3.336E+03 1.269E+02 O.OOOE+00 1.130E+03 3.336E+03 1.235E+02 1.111E+02 8.275E+03 282797.8 3.337E+03 1.268E+02 0.000E+00 1.130E+03 3.336E+03 1.234E+02 1.110E+02 8.263E+03 284047.8 3.339E+03 1.267E+02 0.OOOE+00 1.130E+03 3.336E+03 1.233E+02 1.109E+02 8.250E+03 285297.8 3.337E+03 1.266E+02 O.OOOE+00 1.130E+03 3.336E+03 1.232E+02 1.108E+02 8.238E+03 286547.8 3.337E+03 1.265E+02 0.000E+00 1.130E+03 3.336E+03 1.231E+02 1.108E+02 8.225E+03 287797.8 3.338E+03 1.263E+02 0.000E+00 1.130E+03 3.336E+03 1.230E+02 1.107E+02 8.213E+03 289047.8 3.336E+03 1.262E+02 0.000E+00 1.129E+03 3.336E+03 1.229E+02 1.106E+02 8.200E+03 290297.8 3.338E+03 1.261E+02 O.OOOE+00 1.129E+03 3.336E+03 1.228E+02 1.105E+02 8.188E+03 291547.8 3.336E+03 1.260E+02 O.OOOE+00 1.129E+03 3.336E+03 1.227E+02 1.104E+02 8.176E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 59 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energv Data from SHEX Lona-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Liquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btu/lbm) (lbm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(Btu/lbm) 292797.8 3.337E+03 1.259E+02 O.OOOE+00 1.129E+03 3.336E+03 1.226E+02 1.104E+02 8.163E+03 294047.8 3.338E+03 1.258E+02 O.OOOE+00 1.129E+03 3.336E+03 1.225E+02 1.103E+02 8.151E+03 295297.8 3.340E+03 1.257E+02 O.OOOE+00 1.129E+03 3.336E+03 1.224E+02 1.102E+02 8.138E+03 296547.8 3.336E+03 1.256E+02 O.OOOE+00 1.129E+03 3.336E+03 1.223E+02 1.101E+02 8.126E+03 297797.8 3.337E+03 1.256E+02 O.OOOE+00 1.129E+03 3.336E+03 1.222E+02 1.100E+02 8.113E+03 299047.8 3.338E+03 1.255E+02 0.OOOE+00 1.129E+03 3.336E+03 1.221E+02 1.100E+02 8.101E+03 300297.8 3.337E+03 1.254E+02 O.OOOE+00 1.129E+03 3.336E+03 1.220E+02 1.099E+02 8.089E+03 301547.8 3.336E+03 1.253E+02 O.OOOE+00 1.129E+03 3.336E+03 1.219E+02 1.098E+02 8.076E+03 302797.8 3.339E+03 1.252E+02 O.000E+00 1.129E+03 3.336E+03 1.218E+02 1.098E+02 8.064E+03 304047.8 3.337E+03 1.251E+02 0.000E+00 1.129E+03 3.336E+03 1.217E+02 1.097E+02 8.051E+03 305297.8 3.337E+03 1.250E+02 0.OOOE+00 1.129E+03 3.336E+03 1.216E+02 1.096E+02 8.039E+03 306547.8 3.336E+03 1.249E+02 O.OOOE+00 1.129E+03 3.336E+03 1.216E+02 1.095E+02 8.026E+03 307797.8 3.335E+03 1.248E+02 O.OOOE+00 1.129E+03 3.336E+03 1.215E+02 1.095E+02 8.014E+03 309047.8 3.337E+03 1.247E+02 O.OOOE+00 1.129E+03 3.336E+03 1.214E+02 1.094E+02 8.001E+03 310297.8 3.337E+03 1.246E+02 0.OOOE+00 1.129E+03 3.336E+03 1.213E+02 1.093E+02 7.989E+03 311547.8 3.338E+03 1.246E+02 0.OOOE+00 1.129E+03 3.336E+03 1.212E+02 1.093E+02 7.977E+03 312797.8 3.337E+03 1.245E+02 0.OOOE+00 1.129E+03 3.336E+03 1.211E+02 1.092E+02 7.964E+03 314047.8 3.335E+03 1.244E+02 O.OOOE+00 1.129E+03 3.336E+03 1.211E+02 1.091E+02 7.952E+03 315297.8 3.338E+03 1.243E+02 0.OOOE+00 1.129E+03 3.336E+03 1.210E+02 1.091E+02 7.939E+03 316547.8 3.337E+03 1.242E+02 O.OOOE+00 1.129E+03 3.336E+03 1.209E+02 1.090E+02 7.927E+03 317797.8 3.340E+03 1.241E+02 0.OOOE+00 1.129E+03 3.336E+03 1.208E+02 1.089E+02 7.914E+03 319047.8 3.338E+03 1.240E+02 O.OOOE+00 1.129E+03 3.336E+03 1.207E+02 1.089E+02 7.902E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 60 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Eneray Data from SHEX Lona-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Lquld Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibrn/s) from Spray Power (lbm/s) (Btu/ibm) (Ibm/s) (Btu/ibm) suppression Enthalpy (Btu/s) pool (Btulbm)
(Btu/lbm) 320297.8 3.337E+03 1.240E+02 O.OOOE+00 1.129E+03 3.336E+03 1.207E+02 1.088E+02 7.890E+03 321547.8 3.337E+03 1.239E+02 0.000E+00 1.129E+03 3.336E+03 1.206E+02 1.087E+02 7.877E+03 322797.8 3.336E+03 1.238E+02 O.OOOE+00 1.128E+03 3.336E+03 1.205E+02 1.087E+02 7.865E+03 324047.8 3.337E+03 1.237E+02 O.OOOE+00 1.128E+03 3.336E+03 1.204E+02 1.086E+02 7.852E+03 325297.8 3.337E+03 1.236E+02 O.OOOE+00 1.128E+03 3.336E+03 1.203E+02 1.085E+02 7.840E+03 326547.8 3.337E+03 1.235E+02 O.OOOE+00 1.128E+03 3.336E+03 1.203E+02 1.085E+02 7.827E+03 327797.8 3.337E+03 1.235E+02 0.OOOE+00 1.128E+03 3.336E+03 1.202E+02 1.084E+02 7.815E+03 329047.8 3.336E+03 1.234E+02 O.OOOE+00 1.128E+03 3.336E+03 1.201E+02 1.083E+02 7.803E+03 330297.8 3.336E+03 1.233E+02 O.000E+00 1.128E+03 3.336E+03 1.200E+02 1.083E+02 7.790E+03 331547.8 3.337E+03 1.232E+02 O.OOOE+00 1.128E+03 3.336E+03 1.200E+02 1.082E+02 7.778E+03 332797.8 3.336E+03 1.231E+02 0.OOOE+00 1.128E+03 3.336E+03 1.199E+02 1.082E+02 7.765E+03 334047.8 3.337E+03 1.231E+02 O.OOOE+00 1.128E+03 3.336E+03 1.198E+02 1.081E+02 7.753E+03 335297.8 3.337E+03 1.230E+02 O.OOOE+00 1.128E+03 3.336E+03 1.197E+02 1.080E+02 7.740E+03 336547.8 3.337E+03 1.229E+02 0.OOOE+00 1.128E+03 3.336E+03 1.196E+02 1.080E+02 7.728E+03 337797.8 3.336E+03 1.228E+02 0.OOOE+00 1.128E+03 3.336E+03 1.196E+02 1.079E+02 7.716E+03 339047.8 3.337E+03 1.227E+02 O.OOOE+00 1.128E+03 3.336E+03 1.195E+02 1.078E+02 7.703E+03 340297.8 3.336E+03 1.227E+02 O.OOOE+00 1.128E+03 3.336E+03 1.194E+02 1.078E+02 7.691E+03 341547.8 3.336E+03 1.226E+02 O.OOOE+00 1.128E+03 3.336E+03 1.193E+02 1.077E+02 7.678E+03 342797.8 3.334E+03 1.225E+02 0.OOOE+00 1.128E+03 3.336E+03 1.193E+02 1.077E+02 7.666E+03 344047.8 3.337E+03 1.224E+02 0.OOOE+00 1.128E+03 3.336E+03 1.192E+02 1.076E+02 7.653E+03 345297.8 3.338E+03 1.223E+02 O.OOOE+00 1.128E+03 3.336E+03 1.191E+02 1.075E+02 7.641E+03 346547.8 3.336E+03 1.223E+02 0.OOOE+00 1.128E+03 3.336E+03 1.190E+02 1.075E+02 7.629E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 61 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Enerav Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (BtulAbm) (Ibmls) (Btu/bm) suppression Enthalpy (Bts) pool (Btunbm)
(Btulbm) 347797.8 3.340E+03 1.222E+02 0.0002+00 1.128E+03 3.336E+03 1.190E+02 1.074E+02 7.616E+03 349047.8 3.336E+03 1.221 E+02 O.OOOE+00 1.128E+03 3.336E+03 1.189E+02 1.073E+02 7.604E+03 350297.8 3.338E+03 1.220E+02 O.OOOE+00 1.128E+03 3.336E+03 1.188E+02 1.073E+02 7.591 E+03 351547.8 3.337E+03 1.219E+02 O.OOOE+00 1.128E+03 3.336E+03 1.187E+02 1.072E+02 7.579E+03 352797.8 3.336E+03 1.219E+02 O.OOOE+00 1.128E+03 3.336E+03 1.187E+02 1.072E+02 7.566E+03 354047.8 3.337E+03 1.218E+02 O.OOOE+00 1.128E+03 3.336E+03 1.186E+02 1.071E+02 7.554E+03 355297.8 3.337E+03 1.217E+02 O.OOOE+00 1.128E+03 3.336E+03 1.185E+02 1.070E+02 7.542E+03 356547.8 3.337E+03 1.216E+02 O.OOOE+00 1.128E+03 3.336E+03 1.184E+02 1.070E+02 7.529E+03 357797.8 3.337E+03 1.215E+02 0.0002+00 1.128E+03 3.336E+03 1.184E+02 1.069E+02 7.517E+03 359047.8 3.337E+03 1.215E+02 0.OOOE+00 1.128E+03 3.336E+03 1.183E+02 1.069E+02 7.504E+03 360297.8 3.337E+03 1.214E+02 0.OOOE+00 1.128E+03 3.336E+03 1.182E+02 1.068E+02 7.492E+03 361547.8 3.338E+03 1.213E+02 O.OOOE+00 1.127E+03 3.336E+03 1.181E+02 1.067E+02 7.479E+03 362797.8 3.336E+03 1.212E+02 O.OOOE+00 1.127E+03 3.336E+03 1.181E+02 1.067E+02 7.467E+03 364047.8 3.337E+03 1.211 E+02 O.OOOE+00 1.127E+03 3.336E+03 1.180E+02 1.066E+02 7.455E+03 365297.8 3.338E+03 1.211 E+02 O.OOOE+00 1.127E+03 3.336E+03 1.179E+02 1.066E+02 7.442E+03 366547.8 3.337E+03 1.210E+02 O.OOOE+00 1.127E+03 3.336E+03 1.178E+02 1.065E+02 7.430E+03 367797.8 3.338E+03 1.209E+02 0.0002+00 1.127E+03 3.336E+03 1.178E+02 1.064E+02 7.417E+03 369047.8 3.336E+03 1.208E+02 O.OOOE+00 1.127E+03 3.336E+03 1.177E+02 1.064E+02 7.405E+03 370297.8 3.336E+03 1.208E+02 0.0002+00 1.127E+03 3.336E+03 1.176E+02 1.063E+02 7.392E+03 371547.8 3.337E+03 1.207E+02 0.000E+00 1.127E+03 3.336E+03 1.175E+02 1.063E+02 7.380E+03 372797.8 3.337E+03 1.206E+02 O.OOOE+00 1.127E+03 3.336E+03 1.175E+02 1.062E+02 7.368E+03 374047.8 3.339E+03 1.205E+02 O.OOOE+00 1.127E+03 3.336E+03 1.174E+02 1.061E+02 7.355E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 62 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and EnertData from SHEX lonu-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) ULquld Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s)
Pool (Btullbm)
(Btu/lbm) 375297.8 3.337'E403 I1.205E'+O2 0.000E.00 1.127E+03 3.336E+03 1.173E+02 1.061E+02 7.343E+03 376547.8 3.338E+03 1.204E402 O.000E+00 1.127E+03 3.336E+03 1.173E+02 1.060E+02 7.330E+03 377797.8 3.338E+03 I1.203Ee02 0.OOOE+00 1.127E+03 3.336E+03 1.172E+02 1.060E+02 7.318E+03 379047.8 3.337E+03 I1.202E+02 0.000E40O 1.127E+03 3.336E+03 1.171E+02 1.059E+02 7.305E+03 380297.8 3.334E+03 I1.202E+02 0.OOOE+00 1.127E+03 3.336E+03 1.170E+02 1.058E+02 7.293E+03 381547.8 3.337E+03 1.201 E+02 0.000E+00 1.127E+03 3.336E+03 1.170E402 1.058E+02 7.281 E+03 382797.8 3.337E+03 I1.200E+02 0.000E+00 1.127E+03 3.336E+03 1.169E+02 1.057E+02 7.268E+03 384047.8 3.337E+03 1.199E+02 0.OOOE.00 1.127E+03 3.336E+03 1.168E+02 1.057E+02 7.256E+03 385297.8 3.336E+03 1.198E+02 0.000E+00 1.127E+03 3.336E+03 1.167E+02 1.056E+02 7.243E+03 386547.8 3.336E+03 1.198E+02 0.OOOE+00 1.127E+03 3.336E+03 1.167E+02 1.055E+02 7.231 E+03 387797.8 3.337E+03 1.197E402 0.000E+O0 1.127E+03 3.336E+03 1.166E+02 1.055E+02 7.218E+03 389047.8 3.337E+03 1.198E402 0.OOOE+00 1.127E+03 3.336E+03 1.165E4+02 1.054E+02 7.206E+03 390297.8 3.337E+03 1.195E402 0.000E+00 1.127E+03 3.336E+03 1.165E402 1.054E+02 7.194E+03 391547.8 3.337E4+03 1.195E+02 0.000E400 1.127E+03 3.336E+03 1.164E402 1.053E+02 7.181E+03 392797.8 3.337E+03 1.194E+02 0.000E4O0 1.127E+03 3.336E+03 I1.163E+02 1.053E+02 7.169E+03 394047.8 3.338E+03 I1.193E+02 0.OQOE+00 1.127E+03 3.336E+03 1.162E+02 1.052E+02 7.156E+03 395297.8 3.337E+03 1.192E+02 0.OOOE+00 1.127E+03 3.336E+03 1.162E+02 1.051 E+02 7.144E+03 396547.8 3.337E+03 1.192E+02 0.OOOE+00 1.127E+03 3.336E+03 1.161E.02 1.051E+02 7.131E+03 397797.8 3.338E+03 1.191E+02 0.OOOE+00 1.127E+03 3.336E+03 1.160E+02 1.050E+02 7.119E+03 399047.8 3.337E+03 1.190E+02 0.000E+00 1.127E+03 3.336E+03 1.160E+02 1.050E+02 7.107E+03 400297.8 3.337E+03 1.189Ei02 0.OOOE+00 1.127E+03 3.336E+03 1.159E+02 1.049E+02 7.096E+03 401547.8 3.337E+03 1.189E+02 O.000E+00 1.126E+03 3.336E+03 1.158E+02 1.048E+02 7.091 E+03
Attachment 2 to BVY 04.081 Docket No. 50-271 Page 63 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy WetwelI Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (lbrn/s) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btuflbm)
(Btu/lbm) 402797.8 3.337E+03 1.188E+02 O.OOOE+00 1.126E+03 3.336E+03 1.158E+02 1.048E+02 7.087E+03 404047.8 3.337E+03 1.187E+02 0.000E+00 1.126E+03 3.336E+03 1.157E+02 1.047E+02 7.082E+03 405297.8 3.337E+03 1.187E+02 O.OOOE+00 1.126E+03 3.336E+03 1.156E+02 1.047E+02 7.078E+03 406547.8 3.338E+03 1.186E+02 O.OOOE+00 1.126E+03 3.336E+03 1.156E+02 1.046E+02 7.073E+03 407797.8 3.337E+03 1.185E+02 O.OOOE+00 1.126E+03 3.336E+03 1.155E+02 1.046E+02 7.069E+03 409047.8 3.337E+03 1.185E+02 0.OOOE+00 1.126E+03 3.336E+03 1.154E+02 1.045E+02 7.064E+03 410297.8 3.337E+03 1.184E+02 O.OOOE+00 1.126E+03 3.336E+03 1.154E+02 1.045E+02 7.059E+03 411547.8 3.337E+03 1.184E+02 O.OOOE+00 1.126E+03 3.336E+03 1.153E+02 1.044E+02 7.055E+03 412797.8 3.337E+03 1.183E+02 O.OOOE+00 1.126E+03 3.336E+03 1.153E+02 1.044E+02 7.050E+03 414047.8 3.337E+03 1.182E+02 O.OOOE+00 1.126E+03 3.336E+03 1.152E+02 1.044E+02 7.046E+03 415297.8 3.337E+03 1.182E+02 0.OOOE+00 1.126E+03 3.336E+03 1.152E+02 1.043E+02 7.041E+03 416547.8 3.338E+03 1.181E+02 0.OOOE+00 1.126E+03 3.336E+03 1.151E+02 1.043E+02 7.036E+03 417797.8 3.337E+03 1.181E+02 O.OOOE+00 1.126E+03 3.336E+03 1.151E+02 1.042E+02 7.032E+03 419047.8 3.337E+03 1.180E+02 0.OOOE+00 1.126E+03 3.336E+03 1.150E+02 1.042E+02 7.027E+03 420297.8 3.337E+03 1.180E+02 O.OOOE+00 1.126E+03 3.336E+03 1.150E+02 1.041E+02 7.023E+03 421547.8 3.337E+03 1.179E+02 0.OOOE+00 1.126E+03 3.336E+03 1.149E+02 1.041E+02 7.018E+03 422797.8 3.338E+03 1.179E+02 O.OOOE+00 1.126E+03 3.336E+03 1.149E+02 1.041E+02 7.013E+03 424047.8 3.337E+03 1.178E+02 0.OOOE+00 1.126E+03 3.336E+03 1.148E+02 1.040E+02 7.009E+03 425297.8 3.337E+03 1.178E+02 O.OOOE+00 1.126E+03 3.336E+03 1.148E+02 1.040E+02 7.004E+03 426547.8 3.336E+03 1.178E+02 0.OOOE+00 1.126E+03 3.336E+03 1.147E+02 1.040E+02 7.OOOE+03 427797.8 3.338E+03 1.177E+02 O.OOOE+00 1.126E+03 3.336E+03 1.147E+02 1.039E+02 6.995E+03 429047.8 3.337E+03 1.177E+02 0.OOOE+00 1.126E+03 3.336E+03 1.146E+02 1.039E+02 6.991E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page f4 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Long-Term DBA-LOCA Containment Anal sIs for Evaluation of NPSH-Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Liquid Break Liquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btulbrn) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btuls)
Pool (Btu/lbmn)
