ML090710680

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Monticello, Enclosure 1 to L-MT-09-004, NSPM Response to Containment & Ventilation Branch RAI Number 1 Dated December 18, 2008, Cover Through Copy of MNGP Appr T0406 Data Transmittal Page 424 of 424
ML090710680
Person / Time
Site: Monticello Xcel Energy icon.png
Issue date: 02/17/2009
From:
Northern States Power Co, Xcel Energy
To:
Office of Nuclear Reactor Regulation
References
L-MT-09-004, TAC MD9990
Download: ML090710680 (677)


Text

ENCLOSURE I MONTICELLO NUCLEAR GENERATING PLANT NSPM Response To Containment

& Ventilation Branch RAI Number I dated December 18, 2008 Enclosure 1 NSPM Response To Containment

& Ventilation Branch RAI Number 1 NRC Information Request -(1)Containment analysis input parameters to perform the following: (a) Design-basis accident (DBA) LOCA short-term analysis (b) DBA LOCA long-term analysis (c) DBA LOCA net positive suction head (NPSH) analysis (d) Small steam line break accident analysis (e) Anticipated transient without scram (ATWS) NPSH analysis (f) Appendix R NPSH analysis (g) Station blackout NPSH analysis NSPM Response The requested information is provided in Attachment 1-1.

Attachment 1-1 Containment analysis input parameters to perform a. Design-basis accident (DBA) LOCA short-term analysis b. DBA LOCA long-term analysis c. DBA LOCA net positive suction head (NPSH) analysis d. Small steam line break accident analysis e. Anticipated transient without scram (ATWS) NPSH analysis f. Appendix R NPSH analysis g. Station blackout NPSH analysis Attachment 1-1a through d Containment analysis input parameters to perform Design-basis accident (DBA) LOCA short-term analysis DBA LOCA long-term analysis DBA LOCA net positive suction head (NPSH) analysis Small steam line break accident analysis Containment Analysis Input Parameters (Data from Form OPL-4A)Instructions for GE RE: Source Document: Project: Plant: RE: Date: Input Data in blue boxes below: GE-NE-0000-0060-9174-RI MNGP EPU Monticello Curt Robert April 19, 2007 Copy of MonticelloOPL-4A_

Data (2)Page 1 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri RE: Curt Robert Project: MNGP EPU Plant: Monticello Date: April 19, 2007 Section 1 Reactor Initial & Analytical Conditions 2 Decay Heat 3 Vessel Weights and Volumes4 LOCA 5 Containment Operating Conditions 6 Drywell 7 Vent System 8 Wetwell / Suppression Pool Geometry 9 SRV 10 High Pressure ECCS 11 Low Pressure ECCS 12 RHR 13 Feedwater System Mass and Energy 14 Others Copy of MonticelloOPL-4A_

Data (2)Page 2 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-R1 Curt Robert Project: MNGP EPU April 19, 2007 1 -Reactor Initial & Analytical Conditions Resolved for I No. Parameter Units Analysis a Initial Power (100% rated) MWt 2004 b Analysis Power for DBA MWt 2044 c 100% Rated Core Flow MIbm/hr 57.6 d Initial Dome Pressure at analysis power psia 1040.0 e Turbine steam flow rate at analysis power Mlbm/hr 8.531 f Feedwater flow rate at analysis power Mlbm/hr 8.504 g Vessel inlet feedwater temperature at analysis power OF 398.4 Copy of MonticelloOPL-4A_

Data (2)Page 3 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Project: MNGP EPU 2 -Decay Heat I Curt Robert April 19, 2007 Resolved for Analysis N I Jo. Parameter a Short-term Response 1 Fuel/ Decay Heat Model b Long-term Response 1 Fuel/ Decay Heat Model 2 Type of fuel 3 Fuel Bundle Average Enrichment 4 End-of-Cycle Core Average Exposure (Select one)a. By short ton b. By metric ton 5 Core Average Time at Power(Irradiation Time) 6 Cycle Duration Units ANS 5-1971 +20%ANS 5.1-1979+ 2 sigma GE14% 4.128 GWd/STU 31.0 GWd/MTU 34.14 years months 3.93 24 Copy of MonticelloOPL-4A_

Data (2)Page 4 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-R1 Curt Robert Project: MNGP EPU April 19, 2007 3 -Vessel Weights and Volumes I Resolved for No. Parameter I Units I Analysis a Total vessel free volume ft 3 12,153 b Vessel liquid volume 1 Subcooled 2 Saturated ft 3 ft 3 5,283 1,990 c Steam mass in main steam line to the first MSIV 1 One outer steam line 2 One inner steam line d Liquid mass in one recirculation loop e Liquid mass in connected piping to the first normally closed valve 1 LPCI piping 2 RHR shutdown piping 3 RCIC piping 4 LPCS/CS piping 5 HPCI/HPCS piping Ibm 404 Ibm 404 Ibm Ibm Ibm Ibm Ibm Ibm 28,028 11,693 218 87 1,175 576 Page 5 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-N E-0000-0060-9174-Ri Project: MNGP EPU 3 -Vessel Weights and No. Parameter I Curt Robert April 19, 2007 Volumes Resolved for Units Analysis I I I f Metal mass of RPV internals structure (excluding fuel and fuel assembly)g Metal mass of RPV, including top head but excluding vessel skirt.h Metal mass of RPV connected piping 1 Recirculation piping for all loops 2 RHR shutdown piping 3 LPCI piping 4 Main Steam Lines to second isolation valve 5 LPCS/CS lines to first normally closed valve 6 HPCI/HPCS lines to first normally closed valve 7 RCIC lines to first normally closed valve Number of fuel bundles j Mass of fuel (U02)k Mass of fuel assembly Ibm Ibm Ibm Ibm Ibm Ibm Ibm Ibm Ibm 436,500 859,868 259,316 1,095 32,946 102,602 4,624 12,798 2,855 484 Ibm 235,400 Ibm 106,480 Page 6 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Project: MNGP EPU Curt Robert April 19, 2007 4 -LOCA Resolved for No. Parameter Units Analysis a LOCA Break elevation (from bottom of vessel)1 Recirculation Suction Line 2 Steam Line b Time at which MSIVs start to close for DBA-LOCA 1 Recirculation Line Break 2 Main Steam Line Break c Time at which MSIVs are completely closed for DBA-LOCA ft ft 11.43 48.92 sec 0.5 sec 0.5 1 Recirculation Line Break 2 Main Steam Line Break sec sec 3.5 10.5 63.125 d Inside vessel height (from vessel zero to top of steam dome)e Long-term LOCA break area 1 Recirculation Line Break ft 2 Main Steam Line Break ft 2 4.095 Case ft2 Dependent Copy of MonticelloOPL-4A_

Data (2)Page 7 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Curt Robert Project: MNGP EPU April 19, 2007 4 -LOCA Resolved for No. Parameter Units Analysis f Recirculation line data for short-term containment analysis vessel model 1 Recirculation suction line inside diameter in 2 Nozzle safe end inside diameter or vessel nozzle inside diameter whichever is smaller in 3 RWCU inside diameter in 4 Jet pump nozzle inside diameter in 5 Number of jet pumps per loop 6 Number of nozzles per jet pump 7 Length of nozzle extending from vessel in g Main steam line data for short-term containment analysis vessel model 1 Steam line pipe inside diameter in 2 Nozzle safe end inside diameter or vessel nozzle inside diameter whichever is smaller in 3 Steam Line Flow Limiter diameter in 4 Length of nozzle extending from vessel in Copy of MonticelloOPL-4A_

Data (2)Page 8 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Proiect: MNGP EPU Curt Robert Aoril 19. 2007 5 -Containment Operating Conditions Resolved for No.PaameerUnits Analysis a Atmospheric pressure b Drywell-to-Wetwell operating pressure c Drywell pressure 1 Maximum 2 Minimum 3 Scram setpoint d Drywell temperature 1 Maximum 2 Minimum e Drywell relative humidity 1 Maximum Minimum 2 f Wetwell pressure 1 Maximum 2 Minimum g Wetwell temperature 1 Maximum2 Minimum h Wetwell relative humidity 1 Maximum 2 Minimum psia see note psid 0 psig 3 psig 0 psig 2.0 oF oF 135 N/A 100 20 psig 3 psig 0"F"F 90 77.5 100 Copy of MonticelloOPL-4A_

