ML081830409

GE-NE-0000-0047-1716-R1, DTE Energy Enrico Fermi 2, Safer/Gestr Loss-of-Coolant Accident Analysis for GE11 Fuel.

ML081830409
Person / Time
Site:	Fermi
Issue date:	06/30/2008
From:	GE-Hitachi Nuclear Energy Americas
To:	Office of Nuclear Reactor Regulation
References
DRF # 0000-0044-2864, NRC-08-0046 GE-NE-0000-0047-1716-R1
Download: ML081830409 (98)

Text

ENCLOSURE 5 TO NRC-08-0046 DTE Energy ENRICO FERMI 2 SAFER/GESTR Loss-of-Coolant Accident Analysis for GEll Fuel GE-NE-0000-0047-1716 Revision 1

[NON-PROPRIETARY VERSION]

GE Hitachi Nuclear Energy 3901 Castle Hayne Rd

@ HITACHI Wilmington, NC 28402 GE-NE-0000-0047-1716-Ri DRF # 0000-0044-2864 Class III June 2008 GEHNON-PROPRIETARY VERSION DTE Energy ENRICO FERMI 2 SAFER/GESTR Loss-of-Coolant Accident Analysis for GEll Fuel

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION NON-PROPRIETARY NOTICE This is a non-proprietary version of the document, from which the proprietary information has been removed. Portions of the document that have been removed are identified by white space within double square brackets, as shown here (( )).

IMPORTANT NOTICE REGARDING CONTENTS OF THIS REPORT PLEASE READ CAREFULLY The only undertakings of the GE-Hitachi Nuclear Energy (GEH) respecting information in this document are contained in the contract between DTE Energy and GEH for Fuel Bundle Fabrication and Related Services, as amended to the date of transmittal of this document, and nothing contained in this document shall be construed as changing the contract. The use of this information by anyone other than DTE Energy, or for any purpose other than that for which it is intended is not authorized; and with respect to any unauthorized use, GEH makes no representation or warranty, express or implied, and assumes no liability as to the completeness, accuracy or usefulness of the information contained in this document, or that its use may not infringe privately owned rights.

Copyright 2008, GE-Hitachi Nuclear Energy Americas LLC, All Rights Reserved 1

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION TABLE OF CONTENTS Page

1.0 INTRODUCTION

1

2.0 DESCRIPTION

OF MODELS 1 3.0 ANALYSIS PROCEDURE 1 3.1 Licensing Criteria 1 3.2 SAFER/GESTR-LOCA Licensing Methodology 1 3.3 Generic Analysis 1 3.4 ENRICO FERMI 2 Specific Analysis 1 4.0 INPUT TO ANALYSIS 2 5.0 RESULTS 4 5.1 Large Recirculation Line Breaks 4 5.2 Small Recirculation Line Breaks 5 5.3 Non-Recirculation Line Breaks 6 5.4 Alternate Operating Modes 6 5.5 Compliance Evaluations 7

6.0 CONCLUSION

S 12

7.0 REFERENCES

15 Appendix A Operating Plant Licensing Parameters (OPL-4/5) 35 ii

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION LIST OF TABLES Table Title Pa~e Table 1 Plant Operational Parameters 2 Table 2 GE 1I Fuel Parameters 3 Table 3 Summary of Large Recirculation Line Break Results 9 Table 4 Summary of Small Recirculation Line Break Results 10 Table 5 SLO Analysis for GEl 1 Fuel - Division II Battery Failure 11 Table 6 FWTR Analysis - Division II Battery Failure 11 Table 7 ECCS-LOCA Analysis Results for GEl 1 13 Table 8 Thermal Limits for GE 11 14 iii

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION LIST OF FIGURES Figure Title Page Figure 1-a Water Level in Hot and Average Channels. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available) [Nominal Assumptions] 16 Figure 1-b Reactor Vessel Pressure. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available) [Nominal Assumptions] 17 Figure 1-c Peak Cladding Temperature. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available) [Nominal Assumptions] 18 Figure 1-d Heat Transfer Coefficients. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available) [Nominal Assumptions] 19 Figure l-e ECCS Flows. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available) [Nominal Assumptions] 20 Figure 2-a Water Level in Hot and Average Channels. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available) [Appendix-K Assumptions] 21 Figure 2-b Reactor Vessel Pressure. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available)

[Appendix-K Assumptions] 22 Figure 2-c Peak Cladding Temperature. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available)

[Appendix-K Assumptions] 23 Figure 2-d Heat Transfer Coefficients. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available)

[Appendix-K Assumptions] 24 Figure 2-e ECCS Flows. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available) [Appendix-K Assumptions] 25 Figure 3-a Water Level in Hot and Average Channels. Limiting Small Recirculation Line Break (( f], Division I Battery (HPCI + 2LPCI

+ 1LPCS Available) [Nominal Assumptions] 26 Figure 3-b Reactor Vessel Pressure. Limiting Small Recirculation Line Break H f)), Division I Battery (HPCI + 2LPCI + 1LPCS Available)

[Nominal Assumptions 27 Figure 3-c Peak Cladding Temperature. Limiting Small Recirculation Line Break

(( )), Division I Battery (HPCI + 2LPCI +I1LPCS Available)

[Nominal Assumptions] 28 iv

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Figure 3-d Heat Transfer Coefficients. Limiting Small Recirculation Line Break

[ f)), Division I Battery (HPCI + 2LPCI + 1LPCS Available)

[Nominal Assumptions] 29 Figure 3-e ECCS Flows. Limiting Small Recirculation Line Break

)), Division I Battery (HPCI + 2LPCI + 1LPCS Available)

[Nominal Assumptions] 30 Figure 4-a Water Level in Hot and Average Channels. Limiting Small Recirculation Line Break [1 )), Division I Battery (HPCI + 2LPCI

+ 1LPCS Available) [Appendix K Assumptions] 31 Figure 4-b Reactor Vessel Pressure. Limiting Small Recirculation Line Break R f)), Division I Battery (HPCI + 2LPCI + 1LPCS Available)

[Appendix K Assumptions] 32 Figure 4-c Peak Cladding Temperature. Limiting Small Recirculation Line Break

[ f)), Division I Battery (HPCI + 2LPCI + lLPCS Available)

[Appendix K Assumptions] 33 Figure 4-d Heat Transfer Coefficients. Limiting Small Recirculation Line Break U f)), Division I Battery (HPCI + 2LPCI + 1LPCS Available)

[Appendix K Assumptions] 34 Figure 4-e ECCS Flows. Limiting Small Recirculation Line Break

[ f)), Division I Battery (HPCI + 2LPCI + lLPCS Available)

[Appendix K Assumptions] 34 v

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION

1.0 INTRODUCTION

The purpose of this document is to supplement the ECCS-LOCA evaluation results for the ENRICO FERMI 2 documented in the Reference 1 analysis. Specifically, using the limiting cases, results are provided for GEl 1 fuel. The plant ECCS parameters and analysis methodology are consistent with those defined in Reference 1.

2.0 DESCRIPTION

OF MODELS Consistent with Reference 1, the ECCS-LOCA results are generated using the standard four GE-NE computer models. These models are LAMB, TASC, SAFER and GESTR-LOCA.

See Reference 1 for further details.

3.0 ANALYSIS PROCEDURE 3.1 LICENSING CRITERIA Consistent with Reference 1, the acceptance criteria for the ECCS-LOCA results are based on the Code of Federal Regulations, 10 CFR 50.46. See Reference 1 for further details.

3.2 SAFER/GESTR-LOCA LICENSING METHODOLOGY Consistent with Reference 1, the ECCS-LOCA analysis was generated using the SAFER/GESTR-LOCA licensing methodology (References 2, 3 and 4) as approved by the NRC (References 5 and 6).

3.3 GENERIC ANALYSIS The generic ECCS-LOCA analysis for the BWR-3/4 product line is described in Reference 1.

3.4 ENRICO FERMI 2 SPECIFIC ANALYSIS The ENRICO FERMI 2 specific analysis in Reference 1 demonstrated that the nominal and Appendix K PCT. trends as a function of break size were consistent with one another and with the generic results. For large breaks, the DBA recirculation suction break with Division II Battery is the limiting break/failure combination for both Nominal and Appendix K assumptions. The Division I Battery failure is the limiting failure for small breaks.

1

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION 4.0 INPUT TO ANALYSIS The Operating Parameters List 4/5 (OPL4/5) parameters used in this analysis are given in Appendix A. The plant heat balance conditions utilized in this analysis are presented in Table 1. The GE 11 fuel parameters are given in Table 2.

All known ECCS-LOCA analysis errors (up to and including error # 2007-01) have been accounted for in this analysis.

Table 1 Plant Operational Parameters Plant Parameters Nominal Appendix K Core Thermal Power* (MWt) / 3952/ 403 1/

(% of Current Operating Thermal Power) (115.2) (117.5)

Core Flow (Mlb/hr) / 100.0/ 100.0/

(% of Rated Core Flow) (100) (100)

Vessel Dome Pressure (psia) 1045 1060

• Current Operating Thermal Power (CLTP) is 3430 MWt.

Extended Power Uprate (EPU) Thermal Power is 3952 MWt.

2

GE-NE-OOOO-0047-I 716-RI GEH NON-PROPRIETARY VERSION Table 2 GEll Fuel Parameters Fuel Parameter Analysis Value PLHGR (kW/ft) -LOCA Analysis Limit [H 1]

-Appendix K (( )) x 1.02

-Nominal

_1 1]

MAPLHGR* (kW/ft) -LOCA Analysis Limit 13.42

-Appendix K 13.42 x 1.02

-Nominal 12.86 Worst Case Pellet Exposure for ECCS Evaluation (( ]

(MWd/MTU)

Initial Operating MCPR* -LOCA Analysis Limit 1.25

-Appendix K 1.25 + 1.02

-Nominal 1.25 + 0.02 R-Factor [1 1]

Number of Fuel Rods per Bundle 74 PLHGR: Peak Linear Heat Generation Rate MAPLHGR: Maximum Average Planar Linear Heat Generation Rate MCPR: Minimum Critical Power Ratio 3

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION 5.0 RESULTS 5.1 LARGE RECIRCULATION LINE BREAKS The limiting large break LOCA event for ENRICO FERMI 2 is the maximum recirculation suction line break. Several large recirculation suction line breaks were analyzed for GEl 1 with Nominal and Appendix K assumptions to confirm the limiting break and single failure combination. [I

)) The results of these analyses are given in Table 3 and Figures 1 and 2. These results show that the limiting large break and single failure combination at EPU power level and 100% flow condition is the maximum recirculation suction line break with Division II Battery for both Nominal and Appendix K assumptions. ((

For the maximum recirculation suction line break with Division II Battery and nominal assumptions, there is a rapid vessel depressurization due to vessel inventory loss through the break (Figure lb). r[

The system response to a maximum recirculation suction line break with Division II Battery and Appendix K assumptions is similar to the case with nominal assumptions. There is a rapid vessel depressurization due to vessel inventory loss through the break (Figure 2b) but is slightly faster due to higher break flow from the Appendix K Moody Slip Flow Model. [f 4

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION

)) This process can be observed in the hot bundle water level (Figure 2a), the peak cladding temperature (Figure 2c) and the hot node heat transfer coefficients (Figure 2d).

