Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ......

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Version 7.0 www.soapp.com 1.650.855.2666 [email protected] Project Input Flexible Inputs SOAPP–CT provides worksheets for you to specify your input for each of the four data sets that define a specific project and conceptual design. This worksheet format allows you to copy and paste inputs directly into SOAPP–CT from other sources, such as a spreadsheet you might set up to model some of your key assumptions. Fifteen input arrays allow you to specify your own models of critical project assumptions, such as the behavior of contract or market rates for fuel, en- ergy charges, capacity charges, etc. over time. You can choose to define these models with a full set of discrete values or simply specify a starting value and average escalation rate for any number of periods and SOAPP–CT will generate values that meet these specifications. SOAPP–CT will display plots to assist you in verifying the models you specify.

Transcript of Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ......

Page 1: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

Version 7.0

www.soapp.com

1.650.855.2666 [email protected]

Project Input

Flexible Inputs SOAPP–CT provides worksheets for you to specify your input for each of the four data sets that define a specific project and conceptual design. This worksheet format allows you to copy and paste inputs directly into SOAPP–CT from other sources, such as a spreadsheet you might set up to model some of your key assumptions. Fifteen input arrays allow you to specify your own models of critical project assumptions, such as the behavior of contract or market rates for fuel, en-ergy charges, capacity charges, etc. over time. You can choose to define these models with a full set of discrete values or simply specify a starting value and average escalation rate for any number of periods and SOAPP–CT will generate values that meet these specifications. SOAPP–CT will display plots to assist you in verifying the models you specify.

Page 2: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

Version 7.0

www.soapp.com

1.650.855.2666 [email protected]

Project Input — (continued)

Accurate Combustion Turbine Modeling Select one of the 100 combustion turbines modeled from data supplied to SOAPP’s specifications by manufacturers for specific turbines. Or, use SOAPP–CT’s Advanced Analysis feature to input the performance and emis-sions of any other combustion turbine you would like to evaluate.

Input Validation Input values are validated for internal consistency. Values that are not feasible in the context of other inputs are highlighted in red.

Multiple Choice Selections Simplified specification of project design.

View All Possible Inputs All possible inputs are always shown to speed consideration of options. Unneeded inputs are disabled (“grayed out”) consistent with current user inputs.

Project Validation Input values that cannot be validated out of the context of one or more of the other three data sets of project design criteria are shown in blue. These values are automatically validated before generating a plant design.

Intelligent Defaults Suggested input values are calculated based on current inputs.

Page 3: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStationConceptual Design Inputs SummaryProject: SOAPP-CT v7.0 Sample OutputsConceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Variable Value Units Min Default MaxUnit Data GE 7FA, CCCG, 3P@1800, Int DB

T=1350F, Multi Shaft, SCR, ACC

CT Model Number GE PG7241(FA)-60 Hz N/A N/A GE PG7241(FA)-60 Hz N/ANumber of CT's 1 N/A 1 2 4Cycle Type Combined Cycle Cogeneration N/A N/A Combined Cycle Cogeneration N/ADuty Cycle/Mission Base Load N/A N/A Base Load N/AType of Analysis Periodic N/A N/A Annual N/ANumber of Periods 4 N/A 1 1 12Period Duration - - - hours 0 0 8760CT NOx Control, Natural Gas Dry Low NOx Combustors N/A N/A Dry Low NOx Combustors N/ACT NOx Control, No 2 Fuel Oil Water Injection N/A N/A Water Injection N/ACT Natural Gas NOx Limit 9 ppmvd @ 15% O2 9 9 75CT No 2 Fuel Oil NOx Limit 42 ppmvd @ 15% O2 42 42 375CEM's Included Yes N/A N/A Yes N/AInlet Air Filtration Pulse Type N/A N/A Pulse Type N/AInlet Air Cooling Evaporative Coolers N/A N/A No Cooling N/AInlet Air Cooler Status - - - N/A N/A In Use N/AAir Cooling Discharge Temp - - - FEvaporative Cooler Effectiveness - - - % 0 85 100CT Pressure Loss Method Workstation Calculated N/A N/A Workstation Calculated N/ACT Inlet Pressure Loss 3.75 in H2OCT Exhaust Pressure Loss 14.00 in H2OHeater Selection Condensate Heater N/A N/A Condensate Heater N/ADeaerator Selection Integral Deaerator N/A N/A Integral Deaerator N/ANumber of Pressure Levels Three Pressure N/A N/A Three Pressure N/AHRSG Circulation Natural Circulation N/A N/A Natural Circulation N/AHP Steam Pressure 1800 psia 320 1465 2415IP Steam Pressure 490 psia 170 440 1650LP Steam Pressure 100 psia 20 75 200Hot Reheat Pressure Calc Method Workstation Calculated N/A N/A Workstation Calculated N/AHot Reheat Pressure 366.3 psiaHP Steam Temp 1000 F 628 1000 1050IP Steam Temp 526 F 475 525 642LP Steam Temp 338 F 338 460 642HP Pinch Point 15 F 9 15 400IP Pinch Point 15 F 9 15 400LP Pinch Point 30 F 9 15 400

