Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all...

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Version 9.0 www.soapp.com 1.650.855.2043 [email protected] Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived from this input, and the results of the heat and material balances, using algorithms derived from design practice and manufacturer’s data. SOAPP–CT summarizes the results of this equipment sizing in an Equipment List containing up to 715 equipment design parameters, depending on plant design, including: 22 general project data 28 structural design data 79 combustion turbine system data 83 steam generator equipment data 20 steam turbine equipment data 53 condenser equipment data 135 pump data for 14 systems 44 balance of plant equipment data 26 tank data for 5 systems 201 piping data for 25 systems 24 electrical equipment data The Equipment List is supplemented by a Motor List / Auxiliary Power Summary and an Electri- cal Single Line Drawing. All of these equipment design reports produced by SOAPP–CT are generated dynamically, reflecting every relevant change you make to your Project Input.

Transcript of Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all...

Page 1: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

Version 9.0

www.soapp.com

1.650.855.2043 [email protected]

Equipment Design

Detailed Plant Conceptual Design

SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived from this input, and the results of the heat and material balances, using algorithms derived from design practice and manufacturer’s data. SOAPP–CT summarizes the results of this equipment sizing in an Equipment List containing up to 715 equipment design parameters, depending on plant design, including:

22 general project data

28 structural design data

79 combustion turbine system data

83 steam generator equipment data

20 steam turbine equipment data

53 condenser equipment data

135 pump data for 14 systems

44 balance of plant equipment data

26 tank data for 5 systems

201 piping data for 25 systems

24 electrical equipment data

The Equipment List is supplemented by a Motor List / Auxiliary Power Summary and an Electri-cal Single Line Drawing. All of these equipment design reports produced by SOAPP–CT are generated dynamically, reflecting every relevant change you make to your Project Input.

Page 2: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsGENERAL PROJECT DATAAmbient ConditionsAmbient Air Quality DustyMaximum Site Ambient Dry Bulb Temp 100 FMaximum Site Ambient Wet Bulb Temp 72 FMinimum Site Ambient Dry Bulb Temp 29 FPerformance Point Site Ambient Dry Bulb Temp 68 FPerformance Point Site Ambient Wet Bulb Temp 59 FSite Average Annual Rainfall 11.0 in/yrSite Maximum Daily Rainfall 4.0 in/daySite Elevation Above Mean Sea Level 2584 ftDesign BasisCycle Type Combined Cycle CogenerationNumber of Combustion Turbines 1Number of HRSGs 1Number of Steam Turbines 1Unit Capacity Factor 90 %Frequency 60 HzCT Primary Fuel Type Natural GasCT Secondary Fuel Type NoneSecondary Fuel Usage FactorHeat Rejection Water SourceMaximum Cooling Water TempPerformance Point Cooling Water TempUnit Makeup Water Source Well WaterSTRUCTURAL DESIGN DATAEnclosuresPower Block Enclosure NoWater Treatment Enclosure YesWater Treatment Enclosure Height 20 ftWater Treatment Enclosure Length 70 ftWater Treatment Enclosure Width 70 ftHRSG EnclosuresWarehouse Width 82 ftWarehouse Length 192 ftApproximate Plant DimensionsOverall East/West Dimension 646 ftOverall North/South Dimension 606 ftApproximate Unit Land Area Requirement 9 acresPower Block East/West Dimension 128 ftPower Block North/South Dimension 258 ftFoundations/SubstructureUBC Seismic Zone Zone 0Foundation Type Grade BeamSubstructure Requirements No PilesStacksNumber of HRSG Bypass StacksInside Diameter at Top of HRSG Bypass StacksTop Height Above Grade of HRSG Bypass StacksMaterial of Construction for HRSG Bypass StacksHRSG Bypass Diverter Valve HeightHRSG Bypass Diverter Valve Length