(Btuilbm) 430297.8 3.337E+03 1.176E+02 O.OOOE+00 1.126E+03 3.336E+03 1.146E+02 1.039E+02 6.986E+03 431547.8 3.337E+03 1.176E+02 O.OOOE+00 1.126E+03 3.336E+03 1.146E+02 1.038E+02 6.981E+03 432797.8 3.338E+03 1.175E+02 0.000E+00 1.126E+03 3.336E+03 1.145E+02 1.038E+02 6.977E+03 434047.8 3.337E+03 1.175E+02 0.0002+00 1.126E+03 3.336E+03 1.145E+02 1.038E+02 6.972E+03 435297.8 3.337E+03 1.174E+02 O.OOOE+00 1.126E+03 3.336E+03 1.144E+02 1.037E+02 6.968E+03 436547.8 3.337E+03 1.174E+02 O.OOOE+00 1.126E+03 3.336E+03 1.144E+02 1.037E+02 6.963E+03 437797.8 3.337E+03 1.174E+02 O.OOOE+00 1.126E+03 3.336E+03 1.144E+02 1.037E+02 6.958E+03 439047.8 3.337E+03 1.173E+02 O.OOOE+00 1.126E+03 3.336E+03 1.143E+02 1.036E+02 6.954E+03 440294.2 3.337E+03 1.173E+02 0.OOOE+00 1.126E+03 3.336E+03 1.143E+02 1.036E+02 6.949E+03 441544.2 3.336E+03 1.172E+02 O.OOOE+00 1.126E+03 3.336E+03 1.142E+02 1.036E+02 6.945E+03 442794.2 3.337E+03 1.172E+02 0.OOOE+00 1.126E+03 3.336E+03 1.142E+02 1.035E+02 6.940E+03 444044.2 3.337E+03 1.172E+02 O.OOOE+00 1.126E+03 3.336E+03 1.142E+02 1.035E+02 6.936E+03 445294.2 3.337E+03 1.171E+02 O.OOOE+00 1.126E+03 3.336E+03 1.141E+02 1.035E+02 6.931E+03 446544.2 3.336E+03 1.171E+02 O.OOOE+00 1.126E+03 3.336E+03 1.141E+02 1.034E+02 6.926E+03 447794.2 3.337E+03 1.171E+02 O.OOOE+00 1.126E+03 3.336E+03 1.141E+02 1.034E+02 6.922E+03 449044.2 3.337E+03 1.170E+02 O.OOOE+00 1.126E+03 3.336E+03 1.140E+02 1.034E+02 6.917E+03 450295.5 3.336E+03 1.170E+02 0.OOOE+00 1.126E+03 3.336E+03 1.140E+02 1.034E+02 6.913E+03 451545.5 3.333E+03 1.170E+02 O.OOOE+00 1.126E+03 3.336E+03 1.140E+02 1.033E+02 6.908E+03 452795.5 3.335E+03 1.169E+02 0.OOOE+00 1.126E+03 3.336E+03 1.139E+02 1.033E+02 6.903E+03 454045.5 3.335E+03 1.169E+02 0.OOOE+00 1.126E+03 3.336E+03 1.139E+02 1.033E+02 6.899E+03 455295.5 3.334E+03 1.168E+02 O.OOOE+00 1.126E+03 3.336E+03 1.139E+02 1.032E+02 6.894E+03 456545.5 3.333E+03 1.168E+02 0.0002+00 1.126E+03 3.336E+03 1.138E+02 1.032E+02 6.890E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 65 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Ener Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Lquld Break Liquid Break Vapor Break Vapor Break Flow to RPV enthalpy Weiwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibmls) from Spray Power (Ibm/s) (Btu/lbm) (Ibm/s) (BtuAbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(BtuAbm) 457795.5 3.335E+03 1.168E+02 0.OOOE+00 1.126E+03 3.336E+03 1.138E+02 1.032E+02 6.885E+03 459045.5 3.333E+03 1.168E+02 O.OOOE+00 1.126E+03 3.336E+03 1.138E+02 1.032E+02 6.881E+03 460295.5 3.336E+03 1.167E+02 O.OOOE+00 1.126E+03 3.336E+03 1.137E+02 1.031E+02 6.876E+03 461545.5 3.333E+03 1.167E+02 0.0002+00 1.126E+03 3.336E+03 1.137E+02 1.031E+02 6.871E+03 462795.5 3.335E+03 1.167E+02 O.OOOE+00 1.126E+03 3.336E+03 1.137E+02 1.031E+02 6.867E+03 464045.5 3.336E+03 1.166E+02 O.OOOE+00 1.126E+03 3.336E+03 1.136E+02 1.031E+02 6.862E+03 465295.5 3.335E+03 1.166E+02 O.OOOE+00 1.126E+03 3.336E+03 1.136E+02 1.030E+02 6.858E+03 466545.5 3.335E+03 1.166E+02 O.OOOE+00 1.126E+03 3.336E+03 1.136E+02 1.030E+02 6.853E+03 467795.5 3.334E+03 1.165E+02 0.000E+00 1.126E+03 3.336E+03 1.136E+02 1.030E+02 6.848E+03 469045.5 3.333E+03 1.165E+02 0.OOOE+00 1.126E+03 3.336E+03 1.135E+02 1.030E+02 6.844E+03 470295.5 3.335E+03 1.165E+02 O.OOOE+00 1.125E+03 3.336E+03 1.135E+02 1.030E+02 6.839E+03 471545.5 3.335E+03 1.164E+02 O.OOOE+00 1.125E+03 3.336E+03 1.135E+02 1.029E+02 6.835E+03 472795.5 3.335E+03 1.164E+02 0.0002+00 1.125E+03 3.336E+03 1.134E+02 1.029E+02 6.830E+03 474045.5 3.335E+03 1.1642+02 O.OOOE+00 1.125E+03 3.336E+03 1.134E+02 1.029E+02 6.825E+03 475295.5 3.335E+03 1.164E+02 0.0002+00 1.125E+03 3.336E+03 1.134E+02 1.029E+02 6.821E+03 476545.5 3.333E+03 1.163E+02 O.OOOE+00 1.125E+03 3.336E+03 1.134E+02 1.028E+02 6.816E+03 477795.5 3.335E+03 1.163E+02 O.OOOE+00 1.125E+03 3.336E+03 1.133E+02 1.028E+02 6.812E+03 479045.5 3.334E+03 1.163E+02 O.OOOE+00 1.125E+03 3.336E+03 1.133E+02 1.028E+02 6.807E+03 480295.5 3.336E+03 1.162E+02 O.OOOE+00 1.125E+03 3.336E+03 1.133E+02 1.028E+02 6.803E+03 481545.5 3.335E+03 1.162E+02 O.OOOE+00 1.125E+03 3.336E+03 1.133E+02 1.028E+02 6.798E+03 482795.5 3.335E+03 1.162E+02 0.0002+00 1.125E+03 3.336E+03 1.133E+02 1.028E+02 6.793E+03 484045.5 3.335E+03 1.162E+02 0.000E+00 1.125E+03 3.336E+03 1.132E+02 1.028E+02 6.789E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 66 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) trom Spray Power (Ibm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(Btu/lbm) 485295.5 3.336E+03 1.162E+02 O.OOOE+00 1.125E+03 3.336E+03 1.132E+02 1.027E+02 6.784E+03 486545.3 3.337E+03 1.161E+02 O.OOOE+00 1.125E+03 3.336E+03 1.132E+02 1.027E+02 6.780E+03 487795.3 3.337E+03 1.161E+02 0.OOOE+00 1.125E+03 3.336E+03 1.132E+02 1.027E+02 6.775E+03 489045.3 3.337E+03 1.161E+02 O.OOOE+00 1.125E+03 3.336E+03 1.132E+02 1.027E+02 6.770E+03 490295.3 3.337E+03 1.161E+02 O.OOOE+00 1.125E+03 3.336E+03 1.131E+02 1.027E+02 6.766E+03 491545.3 3.337E+03 1.161E+02 0.OOOE+00 1.125E+03 3.336E+03 1.131E+02 1.027E+02 6.761E+03 492795.3 3.337E+03 1.161E+02 0.0002+00 1.125E+03 3.336E+03 1.131E+02 1.026E+02 6.757E+03 494045.3 3.337E+03 1.160E+02 O.OOOE+00 1.125E+03 3.336E+03 1.131E+02 1.026E+02 8.752E+03 495295.3 3.335E+03 1.160E+02 O.OOOE+00 1.125E+03 3.336E+03 1.131E+02 1.026E+02 6.748E+03 496545.3 3.335E+03 1.160E+02 O.OOOE+00 1.125E+03 3.336E+03 1.131E+02 1.026E+02 6.743E+03 497795.3 3.337E+03 1.160E+02 O.OOOE+00 1.125E+03 3.336E+03 1.131E+02 1.026E+02 6.738E+03 499045.3 3.338E+03 1.160E+02 O.OOOE+00 1.125E+03 3.336E+03 1.130E+02 1.026E+02 6.734E+03 500295.3 3.337E+03 1.160E+02 0.OOOE+00 1.125E+03 3.336E+03 1.130E+02 1.026E+02 6.729E+03 501545.3 3.335E+03 1.159E+02 O.OOOE+00 1.125E+03 3.336E+03 1.130E+02 1.025E+02 6.725E+03 502795.3 3.335E+03 1.159E+02 O.OOOE+00 1.125E+03 3.336E+03 1.130E+02 1.025E+02 6.720E+03 504045.3 3.337E+03 1.159E+02 O.OOOE+00 1.125E+03 3.336E+03 1.130E+02 1.025E+02 6.715E+03 505295.3 3.337E+03 1.159E+02 O.OOOE+00 1.125E+03 3.336E+03 1.130E+02 1.025E+02 6.711E+03 506545.3 3.338E+03 1.158E+02 0.OOOE+00 1.125E+03 3.336E+03 1.129E+02 1.025E+02 6.706E+03 507795.3 3.337E+03 1.158E+02 0.000E+00 1.125E+03 3.336E+03 1.129E+02 1.025E+02 6.702E+03 509045.3 3.337E+03 1.158E+02 O.OOOE+00 1.125E+03 3.336E+03 1.128E+02 1.024E+02 6.697E+03 510295.3 3.337E+03 1.158E+02 O.OOOE+00 1.125E+03 3.336E+03 1.128E+02 1.024E+02 6.692E+03 511545.3 3.337E+03 1.157E+02 0.0002+00 1.125E+03 3.336E+03 1.128E+02 1.024E+02 6.688E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 67 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Enernv Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibms) (Btuilbm) (Ibmrs) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(Btu/lbm) 512795.3 3.337E+03 1.157E+02 O.OOOE+00 1.125E+03 3.336E+03 1.128E+02 1.024E+02 6.683E+03 514045.3 3.337E+03 1.157E+02 O.OOOE+00 1.125E+03 3.336E+03 1.127E+02 1.023E+02 6.679E+03 515295.3 3.335E+03 1.156E+02 O.OOOE+00 1.125E+03 3.336E+03 1.127E+02 1.023E+02 6.674E+03 516545.3 3.338E+03 1.156E+02 O.OOOE+00 1.125E+03 3.336E+03 1.127E+02 1.023E+02 6.670E+03 517795.3 3.337E+03 1.156E+02 O.OOOE+00 1.125E+03 3.336E+03 1.126E+02 1.023E+02 6.665E+03 519045.3 3.338E+03 1.155E+02 O.OOOE+00 1.125E+03 3.336E+03 1.126E+02 1.022E+02 6.660E+03 520295.3 3.337E+03 1.155E+02 O.OOOE+00 1.125E+03 3.336E+03 1.126E+02 1.022E+02 6.656E+03 521545.3 3.335E+03 1.155E+02 O.OOOE+00 1.125E+03 3.336E+03 1.126E+02 1.022E+02 6.651E+03 522795.3 3.337E+03 1.155E+02 0.000E+00 1.125E+03 3.336E+03 1.126E+02 1.022E+02 6.647E+03 524045.3 3.336E+03 1.155E+02 O.OOOE+00 1.125E+03 3.336E+03 1.125E+02 1.022E+02 6.642E+03 525295.4 3.337E+03 1.154E+02 0.000E+00 1.125E+03 3.336E+03 1.125E+02 1.022E+02 6.637E+03 526545.4 3.337E+03 1.154E+02 O.OOOE+00 1.125E+03 3.336E+03 1.125E+02 1.021E+02 6.633E+03 527795.4 3.337E+03 1.154E+02 O.OOOE+00 1.125E+03 3.336E+03 1.125E+02 1.021E+02 6.628E+03 529045.4 3.337E+03 1.153E+02 O.OOOE+00 1.125E+03 3.336E+03 1.124E+02 1.021E+02 6.624E+03 530295.4 3.335E+03 1.153E+02 O.OOOE+00 1.125E+03 3.336E+03 1.124E+02 1.021E+02 6.619E+03 531545.4 3.335E+03 1.153E+02 0.OOOE+00 1.125E+03 3.336E+03 1.124E+02 1.021E+02 6.615E+03 532795.4 3.337E+03 1.153E+02 O.OOOE+00 1.125E+03 3.336E+03 1.124E+02 1.021E+02 6.610E+03 534045.4 3.337E+03 1.153E+02 0.000E+00 1.125E+03 3.336E+03 1.124E+02 1.020E+02 6.605E+03 535295.4 3.336E+03 1.153E+02 O.OOOE+00 1.125E+03 3.336E+03 1.124E+02 1.020E+02 6.601E+03 536545.4 3.335E+03 1.152E+02 O.OOOE+00 1.125E+03 3.336E+03 1.123E+02 1.020E+02 6.596E+03 537795.4 3.339E+03 1.152E+02 O.OOOE+00 1.125E+03 3.336E+03 1.123E+02 1.020E+02 6.592E+03 539045.4 3.337E+03 1.151E+02 O.OOOE+00 1.125E+03 3.336E+03 1.123E+02 1.019E+02 6.587E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 68 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Ener-v Data from SHEX Lona-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Liquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibmhs) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(Btu/lbm) 540295.4 3.337E+03 1.151E+02 O.OOOE+00 1.125E+03 3.336E+03 1.122E+02 1.019E+02 6.582E+03 541545.4 3.337E+03 1.151E+02 O.OOOE+00 1.125E+03 3.336E+03 1.122E+02 1.019E+02 6.578E+03 542795.4 3.337E+03 1.150E+02 O.OOOE+00 1.125E+03 3.336E+03 1.122E+02 1.019E+02 6.573E+03 544045.4 3.335E+03 1.150E+02 O.OOOE+00 1.125E+03 3.336E+03 1.121E+02 1.018E+02 6.569E+03 545295.4 3.337E+03 1.150E+02 0.000E+00 1.125E+03 3.336E+03 1.121E+02 1.0182+02 6.564E+03 546545.4 3.335E+03 1.150E+02 O.OOOE+00 1.125E+03 3.336E+03 1.121E+02 1.018E+02 6.559E+03 547795.4 3.337E+03 1.150E+02 0.OOOE+00 1.125E+03 3.336E+03 1.121E+02 1.018E+02 6.555E+03 549045.4 3.338E+03 1.149E+02 0.OOOE+00 1.125E+03 3.336E+03 1.120E+02 1.018E+02 6.550E+03 550295.4 3.337E+03 1.149E+02 O.OOOE+00 1.125E+03 3.336E+03 1.120E+02 1.017E+02 6.546E+03 551545.4 3.335E+03 1.149E+02 0.OOOE+00 1.125E+03 3.336E+03 1.120E+02 1.017E+02 6.541 E+03 552795.4 3.334E+03 1.148E+02 O.OOOE+00 1.125E+03 3.336E+03 1.120E+02 1.017E+02 6.537E+03 554045.4 3.337E+03 1.148E+02 O.OOOE+00 1.125E+03 3.336E+03 1.120E+02 1.017E+02 6.532E+03 555295.4 3.337E+03 1.148E+02 O.OOOE+00 1.125E+03 3.336E+03 1.119E+02 1.017E+02 6.527E+03 556545.4 3.338E+03 1.148E+02 O.OOOE+00 1.125E+03 3.336E+03 1.119E+02 1.017E+02 6.523E+03 557795.4 3.323E+03 1.148E+02 O.OOOE+00 1.125E+03 3.336E+03 1.119E+02 1.016E+02 6.518E+03 559045.4 3.337E+03 1.147E+02 0.OOOE+00 1.125E+03 3.336E+03 1.118E+02 1.016E+02 6.514E+03 560295.4 3.337E+03 1.147E+02 O.OOOE+00 1.125E+03 3.336E+03 1.118E+02 1.016E+02 6.509E+03 561545.4 3.337E+03 1.147E+02 O.OOOE+00 1.125E+03 3.336E+03 1.118E+02 1.016E+02 6.504E+03 562795.4 3.335E+03 1.146E+02 O.OOOE+00 1.125E+03 3.336E+03 1.118E+02 1.015E+02 6.500E+03 564045.4 3.335E+03 1.146E+02 O.OOOE+00 1.125E+03 3.336E+03 1.118E+02 1.015E+02 6.495E+03 565295.4 3.335E+03 1.146E+02 O.OOOE+00 1.125E+03 3.336E+03 1.118E+02 1.015E+02 6.491 E+03 566545.4 3.337E+03 1.146E+02 O.OOOE+00 1.125E+03 3.336E+03 1.118E+02 1.015E+02 6.486E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 69 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (S) liquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btuflbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btufbm)
(Btullbm) 567795.4 3.337E+03 1.146E+02 O.OOOE+00 1.125E+03 3.336E+03 1.117E+02 1.015E+02 6.482E+03 569045.4 3.337E+03 1.146E+02 O.OOOE+00 1.125E+03 3.336E+03 1.117E+02 1.015E+02 6.477E+03 570295.4 3.337E+03 1.145E+02 O.OOOE+00 1.125E+03 3.336E+03 1.117E+02 1.014E+02 6.472E+03 571545.4 3.338E+03 1.145E+02 O.OOOE+00 1.125E+03 3.336E+03 1.116E+02 1.014E+02 6.468E+03 572795.4 3.337E+03 1.145E+02 O.OOOE+00 1.125E+03 3.336E+03 1.116E+02 1.014E+02 6.463E+03 574045.4 3.338E+03 1.145E+02 0.OOOE+00 1.125E+03 3.336E+03 1.116E+02 1.014E+02 6.459E+03 575295.4 3.337E+03 1.144E+02 O.OOOE+00 1.125E+03 3.336E+03 1.116E+02 1.014E+02 6.454E+03 576545.4 3.336E+03 1.144E+02 O.OOOE+00 1.125E+03 3.336E+03 1.115E+02 1.014E+02 6.449E+03 577795.4 3.337E+03 1.144E+02 O.OOOE+00 1.125E+03 3.336E+03 1.115E+02 1.013E+02 6.445E+03 579045.4 3.337E+03 1.143E+02 O.OOOE+00 1.125E+03 3.336E+03 1.115E+02 1.013E+02 6.440E+03 580295.4 3.336E+03 1.143E+02 O.OOOE+00 1.125E+03 3.336E+03 1.1 14E+02 1.013E+02 6.436E+03 581545.4 3.335E+03 1.143E+02 O.OOOE+00 1.125E+03 3.336E+03 1.114E+02 1.013E+02 6.431E+03 582795.4 3.337E+03 1.142E+02 O.OOOE+00 1.125E+03 3.336E+03 1.114E+02 1.012E+02 6.427E+03 584045.4 3.337E+03 1.142E+02 O.000E+00 1.125E+03 3.336E+03 1.113E+02 1.012E+02 6.422E+03 585295.4 3.338E+03 1.142E+02 O.OOOE+00 1.125E+03 3.336E+03 1.113E+02 1.012E+02 .6.417E+03 586545.4 3.340E+03 1.141E+02 0.000E+00 1.125E+03 3.336E+03 1.113E+02 1.011E+02 6.413E+03 587795.4 3.337E+03 1.141E+02 O.OOOE+00 1.125E+03 3.336E+03 1.112E+02 1.011E+02 6.408E+03 589045.4 3.337E+03 1.141E+02 O.OOOE+00 1.124E+03 3.336E+03 1.112E+02 1.011E+02 6.404E+03 590295.4 3.337E+03 1.140E+02 O.OOOE+00 1.124E+03 3.336E+03 1.112E+02 1.011E+02 6.399E+03 591545.4 3.338E+03 1.140E+02 O.OOOE+00 1.124E+03 3.336E+03 1.112E+02 1.0112+02 6.394E+03 592795.4 3.335E+03 1.140E+02 0.0002+00 1.124E+03 3.336E+03 1.112E+02 1.011E+02 6.390E+03 594045.4 3.338E+03 1.140E+02 O.OOOE+00 1.124E+03 3.336E+03 1.112E+02 1.010E+02 6.385E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 70 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Enerciv Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquld Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibmls) (Btu/lbm) (lbmts) (Btu/lbm) suppression Enthalpy (Btuts) pool (BtuAbm)