Data (2)Page 9 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-R1 Curt Robert Project: MNGP EPU April 19, 2007 5 -Containment Operating Conditions Reri sollvedi for No.Parmetr IUnits IAnalysis Suppression pool temperature 1 Maximum 2 Minimum TF 90°F 77.5 Note: Atmospheirc pressure is case dependent:

For NPSH cases use 14.26 psia; For peak containment pressure cases use 14.7 psia.Copy of MonticelloOPL-4A_

Data (2)Page 10 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Project: MNGP EPU Curt Robert April 19, 2007 6 -Drywell Resolved for No. Parameter Units Analysis a Total drywell free volume (including vent system)b Drywell holdup volume c Drywell pool surface area (in contact with drywell airspace)d Design Pressure (analytical limit)e Design Temperature f Pressure difference between wetwell and drywell for vacuum breakers to start to open g Pressure difference between wetwell and drywell for vacuum breakers to be fully open h Number of WW-DW vacuum breaker systems in use 1 Single Valve 2 Multiple Valve ft 3 ft 3 ft 2 134,200 8,781 1,344 psig 56 OF 281 psid psid 0.096 0 to 0.5 6 Copy of MonticelloOPL-4A_

Data (2)Page 11 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Proiect: MNGP EPU Curt Robert April 19, 2007 6 -0 DwellI I r e IResolved 7for No. IParameter Units Analysis i Total loss coefficient of each WW-DW vacuum breaker line (per system) including entrance and exit coefficients 1 Single Valve 2 Multiple Valve Total flow area of one VW-DW vacuum breaker line (per system)1 Single Valve2 Multiple Valve k Acceptable effective DW-to-WW bypass leakage area (A/'IK)Mark III only I Drywell inside diameter 3.804 ft 2 ft 2 ft 2 1.65 N/A ft Copy of MonticelloOPL-4A_

Data (2)Page 12 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Proiect: MNGP EPUCurt Robert Anril 19. 2007 7 -Vent System No.VeParametermResolved for No. Parameter Units Analysis Containment type (Mark 1, 11 or IlI)Mark I & II Parametersa Number of downcomers b Inside Diameter of each downcomer c Submergence of downcomers 1 High water level 2 Low water level d Loss coefficient for vent system (including entrance and exit losses)ft ft ft 96 1.96 3.58 3 Mark e f g h I only Number of main vents Number of vent header miter bends Main vent I.D.Vent header I.D.5.17 8 16 6.75 4.75 ft ft Copy of MonticelloOPL-4A_

Data (2)Page 13 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Proiect: MNGP EPU Curt Robert Aoril 19. 2007 I 7 -Vent System Resolved for No. Parameter Units Analysis Vent angles (NEDO-21888, Table 4.2-1)1 Angle of main vent with horizontal (01)2 Angle of first downcomer miter bend with horizontal (02)3 Angle of second downcomer miter bend with horizontal (03)4 Angle of main vent miter bend with horizontal (a)5 Vent header mitre bend or angle of bay centerline (90 0-j)Mark III only j Number of horiz. vents per row k Diameter of each horizontal vent Drywell weir annulus pool volume including horizontal vents 1 High water level 2 Low water level m Inside weir wall diameter n Outside weir wall diameter deg 20.13 deg deg deg deg 60 90 20.13 22.5 ft ft 3 ft 3 ft ft Copy of MonticelloOPL-4A_

Data (2)Page 14 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Curt Robert Project: MNGP EPU April 19, 2007 7 -Vent System I t UResolved for INo. IParameter IUnits IAnalysis o Weir annulus surface area ft 2 p Height of weir wall from suppression pool bottom ft q Length of each horizontal vent ft r Centerline elevation of top-row vents from p0ol bottom ft s Centerline elevation of mid-row vents from pool bottom ft Centerline elevation of bottom-row vents from pool bottom ft u Loss coefficient for vent system (including entrance and exit losses)Copy of MonticelloOPL-4A_

Data (2)Page 15 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-R1 Curt Robert Project: MNGP EPU April 19, 2007 8 1. Wetwell / Suppress ion Pool Resolved for No. P1arameter units IAnalysis a Total suppression pool volume 1 High water level 2 Low water level b Wetwell free airspace volume 1 High water level 2 Low water level c Suppression pool depth 1 High water level 2 Low water level d Suppression pool surface area (in contact with wetwell airspace) at NWL e Design Pressure (analytical limit)ft 3 ft 3 f 3 W 3 72,910 68,000 103,340 108,250 ft ft ft 2 8,429 psig 56 f Design Temperature OF 281 Copy of MonticelloOPL-4A_

Data (2)Page 16 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-R1 Project: MNGP EPU 1 8 -Wetwell I Suppression Pool No. IParameter I Units Curt Robert April 19, 2007 Resoved for Analysis RB-WW Vacuum Breakers g Pressure difference between reactor building and wetwell for vacuum breakers to be fully open h Total system flow loss coefficient per valve system (including entrance and exit coefficients)

Total flow area of one RB-VW vacuum breaker line (per valve system)Number of RB-WW vacuum breaker valve systems in use psid 0.5 3.32 ft 2 2.18 2 Mark I only k Torus major radius I Torus cross-sectional (minor)radius ft ft 49 13.83 Copy of MonticelloOPL-4A_

Data (2)Page 17 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Curt Robert Project: MNGP EPU April 19, 2007 8 -Wetwell / Suppression Pool I Resolved for No. 1Parameter Units Analysis Mark II only m Suppression pool volume inside the pedestal 1 High water level ft 3 2 Low water level ft 3 n Suppression pool diameter ft Mark III only o Containment (including wetwell) free airspace volume 1 High water level ft 3 2 Low water level ft 3 p Containment airspace inside diameter ft q Containment airspace outside diameter ft r HCU floor area ft 2 s HCU floor elevation from bottom of pool ft Copy of MonticelloOPL-4A_

Data (2)Page 18 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Proiect: MNGP EPU Curt Robert April 19, 2007 Su ppression Pool No. Parameter Unit Resolveda f No.Units IAnalysis Upper Pool (Mark III only)Initial water volume in upper pool available for dumping u Upper pool initial water temperature v Drywell pressure above which upper pool dump may be initiated w Vessel water level (above vessel zero, AVZ) below which upper pool dump may be initiated x Suppression pool level below which upper pool dump is not subject to time delay y Upper pool surface area z Upper pool dump flow rate aa Upper pool dump time delay after LOCA bb Upper pool maximum volume ft 3 OF psig ft ft ft 2 Ibm/sec sec ft 3 Copy of MonticelloOPL-4A_

Data (2)Page 19 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Curt Robert Project: MNGP EPU April 19, 2007 8 -Wetwell I Suppression Pool N Resolved fror INo. IP~aramneter Units Anallysis Containment Leakage cc Appendix J maximum allowable containment leakage for NPSH dd Appendix J test pressure ee Appendix J test temperature I I ,w%/day psig OF 1.2 42 68 Copy of MonticelloOPL-4A_ Data (2)Page 20 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Project: MNGP EPU Curt Robert April 19, 2007 9 -SRV Resolved for No. Parameter Units Analysis a Minimum number of SRV openings in normal set before SRVs switch to low-low set b Average throat area of SRVs c Suppression pool temperature above which vessel controlled cooldown is initiated (Tech Spec value)d Number of ADS valves e Maximum vessel controlled cooldown rate using SRVs f Average vertical elevation drop from SRV entrance at main steam line to SRV quenchers g SRV quenchers initial submergence at LWL h SRV rated flow at pressure 1. Rated flow 2. Pressure Number of SRVs available for manual pressure and temperature control 0 ft 2 120 2 100°F/hr ft ft 5.6 Ibm/hr 821,000 psig 1120 7 Copy of MonticelloOPL-4A_

Data (2)Page 21 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Project: MNGP EPU Curt Robert Aoril 19. 2007 9 -SRV Resolved for No. ýParamneter Units Analysis _Normal (relief) set mode (nominal)1 1 2 2 3 3 4 4 5 5 6 a. Number of valves Group 1 b. Opening setpoint Group 1 a. Number of valves Group 2 b. Opening setpoint Group 2 a. Number of valves Group 3 b. Opening setpoint Group 3 a. Number of valves Group 4 b. Opening setpoint Group 4 a. Number of valves Group 5 b. Opening setpoint Group 5 Difference between opening setpoint and reset pressure 8 psig 1109 psig psig psig psig psi k Low-low set mode 1 a. Number of valves Group 3 1 b. Opening setpoint Group 3 1 c. Closing setpoint Group 3 2 a. Number of valves Group 2 2 b. Opening setpoint Group 2 2 c. Closing setpoint Group 2 3 a. Number of valves Group 1 3 b. Opening setpoint Group 1 psig psig psig psig 30 1 1052 972 1 1062 982 1 psig 1072 Copy of MonticelloOPL-4A_