Date: 04/06/15 10:42User: System Administrator

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Page 3: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsHRSG Bypass Diverter Valve WidthMain Stack(s) - Number 1Inside Diameter at Top of Main Stack(s) 23.67 ftMinimum Thickness at Top of Main Stack(s) 0.25 inMain Stack Top Height Above Grade 150 ftMaterial of Construction for Main Stack(s) SteelCOMBUSTION TURBINE DATATurbine/Generator DataNumber of CTs in Plant Design 1CT Manufacturer/Model Number Westinghouse 501G-60 HzCT NOx Control, Natural Gas Dry Low NOx CombustorsCT NOx Control, No 2 Fuel OilCT NOx Emission Limit @ 15% O2 - Natural Gas 25 ppmvdCT NOx Emission Limit @ 15% O2 - Fuel OilCT Exhaust Gas Temperature 1143 FCT Generator Type Hydrogen CooledCT Gross Heat Rate (LHV) @ Perf. Pt. Conditions 8726 Btu/kWhCT Gross Output at Generator Terminals @ Perf. Pt. 239587 kWInlet Air Filtration DataInlet Air Filtration Pulse TypeCombustion Turbine Inlet Filter HeightCombustion Turbine Inlet Filter LengthCombustion Turbine Inlet Filter WidthNumber of Barrier FiltersHours Before Change Out of Barrier FiltersNumber of PrefiltersHours Before Change Out of PrefiltersBleed Air Fan SizeCombustion Turbine Inlet Filter HeightCombustion Turbine Inlet Filter LengthCombustion Turbine Inlet Filter WidthNumber of Barrier FiltersHours Before Change Out of Barrier FiltersNumber of PrefiltersHours Before Change Out of PrefiltersPulse Filter Length 53.00 ftPulse Filter Total Height 39.00 ftPulse Filter Width 30.00 ftNumber of Pulse Filter Cartridges 1083Hours Between Change Out of Pulse Filters 12500 hInlet Precooling System DataCT Inlet Precooling System Type Evaporative CoolersCT Inlet Precooling System Outlet Temp 60 FEvaporative Coolers Face Area 1943 ft2Evaporative Coolers Height 51.00 ftEvaporative Coolers Length 3.50 ftEvaporative Coolers Width 38.09 ftHeat Recovery Absorption Chiller Plant HeightHeat Recovery Absorption Chiller Plant LengthHeat Recovery Absorption Chiller Plant WidthChilled Water Cooling Coil HeightChilled Water Cooling Coil Length

Date: 04/06/15 10:42User: System Administrator

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Page 4: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsChilled Water Cooling Coil WidthCooling Coil Face AreaSteam Absorption Chiller Plant HeightSteam Absorption Chiller Plant LengthSteam Absorption Chiller Plant WidthChilled Water Cooling Coil HeightChilled Water Cooling Coil LengthChilled Water Cooling Coil WidthCooling Coil Face AreaSteam Turbine Driven Mechanical Chiller HeightSteam Turbine Driven Mechanical Chiller LengthSteam Turbine Driven Mechanical Chiller WidthChilled Water Cooling Coil HeightChilled Water Cooling Coil LengthChilled Water Cooling Coil WidthCooling Coil Face AreaAmmonia System Compressor Area HeightAmmonia System Compressor Area LengthAmmonia System Compressor Area WidthAmmonia System Cooling Tower HeightAmmonia System Cooling Tower LengthAmmonia System Cooling Tower WidthAmmonia System Pump Area HeightAmmonia System Pump Area LengthAmmonia System Pump Area WidthChilled Water Cooling Coil HeightChilled Water Cooling Coil LengthChilled Water Cooling Coil WidthCooling Coil Face AreaCooling Tower Assembly HeightCooling Tower Assembly LengthCooling Tower Assembly WidthTotal Fog Nozzles per TurbineOperating PressureDesign Cooling CapacityNumber of Cooling StagesFog Water Flow RateMotor Driven Mechanical Chiller HeightMotor Driven Mechanical Chiller LengthMotor Driven Mechanical Chiller WidthChilled Water Cooling Coil HeightChilled Water Cooling Coil LengthChilled Water Cooling Coil WidthCooling Coil Face AreaHEAT RECOVERY STEAM GENERATOR DATAHRSG DesignNumber of Heat Recovery Steam Generators (HRSGs) 1Number of Pressure Levels Three PressureST Reheat Cycle Non-ReheatHigh Pressure Drum Pinch Point Temp 20 FHigh Pressure Steam Drum Approach Temp 20 FIntermediate Pressure Drum Pinch Point Temp 15 F