Overall the bundle heatup for the Appendix K case is higher than the nominal case due to higher bundle power and decay heat.

5.2 SMALL RECIRCULATION LINE BREAKS The most limiting single failure for small recirculation line breaks at the EPU power level is the Division I Battery failure. The small break cases were reanalyzed for GE 11 with Nominal and Appendix K assumptions to determine the small break with the highest PCT. The results of these analyses are given in Table 4 and Figures 3 and 4. ((

5

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION 5.3 NON-RECIRCULATION LINE BREAKS The analysis in Reference 1 demonstrated that the non-recirculation line break cases are clearly non-limiting and therefore not re-analyzed for GE 11 transition. Note that the feedwater line break basis includes an assumption of operator action to depressurize the

'reactor during the Division I Battery failure scenario. This is necessary since HPCI may be lost through the break and therefore is unable to restore level or depressurize the reactor.

5.4 ALTERNATE OPERATING MODES The limiting large break, the maximum recirculation suction line break, was reanalyzed for the MELLLA, Feedwater Temperature Reduction (FWTR), Increased Core Flow (ICF), and Single-Loop Operation (SLO) operating modes.

The analysis for MELLLA condition was performed at 86.8% of EPU thermal power (3430 MWt) and 79.9% of rated flow. The MELLLA condition at EPU thermal power is not specifically analyzed since the core flow for this case is at 99% of rated core flow. This case is essentially covered by the rated flow case at EPU thermal power. ((

)) Therefore there is no 6

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION additional LHGR or MAPLHGR multiplier, beyond the ARTS thermal limit reductions at the SLO power/flow point, is required from an ECCS-LOCA analysis viewpoint.

5.5 Compliance Evaluations 5.5.1 Licensing Basis PCT Evaluation The Appendix K results confirm that the limiting break is the limiting small recirculation suction line (SBA). [I

)) The Licensing Basis PCT for ENRICO FERMI 2 is calculated for GEl 1 fuel based on the above Appendix K PCT and using the SAFER/GESTR-LOCA licensing methodology approved by NRC in Reference 5. ENRICO FERMI 2 unique variable uncertainties, including backflow leakage, ECCS signal, stored energy, gap pressure, and ADS time-delay, were evaluated specifically for GEl 1 fuel to determine plant-specific adders. The calculated licensing Basis PCT is 1830'F.

5.5.2 Removal of the Current Requirement for Evaluation of Upper Bound PCT The NRC SER approving the original SAFER/GESTR-LOCA application methodology (described in Reference 3) placed a restriction of 1600'F on the Upper Bound PCT calculation. Additional supporting information was needed to support the use of the methodology for Upper Bound PCTs in excess of this limit. GENE provided this information on a generic basis in Reference 4. GENE received a SER from the NRC (Reference 6) eliminating the 1600'F restriction on the Upper Bound PCT. The elimination of the restriction on the Upper Bound PCT is applicable to all plants using the SAFER/GESTR-LOCA application methodology described in Reference 3, including ENRICO FERMI 2. In addition, the 16007F restriction on the Upper Bound PCT is no longer applicable when evaluating the impact of changes and errors reported under the requirements of 10CFR50.46.

Plant-specific Upper Bound PCT Calculation The primary purpose of the Upper Bound PCT calculation is to demonstrate that the Licensing Basis PCT is sufficiently conservative by showing that the Licensing Basis PCT is higher than the Upper Bound PCT. The NRC SER approving the SAFER/GESTR-LOCA application methodology also required confirmation that the plant-specific operating parameters have been conservatively bounded by the models and inputs used in the generic calculations. The SER also required confirmation that the plant-specific ECCS configuration is consistent with the referenced plant class ECCS configuration for the purpose of applying the generic LTR Upper Bound PCT calculations to the plant-specific analysis. Because of the wide variation in plant specific operating parameters and ECCS performance parameters within the BWR product lines, it is difficult to judge whether an individual plant is bounded by the generic calculations. Therefore, the practice has been to calculate the Upper Bound PCT on a plant-specific basis rather than rely on the generic Upper Bound PCT calculations in order to demonstrate that the Licensing Basis PCT is sufficiently conservative.

7

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Reference 4 provided generic justification that the Licensing Basis PCT will be conservative with respect to the Upper Bound PCT and that the plant-specific Upper Bound PCT calculation was no longer necessary. The NRC SER in Reference 6 accepted this position by noting that since plant-specific Upper Bound PCT calculations have been performed for all plants, other means may be used to demonstrate compliance with the original SER limitations. These other means are acceptable provided there are no significant changes to the plant configuration that would invalidate the existing Upper Bound PCT calculations.

For the purposes of the Upper Bound PCT calculation, the plant configuration includes the plant equipment and equipment performance (e.g., ECCS pumps and flow rates), fuel type, and the plant operating conditions (e.g., core power and flow) that may affect the PCT calculation. In order to demonstrate continued compliance with the original SER limitations, the PCT impact due to the changes in the plant configuration must be reviewed in order to confirm that the conclusions based on the original Upper Bound PCT calculation have not been invalidated by the changes.

The results showed that the licensing basis PCT for the most limiting case is below the 10CFR50.46 limit of 2200'F and the licensing basis PCT bounds the corresponding Upper Bound PCT. Therefore, 10CFR50.46 acceptance criteria and the NRC SER requirements for SAFER/GESTR methodology are met for all the operating conditions.

As discussed above, the Upper Bound is no longer restricted by the 1600'F limit. Therefore, when evaluating the impact of changes and errors reported under the requirements of 10CFR50.46, the impact on the Upper Bound PCT no longer needs to be evaluated.

8

GE-NE-0000-0047-1716-Ri GEH PROPRIETARY INFORMATION Table 3 Summary of Large Recirculation Line Break Results 9

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Table 4 1 Summary of Small Recirculation Line Break Results( )

1]

10

GE-NE-OOOO-0047-l 716-Ri GEH NON-PROPRIETARY VERSION Table 5 SLO Analysis for GEl1 Fuel - Division II Battery Failure 11

• Considering the off-rated transient ARTS thermal limits as defined in Reference 7 the ECCS-LOCA SLO multiplier is 1.0.

• • A flow dependent LHGR and MAPLHGR multiplier

[LHGRFAC(f)/MAPFAC(f)] of 0.7616 is used for the SLO conditions.

Table 6 FWTR Analysis - Division II Battery Failure FFWTR: Final Feedwater Temperature Reduction Note: 100.0% EPU = 3952 MWt 100.0% F = 100 Mlbm/hr Nominal Dome Pressure = 1045 psia Appendix K Dome Pressure= 1060 psia 11

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION

6.0 CONCLUSION

S The analysis contained in this report demonstrates that for GE 11 fuel, the limiting break and single failure combination is the limiting small recirculation line suction break with Division I Battery failure for both Nominal and Appendix K assumptions.

Based on the limiting large and small breaks and applying the SAFERJGESTR ECCS-LOCA methodology, the ENRICO FERMI 2 ECCS-LOCA analysis was performed for the limiting LOCA event for GEl 1 fuel (( )) The results are summarized in Table 7. The analyses demonstrate that the Licensing Basis PCT corresponds to the limiting small recirculation suction line break. These results meet all licensing and SAFER/GESTR methodology analysis limits. ECCS-LOCA analysis results for all alternate modes (MELLLA, ICF, SLO and FWTR) also meet all licensing limits.

The thermal limits applied to the GE 11 fuel in the ECCS-LOCA evaluation are summarized in Table 8.

Reference 8 concluded that HPCI flow changes above 1135 psia did not impact the LOCA evaluation. The reasons for this are two-fold.

1. The limiting LOCA evaluation at the time did not credit HPCI flow and,

2. Reactor pressure is less than the 1135 psia threshold by the time HPCI initiates for the Appendix K analysis.

While the limiting small break is now an event that credits HPCI, and is the limiting LOCA event, there is still no impact because reactor pressure is sufficiently low at the time of HPCI initiation. However, the limiting small break with the Division I battery failure was analyzed with no HPCI flow above 1135 psia, consistent with the OPL-4 in Appendix A, so a change in HPCI flow above 1135 psia continues to have no effect on the LOCA evaluation.

12

GE-NE-0000-0047-1 716-RI GEH NON-PROPRIETARY VERSION Table 7 ECCS-LOCA Analysis Results for GEll Parameter Analysis Result A 10CFR50.46 tCriteri Acceptance Criteria

1. Licensing Basis PCT 1830°F < 2200 0F*

2. Maximum Local 2% < 17 %*

Oxidation

3. Core-Wide Metal-Water 0.1 % < 1.0 %*

Reaction

4. Coolable Geometry See results from Items 1 and 2 above Maintain coolable geometry, which is satisfied by meeting PCT

• 2200 'F and Maximum Local Oxidation < 17 %.

5. Core Long-Term Cooling Satisfied by either: core reflooded Core Temperature acceptably low above TAF or core reflooded to and long-term decay heat removed elevation of jet pump suction and one core spray system in operation

• 10 CFR 50.46 ECCS-LOCA Analysis Acceptance Criteria 13

GE-NE-OOOO-0047-171 6-Ri GEH NON-PROPRIETARY VERSION Table 8 Thermal Limits for GEll Fuel Parameter Analysis Value LHGR - Exposure Limit Curve GWD/MT kW/ft MAPLHGR - Exposure Limit Curve GWD/MT kW/ft 0.00 13.42 21.74 13.42 30.00 12.29 70.00 8.90 Worst Case Pellet Exposure for ECCS Evaluation H (MWd!MTU)

Initial Operating MCPR -LOCA Analysis Limit 1.25 R-Factor Off-Rated Thermal Limits 0 Core Flow, % of Rated Flow 48 E LHGRFAC(f) / MAPFAC(f) 0.7616 SLO Multiplier on LHGR 1.0

& MAPLHGR 14

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION

7.0 REFERENCES

1. NEDC-31982P, " Fermi-2 SAFER/GESTR-LOCA Loss-of-Coolant Accident Analysis,"

July 1991.

2. NEDC-32950P, "Compilation of Improvements to GENE's SAFER ECCS-LOCA Evaluation Model," January 2000.

3. NEDC-23785-1-PA, "The GESTR-LOCA and SAFER Models for the Evaluation of the Loss-of-Coolant Accident, Volume III, SAFER/GESTR Application Methodology,"

Revision 1, General Electric Company, October 1984.

4. NEDE-23785P-A, Vol. III, Supplement 1, Revision 1, "GESTR-LOCA and SAFER Models for Evaluation of Loss-of Coolant Accident Volume III, Supplement 1, Additional Information for Upper Bound PCT Calculation," March 2002.

5. Letter, C.O. Thomas (NRC) to J.F. Quirk (GE), Acceptance for Referencing of Licensing Topical Report NEDE-23785P, Revision 1, Volume III (P), "The GESTR-LOCA and SAFER Modelsfor the Evaluation of the Loss-of-CoolantAccident, " June 1, 1984.