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SOAPP-CT WorkStationConceptual Design Inputs SummaryProject: SOAPP-CT v7.0 Sample OutputsConceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Variable Value Units Min Default MaxHP Evap Approach 20 F 9 20 120IP Evap Approach 20 F 9 20 120LP Evap Approach 30 F 9 20 120HP Export Flow 0 lb/h 0 0 711790HP Export Process Return Percentage 0.0 %HP Export Process Return Temperature 80 FIP Export Flow 0 lb/h 0 0 43956IP Export Process Return Percentage 0.0 %IP Export Process Return Temperature 80 FLP Export Flow 0 lb/h 0 0 0LP Export Process Return Percentage 50.0 %LP Export Process Return Temperature 80 F 60 80 350Export All Available Flow No N/A N/A No N/ASpecify HRSG HP Steam Production? No N/A N/A No N/AUser Specified HRSG HP Steam Flow Goal 406000 lb/hInclude Duct Burners Yes - Interstage N/A N/A No N/ADuct Burner Maximum Firing Temperature 1400 F 1200 1400 1675Duct Burner Performance Calc Method Specify Firing Temp N/A N/A Specify Firing Temp N/ADuct Burner Status - - - N/A N/A In Use N/ADuct Burner Firing Temperature - - - F 1100 1300 1600Duct Burner HP Stm Flow Increase - - - %Duct Burner Fuel Capability Primary Fuel Only N/A N/A Dual Primary/Secondary Fuel N/ASCR Configuration Anhydrous Ammonia Injection N/A N/A Anhydrous Ammonia Injection N/AInclude CO Oxidation Catalyst No N/A N/A No N/ACT/ST Shaft Arrangement Multi-Shaft N/A N/A Multi-Shaft N/ASteam Turbine Arrangement G-Reheat, 2 Casing, 1 Flow, Direct Drive N/A N/A G-Reheat, 2 Casing, 1 Flow, Direct Drive N/AST Exhaust Configuration Axial N/A N/A Axial N/AST Sizing Criteria Excluding Max Exports/Extractions N/A N/A Excluding Max Exports/Extractions N/ANumber of ST Extractions 0 N/A 0 0 4ST Extraction 1 Export Flow 0 lb/hST Extraction 1 Export Pressure 1391 psiaST Extraction 1 Process Return Percentage 0.0 %ST Extraction 1 Process Return Temperature 80 FST Extraction 2 Export Flow 0 lb/hST Extraction 2 Export Pressure 1245 psiaST Extraction 2 Process Return Percentage 0.0 %ST Extraction 2 Process Return Temperature 80 F

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SOAPP-CT WorkStationConceptual Design Inputs SummaryProject: SOAPP-CT v7.0 Sample OutputsConceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Variable Value Units Min Default MaxST Extraction 3 Export Flow 0 lb/hST Extraction 3 Export Pressure 1098 psiaST Extraction 3 Process Return Percentage 0.0 %ST Extraction 3 Process Return Temperature 80 FST Extraction 4 Export Flow 0 lb/hST Extraction 4 Export Pressure 952 psiaST Extraction 4 Process Return Percentage 0.0 %ST Extraction 4 Process Return Temperature 80 FST Efficiency Method Workstation Calculated N/A N/A Workstation Calculated N/AHP ST Efficiency 80.0 %IP ST Efficiency 83.0 %LP ST Efficiency 85.0 %Include a Steam Bypass Yes N/A N/A Yes N/ACooling System Type Air Cooled Condenser N/A N/A Wet Mech Draft Cooling Twr N/ACycles of Concentration 5.0 N/ACondenser Pressure Calc Method Workstation Calculated N/A N/A Workstation Calculated N/ADesign Condenser Pressure 2.83 in HgCondenser Tube Material Titanium N/A N/A Titanium N/ACondenser Tube Cleaning None N/ACirc Water Pump Sparing 2 - 50% N/AInclude an Auxiliary Boiler No N/A N/A No N/AAuxiliary Boiler Steam Press 1000 psiaAuxiliary Boiler Steam Temp 600 FAuxiliary Boiler Steam Flow 500000 lb/hBoiler Feed Pump Sparing 1 - 100% N/A N/A 1 - 100% N/ABoiler Feed Pump Design Separate HP and IP Pumps N/A N/A Separate HP and IP Pumps N/ACondensate Pump Sparing 2 - 50% N/A N/A 2 - 50% N/AHRSG Enclosures No N/A N/A No N/APower Block Enclosure Yes N/A N/A Yes N/AWater Treatment Enclosure Yes N/A N/A Yes N/AWarehouse Included No N/A N/A No N/AInclude Fire Protection System? Yes N/A N/A Yes N/AFire Water Source River/Lake N/A N/A River/Lake N/ASubstructure Requirements No Piles N/A N/A No Piles N/AFuel Oil Storage Duration 1 daysFuel Oil Storage Basis Oil Tank Size W/O DB Operating N/A N/A Oil Tank Size with DB Operating N/ABypass Stack/Diverter Valve No N/A N/A No N/A

