Project Input - EPRIsoapp.epri.com/output/soapp-ct/wProjectInput_0515.pdf · Project Input Flexible Input SOAPP ... HRSG Circulation Natural Circulation N/A N/A Natural ... Condenser

Version 9.0

www.soapp.com

1.650.855.2043 [email protected]

Project Input

Flexible Input

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.

Version 9.0

www.soapp.com

1.650.855.2043 [email protected]

Project Input — (continued)

Accurate Combustion Turbine Modeling

Select one of the 153 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.

SOAPP-CT WorkStationConceptual Design Inputs SummaryProject: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ

Variable Value Units Min Default MaxUnit Data 1 WH501G, CC PA-SP, Evap Coolers, 3P@1465,

SCR, ACC, AZCT Model Number Westinghouse 501G-60 Hz N/A N/A GE 7FA.05-60 Hz N/ANumber of CT's 1 N/A 1 2 3Cycle 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 2 N/A 1 1 12Period Duration - - - hours 0 0 8760Periodic CT Load Percentage - - - % 40 100 100Periodic Number of CT's Operating - - - N/A 1 1 1CT 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/ACT Natural Gas NOx Limit 25 ppmvd @ 15% O2 9 25 75CT No 2 Fuel Oil NOx Limit 42 ppmvd @ 15% O2CEM'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 No Condensate Heater N/A N/A Condensate Heater N/ADeaerator Selection Standalone 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 1465 psia 320 1465 2415IP Steam Pressure 440 psia 170 440 1315LP Steam Pressure 75 psia 20 45 200HP Pressure Control Method Partial arc - sliding pressure N/A N/A Full arc - sliding pressure N/AHP Minimum Sliding Pressure 512.8 psiaHot Reheat Pressure Calc Method Workstation Calculated N/A N/A Workstation Calculated N/AHot Reheat Pressure 366.3 psiaHP Steam Temp 1000 F 600 1000 1115Hot Reheat Steam Temp 1000 FIP Steam Temp 525 F 464 525 620LP Steam Temp 318 F 318 480 620HP Pinch Point 20 F 9 30 200IP Pinch Point 15 F 9 15 200Date: 04/07/15 14:09User: System Administrator

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Variable Value Units Min Default MaxLP Pinch Point 15 F 9 15 200HP Evap Approach 20 F 9 20 120IP Evap Approach 20 F 9 20 120LP Evap Approach 20 FHP Export Flow 0 lb/h 0 0 587581HP Export Process Return Percentage 0.0 %HP Export Process Return Temperature 80 FIP Export Flow, Superheated 0 lb/h 0 0 62585IP Export Flow, Saturated 0 lb/hIP Export Process Return Percentage 0.0 %IP Export Process Return Temperature 80 FLP Export Flow, Superheated 0 lb/h 0 0 0LP Export Flow, Saturated 0 lb/hLP Export Process Return Percentage 0.0 %LP Export Process Return Temperature 80 FExport 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 0 lb/hInclude Duct Burners No N/A N/A No N/ADuct Burner Maximum Firing Temperature 1400 FDuct Burner Performance Calc Method Specify Firing Temp N/A N/A Specify Firing Temp N/ADuct Burner Status - - - N/ADuct Burner Firing Temperature - - - FDuct Burner HP Stm Flow Increase - - - %Duct Burner Fuel Capability Dual Primary/Secondary Fuel N/AHP Steam Attemperation Location Interstage N/A N/A Interstage N/ASCR Configuration Conventional (with HRSG) N/A N/A Conventional (With HRSG) N/ASCR Reagent Anhydrous Ammonia N/A N/A Anhydrous Ammonia 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/AInclude Synchronous Clutch? No N/A N/A No N/ASteam Turbine Arrangement D-Non-reheat, 2 Casing, 2 Flow, Direct Drive, DownN/A N/A B-Non-Reheat, 2 Casing, 1 Flow, High Speed GearedN/ANumber of Steam Turbines 1 N/A 1 1 1ST Exhaust Configuration Downward N/A N/A Downward N/AST Sizing Criteria Excluding Max Exports/Extractions N/A N/A Excluding Max Exports/ExtractionsN/ANumber of ST Extractions 0 N/A 0 0 4ST Extraction 1 Specify Temperature? No N/A N/A No N/AST Extraction 1 Export Temperature 586 FST Extraction 1 Export Flow 0 lb/hST Extraction 1 Export Pressure 1391 psiaST Extraction 1 Process Return Percentage 0.0 %Date: 04/07/15 14:09User: System Administrator