Data (2)Page 22 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Proiect: MNGP EPU Curt Robert April 19, 2007 9 -SRV I 9SResolved for No. Parameter Units Analysis 3 c. Closing setpoint Group 1 4 a. Number of valves Group 4 4 b. Opening setpoint Group 44 c. Closing setpoint Group 4 5 a. Number of valves Group 5 5 b. Opening setpoint Group 5 5 c. Closing setpoint Group 5 psig 992 psig psig psig psig Copy of MonticelloOPL-4A_

Data (2)Page 23 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Proiect: MNGP EPU Curt Robert Aoril 19, 2007 10 --igh Pressure ECCS Resolved for No. Parameter Units Analysis System Type (HPCI or HPCS)a Vessel water level (above vessel zero, AVZ) below which HPCI/HPCS is automatically actuated b Vessel water level (AVZ) above which HPCI/HPCS is automatically shut off c Maximum suppression pool liquid volume above which suppression pool replaces CST (if available) as water source for HPCI/HPCS d Drywell pressure for actuation of HPCI/HPCS (LOCA signal)e Maximum HPCI/HPCS delay time f Elevation of top of suction strainer from SIP bottom g If high drywell pressure and high vessel water level coexist, HPCI/HPCS will cycle between high and low levels in in 422.5 531.5 ft 3 psig sec 3.0 45 ft (Yes or No) YES Copy of MonticelloOPL-4A_

Data (2)Page 24 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Proiect: MNGP EPU Curt Robert April 19. 2007 10 -High Pressure ECCS Resolved for No. P1aramneter Units IAnalysis HPCI only h HPCI flow rate Maximum vessel pressure for HPCI operation Minimum vessel pressure for HPCI operation k Maximum S/P temperature for HPCI operation (operation limit)I HPCI turbine steam flow rates 1 a. RPV Pressure 1 b. HPCI steam flow rate 2 a. RPV Pressure 2 b. HPCI steam flow rate 3 a. RPV Pressure3 b. HPCI steam flow rate 4 a. RPV Pressure 4 b. HPCI steam flow rate HPCS only m HPCS pump heat n Runout flow o Shut-off head gpm 3,000 psig 1120 psig 150 OF 170 psig -14.7 Ibm/hr 0psig 150.3 Ibm/hr 26,700psig 1120.3 Ibm/hr 85,700 psig 1985.3 Ibm/hr 151,013 hp gpm psid Copy of MonticelloOPL-4A_

Data (2)Page 25 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Proiect: MNGP EPU Curt Robert Aoril 19. 2007 10 -High Pressure ECCS Resolved for No. Parameter Units Analysis RCIC parameters p Vessel water level (AVZ) below which RCIC is automatically actuated q Vessel water level (AVZ) above which RCIC is automatically shut off r Rated flow s Maximum time delay Maximum vessel pressure for RCIC operation u Minimum vessel pressure for RCIC operation v RCIC turbine steam flow rates 1 a. RPV Pressure 1 b. RCIC steam flow rate 2 a. RPV Pressure 2 b. RCIC steam flow rate 3 a. RPV Pressure 3 b. RCIC steam flow rate 4 a. RPV Pressure 4 b. RCIC steam flow rate in in gpm sec psig psig psig Ibm/hr psig Ibm/hr psig Ibm/hr psig Ibm/hr Copy of MonticelloOPL-4A_

Data (2)Page 26 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Curt Robert Project: MNGP EPU April 19, 2007 10 -High Pressure ECCS F I J0. Parameter w Maximum S/P temperature for RCIC operation T parameters x Available CST volume for vessel makeup y CST water temperature Resolved for Units Analysis OF Cs gal OF Copy of MonticelloOPL-4A_

Data (2)Page 27 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report- GE-N E-0000-0060-9174-RI Project: MNGP EPU Curt Robert ADril 19. 2007 1 -Low Pressure ECCS N ReUnits lesid for INo. IParameter Uis Analysis LPCI parameters a LPCI pump heat (per pump)hp b LPCI Shutoff head psid sec 600 300 53.2 c Maximum LPCI time delay d Drywell pressure above which LPCI will automatically be actuated (LOCA signal)e Vessel water level (AVZ) below which LPCI will automatically be actuated f Vessel water level (AVZ) above which LPCI will be shut off by operator g LPCI performance 1 Number of pumps per LPCI loop 2 LPCI runout flow for one pump in one loop.3 LPCI runout flow for two pumps in one loop.h Elevation of top of suction strainer from S/P bottom psig 3.0 in in gpm gpm 422.50 531.50 2 4,320 8,641 ft Copy of MonticelloOPL-4A_

Data (2)Page 28 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Project: MNGP EPU Curt Robert April 19, 2007 11 -Low Pressure ECCS N PResolved for INo. IParameter IUnits IAnalysis LPCS/CS parameters LPCS/CS pump heat (per pump)j LPCS/CS shutoff head k Total LPCS/CS time delay I Drywell pressure above which LPCS/CS will automatically be actuated (LOCA signal)m Vessel water level (AVZ) below which LPCS/CS will automatically be actuated n Vessel water level (AVZ) above which LPCS/CS will be shut off 0 LPCS performance 1 Number of pumps per LPCS loop 2 LPCS runout flow for one pump in one loop.3 LPCS runout flow for two pumps in one loop.p Elevation of top of suction strainer from S/P bottom hp 800 psid 300 sec 38.0 psig 3.0 in in 422.50 531.50 1 gpm 4,245 gpm ft Copy of MonticelloOPL-4A_

Data (2)Page 29 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Project: MNGP EPU Curt Robert April 19, 2007 I 12 -RHR Resolved for No. Parameter Units Analysis a Pool cooling mode 1 RHR flowrate per loop 2 Service water flowrate per loop 3 RHR heat exchanger K-value per loop 4 Number of RHR pumps per loop b Containment spray mode 1 RHR flowrate per loop a. Drywell b. Wetwell c. Total 2 Service water flowrate per loop 3 RHR heat exchanger K-value per loop 4 Number of RHR pump(s) per loop c LPCI cooling mode 1 RHR flowrate per loop 2 Service water flowrate per loop 3 RHR heat exchanger K-value per loop 4 Number of RHR pump(s) per loop 5 Pressure permissive for cooling gpm 4,000 gpm 3,500 Btu/sec-°F see note 1 gpm gpm gpm gpm 3,800 200 4,000 3,500 Btu/sec-°F 147 1 gpm 4,000 gpm 3,500 Btu/sec-0 F see note 1 psig Copy of MonticelloOPL-4A_

Data (2)Page 30 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Project: MNGP EPU Curt Robert April 19, 2007 12 -R-R Resolved for No. Parameter Units Analysis d Normal shutdown cooling mode 1 RHR flowrate per loop 2 Service water flowrate per loop 3 RHR heat exchanger K-value per loop 4 Number of RHR pump(s) per loop 5 Shutdown pressure permissive e Service water temperature f Average vertical distance between drywell spray nozzles and bottom of drywell g Average drywell spray droplet diameter h Average vertical distance between wetwell spray nozzles and suppression pool surface at LWL Average wetwell spray droplet diameter j RHR pump heat (per pump)k Maximum vessel cooldown rate with RHR gpm gpm Btu/sec-°F psig 94 ft ft ft ft hp 46.42 0.002 14 0.002 600°F/hr Copy of MonticelloOPL-4A_

Data (2)Page 31 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Curt Robert Project: MNGP EPU April 19, 2007 12 -RHR Resolved for No. Parameter Units Analysis I Drywell pressure above which drywell sprays can operate psig 0 m Wetwell pressure above which automatic wetwell spray can operate psig n Wetwell pressure below which wetwell spray will be turned off psig Note: For Pool and LPCI cooling modes: With RHRSW @ 90 deg. F, the 1 pump/1 pump "K" (K1) and the 2 pump/2 pump "K" (K2) vary as follows with RHR temperature:

K1 = 146.5 @ 110 deg, 147.6 @ 125 deg, 149.7 @ 160 deg & 151.6 @ 195 deg. K2 = 190.8 @ 110 deg, 194.5 @ 165 deg & 196.1 For Spray cooling mode: SHEX cannot model temperature dependent K-values for Spray Cooling therefore 147 will be assumed.Copy of MonticelloOPL-4A_