Date: 04/06/15 10:42User: System Administrator

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Page 5: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsIntermediate Pressure Steam Drum Approach Temp 20 FLow Pressure Drum Pinch Point Temp 15 FLow Pressure Steam Drum Approach TempHRSG Exhaust Gas Stack Temp 334 FHRSG Exhaust Gas Stack Volumetric Flow 1583527 ft3/min-stdHRSG DimensionsHRSG Height 64.00 ftHRSG Length 93.00 ftHRSG Width 57.00 ftDeaeratorDeaerator Selection Standalone DeaeratorDeaerator Cond Inlet Perf. Pt. Mass Flow 667018 lb/hDeaerator Cond Inlet Perf. Pt. Mass FlowDeaerator Cond Inlet Perf. Pt. Pressure 110.0 psiaDeaerator Cond Inlet Perf. Pt. Temperature 109.4 FDeaerator Vent Losses Perf. Pt. Mass Flow 1334 lb/hVacuum Deaerator Cond Perf. Pt. Outlet Mass FlowVacuum Deaerator Cond Perf. Pt. Outlet PressureVacuum Deaerator Cond Perf. Pt. Outlet TemperatureDeaerator Vent Losses Perf. Pt. Mass FlowCondensate HeaterHeater SelectionCondensate Heater Perf. Pt. Inlet Mass FlowCondensate Heater Perf. Pt. Inlet PressureCondensate Heater Perf. Pt. Inlet TempCondensate Heater Perf. Pt. Outlet Mass FlowCondensate Heater Perf. Pt. Outlet PressureCondensate Heater Perf. Pt. Outlet TempCondensate Heater HeightCondensate Heater LengthCondensate Heater WidthW-W Hx Perf. Pt. Inlet Mass FlowW-W Hx Perf. Pt. Inlet PressureW-W Hx Perf. Pt. Inlet TemperatureW-W Hx Perf. Pt. Outlet Mass FlowW-W Hx Perf. Pt. Outlet PressureW-W Hx Perf. Pt. Outlet TemperatureW-W Hx HeightW-W Hx LengthW-W Hx WidthW-W Hx Surface AreaFeedwater Economizer HeightFeedwater Economizer LengthFeedwater Economizer WidthDuct BurnersInclude Duct BurnersDuct Burner UseDuct Burner Fuel CapabilityDuct Burner HP Steam Flow Increase % of unfired steam flowHRSG Gas Temperature After Ductburner (Perf. Pt.)Number of Duct Burner Elements (each HRSG)Duct Burner Width

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Page 6: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsDuct Burner HeightDuct Burner Cooling Air Fan SizeDuct Burner Auxiliary PowerSelective Catalytic Reduction (per HRSG)SCR Technology Included YesSCR Configuration Conventional (with HRSG)SCR Ammonia Slip Limit (@15% O2) 5 ppmvdSCR Ammonia System Auxiliary Power 13.2 kWSCR Ammonia Vaporizer Auxiliary Power 10.0 kWSCR Catalyst Duct Height 48 ftSCR Catalyst Duct Length 15 ftSCR Catalyst Duct Width 42 ftSCR Catalyst Volume 3099 ft3Anhydrous Ammonia Injection Dilution Air Fan Size 5.0 hpAnhydrous Ammonia Storage Tank - Number 1Anhydrous Ammonia Storage Tank Diameter 7 ftAnhydrous Ammonia Storage Tank Length 15 ftAnhydrous Ammonia Storage Tank Volume 3252 galAqueous Ammonia Dilution Air Heater Aux PowerAqueous Ammonia Dilution Fan SizeAqueous Ammonia Pump SizeAqueous Ammonia Storage Tank - NumberAqueous Ammonia Storage Tank DiameterAqueous Ammonia Storage Tank LengthAqueous Ammonia Storage Tank VolumeCO CatalystInclude CO Oxidation CatalystCO Catalyst Duct HeightCO Catalyst Duct LengthCO Catalyst Duct WidthCO Catalyst VolumeSTEAM TURBINE DATANumber of Steam Turbines Operating 1Non-reheat, single-flow, geared, axial exhaustNon-reheat, single-flow, geared, down exhaustNon-reheat, HP geared sec, sep. LP sec, axial exhaustNon-reheat, HP geared sec, sep. LP sec, down exhaustNon-reheat, single flow, axial exhaustNon-reheat, single flow, down exhaustNon-reheat, 2 casing, 2 flow LP sec down exhaustReheat, 2 casing, HP/IP, 2-flow LP sec, down exhaustReheat, 3 casing, HP/IP, 4-flow LP sec, down exhaustReheat, 2 casing, HP sec and IP/LP sec, axial exhaustReheat, 2 casing, HP sec and IP/LP sec, down exhaustSingle, casing reheat, axial exhaustSingle, casing reheat, down exhaustNumber of Steam Turbine Exhausts (per ST) 2ST Sizing Criteria Excluding Max ExportsInclude a Steam Bypass NoST Gross Output at Generator Terminals @ Perf. Pt. (per ST) 92162 kWST Gross Output at Generator Terminals @ Perf. Pt. (Total) 92162 kWSteam Turbine Exhaust Annulus Area (per ST) 28.38 ft2