6. Letter, S.A. Richards (NRC) to J.F. Klapproth (GENE), Review of NEDE-23785P, Vol.

III, Supplement 1, Revision 1, "GESTR-LOCA and SAFER Models for Evaluation of Loss-of Coolant Accident Volume III, Supplement 1, Additional Information for Upper Bound PCT Calculation," (TAC No. MB2774), February 1, 2002.

7. NEDC-31843P, "Maximum Extended Operating Domain Analysis for Detroit Edison Company Enrico Fermi Energy Center Unit 2," July 1990.

8. GHNE-0000-0075-7779-RO, "Enrico Fermi Energy Center Unit 2 Impact of Revised HPCI Discharge Head Capability on the ECCS-LOCA Evaluations," October 2007.

15

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Figure 1-a Water Level in Hot and Average Channels. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available) INominal Assumptions]

16

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Figure 1-b Reactor Vessel Pressure. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available) [Nominal Assumptions]

I]

17

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Figure 1-c Peak Cladding Temperature. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS

+ 4 ADS Available) [Nominal Assumptions]

((l 18

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Figure 1-d Heat Transfer Coefficients. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS +

4 ADS Available) [Nominal Assumptions]

19

GE-NE-0000-0047-1716-Ri GEHI NON-PROPRIETARY VERSION Figure 1-e ECCS Flows. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available) [Nominal Assumptions]

((I 20

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Figure 2-a Water Level in Hot and Average Channels. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS+ 4 ADS Available) [Appendix-K Assumptions]

[E 21

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Figure 2-b Reactor Vessel Pressure. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI +

1LPCS + 4 ADS Available) [Appendix-K Assumptions]

((I 22

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Figure 2-c Peak Cladding Temperature. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS

+ 4 ADS Available) [Appendix-K Assumptions]

23

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Figure 2-d Heat Transfer Coefficients. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS +

4 ADS Available) [Appendix-K Assumptions]

((l 24

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Figure 2-e ECCS Flows. Maximum Recirculation Line Suction Break, Division II Battery (2LPCI + 1LPCS + 4 ADS Available) [Appendix-K Assumptions]

((

25

GE-NE-OOOO-0047- 1716-Ri GEH NON-PROPRIETARY VERSION Figure 3-a Water Level in Hot and Average Channels. Limiting Small Recirculation Line Break (( ], Division I Battery (HPCI + 2LPCI + 1LPCS Available) [Nominal Assumptions]

[1 I

26

GE-N E-OOOO-0047- 1716-Ri GEH NON-PROPRIETARY VERSION Figure 3-b Reactor Vessel Pressure. Limiting Small Recirculation Line Break (( )), Division I Battery (HPCI +

2LPCI + 1LPCS Available) [Nominal Assumptions]

11 27 27

GE-NE-OOOO-0047- 1716-RI GEH NON-PROPRIETARY VERSION Figure 3-c Peak Cladding Temperature. Limiting Small Recirculation Line Break (( 1], Division I Battery (HPCI +

2LPCI + 1LPCS Available) [Nominal Assumptions]

[1 28

GE-N E-OOOO-0047- 1716-RI GEH NON-PROPRIETARY VERSION Figure 3-d Heat Transfer Coefficients. Limiting Small Recirculation Line Break (( ], Division I Battery (HPCI +

2LPCI + 1LPCS Available) [Nominal Assumptions]

11 1]

29

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Figure 3-e ECCS Flows. Limiting Small Recirculation Line Break (( )), Division I Battery (HPCI + 2LPCI +

1LPCS Available) [Nominal Assumptions]

11 30

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Figure 4-a Water Level in Hot and Average Channels. Limiting Small Recirculation Line Break ((

Division I Battery (HPCI + 2LPCI + 1LPCS Available) [Appendix K Assumptions]

((

31

GE-NE-0000-0047-1716-RI GEHI NON-PROPRIETARY VERSION Figure 4-b Reactor Vessel Pressure. Limiting Small Recirculation Line Break (( )), Division I Battery (HPCI +

2LPCI + 1LPCS Available) [Appendix K Assumptions]

((

32

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Figure 4-c Peak Cladding Temperature. Limiting Small Recirculation Line Break (( f], Division I Battery (HPCI +

2LPCI + 1LPCS Available) [Appendix K Assumptions]

11 33

GE-NE-OOOO-0047-171 6-Ri GEH NON-PROPRIETARY VERSION Figure 4-d Heat Transfer Coefficients. Limiting Small Recirculation Line Break (( )), Division I Battery (HPCI +

2LPCI + 1LPCS Available) [Appendix K Assumptions]

I4 34

GE-NE-OOOO-0047- 1716-Ri GEH NON-PROPRIETARY VERSION Figure 4-e ECCS Flows. Limiting Small Recirculation Line Break [ f], Division I Battery (HPCI + 2LPCI +

1LPCS Available) [Appendix K Assumptions]

11 35

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Appendix A Operating Plant Licensing Parameters (OPL-4/5)

The OPL-4/5 parameters shown in the "Resolved for Analysis" column are used for the ECCS-LOCA analysis. When the values are not shown, the inputs in the "Proposed by Customer" are used instead.

36

GE-NE-O000-0047-l 716-Ri GEH NON-PROPRIETARY VERSION neDRF 0000-0015-4730, neDRFSection 0000-0015- Responsible Report: OPL4/5 eDRF: 4734, Rev. 1 Engineer W.I. Roman Fermi-2 Extended Power Uprate/MELLLA + ECCS-LOCA Project: SAFER/GESTR (T0407) Plant: Fermi-2 Date: August 15, 2003 Page 3 Section 1 Plant Operational Parameters 4 Section 2 Emergency Diesel Generators 5 Section 3 Low Pressure Coolant Injection (LPCI) System 6 Section 4 Core Spray (CS)/Low Pressure Core Spray (LPCS) System 7 Section 5 High Pressure Core Spray (HPCS) System 8 Section 6 High Pressure Coolant Injection (HPCI) System 9 Section 7 Reactor Core Isolation Cooling (RCIC) System 10 Section 8 Isolation/Emergency Condensers (IC/EC) 11 Section 9 Automatic Depressurization System (ADS) 12 Section 10 In-Vessel Leakage Rates 13 Section 11 Miscellaneous Inputs 14 Section 12 Others 15 Section R1 GE References 16 Section N1 GE Notes 17 Section R2 Customer References 18 Section N2 Customer Notes 37

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407) 1 - Plant Operational Parameters Proposed Proposed GE by Cust. Resolved for Resol.

No. Parameter Units by GE GE Ref Notes Customer Cust. Ref. Notes Analysis Notes A. Operational Parameters-Rated Conditions [120% of OLTP (EPU)]

1Core thermal power- MWt 3952.0 Ref. 4 3952.0 1-2 3952.0 Nominal 2 Core thermal power- MWt or 102% of 4031.0 4031.0 1-2 4031.0 Appendix K nominal 3 Vessel steam dome psia 1045.0 Ref. 12 1045.0 1-2 1045.0 pressure-Nominal 4Wessel steam dome psia 1060.0 Ref. 13 1060.0 1-2 and pressure-Appendix K 1-4 5 essel steam output- Mlbm/hr Note (1) 1 17.204 1-2 Nominal 6Wessel steam output- Mlbm/hr Note (1) 1 17.621 1-2

-_ Appendix K 7Core flow Mlbm/hr 100.0 Ref. 12 100.0 100.0 GE Note 23 8 Recirculation drive flow- Mlbm/hr 16.500 Ref. 12 16.34 1-3 IC Loop A I 9Recirculation drive flow- Mlbm/hr 16.500 Ref. 12 16.34 1-3 1C Loop B 38

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-00 15-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407) 1- Plant Operational Parameters Proposed Proposed GE by Cust. Resolved for Resol.

No. Parameter Units by GE GE Ref Notes Customer Cust. Ref. Notes Analysis Notes 10 Feedwater temperature- OF Note (2) 2 428.2 1-2 Nominal 11 Feedwater temperature- OF Note (2) 2 430.2 1-4 Appendix K B. Alternate Operation Mode Parameters-

[MEOD/MELLLA] (EPU)

ICore thermal power- MWt 3952.0 Ref. 4 3952.0 1-2 3952.0 GE Note Nominal 23 2Core thermal power- MWt or 102% of 4031.0 4031.0 1-4 4031.0 Appendix K nominal 3 Vessel steam dome psia 1045.0 Ref. 12 1045.0 1-2 1045.0 GE Note pressure-Nominal 23 4essel steam dome psia 1060.0 Ref. 13 1060.0 1-2 and pressure-Appendix K 1-4 Wessel steam output- Mlbmlhr Note (1) 1 Value to be Nominal consistent with Task 100 heat balance model at this 39

GE-NE-O000-0047-1 716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407) 1 - Plant Operational Parameters Proposed Proposed GE by Cust. Resolved for Resol.

No. Parameter Units by GE GE Ref Notes Customer Cust. Ref. Notes Analysis Notes condition.

6essel steam output- Mlbm/hr Note (1) 1 =1.023*1.B.5 1-4 Appendix K 7Core flow (99.0% of 1.A.7) Mlbm/hr 99.0 Ref. 12 99.0 99.0 8 Recirculation drive flow- Mlbm/hr 16.335 16.18 Loop A (99.0% of 1.A.8) 9Recirculation drive flow- Mlbm/hr 16.335 16.18 Loop B (99.0% of 1.A.9) 10 Feedwater temperature- OF Note (2) 2 428.2 1-2 Nominal 11 Feedwater temperature- OF Note (2) 2 430.2 1-4 Appendix K C. iternate Operation Mode Parameters-FWHOOS/FFWTR] (EPU) 1Core thermal power- MWt 3952.0 Ref. 4 3952.0 1-2 3952.0 GE Note Nominal 23 40

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407) 1 - Plant Operational Parameters Proposed Proposed GE by Cust. Resolved for Resol.

No. Parameter Units by GE GE Ref Notes Customer Cust. Ref. Notes Analysis Notes 2Core thermal power- MWt or 102% of 4031.0 4031.0 1-4 4031.0 Appendix K nominal 3 Vessel steam dome psia 1045.0 Ref. 12 1045.0 1-2 1045.0 GE Note pressure-Nominal 23 Wessel steam dome psia 1060.0 Ref. 13 1060.0 1-2 and 1060.0 ressure-Appendix K 1-4 5 Vessel steam output- Mlbm/hr Note (1) 1 Value to be Nominal consistent with Task 100 heat balance model at this condition.

6Wessel steam output- Mlbm/hr Note (1) 1 =1.023"1.C.5 1-4

-_ Appendix K 7Core flow Mlbm/hr 100.0 Ref. 12 100.0 100.0 GE Note 23 8Recirculation drive flow- Mlbm/hr 16.500 Ref. 12 1.A.8 Loop A adjusted for reduced void fraction 41

GE-NE-0000-0047-1 716-Ri GEl- NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407) 1 - Plant Operational Parameters Proposed Proposed GE by Cust. Resolved for Resol.