Data (2)Page 32 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-R1 Curt Robert Project: MNGP EPU April 19, 2007 13 -Feedwater System Mass and Energy No. Parameter I Units IReslved frAnalysis a Reference power b Node 1 -Vessel to closest FW heater 1 Fluid temperature 2 Fluid mass 3 Metal mass c Node 2 1 Fluid temperature 2 Fluid mass 3 Metal mass d Node 3 1 Fluid temperature 2 Fluid mass 3 Metal mass e Node 4 1 Fluid temperature 2 Fluid mass 3 Metal mass f Node 5 1 Fluid temperature 2 Fluid mass 3 Metal mass MWt 2006 OF 397.9 Ibm 70,306.1 Ibm 333,487.8 OF 332.1 Ibm 47,792.0 Ibm 217,839.4 OF 278.5 Ibm 23,642.7 Ibm 107,794.1 OF 210.9 Ibm 82,077.7 Ibm 164,983.6 OF Ibm Ibm Copy of MonticelloOPL-4A_

Data (2)Page 33 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)I Report: GE-NE-0000-0060-9174-Ri Project: MNGP EPU 13 -Feedwater System Mass No. Parameter Curt Robert April 19, 2007 and Energy Resolved for Units Analysis g Node 6 1 Fluid temperature 2 Fluid mass 3 Metal mass -h Node 7 1 Fluid temperature 2 Fluid mass 3 Metal mass Node 8 1 Fluid temperature 2 Fluid mass 3 Metal mass j Node 9 1 Fluid temperature 2 Fluid mass 3 Metal mass k Node 10 1 Fluid temperature 2 Fluid mass 3 Metal mass Node 11 1 Fluid temperature 2 Fluid mass 3 Metal mass OF Ibm Ibm OF Ibm Ibm OF Ibm Ibm OF Ibm Ibm OF Ibm Ibm OF Ibm Ibm Copy of MonticelloOPL-4A_

Data (2)Page 34 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Curt Robert Project: MNGP EPU April 19, 2007 13 -Feedwater System Mass and Energy Resolved for I No. Parameter Units IAnalysis m Node 12 1 Fluid temperature 2 Fluid mass 3 Metal mass n Node 13 1 Fluid temperature 2 Fluid mass 3 Metal mass o Node 14 1 Fluid temperature 2 Fluid mass 3 Metal mass OF Ibm Ibm OF Ibm Ibm OF Ibm Ibm Copy of MonticelloOPL-4A_

Data (2)Page 35 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Project: MNGP EPU Curt Robert April 19, 2007 14 -Others K No. Parameter a Control Rod Drive 1 CRD Flow Rate 2 CRD Flow Enthapy b Elevation from S/P bottom to top of RC1C suction strainer c Feedwater Coastdown (used in short-term DBA-LOCA only)1 Time 2 Percent Flow 3 Time 4 Percent Flow 5 Time 6 Percent Flow 7 Time 8 Percent Flow 9 Time Resolved for Units IAnalysis I Ibm/sec Btu/Ibm 0 0 ft seconds percent seconds percent seconds percent seconds percent seconds 0.0 100%5.0 0%Copy of MonticelloOPL-4A-Data (2)Page 36 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Project: MNGP EPU 14 -Ot No. Parameter 10 Percent Flow 11 Time 12 Percent Flow d Heat Sink Data 1 Drywell steel mass 2 Drywell steel SA 3 Drywell concrete mass 4 Drywell concrete SA 5 WW airspace steel mass 6 WW airspace steel SA 7 WW airspace concrete mass 8 WW airspace concrete SA 9 SP steel mass 10 SP steel SA 11 SP concrete mass 12 SP concrete SA Copy of MonticelloOPL-4A_

Data (2)Curt Robert April 19, 2007 hers I IResolved for Units Analysis percent seconds percent Ibm sqft Ibm sqft Ibm sqft Ibm sqft Ibm sqft Ibm sqft 587,263.0 26,058.0 291,095.0 13,380.0 319,287.0 13,380.0 Page 37 of 38 Containment Analysis Input Parameters (Data from Form OPL-4A)Report: GE-NE-0000-0060-9174-Ri Project: MNGP EPU Curt Robert April 19, 2007 14- Others Resolved for No. iParameter Units Analysis e RHR Hx Performance 1 Low RHR Temperature 2 High RHR Temperature 3 RHR Perf at Low RHR Temp 4 RHR Perf at High RHR Temp oF OF BTU/sec/°F BTU/sec/°F Copy of MonticelloOPL-4A_

Data (2)Page 38 of 38 Attachment 1-1e Containment analysis input parameters to perform Anticipated Transient Without Scram (ATWS) NPSH Analysis Copy of MNGPATWST0406_DataTransmittal.xls 2/11/2009 Page 1 of 17 0 3.0302734 6.3115234 9.4365234 12.561523 15.686523 18.811523 21.936523 25.061523 28.186523 31.311523 34.436523 37.561523 40.686523 43.811523 46.936523 50.061523 53.186523 56.311523 59.436523 62.561523 65.686523 68.811523 71.936523 75.061523 78.186523 81.311523 84.436523 87.561523 90.686523 93.811523 96.936523 100.06152 103.18652 106.31152 109.43652 112.56152 115.68652 118.81152 121.93652 125.06152 128.18652 131.31152 134.43652 137.56152 140.68652 143.81152 146.93652 150.06152 153.18652 1.43E+01 1.43E+01 1.43E+01 1.43E+01 1.43E+01 1.43E+01 1.43E+01 1.43E+01 1.43E+01 1.43E+01 1.43E+01 1.43E+01 1.44E+01 1.44E+01 1.44E+01 1.44E+01 1.44E+01 1.44E+01 1.44E+01 1.44E+01 1.44E+01 1.45E+01 1.45E+01 1.45E+01 1.45E+01 1.45E+01 1.45E+01 1.46E+01 1.46E+01 1.46E+01 1.46E+01 1.46E+01 1.46E+01 1.47E+01 1.47E+01 1.47E+01 1.47E+01 1.47E+01 1.47E+01 1.48E+01 1.48E+01 1.48E+01 1.48E+01 1.48E+01 1.48E+01 1.48E+01 1.49E+01 1.49E+01 1.49E+01 1.49E+01 9.OOE+01 9.09E+01 9.18E+01 9.27E+01 9.36E+01 9.45E+01 9.54E+01 9.63E+01 9.71E+01 9.80E+01 9.89E+01 9.98E+01 1.01 E+02 1.02E+02 1.02E+02 1.03E+02 1.04E+02 1.05E+02 1.06E+02 1.07E+02 1.08E+02 1.08E+02 1.09E+02 1.10E+02 1.11 E+02 1.12E+02 1.13E+02 1.13E+02 1.14E+02 1.15E+02 1.16E+02 1.17E+02 1.18E+02 1.19E+02 1.19E+02 1.20E+02 1.21 E+02 1.22E+02 1.23E+02 1.23E+02 1.24E+02 1.25E+02 1.25E+02 1.26E+02 1.26E+02 1.27E+02 1.28E+02 1.28E+02 1.29E+02 1.29E+02 6.80E+04 6.81 E+04 6.81 E+04 6.82E+04 6.82E+04 6.83E+04 6.84E+04 6.84E+04 6.85E+04 6.86E+04 6.86E+04 6.87E+04 6.88E+04 6.88E+04 6.89E+04 6.90E+04 6.90E+04 6.91 E+04 6.92E+04 6.92E+04 6.93E+04 6.94E+04 6.94E+04 6.95E+04 6.96E+04 6.96E+04 6.97E+04 6.98E+04 6.98E+04 6.99E+04 6.99E+04 7.OOE+04 7.01E+04 7.02E+04 7.02E+04 7.03E+04 7.04E+04 7.04E+04 7.05E+04 7.06E+04 7.06E+04 7.07E+04 7.07E+04 7.08E+04 7.08E+04 7.09E+04 7.09E+04 7.1OE+04 7.1OE+04 7.11 E+04 10.90 10.92 10.93 10.95 10.96 10.98 11.00 11.02 11.03 11.05 11.07 11.08 11.10 11.11 11.13 11.15 11.16 11.19 11.20 11.22 11.23 11.25 11.27 11.29 11.30 11.32 11.34 11.35 11.37 11.39 11.40 11.43 11.44 11.46 11.47 11.49 11.51 11.53 11.55 11.56 11.58 11.59 11.60 11.61 11.63 11.64 11.65 11.67 11.68 11.69 Sheet Name: PRFO Case 1 (Main Case)