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SOAPP-CT WorkStationConceptual Design Inputs SummaryProject: SOAPP-CT v7.0 Sample OutputsConceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Variable Value Units Min Default MaxMain Stack Height 150 ft 35 150 300Switchyard Voltage 115.0 kV 15.0 115.0 500.0Book Life 30 years 3 30 50Tax Life 20 years 3 20 50Commercial Operating Year 2007 N/A 1950 2006 2050Commercial Operating Month January N/A N/A January N/ACapacity Factor - - - % 1 70 75Service Factor 75.0 % 40.0 75.0 98.0Equivalent Availability Factor 92.0 % 75.0 92.0 98.0Output Degradation Factor - - - %/yr 0.00 1.00 20.00Heat Rate Degradation Factor - - - %/yr 0.00 0.50 10.00Number of Starts Per Year 17 N/A 1 17 2000Tax Depreciation Method MACRS N/A N/A MACRS N/ATax Depreciation Schedule - - - %/yr 0 0 100Capital Tax Adjustment - - - % -100 0 100Import Duties Adjustment - - - % -100 0 100Freight Adjustment - - - % -100 0 100Royalties Adjustment - - - % -100 0 100User Specified Adjustment - - - % -200 0 200Salvage Values - - - % 0 0 100Site Data AZ - Moderate Labor Rates, 5 ppm

NOx, periodic

Max Ambient Dry Bulb Temp 104 F 31 85 125Max Ambient Wet Bulb Temp 75 F 58 89 104Min Ambient Dry Bulb Temp 31 F -35 -20 104Min Ambient Wet Bulb Temp 20 F -35 -20 75Perf Point Dry Bulb Temp - - - F 31.00 59.00 104.00Perf Point Wet Bulb Temp - - - F 54.17 52.00 93.00Site Elevation 1,117 ft -1,500 600 9,000Ambient Air Quality Clean N/A N/A Dusty N/AMax Daily Rainfall 3.0 in/day 0.0 7.0 100.0Average Annual Rainfall 7.5 in/yr 0.0 31.0 460.0Max Cooling Water Temp 80 FPerf Point Cooling Water Temp - - - FHeat Rejection Water Source River N/AUnit Makeup Water Source Well Water N/A N/A Well Water N/AMakeup Raw Water Consump Charge - - - USD/1,000 gal 0.00 1.00 100.00

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SOAPP-CT WorkStationConceptual Design Inputs SummaryProject: SOAPP-CT v7.0 Sample OutputsConceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Variable Value Units Min Default MaxCirculating Water Thermal Charge - - - USD/MBtuUBC Seismic Zone Zone 0 N/A N/A Zone 0 N/AStack Natural Gas NOx Limit 5.0 ppmvd @ 15% O2 2.5 5.0 9.0Stack Fuel Oil NOx Limit 9.0 ppmvd @ 15% O2Ammonia Emission Limit 5 ppmvd @ 15% O2 2 5 15Labor Crew Wage Rates - - - USD/h 0.00 50.00 150.00Construction Labor Index Value - - - N/A 0.00 1.00 2.00Productivity Multiplier - - - N/A 0.10 1.00 3.00General Facilities Capital 3.00 % 0.00 5.00 20.00Eng. & Home Office Fees 6.00 % 0.00 7.00 30.00Project Contingency 10.00 % 0.00 10.00 50.00Process Contingency 0.00 % 0.00 0.00 70.00Land Cost 1,000 USD/acre 0 10,000 1,000,000Ammonia (Delivered) 192.82 USD/ton 0.00 180.00 500.00NaOH (Delivered) 240.00 USD/ton 50.00 240.00 500.00H2SO4 (Delivered) 300.00 USD/ton 50.00 300.00 500.00SCR Catalyst (Delivered) 200.00 USD/ft3 50.00 280.00 500.00CO Catalyst (Delivered) 150.00 USD/ft3Other Waste Disposal 12.85 USD/ton 0.00 12.00 500.00Catalyst Disposal 22.50 USD/ft3 0.00 21.00 500.00Non-operating Purchased Power Cost 50.00 USD/MWh 10.00 50.00 100.00O&M Cost Method WorkStation Calculated N/A N/A Workstation Calculated N/AFixed O&M Direct Operating Labor 798,000 USD/yrFixed O&M Direct Maintenance Labor 510,000 USD/yrFixed O&M Annual Services, Materials & Purch Power 259,000 USD/yrFixed O&M Indirect Labor Costs 778,000 USD/yrVariable O&M Sched Maintenance Parts & Materials 922,000 USD/yrVariable O&M Sched Maintenance Labor 3,690,000 USD/yrVariable O&M Unplanned Maintenance Allowance 280,000 USD/yrVariable O&M Catalyst Replacement 709,000 USD/yrVariable O&M Other Consumables 691,000 USD/yrVariable O&M Disposal Charges 113,000 USD/yrVariable O&M Byproduct Credit 0 USD/yrTotal Fixed Costs 15.50 USD/kW-yrTotal Variable Costs 1.50 USD/MWhO&M Labor Index Value 1.000 N/A 0.000 1.000 2.000O&M Labor Productivity Multiplier 1.000 N/A 0.100 1.000 3.000