Date: 04/06/15 10:42User: System Administrator

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Page 7: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsSteam Turbine Exhaust Losses (per ST) 15.00 Btu/lbApproximate Steam Turbine Last Stage Blade Length 21.00 inCONDENSER DATADesign DataCooling System TypeNumber of CondensersCondenser ArrangementCondenser Number of Passes (per condenser)Condenser Number of Pressures (per condenser)Number of Condenser Shells (per condenser)Condenser Pressure - Design 6.24 in HgPerformance DataDesign Heat Load (per condenser) 580,816,768 Btu/hSteam Inlet Mass Flow (per condenser)Steam Inlet PressureSteam Inlet TemperatureCondensate Outlet Mass Flow (per condenser)Condensate Outlet PressureCondensate Outlet TemperatureCirculating Water Inlet Flow (per condenser)Circulating Water Inlet Temperature - PerformanceCirculating Water Inlet Temperature - DesignCirculating Water Outlet Temperature - PerformanceCirculating Water Outlet Temperature - DesignDimensions (per condenser)Condenser Overall LengthCondenser Total HeightCondenser Shell HeightCondenser Shell LengthCondenser Shell WidthCondenser Hotwell HeightCondenser Shell HeightCondenser Shell LengthCondenser Shell WidthCondenser Water Box LengthCondenser Water Box Side LengthCondenser Expansion Joint LengthCondenser Expansion Joint WidthTube Data (per condenser)Number of Condenser TubesCondenser Tube Outside DiameterCirculating Water VelocityCondenser Tube GaugeCondenser Tube Wall ThicknessCondenser Tube LengthCondenser Tube MaterialCondenser Tube Surface AreaCondenser Tube TypeCondenser Tube CleaningAir Cooled CondenserCooling System Type Air Cooled CondenserCell Length 34 ft

Date: 04/06/15 10:42User: System Administrator

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Page 8: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsCell Width 34 ftNumber of Cells Long 5Number of Cells Wide 3Total Number of Cells 15Fan Diameter 28 ftFan Motor Size 150 hpHeight of Tube Bundles 20 ftTotal Height 56 ftTotal Length 170 ftTotal Width 102 ftCOOLING TOWER DATACooling System TypeNumber of Cooling TowersCooling Tower(s) Total Number of CellsDesign Heat Rejected (Total Plant)Circulating Water Inlet Flow (Total Plant)Circulating Water Inlet TemperatureCooling Tower Fan Capacity EachCooling Tower Fan Motor SizeCooling Tower Fan DiameterCooling Tower - Height of Fan DeckCooling Tower - Height of Fan StackCooling Tower Cell LengthCooling Tower WidthCooling Tower HeightCooling Tower #1 - LengthCooling Tower #2 - LengthCooling Tower #3 - LengthCooling Tower #4 - LengthPUMP DATABoiler Feed PumpsBoiler Feed Pump Sparing 1 - 100%High Pressure Feed PumpsHigh Pressure Feed Pump SparingTotal Number of Pumps for PlantTypeCapacity eachNet Developed HeadBrake HorsepowerStandard Motor SizeDriver SpeedDriver TypeHigh Pressure/Intermediate Pressure Feed PumpsBoiler Feed Pump Design HP Pump with IP TakeoffHP/IP Feed Pump Sparing 1 - 100%Total Number of Pumps Per Plant 1Pump Type Split Case w/Take OffHP Capacity each 1450 gpmHP Net Developed Head 4474 ft H2OIP Capacity each 149 gpmIP Net Developed Head 1437 ft H2OBrake Horsepower 2195 hp

Date: 04/06/15 10:42User: System Administrator

Page: 7

Page 9: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsStandard Motor Size 2250 hpDriver Speed 3600 rpmDriver Type MotorIntermediate Pressure Feed PumpsIP Feed Pump SparingTotal Number of Pumps for PlantTypeCapacity eachNet Developed HeadBrake HorsepowerStandard Motor SizeDriver SpeedDriver TypeLow Pressure Feed PumpsLP Feed Pump Sparing 1 - 100%Total Number of Pumps for Plant 1Type Hor Split CaseCapacity each 150 gpmNet Developed Head 143 ft H2OBrake Horsepower 9 hpStandard Motor Size 10 hpDriver Speed 1800 rpmDriver Type MotorCondensate Pump(s)Number 1 - 100%Total Number of Pumps for Plant 1Type VerticalDischarge Flow Capacity 1449 gpmNet Developed Head 162 ft H2OBrake Horsepower 78 hpStandard Motor Size 100 hpCirculating Water PumpsNumberTotal Number of Pumps for PlantTypeDischarge Flow CapacityNet Developed HeadMotor TypeBrake HorsepowerStandard Motor SizeMiscellaneous PumpsFire Water PumpsNumberCapacityNet Developed HeadAuxiliary PowerBrake HorsepowerStandard Motor SizeScreen Wash PumpsTotal Number of Pumps for PlantCapacityNet Developed Head