Copy of MNGPATWST0406_DataTransmittal.xls 2/11/2009 Page 2 of 17 156.31152 159.43652 162.56152 165.68652 168.81152 171.93652 175.06152 178.18652 181.31152 184.43652 187.56152 190.68652 193.81152 196.93652 200.06152 203.18652 206.31152 209.43652 212.56152 215.68652 218.81152 221.93652 225.06152 228.18652 231.31152 234.43652 237.56152 240.68652 243.81152 246.93652 250.06152 253.18652 256.31152 259.43652 262.56152 265.68652 268.81152 271.93652 275.06152 278.18652 281.31152 284.43652 287.56152 290.68652 293.81152 296.93652 300.06152 303.18652 306.31152 309.43652 312.56152 315.68652 1.49E+01 1.49E+01 1.50E+01 1.50E+01 1.50E+01 1.50E+01 1.50E+01 1.50E+01 1.51 E+01 1.51E+01 1.51E+01 1.51E+01 1.51E+01 1.51E+01 1.52E+01 1.52E+01 1.52E+01 1.52E+01 1.52E+01 1.53E+01 1.53E+01 1.53E+01 1.53E+01 1.53E+01 1.53E+01 1.54E+01 1.54E+01 1.54E+01 1.54E+01 1.54E+01 1.55E+01 1.55E+01 1.55E+01 1.55E+01 1.55E+01 1.55E+01 1.55E+01 1.56E+01 1.56E+01 1.56E+01 1.56E+01 1.56E+01 1.56E+01 1.56E+01 1.57E+01 1.57E+01 1.57E+01 1.57E+01 1.57E+01 1.57E+01 1.57E+01 1.58E+01 1.30E+02 1.31 E+02 1.31E+02 1.32E+02 1.32E+02 1.33E+02 1.34E+02 1.34E+02 1.35E+02 1.35E+02 1.36E+02 1.37E+02 1.37E+02 1.38E+02 1.38E+02 1.39E+02 1.39E+02 1.40E+02 1.41 E+02 1.41 E+02 1.42E+02 1.42E+02 1.43E+02 1.44E+02 1.44E+02 1.45E+02 1.45E+02 1.46E+02 1.46E+02 1.47E+02 1.48E+02 1.48E+02 1.48E+02 1.48E+02 1.49E+02 1.49E+02 1.49E+02 1.50E+02 1.50E+02 1.50E+02 1.51 E+02 1.51E+02 1.51E+02 1.51E+02 1.52E+02 1.52E+02 1.52E+02 1.53E+02 1.53E+02 1.53E+02 1.53E+02 1.54E+02 7.11 E+04 7.12E+04 7.12E+04 7.13E+04 7.13E+04 7.14E+04 7.14E+04 7.15E+04 7.15E+04 7.16E+04 7.16E+04 7.17E+04 7.17E+04 7.18E+04 7.18E+04 7.19E+04 7.19E+04 7.20E+04 7.20E+04 7.21 E+04 7.21 E+04 7.22E+04 7.22E+04 7.23E+04 7.24E+04 7.24E+04 7.24E+04 7.25E+04 7.25E+04 7.26E+04 7.26E+04 7.27E+04 7.27E+04 7.27E+04 7.28E+04 7.28E+04 7.28E+04 7.29E+04 7.29E+04 7.29E+04 7.29E+04 7.30E+04 7.30E+04 7.30E+04 7.31 E+04 7.31 E+04 7.31 E+04 7.31 E+04 7.31 E+04 7.32E+04 7.32E+04 7.32E+04 11.71 11.72 11.73 11.74 11.76 11.77 11.78 11.80 11.81 11.82 11.84 11.85 11.86 11.88 11.89 11.90 11.92 11.93 11.94 11.95 11.97 11.98 11.99 12.01 12.03 12.04 12.05 12.06 12.08 12.09 12.10 12.11 12.12 12.13 12.13 12.14 12.15 12.16 12.16 12.17 12.17 12.17 12.18 12.18 12.18 12.18 12.19 12.19 12.19 12.19 12.20 12.20 Sheet Name: PRFO Case 1 (Main Case)

Copy of MNGPATWST0406_DataTransmittal.xls 2/11/2009 Page 3 of 17 318.81152 321.93652 325.06152 328.18652 331.31152 334.43652 337.56152 340.68652 343.81152 346.93652 350.06152 353.18652 356.31152 359.43652 362.56152 365.68652 368.81152 371.93652 375.06152 378.18652 381.31152 384.43652 387.56152 390.68652 393.81152 396.93652 400.06152 403.18652 406.31152 409.43652 412.56152 415.68652 418.81152 421.93652 425.06152 428.18652 431.31152 434.43652 437.56152 440.68652 443.81152 446.93652 450.06152 453.18652 456.31152 459.43652 462.56152 465.68652 468.81152 471.93652 475.06152 478.18652 1.58E+01 1.58E+01 1.58E+01 1.58E+01 1.58E+01 1.59E+01 1.59E+01 1.59E+01 1.59E+01 1.59E+01 1.59E+01 1.59E+01 1.60E+01 1.60E+01 1.60E+01 1.60E+01 1.60E+01 1.60E+01 1.61E+01 1.61 E+01 1.61 E+01 1.61 E+01 1.61 E+01 1.61 E+01 1.61E+01 1.62E+01 1.62E+01 1.62E+01 1.62E+01 1.62E+01 1.62E+01 1.62E+01 1.62E+01 1.63E+01 1.63E+01 1.63E+01 1.63E+01 1.63E+01 1.63E+01 1.63E+01 1.63E+01 1.64E+01 1.64E+01 1.64E+01 1.64E+01 1.64E+01 1.64E+01 1.64E+01 1.64E+01 1.65E+01 1.65E+01 1.65E+01 1.54E+02 1.54E+02 1.55E+02 1.55E+02 1.55E+02 1.56E+02 1.56E+02 1.56E+02 1.56E+02 1.57E+02 1.57E+02 1.57E+02 1.58E+02 1.58E+02 1.58E+02 1.58E+02 1.59E+02 1.59E+02 1.59E+02 1.60E+02 1.60E+02 1.60E+02 1.60E+02 1.60E+02 1.61 E+02 1.61 E+02 1.61 E+02 1.61 E+02 1.61 E+02 1.62E+02 1.62E+02 1.62E+02 1.62E+02 1.62E+02 1.63E+02 1.63E+02 1.63E+02 1.63E+02 1.63E+02 1.64E+02 1.64E+02 1.64E+02 1.64E+02 1.64E+02 1.65E+02 1.65E+02 1.65E+02 1.65E+02 1.65E+02 1.66E+02 1.66E+02 1.66E+02 7.33E+04 7.33E+04 7.33E+04 7.34E+04 7.34E+04 7.34E+04 7.34E+04 7.35E+04 7.35E+04 7.35E+04 7.35E+04 7.36E+04 7.36E+04 7.36E+04 7.37E+04 7.37E+04 7.37E+04 7.37E+04 7.38E+04 7.38E+04 7.38E+04 7.38E+04 7.39E+04 7.39E+04 7.39E+04 7.39E+04 7.39E+04 7.39E+04 7.40E+04 7.40E+04 7.40E+04 7.40E+04 7.40E+04 7.41 E+04 7.41 E+04 7.41 E+04 7.41 E+04 7.41 E+04 7.42E+04 7.42E+04 7.42E+04 7.42E+04 7.42E+04 7.43E+04 7.43E+04 7.43E+04 7.43E+04 7.43E+04 7.43E+04 7.44E+04 7.44E+04 7.44E+04 12.20 12.20 12.21 12.21 12.21 12.21 12.21 12.22 12.22 12.22 12.22 12.23 12.23 12.23 12.23 12.24 12.24 12.24 12.24 12.25 12.25 12.25 12.25 12.25 12.25 12.26 12.26 12.26 12.26 12.26 12.26 12.26 12.27 12.27 12.27 12.27 12.27 12.27 12.28 12.28 12.28 12.28 12.28 12.28 12.29 12.29 12.29 12.29 12.29 12.29 12.30 12.30 Sheet Name: PRFO Case 1 (Main Case)