(Btu/bm) 595295.4 3.337E+03 1.140E+02 O.OOOE+00 1.124E+03 3.336E+03 1.111E+02 1.010E+02 6.381 E+03 596545.4 3.336E+03 1.139E+02 O.OOOE+00 1.124E+03 3.336E+03 1.111E+02 1.0102+02 6.376E+03 597795.4 3.338E+03 1.139E+02 O.OOOE+00 1.124E+03 3.336E+03 1.110E+02 1.010E+02 6.371 E+03 599045.4 3.337E+03 1.138E+02 0.OOOE+00 1.124E+03 3.336E+03 1.110E+02 1.009E+02 6.367E+03 600295.4 3.337E+03 1.138E+02 O.OOOE+00 1.124E+03 3.336E+03 1.110E+02 1.009E+02 6.362E+03 601545.4 3.337E+03 1.138E+02 O.OOOE+00 1.124E+03 3.336E+03 1.109E+02 1.009E+02 6.358E+03 602795.4 3.337E+03 1.138E+02 O.OOOE+00 1.124E+03 3.336E+03 1.109E+02 1.009E+02 6.353E+03 604045.4 3.335E+03 1.138E+02 0.0002+00 1.124E+03 3.336E+03 1.109E+02 1.009E+02 6.349E+03 605295.4 3.335E+03 1.138E+02 O.OOOE+00 1.124E+03 3.336E+03 1.109E+02 1.009E+02 6.344E+03 606545.4 3.340E+03 1.138E+02 O.OOOE+00 1.124E+03 3.336E+03 1.109E+02 1.009E+02 6.339E+03 607795.4 3.336E+03 1.137E+02 O.OOOE+00 1.124E+03 3.336E+03 1.109E+02 1.0082+02 6.335E+03 609045.4 3.338E+03 1.137E+02 0.OOOE+00 1.124E+03 3.336E+03 1.109E+02 1.008E+02 6.330E+03 610295.4 3.337E+03 1.136E+02 O.OOOE+00 1.124E+03 3.336E+03 1.108E+02 1.008E+02 6.326E+03 611545.4 3.337E+03 1.136E+02 O.OOOE+00 1.124E+03 3.336E+03 1.108E+02 1.007E+02 6.321E+03 612795.4 3.335E+03 1.136E+02 O.OOOE+00 1.124E+03 3.336E+03 1.108E+02 1.007E+02 6.316E+03 614045.4 3.335E+03 1.136E+02 O.OOOE+00 1.124E+03 3.336E+03 1.108E+02 1.007E+02 6.312E+03 615295.4 3.337E+03 1.136E+02 O.OOOE+00 1.124E+03 3.336E+03 1.107E+02 1.007E+02 6.307E+03 616545.4 3.337E+03 1.135E+02 O.OOOE+00 1.124E+03 3.336E+03 1.107E+02 1.007E+02 6.303E+03 617795.4 3.337E+03 1.135E+02 O.OOOE+00 1.124E+03 3.336E+03 1.107E+02 1.007E+02 6.298E+03 619045.4 3.337E+03 1.135E+02 O.OOOE+00 1.124E+03 3.336E+03 1.107E+02 1.006E+02 6.2942+03 620295.4 3.335E+03 1.135E+02 O.OOOE+00 1.124E+03 3.336E+03 1.106E+02 1.006E+02 6.289E+03 621545.4 3.337E+03 1.134E+02 O.OOOE+00 1.124E+03 3.336E+03 1.106E+02 1.006E+02 6.284E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 71 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/lbrn)
(Btu/lbm) 622795.4 3.337E+03 1.134E+02 O.OOOE+00 1.124E+03 3.336E+03 1.106E+02 1.006E+02 6.280E+03 624045.4 3.337E+03 1.134E+02 O.OOOE+00 1.124E+03 3.336E+03 1.106E+02 1.006E+02 6.275E+03 625295.4 3.339E+03 1.133E+02 0.0002+00 1.124E+03 3.336E+03 1.105E+02 1.005E+02 6.271E+03 626545.4 3.337E+03 1.133E+02 O.OOOE+00 1.124E+03 3.336E+03 1.105E+02 1.005E+02 6.266E+03 627795.4 3.335E+03 1.133E+02 O.OOOE+00 1.124E+03 3.336E+03 1.105E+02 1.005E+02 6.261 E+03 629045.4 3.335E+03 1.133E+02 O.OOOE+00 1.124E+03 3.336E+03 1.105E+02 1.005E+02 6.257E+03 630295.4 3.338E+03 1.133E+02 O.OOOE+00 1.124E+03 3.336E+03 1.105E+02 1.005E+02 6.252E+03 631545.4 3.337E+03 1.132E+02 O.OOOE+00 1.124E+03 3.336E+03 1.104E+02 1.004E+02 6.248E+03 632795.4 3.337E+03 1.132E+02 O.OOOE+00 1.124E+03 3.336E+03 1.104E+02 1.004E+02 6.243E+03 634045.4 3.336E+03 1.131E+02 O.OOOE+00 1.124E+03 3.336E+03 1.103E+02 1.0042+02 6.238E+03 635295.4 3.338E+03 1.131E+02 O.OOOE+00 1.124E+03 3.336E+03 1.103E+02 1.004E+02 6.234E+03 636545.4 3.336E+03 1.131E+02 O.OOOE+00 1.124E+03 3.336E+03 1.103E+02 1.003E+02 6.229E+03 637795.4 3.337E+03 1.130E+02 O.OOOE+00 1.124E+03 3.336E+03 1.102E+02 1.003E+02 6.225E+03 639045.4 3.337E+03 1.130E+02 O.OOOE+00 1.124E+03 3.336E+03 1.102E+02 1.003E+02 6.220E+03 640295.4 3.337E+03 1.130E+02 0.OOOE+00 1.124E+03 3.336E+03 1.102E+02 1.002E+02 6.216E+03 641545.4 3.338E+03 1.129E+02 O.OOOE+00 1.124E+03 3.336E+03 1.101E+02 1.002E+02 6.211E+03 642795.4 3.340E+03 1.129E+02 0.OOOE+00 1.124E+03 3.336E+03 1.101E+02 1.002E+02 6.206E+03 644045.4 3.337E+03 1.129E+02 O.OOOE+00 1.124E+03 3.336E+03 1.101E+02 1.002E+02 6.202E+03 645295.4 3.337E+03 1.128E+02 O.OOOE+00 1.124E+03 3.336E+03 1.100E+02 1.001E+02 6.197E+03 646545.4 3.337E+03 1.128E+02 O.OOOE+00 1.124E+03 3.336E+03 1.100E+02 1.0012+02 6.193E+03 647795.4 3.337E+03 1.128E+02 O.OOOE+00 1.124E+03 3.336E+03 1.100E+02 1.001E+02 6.188E+03 649045.4 3.337E+03 1.127E+02 O.OOOE+00 1.124E+03 3.336E+03 1.099E+02 1.001E+02 6.183E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 72 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Ener-v Data from SHEX Long-Term DBA-LOCA Containment Analvsis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (lbm/s) from Spray Power (Ibm/s) (BtuAbm) (Ibm/s) (BtuiAbm) suppression Enthalpy (Btu/s) pool (BtuAbm)
(Btuftbm) 650295.4 3.337E+03 1.127E+02 O.OOOE+00 1.124E+03 3.336E+03 1.099E+02 1.000E+02 6.179E+03 651545.4 3.335E+03 1.127E+02 0.0002+00 1.124E+03 3.336E+03 1.099E+02 1.0002+02 6.174E+03 652795.4 3.337E+03 1.127E+02 O.OOOE+00 1.124E+03 3.336E+03 1.099E+02 1.000E+02 6.170E+03 654045.4 3.337E+03 1.127E+02 O.OOOE+00 1.124E+03 3.336E+03 1.099E+02 1.000E+02 6.165E+03 655295.4 3.335E+03 1.126E+02 0.OOOE+00 1.124E+03 3.336E+03 1.099E+02 1.000E+02 6.161E+03 656545.4 3.335E+03 1.126E+02 O.OOOE+00 1.124E+03 3.336E+03 1.098E+02 9.997E+01 6.156E+03 657795.4 3.337E+03 1.126E+02 O.OOOE+00 1.124E+03 3.336E+03 1.098E+02 9.994E+01 6.151E+03 659045.4 3.338E+03 1.125E+02 O.OOOE+00 1.124E+03 3.336E+03 1.098E+02 9.991E+01 6.147E+03 660295.4 3.337E+03 1.125E+02 0.0002+00 1.124E+03 3.336E+03 1.098E+02 9.991E+01 6.142E+03 661545.4 3.337E+03 1.125E+02 O.OOOE+00 1.124E+03 3.336E+03 1.097E+02 9.989E+01 6.138E+03 662795.4 3.337E+03 1.125E+02 O.OOOE+00 1.124E+03 3.336E+03 1.097E+02 9.986E+01 6.133E+03 664045.4 3.336E+03 1.124E+02 O.OOOE+00 1.124E+03 3.336E+03 1.097E+02 9.983E+01 6.128E+03 665295.4 3.337E+03 1.124E+02 0.OOOE+00 1.124E+03 3.336E+03 1.096E+02 9.981E+01 6.124E+03 666545.4 3.337E+03 1.124E+02 O.OOOE+00 1.124E+03 3.336E+03 1.096E+02 9.978E+01 6.119E+03 667795.4 3.337E+03 1.123E+02 0.0002+00 1.124E+03 3.336E+03 1.096E+02 9.975E+01 6.115E+03 669045.4 3.338E+03 1.123E+02 O.OOOE+00 1.124E+03 3.336E+03 1.095E+02 9.972E+01 6.110E+03 670295.4 3.337E+03 1.123E+02 O.OOOE+00 1.124E+03 3.336E+03 1.095E+02 9.970E+01 6.105E+03 671545.4 3.337E+03 1.122E+02 O.OOOE+00 1.124E+03 3.336E+03 1.095E+02 9.967E+01 6.101E+03 672795.4 3.337E+03 1.122E+02 O.OOOE+00 1.124E+03 3.336E+03 1.095E+02 9.966E+01 6.096E+03 674045.4 3.337E+03 1.122E+02 0.0002+00 1.124E+03 3.336E+03 1.094E+02 9.963E+01 6.092E+03 675295.4 3.337E+03 1.121E+02 O.OOOE+00 1.124E+03 3.336E+03 1.094E+02 9.961E+01 6.087E+03 676545.4 3.335E+03 1.121E+02 0.0002+00 1.124E+03 3.336E+03 1.094E+02 9.960E+01 6.083E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 73 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Ener-v Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH rime Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Liquld Break Liquld Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btullbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(Btu/lbm) 677795.4 3.337E+03 1.121E+02 O.OOOE+00 1.124E+03 3.336E+03 1.094E+02 9.957E+01 6.078E+03 679045.4 3.337E+03 1.121E+02 O.OOOE+00 1.124E+03 3.336E+03 1.094E+02 9.957E+01 6.073E+03 680295.4 3.338E+03 1.121E+02 O.OOOE+00 1.124E+03 3.336E+03 1.093E+02 9.956E+01 6.069E+03 681545.5 3.336E+03 1.120E+02 O.OOOE+00 1.124E+03 3.336E+03 1.093E+02 9.954E+01 6.064E+03 682795.5 3.336E+03 1.120E+02 O.OOOE+00 1.124E+03 3.336E+03 1.093E+02 9.951E+01 6.060E+03 684045.5 3.335E403 1.120E+02 O.OOOE+00 1.124E+03 3.336E+03 1.092E+02 9.948E+01 6.055E+03 685295.6 3.334E+03 1.1 19E+02 O.OOOE+00 1.124E+03 3.336E+03 1.092E+02 9.946E+01 6.050E+03 686545.6 3.336E403 1.119E+02 O.OOOE+00 1.124E+03 3.336E+03 1.092E+02 9.943E+01 6.046E+03 687795.6 3.333E+03 1.1 19E+02 O.OOOE+00 1.124E+03 3.336E+03 1.091E+02 9.941E+01 6.041 E+03 689045.6 3.335E+03 1.118E+02 O.OOOE+00 1.124E+03 3.336E+03 1.091 E+02 9.938E+01 6.037E+03 690295.6 3.335E403 1.118E+02 O.OOOE+00 1.124E+03 3.336E+03 1.091E+02 9.938E+01 6.032E+03 691545.9 3.338Ee03 1.118E+02 O.OOOE+00 1.124E+03 3.336E+03 1.091E+02 9.937E+01 6.028E+03 692795.9 3.338E+03 1.118E+02 0.OOOE+00 1.124E+03 3.336E+03 1.091E+02 9.936E+01 6.023E+03 694045.9 3.337E403 1.118E+02 O.OOOE+00 1.124E+03 3.336E+03 1.091E+02 9.933E+01 6.018E+03 695295.9 3.337E+03 1.118E+02 O.OOOE+00 1.124E+03 3.336E+03 1.090E+02 9.932E+01 6.014E+03 696545.9 3.337E403 1.117E+02 O.OOOE+00 1.124E+03 3.336E+03 1.090E+02 9.931E+01 6.009E+03 697795.9 3.336E+03 1.117E+02 O.OOOE+00 1.124E+03 3.336E+03 1.090E+02 9.928E+01 6.005E+03 699045.9 3.337E+03 1.117E+02 O.OOOE+00 1.124E+03 3.336E+03 1.090E+02 9.925E+01 6.OOOE+03 700295.9 3.337E+03 1.117E+02 O.OOOE+00 1.124E+03 3.336E+03 1.089E+02 9.923E+01 5.995E+03 701545.9 3.337E+03 1.1 16E+02 0.OOOE+00 1.124E+03 3.336E+03 1.089E+02 9.923E+01 5.991E+03 702795.9 3.337E403 1.1 16E+02 O.OOOE+00 1.123E+03 3.336E+03 1.089E+02 9.920E+01 5.986E+03 704045.9 3.337E+03 1.116E+02 O.OOOE+00 1.123E+03 3.336E+03 1.089E+02 9.917E+01 5.982E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 74 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) ftrm Spray Power (lbm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(BtufLbm) 705295.9 3.337E+03 1.115E+02 O.OOOE+00 1.123E+03 3.336E+03 1.088E+02 9.914E+01 5.977E+03 706545.9 3.337E+03 1.115E+02 O.OOOE+00 1.123E+03 3.336E+03 1.088E+02 9.914E+01 5.973E+03 707795.9 3.335E+03 1.115E+02 O.OOOE+00 1.123E+03 3.336E+03 1.088E+02 9.913E+01 5.968E+03 709045.9 3.337E+03 1.115E+02 O.OOOE+00 1.123E+03 3.336E+03 1.088E+02 9.911E+01 5.963E+03 710295.9 3.337E+03 1.115E+02 O.OOOE+00 1.123E+03 3.336E+03 1.088E+02 9.909E+01 5.959E+03 711545.9 3.337E+03 1.114E+02 O.OOOE+00 1.123E+03 3.336E+03 1.087E+02 9.906E+01 5.954E+03 712795.9 3.337E+03 1.114E+02 O.OOOE+00 1.123E+03 3.336E+03 1.087E+02 9.904E+01 5.950E+03 714045.9 3.338E+03 1.114E+02 0.OOOE+00 1.123E+03 3.336E+03 1.087E+02 9.903E+01 5.945E+03 715295.9 3.335E+03 1.113E+02 O.OOOE+00 1.123E+03 3.336E+03 1.086E+02 9.900E+01 5.940E+03 716545.9 3.337E+03 1.113E+02 0.0002+00 1.123E+03 3.336E+03 1.086E+02 9.897E+01 5.936E+03 717795.9 3.335E+03 1.113E+02 O.OOOE+00 1.123E+03 3.336E+03 1.086E+02 9.895E+01 5.931E+03 719045.9 3.337E+03 1.113E+02 O.OOOE+00 1.123E+03 3.336E+03 1.086E+02 9.893E+01 5.927E+03 720295.9 3.337E+03 1.112E+02 O.OOOE+00 1.123E+03 3.336E+03 1.085E+02 9.890E+01 5.922E+03 721545.9 3.335E+03 1.112E+02 O.OOOE+00 1.123E+03 3.336E+03 1.085E+02 9.889E+01 5.917E+03 722795.9 3.336E+03 1.112E+02 0.000E+00 1.123E+03 3.336E+03 1.085E+02 9.885E+01 5.913E+03 724045.9 3.337E+03 1.111E+02 O.OOOE+00 1.123E+03 3.336E+03 1.084E+02 9.883E+01 5.908E+03 725295.9 3.336E+03 1.111E+02 O.OOOE+00 1.123E+03 3.336E+03 1.084E+02 9.880E+01 5.904E+03 726545.9 3.337E+03 1.111E+02 O.OOOE+00 1.123E+03 3.336E+03 1.084E+02 9.878E+01 5.899E+03 727795.9 3.337E+03 1.110E+02 O.OOOE+00 1.123E+03 3.336E+03 1.083E+02 9.875E+01 5.895E+03 729045.9 3.336E+03 1.110E+02 O.OOOE+00 1.123E+03 3.336E+03 1.083E+02 9.874E+01 5.890E+03 730295.9 3.338E+03 1.110E+02 O.OOOE+00 1.123E+03 3.336E+03 1.083E+02 9.872E+01 5.885E+03 731545.9 3.337E+03 1.109E+02 O.OOOE+00 1.123E+03 3.336E+03 1.083E+02 9.869E+01 5.881E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 75 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Enery Datarom SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywall and Core (s) Liquld Break Liquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (BtuIbm) (Ibm/s) (Btuflbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(Btu/lbm) 732795.9 3.337E+03 1.109E402 0.OOOE+00 1.123E+03 3.336E+03 1.082E+02 9.865E+01 5.876E+03 734045.9 3.337E+03 1.109E+02 0.OOOE2+00 1.123E+03 3.336E+03 1.082E+02 9.864E+01 5.872E+03 735295.9 3.337E.03 1.109E+02 0.000E+00 I1.123E+03 3.336E+03 1.082E+02 9.861E+01 5.867E+03 736545.9 3.337E+03 1.108E+02 0.000E+00 1.123E+03 3.336E+03 1.081 E+02 9.858E+01 5.862E+03 737795.9 3.337E403 1.109E+02 0.0001E+00 1.123E+03 3.336E+03 1.081 E+02 9.859E+01 5.858E+03 739045.9 3.336E+03 1.109E+02 0.OOOE+00 I1.123E+03 3.336E+03 1.081E+02 9.858E+01 5.853E+03 740295.9 3.336E403 1.109E+02 0.000E+00 I1.123E+03 3.336E+03 1.081E+02 9.858E+01 5.849E+03 741545.9 3.336E+03 1.109E+02 O.OOOE+00 1.123E+03 3.336E+03 1.081 E+02 9.858E+01 5.844E+03 742795.9 3.336E+03 1.109E+02 0.000E400 1.123E+03 3.336E+03 1.081 E+02 9.858E+01 5.840E+03 744045.9 3.335E+03 1.109E+02 0.OOOE+00 I1.123E.03 3.336E+03 1.081E+02 9.858E+01 5.835E+03 745295.9 3.337E+03 1.108E402 0.OOOE+00 1.123E+03 3.336E+03 1.081E+02 9.857E+01 5.830E+03 746545.9 3.339E+03 1.108E+02 o.000E*00 1.123E403 3.336E+03 1.081 E+02 9.856E+01 5.826EI03 747795.9 3.336E+03 1.108E402 0.000E+00 1.123E+03 3.336E403 1.081E+02 9.856E+01 5.821E+03 749045.9 3.336E+03 1.108E4+02 0.OOOE+00 1.123E+03 3.336E+03 1.081E+02 9.857E+01 5.817E+03 750295.9 3.340E.03 1.108E+02 0.000E400 1.123E+03 3.336E+03 1.081E+.02 9.857E+01 5.812E+03 751545.9 3.338E+03 1.108E+02 0.OOOE+00 1.123E+03 3.336E+03 1.081 E+02 9.857E+01 5.807E+03 752795.9 3.338E+03 I1.108E402 O.OOOE.00 1.123E+03 3.336E+03 1.081E+02 9.856E+01 5.803E4+03 754045.9 3.338E403 1.108E.02 0.000E+O0 1.123E+03 3.336E+03 1.081E+02 9.855E+01 5.798E+03 755295.9 3.337E+03 1.107E+02 0.OOOE2+00 I1.123E+03 3.336E+03 1.081 E+02 9.851 E+01 5.794E+03 756545.9 3.336E+03 1.107E+02 O.0001E+00 1.123E+03 3.336E+03 1.080E+02 9.848E+01 5.789E+03 757795.9 3.339E.03 1.106E.02 O.OOOEO00 1.123E.03 3.336E.03 1.080E+02 9.845E+01 5.784E+03 759045.9 3.337E+03 1.106E+02 O.OOOE+00 1.123E+03 3.336E+03 1.079E+02 9.841E+01 5.780E403