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SOAPP-CT WorkStationConceptual Design Inputs SummaryProject: SOAPP-CT v7.0 Sample OutputsConceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Variable Value Units Min Default MaxMaintenance Cost Adjustment 1.000 N/A 0.100 1.000 10.000Operating Tax Rates - - - % 0.00 35.00 90.00Insurance Rate 0.40 % 0.00 0.50 30.00Economic Data IPP, Current$, ROE18%, Mortgage,

2% Inf

IPP Loan Period 15 years 5 15 50Evaluation Basis Current Dollar Analysis N/A N/A Current Dollar Analysis N/AOwnership Type Independent Power Producer N/A N/A Independent Power Producer N/AIPP Analysis Method Solve for Capacity/Energy Charges N/A N/A Solve for Capacity and Energy Charges N/AIPP Equity Repayment Period 20 years 1 20 50IPP Loan Repay Method Mortgage Style N/A N/A Mortgage Style N/AInflation Rate 2.00 %/yr 0.00 2.00 30.00Base Year 2003 N/A 1950 2003 2100Const Sched Calc Method Workstation Calculated N/A N/A Workstation Calculated N/AUser Defined Const Sched Duration 30 monthsCapital Costs Esc Rate 2.00 %/yr 0.00 2.00 30.00O&M Costs Esc Rate 2.00 %/yr 0.00 2.00 30.00Common Equity Fraction 0.25 N/A 0.00 0.25 1.00Preferred Equity Fraction 0.10 N/ADebt Fraction 0.75 N/A 0.00 0.75 1.00Return on Common Equity 18.00 % 0.00 18.00 50.00Return on Preferred Equity 8.40 %Return on Debt 9.000 % 0.000 9.000 30.000Return on Debt During Construction 10.000 % 0.000 10.000 30.000Investment Tax Credit Rate 0.00 % 0.00 0.00 90.00Capacity Payments - - -Energy Payments - - -Byproduct Payments 0.00 USD/klb 0.00 0.00 0.00HP Steam Export Sales - - - USD/klbIP Steam Export Sales - - - USD/klbLP Steam Export Sales - - - USD/klbST Extraction 1 Steam Sales - - - USD/klbST Extraction 2 Steam Sales - - - USD/klbST Extraction 3 Steam Sales - - - USD/klbST Extraction 4 Steam Sales - - - USD/klbFuel Data Natural Gas- $5.25MBtu, 3.5% Esc

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SOAPP-CT WorkStationConceptual Design Inputs SummaryProject: SOAPP-CT v7.0 Sample OutputsConceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Variable Value Units Min Default MaxCT Primary Fuel Type Natural Gas N/A N/A Natural Gas N/ACT Secondary Fuel Type None N/A N/A No 2 Fuel Oil N/ACT Secondary Fuel Usage - - - %CT Primary Fuel Price - - - USD/MBtu 0.00 3.00 100.00CT Secondary Fuel Price - - - USD/MBtuNatural Gas Supply Pressure 400 psig 50 400 1,000DB Primary Fuel Type Natural Gas N/A N/A Natural Gas N/ADB Secondary Fuel Type None N/A N/A None N/ADB Secondary Fuel Usage - - - %DB Primary Fuel Hydrogen (H2) Constituent 0.00000 mole fractionDB Primary Fuel Hydrocarbon (CxHy) Constituent 0.98806 mole fractionDB Primary Fuel Carbon Dioxide (CO2) Constituent 0.00804 mole fractionDB Primary Fuel Nitrogen (N2) Constituent 0.00390 mole fractionDB Primary Fuel Carbon (C) Constituent 0.00000 mole fractionDB Primary Fuel Sulfur (S) Constituent 0.00000 mole fractionDB Primary Fuel LHV 20,960 Btu/lbDB Primary Fuel HHV Factor 1.11 N/ADB Primary Fuel Price - - - USD/MBtu 0.00 3.00 100.00DB Secondary Fuel Hydrogen (H2) Constituent 0.13000 mole fractionDB Secondary Fuel HydroCarbon (CxHy) Constituent 0.00000 mole fractionDB Secondary Fuel Carbon Dioxide (CO2) Constituent 0.00000 mole fractionDB Secondary Fuel Nitrogen (N2) Constituent 0.00000 mole fractionDB Secondary Fuel Carbon (C) Constituent 0.86950 mole fractionDB Secondary Fuel Sulfur (S) Constituent 0.00050 mole fractionDB Secondary Fuel LHV 18,560 Btu/lbDB Secondary Fuel HHV Factor 1.06 N/ADB Secondary Fuel Price - - - USD/MBtu