Copy of MNGPATWST0406_DataTransmittal.xls 2/11/2009 Page 4 of 17 481.31152 484.43652 487.56152 490.68652 493.81152 496.93652 500.06152 503.18652 506.31152 509.43652 512.56152 515.68652 518.81152 521.93652 525.06152 528.18652 531.31152 534.43652 537.56152 540.68652 543.81152 546.93652 550.06152 553.18652 556.31152 559.43652 562.56152 565.68652 568.81152 571.93652 575.06152 578.18652 581.31152 584.43652 587.56152 590.68652 593.81152 596.93652 600.00684 635.99902 636.99902 636.59998 639.31873 642.44373 645.56873 648.31091 688.81873 734.63123 764.56873 788.00623 815.34998 845.91248 1.65E+01 1.65E+01 1.65E+01 1.65E+01 1.66E+01 1.66E+01 1.66E+01 1.66E+01 1.66E+01 1.66E+01 1.66E+01 1.66E+01 1.66E+01 1.67E+01 1.67E+01 1.67E+01 1.67E+01 1.67E+01 1.67E+01 1.67E+01 1.67E+01 1.67E+01 1.68E+01 1.68E+01 1.68E+01 1.68E+01 1.68E+01 1.68E+01 1.68E+01 1.68E+01 1.68E+01 1.68E+01 1.69E+01 1.69E+01 1.69E+01 1.69E+01 1.69E+01 1.69E+01 1.69E+01 1.70E+01 1.70E+01 1.70E+01 1.71 E+01 1.71 E+01 1.71E+01 1.71E+01 1.72E+01 1.72E+01 1.72E+01 1.72E+01 1.72E+01 1.72E+01 1.66E+02 1.66E+02 1.67E+02 1.67E+02 1.67E+02 1.67E+02 1.67E+02 1.68E+02 1.68E+02 1.68E+02 1.68E+02 1.68E+02 1.68E+02 1.69E+02 1.69E+02 1.69E+02 1.69E+02 1.69E+02 1.69E+02 1.69E+02 1.69E+02 1.70E+02 1.70E+02 1.70E+02 1.70E+02 1.70E+02 1.70E+02 1.70E+02 1.70E+02 1.70E+02 1.71E+02 1.71 E+02 1.71E+02 1.71 E+02 1.71 E+02 1.71 E+02 1.71 E+02 1.71E+02 1.72E+02 1.73E+02 1.73E+02 1.73E+02 1.73E+02 1.73E+02 1.73E+02 1.73E+02 1.73E+02 1.73E+02 1.73E+02 1.73E+02 1.73E+02 1.73E+02 7.44E+04 7.44E+04 7.45E+04 7.45E+04 7.45E+04 7.45E+04 7.45E+04 7.46E+04 7.46E+04 7.46E+04 7.46E+04 7.46E+04 7.47E+04 7.47E+04 7.47E+04 7.47E+04 7.47E+04 7.47E+04 7.47E+04 7.47E+04 7.47E+04 7.48E+04 7.48E+04 7.48E+04 7.48E+04 7.48E+04 7.48E+04 7.48E+04 7.48E+04 7.48E+04 7.49E+04 7.49E+04 7.49E+04 7.49E+04 7.49E+04 7.49E+04 7.49E+04 7.50E+04 7.50E+04 7.51 E+04 7.51 E+04 7.51 E+04 7.51 E+04 7.51 E+04 7.51 E+04 7.51 E+04 7.51 E+04 7.51 E+04 7.52E+04 7.52E+04 7.52E+04 7.52E+04 12.30 12.30 12.30 12.30 12.30 12.31 12.31 12.31 12.31 12.31 12.31 12.32 12.32 12.32 12.32 12.32 12.32 12.32 12.32 12.32 12.33 12.33 12.33 12.33 12.33 12.33 12.33 12.33 12.33 12.33 12.34 12.34 12.34 12.34 12.34 12.34 12.34 12.34 12.34 12.35 12.35 12.36 12.36 12.36 12.36 12.36 12.36 12.36 12.36 12.36 12.36 12.36 Sheet Name: PRFO Case 1 (Main Case)

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Copy of MNGPATWST0406_DataTransmittal.xls 2/109Pae6of8 2/11/2009 Page 26 of 88 7140.5376 7147.6626 7155.5376 7162.5376 7 169.2876 7176.7876 71 84. 1626 7192. 1626 7198.4751 7205.2251 7211.8501 72 18.2251 7225.2251 7231 .8501 7238.7251 7245.7876 7253.2251 7259.7876 7266.7251 7271.9126 7278.9751 7286.5376 7293.2876 7300.5376 7306.5376 7312. 9126 7319.8501 7325.8501 7332.2251 7338.7876 7346.0376 7352.6626 7359.2251 7366.9126 7373.5376 7380.1626 7386.4751 7393.6001 7400.4751 7406.8501 7413.9751 7421.8501 7428.8501 7435.3501 7442.4126 7448.7876 7455.6626 7462.2876 7469.5376 7477.0376 7483.5376 7490.6626 22.3 22.3 22.3 22.31 22.31 22.31 22.32 22.32 22.32 22.33 22.33 22.33 22.33 22.34 22.34 22.34 22.35 22.35 22.35 22.36 22.36 22.36 22.37 22.37 22.37 22.38 22.38 22.38 22.39 22.39 22.39 22.4 22.4 22.41 22.41 22.41 22.41 22.42 22.42 22.42 22.43 22.43 22.44 22.44 22.44 22.44 22.45 22.45 22.46 22.46 22.46 22.47 187.4 187.4 187.4 187.4 187.5 187.5 187.5 187.5 187.6 187.6 187.6 187.6 187.7 187.7 187.7 187.7 187.8 187.8 187.8 187.8 187.9 187.9 187.9 187.9 187.9 188 188 188 188 188 188.1 188.1 188.1 188.1 188.2 188.2 188.2 188.2 188.2 188.3 188.3 188.3 188.3 188.3 188.4 188.4 188.4 188.4 188.4 188.5 188.5 188.5 68938.917 68938.917 68955.471 68970.199 68975.166 68986.755 68975.166 68991.722 69001.656 69004.967 69006.623 69016.556 69008.278 69023,179 69026.49 69041.391 69044.702 69044.702 69057.947 69059.603 69057.947 69071.038 69085.941 69087.597 69084.285 69100.845 69 104.156 69107.468 69105.812 69124.027 69124.027 69124.027 69133.963 69142.242 69137.274 69150.522 69150.522 69158. 801 69170.392 69173.704 69175.36 69183.504 69200.066 69198.41 69205.035 69219.94 69219.94 69221.597 69223.253 69236.502 69246.439 69253.064 11.14 11.14 11.15 11.15 11.15*11.16 11.15 11.16 11.16 11.16 11.16 11.16 11.16 11.16 11.17 11.17 11.17 11.17 11.17 11.17 11.17 11.18 11.18 11.18 11.18 11.18 11.19 11.19 11.19 11.19 11.19 11.19 11.19 11.20 11.19 11.20 11.20 11.20 11.20 11.20 11.20 11.21 11.21 11.21 11.21 11.22 11.22 11.22 11.22 11.22 11.22 11.22 Sheet Name: PRFO Case 2 (Appendix B Case)