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Variable Value Units Min Default MaxST Extraction 1 Process Return Temperature 80 FST Extraction 2 Specify Temperature? No N/A N/A No N/AST Extraction 2 Export Temperature 571 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 FST Extraction 3 Specify Temperature? No N/A N/A No N/AST Extraction 3 Export Temperature 556 FST 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 Specify Temperature? No N/A N/A No N/AST Extraction 4 Export Temperature 538 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 User-Specified N/A N/A Workstation Calculated N/AHP ST Efficiency 80.0 % 60.0 90.0 100.0IP ST Efficiency 83.0 % 60.0 90.0 100.0LP ST Efficiency 85.0 % 60.0 90.0 100.0Include a Steam Bypass No 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/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 HP Pump with IP Takeoff N/A N/A Separate HP and IP Pumps N/ACondensate Pump Sparing 1 - 100% N/A N/A 2 - 50% N/AHRSG Enclosures No N/A N/A No N/APower Block Enclosure No N/A N/A Yes N/AWater Treatment Enclosure Yes N/A N/A Yes N/ADate: 04/07/15 14:09User: System Administrator

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Variable Value Units Min Default MaxWarehouse Included Yes N/A N/A No N/AInclude Fire Protection System? No N/A N/A Yes N/AFire Water Source City/Well Water 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 W/O DB OperatingN/ABypass Stack/Diverter Valve No N/A N/A No N/AMain Stack Height 150 ft 35 150 300Switchyard Voltage 115.0 kV 15.0 115.0 500.0Book Life 20 years 3 30 50Tax Life 20 years 3 20 50Commercial Operating Year 2015 N/A 1950 2015 2050Commercial Operating Month January N/A N/A January N/ACapacity Factor - - - %Service Factor 90.0 %Equivalent Availability Factor 92.0 % 90.0 96.0 98.0Output Degradation Factor - - - % 0.00 1.00 20.00Heat Rate Degradation Factor - - - % 0.00 0.50 10.00Number of Starts Per Year 17 N/A 1 4 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 100Capital Cost Adders - - - USD -1,000,000,000 01,000,000,000Site Data Tuscon, Arizona

Max Ambient Dry Bulb Temp 100 F 29 85 125Max Ambient Wet Bulb Temp 72 F 56 86 100Min Ambient Dry Bulb Temp 29 F -35 -20 100Min Ambient Wet Bulb Temp 29 F -35 -20 72Perf Point Dry Bulb Temp - - - F 29.00 59.00 100.00Perf Point Wet Bulb Temp - - - F 37.78 52.00 59.00Ambient Dry Bulb Temp Basis for ST Design 48 F 29 68 68Min Ambient Dry Bulb Temp with Duct Firing 48 FSite Elevation 2,584 ft -1,500 600 9,000Ambient Air Quality Dusty N/A N/A Dusty N/AMax Daily Rainfall 4.0 in/day 0.0 7.0 100.0Date: 04/07/15 14:09User: System Administrator

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Variable Value Units Min Default MaxAverage Annual Rainfall 11.0 in/yr 0.0 31.0 460.0Max Cooling Water Temp 90 FPerf Point Cooling Water Temp - - - FHeat Rejection Water Source Lake 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 1.00 100.00Circulating Water Thermal Charge - - - USD/MBtuUBC Seismic Zone Zone 0 N/A N/A Zone 0 N/AStack Natural Gas NOx Limit 2.5 ppmvd @ 15% O2 1.5 5.0 25.0Stack Fuel Oil NOx Limit 9.0 ppmvd @ 15% O2Ammonia Emission Limit 5.0 ppmvd @ 15% O2 2.0 3.5 15.0Labor 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 5.00 % 0.00 5.00 20.00Project Contingency 10.00 % 0.00 10.00 50.00Process Contingency 0.00 % 0.00 0.00 70.00Contractor Cost Components - - - % 0.00 8.00 15.00Owner Cost Components - - - % 0.00 1.00 10.00NG Pipeline Interconnection Cost Adder 500 USD 0 025,000,000Transmission Line Interconnection Cost Adder 500 USD 0 025,000,000Land Cost 10,000 USD/acre 0 100,00010,000,000Ammonia (Delivered) 180.00 USD/ton 0.00 700.00 1,000.00NaOH (Delivered) 240.00 USD/ton 50.00 430.00 1,000.00H2SO4 (Delivered) 300.00 USD/ton 50.00 80.00 1,000.00SCR Catalyst (Delivered) 280.00 USD/ft3 50.00 460.00 1,000.00CO Catalyst (Delivered) 2,100.00 USD/ft3Other Waste Disposal 12.00 USD/ton 0.00 35.00 1,000.00Catalyst Disposal 21.00 USD/ft3 0.00 30.00 1,000.00Non-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 876,000 USD/yrFixed O&M Direct Maintenance Labor 559,000 USD/yrFixed O&M Annual Services, Materials & Purch Power 341,000 USD/yrFixed O&M Indirect Labor Costs 687,000 USD/yrVariable O&M Sched Maintenance Parts & Materials 4,674,000 USD/yrVariable O&M Sched Maintenance Labor 215,000 USD/yrVariable O&M Unplanned Maintenance Allowance 244,000 USD/yrVariable O&M Catalyst Replacement 254,000 USD/yrVariable O&M Other Consumables 1,109,000 USD/yrVariable O&M Disposal Charges 18,000 USD/yrDate: 04/07/15 14:09User: System Administrator