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 76 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Enervy Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquld Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (lbm/s) from Spray Power (Ibm/s) (Btullbm) (lbmls) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(Btu/lbm) 760295.9 3.338E+03 1.105E+02 O.OOOE+00 1.123E+03 3.336E+03 1.079E+02 9.838E+01 5.775E+03 761545.9 3.337E+03 1.105E+02 O.OOOE+00 1.123E+03 3.336E+03 1.078E+02 9.835E+01 5.771E+03 762795.9 3.337E+03 1.105E+02 0.0002+00 1.123E+03 3.336E+03 1.078E+02 9.831E+01 5.766E+03 764045.9 3.337E+03 1.104E+02 O.OOOE+00 1.123E+03 3.336E+03 1.078E+02 9.828E+01 5.762E+03 765295.9 3.337E+03 1.104E+02 O.OOOE+00 1.123E+03 3.336E+03 1.077E+02 9.826E+01 5.757E+03 766545.9 3.337E+03 1.103E+02 O.OOOE+00 1.123E+03 3.336E+03 1.077E+02 9.822E+01 5.752E+03 767795.9 3.336E+03 1.103E+02 0.000E+00 1.123E+03 3.336E+03 1.077E+02 9.819E+01 5.748E+03 769045.9 3.338E+03 1.103E+02 O.OOOE+00 1.123E+03 3.336E+03 1.076E+02 9.817E+01 5.743E+03 770295.9 3.337E+03 1.102E+02 O.OOOE+00 1.123E+03 3.336E+03 1.076E+02 9.813E+01 5.739E+03 771545.9 3.338E+03 1.102E+02 0.0002+00 1.123E+03 3.336E+03 1.076E+02 9.812E+01 5.734E+03 772795.9 3.337E+03 1.102E+02 0.OOOE+00 1.123E+03 3.336E+03 1.076E+02 9.811E+01 5.729E+03 774045.9 3.337E+03 1.102E+02 0.OOOE+00 1.123E+03 3.336E+03 1.075E+02 9.808E+01 5.725E+03 775295.9 3.338E+03 1.102E+02 O.OOOE+00 1.123E+03 3.336E+03 1.075E+02 9.807E+01 5.720E+03 776545.9 3.337E+03 1.101E+02 0.OOOE+00 1.123E+03 3.336E+03 1.075E+02 9.805E+01 5.716E+03 777795.9 3.337E+03 1.101E+02 O.OOOE+00 1.123E+03 3.336E+03 1.075E+02 9.802E+01 5.711 E+03 779045.9 3.335E+03 1.101E+02 0.OOOE+00 1.123E+03 3.336E+03 1.074E+02 9.799E+01 5.707E+03 780295.9 3.337E+03 1.100E+02 O.OOOE+00 1.123E+03 3.336E+03 1.074E+02 9.797E+01 5.702E+03 781545.9 3.337E+03 1.100E+02 O.OOOE+00 1.123E+03 3.336E+03 1.073E+02 9.793E+01 5.697E+03 782795.9 3.337E+03 1.100E+02 O.OOOE+00 1.123E+03 3.336E+03 1.073E+02 9.792E+01 5.693E+03 784045.9 3.338E+03 1.099E+02 O.OOOE+00 1.123E+03 3.336E+03 1.073E+02 9.792E+01 5.688E+03 785295.9 3.337E+03 1.099E+02 O.OOOE+00 1.123E+03 3.336E+03 1.073E+02 9.788E+01 5.684E+03 786545.9 3.337E+03 1.099E+02 0.OOOE+00 1.123E+03 3.336E+03 1.073E+02 9.787E+01 5.679E+03
Attachment 2 to BW 04-081 Docket No. 50-271 Page 77 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Energy Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquld Break Uquld Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/bm)
(Btuibm) 787795.9 3.338E+03 1.098E+02 0.OOOE.00 1.123E+03 3.336E+03 1.072E+02 9.784E+01 5.674E+03 789045.9 3.337E+03 1.098E+02 0.OOOE+00 1.123E+03 3.336E+03 1.072E+02 9.781 E+01 5.670E+03 790295.9 3.334E+03 1 .098E+02 0.OOOE+00 1.123E+03 3.336E+03 1.072E+02 9.778E+01 5.665E+03 791545.9 3.338E+03 I1.098E+02 0.OOOEO00 1.123E+03 3.336E+03 1.071E+02 9.778E+01 5.661 E+03 792795.9 3.336E+03 1.097E+02 0.OOQE+00 1.123E403 3.336E+03 1.071 E+02 9.775E+01 5.656E+03 794045.9 3.335E.03 I1.097E+02 0.OOOE+00 1.123E+03 3.336E403 1.071 E+02 9.772E+01 5.651E+03 795295.9 3.337E+03 I1.097E402 0.000E400 I1.123E+03 3.336E+03 1.070E+02 9.769E+01 5.647E+03 796545.9 3.338E+03 1.096E402 0.OOOE+00 1.123E+03 3.336E+03 1.070E+02 9.767E+01 5.642E+03 797795.9 3.337E+03 I1.096E402 0.OOOE+00 1.123E+03 3.336E+03 1.070E+02 9.764E+01 5.638E+03 799045.9 3.337E+03 1.096E+02 0.OOOEO00 1.123E403 3.336E+03 1.070E+02 9.763E+01 5.633E+03 800295.9 3.337E403 I1.095E402 0.OOOE+00 1.123E+03 3.336E+03 1.069E+02 9.759E+01 5.629E+03 801545.9 3.337E403 1.095E402 0.OOOE+00 1.123E+03 3.336E+03 1.069E+02 9.757E+01 5.624E+03 802795.9 3.337E.03 I1.095E.02 0.OOOE+00 1.123E4+03 3.336E+03 1.069E+02 9.754E+01 5.619E+03 804045.9 3.338E.03 1.095E.02 0.OOOE+00 1.123E+03 3.336E+03 1.069E+02 9.754E+01 5.615E+03 805295.9 3.338E+03 I1.095E.02 0.OOOEOO0 I1.123E+03 3.336E+03 1.069E+02 9.754E+01 5.610E+03 806545.9 3.335E+03 1.095E.02 0.OOOE+00 1.123E+03 3.336E+03 1.069E+02 9.754E+01 5.606E+03 807795.9 3.337E+03 I1.094E+02 0.OOOE+00 1.123E+03 3.336E+03 1.068E+02 9.752E+01 5.601E+03 809045.9 3.338E+03 I1.094E+02 O.OOOE+00 1.123E+03 3.336E+03 1.068E+02 9.749E+01 5.596E+03 810295.9 3.335E+03 I1.094E+02 0.OOOE+00 1.123E+03 3.336E+03 1.068E+02 9.745E+01 5.592E+03 811545.9 3.338E+03 I1.093E+02 0.OOOE+00 1.123E+03 3.336E+03 1.067E+02 9.743E+01 5.587E+03 812795.9 3.340E+03 I1.093E+02 0.OOOE2+00 I1.123E+03 3.336E+03 1.067E+02 9.740E+01 5.583E+03 814045.9 3.340E+03 I .093E4+02 0.OOOE+00 1.123E+03 3.336E+03 1.067E+02 9.740E+01 5.578E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 78 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Enerqv Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquld Break Uquld Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) from Spray Power (Ibm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btuibm)
(Btulbm) 815295.9 3.340E+03 1.093E+02 O.OOOE+00 1.123E+03 3.336E+03 1.067E+02 9.740E+01 5.574E+03 816545.9 3.340E+03 1.093E+02 0.000E+OO 1.123E+03 3.336E+03 1.067E+02 9.740E+01 5.569E+03 817795.9 3.337E+03 1.093E+02 O.OOOE+0O 1.123E+03 3.336E+03 1.067E+02 9.739E+01 5.564E+03 819045.9 3.337E+03 1.092E+02 O.OOOE+00 1.123E+03 3.336E+03 1.066E+02 9.736E+01 5.560E+03 820295.9 3.337E+03 1.092E+02 0.OOOE+OO 1.122E+03 3.336E+03 1.066E+02 9.733E+01 5.555E+03 821545.9 3.337E+03 1.091E+02 O.OOOE+00 1.122E+03 3.336E+03 1.066E+02 9.730E+01 5.551E+03 822795.9 3.337E+03 1.091E+02 O.000E+00 1.122E+03 3.336E+03 1.065E+02 9.727E+01 5.546E+03 824045.9 3.338E+03 1.091E+02 O.OOOE+0O 1.122E+03 3.336E+03 1.065E+02 9.725E+01 5.541 E+03 825295.9 3.337E+03 1.091E+02 0.000E+O0 1.122E+03 3.336E+03 1.065E+02 9.724E+01 5.537E+03 826545.9 3.337E+03 1.090E+02 O.OOOE+00 1.122E+03 3.336E+03 1.065E+02 9.721E+01 5.532E+03 827795.9 3.336E+03 1.090E+02 O.OOOE+O0 1.122E+03 3.336E+03 1.064E+02 9.718E+01 5.528E+03 829045.9 3.337E+03 1.090E+02 O.OOOE+00 1.122E+03 3.336E+03 1.064E+02 9.715E+01 5.523E+03 830295.9 3.337E+03 1.089E+02 O.OOOE+00 1.122E+03 3.336E+03 1.063E+02 9.712E+01 5.519E+03 831545.9 3.337E+03 1.089E+02 O.OOOE+00 1.122E+03 3.336E+03 1.063E+02 9.710E+01 5.514E+03 832795.9 3.337E+03 1.088E+02 O.OOOE+O0 1.122E+03 3.336E+03 1.063E+02 9.706E+01 5.509E+03 834045.9 3.338E+03 1.088E+02 O.OOOE+00 1.122E+03 3.336E+03 1.063E+02 9.706E+01 5.505E+03 835295.9 3.337E+03 1.088E+02 O.OOOE+00 1.122E+03 3.336E+03 1.063E+02 9.705E+01 5.500E+03 836545.9 3.336E+03 1.088E+02 0.OOOE+00 1.122E+03 3.336E+03 1.062E+02 9.702E+01 5.496E+03 837795.9 3.337E+03 1.088E+02 O.OOOE+00 1.122E+03 3.336E+03 1.062E+02 9.701E+01 5.491E+03 839045.9 3.337E+03 1.087E+02 O.OOOE+O0 1.122E+03 3.336E+03 1.062E+02 9.698E+01 5.486E+03 840295.9 3.338E+03 1.087E+02 O.OOOE+00 1.122E+03 3.336E+03 1.061E+02 9.696E+01 5.482E+03 841545.9 3.338E+03 1.087E+02 O.OOOE+00 1.122E+03 3.336E+03 1.061E+02 9.696E+01 5.477E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 79 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-32-6 Mass and Enerqv Data from SHEX Long-Term DBA-LOCA Containment Analysis for Evaluation of NPSH Time Vessel Vessel Vessel Vessel Total ECCS ECCS flow Drywell and Core (s) Uquid Break Uquid Break Vapor Break Vapor Break Flow to RPV enthalpy Wetwell Thermal Flow Rate Enthalpy Flow Rate Enthalpy (Ibm/s) romn Spray Power (Ibm/s) (Btu/lbm) (Ibm/s) (Btu/lbm) suppression Enthalpy (Btu/s) pool (Btu/lbm)
(Btu/lbm) 842795.9 3.334E+03 1.087E+02 O.OOOE+00 1.122E+03 3.336E+03 1.061E+02 9.694E+01 5.473E+03 844045.9 3.337E+03 1.087E+02 O.OOOE+00 1.122E+03 3.336E+03 1.061E+02 9.691E+01 5.468E+03 845295.9 3.337E+03 1.086E+02 O.OOOE+00 1.122E+03 3.336E+03 1.061E+02 9.690E+01 5.463E+03 846545.9 3.337E+03 1.086E+02 O.OOOE+00 1.122E+03 3.336E+03 1.060E+02 9.687E+01 5.459E+03 847795.9 3.337E+03 1.086E+02 0.0002+00 1.122E+03 3.336E+03 1.060E+02 9.684E+01 5.454E+03 849045.9 3.336E+03 1.085E+02 O.OOOE+00 1.122E+03 3.336E+03 1.060E+02 9.682E+01 5.450E+03 850295.9 3.337E+03 1.085E+02 0.OOOE+00 1.122E+03 3.336E+03 1.059E+02 9.679E+01 5.445E+03 851545.9 3.339E+03 1.085E+02 O.OOOE+00 1.122E+03 3.336E+03 1.059E+02 9.677E+01 5.441 E+03 852795.9 3.337E+03 1.085E+02 O.OOOE+00 1.122E+03 3.336E+03 1.059E+02 9.676E+01 5.436E+03 854045.9 3.337E+03 1.084E+02 O.OOOE+00 1.122E+03 3.336E+03 1.059E+02 9.672E+01 5.431E+03 855295.9 3.337E+03 1.084E+02 O.OOOE+00 1.122E+03 3.336E+03 1.058E+02 9.670E+01 5.427E+03 856545.9 3.337E+03 1.083E+02 0.0002+00 1.122E+03 3.336E+03 1.058E+02 9.667E+01 5.422E+03 857795.9 3.339E+03 1.083E+02 O.OOOE+00 1.122E+03 3.336E+03 1.058E+02 9.666E+01 5.418E+03 859045.9 3.338E+03 1.083E+02 O.OOOE+00 1.122E+03 3.336E+03 1.057E+02 9.663E+01 5.413E+03 860295.9 3.337E+03 1.083E+02 O.OOOE+00 1.122E+03 3.336E+03 1.057E+02 9.661E+01 5.408E+03 861545.9 3.339E+03 1.082E+02 O.OOOE+00 1.122E+03 3.336E+03 1.057E+02 9.658E+01 5.404E+03 862795.9 3.338E+03 1.082E+02 O.OOOE+00 1.122E+03 3.336E+03 1.057E+02 9.656E+01 5.399E+03 864000 3.336E+03 1.082E+02 O.OOOE+00 1.122E+03 3.336E+03 1.056E+02 9.653E+01 5.395E+03
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 80 of 123 NON-PROPRIETARY INFORMATION FIGURE SPSB-C-32-1 VYNPS DBA-LOCA SHEX ANALYSIS MODEL SCHEMATIC I
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 81 of 123 NON-PROPRIETARY INFORMATION RAI SPSB-C-33 Please provide the results of the containment accident pressure calculation used for ECCS pump NPSH calculations. Include:
a) drywell pressure vs. time b) drywell temperature vs. time c) wetwell pressure vs. time d) wetwell air temperature vs. time e) suppression pool temperature vs. time f) suppression pool level vs. time Response to RAI SPSB-C-33 Figures SPSB-C-33-1 and SPSB-C-33-2 provide the containment response histories for the short-term (600 second) SHEX containment analysis used for ECCS pump NPSH calculations. Figures SPSB-C-33-3 and SPSB-C-33-4 provide the containment response histories for the long-term short-term (10 day) SHEX containment analysis used for ECCS pump NPSH calculations.
Tables SPSB-C-33-1 and SPSB-C-33-2 contain tabular data with time varying containment response parameters requested in NRC RAI SPSB-C-33.
Table SPSB-C-33-1 provides drywell pressure (without leakage effects accounted for) and temperature, wetwell airspace pressure (with and without leakage effects) and temperature, suppression pool temperature and suppression pool volume vs. time from the short-term (600 second) SHEX containment analysis used for ECCS pump NPSH calculabons.
Table SPSB-C-33-2 provides drywell pressure (with leakage effects not accounted for) and temperature, wetwell airspace pressure (with and without leakage effects) and temperature, suppression pool temperature and suppression pool volume vs. time from the long-term (10 day) SHEX containment analysis used for ECCS pump NPSH calculations. I[
)) The suppression pool temperature at the time the long-term wetwell pressure falls to 14.7 psia is 143.50F.
Figures SPSB-C-33-5 and SPSB-C-33-6 show suppression pool water level response for the short-term and long-term post-LOCA, respectively. The SHEX suppression pool volume was converted to an equivalent level using VYNPS suppression pool geometric data. The NPSH calculation was not based on a time-dependent level. Short-term NPSH was determined at 600 seconds using a level of 11.93 ft. The SHEX equivalent
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 82 of 123 NON-PROPRIETARY INFORMATION level is 12.24 ft. Long-term NPSH was determined using a level of 12.03 ft. The SHEX equivalent at the peak suppression pool temperature was 12.27 ft. The levels used for the NPSH calculation are based on the current licensing basis.