Copy of MNGPATWST0406_DataTransmittal.xls 2/109Pae7of8 2/11/2009 Page 27 of 88 7496.2876 7503.0376 7509.9126 7517.2876 7523.5376 7530.7876 7538.1001 7544.7251 7552.2251 7559.2251 7565.7251 7572.7876 7579.2251 7585.9126 7593.2876 7600.1626 7606.9126 7613.4126 7620.6626 7627.2251 7633.9126 7641.1626 7648.0376 7654.6001 7661 .475 1 7668.3501 7675.9751 7682.2876 7689.1626 7696.1626 7702.3501 7708.8501 7715.8501 7722.7251 7729.1626 7735.7876 7742.1626 7749.2251 7756.4751 7763.2251 7770.2876 7776.8501 7783.8501 7790.7251 7797.6001 7804.4751 7811.3501 7817.5376 7824.5376 7831.1626 7837.9126 7844.9126 22.47 22.47 22.47 22.48 22.48 22.48 22.49 22.49 22.5 22.5 22.5 22.51 22.51 22.51 22.51 22.52 22.52 22.52 22.53 22.53 22.53 22.54 22.54, 22.54 22.55 22.55 22.56 22.56 22.56 22.56 22.57 22.57 22.57 22.58 22.58 22.58 22.59 22.59 22.59 22.59 22.6 22.6 22.6 22.61 22.61 22.61 22.61 22.62 22.62 22.62 22.63 22.63 188.5 188.5 188.6 188.6 188.6 188.6 188.6 188.7 188.7 188.7 188.7 188.7 188.8 188.8 188.8 188.8 188.8 188.8 188.9 188.9 188.9 188.9 188.9 189 189 189 189 189 189 189.1 189.1 189.1 189.1 189.1 189.1 189.2 189.2 189.2 189.2 189.2 189.2 189.3 189.3 189.3 189.3 189.3 189.3 189.4 189.4 189.4 189.4 189.4 69254.72 69249.752 69256.376 69269.626 69266.313 69284.531 69282.875 69289.5 69301.093 69307.718 69306.062 69327.481 69334.106 69329.137 69332.45 69345.702 69352.327 69349.014 69362.266 69370.548 69368.892 69370.548 69380.487 69383.8 69385.456 69397.052 69400.364 69398.708 69411.96 69418.585 69431.837 69433.493 69438.463 69438.463 69448.402 69456.684 69461.564 69476.474 69484.758 69479.788 69484.758 69496.355 69501.325 69501.325 69502.982 69519.549 69516.236 69517.893 69534.46 69531.146 69531.146 69546.057 11.22 11.22 11.22 11.23 11.23 11.23 11.23 11.23 11.24 11.24 11.24 11.24 11.25 11.24 11.24 11.25 11.25 11.25 11.25 11.25 11.25 11.25 11.26 11.26 11.26 11.26 11.26 11.26 11.27 11.27 11.27 11.27 11.27 11.27 11.27 11.28 11.28 11.28 11.28 11.28 11.28 11.29 11.29 11.29 11.29 11.29 11.29 11.29 11.30 11.30 11.30 11.30 Sheet Name: PRFO Case 2 (Appendix B Case)

Copy of MNGPATWST0406_DataTransmittal.xfs 2/109Pae8of8 2/11/2009 Page 28 of 88 7851 .9751 7857.8501 7863. 850 1 7870.4751 7876.3501 7883.7251 7890.4751 7897.0376 7904.4126 7910.6001 7917.7251 7924.6626 7931.5376 7938.3501 7945.0376 7951.8501 7958.9751 7966.4751 7972.7876 7979.7876 7986.5376 7993.4126 8000.7251 8008.0376 8015.5376 8022.5376 8029.1626 8036.6626 8043.6626 8049.9751 8056.8501 8064.2251 8070.6001 8077.4126 8084.4126 8091.7876 8099.0376 8105.7876 8112.1626 8119.0376 8125.2251 8131 .7251 8137. 9126 8145.2876 8151 .7876 8159. 1626 8166.1626 8172.5376 8178.9126 8185.600 1 8192.3496 8199.2246 22.63 22.63 22.64*22.64 22.64 22.65 22.65 22.65 22.65 22.66 22.66 22.66 22.67 22.67 22.67 22.68 22.68 22.68 22.68 22.69 22.69 22.69 22.69 22.7 22.7 22.7 22.71 22.71 22.71 22.71 22.71 22.72 22.72 22.72 22.73 22.73 22.73 22.73 22.73 22.74 22.74 22.74 22.75 22.75 22.75 22.75 22.76 22.76 22.76 22.76 22.76 189.4 189.4 189.5 189.5 189.5 189.5 189.5 189.5 189.6 189.6 189.6 189.6 189.6 189.6 189.6 189.7 189.7 189.7 189.7 189.7 189.7 189.7 189.8 189.8 189.8 189.8 189.8 189.8 189.9 189.9 189.9 189.9 189.9 189.9 189.9 189.9 190 190 190 190 190 190 190 190.1 190.1 190.1 190.1 190.1 190.1 190.1 190.1 190.2 69546.057 69549.37 69552.684 69569.251 69564.281 69569.251 69582.505 69582.505 69585.818 69589.132 69600.729 69608.948 69613.919 69633.803 69628.832 69635.46 69635.46 69647.059 69660.315 69666.943 69663.629 69668.6 69681.856 69678.542 69683.513 69683.513 69695.112 69701.74 69703.39769711 .682 69714.996 69714.996 69728.252 69729.909 69736.537 69736.537 69748.136 69753.107 69753.107 69771.334 69771.334 69768.02 69794.498 69801.127 69799.47 69812.728 69812.728 69811.071 69814.385 69827.643 69825.986 69832.615 11.30 11.30 11.30 11.31 11.30 11.31 11.31 11.31 11.31 11.31 11.31 11.32 11.32 11.32 11.32 11.32 11.32 11.33 11.33 11.33 11.33 11.33 11.34 11.33 11.34 11.34 11.34 11.34 11.34 11.34 11.34 11.34 11.35 11.35 11.35 11.35 11.35 11.35 11.35 11.36 11.36 11.36 11.36 11.37 11.37 11.37 11.37 11.37 11.37 11.37 11.37 11.37 Sheet Name: PRFO Case 2 (Appendix B Case)

Copy of MNGPATWST0406_DataTransmittal.xls 2/109Pae9of8 2/11/2009 Page 29 of 88 8206.0996 8213.0996 8220. 8496 8227.4746 8234.2246 8240.4746 8247.5371 8254.5371 8262.0371 8268.5371 8275.4746 8282.4746 8289.4746 8296.412 1 8302.4746 8309.7246 8315.9746 8323.0996 8328.912 1 8336.0371 8341.9121 8348.9121 8355.5996 8362.2246 8369. 1621 8375.2246 8380.8496 8387.7871 8395.0371 8400.9746 8408.9746 8416.0996 8423.0996 8428.4746 8434.1621 8440.2871 8445.5371 8451 .2871 8456.4121 8461.4746 8467.8496 8474.5371 8481.2246 8486.2871 8493.3496 8499.0371 8505.0996 8512.4121 8519.8496 8526.2246 8532.7871 8539.0996 22.77 22.77 22.78 22.78 22.78 22.78 22.78 22.79 22.79 22.79 22.79 22.8 22.8 22.8 22.8 22.81 22.81 22.81 22.81 22.82 22.82 22.82 22.82 22.82 22.83 22.83 22.83 22.83 22.84 22.84 22.84 22.84 22.85 22.85 22.85 22.85 22.85 22.86 22.86 22.86 22.85 22.86 22.87 22.86 22.87 22.87 22.86 22.87 22.87 22.88 22.88 22.88 190.2 190.2 190.2 190.2 190.2 190.2 190.2 190.3 190.3 190.3 190.3 190.3 190.3 190.3 190.3 190.4 190.4 190.4 190.4 190.4 190.4 190.4 190.4 190.5 190.5 190.5 190.5 190.5 190.5 190.5 190.5 190.5 190.6 190.6 190.6 190.6 190.6 190.6 190.6 190.6 190.6 190.6 190.6 190.7 190.7 190.7 190.7 190.7 190.7 190.7 190.7 190.7 69834.272 69847.531 69852.502 69862.446 69867.418 69860.789 69867.418 69869.075 69883.991 69883.991 69900.563 69897.249 69902.221 69913.822 69918.794 69920.451 69920.451 69920.451 69937.024 69937.024 69946.967 69953.596 69951.939 69948.624 69976.794 69980.109 69990.055 69995.027 69983.424 70000 70000 70013.26 70018.233 70016.576 70028.178 70019.891 70033.151 70033.151 70031.493 70034.809 70039.781 70044.754 70049.727 70054.699 70069.617 70062.987 70074.59 70076.247 70092.823 70084.535 70097.795 70099.453 11.37 11.38 11.38 11.38 11.38 11.38 11.38 11.38 11.39 11.39 11.39 11.39 11.39 11.40 11.40 11.40 11.40 11.40 11.40 11.40 11.40 11.41 11.40 11.40 11.41 11.41 11.41 11.42 11.41 11.42 11.42 11.42 11.42 11.42 11.42 11.42 11.43 11.43 11.43 11.43 11.43 11.43 11.43 11.43 11.44 11.43 11.44 11.44 11.44 11.44 11.44 11.44 Sheet Name: PRFO Case 2 (Appendix B Case)