Date: 04/06/15 10:42User: System Administrator

Page: 8

Page 10: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsBrake HorsepowerStandard Motor SizeService Water PumpsCapacity 4580 gpmNet Developed Head 115 ft H2OComponent Cooling Water PumpsNumber 2 - 100%Pump Type HorizontalCapacity 4354 gpmNet Developed Head 115 ft H2OBrake Horsepower 167 hpStandard Motor Size 200 hpCondenser Vacuum PumpsNumberTotal Number of Pumps for PlantPump TypeBrake HorsepowerStandard Motor SizeCT Fuel Oil Unloading PumpsNumberBrake HorsepowerStandard Motor SizeCT Fuel Oil Forwarding PumpsNumber ErrorCapacity 0 gpmTotal Developed Head 0 ft H2OBrake Horsepower 0.00 hpStandard Motor Size 0.00 hpDuct Burner Fuel Oil Forwarding PumpsNumberCapacityTotal Developed HeadBrake HorsepowerStandard Motor SizeCondensate Makeup PumpNumber 2 - 100%Type Hor Split CaseCapacity 48 gpmTotal Developed Head 100 ft H2OBrake Horsepower 2.00 hpStandard Motor Size 3.00 hpPretreatment Backwash Transfer PumpNumber 2 - 100%Type VerticalCapacity 2 gpmTotal Developed Head 100 ft H2OBrake Horsepower 0.09 hpStandard Motor Size 0.13 hpWaste Water PumpsNumber 2 - 100%Type VerticalCapacity 187 gpm

Date: 04/06/15 10:42User: System Administrator

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Page 11: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsTotal Developed Head 200 ft H2OBrake Horsepower 3.17 hpStandard Motor Size 15.00 hpWater Treatment System Makeup PumpsNumber 2 - 100%Type Hor Split CaseCapacity 75 gpmTotal Developed Head 200 ft H2OBrake Horsepower 6.24 hpStandard Motor Size 7.50 hpWater Treatment System Raw Water PumpsNumber 1 - 100%Type VerticalCapacity 75 gpmTotal Developed Head 300 ft H2OBrake Horsepower 6.87 hpStandard Motor Size 10.00 hpHRSG HP Circulation PumpsNumberTypeCapacityTotal Developed HeadBrake HorsepowerStandard Motor SizeHRSG IP Circulation PumpsNumberTypeCapacityTotal Developed HeadBrake HorsepowerStandard Motor SizeHRSG LP Circulation PumpsNumberTypeCapacityTotal Developed HeadBrake HorsepowerStandard Motor SizeBOP EQUIPMENT DATANatural Gas CompressorCT Nat Gas Pressure Required 625 psigNumber of NG Booster Compressors 2Compressor Capacity 97241 lb/hCompressor Total Developed Pressure 225 psidCompressor Brake Horsepower 1366 hpStandard Motor Size 1500 hpInstrument & Station Air CompressorsType ScrewNumber 3 - 50%Capacity,Total 277 ft3/min-stdDischarge Pressure 125 psigBrake Horsepower 48 hp

Date: 04/06/15 10:42User: System Administrator

Page: 10

Page 12: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsStandard Motor Size 50 hpNumber of Receivers 2Volume of Receivers,Each 28 ft3Instrument Air Dryers Type DessicantAftercoolers & Moisture Separators Included YesAuxiliary BoilerAuxiliary Boiler Steam PressureAuxiliary Boiler Steam TemperatureAuxiliary Boiler Steam FlowAuxiliary Boiler Fuel Flow (primary fuel)Number of Auxiliary Boiler UnitsOverall Auxiliary Boiler LengthOverall Auxiliary Boiler WidthOverall Auxiliary Boiler HeightComponent Cooling Water Heat ExchangerComponent Cooling Water Hx Inlet Flow 4147 gpmComponent Cooling Water Hx Inlet Temperature 110 FComponent Cooling Water Hx Outlet Flow 4147 gpmComponent Cooling Water Hx Outlet Temperature 86 FComponent Cooling Water Hx Total Heat Load 49109632 Btu/hTurbine Room CraneNumberSpanMain Hook CapacityAuxiliary Hook CapacityWater Treating SystemNumber of Parallel Trains 2 - 100%Total Auxiliary Power 20.83 kWTotal Installed Capacity 8139 gphCondensate PolisherNumber of Service VesselsService Vessel DiameterSpace RequirementPrecoat Tank/Pumps & Air Surge Tank IncludedCondensate Preheating Heat ExchangerHeat Exchanger Heat LoadHeat Exchanger Surface AreaTANKSTreated Water Storage TankTank Capacity 61043 galTank Diameter 24 ftTank Height 18 ftNeutralization Tank and AgitatorNeutralization Tank Capacity 268915 galNeutralization Tank Diameter 36 ftNeutralization Tank Height 34 ftNumber of Neutralization Tank Agitators 1 - 100%Neutralization Tank Agitator Motor Size 0.500 hpOil/Water Separator(s)Oil Separator Number 1Oil Separator Type Corrugated PlateOil Separator Capacity 31 gpm