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Variable Value Units Min Default MaxVariable O&M Byproduct Credit 500 USD/yrTotal Fixed Costs 4.54 USD/kW-yrTotal Variable Costs 1.96 USD/MWhO&M Labor Index Value 0.880 N/A 0.000 1.000 2.000O&M Labor Productivity Multiplier 1.000 N/A 0.100 1.000 3.000Maintenance Cost Adjustment 1.000 N/A 0.100 1.000 10.000Operating Tax Rates - - - % 0.00 35.00 90.00Insurance Rate 0.50 % 0.00 0.50 30.00Economic Data IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf,

24m, AZIPP 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 ChargesN/AIPP Equity Repayment Period 20 years 1 20 50IPP Loan Repay Method Equal Principal Payments N/A N/A Mortgage Style N/AInflation Rate 2.50 %/yr 0.00 2.00 30.00Base Year 2012 N/A 1950 2012 2100Const Sched Calc Method User-Specified N/A N/A Workstation Calculated N/AUser Defined Const Sched Duration 24 months 6 30 60Capital 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 0.30 1.00Preferred Equity Fraction 0.10 N/ADebt Fraction 0.75 N/A 0.00 0.70 1.00Return on Common Equity 10.00 % 0.00 15.00 50.00Return on Preferred Equity 8.40 %Return on Debt 9.000 % 0.000 7.000 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/klb

Date: 04/07/15 14:09User: System Administrator

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Variable Value Units Min Default MaxFuel Data Natural Gas - Current$, $7.00MMBtu, 2%Esc,

2.5%Inf, AZCT 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 7.39 100.00CT 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 98.80600 mole fractionDB Primary Fuel Hydrocarbon (CxHy) Constituent 0.00000 mole fractionDB Primary Fuel Carbon Dioxide (CO2) Constituent 0.80400 mole fractionDB Primary Fuel Nitrogen (N2) Constituent 0.39000 mole fractionDB Primary Fuel Carbon (C) Constituent 0.00000 mole fractionDB Primary Fuel Sulfur (S) Constituent 0.00000 mole fractionDB Primary Fuel LHV 20,000 Btu/lbDB Primary Fuel HHV Factor 1.11 N/ADB Primary Fuel Price - - - USD/MBtuDB 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 v9 Sample OutputArray Values for Conceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ

Period Number Period Duration1 20002 2000Period Number Periodic CT Load Percentage1 902 80Period Number Periodic Number of CT's Operating1 12 1Period Number Inlet Air Cooler StatusDesign Point In Use1 Not in Use2 Not in UsePeriod Number Air Cooling Discharge TempDesign Point 591 592 59Period Number Evaporative Cooler EffectivenessDesign Point 851 852 85Period Number Duct Burner StatusDesign Point In Use1 Not in Use2 Not in UsePeriod Number Duct Burner Firing TemperatureDesign Point 13001 13002 1300Period Number Duct Burner HP Stm Flow IncreaseDesign Point 51 52 5Period Number Capacity FactorDesign Point 901 702 70Year Output Deg. Factor2012 1Year HR Deg. Factor2012 .5


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Year 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 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 Materials 0Cranes & Hoists 0Deaerator 0Diverter Valve/Bypass Stack 0Duct Burner 0Duct Materials 0Electrical Equipment 0Electrical Materials 0


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Fire 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 0Component 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 Materials 0Cranes & Hoists 0Deaerator 0Diverter Valve/Bypass Stack 0Duct Burner 0Duct Materials 0Electrical Equipment 0Electrical Materials 0


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Fire 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 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 Materials 0Cranes & Hoists 0Deaerator 0Diverter Valve/Bypass Stack 0Duct Burner 0Duct Materials 0Electrical Equipment 0Electrical Materials 0


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Fire 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 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 Materials 0Cranes & Hoists 0Deaerator 0Diverter Valve/Bypass Stack 0Duct Burner 0Duct Materials 0Electrical Equipment 0Electrical Materials 0


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Fire 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 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 Materials 0Cranes & Hoists 0Deaerator 0Diverter Valve/Bypass Stack 0Duct Burner 0Duct Materials 0Electrical Equipment 0Electrical Materials 0