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SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Period Number Period Duration1 23832 19533 24624 1962Period Number Inlet Air Cooler StatusDesign Point In Use1 In Use2 Not in Use3 Not in Use4 In UsePeriod Number Air Cooling Discharge TempDesign Point 591 592 593 594 59Period Number Evaporative Cooler EffectivenessDesign Point 851 852 853 854 85Period Number Duct Burner StatusDesign Point In Use1 In Use2 Not in Use3 Not in Use4 In UsePeriod Number Duct Burner Firing TemperatureDesign Point 13501 13502 13503 13504 1350Period Number Duct Burner HP Stm Flow IncreaseDesign Point 51 5

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SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

2 53 54 5Period Number Capacity FactorDesign Point 701 702 703 704 70Year Output Deg. Factor2003 1Year HR Deg. Factor2003 .5Year Tax Deprec. Sched.1 6.5632 73 6.4824 5.995 5.5466 5.137 4.7468 4.4599 4.45910 4.45911 4.45912 4.4613 4.45914 4.4615 4.45916 4.4617 4.45918 4.4619 4.45920 4.4621 .56Component Local Sales TaxAuxiliary Boiler 0Boiler Feed System Equipment 0

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SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

CEM Equipment 0Circ Water System Equipment 0Closed Cooling Water System Equip.0Combustion Turbine 0Concrete Materials 0Condensate Heating Equipment 0Condensate System Equipment 0Controls & Instrumentation Equipment0Controls & Instrumentation Materials0Cranes & Hoists 0Deaerator 0Diverter Valve/Bypass Stack 0Duct Burner 0Duct Materials 0Electrical Equipment 0Electrical Materials 0Fire Protection Equipment 0Fuel Gas Compressor 0Fuel System Equipment 0HRSG 0HVAC Equipment 0HVAC Materials 0Inlet Air Cooling Equipment 0Inlet Air Filtration Equipment 0Insulation Materials 0Main Condenser and Accessories 0Main Stack Materials 0Misc Mechanical Equipment 0Misc Mechanical Materials 0Piping Materials 0Plant Control Systems 0Post Combustion Emission Cont Equip.0Station & Instrument Air Equipment 0Steam Turbine 0Steam Turbine Bypass Equipment 0Steel Materials 0Water Treatment Equipment 0Wiring Materials 0

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SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Component Import Duties AdjustmentAuxiliary Boiler 0Boiler Feed System Equipment 0CEM Equipment 0Circ Water System Equipment 0Closed Cooling Water System Equip.0Combustion Turbine 0Concrete Materials 0Condensate Heating Equipment 0Condensate System Equipment 0Controls & Instrumentation Equipment0Controls & Instrumentation Materials0Cranes & Hoists 0Deaerator 0Diverter Valve/Bypass Stack 0Duct Burner 0Duct Materials 0Electrical Equipment 0Electrical Materials 0Fire Protection Equipment 0Fuel Gas Compressor 0Fuel System Equipment 0HRSG 0HVAC Equipment 0HVAC Materials 0Inlet Air Cooling Equipment 0Inlet Air Filtration Equipment 0Insulation Materials 0Main Condenser and Accessories 0Main Stack Materials 0Misc Mechanical Equipment 0Misc Mechanical Materials 0Piping Materials 0Plant Control Systems 0Post Combustion Emission Cont Equip.0Station & Instrument Air Equipment 0Steam Turbine 0Steam Turbine Bypass Equipment 0

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SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Steel Materials 0Water Treatment Equipment 0Wiring Materials 0Component Freight AdjustmentAuxiliary Boiler 0Boiler Feed System Equipment 0CEM Equipment 0Circ Water System Equipment 0Closed Cooling Water System Equip.0Combustion Turbine 0Concrete Materials 0Condensate Heating Equipment 0Condensate System Equipment 0Controls & Instrumentation Equipment0Controls & Instrumentation Materials0Cranes & Hoists 0Deaerator 0Diverter Valve/Bypass Stack 0Duct Burner 0Duct Materials 0Electrical Equipment 0Electrical Materials 0Fire Protection Equipment 0Fuel Gas Compressor 0Fuel System Equipment 0HRSG 0HVAC Equipment 0HVAC Materials 0Inlet Air Cooling Equipment 0Inlet Air Filtration Equipment 0Insulation Materials 0Main Condenser and Accessories 0Main Stack Materials 0Misc Mechanical Equipment 0Misc Mechanical Materials 0Piping Materials 0Plant Control Systems 0Post Combustion Emission Cont Equip.0