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 83 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-1 SHEX Short-Term (600 sec) DBA-LOCA Containment Response for NPSIHI Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 0 16.40 170.0 14.70 90.0 14.70 90.0 6.800E+04 0.674805 29.33 231.0 19.14 125.8 19.14 90.7 6.814E+04 3.487305 37.50 261.5 27.14 135.8 27.14 97.3 6.918E+04 12.11231 37.24 262.9 28.79 120.2 28.79 118.1 7.264E+04 20.98731 33.36 298.5 30.34 129.8 30.34 130.5 7.406E+04 28.75293 33.30 256.4 30.99 134.0 30.99 134.4 7.437E+04 32.12793 33.10 256.0 31.04 134.2 31.04 135.4 7.439E+04 35.40918 33.12 256.1 31.05 134.3 31.05 136.1 7.449E+04 39.65918 33.16 256.1 31.07 134.3 31.07 136.9 7.461 E+04 56.22168 33.23 256.2 31.15 134.2 31.15 139.4 7.507E+04 72.56543 32.94 255.7 31.21 134.1 31.21 140.4 7.547E+04 95.09668 31.01 252.2 31.48 135.0 31.48 142.2 7.639E+04 106.1592 29.69 248.0 30.18 127.6 30.18 144.1 7.684E+04 116.7217 28.17 242.4 28.65 124.2 28.65 146.0 7.733E+04 127.2842 26.62 236.1 27.12 120.7 27.12 147.8 7.785E+04 136.8467 25.08 229.4 25.55 116.8 25.55 149.3 7.822E+04 147.7529 23.56 222.1 24.05 113.1 24.05 150.8 7.864E+04 161.2842 22.06 213.9 22.55 109.2 22.54 152.5 7.914E+04 176.5654 20.57 205.0 21.08 105.2 21.08 154.0 7.934E+04 190.3154 19.55 198.0 20.03 102.4 20.03 155.0 7.945E+04 207.1279 18.62 190.9 19.09 100.0 19.09 156.1 7.951 E+04 226.4717 17.91 184.8 18.41 98.8 18.41 157.1 7.956E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 84 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-1 SHEX Short-Term (600 sec) DBA-LOCA Containment Response for NPSH Evaluation Time (see) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 246.3154 17.48 180.6 17.95 98.3 17.94 157.9 7.956E+04 273.8467 17.14 177.1 17.63 98.9 17.63 158.8 7.956E+04 301.4092 16.99 175.1 17.47 100.0 17.47 159.6 7.952E+04 332.7217 16.93 174.0 17.40 101.5 17.40 160.4 7.949E+04 367.6279 16.92 173.4 17.40 103.2 17.40 161.2 7.945E+04 398.2529 16.93 173.1 17.41 104.5 17.41 161.9 7.943E+04 429.1904 16.95 173.0 17.44 105.8 17.44 162.4 7.942E+04 460.6904 17.00 173.0 17.44 106.9 17.44 163.0 7.940E+04 491.6904 17.03 173.0 17.49 108.1 17.49 163.5 7.940E+04 522.6904 17.07 173.2 17.54 109.1 17.54 164.0 7.939E+04 553.7529 17.11 173.3 17.58 110.0 17.58 164.5 7.939E+04 585.0029 17.14 173.5 17.64 111.0 17.64 164.9 7.939E+04 600.0654 17.17 173.6 17.64 111.3 17.64 165.1 7.939E+04
Attachment 2 to BW 04-081 Docket No. 50-271 Page 85 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Lona-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 0 16.40 170.00 14.70 90.0 14.70 90.0 6.800E+04 138.1357 29.74 248.30 30.22 127.6 30.22 149.2 7.681 E+04 236.792 24.38 227.40 24.87 114.0 24.87 157.4 7.677E+04 353.1982 19.86 201.10 20.35 105.0 20.34 162.5 7.769E+04 500.0107 18.16 186.20 18.65 106.8 18.65 166.1 7.818E+04 552.042 18.01 184.20 18.50 108.6 18.49 167.1 7.825E+04 785.6045 17.28 167.70 17.71 149.8 17.71 169.7 7.921 E+04 1097.855 17.52 168.80 17.94 152.1 17.94 171.8 7.926E+04 1410.355 17.70 169.90 18.19 154.3 18.19 173.7 7.930E+04 1722.073 17.91 171.00 18.36 155.4 18.36 175.3 7.933E+04 2033.355 18.09 171.90 18.57 156.5 18.57 176.6 7.936E+04 2343.417 18.28 172.80 18.78 158.2 18.77 177.9 7.938E+04 2653.073 18.48 173.60 18.96 159.3 18.95 179.0 7.941 E+04 2962.323 18.68 174.40 19.18 160.2 19.17 180.0 7.942E+04 3270.355 18.90 175.10 19.38 161.8 19.37 181.0 7.943E+04 3578.792 19.09 175.70 19.59 163.2 19.58 181.9 7.944E+04 3887.23 19.27 176.30 19.77 163.9 19.76 182.6 7.944E+04 4196.48 19.43 176.90 19.91 164.8 19.90 183.4 7.944E+04 4506.136 19.58 177.40 20.06 165.2 20.05 184.0 7.946E+04 4815.792 19.73 177.80 20.22 165.9 20.20 184.6 7.946E+04 5125.042 19.87 178.30 20.36 166.7 20.34 185.2 7.946E+04 5434.23 20.01 178.70 20.50 167.6 20.49 185.7 7.947E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 86 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (see) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 5736.948 20.15 179.10 20.63 167.9 20.61 186.2 7.947E+04 6031.792 20.30 179.40 20.77 168.5 20.76 186.7 7.947E+04 6275.292 20.42 179.70 20.83 168.3 20.82 187.0 7.947E+04 6534.73 20.51 180.00 21.00 169.6 20.98 187.4 7.946E+04 6814.355 20.63 180.30 21.10 170.7 21.08 187.7 7.947E+04 7115.386 20.73 180.60 21.23 171.9 21.21 188.1 7.947E+04 7420.605 20.86 180.90 21.34 173.1 21.32 188.5 7.947E+04 7724.355 20.96 181.10 21.44 174.0 21.42 188.8 7.947E+04 8035.636 21.03 181.40 21.52 174.7 21.50 189.1 7.947E+04 8346.917 21.10 181.70 21.58 175.2 21.56 189.5 7.948E+04 8659.011 21.16 181.90 21.65 175.6 21.63 189.8 7.949E+04 8971.105 21.21 182.10 21.70 176.0 21.68 190.0 7.950E+04 9282.792 21.26 182.30 21.74 176.3 21.72 190.3 7.950E+04 9595.292 21.30 182.50 21.80 176.6 21.78 190.6 7.951 E+04 9907.386 21.35 182.70 21.84 176.9 21.81 190.8 7.951 E+04 10219.89 21.38 182.90 21.88 177.1 21.86 191.0 7.953E+04 10531.98 21.43 183.10 21.91 177.3 21.88 191.2 7.953E+04 10844.48 21.46 183.30 21.95 177.5 21.93 191.4 7.954E+04 11469.07 21.53 183.60 22.02 177.9 21.99 191.8 7.956E+04 12093.67 21.60 183.90 22.09 178.3 22.06 192.2 7.957E+04 12718.67 21.66 184.20 22.15 178.7 22.12 192.5 7.957E+04 13343.26 21.72 184.40 22.20 179.0 22.17 192.8 7.959E+04 13968.26 21.76 184.70 22.26 179.3 22.23 193.1 7.960E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 87 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 14592.01 21.82 184.90 22.30 179.6 22.26 193.4 7.960E+04 15169.6 21.86 185.10 22.35 179.9 22.31 193.6 7.961 E+04 15794.6 21.90 185.20 22.38 180.0 22.34 193.8 7.961 E+04 16419.61 21.92 185.40 22.42 180.2 22.38 194.0 7.963E+04 17044.2 21.96 185.50 22.44 180.4 22.39 194.2 7.962E+04 17669.2 21.98 185.60 22.47 180.5 22.43 194.3 7.962E+04 18293.79 22.00 185.70 22.49 180.7 22.44 194.4 7.964E+04 18906.76 22.02 185.70 22.51 180.8 22.46 194.5 7.963E+04 19531.76 22.02 185.80 22.52 180.9 22.47 194.6 7.963E+04 20156.36 22.03 185.80 22.52 180.9 22.46 194.6 7.963E+04 20781.36 22.04 185.80 22.53 181.0 22.48 194.6 7.963E+04 21406.36 22.04 185.80 22.53 181.0 22.48 194.6 7.963E+04 22030.95 22.04 185.80 22.53 181.0 22.47 194.6 7.963E+04 22655.95 22.04 185.80 22.53 181.0 22.47 194.6 7.963E+04 23244.98 22.06 185.80 22.54 181.2 22.48 194.7 7.962E+04 23811.7 22.06 185.80 22.54 181.2 2248 194.7 7.962E+04 23869.98 22.06 185.80 22.55 181.2 22.48 194.7 7.963E+04 24494.98 22.05 185.80 22.54 181.2 22.48 194.7 7.962E+04 25119.98 22.05 185.80 22.54 181.2 22.47 194.7 7.962E+04 25744.98 22.05 185.80 22.54 181.2 22.47 194.6 7.962E+04 26369.98 22.04 185.70 22.53 181.1 22.46 194.6 7.962E+04 26994.98 22.03 185.70 22.53 181.1 22.46 194.6 7.962E+04 27595.76 22.04 185.70 22.53 181.2 22.46 194.5 7.962E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 88 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 28220.36 22.03 185.60 22.52 181.2 22.45 194.5 7.961 E+04 28844.95 22.02 185.60 22.51 181.2 22.44 194.5 7.961 E+04 29469.95 22.01 185.50 22.51 181.2 22.43 194.4 7.961 E+04 30094.54 22.00 185.40 22.50 181.2 22.42 194.3 7.961 E+04 30719.14 22.00 185.40 22.48 181.1 22.41 194.3 7.960E+04 31343.73 21.99 185.30 22.47 181.1 22.39 194.2 7.959E+04 31968.73 21.97 185.30 22.47 181.1 22.39 194.2 7.959E+04 32592.92 21.97 185.20 22.45 181.1 22.37 194.1 7.959E+04 33191.54 21.97 185.10 22.46 181.2 22.37 194.0 7.958E+04 33815.73 21.96 185.00 22.45 181.2 22.36 193.9 7.958E+04 34440.32 21.94 184.90 22.44 181.2 22.35 193.8 7.956E+04 35064.51 21.93 184.80 22.42 181.1 22.33 193.7 7.956E+04 35688.7 21.92 184.70 22.41 181.1 22.32 193.6 7.956E+04 36312.89 21.90 184.60 22.39 181.1 22.29 193.5 7.955E+04 36937.07 21.89 184.50 22.37 181.0 22.28 193.4 7.954E+04 37561.26 21.87 184.40 22.36 181.0 22.26 193.3 7.954E+04 38185.45 21.86 184.30 22.35 181.0 22.25 193.2 7.953E+04 38809.64 21.84 184.20 22.33 181.0 22.23 193.0 7.953E+04 39423.29 21.82 184.10 22.31 181.0 22.21 192.9 7.951 E+04 40020.36 21.80 183.90 22.30 180.9 22.20 192.8 7.951 E+04 40644.14 21.78 183.80 22.28 180.9 22.18 192.6 7.951 E+04 41267.92 21.77 183.70 22.26 180.9 22.15 192.5 7.949E+04 41891.7 21.75 183.50 22.24 180.8 22.13 192.4 7.949E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 89 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Lon -Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 42515.48 21.73 183.40 22.22 180.8 22.11 192.2 7.948E+04 43139.26 21.72 183.30 22.20 180.8 22.09 192.1 7.946E+04 43763.45 21.69 183.10 22.19 180.8 22.08 191.9 7.946E+04 44387.64 21.67 183.00 22.16 180.7 22.05 191.8 7.946E+04 45012.23 21.65 182.90 22.14 180.6 22.03 191.6 7.944E+04 45637.23 21.62 182.70 22.12 180.5 22.01 191.5 7.944E+04 46189.45 21.60 182.60 22.09 180.3 21.97 191.3 7.944E+04 46724.76 21.58 182.50 22.05 180.1 21.93 191.2 7.942E+04 47260.45 21.55 182.30 22.03 180.1 21.91 191.0 7.942E+04 47796.32 21.52 182.10 22.01 180.0 21.89 190.9 7.941 E+04 48331.95 21.49 182.00 21.98 179.8 21.86 190.7 7.941 E+04 48867.57 21.46 181.90 21.95 179.7 21.83 190.6 7.940E+04 49406.11 21.42 181.60 21.91 179.5 21.78 190.4 7.939E+04 50656.11 21.37 181.40 21.84 179.1 21.72 190.0 7.939E+04 51906.11 21.31 181.10 21.78 178.8 21.65 189.7 7.937E+04 53156.11 21.25 180.80 21.72 178.5 21.58 189.4 7.935E+04 54406.11 21.19 180.40 21.65 178.1 21.52 189.0 7.934E+04 55555.17 21.13 180.10 21.60 177.9 21.46 188.7 7.932E+04 56805.17 21.07 179.80 21.53 177.5 21.39 188.3 7.932E+04 58055.17 21.01 179.50 21.47 177.1 21.32 187.9 7.930E+04 59300.54 20.94 179.10 21.42 176.9 21.27 187.6 7.928E+04 60550.54 20.88 178.80 21.36 176.5 21.21 187.2 7.927E+04 61800.54 20.82 178.50 21.30 176.2 21.15 186.9 7.925E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 90 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Lona-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 63050.54 20.76 178.10 21.24 175.9 21.09 186.5 7.923E+04 64300.54 20.71 177.80 21.18 175.6 21.02 186.1 7.923E+04 65550.54 20.65 177.50 21.12 175.2 20.96 185.8 7.921 E+04 66776.29 20.59 177.20 21.07 174.9 20.91 185.5 7.920E+04 67847.79 20.54 176.90 21.01 174.6 20.84 185.1 7.918E+04 69092.29 20.48 176.60 20.95 174.3 20.78 184.8 7.918E+04 70342.29 20.43 176.30 20.90 173.9 20.72 184.4 7.916E+04 71592.29 20.37 176.00 20.84 173.6 20.66 184.1 7.915E+04 72842.29 20.32 175.70 20.79 173.3 20.61 183.8 7.913E+04 74092.29 20.26 175.40 20.73 173.0 20.55 183.4 7.912E+04 75342.29 20.21 175.10 20.68 172.7 20.49 183.1 7.911 E+04 76592.29 20.16 174.80 20.63 172.4 20.44 182.8 7.91 OE+04 77842.29 20.11 174.50 20.58 172.1 20.38 182.4 7.908E+04 79092.29 20.06 174.20 20.53 171.8 20.33 182.1 7.908E+04 80342.29 20.01 173.90 20.48 171.4 20.28 181.8 7.906E+04 81592.29 19.96 173.60 20.43 171.1 20.22 181.5 7.905E+04 82842.29 19.91 173.30 20.38 170.8 20.17 181.2 7.903E+04 84089.91 19.86 173.00 20.34 170.6 20.13 180.8 7.903E+04 85339.91 19.81 172.70 20.28 170.2 20.07 180.5 7.901 E+04 86589.91 19.77 172.40 20.23 169.9 20.02 180.2 7.900E+04 87839.91 19.72 172.10 20.20 169.7 19.98 179.9 7.900E+04 89089.91 19.67 171.80 20.16 169.5 19.94 179.6 7.898E+04 90339.91 19.63 171.60 20.11 169.2 19.89 179.3 7.897E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 91 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Res onse for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 91589.91 19.58 171.30 20.07 168.9 19.84 179.0 7.896E+04 92839.91 19.53 171.00 20.02 168.6 19.79 178.6 7.895E+04 94089.91 19.49 170.70 19.98 168.3 19.75 178.3 7.893E+04 95339.91 19.44 170.40 19.93 168.0 19.70 178.0 7.892E+04 96589.91 19.40 170.20 19.89 167.7 19.65 177.7 7.892E+04 97839.91 19.36 169.90 19.85 167.4 19.61 177.4 7.890E+04 99089.91 19.31 169.60 19.81 167.2 19.56 177.1 7.889E+04 100339.9 19.27 169.30 19.76 166.9 19.52 176.8 7.888E+04 101589.9 19.23 169.10 19.72 166.6 19.47 176.5 7.887E+04 102839.9 19.18 168.80 19.68 166.3 19.43 176.2 7.887E+04 104089.7 19.15 168.50 19.63 166.0 19.37 175.9 7.885E+04 105339.7 19.11 168.30 19.60 165.8 19.34 175.7 7.884E+04 106589.7 19.08 168.10 19.57 165.6 19.31 175.4 7.884E+04 107839.7 19.04 167.90 19.53 165.4 19.27 175.2 7.882E+04 109089.7 19.01 167.60 19.50 165.2 19.23 175.0 7.882E+04 110339.7 18.98 167.50 19.47 165.0 19.20 174.8 7.881 E+04 111589.7 18.96 167.30 19.44 164.8 19.16 174.5 7.881 E+04 112839.7 18.93 167.10 19.40 164.6 19.13 174.4 7.879E+04 114089.7 18.90 166.90 19.37 164.4 19.09 174.2 7.879E+04 115339.7 18.87 166.70 19.34 164.2 19.06 174.0 7.879E+04 116589.7 18.85 166.60 19.31 164.0 19.02 173.8 7.878E+04 117839.7 18.82 166.40 19.28 163.8 18.99 173.6 7.877E+04 119055.5 18.79 166.20 19.25 163.6 18.96 173.4 7.876E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 92 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation lime (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 120305.5 18.77 166.00 19.22 163.5 18.93 173.2 7.876E+04 121555.5 18.74 165.90 19.19 163.3 18.90 173.0 7.876E+04 122802 18.72 165.70 19.17 163.1 18.87 172.8 7.874E+04 124052 18.69 165.50 19.14 163.0 18.84 172.7 7.874E+04 125302 18.67 165.40 19.11 162.8 18.81 172.5 7.873E+04 126552 18.64 165.20 19.08 162.6 18.77 172.3 7.873E+04 127802 18.62 165.10 19.05 162.4 18.75 172.1 7.873E+04 129052 18.60 164.90 19.03 162.3 18.72 171.9 7.871 E+04 130302 18.57 164.70 19.00 162.1 18.69 171.8 7.871 E+04 131552 18.55 164.60 18.98 162.0 18.66 171.6 7.871 E+04 132802 18.53 164.40 18.95 161.8 18.63 171.4 7.870E+04 134052 18.50 164.30 18.93 161.7 18.61 171.3 7.870E+04 135302 18.48 164.10 18.91 161.5 18.58 171.1 7.868E+04 136552 18.46 164.00 18.88 161.4 18.56 170.9 7.868E+04 137802 18.44 163.80 18.86 161.2 18.53 170.7 7.868E+04 139052 18.42 163.70 18.84 161.1 18.50 170.6 7.867E+04 140302 18.39 163.50 18.81 160.9 18.47 170.4 7.867E+04 141552 18.37 163.40 18.79 160.8 18.45 170.2 7.867E+04 142802 18.35 163.20 18.76 160.6 18.42 170.1 7.865E+04 144052 18.33 163.10 18.74 160.5 18.39 169.9 7.865E+04 145302 18.31 162.90 18.72 160.3 18.37 169.8 7.865E+04 146552 18.29 162.80 18.70 160.2 18.34 169.6 7.864E+04 147802 18.26 162.60 18.67 160.0 18.32 169.4 7.864E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 93 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (see) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 149052 18.24 162.50 18.65 159.9 18.29 169.3 7.864E+04 150302 18.22 162.30 18.63 159.7 18.27 169.1 7.862E+04 151552 18.20 162.20 18.60 159.6 18.24 168.9 7.862E+04 152802 18.18 162.00 18.58 159.4 18.22 168.8 7.862E+04 154052 18.16 161.90 18.56 159.3 18.19 168.6 7.861 E+04 155302 18.14 161.70 18.54 159.1 18.17 168.5 7.861 E+04 156552 18.12 161.60 18.52 159.0 18.14 168.3 7.860E+04 157802 18.10 161.40 18.49 158.8 18.12 168.1 7.859E+04 159052 18.08 161.30 18.47 158.7 18.09 168.0 7.859E+04 160302 18.06 161.20 18.45 158.6 18.07 167.8 7.859E+04 161552 18.04 161.00 18.43 158.4 18.04 167.7 7.858E+04 162802 18.02 160.90 18.41 158.3 18.02 167.5 7.858E+04 164052 18.00 160.70 18.39 158.1 18.00 167.4 7.858E+04 165302 17.98 160.60 18.37 158.0 17.97 167.2 7.856E+04 166552 17.96 160.40 18.34 157.8 17.95 167.0 7.856E+04 167802 17.94 160.30 18.32 157.7 17.92 166.9 7.856E+04 169052 17.92 160.10 18.31 157.6 17.90 166.7 7.855E+04 170302 17.90 160.00 18.30 157.6 17.90 166.6 7.855E+04 171552 17.88 159.90 18.29 157.5 17.88 166.4 7.854E+04 172802 17.87 159.70 18.27 157.3 17.86 166.3 7.853E+04 174052 17.85 159.60 18.25 157.2 17.83 166.1 7.853E+04 175302 17.83 159.40 18.23 157.1 17.81 166.0 7.853E+04 176552 17.81 159.30 18.21 156.9 17.79 165.8 7.852E+04