No. Parameter Units by GE GE Ref Notes Customer Cust. Ref. Notes Analysis Notes 9 Recirculation drive flow- Mlbm/hr 16.500 Ref. 12 1.A.9 Loop B adjusted for reduced void fraction IOFeedwater temperature- OF Note (2) 2,15 378.2 Nominal (I.A. 10 - 5 0F) 11 eedwater temperature- OF Note (2) 2 380.2 1-4 Appendix K D. Alternate Operation Mode Parameters- [SLO] (EPU) 1 Core thermal power- MWt 2853.6 Ref. 7 3 2305 DTE Nominal (58.3% of I.A. 1) Note 1A 2Core thermal power- MWt or 102% of 2910.6 2351.1 DTE Appendix K SLO nominal Note 1A 3 Vessel steam dome psia 1045.0 Ref. 12 1045.0 1-2 1045.0 GE Note pressure-Nominal 23 4essel steam dome psia 1060.0 Ref. 13 1060.0 1-2 and 1060.0 pressure-Appendix K 1-4 42

GE-NE-O000-0047-1 716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407) 1 - Plant Operational Parameters Proposed Proposed GE by Cust. Resolved for Resol.

No. Parameter Units by GE GE Ref Notes Customer Cust. Ref. Notes Analysis Notes 5 Vessel steam output- Mlbrn/hr Note (1) 1 Value to be Nominal consistent with Task 100 heat balance model at this I_ _ Icondition.

6 Vessel steam output- Mlbm/hr Note (1) 1 =1.023*1.D.5 1-4

-_ Appendix K 7Core flow (48% of 1.A.7) Mlbm/hr 60.0 Ref. 7 3 DTE Note 1A 8Recirculation drive flow- Mlbm/hr 9.900 7.84 DTE Loop A (48.0% of 1.A.8) Note 1A 9Recirculation drive flow- Mlbml/hr 0 0 Definition 0 Loop B of SLO Mode 1 Feedwater temperature- OF Note (2) 2 Value to be Nominal consistent with Task 100 heat balance model at this condition.

43

GE-NE-O000-0047-171 6-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407) 1 - Plant Operational Parameters Proposed Proposed GE by Cust. Resolved for Resol.

No. Parameter Units by GE GE Ref Notes Customer Cust. Ref. Notes Analysis Notes 1 I Feedwater temperature- OF Note (2) 2 =1.D.10+2 1-4 Appendix K E. Alternate Operation Mode Parameters-[ICF] (EPU) 1Core thermal power- MWt 3952.0 Ref. 4 3952.0 1-2 3952.0 GE Note Nominal 23 2Core thermal power- MWt or 102% of 4031.0 4031.0 1-4 4031.0 GE Note Appendix K nominal 23 3 Vessel steam dome psia 1045.0 Ref. 12 1045.0 1-2 1045.0 GE Note pressure-Nominal 23 4 essel steam dome psia 1060.0 Ref. 13 1060.0 1-2 and 1060.0 GE Note pressure-Appendix K 1-4 23 5 Vessel steam output- Mlbm/hr Note (1) 1 Value to be Nominal consistent with Task 100 heat balance model at this condition.

6 Vessel steam output- Mlbm/hr Note (1) 1 =1.023*1.E.5 1-4

-_ Appendix K 44

GE-NE-0000-0047-1 716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407) 1 - Plant Operational Parameters Proposed Proposed GE by Cust. Resolved for Resol.

No. Parameter Units by GE GE Ref Notes Customer Cust. Ref. Notes Analysis Notes 7Core flow (105.0% of 1.A.7) Mlbm/hr 110.0 Ref. 2 105.0 DTE (A.f) Note1B 8 Recirculation drive flow- Mlbm/hr 18.150 17.160 DTE Loop A (105.0% of 1.A.8) NotelB 9Recirculation drive flow- Mlbm/hr 18.150 17.160 DTE Loop B (105.0% of 1.A.9) NotelB 10 Feedwater temperature- OF Note (2) 2 428.2 1-2 Nominal 11 Feedwater temperature- OF Note (2) 2 430.2 1-4 Appendix K 45

GE-NE-0000-0047- 1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

2. Emergency Diesel Generators (EDGs)

Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes A. Initiating signals 1Low water level 1 Ref. 2 See 1 DTE DTE 1 See (B.ld.ii) 11.B.6 Ref. 2-1 Note 2A 11.B.6

& Ref. 8 and OPL Level# 4A Note 11B 2 High drywell pressure Yes Ref. 2 Yes DTE Yes Yes/No (B.ld.i) Ref. 2-2

& Ref. 8 B. Delay time to process initiation seconds 1 Ref. 2 1 GE Ref. DTE 1 DTE signal (TspD on Fig. 1, 2) (B.1.g, 2 Note 3B Note 3B B.2.g)

C. Maximum delay time from EDG seconds 13 Ref. 2 25 - LPCI DTE 25 - LPCI DTE Ref start signal until bus is at rated (D.a) 25 - CS Ref. 2C 25 - CS 2C voltage (TDG on Fig. 1, 2) 46

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECGS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

3. Low Pressure Coolant Injection (LPCI) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes A. Initiating signals 1Low water level Level# 1 Ref. 2 See 1 DTE OPL 4A 1 See (B.ld.ii) 11.B.6 Ref. 2-1 Note 11.B.6

& Ref. 8 11B 2 High drywell pressure Yes/No Yes Ref. 2 Yes DTE Yes (B.ld.i) & Ref. 3-1 Ref. 8 3 Low vessel pressure permissive psig 350 Ref. 2 350 GE Ref. DTE 350 DTE (B.l.n) 2 Note 3B Note 3B 4 Timer delay for sustained low Customer to None DTE None water level (TSLL on Fig. 1) provide Ref. 3-9 B. Delay time to process initiation seconds 1 Ref. 2 1 GE Ref. 1 signal (TsPD on Fig. 1, 2) (B. 1.g) 2 C. Maximum vessel pressure at psid (vessel 295 Ref. 2 295 psig DTE 295 psi9 which pumps can inject flow to drywell) (B.1 .a) Ref. 3-2 (pressure associated with TCIPH on

-_ Fig. 1)

D. Minimum flow delivered to vessel 1Vessel pressure at which flow psid (vessel 20 Ref. 2 20 DTE 20 rates listed below are quoted to drywell) (B.1.b.i) Ref. 3-3 47

GE-NE-0000-0047- 1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR T0407)

3. Low Pressure Coolant Injection (LPCI) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 2or one LPCI pump injecting into gpm N/A N/A N/A one recirculation loop 3 or two LPCI pumps injecting gpm 22050 Ref. 2 4 22050 DTE 22050 GE Note nto one recirculation loop (B.l.b.ii) Ref. 3-3 4

& 3-4 4 or three LPCI pumps injecting gpm 26460 Ref. 2 5 26460 DTE 26460 GE Note into one recirculation loop (B.1.b.iii) Ref. 3-3 5

& 3-4 5 For four LPCI pumps injecting gpm 27625 Ref. 2 6 27625 DTE 27625 GE Note into one recirculation loop (B.l.b.iv) Ref. 3-3 5

& 3-4 6jOne LPCI pump into shroud gpm N/A N/A N/A E. Minimum flow at 0 psid (vessel-

_o-drywell) 1 For one LPCI pump injecting into gpm N/A N/A N/A one recirculation loop 2 or two LPCI pumps injecting gpm 22752 Ref. 2 22752 GE Ref. DTE 22752 DTE into one recirculation loop (B.l.c.i) 2 Note 3B Notes 3B

& 3D & 3D 3 For three LPCI pumps injecting gpm 27257 Ref. 2 27257 GE Ref. DTE 27257 DTE into one recirculation loop (B.1.c.ii) 2 Note 3B Notes 3B

& 3D & 3D 48

GE-NE-0000-0047- 1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + EGGS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

3. Low Pressure Coolant Injection (LPCI) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 4For four LPCI pumps injecting gpm 28444 Ref. 2 28444 GE Ref. DTE 28444 DTE into one recirculation loop (B.1.c.iii) 2 Note 3B Notes 3B I~& 3D &3D 5One LPCI pump into shroud gpm N/A N/A N/A F. Maximum delay time from bus at seconds 0 Ref. 2 0 GE Ref. 0 rated voltage until power available (B.1 .i) 2 for pump start. (TcIPA on Fig. 1)

G. Maximum delay time from pump seconds 5 Ref. 2 5 GE Ref. DTE 5 DTE start until pump is at rated (B.1.k) 2 Note 3B Note 3B speed (TcIPR on Fig. 1)

H. LPCI Injection Valves IMaximum delay time from bus at seconds 6 Ref. 2 6 GE Ref. DTE 6 DTE rated voltage until power available (B.1 .j) 2 Note 3B Note 3B at injection valve (Tclpv on Fig. 1) 2 ressure at which injection valve psig (vessel) 350 Ref. 2 350 GE Ref. DTE 350 DTE ay open (pressure permissive (B1.1.n) 2 Note 3B Note 3B ssociated with Tcpp on Fig. 1) 3 Maximum injection valve stroke seconds 30 Ref. 2 30 DTE DTE 30 DTE time - opening (TcIIv on Fig. 1) (B.1.I) Ref. 4-5 Note 3A Note 3B Recirculation discharge valves 49

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

3. Low Pressure Coolant Injection (LPCI) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 1 Maximum delay time from bus at seconds 6 Ref. 2 6 GE Ref. DTE 6 DTE rated voltage until power available (B.1.j) 2 Note 3B Note 3B at discharge valve (Tcipv on Fig.

2 Pressure at which discharge valve psig (vessel) Any Ref. 2 Any GE Ref. DTE Any DTE may close (pressure associated (B.1.s) 2 Note 3B Note 3B with Tctpp on Fig. 1) 3 Discharge valve stroke time - seconds 45 Ref. 2 45 DTE 45 closing (TDv on Fig. 1) (B.1.r) Ref. 3-6 4 Discharge bypass valve stroke seconds Customer to No Discharge DTE No Discharge time - closing (not shown on Fig. provide Bypass valve Ref. 3-7 Bypass valve Minimum flow bypass (MFB) valve 1 Normal position of MFB valve at Open/Closed Customer to Open DTE Open GE Note system startup provide Ref. 3-1 20

& 3-8 2 System flow at which MFB valve gpm Customer to 500 DTE 500 GE Note is signaled to close provide Ref. 3-1 20 3 MFB valve stroke time seconds Customer to 20 DTE DTE 20 GE Note provide Ref. 3-1 Note 3C 20 50

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

3. Low Pressure Coolant Injection (LPCI) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 4MFB flow rate gpm Customer to 481 (A/C), 480 DTE 481 (A/C), 480 GE Note provide (B/D) Ref. 3-1 (B/D) 20 K. Minimum detectable break size fo f 0.15 Ref. 2 0.15 GE Ref. DTE 0.15 G--Nete Loop Selection Logic (D.e) 2 Note 3B 20 51

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFERIGESTR (T0407)

4. Core Spray (CS)/Low Pressure Core Spray (LPCS) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes A. Initiating signals 1Low water level Level# 1 Ref. 2 See 1 DTE OPL 4A 1 See (B.2.d.ii) 11..B.6 Ref. 2-1 Note 11..B.6

& Ref. 8 11B 2 High drywell pressure Yes/No Yes Ref. 2 Yes DTE Yes (B.2.d.i) Ref. 4-1