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SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Station & Instrument Air Equipment 0Steam Turbine 0Steam Turbine Bypass Equipment 0Steel Materials 0Water Treatment Equipment 0Wiring Materials 0Component Royalties AdjustmentAuxiliary Boiler 0Boiler Feed System Equipment 0CEM Equipment 0Circ Water System Equipment 0Closed Cooling Water System Equip.0Combustion Turbine 0Concrete Materials 0Condensate Heating Equipment 0Condensate System Equipment 0Controls & Instrumentation Equipment0Controls & Instrumentation Materials0Cranes & Hoists 0Deaerator 0Diverter Valve/Bypass Stack 0Duct Burner 0Duct Materials 0Electrical Equipment 0Electrical Materials 0Fire Protection Equipment 0Fuel Gas Compressor 0Fuel System Equipment 0HRSG 0HVAC Equipment 0HVAC Materials 0Inlet Air Cooling Equipment 0Inlet Air Filtration Equipment 0Insulation Materials 0Main Condenser and Accessories 0Main Stack Materials 0Misc Mechanical Equipment 0Misc Mechanical Materials 0

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SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Piping Materials 0Plant Control Systems 0Post Combustion Emission Cont Equip.0Station & Instrument Air Equipment 0Steam Turbine 0Steam Turbine Bypass Equipment 0Steel Materials 0Water Treatment Equipment 0Wiring Materials 0Component User Specified AdjustmentAuxiliary Boiler 0Boiler Feed System Equipment 0CEM Equipment 0Circ Water System Equipment 0Closed Cooling Water System Equip.0Combustion Turbine 0Concrete Materials 0Condensate Heating Equipment 0Condensate System Equipment 0Controls & Instrumentation Equipment0Controls & Instrumentation Materials0Cranes & Hoists 0Deaerator 0Diverter Valve/Bypass Stack 0Duct Burner 0Duct Materials 0Electrical Equipment 0Electrical Materials 0Fire Protection Equipment 0Fuel Gas Compressor 0Fuel System Equipment 0HRSG 0HVAC Equipment 0HVAC Materials 0Inlet Air Cooling Equipment 0Inlet Air Filtration Equipment 0Insulation Materials 0Main Condenser and Accessories 0

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SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Main Stack Materials 0Misc Mechanical Equipment 0Misc Mechanical Materials 0Piping Materials 0Plant Control Systems 0Post Combustion Emission Cont Equip.0Station & Instrument Air Equipment 0Steam Turbine 0Steam Turbine Bypass Equipment 0Steel Materials 0Water Treatment Equipment 0Wiring Materials 0Component Salvage ValuesAuxiliary Boiler 0Boiler Feed System Equipment 0CEM Equipment 0Circ Water System Equipment 0Closed Cooling Water System Equip.0Combustion Turbine 0Concrete Materials 0Condensate Heating Equipment 0Condensate System Equipment 0Controls & Instrumentation Equipment0Controls & Instrumentation Materials0Cranes & Hoists 0Deaerator 0Diverter Valve/Bypass Stack 0Duct Burner 0Duct Materials 0Electrical Equipment 0Electrical Materials 0Fire Protection Equipment 0Fuel Gas Compressor 0Fuel System Equipment 0HRSG 0HVAC Equipment 0HVAC Materials 0Inlet Air Cooling Equipment 0

Date: 02/21/04 16:14User: System Administrator

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Page 18: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Inlet Air Filtration Equipment 0Insulation Materials 0Main Condenser and Accessories 0Main Stack Materials 0Misc Mechanical Equipment 0Misc Mechanical Materials 0Piping Materials 0Plant Control Systems 0Post Combustion Emission Cont Equip.0Station & Instrument Air Equipment 0Steam Turbine 0Steam Turbine Bypass Equipment 0Steel Materials 0Water Treatment Equipment 0Wiring Materials 0Period Number Perf Point Dry Bulb TempDesign Point 711 93.52 48.33 644 88.9Period Number Perf Point Wet Bulb TempDesign Point 621 682 413 504 66Period Number Perf Point Cooling Water TempDesign Point 601 602 603 604 60Year MU Consump Charge Escalation2003 1 0Year CW Thermal Charge Escalation2003 .06 0