Attachment 2 to BVY 04.081 Docket No. 50-271 Page 94 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (including leakage (psia) leakage (psia) (F) Vent Liquid) 177802 17.79 159.20 18.19 156.8 17.76 165.6 7.852E+04 179052 17.77 159.00 18.17 156.6 17.74 165.5 7.851 E+04 180302 17.75 158.90 18.15 156.5 17.72 165.3 7.850E+04 181552 17.73 158.70 18.13 156.4 17.70 165.2 7.850E+04 182802 17.71 158.60 18.11 156.2 17.67 165.0 7.850E+04 184052 17.70 158.40 18.09 156.1 17.65 164.9 7.849E+04 185302 17.68 158.30 18.07 156.0 17.63 164.7 7.849E+04 186552 17.66 158.20 18.05 155.8 17.61 164.6 7.849E+04 187802 17.64 158.00 18.03 155.7 17.58 164.4 7.847E+04 189052 17.62 157.90 18.01 155.5 17.56 164.3 7.847E+04 190302 17.60 157.70 17.99 155.4 17.54 164.1 7.847E+04 191552 17.59 157.60 17.97 155.3 17.52 164.0 7.846E+04 192802 17.57 157.50 17.95 155.1 17.50 163.8 7.846E+04 194052 17.55 157.30 17.93 155.0 17.47 163.6 7.846E+04 195302 17.53 157.20 17.91 154.9 17.45 163.5 7.846E+04 196552 17.51 157.00 17.90 154.7 17.43 163.3 7.844E+04 197802 17.49 156.90 17.88 154.6 17.41 163.2 7.844E+04 199052 17.48 156.80 17.86 154.4 17.39 163.0 7.844E+04 200302 17.46 156.60 17.84 154.3 17.37 162.9 7.843E+04 201552 17.44 156.50 17.82 154.2 17.34 162.7 7.843E+04 202802 17.42 156.30 17.80 154.0 17.32 162.6 7.843E+04 204052 17.41 156.20 17.78 153.9 17.30 162.4 7.841 E+04 205302 17.39 156.10 17.77 153.8 17.28 162.3 7.841 E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 95 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (see) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 206552 17.37 156.00 17.75 153.7 17.26 162.1 7.841 E+04 207802 17.36 155.80 17.73 153.5 17.24 162.0 7.841 E+04 209052 17.34 155.70 17.72 153.4 17.23 161.9 7.840E+04 210302 17.33 155.60 17.70 153.3 17.21 161.7 7.840E+04 211552 17.31 155.50 17.69 153.2 17.19 161.6 7.840E+04 212802 17.30 155.40 17.67 153.1 17.17 161.5 7.839E+04 214052 17.29 155.20 17.66 153.0 17.15 161.4 7.839E+04 215302 17.27 155.10 17.64 152.9 17.14 161.2 7.838E+04 216552 17.26 155.00 17.63 152.7 17.12 161.1 7.838E+04 217802 17.25 154.90 17.61 152.6 17.10 161.0 7.837E+04 219052 17.23 154.80 17.60 152.5 17.09 160.9 7.837E+04 220302 17.22 154.70 17.59 152.4 17.07 160.8 7.837E+04 221552 17.21 154.60 17.57 152.3 17.06 160.7 7.837E+04 222802 17.20 154.50 17.56 152.2 17.04 160.6 7.837E+04 224052 17.18 154.40 17.55 152.1 17.02 160.5 7.836E+04 225302 17.17 154.30 17.54 152.1 17.01 160.4 7.836E+04 226552 17.16 154.20 17.53 152.0 16.99 160.2 7.836E+04 227802 17.15 154.10 17.51 151.9 16.98 160.1 7.835E+04 229052 17.14 154.00 17.50 151.8 16.96 160.0 7.835E+04 230302 17.13 153.90 17.49 151.7 16.95 159.9 7.834E+04 231552 17.11 153.90 17.48 151.6 16.94 159.8 7.834E+04 232802 17.10 153.80 17.47 151.5 16.92 159.7 7.834E+04 234047.9 17.09 153.70 17.45 151.4 16.91 159.6 7.834E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 96 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 235297.9 17.08 153.60 17.44 151.3 16.89 159.5 7.834E+04 236547.9 17.07 153.50 17.43 151.3 16.88 159.4 7.833E+04 237797.9 17.06 153.40 17.42 151.2 16.87 159.3 7.833E+04 239047.9 17.05 153.30 17.41 151.1 16.85 159.3 7.833E+04 240297.9 17.04 153.30 17.40 151.0 16.84 159.2 7.833E+04 241547.9 17.03 153.20 17.39 150.9 16.83 159.1 7.833E+04 242797.9 17.02 153.10 17.38 150.8 16.81 159.0 7.831 E+04 244047.9 17.01 153.00 17.37 150.8 16.80 158.9 7.831 E+04 245297.9 17.00 152.90 17.36 150.7 16.79 158.8 7.831 E+04 246547.9 16.99 152.80 17.35 150.6 16.77 158.7 7.831 E+04 247797.9 16.98 152.80 17.34 150.5 16.76 158.6 7.831 E+04 249047.9 16.97 152.70 17.33 150.5 16.75 158.6 7.831 E+04 250297.9 16.97 152.60 17.32 150.4 16.74 158.5 7.830E+04 251547.9 16.96 152.50 17.31 150.3 16.72 158.4 7.830E+04 252797.9 16.95 152.50 17.30 150.2 16.71 158.3 7.830E+04 254047.9 16.94 152.40 17.29 150.2 16.70 158.2 7.830E+04 255297.9 16.93 152.30 17.28 150.1 16.69 158.1 7.830E+04 256547.9 16.92 152.20 17.27 150.0 16.68 158.0 7.830E+04 257797.9 16.91 152.20 17.27 149.9 16.66 158.0 7.829E+04 259047.9 16.87 151.80 17.25 149.8 16.65 157.8 7.829E+04 260297.9 16.85 151.70 17.23 149.7 16.63 157.7 7.829E+04 261547.9 16.84 151.50 17.22 149.5 16.61 157.5 7.828E+04 262797.8 16.83 151.40 17.20 149.4 16.59 157.4 7.828E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 97 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 264047.8 16.81 151.30 17.19 149.3 16.57 157.2 7.827E+04 265297.8 16.80 151.20 17.17 149.2 16.55 157.1 7.827E+04 266547.8 16.78 151.00 17.16 149.0 16.54 156.9 7.826E+04 267797.8 16.77 150.90 17.14 148.9 16.52 156.8 7.826E+04 269047.8 16.75 150.80 17.13 148.8 16.50 156.7 7.826E+04 270297.8 16.74 150.70 17.12 148.7 16.49 156.5 7.826E+04 271547.8 16.73 150.60 17.10 148.6 16.47 156.4 7.825E+04 272797.8 16.72 150.50 17.09 148.5 16.46 156.3 7.825E+04 274047.8 16.70 150.40 17.08 148.4 16.44 156.2 7.825E+04 275297.8 16.69 150.20 17.07 148.3 16.43 156.1 7.825E+04 276547.8 16.68 150.10 17.05 148.2 16.41 155.9 7.823E+04 277797.8 16.67 150.00 17.04 148.1 16.40 155.8 7.823E+04 279047.8 16.66 149.90 17.03 148.0 16.38 155.7 7.823E+04 280297.8 16.64 149.80 17.02 147.9 16.37 155.6 7.823E+04 281547.8 16.63 149.70 17.01 147.8 16.36 155.5 7.822E+04 282797.8 16.62 149.60 17.00 147.7 16.34 155.4 7.822E+04 284047.8 16.61 149.50 16.99 147.6 16.33 155.3 7.822E+04 285297.8 16.60 149.40 16.98 147.5 16.32 155.2 7.822E+04 286547.8 16.59 149.30 16.97 147.4 16.30 155.1 7.822E+04 287797.8 16.58 149.30 16.96 147.3 16.29 155.0 7.820E+04 289047.8 16.57 149.20 16.95 147.2 16.28 154.9 7.820E+04 290297.8 16.56 149.10 16.94 147.1 16.26 154.8 7.820E+04 291547.8 16.55 149.00 16.93 147.1 16.25 154.7 7.820E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 98 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 292797.8 16.54 148.90 16.92 147.0 16.24 154.6 7.820E+04 294047.8 16.53 148.80 16.91 146.9 16.23 154.5 7.819E+04 295297.8 16.52 148.70 16.90 146.8 16.21 154.4 7.819E+04 296547.8 16.51 148.60 16.89 146.7 16.20 154.3 7.819E+04 297797.8 16.50 148.60 16.88 146.6 16.19 154.2 7.819E+04 299047.8 16.49 148.50 16.87 146.6 16.18 154.1 7.819E+04 300297.8 16.48 148.40 16.86 146.5 16.17 154.0 7.819E+04 301547.8 16.47 148.30 16.85 146.4 16.16 153.9 7.818E+04 302797.8 16.47 148.20 16.85 146.3 16.15 153.9 7.818E+04 304047.8 16.46 148.10 16.84 146.2 16.13 153.8 7.818E+04 305297.8 16.45 148.10 16.83 146.2 16.12 153.7 7.818E+04 306547.8 16.44 148.00 16.82 146.1 16.11 153.6 7.818E+04 307797.8 16.43 147.90 16.81 146.0 16.10 153.5 7.818E+04 309047.8 16.42 147.80 16.80 145.9 16.09 153.4 7.816E+04 310297.8 16.41 147.80 16.80 145.9 16.08 153.3 7.816E+04 311547.8 16.41 147.70 16.79 145.8 16.07 153.3 7.816E+04 312797.8 16.40 147.60 16.78 145.7 16.06 153.2 7.816E+04 314047.8 16.39 147.50 16.77 145.6 16.05 153.1 7.816E+04 315297.8 16.38 147.50 16.76 145.6 16.04 153.0 7.816E+04 316547.8 16.37 147.40 16.76 145.5 16.03 152.9 7.815E+04 317797.8 16.36 147.30 16.75 145.4 16.02 152.8 7.815E+04 319047.8 16.36 147.20 16.74 145.4 16.01 152.8 7.815E+04 320297.8 16.35 147.20 16.73 145.3 16.00 152.7 7.815E+04
Attachment 2 to BVY 04.081 Docket No. 50-271 Page 99 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 321547.8 16.34 147.10 16.73 145.2 15.98 152.6 7.815E+04 322797.8 16.33 147.00 16.72 145.2 15.98 152.5 7.815E+04 324047.8 16.33 146.90 16.71 145.1 15.97 152.4 7.814E+04 325297.8 16.32 146.90 16.70 145.0 15.95 152.4 7.814E+04 326547.8 16.31 146.80 16.70 144.9 15.95 152.3 7.814E+04 327797.8 16.30 146.70 16.69 144.9 15.94 152.2 7.813E+04 329047.8 16.29 146.60 16.68 144.8 15.93 152.1 7.813E+04 330297.8 16.29 146.60 16.68 144.7 15.92 152.1 7.813E+04 331547.8 16.28 146.50 16.67 144.7 15.91 152.0 7.813E+04 332797.8 16.27 146.40 16.66 144.6 15.90 151.9 7.812E+04 334047.8 16.26 146.40 16.66 144.5 15.89 151.8 7.812E+04 335297.8 16.26 146.30 16.65 144.5 15.88 151.7 7.812E+04 336547.8 16.25 146.20 16.64 144.4 15.87 151.7 7.812E+04 337797.8 16.24 146.20 16.64 144.3 15.86 151.6 7.812E+04 339047.8 16.24 146.10 16.63 144.3 15.85 151.5 7.812E+04 340297.8 16.23 146.00 16.62 144.2 15.84 151.4 7.812E+04 341547.8 16.22 146.00 16.62 144.1 15.83 151.4 7.811 E+04 342797.8 16.21 145.90 16.61 144.1 15.82 151.3 7.811 E+04 344047.8 16.21 145.80 16.60 144.0 15.81 151.2 7.811 E+04 345297.8 16.20 145.70 16.60 143.9 15.80 151.1 7.811 E+04 346547.8 16.19 145.70 16.59 143.9 15.79 151.1 7.811 E+04 347797.8 16.18 145.60 16.58 143.8 15.78 151.0 7.811 E+04 349047.8 16.18 145.50 16.58 143.7 15.77 150.9 7.811 E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 100 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 350297.8 16.17 145.50 16.57 143.7 15.76 150.8 7.809E+04 351547.8 16.16 145.40 16.56 143.6 15.75 150.8 7.809E+04 352797.8 16.15 145.30 16.56 143.5 15.74 150.7 7.809E+04 354047.8 16.15 145.30 16.55 143.5 15.74 150.6 7.809E+04 355297.8 16.14 145.20 16.54 143.4 15.73 150.5 7.809E+04 356547.8 16.13 145.10 16.54 143.3 15.72 150.5 7.809E+04 357797.8 16.13 145.10 16.53 143.3 15.71 150.4 7.808E+04 359047.8 16.12 145.00 16.52 143.2 15.70 150.3 7.808E+04 360297.8 16.11 144.90 16.52 143.2 15.69 150.2 7.808E+04 361547.8 16.11 144.90 16.51 143.1 15.68 150.2 7.808E+04 362797.8 16.10 144.80 16.50 143.0 15.67 150.1 7.808E+04 364047.8 16.09 144.70 16.50 143.0 15.66 150.0 7.808E+04 365297.8 16.08 144.60 16.49 142.9 15.65 149.9 7.808E+04 366547.8 16.08 144.60 16.49 142.8 15.65 149.9 7.808E+04 367797.8 16.07 144.50 16.48 142.8 15.64 149.8 7.807E+04 369047.8 16.06 144.40 16.47 142.7 15.63 149.7 7.807E+04 370297.8 16.06 144.40 16.47 142.6 15.62 149.6 7.807E+04 371547.8 16.05 144.30 16.46 142.6 15.61 149.6 7.807E+04 372797.8 16.04 144.20 16.46 142.5 15.60 149.5 7.807E+04 374047.8 16.04 144.20 16.45 142.5 15.59 149.4 7.807E+04 375297.8 16.03 144.10 16.44 142.4 15.58 149.3 7.807E+04 376547.8 16.02 144.00 16.44 142.3 15.58 149.3 7.805E+04 377797.8 16.02 144.00 16.43 142.3 15.57 149.2 7.805E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 101 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Lonq-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 379047.8 16.01 143.90 16.43 142.2 15.56 149.1 7.805E+04 380297.8 16.00 143.80 16.42 142.1 15.55 149.1 7.805E+04 381547.8 16.00 143.80 16.42 142.1 15.54 149.0 7.805E+04 382797.8 15.99 143.70 16.41 142.0 15.53 148.9 7.805E+04 384047.8 15.98 143.70 16.40 141.9 15.52 148.8 7.805E+04 385297.8 15.98 143.60 16.40 141.9 15.51 148.8 7.804E+04 386547.8 15.97 143.50 16.39 141.8 15.51 148.7 7.804E+04 387797.8 15.96 143.50 16.39 141.8 15.50 148.6 7.804E+04 389047.8 15.96 143.40 16.38 141.7 15.49 148.6 7.804E+04 390297.8 15.95 143.30 16.38 141.6 15.48 148.5 7.804E+04 391547.8 15.94 143.30 16.37 141.6 15.47 148.4 7.804E+04 392797.8 15.94 143.20 16.36 141.5 15.46 148.3 7.804E+04 394047.8 15.93 143.10 16.36 141.4 15.46 148.3 7.803E+04 395297.8 15.92 143.10 16.35 141.4 15.45 148.2 7.803E+04 396547.8 15.92 143.00 16.35 141.3 15.44 148.1 7.803E+04 397797.8 15.91 142.90 16.34 141.3 15.43 148.1 7.802E+04 399047.8 15.90 142.90 16.34 141.2 15.42 148.0 7.802E+04 400297.8 15.90 142.80 16.33 141.1 15.41 147.9 7.802E+04 401547.8 15.89 142.70 16.33 141.1 15.41 147.8 7.802E+04 402797.8 15.89 142.70 16.32 141.0 15.40 147.8 7.802E+04 404047.8 15.88 142.60 16.32 141.0 15.39 147.7 7.801 E+04 405297.8 15.87 142.60 16.31 140.9 15.38 147.6 7.801 E+04 406547.8 15.87 142.50 16.31 140.9 15.38 147.6 7.801 E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 102 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Lona-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 407797.8 15.86 142.40 16.30 140.8 15.37 147.5 7.801 E+04 409047.8 15.86 142.40 16.30 140.7 15.36 147.5 7.801 E+04 410297.8 15.85 142.30 16.29 140.7 15.35 147.4 7.801 E+04 411547.8 15.85 142.30 16.29 140.6 15.35 147.3 7.801 E+04 412797.8 15.84 142.20 16.28 140.6 15.34 147.3 7.801 E+04 414047.8 15.84 142.20 16.28 140.5 15.33 147.2 7.801 E+04 415297.8 15.83 142.10 16.28 140.5 15.33 147.2 7.800E+04 416547.8 15.83 142.10 16.27 140.5 15.32 147.1 7.800E+04 417797.8 15.82 142.00 16.27 140.4 15.31 147.1 7.800E+04 419047.8 15.82 142.00 16.27 140.4 15.31 147.0 7.800E+04 420297.8 15.81 142.00 16.26 140.3 15.30 147.0 7.800E+04 421547.8 15.81 141.90 16.26 140.3 15.30 146.9 7.800E+04 422797.8 15.81 141.90 16.26 140.2 15.29 146.9 7.800E+04 424047.8 15.80 141.80 16.25 140.2 15.28 146.8 7.800E+04 425297.8 15.80 141.80 16.25 140.2 15.28 146.8 7.800E+04 426547.8 15.79 141.70 16.25 140.1 15.27 146.8 7.800E+04 427797.8 15.79 141.70 16.24 140.1 15.27 146.7 7.800E+04 429047.8 15.79 141.70 16.24 140.1 15.26 146.7 7.798E+04 430297.8 15.78 141.60 16.24 140.0 15.26 146.6 7.798E+04 431547.8 15.78 141.60 16.24 140.0 15.25 146.6 7.798E+04 432797.8 15.78 141.60 16.23 139.9 15.24 146.5 7.798E+04 434047.8 15.77 141.50 16.23 139.9 15.24 146.5 7.798E+04 435297.8 15.77 141.50 16.23 139.9 15.23 146.5 7.798E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 103 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 436547.8 15.77 141.40 16.23 139.8 15.23 146.4 7.798E+04 437797.8 15.76 141.40 16.22 139.8 15.22 146.4 7.798E+04 439047.8 15.76 141.40 16.22 139.8 15.22 146.3 7.798E+04 440294.2 15.75 141.30 16.22 139.7 15.21 146.3 7.798E+04 441544.2 15.75 141.30 16.22 139.7 15.21 146.3 7.798E+04 442794.2 15.75 141.30 16.21 139.7 15.20 146.2 7.798E+04 444044.2 15.74 141.20 16.21 139.6 15.20 146.2 7.798E+04 445294.2 15.74 141.20 16.21 139.6 15.19 146.2 7.797E+04 446544.2 15.74 141.20 16.21 139.6 15.19 146.1 7.797E+04 447794.2 15.74 141.10 16.21 139.5 15.18 146.1 7.797E+04 449044.2 15.73 141.10 16.20 139.5 15.18 146.0 7.797E+04 450295.5 15.73 141.10 16.20 139.5 15.17 146.0 7.797E+04 451545.5 15.73 141.00 16.20 139.4 15.17 146.0 7.797E+04 452795.5 15.72 141.00 16.20 139.4 15.16 145.9 7.797E+04 454045.5 15.72 141.00 16.20 139.4 15.16 145.9 7.797E+04 455295.5 15.72 141.00 16.19 139.4 15.15 145.9 7.797E+04 456545.5 15.71 140.90 16.19 139.3 15.15 145.9 7.797E+04 457795.5 15.71 140.90 16.19 139.3 15.14 145.8 7.797E+04 459045.5 15.71 140.90 16.19 139.3 15.14 145.8 7.797E+04 460295.5 15.71 140.80 16.19 139.2 15.14 145.8 7.797E+04 461545.5 15.70 140.80 16.19 139.2 15.13 145.7 7.797E+04 462795.5 15.70 140.80 16.18 139.2 15.13 145.7 7.797E+04 464045.5 15.70 140.80 16.18 139.2 15.12 145.7 7.797E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 104 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 465295.5 15.70 140.70 16.18 139.1 15.12 145.6 7.797E+04 466545.5 15.69 140.70 16.18 139.1 15.11 145.6 7.796E+04 467795.5 15.69 140.70 16.18 139.1 15.11 145.6 7.796E+04 469045.5 15.69 140.60 16.18 139.1 15.11 145.6 7.796E+04 470295.5 15.69 140.60 16.18 139.0 15.10 145.5 7.796E+04 471545.5 15.68 140.60 16.18 