& Ref. 8 3 Low vessel pressure permissive psig 350 Ref. 2 350 GE Ref. DTE 350

,_(B.2.n) 2 Note 3B 4Timer delay for sustained low water minutes Customer to None DTE DTE None DTE Note level (TSLL on Fig. 2) provide Ref. 4-1 Note 4C *4C

&4C B. Delay time to process initiation seconds 1 Ref. 2 1 GE Ref. DTE 1 DTE Note signal (TsPD on Fig. 2) (B.2.g) 2 Note 3B 4C C. Maximum vessel pressure at which psid (vessel 280 Ref. 2 280 DTE 280 pumps can inject flow (pressure to drywell) (B.2.a) Ref. 4-1 associated with TcsPH on Fig. 2)

D. Minimum flow delivered to vessel 1Vessel pressure at which flow rates psid (vessel 100 Ref. 2 100 DTE 100 listed below are quoted to drywell) (B.2.b.i) Ref. 4-2 52

GE-NE-0000-0047-1 716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

4. Core Spray (CS)/Low Pressure Core Spray (LPCS) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 2 Minimum flow at vessel pressure gpm 5625 Ref. 2 7 5625 GE Ref. DTE 5625 GE Note (B.2.b.ii) 2 Note 3B 7 and DTE Note 3B E. Minimum flow at 0 psid (vessel-to- gpm 7013 Ref. 2 7013 GE Ref. DTE 7013 DTE Note drywell) (B.2.c.i) 2 Note 4A 4A F. Maximum delay time from bus at seconds 6 Ref. 2 6 GE Ref. DTE 6 DTE Note rated voltage until power available (B.2.i) 2 Note 3B 3B for pump start. (TcsPA on Fig. 2)

G. Maximum delay time from pump seconds 5 Ref. 2 5 GE Ref. DTE 5 DTE Note start until pump is at rated (B.2.k) 2 Note 3B 3B speed (TcsPR on Fig. 2)

H. CS/LPCS Injection Valve(s) 1Maximum delay time from bus at seconds 6 Ref. 2 6 GE Ref. DTE 6 DTE Note rated voltage until power available (B.2.j) 2 Note 3B 3B at injection valve (Tcspv on Fig. 2) 2Pressure at which injection valve psig (vessel) 350 Ref. 2 350 GE Ref. DTE 350 DTE Note may open (pressure permissive (B.2.n) 2 Note 3B 3B associated with Tcspp on Fig. 2) 53

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

4. Core Spray (CS)/Low Pressure Core Spray (LPCS) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 3Maximum injection valve stroke seconds 15 Ref. 2 15 GE Ref. DTE 15 DTE Note time - opening (Tcsiv on Fig. 2) (B.2.1) 2 Note 3B 3B Minimum flow bypass (MFB) valve 1Normal position of MFB valve at Open/Closed Customer to Open DTE Open GE Note system startup provide Ref. 4-1 20 2 System flow at which MFB valve is gpm Customer to 320 DTE 320 GE Note signaled to close provide Ref. 4-1 20 3 MFB valve stroke time seconds Customer to 15 DTE DTE 15 GE Note provide Ref. 4-1 Note 4B 20 4MFB flow rate gpm Customer to N/A DTE DTE N/A GE Note provide Ref. 4-1 Note 4D 20 and DTE Note 4D 54

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

5. High Pressure Core Spray (HPCS) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes A. Initiating signals Not Applicable Not Applicable Not Applicable 1 Low water level Level# Not Applicable Not Applicable Not Applicable 2 High drywell pressure Yes/No Not Applicable Not Applicable Not Applicable B. Delay time to process initiation seconds Not Applicable N/A Not Applicable signal (TsPD)

C. Maximum vessel pressure at which psid (vessel Not Applicable Not Applicable Not Applicable pumps can inject flow (pressure to drywell) associated with TCSPH)

D. Minimum flow delivered to vessel 1Vessel pressure at which flow rates psid (vessel Not Applicable Not Applicable Not Applicable listed below are quoted to drywell) 2 Minimum flows at vessel pressure gpm Not Applicable Not Applicable Not Applicable E. Minimum flow at 0 psid (vessel-to- gpm Not Applicable Not Applicable Not Applicable source) 55

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

5. High Pressure Core Spray (HPCS) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes F M aximum delay time from bus at seconds Not Applicable Not Applicable Not Applicable rated voltage until power available for pump start. (TcsPA)

G. Maximum delay time from pump seconds Not Applicable Not Applicable Not Applicable start until pump is at rated speed (TcspR)

H. HPCS Injection Valve 1Maximum delay time from bus at seconds Not Applicable Not Applicable Not Applicable rated voltage until power available at injection valve (Tcspv) 2 Maximum injection valve stroke seconds Not Applicable Not Applicable Not Applicable time - opening (TcsIv on Fig. 2)

Minimum flow bypass (MFB) valve 1Normal position of MFB valve at Open/Closed Not Applicable Not Applicable Not Applicable system startup 2System flow at which MFB valve is gpm Not Applicable Not Applicable Not Applicable signaled to close 3MFB valve stroke time seconds Not Applicable Not Applicable Not Applicable 56

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

5. High Pressure Core Spray (HPCS) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 4MFB flow rate gpm Not Applicable Not Applicable Not Applicable 57

GE-NE-OOOO-0047- 1716-Ri VERSION GEHI NON-PROPRIETARY VERSION NON-PROPRIETARY GEH GE-NE-0000-0047-1716-RI Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

6. High Pressure Coolant Injection (HPCI) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE, GE Ref Notes Customer Ref. Notes Analysis Notes A. Initiating signals 1 Low water level Level# 2 Ref. 2 See 2 DTE 2 See (B.3.e.ii) 11.B.5 Ref. 2-1 11.B.5

& Ref. 8 2 High drywell pressure Yes/No Yes Ref. 2 Yes DTE Yes (B.3.e.i) Ref. 6-1

& Ref. 8 B. Delay time to process initiating seconds 1 Ref. 2 No value DTE DTE Note No value DTE signal (TsPD) (B.1.g, Ref. 6-2 6A Note 6A B.2.g)

C. Operating pressure range 1Maximum psia 1135.0 Ref. 2 1184 psia/ DTE Response 1135.0 GE Note (B.3.b.i) 1169 psig Ref. 6-3 in OPL4A 22 2Minimum psia 165.0 Ref. 2 165 psia/ 150 Response 165.0 (B.3.b.ii) psig in OPL4A D. Minimum flow over pressure range gpm 5000.0 Ref. 2 5000 5000.0 in Item C (B.3.a) 58

GE-NE-0000-0047- 1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

6. High Pressure Coolant Injection (HPCI) System Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes E. Maximum allowed delay time from seconds 60.0 Ref. 2 60 DTE DTE Note 60.0 DTE initiating signal to pump at rated (B.3.f) Ref. 6-2 6A Note 6A flow, injection valve wide open and bypass valve closed F. Steam flow over operating pressure iT-F-Nete range 64 1 Maximum lbm/hr 173500.0 Ref. 14 16 173500 Response 173500 GE Note in OPL4A 16 2 inimum lbm/hr 75000.0 Ref. 14 17 75000 Response 75000 GE Note in OPL4A 17 G. Maximum time delay from seconds Customer to 60 DTE DTE Note 60 DTE initiating signal to start of steam provide Ref. 6-2 6A Note 6A

-_supply valve opening H. Steam supply valve opening stroke seconds Customer to 60 DTE DTE Note 60 DTE time provide Ref. 6-2 6A Note 6A HPCI flow at minimum operating gpm Not Applicable N/A N/A pressure diverted to core spray (BWR 4 1/2 only) 59

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

7. Reactor Core Isolation Cooling (RCIC) System (Not needed in ECCS-LOCA Calculations)

Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes A. Initiating signals 1Low water level Level# 2 DTE Ref. 2 2-1 B. !Delaytime to process initiating seconds no value See Item no value See Item signal (TspD) G Below G Below C. Operating pressure range 1Maximum psia Response 1184 1184 psia/ in OPL4A 1169 psig 2 Minimum psia Response 77 77 psia/ in OPL4A 62 psig D. Minimum flow over pressure range gpm 600 DTE 600 DTE in Item C Note 7A Note 7A E. Maximum allowed delay time from seconds 50 Response 50 initiating signal to pump at rated in OPL4A flow, injection valve wide open and bypass valve closed F. Steam flow over operating pressure seconds DTE DTE range Note 6B Note 6B 1Maximum lbm/hr 27,800 lb/hr DTE Ref. DTE 27,800 DTE 7-1 Note 7B Note 7B 60

GE-NE-0000-0047-1 716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

7. Reactor Core Isolation Cooling (RCIC) System (Not needed in ECCS-LOCA Calculations)

Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 2 Minimum lbm/hr 9,300 DTE Ref. DTE 9,300 DTE 7-1 Note 7B Note 7B G. Maximum time delay from seconds 50 Response 50 initiating signal to start of steam in OPL4A supply valve opening H. Steam supply valve opening stroke seconds 45 DTE Ref. 45 time 7-2 61

GE-NE-O0O0-0047- 1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

8. Isolation/Emergency Condensers (IC/EC)

Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes A. Total number of condensers Not Applicable Not Applicable Not Applicable B. Initiating signals 1Low water level Level#

Not Applicable Not Applicable Not Applicable 2 High vessel pressure Yes/No Not Applicable Not Applicable Not Applicable 3 Bypass timer delay for sustained seconds low water level or sustained high vessel pressure Not Applicable Not Applicable Not Applicable C. Delay time to process initiation seconds signal Not Applicable Not Applicable Not Applicable D. Maximum time to process seconds initiation signal Not Applicable Not Applicable Not Applicable E. Maximuim operating pressure psig (vessel) Not Applicable Not Applicable Not Applicable F. Initial operating temperature on shell side of condenser OF Not Applicable Not Applicable Not Applicable G. Initial water mass on shell side of gallons condenser Not Applicable Not Applicable Not Applicable H. Surface heat transfer area of condenser ft 2 Not Applicable Not Applicable Not Applicable 62

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

8. Isolation/Emergency Condensers (IC/EC)

Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes Elevation difference between recirculation loop suction nozzle to IC condensate return line 1 connection. (BWR/2s only) ft Not Applicable Not Applicable Not Applicable inimum inner diameter of IC J. ýsteam line ft Not Applicable Not Applicable Not Applicable Minimum inner diameter of IC K. condensate return line ft Not Applicable Not Applicable Not Applicable Minimum inner diameter of L. Fecirculation suction line ft Not Applicable Not Applicable Not Applicable Elevation difference between condenser and main steam line M. nozzle ft Not Applicable Not Appiicable Not Applicable Elevation of condenser above recirculation loop connection (BWR/2s) or recirculation loop N. suction nozzle (BWR/3s) ft Not Applicable Not Applicable Not Applicable

0. Overall FL/D I Steam side Not Applicable Not Applicable Not Applicable 2Return side I Not Applicable _Not Applicable I Not Applicable_