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Fire 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 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 Materials 0Cranes & Hoists 0Deaerator 0Diverter Valve/Bypass Stack 0Duct Burner 0Duct Materials 0Electrical Equipment 0Electrical Materials 0


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Fire 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 0Capital Cost Adder Category ($)<Enter any name of category> 0Period Number Perf Point Dry Bulb TempDesign Point 681 632 59Period Number Perf Point Wet Bulb TempDesign Point 591 572 55Period Number Perf Point Cooling Water TempDesign Point 701 602 60Year MU Consump Charge Escalation2012 1.07 2Year CW Thermal Charge Escalation2012 .06 2


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Name Code Base Comp Fringes Other Equip FICA Profit RateConcrete Chimney CONC 27.53 4.91 15.42 3.3 9.36 2.6 22.09 85.21Concrete Direct COND 25.84 4.07 14.75 3.1 3.53 2.47 18.82 72.58Concrete Pump CONP 26.94 4.07 15.27 3.23 11.13 2.56 22.12 85.32Condenser CNDR 32.86 3.83 18.3 3.94 9.8 3.01 25.11 96.85001Conduits And Trays ECND 30.61 3.2 16.26 3.67 1.19 2.84 20.21 77.98Earthwork ETWK 34.67 3.63 18.3 4.16 83.13 3.15 51.47 198.51Electrical, Heavy EQ 1 EHEA 29.27 3.07 17.65 3.51 2.78 2.74 20.66 79.67999Electrical, Heavy EQ 2&3 EHEB 31.7 4.09 18.92 3.8 4.14 2.92 22.95 88.52Electrical, Heavy EQ 4 EHEC 31.7 4.09 18.92 3.8 5.79 2.92 23.53 90.74999Embedded Steel EMBD 31.59 6.47 22.04 3.79 3.75 2.91 24.69 95.24001Excavation EXFD 30.34 3.47 16.99 3.64 15.11 2.82 25.33 97.7Formwork FORM 29.2 4.58 14.48 3.5 23.42 2.73 27.27 105.18HVAC HVAC 31.61 2.78 18.95 3.79 6.52 2.91 23.3 89.86Instrumentation Electrical INEL 33.75 1.91 18.65 4.05 4.34 3.08 23.02 88.8Insulation INSL 31.45 3.93 20.57 3.77 2.67 2.9 22.85 88.14Masonry MSRY 30.08 4.72 14.11 3.61 4.16 2.8 20.82 80.3Misc. Mechanical EQ MECH 32.4 2.31 17.22 3.89 10.26 2.98 24.17 93.23Painting PNTR 27.25 12.53 14.14 3.27 5.42 2.58 22.82 88.01Paving Bituminous PBIT 30.1 3.59 15.69 3.61 19.95 2.8 26.51 102.25Pumps And Drives PUMP 33.05 2.47 17.39 3.97 10 3.03 24.47 94.38Reinforcing Cadwelds REIN 31.31 6.79 22.45 3.76 1.41 2.89 24.01 92.62Seeding & Mulching MSTR 24.4 3.99 13.31 2.93 13.84 2.36 21.29 82.12Station Piping SPNG 33.89 2.54 16.22 4.07 16 3.09 26.54 102.35Steam Generator SGEN 33.64 3.82 19.32 4.04 21.33 3.07 29.82 115.04Structural Steel STST 32.49 5.98 21.66 3.9 24.18 2.98 31.91 123.1Tanks TANK 31.84 2.4 16.7 3.82 11.77 2.94 24.31 93.78Turbine Generator TURB 30.33 2.98 18.66 3.64 2.72 2.82 21.4 82.55Water Treatment WTRT 33.06 2.31 17.21 3.97 11.17 3.03 24.76 95.51Wiremen WIRE 34.49 2.19 18.74 4.14 13.89 3.14 26.81 103.4Yard Piping YDPP 33.4 2.5 16.22 4.01 13.18 3.06 25.33 97.7


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


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


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HVAC INEL INSL MECH MSRY MSTR PBIT PNTR PUMP REIN SGEN SPNG STST TANK TURB.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88.88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88 .88HVAC INEL INSL MECH MSRY MSTR PBIT PNTR PUMP REIN SGEN SPNG STST TANK TURB1 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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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 1


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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 .88WIRE WTRT YDPP1 1 11 1 11 1 11 1 11 1 11 1 11 1 1


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


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Project Input - EPRIsoapp.epri.com/output/soapp-ct/wProjectInput_0515.pdf · Project Input Flexible Input SOAPP ... HRSG Circulation Natural Circulation N/A N/A Natural ... Condenser

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