Date: 02/21/04 16:14User: System Administrator

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Page 19: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Name Code Base Comp Fringes Other Equip FICA Profit RateConcrete Chimney CONC 22.5 5.49 8.64 0 6.95 1.98 14.48 60.04Concrete Direct COND 21.66 3.39 8.33 0 2.63 1.91 12.16 50.08Concrete Pump CONP 22.15 3.35 8.65 0 8.25 1.94 14.1 58.44Condenser CNDR 24.86 2.8 10.52 0 7.28 2.15 15.18 62.79Conduits And Trays ECND 24.36 2.36 8.59 0 .88 2.12 12.37 50.68Earthwork ETWK 25.28 2.2 10.48 0 61.72 2.19 31.47 133.34Electrical, Heavy EQ 1 EHEA 23.52 2.46 8.73 0 2.08 2.05 12.5 51.34Electrical, Heavy EQ 2&3 EHEB 24.9 3.85 9.95 0 3.07 2.16 14.08 58.01Electrical, Heavy EQ 4 EHEC 24.9 3.85 9.95 0 4.3 2.16 14.45 59.61Embedded Steel EMBD 20.99 1.97 8.74 0 11.22 1.86 14.19 58.97Excavation EXFD 20.98 1.97 8.73 0 11.21 1.86 14.18 58.93Formwork FORM 22.55 3.58 8.18 0 17.39 1.97 16.91 70.58HVAC HVAC 24.71 1.82 9.5 0 4.84 2.13 13.79 56.79Instrumentation Electrical INEL 26.71 1.22 9.36 0 3.22 2.29 13.8 56.6Insulation INSL 24.54 2.49 9.71 0 1.99 2.12 13.14 53.99Masonry MSRY 24.7 3.4 8.22 0 3.08 2.14 13.35 54.89Misc. Mechanical EQ MECH 25.05 1.64 9.66 0 7.62 2.17 14.75 60.89Painting PNTR 21.63 8.06 6.56 0 4.02 1.9 13.43 55.6Paving Bituminous PBIT 23.97 2.45 9.02 0 14.83 2.09 16.57 68.93001Pumps And Drives PUMP 25.44 1.82 9.79 0 7.42 2.2 14.92 61.59Reinforcing Cadwelds REIN 25.57 8.41 11.48 0 1.05 2.21 15.54 64.25999Seeding & Mulching MSTR 20.88 2.91 7.44 0 10.26 1.85 13.76 57.1Station Piping SPNG 25.48 1.76 9.7 0 11.88 2.21 16.23 67.25999Steam Generator SGEN 25.44 2.84 10.69 0 15.83 2.2 18.02 75.02Structural Steel STST 25.7 6.85 11.46 0 17.96 2.22 20.18 84.37Tanks TANK 24.76 1.7 9.4 0 8.74 2.14 14.91 61.65Turbine Generator TURB 24.31 2.41 9.45 0 2.03 2.12 12.97 53.29Water Treatment WTRT 25.43 1.64 9.74 0 8.28 2.2 15.1 62.39Wiremen WIRE 26.99 1.39 9.67 0 10.31 2.32 16.18 66.86Yard Piping YDPP 25.01 1.72 9.7 0 9.8 2.17 15.42 63.82

Date: 02/21/04 16:14User: System Administrator

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Page 20: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Cost Category CNDR CONC COND CONP ECND EHEA EHEB EHEC EMBD ETWK EXFDAuxiliary Boiler And Accessories .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Boiler Feed System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Buildings .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Bypass Stack and Diverter Valve .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Circulating Water System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Closed Cooling Water System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Combustion Turbine And Accessories.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Condensate Heating System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Condensate System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Condenser and Accessories .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Continuous Emission Monitoring System.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Cranes and Hoists .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Deaeration System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Duct Burner System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Electrical Systems - Combustion Turbine.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Electrical Systems - HRSGs .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Electrical Systems - Steam Turbine .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Fire Protection System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Fuel Gas Compressor and Accessories.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Fuel Systems .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88HRSGs and Accessories .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Inlet Air Cooling System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Inlet Filtration System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Main Exhaust Stack .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Plant Control System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Post Combustion Emission Controls .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Station and Instrument Air System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Steam Bypass System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Steam Piping .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Steam Turbine And Accessories .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Waste Water Treatment System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Water Treatment System .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88Cost Category CNDR CONC COND CONP ECND EHEA EHEB EHEC EMBD ETWK EXFDAuxiliary Boiler And Accessories 1 1 1 1 1 1 1 1 1 1 1Boiler Feed System 1 1 1 1 1 1 1 1 1 1 1Buildings 1 1 1 1 1 1 1 1 1 1 1Bypass Stack and Diverter Valve 1 1 1 1 1 1 1 1 1 1 1