63

GE-NE-0000-0047- 1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

8. Isolation/Emergency Condensers (IC/EC)

Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes Condenser heat transfer P. coefficients Btu/sec-ft2-iCi OF Not Applicable Not Applicable Not Applicable 2

Btulsec-ft -

2 C2 OF Not Applicable Not Applicable Not Applicable 3 C3 Not Applicable Not Applicable Not Applicable 64

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + Plant: Fermi-2 Date: August 15, 2003 ECCS-LOCA SAFER/GESTR (T0407)

9. Automatic Depressurization System (ADS)

Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes A. Initiating signals 1 Low water level Level# 1 Ref. .2 See 1 DTE Permissive 1 See (B.4.g.i.A) 11.B.6 Ref. 2-1 at L3 11.B.6

& Ref. 8 2 High vessel pressure Yes/No Yes Ref. 2 Yes DTE DTE Note Yes (B.4.g.i.B) Ref. 9-1 9C

& Ref. 8 3 High drywell pressure bypass minutes 8.0 Ref. 2 8.0 GE Ref. 8.0 timer delay for sustained low (B.4.g.ii.A) 2 &8 water level (TBT on Fig. 3) & Ref. 8 4 ECCS ready permissive Yes/No Yes Yes DTE Yes Ref. 9-1 B. Delay time to process initiating seconds 1 Ref. 2 1 GE Ref. DTE Note 1 DTE signal (TSPD on Fig. 3) (B.1.g, 2 3B Note 3B igna TSDB.2.g)

C. Total number of relief valves 5 Ref. 2 5 GE Ref. 5 with ADS function (B.4.a) 2 D. Total number of relief valves 4 Ref. 2 4 GE Ref. 4 with ADS function assumed in (B.4.d) 2 analysis 65

GE-NE-O000-0047-1 716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + Plant: Fermi-2 Date: August 15, 2003 ECCS-LOCA SAFER/GESTR (T0407)

9. Automatic Depressurization System (ADS)

Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes E. Pressure at which flow capacity psig 1090.0 Ref. 2 1190 GE Ref. 1190.0 GE Note listed below is quoted (vessel) (B.4.e) 2 21 F. Minimum flow rate for one valve lbm/hr 3.480E+06 Ref. 2 870,000 GE Ref. DTE Note 870,000 DTE open at above listed pressure (B.4.f) 2 9A Note 9A G. ADS timer delay from initiating seconds 120 Ref. 2 120 DTE 120 signal completed to the time (B.4.h) Ref. 9-1 valves are opened (TST on Fig. 3)

H. Valve pressure setpoints 1ADS close on vessel pressure psig <50.0 Ref. 10 <50.0 DTE DTE Note <50.0 DTE Ref. 9-2 9B Note 9B 2 ADS reopen on vessel pressure psig >100.0 Ref. 10 >100.0 DTE DTE Note >100.0 DTE Ref. 9-2 9B Note 9B 3 ADS reclose on vessel pressure psig <50.0 Ref. 10 <50.0 DTE DTE Note <50.0 DTE Ref. 9-2 9B Note 9B 66

GE-NE-0000-0047- 1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

10. In-Vessel Leakage Rates Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes A. LPCI leakage (principally around jet pump joints) 1Leakage flow gpm 0 3.D.3, 13 DTE 0 GE Note 3.D.4, Note 13-3.D.5 .10B 2Pressure at which leakage flow is psid 20 3.D.1 13 20 3.D.1 20 GE Note defined 13 B. CS leakage (principally through vent hole of T-joint) 1Leakage flow gpm 0 4.D.2 14 4.D.2 DTE 0 GE Note Note 14 10B 2 Pressure at which leakage flow is psid 100 4.D.1 14 100 4.D.1 100 GE Note defined (CS/LPCS) 14 3 Pressure at which leakage flow is psid Not Applicable Not Applicable Not Applicable defined (HPCS)

C. Leakage allowance for shroud cracks 1 Leakage flow gpm Not Applicable Not Applicable Not Applicable 67

GE-NE-O0O0-0047-1 716-Ri GEH-NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

10. In-Vessel Leakage Rates Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 2Core flow at which leakage flow is % of rated Not Applicable Not Applicable Not Applicable defined 3 Elevation of core shroud cracks inches Not Applicable Not Applicable Not Applicable AVZ D. Leakage allowance for access hole cover cracks 1ILeakage flow gpm Not Applicable Not Applicable Not Applicable 2 Core flow at which leakage flow is % of rated Not Applicable Not Applicable Not Applicable defined FE. Leakage allowance for LPCI-related cracks 1 Leakage flow gpm Not Applicable Not Applicable Not Applicable 2 Pressure at which leakage flow is psid Not Applicable Not Applicable Not Applicable defined F. Leakage allowance for CS header and riser cracks 1 Leakage flow gpm Not Applicable Not Applicable Not Applicable 68

GE-NE-0000-0047-1 716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

10. In-Vessel Leakage Rates Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 2Pressure at which leakage flow is psid Not Applicable Not Applicable Not Applicable defined

0. Leakage allowance for internal modifications and shroud repairs 1Leakage flow gpm Not Applicable Not Applicable Not Applicable 2 Core flow at which leakage flow is % of rated Not Applicable Not Applicable Not Applicable defined 3 Elevation of leakage path inches Not Applicable Not Applicable Not Applicable AVZ H. Leakage allowance for access hole cover repairs 1Leakage flow gpm Not Applicable Not Applicable Not Applicable 2Core flow at which leakage flow is % of rated Not Applicable Not Applicable Not Applicable defined Leakage allowance for LPCI-related repairs 1Leakage flow gpm Not Applicable Not Applicable Not Applicable 69

GE-NE-O000-O 047- 1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

10. In-Vessel Leakage Rates Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 2 Pressure at which leakage flow is psid Not Applicable Not Applicable Not Applicable defined J. Leakage allowance CS repairs 1 Leakage flow gpm Not Applicable Not Applicable Not Applicable 2 Pressure at which leakage flow is psid Not Applicable Not Applicable Not Applicable defined 70

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

11. Miscellaneous Inputs Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes A. Normal water level at rated power inches 563.5 Ref.2 563.5 DTE Ref. DTE 563.5 DTE (indicated level) AVZ (D.b) 2-1 Note Note 11A 11A B. Water level setpoints iLevel 8-High Level inches 585.31 Ref. 8 588.31 DTE 588.31 DTE AVZ Note Note 11B 11B Revised 2 Level 7-High Level Alarm inches Customer to N/A DTE N/A DTE (indicated level) AVZ provide Note Note 11B 11B 3 Level 4-Low Level Alarm inches Customer to N/A DTE N/A DTE (indicated level) AVZ provide Note Note 11B 11B 4 Level 3-Low Level (indicated inches 515 Ref. 2 515 DTE 515 DTE level) AVZ (D.c) Note Note 11L 11L 5 Level 2-Low Low Level inches 457.5 Ref. 2 457.5 DTE 457.5 DTE AVZ (D.d) Note Note 11B 11B 6 Level 1-Low Low Low Level inches 378.51 Ref. 8 9 DTE Note DTE 378.51 DTE AVZ 11B Note Note 11B 11B C. Steam dryer pressure drop psid Note (18) 18 Concur with GE Note 18 GE Note Note 18 18 71

GE-NE-0000-0047-1 716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

11. Miscellaneous Inputs Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes D. MSIV isolation-initiation signal 1 Low water level Level # 1 Ref. 8 1 DTE Ref. 1 2-1 2Low steam line pressure psig Customer to 736 psig DTE Ref. DTE 736 DTE provide 11-6 Note Note 11K 11K 3 High steam line flow  % of rated Customer to 140% DTE Ref. 140%

provide 11-5 E. MSIV signal delay (from initiating seconds 0.5 AG-0019, 0.5 DTE Ref. 0.5 event to start of valve motion) Sec. 6, 11-3 Item #

11.E F. MSIV closure time 1 Minimum closing time seconds 3 AG-0019, 3 DTE Ref. 3 Sec. 6, 11-3 Item #

11.F 2 aximum closing time seconds 10 Ref. 2 10 GE 10 II_(D.f) Ref.2 72

GE-NE-0000-0047- 1716-Ri GEH NON-PROPRIETARY VERSION

,Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

11. Miscellaneous Inputs Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes G. Feedwater pump coastdown (from seconds 5 AG-0019, 10 5 GE Note DTE 5 GE Note initial value to zero flow) Sec. 6, 10 Note 10 Item # 11J 11.G &

Ref. 9 H. Time constant for recirculation seconds 5 AG-0019, 11 5 DTE Ref. 5 GE Note pump coastdown Sec. 6, 11-4 11 Item #

11.H &

Ref. 9 Number of pilot-actuated Safety/Relief Valves (SRVs) in

-_group 1Group A 5 Ref.5 5 DTE 5 DTE (1.4) Note Note 11C 11C 2Group B 5 Ref.5 5 DTE 5 DTE (1.4) Note Note 11C 11C 3 Group C 5 Ref.5 5 DTE 5 DTE (1.4) Note Note 11C 11C 73

GE-NE-0000-0047-171 6-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

11. Miscellaneous Inputs Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes J. Opening/closing setpoints of pilot-actuated SRVs I Group A psig 1165/1087 Ref. 2 1135/1100.9 11-1 and (D.g) / 11-9 Ref. 11 2Group B psig 1175/1097 Ref. 2 1145/1110.7 11-1 and (D.g) / 11-9 Ref. 11 3Group C psig 1185/1107 Ref. 2 1155/1120.4 11-1 and (D.g) / 11-9 Ref. 11 K. Number of low-low set SRVs in Group 1 Group A 1 Ref. 5 1 DTE Ref. DTE 1 DTE (1.4) 11-1 Note Note 11F 11F 2 Group B 1 Ref. 5 1 DTE Ref. DTE 1 DTE (1.4) 11-1 Note Note 11F 11F 3 Group C Not Applicable Not Applicable Not Applicable L. Opening/closing pressure setpoints of low-low set SRVs 74

GE-NE-0000-0047-1 716-Ri GEl- NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

11. Miscellaneous Inputs Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes I Group A psig 1017/905 Ref. 2 1017/905 1017/905 (D.h) _ ._

2 Group B psig 1047/935 Ref. 2 1047/935 1047/935

._(D.h) 3 Group C psig M. Low-low set logic Yes Yes Yes N. Pilot-actuated SRV capacity 1 SRV capacity at (100+ACC)% of lbm/hr 870000 Ref. 5 870000 DTE Ref. 870000 popping pressure (1.4) 11-1 2 Popping pressure psig 1090 Ref. 5 1090 DTE Ref. 1090 (1.4) 11-1 3 Overpressure Accumulation Factor 3% Ref. 5 3 DTE Ref. 3 (ACC) (1.4) 11-1

0. Additional Pilot-actuated SRV opening/closing parameters 1Time delay before opening of seconds 0.4 Ref. 5 0.4 DTE Ref. 0.4 pilot-actuated SRVs (1.4A) & 11-1 Ref. 11.