139.0 15.10 145.5 7.796E+04 472795.5 15.68 140.60 16.17 139.0 15.09 145.5 7.796E+04 474045.5 15.68 140.50 16.17 139.0 15.09 145.4 7.796E+04 475295.5 15.68 140.50 16.17 138.9 15.08 145.4 7.796E+04 476545.5 15.68 140.50 16.17 138.9 15.08 145.4 7.796E+04 477795.5 15.67 140.50 16.17 138.9 15.08 145.4 7.796E+04 479045.5 15.67 140.50 16.16 138.8 15.06 145.3 7.796E+04 480295.5 15.67 140.40 16.16 138.8 15.06 145.3 7.796E+04 481545.5 15.67 140.40 16.16 138.8 15.06 145.3 7.796E+04 482795.5 15.67 140.40 16.16 138.8 15.06 145.3 7.796E+04 484045.5 15.67 140.40 16.16 138.8 15.06 145.3 7.796E+04 485295.5 15.66 140.40 16.16 138.8 15.06 145.2 7.796E+04 486545.3 15.66 140.30 16.16 138.8 15.04 145.2 7.796E+04 487795.3 15.66 140.30 16.16 138.8 15.04 145.2 7.796E+04 489045.3 15.66 140.30 16.16 138.8 15.04 145.2 7.796E+04 490295.3 15.66 140.30 16.16 138.8 15.04 145.2 7.796E+04 491545.3 15.66 140.30 16.16 138.8 15.03 145.2 7.796E+04 492795.3 15.66 140.30 16.15 138.7 15.02 145.1 7.796E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 105 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Tern DBA-LOCA Containment Response for NPSH Evaluation Time (see) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 494045.3 15.66 140.20 16.15 138.7 15.02 145.1 7.796E+04 495295.3 15.66 140.20 16.15 138.7 15.02 145.1 7.796E+04 496545.3 15.66 140.20 16.15 138.7 15.02 145.1 7.796E+04 497795.3 15.65 140.20 16.15 138.7 15.01 145.1 7.794E+04 499045.3 15.65 140.20 16.14 138.6 15.00 145.0 7.794E+04 500295.3 15.65 140.20 16.14 138.6 15.00 145.0 7.794E+04 501545.3 15.65 140.20 16.14 138.6 15.00 145.0 7.794E+04 502795.3 15.65 140.10 16.14 138.6 14.99 145.0 7.794E+04 504045.3 15.65 140.10 16.14 138.6 14.99 145.0 7.794E+04 505295.3 15.65 140.10 16.14 138.6 14.99 145.0 7.794E+04 506545.3 15.65 140.10 16.13 138.5 14.97 144.9 7.794E+04 507795.3 15.64 140.10 16.13 138.5 14.97 144.9 7.794E+04 509045.3 15.64 140.00 16.13 138.5 14.97 144.9 7.794E+04 510295.3 15.64 140.00 16.13 138.5 14.97 144.8 7.794E+04 511545.3 15.64 140.00 16.12 138.4 14.95 144.8 7.794E+04 512795.3 15.63 139.90 16.12 138.4 14.95 144.8 7.794E+04 514045.3 15.63 139.90 16.12 138.4 14.95 144.8 7.794E+04 515295.3 15.63 139.90 16.12 138.4 14.95 144.7 7.794E+04 516545.3 15.63 139.90 16.13 138.4 14.95 144.7 7.794E+04 517795.3 15.63 139.80 16.11 138.3 14.93 144.7 7.794E+04 519045.3 15.62 139.80 16.11 138.3 14.93 144.6 7.794E+04 520295.3 15.62 139.80 16.11 138.3 14.93 144.6 7.794E+04 521545.3 15.62 139.80 16.12 138.3 14.92 144.6 7.794E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 106 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (19) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 522795.3 15.62 139.80 16.12 138.3 14.92 144.6 7.794E+04 524045.3 15.62 139.80 16.10 138.2 14.91 144.6 7.794E+04 525295.4 15.62 139.70 16.10 138.2 14.90 144.6 7.794E+04 526545.4 15.61 139.70 16.11 138.2 14.90 144.5 7.793E+04 527795.4 15.61 139.70 16.11 138.2 14.90 144.5 7.793E+04 529045.4 15.61 139.60 16.11 138.2 14.90 144.5 7.793E+04 530295.4 15.61 139.60 16.11 138.2 14.90 144.5 7.793E+04 531545.4 15.61 139.60 16.11 138.2 14.89 144.4 7.793E+04 532795.4 15.61 139.60 16.09 138.1 14.88 144.4 7.793E+04 534045.4 15.61 139.60 16.10 138.1 14.88 144.4 7.793E+04 535295.4 15.60 139.60 16.10 138.1 14.87 144.4 7.793E+04 536545.4 15.60 139.50 16.10 138.1 14.87 144.3 7.793E+04 537795.4 15.61 139.60 16.08 138.0 14.85 144.3 7.792E+04 539045.4 15.60 139.50 16.09 138.0 14.85 144.3 7.793E+04 540295.4 15.59 139.40 16.09 138.0 14.85 144.2 7.793E+04 541545.4 15.59 139.40 16.09 138.0 14.85 144.2 7.793E+04 542795.4 15.59 139.40 16.09 138.0 14.85 144.2 7.793E+04 544045.4 15.59 139.40 16.07 137.9 14.83 144.1 7.793E+04 545295.4 15.59 139.30 16.08 137.9 14.83 144.1 7.793E+04 546545.4 15.58 139.30 16.08 137.9 14.83 144.1 7.793E+04 547795.4 15.58 139.30 16.08 137.9 14.83 144.1 7.793E+04 549045.4 15.58 139.30 16.08 137.9 14.82 144.0 7.793E+04 550295.4 15.58 139.30 16.08 137.9 14.82 144.0 7.793E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 107 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 551545.4 15.58 139.30 16.06 137.8 14.81 144.0 7.792E+04 552795.4 15.57 139.20 16.07 137.8 14.80 144.0 7.791 E+04 554045.4 15.57 139.20 16.07 137.8 14.80 144.0 7.791 E+04 555295.4 15.57 139.20 16.07 137.8 14.80 144.0 7.791 E+04 556545.4 15.57 139.20 16.07 137.8 14.80 143.9 7.791 E+04 557795.4 15.59 139.40 16.05 137.6 14.78 143.9 7.791 E+04 559045.4 15.57 139.10 16.05 137.7 14.78 143.9 7.791 E+04 560295.4 15.56 139.10 16.06 137.7 14.78 143.8 7.791 E+04 561545.4 15.56 139.00 16.06 137.7 14.77 143.8 7.791 E+04 562795.4 15.56 139.00 16.06 137.7 14.77 143.8 7.791 E+04 564045.4 15.56 139.00 16.06 137.7 14.77 143.8 7.791 E+04 565295.4 15.56 139.00 16.06 137.7 14.77 143.8 7.791 E+04 566545.4 15.56 139.00 16.06 137.7 14.76 143.8 7.791 E+04 567795.4 15.56 139.00 16.04 137.5 14.75 143.7 7.791 E+04 569045.4 15.56 139.00 16.04 137.5 14.75 143.7 7.791 E+04 570295.4 15.55 138.90 16.05 137.5 14.74 143.7 7.791 E+04 571545.4 15.55 138.90 16.05 137.5 14.74 143.6 7.791 E+04 572795.4 15.55 138.90 16.05 137.5 14.74 143.6 7.791 E+04 574045.4 15.55 138.90 16.03 137.4 14.72 143.6 7.791 E+04 575295.4 15.55 138.80 16.03 137.4 14.72 143.6 7.791 E+04 576545.4 15.54 138.80 16.04 137.4 14.72 143.6 7.791 E+04 577795.4 15.54 138.80 16.04 137.4 14.72 143.5 7.791 E+04 579045.4 15.54 138.80 16.04 137.4 14.72 143.5 7.791 E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 108 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 580295.4 15.54 138.70 16.02 137.3 14.70 143.5 7.790E+04 581545.4 15.54 138.70 16.02 137.3 14.70 143.4 7.790E+04 582795.4 15.53 138.70 16.03 137.3 14.70 143.4 7.790E+04 584045.4 15.53 138.70 16.03 137.3 14.70 143.4 7.790E+04 585295.4 15.53 138.60 16.01 137.2 14.70 143.3 7.790E+04 586545.4 15.53 138.60 16.01 137.2 14.70 143.3 7.790E+04 587795.4 15.52 138.50 16.02 137.2 14.70 143.3 7.790E+04 589045.4 15.52 138.50 16.02 137.2 14.70 143.2 7.790E+04 590295.4 15.52 138.50 16.02 137.2 14.70 143.2 7.790E+04 591545.4 15.52 138.50 16.00 137.1 14.70 143.2 7.790E+04 592795.4 15.52 138.50 16.00 137.1 14.70 143.2 7.790E+04 594045.4 15.52 138.50 16.00 137.1 14.70 143.2 7.790E+04 595295.4 15.51 138.40 16.01 137.1 14.70 143.1 7.790E+04 596545.4 15.51 138.40 16.01 137.1 14.70 143.1 7.790E+04 597795.4 15.52 138.50 15.99 136.9 14.70 143.1 7.790E+04 599045.4 15.51 138.30 16.00 137.0 14.70 143.0 7.790E+04 600295.4 15.50 138.30 16.00 137.0 14.70 143.0 7.790E+04 601545.4 15.50 138.30 16.00 137.0 14.70 143.0 7.790E+04 602795.4 15.50 138.30 16.00 137.0 14.70 143.0 7.790E+04 604045.4 15.50 138.30 16.00 137.0 14.70 143.0 7.790E+04 605295.4 15.50 138.30 16.00 137.0 14.70 143.0 7.790E+04 606545.4 15.50 138.30 16.00 137.0 14.70 143.0 7.790E+04 607795.4 15.50 138.20 15.99 136.8 14.70 142.9 7.788E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 109 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Lonq-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 609045.4 15.50 138.20 15.99 136.8 14.70 142.9 7.788E+04 610295.4 15.49 138.20 15.99 136.8 14.70 142.8 7.788E+04 611545.4 15.49 138.10 15.99 136.8 14.70 142.8 7.788E+04 612795.4 15.49 138.10 15.98 136.7 14.70 142.8 7.788E+04 614045.4 15.49 138.10 15.98 136.7 14.70 142.8 7.788E+04 615295.4 15.49 138.10 15.98 136.7 14.70 142.8 7.788E+04 616545.4 15.48 138.10 15.98 136.7 14.70 142.7 7.788E+04 617795.4 15.48 138.00 15.98 136.7 14.70 142.7 7.788E+04 619045.4 15.48 138.00 15.98 136.7 14.70 142.7 7.788E+04 620295.4 15.48 138.00 15.97 136.6 14.70 142.7 7.788E+04 621545.4 15.48 138.00 15.97 136.6 14.70 142.6 7.788E+04 622795.4 15.48 138.00 15.97 136.6 14.70 142.6 7.788E+04 624045.4 15.47 137.90 15.97 136.6 14.70 142.6 7.788E+04 625295.4 15.47 137.90 15.96 136.5 14.70 142.5 7.788E+04 626545.4 15.47 137.90 15.96 136.5 14.70 142.5 7.788E+04 627795.4 15.47 137.90 15.96 136.5 14.70 142.5 7.788E+04 629045.4 15.47 137.90 15.96 136.5 14.70 142.5 7.788E+04 630295.4 15.47 137.80 15.96 136.5 14.70 142.5 7.788E+04 631545.4 15.46 137.80 15.96 136.5 14.70 142.4 7.788E+04 632795.4 15.46 137.80 15.95 136.4 14.70 142.4 7.788E+04 634045.4 15.46 137.70 15.95 136.4 14.70 142.4 7.787E+04 635295.4 15.46 137.70 15.95 136.4 14.70 142.3 7.787E+04 636545.4 15.45 137.70 15.95 136.4 14.70 142.3 7.787E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 110 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (f1) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 637795.4 15.45 137.60 15.94 136.3 14.70 142.3 7.787E+04 639045.4 15.45 137.60 15.94 136.3 14.70 142.2 7.787E+04 640295.4 15.45 137.60 15.94 136.3 14.70 142.2 7.787E+04 641545.4 15.45 137.60 15.94 136.3 14.70 142.2 7.787E+04 642795.4 15.44 137.50 15.93 136.2 14.70 142.1 7.787E+04 644045.4 15.44 137.50 15.93 136.2 14.70 142.1 7.787E+04 645295.4 15.44 137.50 15.93 136.2 14.70 142.1 7.787E+04 646545.4 15.44 137.40 15.92 136.1 14.70 142.0 7.787E+04 647795.4 15.43 137.40 15.92 136.1 14.70 142.0 7.787E+04 649045.4 15.43 137.40 15.92 136.1 14.70 142.0 7.787E+04 650295.4 15.43 137.30 15.93 136.1 14.70 141.9 7.787E+04 651545.4 15.43 137.30 15.93 136.1 14.70 141.9 7.787E+04 652795.4 15.43 137.30 15.91 136.0 14.70 141.9 7.787E+04 654045.4 15.43 137.30 15.91 136.0 14.70 141.9 7.787E+04 655295.4 15.43 137.30 15.92 136.0 14.70 141.9 7.787E+04 656545.4 15.42 137.30 15.92 136.0 14.70 141.9 7.787E+04 657795.4 15.42 137.20 15.92 136.0 14.70 141.8 7.785E+04 659045.4 15.42 137.20 15.91 135.9 14.70 141.8 7.785E+04 660295.4 15.42 137.20 15.91 135.9 14.70 141.8 7.785E+04 661545.4 15.42 137.20 15.91 135.9 14.70 141.8 7.785E+04 662795.4 15.41 137.10 15.91 135.9 14.70 141.7 7.785E+04 664045.4 15.41 137.10 15.91 135.9 14.70 141.7 7.785E+04 665295.4 15.41 137.10 15.90 135.8 14.70 141.7 7.785E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 111 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 666545.4 15.41 137.00 15.90 135.8 14.70 141.6 7.785E+04 667795.4 15.41 137.00 15.90 135.8 14.70 141.6 7.785E+04 669045.4 15.40 137.00 15.89 135.7 14.70 141.6 7.785E+04 670295.4 15.40 137.00 15.89 135.7 14.70 141.5 7.785E+04 671545.4 15.40 136.90 15.89 135.7 14.70 141.5 7.785E+04 672795.4 15.40 136.90 15.89 135.7 14.70 141.5 7.785E+04 674045.4 15.40 136.90 15.88 135.6 14.70 141.4 7.785E+04 675295.4 15.39 136.90 15.88 135.6 14.70 141.4 7.785E+04 676545.4 15.39 136.90 15.89 135.6 14.70 141.4 7.785E+04 677795.4 15.39 136.80 15.89 135.6 14.70 141.4 7.785E+04 679045.4 15.39 136.80 15.89 135.6 14.70 141.4 7.785E+04 680295.4 15.39 136.80 15.89 135.6 14.70 141.4 7.785E+04 681545.5 15.39 136.80 15.88 135.5 14.70 141.3 7.785E+04 682795.5 15.39 136.80 15.88 135.5 14.70 141.3 7.785E+04 684045.5 15.38 136.70 15.88 135.5 14.70 141.3 7.784E+04 685295.6 15.38 136.70 15.87 135.4 14.70 141.2 7.784E+04 686545.6 15.38 136.70 15.87 135.4 14.70 141.2 7.784E+04 687795.6 15.38 136.60 15.87 135.4 14.70 141.2 7.784E+04 689045.6 15.37 136.60 15.87 135.4 14.70 141.1 7.784E+04 690295.6 15.37 136.60 15.87 135.4 14.70 141.1 7.784E+04 691545.9 15.38 136.60 15.86 135.3 14.70 141.1 7.784E+04 692795.9 15.38 136.60 15.86 135.3 14.70 141.1 7.784E+04 694045.9 15.37 136.50 15.87 135.3 14.70 141.1 7.784E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 112 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 695295.9 15.37 136.50 15.87 135.3 14.70 141.1 7.784E+04 696545.9 15.37 136.50 15.87 135.3 14.70 141.0 7.784E+04 697795.9 15.37 136.50 15.86 135.2 14.70 141.0 7.784E+04 699045.9 15.37 136.50 15.86 135.2 14.70 141.0 7.784E+04 700295.9 15.36 136.40 15.86 135.2 14.70 141.0 7.784E+04 701545.9 15.36 136.40 15.86 135.2 14.70 140.9 7.784E+04 702795.9 15.36 136.40 15.85 135.1 14.70 140.9 7.784E+04 704045.9 15.36 136.40 15.85 135.2 14.70 140.9 7.784E+04 705295.9 15.36 136.30 15.85 135.2 14.70 140.8 7.784E+04 706545.9 15.36 136.30 15.85 135.2 14.70 140.8 7.784E+04 707795.9 15.36 136.30 15.85 135.2 14.70 140.8 7.784E+04 709045.9 15.35 136.30 15.84 135.1 14.70 140.8 7.784E+04 710295.9 15.35 136.30 15.85 135.1 14.70 140.8 7.784E+04 711545.9 15.35 136.20 15.85 135.1 14.70 140.7 7.784E+04 712795.9 15.35 136.20 15.84 135.0 14.70 140.7 7.782E+04 714045.9 15.35 136.20 15.84 135.0 14.70 140.7 7.782E+04 715295.9 15.35 136.20 15.84 135.0 14.70 140.7 7.782E+04 716545.9 15.34 136.10 15.84 135.0 14.70 140.6 7.782E+04 717795.9 15.34 136.10 15.83 134.9 14.70 140.6 7.782E+04 719045.9 15.34 136.10 15.83 134.9 14.70 140.6 7.782E+04 720295.9 15.34 136.10 15.83 134.9 14.70 140.5 7.782E+04 721545.9 15.34 136.10 15.83 134.8 14.70 140.5 7.782E+04 722795.9 15.33 136.00 15.83 134.8 14.70 140.5 7.782E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 113 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Tenn DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 724045.9 15.33 136.00 15.83 134.8 14.70 140.5 7.782E+04 725295.9 15.33 136.00 15.82 134.7 14.70 140.4 7.782E+04 726545.9 15.33 135.90 15.82 134.7 14.70 140.4 7.782E+04 727795.9 15.33 135.90 15.82 134.7 14.70 140.4 7.782E+04 729045.9 15.33 135.90 15.82 134.7 14.70 140.3 7.782E+04 730295.9 15.32 135.90 15.81 134.7 14.70 140.3 7.782E+04 731545.9 15.32 135.80 15.82 134.7 14.70 140.3 7.782E+04 732795.9 15.32 135.80 15.82 134.7 14.70 140.2 7.782E+04 734045.9 15.32 135.80 15.81 134.6 14.70 140.2 7.782E+04 735295.9 15.32 135.80 15.81 134.6 14.70 140.2 7.782E+04 736545.9 15.31 135.70 15.81 134.6 14.70 140.2 7.781 E+04 737795.9 15.32 135.70 15.80 134.5 14.70 140.2 7.781 E+04 739045.9 15.32 135.70 15.81 134.5 14.70 140.2 7.781 E+04 740295.9 15.32 135.70 15.81 134.5 14.70 140.2 7.781 E+04 741545.9 15.32 135.70 15.81 134.5 14.70 140.2 7.781 E+04 742795.9 15.32 135.70 15.81 134.5 14.70 140.2 7.781 E+04 744045.9 15.32 135.70 15.81 134.5 14.70 140.2 7.781 E+04 745295.9 15.32 135.70 15.81 134.5 14.70 140.1 7.781 E+04 746545.9 15.32 135.70 15.81 134.5 14.70 140.1 7.781 E+04 747795.9 15.32 135.70 15.81 134.5 14.70 140.1 7.781 E+04 749045.9 15.32 135.70 15.81 134.5 14.70 140.1 7.781 E+04 750295.9 15.32 135.70 15.81 134.5 14.70 140.1 7.781 E+04 751545.9 15.32 135.70 15.81 134.5 14.70 140.1 7.781 E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 114 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 752795.9 15.32 135.70 15.81 134.4 14.70 140.1 7.781 E+04 754045.9 15.32 135.70 15.81 134.5 14.70 140.1 7.781 E+04 755295.9 15.31 135.60 15.81 134.5 14.70 140.1 7.781 E+04 756545.9 15.31 135.60 15.80 134.3 14.70 140.0 7.781 E+04 757795.9 15.31 135.60 15.80 134.4 14.70 140.0 7.781 E+04 759045.9 15.31 135.50 15.79 134.3 14.70 139.9 7.781 E+04 760295.9 15.30 135.50 15.80 134.3 14.70 139.9 7.781 E+04 761545.9 15.30 135.40 15.80 134.3 14.70 139.9 7.781 E+04 762795.9 15.30 135.40 15.79 134.3 14.70 139.8 7.781 E+04 764045.9 15.30 135.40 15.79 134.3 14.70 139.8 7.781 E+04 765295.9 15.29 135.30 15.78 134.2 14.70 139.8 7.781 E+04 766545.9 15.29 135.30 15.79 134.2 14.70 139.7 7.781 E+04 767795.9 15.29 135.30 15.79 134.2 14.70 139.7 7.781 E+04 769045.9 15.29 135.20 15.78 134.1 14.70 139.6 7.781 E+04 770295.9 15.28 135.20 15.78 134.1 14.70 139.6 