Date: 02/21/04 16:14User: System Administrator

Page: 1

Page 21: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Circulating Water System 1 1 1 1 1 1 1 1 1 1 1Closed Cooling Water System 1 1 1 1 1 1 1 1 1 1 1Combustion Turbine And Accessories1 1 1 1 1 1 1 1 1 1 1Condensate Heating System 1 1 1 1 1 1 1 1 1 1 1Condensate System 1 1 1 1 1 1 1 1 1 1 1Condenser and Accessories 1 1 1 1 1 1 1 1 1 1 1Continuous Emission Monitoring System1 1 1 1 1 1 1 1 1 1 1Cranes and Hoists 1 1 1 1 1 1 1 1 1 1 1Deaeration System 1 1 1 1 1 1 1 1 1 1 1Duct Burner System 1 1 1 1 1 1 1 1 1 1 1Electrical Systems - Combustion Turbine1 1 1 1 1 1 1 1 1 1 1Electrical Systems - HRSGs 1 1 1 1 1 1 1 1 1 1 1Electrical Systems - Steam Turbine 1 1 1 1 1 1 1 1 1 1 1Fire Protection System 1 1 1 1 1 1 1 1 1 1 1Fuel Gas Compressor and Accessories1 1 1 1 1 1 1 1 1 1 1Fuel Systems 1 1 1 1 1 1 1 1 1 1 1HRSGs and Accessories 1 1 1 1 1 1 1 1 1 1 1Inlet Air Cooling System 1 1 1 1 1 1 1 1 1 1 1Inlet Filtration System 1 1 1 1 1 1 1 1 1 1 1Main Exhaust Stack 1 1 1 1 1 1 1 1 1 1 1Plant Control System 1 1 1 1 1 1 1 1 1 1 1Post Combustion Emission Controls1 1 1 1 1 1 1 1 1 1 1Station and Instrument Air System 1 1 1 1 1 1 1 1 1 1 1Steam Bypass System 1 1 1 1 1 1 1 1 1 1 1Steam Piping 1 1 1 1 1 1 1 1 1 1 1Steam Turbine And Accessories 1 1 1 1 1 1 1 1 1 1 1Waste Water Treatment System 1 1 1 1 1 1 1 1 1 1 1Water Treatment System 1 1 1 1 1 1 1 1 1 1 1

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Page 22: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

FORM HVAC INEL INSL MECH MSRY MSTR PBIT PNTR PUMP REIN SGEN SPNG STST TANK.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88FORM HVAC INEL INSL MECH MSRY MSTR PBIT PNTR PUMP REIN SGEN SPNG STST TANK1 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 1

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Page 23: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

1 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 11 1 1 1 1 1 1 1 1 1 1 1 1 1 1

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Page 24: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

TURB WIRE WTRT YDPP.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88.88 .88 .88 .88TURB WIRE WTRT YDPP1 1 1 11 1 1 11 1 1 11 1 1 1

Date: 02/21/04 16:14User: System Administrator

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Page 25: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

1 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 11 1 1 1

Date: 02/21/04 16:14User: System Administrator

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Page 26: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Year Federal Income TaxState Income Tax City Income Tax Property Tax Revenue Tax2003 35 9 0 1.5 0

Date: 02/21/04 16:14User: System Administrator

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Page 27: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Year Escalation Period #1 Period #2 Period #3 Period #42003 0 0 0 0 0Year Escalation Period #1 Period #2 Period #3 Period #42003 0 0 0 0 0

Date: 02/21/04 16:14User: System Administrator

Page: 1

Page 28: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Year HP Steam Export Sales Escalation2003 4.82 0Year IP Steam Export Sales Escalation2003 4.82 0Year LP Steam Export Sales Escalation2003 4.82 0Year ST Extraction 1 Steam Sales Escalation2003 5 0Year ST Extraction 2 Steam Sales Escalation2003 5 0Year ST Extraction 3 Steam Sales Escalation2003 5 0Year ST Extraction 4 Steam Sales Escalation2003 5 0Period Number CT Secondary Fuel UsageDesign Point 51 52 53 54 5

Date: 02/21/04 16:15User: System Administrator

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Page 29: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Year Escalation Period #1 Period #2 Period #3 Period #42003 3.5 5.25 5.25 5.25 5.25Year Escalation Period #1 Period #2 Period #3 Period #42003 3.5 0 0 0 0

Date: 02/21/04 16:15User: System Administrator

Page: 1

Page 30: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Period Number DB Secondary Fuel UsageDesign Point 51 52 53 54 5

Date: 02/21/04 16:15User: System Administrator

Page: 1

Page 31: Insert SOAPP-CT 7.0soapp.epri.com/output/soapp-ct/wProjectInput.pdfProject Input Flexible Inputs ... Multi Shaft, SCR, ACC, Arizona Variable Value Units Min Default Max Unit Data GE

SOAPP-CT WorkStation

Project: SOAPP-CT v7.0 Sample OutputsArray Values for Conceptual Design: 250 MW CCCG, GE 7FA, Multi Shaft, SCR, ACC, Arizona

Year Escalation Period #1 Period #2 Period #3 Period #42003 3.5 5.25 5.25 5.25 5.25Year Escalation Period #1 Period #2 Period #3 Period #42003 3.5 0 0 0 0

Date: 02/21/04 16:15User: System Administrator

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