2Time constant of SRV seconds Customer to 0.1 sec DTE Ref. DTE 0.1 .sec DTE opening/closing provide 11-7 Note Note 11M 11M 75

GE-NE-0000-0047-1 716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

11. Miscellaneous Inputs Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes P. Number of Spring Safety Valves (SSVs)

I Group A Not Applicable Not Applicable Not Applicable 2 Group B Not.Applicable Not Applicable Not Applicable 3 Group C Not Applicable Not Applicable Not Applicable 4 Group D Not Applicable Not Applicable Not Applicable Q. Opening/closing setpoint of SSVs 1Group A psig Not Applicable Not Applicable Not Applicable 2 Group B psig Not Applicable Not Applicable Not Applicable 3 Group C psig Not Applicable Not Applicable Not Applicable 4 Group D psig Not Applicable Not Applicable Not Applicable R. SSV capacity at opening setpoint 1Group A ibm/hr Not Applicable Not Applicable Not Applicable 2 Group B ibmr/hr Not Applicable Not Applicable Not Applicable 76

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS- Plant: Fermi-2 . Date: August 15, 2003 LOCA SAFER/GESTR (T0407)

11. Miscellaneous Inputs Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 3 Group C ibm/hr Not Applicable Not Applicable Not Applicable 4 Group D ibm/hr Not Applicable Not Applicable Not Applicable S. ECCS make-up water temperature OF 120.0 AG-0019, 12 120 DTE 120.0 GE Note Sec. 6, Note 12 and Item # 11G DTE 11.S & Note Ref. 9 11G T. Operator action time seconds Customer to 600 DTE Ref. 600 provide 11-2 U. High drywell pressure setpoint psig 2.0 Ref. 2 2 DTE 2.0 (B.1.i) Note 11E 77

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + Plant: Fermi-2 Date: August 15, 2003 ECCS-LOCA SAFER/GESTR (T0407) 12 - Others Proposed by GE Proposed by Cust. Cust. Resolved for Resol.

No. Parameter Units GE GE Ref Notes Customer Ref. Notes Analysis Notes 78

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA Plant: Fermi-2 Date: August 15, 2003

+ ECCS-LOCA SAFER/GESTR (T0407)

R1 - GE References No. Reference 1 Letter, CO.. Thomas (NRC) to J.F. Quirk (GE), "Acceptance for Referencing of Licensing Topical Report NEDE-23785, Revision 1, Volume III (P), The GESTR-LOCA and SAFER Models for the Evaluation of the Loss-of-Coolant Accident," June 1, 1984.

2 DC-6034, "Significant Input Parameter for SAFER/GESTR LOCA Analysis, OPL-4 Form," June 9, 2000.

3 NEDC-31982P, Fermi-2 SAFER/GESTR-LOCA Loss-of-CoolantAccident Analysis, July 1991 and E&A No. 1, April 1992.

4 Detroit Edison Fermi-2 Energy Center AEP Project-Specific Project Work Plan, April 2003 5 neDRF 0000-0008-5385, Fermi-2 Cycle 10 Reload Transient Analysis (neDRFSection 0000-0008-5390, Fermi-2 Cycle 10 OPL-3) 6 neDRF 0000-0013-6785, Fermi-2 EPU/MELLLA+ Power/Flow Map (T0201) (neDRFSection 0000-0013-6790, EPU-Draft Report) 7 neDRF J11-03346-09, FERMI 2 R6/C7 RELOAD LIC. - ECCS/LOCA (neFile J11-03346-09 SECTION 5 SH 0001) 8 neDrawing 22A2919AB, NUCLEAR BOILER SYSTEM DES, Rev. 13 9 neDRF 0000-0002-7678, TDP-0106, "SAFER/GESTR-LOCA ECCS ANALYSIS," Rev. 3, February 2003.

10 GENE Engineering Data Bank: BWREDB _PLANT:[KH1.SAFER04.PUP1]ADS.BDK 11 GENE Engineering Data Bank: BWREDBPLANT:[KH1 .SAFER04.PUP1]SAFER04.BDK 79

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA Plant: Fermi-2 Date: August 15, 2003

+ ECCS-LOCA SAFER/GESTR (T0407)

R1 - GE References 12 neDRF Section 0000-0015-3465, Rev. 1, Project Task Report, "DTE Energy Dermi-2 Energy Center Extended Power Uprate Task T100:

Reactor Heat Balance," GE-NE-0000-0015-3466-Ri, Rev. 1, July 2003 13 Fermi Tech Spec LCO 3.4.11 14 neDRF 0000-0014-0253, "Fermi 2 EPU/MELLLA+ HPCI System (T0404)," neDRF Section 0000-0014-0255. (Detroit Edison Drawing 6M721-5860, Rev. D, Process Diagram HPCI System.)

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GE-NE-0000-0047-11716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + Plant: Fermi-2 Date: August 15, 2003 ECCS-LOCA SAFER/GESTR (T0407)

N1 - GE Notes No. Note 1 Rated Nominal value to be consistent with Task 100 heat balance parameters at this condition. Appendix-K and off-rated power nominal cases calculated using Task 100 model at the case corresponding power and pressure.

2 Feedwater temperature to be determined consistent with the heat balance calculations at this condition.

3 The SLO power axis scaled based on EPU=100% rated power. The SLO core flow is 60% 48% of the rated core flow in Item 1.A.7 (Reference 7).

4 The 2 LPCI pump flow value selected for the analysis is conservative relative to the 2 LPCI pump specification of 25860 gpm. The analytical value includes a leakage flow reduction of 600 gpm and additional flow reduction for conservatism. (Reference 2) 5 The 3 LPCI pump flow value selected for the analysis is conservative relative to the 3 LPCI pump specification of 30000 gpm. The analytical value includes a leakage flow reduction of 600 gpm and additional flow reduction for conservatism. (Reference 2) 6 The 4 LPCI pump is assumed to deliver at least as much as 3 pumps. Therefore, the analytical value selected is conservative relative to the 3 LPCI pump flow obtained after subtracting 600 gpm assumed in LPCI leakages (I.e. 30000 - 600 = 29400). (Reference 2) 7 The core spray one loop flow value selected for the analysis is conservative relative to the one loop flow specification of 6350 gpm. The analytical value includes a leakage flow reduction of 100 gpm and additional flow reduction for conservatism. (Reference 2) 8 Per Reference 8, Level 8=219 in and reference instrument zero = 366.31 in. Therefore, 366.31 in + 219 in =585.31 in above vessel zero.

9 Per Reference 8, Level 1=12.2 in and reference instrument zero = 366.31 in. Therefore, 366.31 in + 12.2 in =378.51 in above vessel zero.

10 The feedwater pumps are assumed to trip at the beginning of the event. The feedwater pumps are conservatively assumed to linearly coast down from the initial value to zero in 5 seconds. The feedwater flow coastdown has little effect on the results for the limiting break because the feedwater is injected into the downcomer where it then flows out the break. The feedwater flow is stopped immediately (no coastdown) for a feedwater line break. (Reference 9, Sec. 5.1.3) 81

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + Plant: Fermi-2 Date: August 15, 2003 ECCS-LOCA SAFER/GESTR (T0407)

N1 - GE Notes 11 The reactor recirculation pumps are assumed to be tripped at the beginning of the event. This assumption results in a rapid decrease in the core flow and results in a conservatively early boiling transition time for the fuel. Unless otherwise specified by the customer, a time constant of 5 seconds is assumed for the pump coastdown in the Short-Term Thermal Hydraulic Model (LAMB) for BWR/4 plants.

(Reference 9, Sec. 5.1.3) 12 An ECCS water temperature of 120'F is used for all calculations. This assumption decouples the SAFER/GESTR-LOCA analysis from the containment response. (Reference 9, Sec. 5.1.3) 13 LPCI leakage included in LPCI flows in Items 3.D.3, 3.D.4 and 3.D.5. See also notes 4, 5 and 6. Therefore, no additional leakage will be assumed in the analysis 14 LPCS leakage included in LPCS flows in Item 4.D. See also note 7. Therefore, no additional leakage will be assumed in the analysis 15 A 100°F temperature reduction is assumed per Reference 5, Item 1.1.G 16 Steam flow from HPCI Process Diagram (Ref. 14), "Mode C", Point 9, RPV at high pressure and suppression pool at low pressure.

17 Steam flow from HPCI Process Diagram (Ref. 14), "Mode D", Point 9, RPV at low pressure and suppression pool at low pressure.

18 To be calculated in the analysis.

19 Deleted 20 In the ECCS LOCA analysis, the minimum flow bypass (MFB) valves are assumed to be closed at the time of ECCS injection and the ECCS injection valves fully open. Therefore, the ECCS LOCA analysis does not account for flow through the MFB valves.

21 DTE's proposed response is a typo. DTE's acknowledgement in the following note from P. Tutton (DTE) to W. Roman (GE) (email sent on 8/12/03): "The correct value for OPL4 Item 8.E. is 1090 PSIG, which Item B.4.b of GE Ref. 2, DTE Calculation DC-6-34."

22 The resolved value is consistent with the previous Fermi SAFER/GESTR-LOCA analysis and the previous OPL-4, items B.3.b.I (Reference 2). Per AG-001 9, App-20, it is more conservative to use a lower pressure for the "Maximum" pressure parameter in Item 6.c.1. Therefore, a 1135 Psia for the maximum pressure is conservative over the 1189 Psia proposed by DTE.

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GE-NE-OOO0-0047- 1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + Plant: Fermi-2 Date: August 15, 2003 ECCS-LOCA SAFER/GESTR (T0407) 83

GE-NE-0000-0047-1 716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS-LOCA Plant: Fermi-2 Date: August 15, 2003 SAFER/GESTR (T0407)

R2 - Customer References No. Reference 1-1 Fermi 2 DTR T0201 1-2 Fermi-2 FTR TO 100 1-3 Cycle 10 Startup Test 56.000.02, "Core Flow Calibration",

Attachment 4, performed 5/15/03, DTC:VSPERF, DSN:56.000.02.030515 1-4 GNF Technical Design Procedure TDP-0087 Appendix 50 2-1 DTE Drawing 6M721-5538, Rev. L, Nuclear Boiler System Instrument Information Table 2-2 Fermi 2 DBD R30-00 Rev. B, Emergency Diesel Generators, Section 2.0 2-3 Fermi 2 DBD R30-00 Rev. B, Emergency Diesel Generators, Section 4.1.2.2 & Tech Specs B 3.3.5.1 2-4 Fermi 2 Tech Specs B 3.3.5.1 2-5 GE-NE-B13-01920-12: The value for TDG should be 25 sec for CS and 20 sec for LPCI. The current SAFER/GESTR-LOCA analysis uses 25 sec for CS. However, for LPCI, the value of TDG was reduced from 25 sec to 20 sec because the recirc valve discharge valve stroke time was increased from 40 sec to 45 sec. The total response time for CS is 47 sec and for LPCI is 72 sec.