Copy of MNGPATWST0406_DataTransmittal.xls 2/109Pae3of8 2/11/2009 Page 30 of 88 8545.9746 8553.0996 8559.9121 8566.8496 8572.7246 8579.4121 8587.4746 8594.4746 8602.0996 8609.4121 8616.0371 8623.0371 8630.0371 8636.412 1 8643.6621 8648.9746 8655.9121 8663.2871 8669.5371 8676.7871 8683.4746 8691.0059 8695.9473 8701.6973 8707.2598 8713.3223 8719.0723 8725,8223 8731.6348 8737.6348 8743.5098 8749.0098 8755.1973 8761.1973 8767.3223 8772.8223 8777.6973 8781.8848 8786.3848 8790.7598 8795.5098 8800.1348 8804.6973 8809.6973 881 5.1348 8819.6348 8825.0098 8830.7598 8836.0723 8841.6348 8846.6348 8851.3848 22.88 22.89 22.89 22.89 22.89 22.9 22.9 22.9 22.91 22.91 22.91 22.91 22.92 22.92 22.92 22.92 22.92 22.93 22.93 22.93 22.93 22.93 22.92 22.91 22.9 22.89 22.88 22.86 22.85 22.84 22.83 22.82 22.81 22.8 22.78 22.77 22.76 22.76 22.75 22.74 22.73 22.72 22.72 22.71 22.7 22.69 22.68 22.67 22.66 22.65 22.64 22.63 190.7 190.8 190.8 190.8 190.8 190.8 190.8 190.8 190.8 190.8 190.9 190.9 190.9 190.9 190.9 190.9 190.9 190.9 190.9 190.9 190.9 191 190.9 190.9 190.8 190.7 190.7 190.6 190.6 190.5 190.4 190.4 190.3 190.3 190.2 190.2 190.1 190.1 190.1 190.1 190.1 190.1 190.1 190 190 189.9 189.9 189.8 189.8 189.7 189.7 189.6 70101.111 70101.111 70116.029 70112.713 70116.09 70127.631 70134.262 70134.262 70150.837 70147.522 70155.81 70164.097 70164.097 70172.385 70167.413 70195.623 70195.623 70200.597 70200.597 702 17. 175 70217.175 70215.517 70175.729 70104.426 70051.384 69991.712 69930.383 69862.423 69817.669 69746.395 69691.747 69625.456 69565.794 69507.789 69451.442 69396.752 69355.32 69317.203 69264.17 69224.395 69179.649 69143.189 69108.386 69033.969 68979.287 68944.49 68884.838 68828.5 68772.162 68722.452 68682.684 68631.317 11.44 11.44 11.45.11.45 11.45 11.45 11.45 11.45 11.46 11.46 11.46 11.46 11.46 11.46 11.46 11.47 11.47 11.47 11.47 11.47 11.47 11.47 11.46 11.44 11.43 11.42 11.40 11.38 11.37 11.35 11.34 11.32 11.31 11.29 11.28 11.26 11.25 11.24 11.23 11.22 11.21 11.20 11.19 11.17 11.15 11.14 11.13 11.11 11.10 11.09 11.08 11.06 Sheet Name: PRFO Case 2 (Appendix B Case)

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10.99 9731.1348 22.5 186.4 68368.36 11.0.0 9738.0723 22.5 186.3 68373.325 11.00 9744.5723 22.5 186.3 68370.015 11.00 9751.6348 22.5 186.3 68370.015 11.00 9759.0098 22.5 186.3 68371.67 11.00 9766.1973 22.49 186.3 68374.979 11.00 9772.9473 22.49 186.3 68388.218 11.00 9780.0723 22.49 186.3 68384.908 11.00 9786.7598 22.49 186.2 68393.182 11.00 9793.2598 22.49 186.2 68389.873 11.00 9799.9473 22.49 186.2 68384.908 11.00 9806.6973 22.49 186.2 68393.182 11.00 9813.0723 22.49 186.2 68388.218 11.00 9819.5098 22.49 186.2 68403.111 11.00 9826.0098 22.49 186.2 68408.075 11.01 9832.1348 22.48 186.1 68401.456 11.00 9839.8848 22.48 186.1 68403.111 11.00 9846.6348 22.48 186.1 68408.0751.0 9852.8848 22.48 186.1 68408.339 11.01 9858.9473 22.48 186.1 68398.412 11.00 9865.1973 22.48 186.1 68398.412 11.00 9872.2598 22.48 186.1 68413.302 11.01 9878.1973 22.48 186 68413.302 11.01 Sheet Name: PRFO Case 2 (Appendix B Case)

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69268.615 69275.219 69273.568 69275.219 69275.219 69286.776 69285.125 69291.729 69291.729 69291.729 69301.634 69303.285 69309.889 69301.634 69308.238 69308.238 69308.238 69318. 144 69321.446 69323.097 69326.399 69321.446 69318. 144 69314.955 11.22 11.21 11.22 11.21 11.22 11.22 11.22 11.22 11.22 11.22 11.22 11.22 11.22 11.22 11.22 11.22 11.22 11.22 11.22 11.23 11.23 11.22 11.22 11.23 11.23 11.23 11.23 11.23 11.23 11.23 11.23 11.23 11.23 11.23 11.23 11.23 11.23 11.23 11.24 11.24 11.24 11.24 11.24 11.24 11.24 11.24 11.24 11.24 11.24 11.24 11.24 11.24 Sheet Name: PRFO Case 2 (Appendix B Case)

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18.49 18.49 18.49 18.49 18.49 18.49 18.49 18.49 18.49 18.49 18.49 18.49 18.49 18.49 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 18.48 161.3 161.3 161.3 161.3 161.3 161.3 161.3 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.2 161.1 161.1 161.1 161.1 161.1.161.1 161.1 161.1 161.1 161.1 161.1 161.1 161.1 161.1 161.1 67988.519 67987.207 67988.519 168000 68002.952 68004.92 68003.772 68005.905 68005.248 68002.46 68004.428 68005.084 68019.19 68021.65 68022.306 68019.026 68021.322 68020.502 68022.47 68021.158 68035.099 68037.067 68039.856 68034.279 68036.739 68037.231 68038.052 68039.856 68055.273 68056.421 68054.617 68054.453 68058.225 68054.945 68053.633 68058.717 68058.881 68071.347 68075.119 68073.971 68075.119 68074.79 1 68071.675 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35305.449 3531 3.887 35321.574 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47 18.47.18.47 18.47 18.47 18.47 18.47 18.47 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.9 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 160.8 68203.509 68204.821 68204.821 68204.985 68203.673 68203.017 68206.133 68221 .712 68218.268 68220.728 68217.612 68221.876 68223.188 68234.503 68234.831 68236.635 68237.783 68240.243 68240.243 68240.571 68239.587 68240.079 68239.915 68257.297 68255.002 68251.558'68255.986 68251.23 68257.953 68258.281 68271.892 68269.433 68273.204 68272.384 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35991.574 35999.262 36000.012 18.3 18.3 18.3 18.29 18.29 18.29 18.29 18.29 18.29 18.29 18.29 18.28 18.28 18.28 18.28 18.28 18.28 18.28 18.28 18.27 18.27 18.27 18.27 18.27 18.27 18.27 18.26 18.26 18.26 18.26 18.26 18.26 18.26 18.25 18.25 18.25 18.25 18.25 18.25 159.5 159.4 159.4 159.3 159.3 159.3 159.2 159.2 159.2 159.1 159.1 159.1 159 159 159 158.9 158.9 158.8 158.8 158.8 158.7 158.7 158.7 158.6 158.6 158.6 158.5 158.5 158.5 158.4 158.4 158.4 158.3 158.3 158.3 158.2 158.2 158.2 158.2 66302.901 66290.936 66292.247 66303.885 66293.395 66291.755 66295.689 66296.673 66295.034 66297.164 66298.64 66295.853 66288.758 66288.922 66291.052 66287.938 66292.691 66292.199 66293.674 66278.433 66291.052 66279.744 66280.892 66293.183 66293.674 66282.366 66282.32 66271.67 66269.867 66269.048 66272.325 66276.094 66276.913 66271.834 66272.817 66273.964 66273.8 66278.552 66275.766 10.69 10.68 10.68 10.69 10.68 10.68 10.68 10.68 10.68 10.68 10.68 10.68 10.68 10.68 10.68 10.68 10.68 10.68 10.68 10.68 10.68 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14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 14.31 97.18 97.18 97.19 97.19 97.2 97.2 97.21 97.21 97.22 97.22 97.23 97.23 97.24 97.25 97.25 97.26 97.26 97.27 97.27 97.28 97.28 97.29 97.29 97.3 97.3 97.31 97.31 97.32 97.33 97.33 97.34 97.34 97.35 97.35 97.36 97.36 97.37 97.37 97.38 97.38 97.39 97.39 97.4 97.41 97.41 97.42 97.42 97.43 97.43 97.44 97.44 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 6.85E+04 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