7.779E+04 771545.9 15.28 135.20 15.78 134.1 14.70 139.6 7.779E+04 772795.9 15.28 135.20 15.78 134.1 14.70 139.6 7.779E+04 774045.9 15.28 135.20 15.77 134.0 14.70 139.5 7.779E+04 775295.9 15.28 135.10 15.77 134.0 14.70 139.5 7.779E+04 776545.9 15.28 135.10 15.77 134.0 14.70 139.5 7.779E+04 777795.9 15.28 135.10 15.77 134.0 14.70 139.5 7.779E+04 779045.9 15.27 135.10 15.77 133.9 14.70 139.4 7.779E+04 780295.9 15.27 135.00 15.77 133.9 14.70 139.4 7.779E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 115 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 781545.9 15.27 135.00 15.75 133.8 14.70 139.4 7.779E+04 782795.9 15.27 135.00 15.76 133.8 14.70 139.3 7.779E+04 784045.9 15.27 135.00 15.76 133.8 14.70 139.3 7.779E+04 785295.9 15.27 134.90 15.76 133.8 14.70 139.3 7.779E+04 786545.9 15.26 134.90 15.76 133.8 14.70 139.3 7.779E+04 787795.9 15.26 134.90 15.75 133.8 14.70 139.2 7.779E+04 789045.9 15.26 134.90 15.75 133.8 14.70 139.2 7.779E+04 790295.9 15.26 134.80 15.75 133.8 14.70 139.2 7.779E+04 791545.9 15.26 134.80 15.75 133.8 14.70 139.2 7.779E+04 792795.9 15.26 134.80 15.75 133.7 14.70 139.1 7.779E+04 794045.9 15.25 134.70 15.75 133.7 14.70 139.1 7.779E+04 795295.9 15.25 134.70 15.75 133.7 14.70 139.1 7.778E+04 796545.9 15.25 134.70 15.74 133.6 14.70 139.0 7.778E+04 797795.9 15.25 134.70 15.74 133.6 14.70 139.0 7.778E+04 799045.9 15.25 134.60 15.74 133.6 14.70 139.0 7.778E+04 800295.9 15.24 134.60 15.73 133.5 14.70 138.9 7.778E+04 801545.9 15.24 134.60 15.73 133.5 14.70 138.9 7.778E+04 802795.9 15.24 134.50 15.74 133.5 14.70 138.9 7.778E+04 804045.9 15.24 134.60 15.74 133.5 14.70 138.9 7.778E+04 805295.9 15.24 134.50 15.74 133.5 14.70 138.9 7.778E+04 806545.9 15.24 134.50 15.74 133.5 14.70 138.9 7.778E+04 807795.9 15.24 134.50 15.73 133.4 14.70 138.9 7.778E+04 809045.9 15.24 134.50 15.73 133.4 14.70 138.8 7.778E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 116 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 810295.9 15.23 134.50 15.73 133.4 14.70 138.8 7.778E+04 811545.9 15.23 134.40 15.72 133.3 14.70 138.7 7.778E+04 812795.9 15.23 134.40 15.72 133.3 14.70 138.7 7.778E+04 814045.9 15.23 134.40 15.72 133.3 14.70 138.7 7.778E+04 815295.9 15.23 134.40 15.72 133.3 14.70 138.7 7.777E+04 816545.9 15.23 134.40 15.72 133.3 14.70 138.7 7.777E+04 817795.9 15.23 134.40 15.72 133.3 14.70 138.7 7.778E+04 819045.9 15.23 134.30 15.72 133.3 14.70 138.7 7.778E+04 820295.9 15.22 134.30 15.72 133.3 14.70 138.6 7.778E+04 821545.9 15.22 134.30 15.72 133.3 14.70 138.6 7.777E+04 822795.9 15.22 134.20 15.71 133.2 14.70 138.5 7.777E+04 824045.9 15.22 134.20 15.71 133.2 14.70 138.5 7.777E+04 825295.9 15.22 134.20 15.71 133.2 14.70 138.5 7.777E+04 826545.9 15.22 134.20 15.70 133.1 14.70 138.5 7.776E+04 827795.9 15.21 134.10 15.70 133.1 14.70 138.4 7.776E+04 829045.9 15.21 134.10 15.71 133.1 14.70 138.4 7.776E+04 830295.9 15.21 134.10 15.70 133.0 14.70 138.4 7.776E+04 831545.9 15.21 134.00 15.70 133.0 14.70 138.3 7.776E+04 832795.9 15.20 134.00 15.70 133.0 14.70 138.3 7.776E+04 834045.9 15.20 134.00 15.70 133.0 14.70 138.3 7.776E+04 835295.9 15.20 134.00 15.69 132.9 14.70 138.3 7.776E+04 836545.9 15.20 134.00 15.69 132.9 14.70 138.2 7.776E+04 837795.9 15.20 133.90 15.69 132.9 14.70 138.2 7.776E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 117 of 123 NON-PROPRIETARY INFORMATION Table SPSB-C-33-2 SHEX Long-Term DBA-LOCA Containment Response for NPSH Evaluation Time (sec) Drywell Drywell Wetwell Wetwell Wetwell Suppression Suppression Pressure Temperature Pressure Temperature Pressure with Pool Pool Volume without ((F) without (F) Leakage (psia) Temperature (ft3 ) (Including leakage (psia) leakage (psia) (F) Vent Liquid) 839045.9 15.20 133.90 15.70 132.9 14.70 138.2 7.776E+04 840295.9 15.20 133.90 15.69 132.9 14.70 138.2 7.776E+04 841545.9 15.20 133.90 15.69 132.9 14.70 138.2 7.776E+04 842795.9 15.20 133.90 15.69 132.9 14.70 138.1 7.776E+04 844045.9 15.19 133.80 15.69 132.9 14.70 138.1 7.776E+04 845295.9 15.19 133.80 15.69 132.9 14.70 138.1 7.776E+04 846545.9 15.19 133.80 15.68 132.8 14.70 138.1 7.776E+04 847795.9 15.19 133.80 15.68 132.8 14.70 138.0 7.776E+04 849045.9 15.19 133.70 15.67 132.7 14.70 138.0 7.776E+04 850295.9 15.18 133.70 15.68 132.7 14.70 138.0 7.776E+04 851545.9 15.18 133.70 15.68 132.7 14.70 137.9 7.775E+04 852795.9 15.18 133.70 15.68 132.7 14.70 137.9 7.775E+04 854045.9 15.18 133.60 15.67 132.6 14.70 137.9 7.775E+04 855295.9 15.18 133.60 15.67 132.6 14.70 137.9 7.775E+04 856545.9 15.18 133.60 15.67 132.6 14.70 137.8 7.775E+04 857795.9 15.18 133.60 15.66 132.5 14.70 137.8 7.775E+04 859045.9 15.17 133.50 15.67 132.6 14.70 137.8 7.775E+04 860295.9 15.17 133.50 15.67 132.6 14.70 137.7 7.775E+04 861545.9 15.17 133.50 15.66 132.5 14.70 137.7 7.775E+04 862795.9 15.17 133.40 15.66 132.5 14.70 137.7 7.774E+04 864000 15.16 133.40 15.66 132.5 14.70 137.6 7.775E+04
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 118 of 123 NON-PROPRIETARY INFORMATION 350.0 300.0 250.0 E 200.0 I 150.0 100.0 50.0 0.0 0 100 200 300 400 500 600 700 Time nsec)
Figure SPSB-C-33-1 SHEX Short-Term (600 sec) Containment Temperature for NPSH
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 119 of 123 NON-PROPRIETARY INFORMATION Figure SPSB-C-33-2 40.00 35.00 Drywell Pressure
- - - Wetwell Pressure with 1.5% per 30.00 ;- day Leakage 25.00 J 20.00 0 100 200 300 400 S00 600 700 Tkne (sec)
SHEX Short-Term (600 sec) Containment Pressure for NPSH
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 120 of 123 NON-PROPRIETARY INFORMATION 300.00 E
0.004 .
100 1000 10000 100000 1000000 Tnm. (sec)
Figure SPSB-C-33-3 SHEX Long-Term (10 Day) Containment Temperature for NPSH
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 121 of 123 NON-PROPRIETARY INFORMATION 35.00 30.00 25.00 s 20.00 I 15.00 10.00 5.00 0.00 4-100 1000 10000 100000 1000000 Time (sec)
Figure SPSB-C-33-4 SHEX Long-Term (10 Day) Containment Pressure for NPSH
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 122 of 123 NON-PROPRIETARY INFORMATION Suppression Pool Level Short-Term
- NPSH Basis - Based on SHEX SPVolume 12.4 12.2 12.0
- 11.8
, 11.6 n 11.4 wn ., -
11.2 11.0 10.8 0 100 200 300 400 500 600 Time (sec)
Figure SPSB-C-33-5 Suppression Pool Level Response - Short-Term
Attachment 2 to BVY 04-081 Docket No. 50-271 Page 123 of 123 NON-PROPRIETARY INFORMATION Suppression Pool Level Long-Term NPSH . Basis Based on SHEX SP Volume I 12.4 12.2 rp--,
. . . %-W.
12.0 . . . . . . . . . wm a a a w w a wa w a a wa . . . . . .
'-W 11.8 4-0W 11.6 z~ 11.4 11.2 11.0 10.8 I I i I I C> UL) I', Lfl Cf) LC) UI) In) co 01 Co 0 C) 0D C> CD W1 +
0 W W IL w~ C) C+
C) +4 C) C)w' 0~ Us w:
I. C)i 0 1- 06 CD C6 Time (sec)
Figure SPSB-C-33-6 Suppresslon Pool Level Response - Long-Term
BVY 04-081 Docket No. 50-271 Attachment 3 Vermont Yankee Nuclear Power Station Proposed Technical Specification Change No. 263 - Supplement No. 11 Extended Power Uprate Response to Request for Additional Information Affidavit - General Electric Company Total number of pages In Attachment 3 (excludinc this cover sheet) Is 3.
General Electric Company AFFIDAVIT I, James F. Klapproth, state as follows:
(1) I am General Manager, Engineering and Technology, General Electric Company ("GE")
and have been delegated the function of reviewing the information described in paragraph (2) which is sought to be withheld, and have been authorized to apply for its withholding.
(2) The information sought to be withheld is contained in Attachment 2 to GE letter GE-VYNPS-AEP-355, Michael Dick (GE) to Craig Nichols (ENOI), VYNPS Extended Power Uprate - Response to NRC Request for Additional Information, Proprietary and Non-ProprietaryVersions, dated August 6, 2004. The Attachment 2 proprietary information, GE Responses to NRC RAIs (SPSB-C-32 and 33), is delineated by a double underline inside double square brackets. In each case, the superscript notation( 1 refers to Paragraph (3) of this affidavit, which provides the basis for the proprietary determination.
(3) In making this application for withholding of proprietary information of which it is the owner, GE relies upon the exemption from disclosure set forth in the Freedom of Information Act ("FOIA"), 5 USC Sec. 552(b)(4), and the Trade Secrets Act, 18 USC Sec. 1905, and NRC regulations 10 CFR 9.17(a)(4), and 2.790(a)(4) for "trade secrets" (Exemption 4). The material for which exemption from disclosure is here sought also qualify under the narrower definition of "trade secret", within the meanings assigned to those terms for purposes of FOIA Exemption 4 in, respectively, Critical Mass Energv Project v. Nuclear Repulatorv Commission. 975F2d871 (DC Cir. 1992), and Public Citizen Health Research Group v. FDA, 704F2dl280 (DC Cir. 1983).
(4) Some examples of categories of information which fit into the definition of proprietary information are:
- a. Information that discloses a process, method, or apparatus, including supporting data and analyses, where prevention of its use by General Electric's competitors without license from General Electric constitutes a competitive economic advantage over other companies;
- b. Information which, if used by a competitor, would reduce his expenditure of resources or improve his competitive position in the design, manufacture, shipment, installation, assurance of quality, or licensing of a similar product;
- c. Information which reveals aspects of past, present, or future General Electric customer-funded development plans and programs, resulting in potential products to General Electric;
- d. Information which discloses patentable subject matter for which it maybe desirable to obtain patent protection.
The information sought to be withheld is considered to be proprietary for the reasons set forth in paragraphs (4)a., and (4)b, above.
JFK-08-06-04-AFAff 355.doc Affidavit Page I
(5) To address 10 CFR 2.790 (b) (4), the information sought to be withheld is being submitted to NRC in confidence. The information is of a sort customarily held in confidence by GE, and is in fact so held. The information sought to be withheld has, to the best of my knowledge and belief, consistently been held in confidence by GE, no public disclosure has been made, and it is not available in public sources. All disclosures to third parties including any required transmittals to NRC, have been made, or must be made, pursuant to regulatory provisions or proprietary agreements which provide for maintenance of the information in confidence. Its initial designation as proprietary information, and the subsequent steps taken to prevent its unauthorized disclosure, are as set forth in paragraphs (6) and (7) following.
(6) Initial approval of proprietary treatment of a document is made by the manager of the originating component, the person most likely to be acquainted with the value and sensitivity of the information in relation to industry knowledge. Access to such documents within GE is limited on a "need to know" basis.
(7) The procedure for approval of external release of such a document typically requires review by the staff manager, project manager, principal scientist or other equivalent authority, by the manager of the cognizant marketing function (or his delegate), and by the Legal Operation, for technical content, competitive effect, and determination of the accuracy of the proprietary designation. Disclosures outside GE are limited to regulatory bodies, customers, and potential customers, and their agents, suppliers, and licensees, and others with a legitimate need for the information, and then only in accordance with appropriate regulatory provisions or proprietary agreements.
(8) The information identified in paragraph (2), above, is classified as proprietary because it contains detailed information in support of NEDC-33090P, Safety Analysis Report for Vermont Yankee Nuclear Power Station Constant Pressure Power Uprate, Class m (GE Proprietary Information), Revision 0, dated September 2003, which was submitted to the NRC. This power uprate report contains detailed results and conclusions from evaluations of the safety-significant changes necessary to demonstrate the regulatory acceptability for the power uprate of a GE BWR, utilizing analytical models, methods and processes, including computer codes, which GE has developed, obtained NRC approval of and applied to perform evaluations of the transient and accident events in the GE Boiling Water Reactor
('BWR"). The development and approval of these system, component, and thermal hydraulic models and computer codes was achieved at a significant cost to GE, on the order of several million dollars.
The development of the evaluation process along with the interpretation and application of the analytical results is derived from the extensive experience database that constitutes a major GE asset.
(9) Public disclosure of the information sought to be withheld is likely to cause substantial harm to GE's competitive position and foreclose or reduce the availability of profit-making opportunities. The information is part of GE's comprehensive BWR safety and technology base, and its commercial value extends beyond the original development cost. The value of the technology base goes beyond the extensive physical database and analytical methodology and includes development of the expertise to determine and apply the JFK-08-06-04-AFAff 355.doc Affidavit Page 2
appropriate evaluation process. In addition, the technology base includes the value derived from providing analyses done with NRC-approved methods.
The research, development, engineering, analytical and NRC review costs comprise a substantial investment of time and money by GE.
The precise value of the expertise to devise an evaluation process and apply the correct analytical methodology is difficult to quantify, but it clearly is substantial.
GE's competitive advantage will be lost if its competitors are able to use the results of the GE experience to normalize or verify their own process or if they are able to claim an equivalent understanding by demonstrating that they can arrive at the same or similar conclusions.
The value of this information to GE would be lost if the information were disclosed to the public. Making such information available to competitors without their having been required to undertake a similar expenditure of resources would unfairly provide competitors with a windfall, and deprive GE of the opportunity to exercise its competitive advantage to seek an adequate return on its large investment in developing these very valuable analytical tools.
I declare under penalty of penury that the foregoing affidavit and the matters stated therein are true and correct to the best of my knowledge, information, and belief Executed on this J Iday of OVI D 2004.
James F. Klappctic C General Electric Company JFK-08-06-04-AFAff 355.doc Affidavit Page 3