3-1 Fermi 2 DBD El 1-00 Rev. A RHR 3-2 T0310 DIR Item 4.1.3 3-3 DTE Drawings 6M721-5857, Rev. 0 Process Diagram RHR and 6M721-5690, Rev. E Process Schedules RHR 3-4 T0310 DIR Item 4.1.5 3-5 T0310 DIR Item 4.1.4 3-5 T0310 DIR Item 4.1.8 3-6 Fermi 2 DBD B31-00, Rev. A, Recirculation System 3-7 P&ID M-2833, Rev. AE Recirculation System 3-8 P&ID M-2083, Rev. BE RHR 84

GE-NE-O000-0047- 1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + ECCS-LOCA Plant: Fermi-2 DatEe: August 15, 2003 SAFER/GESTR (T0407)

R2 - Customer References 4-1 Fermi 2 DBD E21-00 Rev. A Core Spray 4-2 Fermi 2 Drawing M-5861, Rev. A Core Spray Process Diagram 4-3 Ferni 2 Drawing No. 61721-2210-01 Core Spray System Logic Diagram 6-1 Fermi 2 DBD E41-00 Rev. C HPCI 6-2 T0404 DIR Item 4.1.1 6-3 T0404 DIR Item 4.1.3 7-1 Fermi 2 Drawing 6M721-5859, Rev. D RCIC Process Diagram 7-2 Fermi 2 DBD E51-00 Rev. C RCIC Sec 4.2.3.21 9-1 Fermi 2 DBD B-21-04 Rev. B 9-2 GE Specification 22A2919AB Nuclear Boiler System Design Specification Data Sheet, paragraph 4.3.g 11-1 Fermi 2 calculation DC--5134 Rev. F, OPL 3 Cycle 10 11-2 Fermi 2 UFSAR 15.0.3.2.1 11-3 T0400 OPL 4A 11-4 Fermi 2 DBD B31-00, Rev. A 11-5 T0300 DIR 11-6 Fermi 2 Tech Specs 11-7 GE Specification22A2919AB Nuclear Boiler System Design Specification Data Sheet, paragraph 4.3.e 11-8 AG-0019, Sec. 6; Item # 11.S 11-9 .G-0019, Rev. 0 Page 36 issue resolved 85

GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + Plant: Fermi-2 Date: August 15, 2003 ECCS-LOCA SAFER/GESTR (T0407)

N2 - Customer Notes No. Note 1A NEDC-32313P, September 1994; The nominal core thermal power for SLO of 2470 mwth (62.5% of LPU) is not the correct initial power level to be assuming for the EPU SLO LOCA Analysis. 2470 mwth was a conservative initial condition assumption for the original Fermi2 SLO analysis transient analysis (MDE-56-0386), which has since been superseded by SLO analysis NEDC-32313P. Tech Spec 3.4.1 only allows SLO operation up to 67.2% of CLTP (2305 mwth). Therefore, the nominal core thermal power for EPU SLO should be 58.3% of LPU. Also, the 60% core flow assumption for SLO is incorrect. The single operating Recirc pump would have to operate at 100% speed to attain this core flow. The SLO analysis limits the speed of the single operating recirc pump to 75%, which translates to a core flow of approximately 48% of rated on the MELLL.

1B EPU is being licensed with a maximum core flow of 105% so analysis at 110% is not necessary.

1C Per Task T0307, Recirc Loop Flow at 100% core flow increases by 0.35 Mlb/hr from CLTP to LPU. Per T0307 Section 3.3.3 Item 1, the BILBO calculated difference in drive flow is used with current operational data to determine the drive flow requirements at LPU conditions. Per Reference 1-3, the Total Rated Drive Flow at the beginning of the current operating cycle was empirically determined to be 31.973 Mlb/hr, or 15.99 Mlb/hr per pump. 15.99+0.35=16.34 Mlb/hr.

2A OPL 4A Note 11 B discusses the use of specific instrument values.

2B Deleted 2C LPCI and CS EDG delay times adjusted to 25 seconds for each system. This will recover the 5 seconds reassigned from the EDH delay to recirc valve stroke for LPCI as documented in GE-NE-B13-01920-12. This wiill result in CS total delay time to be 47 seconds amd LPCI total delay time to be 77 seconds.

3A otal Response time = 30 sec, Maximum valve stroke time = 24 sec.

3B Per GE Ref. 2, this number is conservative engineering judgment not backed by specific data.

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GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + Plant: Fermi-2 Date: August 15, 2003 ECCS-LOCA SAFER/GESTR (T0407)

N2 - Customer Notes 3C. A specific stroke time is not required for this valve. The GE standard for a gate valve is 12"/minute which would correspond to 20 seconds for a 4 inch valve.

3D Per DTE Drawings 6M721-5857, Rev. 0 Process Diagram RHR and 6M721-5690, Rev. E Process Schedules RHR, Mode G gives a two pump accident flow of 26,000 gpm 4A Fermi 2 Drawing M-5861, Rev. A Core Spray Process Diagram gives a Mode "runout' condition which is cited in GE Ref. 2 and a Mode D "Accident System Injection at Rated Core Spray (long term). The Mode D gives a lower flow of 6350 gpm.

4B A specific stroke time is not required for this valve. The GE standard for a gate valve is 12"/minute which would correspond to 15 seconds for a 3 inch valve..

4C Per DTE Ref. 4-1 & 4-3 there is a 5 second delay in the start of the Core Spray Pumps to sequence power to the motors. This is not related to reactor pressure vessel level.

4D The Core Spray System minimum flow valves would be closed during normal high flow core spray injection and therefore would not affect the LOCA model.

6A Per DTE Ref. 6-1 the system response time is 60 seconds with a 5 second allowance for instrument uncertainty.

6B The word "seconds" is acknowledged as a typo and is removed, the issue is resolved.

7A Design flow rate.

7B The RCIC High and Low Steam Flow values taken from Fermi 2 drawing 6M721-5859, Rev. D, DTE Ref. 7-1. These values correspond to Modes A & B, which are for flow to the RPV with suction from the CST for high reactor pressure and low reactor pressure respectively. There is a lower steam flow of 8,400 lb/hr provided for Mode D, low reactor pressure injection from the suppression pool.

9A Per GE Ref. 2 - B.4.f, 3.48E6 is the value for four valves open, the value for one valve open is 870,000.

9B Alternate reference provided to DTE, see DTE Ref. 9-2. Issue resolved.

9C The GE requested parameter should read "High Drywell Pressure". The error was acknowledged and correction made.

10A AIl of the GE references on this sheet should be noted as Ref. 2 and then the subreference.

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GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION Report: OPL4/5 eDRF: neDRF 0000-0015-4730, RE: W.I. Roman neDRF Section 0000-0015-4734, Rev. 1 Project: Ferm-2 Extended Power Uprate/MELLLA + Plant: Fermi-2 Date: August 15, 2003 ECCS-LOCA SAFER/GESTR (T0407)

N2 - Customer Notes 10B The GE notes and references do not lead to the 0 leakage value. This issue is resolved by GE's revised notes 13 & 14.

11A Per Operating Procedure 23.107 the reactor water level is maintained between L4 (599:01 AVZ) and L7 (568.21 AVZ) The GE Proposed Value of 563.5 AVZ is approximately midway between these two points and is therefore acceptable.

11B This issue has been corrected, the following note is retained for record purposes. "The GE proposed values in 11 B are an inconsistent combination of Nominal Trip Set Points (NTSP), Allowable Values (AV) and Anayltical Limits (Alim). The heading of the section calls for "Set Points". The table below provided all of the values for levels 1 through 8 for GE's use. All values are above vessel zero (AVZ).

The Alim values come from GE Ref. 2 Sub reference 38 (22A2919AB). The NTSP Values come from Reference 2-1 and the AV values come from various Fermi 2 Instrument Calcs. It is essential that GE assure that the proper value and consistent values are used for this evaluation" NTSP AV Alim Level 8 580.31 585.31 588.31 Level 7 568.21 Levels 4 and 7 are nominal alarm set points which do not Level 4 559.01 land Alim valuesl Level 3 540.01 538.21 535.01 Level 2 477.41 470.11 457.51 Level 1 398.11 391.11 378.51 11C DTE has no access to Ref.. 5. Per OPL-3, there are 5 SRV's in each of the three subsets corresponding to opening pressures in 11 .J 1,2 &3 11D Ref. 11 has been provided to DTE by GE email on 7/29/03.

11E The GE references is incorrectly stated, it should be Ref. 2 B.1.d.l. [Corrected by GE. WIR-8/11/2003]

11 F Per DTE Ref. 11-1 there are a total of 2 SRV's with low-low set; it is assumed that this is one from each group as defined in the question.

11G Per Task T0400 OPL 4A the maximum suppression pool temperature is 95F. Per DTE Ref. 11-8 120F is used as a conservatism.

11H blank 11J Use value per GE note. GE note should say that the feedwater flows into the downcomer region, not the downcomers.

11K This value is the Allowable Value (AV) for CLTP 88

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N2 - Customer Notes 11L This value is the Allowable Limit (Alim) minus 20 inches for conservatism.

11 M Per GE guidance, this value correponds to the response time in DTE Ref. 11-7, 4.3.e, and has been used in previous analyses.

Issue resolved 89

GE-NE-0000-0047-1716-Ri GEH NON-PROPRIETARY VERSION SINGLE FAILURE EVALUATION FOR SAFER/GESTR ANALYSIS")

The table below shows the various combinations of Automatic Depressurization System (ADS), High Pressure Coolant Injection (HPCI) System, Core Spray (CS) System, and Low Pressure Coolant Injection (LPCI) System which might be operable in an assumed design basis accident situation. In performing the ECCS performance analysis with SAFER/GESTR, GE will assume that no postulated single active component will result in less than certain minimum combinations of systems remaining operable. The utility is requested to verify this assumption. The consequences of all possible single active electrical and mechanical failures an DC power source failures have been considered and have been found to have as a minimum one of the above combinations of systems remaining operable.

The following single, active failures will be considered in the ECCS performance evaluation:

Assumed Failure (1) Recirculation Line Break Systems Remaining(2)

Division I DC Power Source (Div I Battery) HPCI, 2 LPCI, 1 LPCS Division II DC Power Source (Div II Battery) 4 ADS, 2 LPCI, 1 LPCS (31)4)

LPCI Injection Valve 4 ADS, HPCI, 2 LPCS (3)

Diesel Generator (D/G) 4 ADS, HPCI, 2 LPCI, 1 LPCS (3)

HPCI 4 ADS, 4 LPCI, 2 LPCS (3)( 4)

One ADS Valve 4 ADS, 4 LPCI, HPCI, 2 LPCS Notes for OPL-5 (1) Other postulated failures are not specifically considered because they all result in at least as much ECCS capacity as one of the above assumed failures.

(2) Systems remaining, as identified in this table, are with the concurrent loss of off-site power and are applicable to all non-ECCS line breaks. For a LOCA from an ECCS line break, the systems remaining are those listed, less the ECCS system in which the break is assumed.

(3) The analysis conservatively assumes 4 ADS valves available.

(4) The HPCI failure small break analysis (SBA) case is analyzed with 4 ADS valves available, if SBA PCT > than DBA this case will be reported as a sensitivity study and a case with all ADS valves operable (5 ADS valves) will also be evaluated.

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GE-NE-0000-0047-1716-RI GEH NON-PROPRIETARY VERSION Legend:

ADS= Automatic Depressurization System LPCI = Low Pressure Coolant Injection System LPCS = Core Spray (CS)/Low Pressure Core Spray System HPCI = High Pressure Coolant Injection System 91