Date: 04/06/15 10:42User: System Administrator

Page: 11

Page 13: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsFire Water TankFire Water SourceNumber of TanksTank CapacityTank DiameterTank HeightFuel Oil Storage Tank(s)DB Fuel Oil Storage BasisFuel Oil Storage DurationTotal Storage Volume RequirementNumberCapacityDiameterHeightDike AreaDike LengthDike WidthPIPING DATAFuel Oil PipingCT Fuel Oil Branch Pipe SizeCT Fuel Oil Branch Pipe ScheduleCT Fuel Oil Branch Pipe Total LengthCT Fuel Oil Header Pipe SizeCT Fuel Oil Header Pipe ScheduleCT Fuel Oil Header Pipe LengthFuel Oil Storage Tank Header Piping SizeFuel Oil Storage Tank Header Piping ScheduleFuel Oil Storage Tank Header Piping Total LengthHRSG Fuel Oil Header Pipe SizeHRSG Fuel Oil Header Pipe ScheduleHRSG Fuel Oil Header Pipe LengthNatural Gas PipingPlant Nat Gas Header Pipe Size 6 inPlant Nat Gas Header Pipe Schedule 40Plant Nat Gas Header Pipe Length 500 ftCT Nat Gas Header Pipe Size 4 inCT Nat Gas Header Pipe Schedule 40CT Nat Gas Header Pipe Length 120 ftCT Nat Gas Branch Pipe Size 4 inCT Nat Gas Branch Pipe Schedule 40CT Nat Gas Branch Pipe Length 250 ftHRSG Nat Gas Header Pipe SizeHRSG Nat Gas Header Pipe ScheduleHRSG Nat Gas Header Pipe LengthCold Reheat Steam PipingCold Reheat Steam Mass Flow, per HRSGCold Reheat Steam PressureCold Reheat Steam TemperaturePlant Header DiameterPlant Header LengthPlant Header MaterialPlant Header Thickness

Date: 04/06/15 10:42User: System Administrator

Page: 12

Page 14: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsHRSG Leads DiameterHRSG Leads LengthHRSG Leads MaterialHRSG Leads ThicknessHot Reheat Steam PipingHot Reheat Steam Mass Flow, per HRSGHot Reheat Steam PressureHot Reheat Steam TemperaturePlant Header DiameterPlant Header LengthPlant Header MaterialPlant Header ThicknessHRSG Leads DiameterHRSG Leads LengthHRSG Leads MaterialHRSG Leads ThicknessHigh Pressure Steam PipingMass Flow, per HRSG 587277 lb/hPressure at HRSG 1545 psiaTemperature at HRSG 1005 FPlant Header Diameter 10 inPlant Header Length 630 ftPlant Header Material A335GRP22Plant Header Thickness 0.365 inHRSG Leads Diameter 10 inHRSG Leads Length 840 ftHRSG Leads Material A335GRP22HRSG Leads Thickness 0.365 inIntermediate Pressure Steam PipingMass Flow, per HRSG 62406 lb/hPressure at HRSG 464 psiaTemperature at HRSG 528 FPlant Header Diameter 8 inPlant Header Length 630 ftPlant Header Material A106GRBPlant Header Thickness 0.322 inHRSG Leads Diameter 8 inHRSG Leads Length 840 ftHRSG Leads Material A106GRBHRSG Leads Thickness 0.322 inLow Pressure Steam PipingMass Flow, per HRSGPressure at HRSGTemperature at HRSGPlant Header DiameterPlant Header LengthPlant Header MaterialPlant Header ThicknessHRSG Leads DiameterHRSG Leads LengthHRSG Leads MaterialHRSG Leads Thickness

Date: 04/06/15 10:42User: System Administrator

Page: 13

Page 15: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsHigh Pressure Steam Turbine Bypass PipingDiameterLengthMaterialThicknessIntermed. Pressure Steam Turbine Bypass PipingDiameterLengthMaterialThicknessLow Pressure Steam Turbine Bypass PipingDiameterLengthMaterialThicknessHigh Pressure HRSG Export PipingHigh Pressure HRSG Export Steam FlowDiameterLengthMaterialThicknessIntermediate Pressure HRSG Export PipingIntermediate Pressure HRSG Export Steam FlowDiameterLengthMaterialThicknessIntermediate Pressure HRSG Saturated Export PipingIntermediate Pressure HRSG Saturated Export Steam FlowDiameterLengthMaterialThicknessLow Pressure HRSG Export PipingLow Pressure HRSG Export Steam FlowDiameterLengthMaterialThicknessLow Pressure HRSG Saturated Export PipingLow Pressure HRSG Saturated Export Steam FlowDiameterLengthMaterialThicknessSteam Turbine Controlled Extraction 1 PipingControlled Steam Turbine Extraction 1 Mass FlowControlled Steam Turbine Extraction 1 PressureControlled Steam Turbine Extraction 1 TemperatureControlled Steam Turbine Extraction 1 DiameterControlled Steam Turbine Extraction 1 LengthControlled Steam Turbine Extraction 1 Material

Date: 04/06/15 10:42User: System Administrator

Page: 14

Page 16: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsControlled Steam Turbine Extraction 1 ThicknessSteam Turbine Controlled Extraction 2 PipingControlled Steam Turbine Extraction 2 Mass FlowControlled Steam Turbine Extraction 2 PressureControlled Steam Turbine Extraction 2 TemperatureControlled Steam Turbine Extraction 2 DiameterControlled Steam Turbine Extraction 2 LengthControlled Steam Turbine Extraction 2 MaterialControlled Steam Turbine Extraction 2 ThicknessSteam Turbine Controlled Extraction 3 PipingControlled Steam Turbine Extraction 3 Mass FlowControlled Steam Turbine Extraction 3 PressureControlled Steam Turbine Extraction 3 TemperatureControlled Steam Turbine Extraction 3 DiameterControlled Steam Turbine Extraction 3 LengthControlled Steam Turbine Extraction 3 MaterialControlled Steam Turbine Extraction 3 ThicknessSteam Turbine Controlled Extraction 4 PipingControlled Steam Turbine Extraction 4 Mass FlowControlled Steam Turbine Extraction 4 PressureControlled Steam Turbine Extraction 4 TemperatureControlled Steam Turbine Extraction 4 DiameterControlled Steam Turbine Extraction 4 LengthControlled Steam Turbine Extraction 4 MaterialControlled Steam Turbine Extraction 4 ThicknessCombustion Turbine Steam Injection PipingCT Steam Injection PressureCT Steam Injection TemperatureCT Steam Injection Mass Flow, per CT - MaxDiameterLengthMaterialThicknessCold Reheat Steam Injection PipingCT Steam Injection Piping PressureCT Steam Injection Piping TemperatureCT Steam Injection Piping Mass Flow, per CT - MaxDiameterLengthMaterialThicknessHigh Pressure Feedwater PipingHigh Pressure Feedwater Mass Flow, per HRSG 697034 lb/hHigh Pressure Feedwater Pressure 1763 psiaHigh Pressure Feedwater Temperature 322 FHeader Diameter 8 inHeader Length 130 ftHeader Material A106GRBHeader Thickness 0.322 inLeads Diameter 8 inLeads Length 100 ftLeads Material A106GRB

Date: 04/06/15 10:42User: System Administrator

Page: 15

Page 17: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsLeads Thickness 0.322 inIntermediate Pressure Feedwater PipingIntermediate Pressure Feedwater Mass Flow, per HRSG 63773 lb/hIntermediate Pressure Feedwater Pressure 555 psiaIntermediate Pressure Feedwater Temperature 324 FHeader Diameter 3 inHeader Length 130 ftHeader Material A106GRBHeader Thickness 0.203 inLeads Diameter 3 inLeads Length 80 ftLeads Material A106GRBLeads Thickness 0.203 inLow Pressure Feedwater PipingLow Pressure Feedwater Mass Flow, per HRSG 54062 lb/hLow Pressure Feedwater Pressure 88 psiaLow Pressure Feedwater Temperature 319 FHeader Diameter 2 inHeader Length 130 ftHeader Material A106GRBHeader Thickness 0.154 inLeads Diameter 2 inLeads Length 80 ftLeads Material A106GRBLeads Thickness 0.154 inCondensate PipingHeader Diameter 8 inHeader Length 200 ftHeader Material A106GRBHeader Thickness 0.322 inLeads Diameter 8 inLeads Length 20 ftLeads Material A106GRBLeads Thickness 0.322 inCirculating Water PipingDiameterLengthMaterialThicknessComponent Cooling Water PipingHeat Exchanger Outlet Piping - Header Diameter 16 inHeat Exchanger Outlet Piping - Header Length 580 ftHeat Exchanger Outlet Piping - Header Material A106GRBHeat Exchanger Outlet Piping - Header Thickness 0.500 inELECTRICAL EQUIPMENT DATAHigh Voltage Breakers - Number 4Motorized Disconnects - Number 8Switchgear MV Breakers - Number 8MCC (480 V) Groups - Number 9Main Power Transformer - Combustion Turbine 244 MVAUnit Auxiliary Transformer - Combustion Turbine 1500 kVAMain Power Transformer - Steam Turbine 94 MVA

Date: 04/06/15 10:42User: System Administrator

Page: 16

Page 18: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationEntire Equipment List- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

Variable Value UnitsUnit Auxiliary Transformer - Steam Turbine 9216 kVAMain Power Transformer - Single-Shaft ConfigurationUnit Auxiliary Transformer - Singe-Shaft ConfigurationReserve Auxiliary Transformer 10716 kVAUnit Subs 4Isolated Phase Bus Duct - CT MPT to Generator 11500 AIsolated Phase Bus Duct - CT MPT to UAT 100 AIsolated Phase Bus Duct - CT UAT to Non-Seg Bus Ducts 200 AIsolated Phase Bus Duct - ST MPT to Generator 4400 AIsolated Phase Bus Duct - ST MPT to UAT 400 AIsolated Phase Bus Duct - ST UAT to Non-Seg Bus Ducts 1100 AIsolated Phase Bus Duct - MPT to GeneratorIsolated Phase Bus Duct - MPT to UATIsolated Phase Bus Duct - UAT to Non-Seg Bus DuctsIsolated Phase Bus Duct - RAT to Non-Seg Bus Ducts 1300 ASwitchyard Voltage 115 kVElectrical System Low Voltage 15 kV

Date: 04/06/15 10:42User: System Administrator

Page: 17

Page 19: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived

SOAPP-CT WorkStationMotor List and Auxiliary Power Summary- English scale for:

Project: SOAPP-CT v9 Sample OutputConceptual Design: 291 MW CCCG, 501G, IAC@60F, 3P, ACC, C-E Charge, AZ Unit: �1 WH501G, CC PA-SP, Evap Coolers, 3P@1465, SCR, ACC, AZ Site: �Tuscon, Arizona Econ: �IPP, Current$, ROE10%, Eq Princ Pay, 2.5%Inf, 24m, AZ Pri. Fuel: �Natural Gas - Current$, $7.00MMBtu, 2%Esc, 2.5%Inf, AZ

System/Component Sparing orTotal #

Design HP(each)

NumberOperating

OperatingAux kW

OperatingAux kW

OperatingAux kW

Design Period#1 Period#2Circulating Water Pumps (Sparing per condenser)Screen Wash Pumps (Sparing per condenser)Component Cooling Water Pumps 2 - 100% 200 1 124.4 112.6 102.8Cooling Tower FansAir Cooled Condenser Fans 15 150 15 1,510.0 1,510.0 1,510.0Condenser Vacuum Pumps (Sparing per condenser)Condensate Pumps (Sparing per condenser) 1 - 100% 100 1 58.3 53.8 50.0Condensate Makeup Pumps 2 - 100% 3.00 1 1.01 0.93 0.86High Pressure Feedwater PumpsIntermediate Pressure Feedwater PumpsHigh/Intermediate Pressure Feedwater Pumps 1 - 100% 2250 1 1,665.6 1,520.5 1,421.0Low Pressure Feedwater Pumps 1 - 100% 10 1 5.7 5.9 5.4HRSG HP Circulation PumpsHRSG IP Circulation PumpsHRSG LP Circulation PumpsWater Treatment System N/A N/A N/A 20.9 20.9 20.9Raw Water Pumps 1 - 100% 10 1 5.1 3.1 2.9Water Treatment Makeup Pumps 2 - 100% 8 1 3.4 2.1 1.9Pretreatment Backwash Pumps 2 - 100% 0.125 1 0.051 0.031 0.028Waste Water Pumps 2 - 100% 15 1 2.4 2.1 1.9Waste Water Neutralization Tank Agitator 1 - 100% 0.500 1 0.279 0.279 0.279CT Fuel Oil Forwarding PumpsCT Fuel Oil Unloading PumpsDuct Burner Fuel Oil Forwarding PumpsNatural Gas Compressors 2 1500 1 1,018.6 934.8 865.6Fire Water PumpsStation Air Compressors 3 - 50% 50 2 71.6 71.6 71.6Bypass Stack/Diverter Valve Seal Air FansInlet Air Cooling System N/A N/A N/A 57.6 0.0 0.0SCR Ammonia Injection System N/A N/A N/A 13.2 12.9 12.7Dilution Air FansCombustion Turbine Auxiliaries N/A N/A N/A 599.0 534.4 481.3Transformer Losses N/A N/A N/A 1,161.1 1,048.9 955.1Miscellaneous Auxiliaries N/A N/A N/A 663.5 599.4 545.8Total Auxiliary Power Consumption 6,981.7 6,434.1 6,050.1

Date: 04/07/15 14:06User: System Administrator

Page: 1

Page 20: Equipment Design - EPRI · Equipment Design Detailed Plant Conceptual Design SOAPP–CT sizes all major plant equipment, based on your Project Input, the process configuration derived