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Equipment Design

Detailed Plant Conceptual Design SOAPP–CT.25 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.25 summarizes the results of this equipment sizing in an Equipment List containing over 250 equipment design parameters, depending on plant design, including:

• 17 general project data • 10 structural design data • 10 combustion turbine system data • 30 HRSG equipment data • 35 pump data • 15 balance of plant equipment data • 30 tank data • 110 piping data • 17 electrical equipment data

The Equipment List is supplemented by a Plant Performance Summary, a multimedia Emissions Summary at full load operation, and a Motor List / Auxiliary Power Summary. All of these equip-ment design reports produced by SOAPP–CT.25 are generated dynamically, reflecting every relevant change you make to your Project Input.

SOAPP-CT.25 WorkStation 11/1/00

Equipment ListProject: Sample OutputsConceptual Design: Cogen, 1 x 27 MW, NG, Quarterly

Variable Value UnitsGENERAL PROJECT DATAAmbient ConditionsMaximum Site Ambient Dry Bulb Temp 85.00 FMaximum Site Ambient Wet Bulb Temp 74.00 FMinimum Site Ambient Dry Bulb Temp -20.00 FSite Average Annual Rainfall 31.00 in/yrSite Maximum Daily Rainfall 7.00 in/daySite Elevation Above Mean Sea Level 600.00 ftDesign BasisUnit Cycle Configuration CogenerationNumber of Combustion Turbines 1 Number of HRSG's 1 Unit Frequency Market 60 HzPrimary Fuel - CT Natural GasSecondary Fuel - CT NonePrimary Fuel - DB Natural GasSecondary Fuel - DB NoneWater Treating System Source of Make-up Water Well WaterSTRUCTURAL DESIGN DATAEnclosuresPower Block Enclosure Length 76.00 ftPower Block Enclosure Width 56.00 ftPower Block Enclosure Height 34.00 ftWater Treatment Enclosure Length 77.28 ftWater Treatment Enclosure Width 80.40 ftWater Treatment Enclosure Height 20.00 ftHRSG Enclosure NoApproximate Plant DimensionsApproximate Unit Land Area Requirement 2.29 acresApproximate Length of Main Roadway 160.00 ftApproximate Pipe Bridge Length for Natural Gas Supply Pipe 187.00 ftApproximate Pipe Bridge Length for Export Steam Pipe 197.00 ftApproximate Pipe Bridge Length for Main Pipe Header 56.00 ftApproximate Pipe Bridge Length for CT Pipe Leads 38.00 ftApproximate Pipe Bridge Length for HRSG Pipe Leads 174.00 ftApproximate Pipe Bridge Length for Treated Water Main Pipe 196.00 ftFoundations/SubstructurePlant Seismic Zone Location Zone 0Foundation Type Grade BeamStacksBypass Stack(s) - Number 1 Inside Diameter at Top of HRSG Bypass Stack(s) 9.00 ftTop Height Above Grade of HRSG Bypass Stack(s) 80.00 ftMaterial of Construction for HRSG Bypass Stack(s) A238 Carbon Steel w/ 409Diverter Valve Height 15.00 ftDiverter Valve Length 13.00 ftDiverter Valve Width 11.00 ftMain Stack(s) - Number 1

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SOAPP-CT.25 WorkStation 11/1/00

Equipment ListProject: Sample OutputsConceptual Design: Cogen, 1 x 27 MW, NG, Quarterly

Variable Value UnitsInside Diameter at Top of Main Stack(s) 9.78 ftMinimum Thickness at Top of Main Stack(s) .25 inMain Stack Top Height Above Grade 80.00 ftMaterial of Construction for Main Stack(s) SteelCOMBUSTION TURBINE DATATurbine/Generator DataNumber of CTs in Plant Design 1 CT NOx Control Technology, Natural Gas Firing Water InjectionCT NOx Emission Limit @ 15% O2 - Natural Gas 25.00 ppmvd @ 15% O2CT Gross Output, per CT 28,939.02 kWCT Gross Heat Rate (LHV) 9,268.00 Btu/kWhCT Exhaust Gas Mass Flow Rate 665,765.75 lb/hCT Exhaust Gas Temperature 909.20 FCT Generator Type Air CooledInlet Air Filtration DataCombustion Turbine Inlet Filter Type Static FilterCombustion Turbine Inlet Filter Height 12.25 ftCombustion Turbine Inlet Filter Length 12.06 ftCombustion Turbine Inlet Filter Width 22.80 ftNumber of Barrier Filters 70 Hours Before Change Out of Barrier Filters 7,500.00 Number of Prefilters 70 Hours Before Change Out of Prefilters 2,500.00 HEAT RECOVERY STEAM GENERATOR DATAHRSG DesignNumber of Heat Recovery Steam Generators (HRSG's) 1 Number of Pressure Levels 2 High Pressure Drum Pinch Point Temp 15.00 FHigh Pressure Steam Drum Approach Temp 20.00 FLow Pressure Drum Pinch Point Temp 15.00 FLow Pressure Steam Drum Approach Temp .00 FHRSG DimensionsHRSG Height 64.00 ftHRSG Length 96.00 ftHRSG Width 29.00 ftDeaeratorDeaerator Type Standalone DeaeratorDeaerator Cond Inlet Perf. Pt. Mass Flow 122,762.04 lb/hDeaerator Cond Inlet Perf. Pt. Pressure 110.00 psiaDeaerator Cond Inlet Perf. Pt. Temperature 60.08 FDeaerator Vent Losses Perf. Pt. Mass Flow 245.52 lb/hDuct BurnersDuct Burner Included YesDuct Burner Primary Fuel Natural GasNumber of Duct Burner Elements 2 Duct Burner Width 29.00 ftDuct Burner Height 34.47 ftDuct Burner Cooling Air Fan Standard Motor Size .33 hp

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SOAPP-CT.25 WorkStation 11/1/00

Equipment ListProject: Sample OutputsConceptual Design: Cogen, 1 x 27 MW, NG, Quarterly

Variable Value UnitsDuct Burner Cooling Air Fan Auxiliary Power .50 kWPUMP DATAHigh Pressure Feed PumpsSparing 1@100%Type Horizontal Split-Cage MulCapacity 351.87 gpmNet Developed Head 1,870.78 ft H2OStandard Motor Size 250.00 hpLow Pressure Feed PumpsSparing 1@100%Type Horizontal Split-CageCapacity 19.83 gpmNet Developed Head 106.90 ft H2OStandard Motor Size 1.00 hpCondensate PumpsSparing 1@100%Type Horizontal Split-CageCapacity 349.37 gpmNet Developed Head 70.07 ft H2OStandard Motor Size 10.00 hpMiscellaneous PumpsPretreatment Backwash Transfer PumpsSparing 2@100%Type VerticalCapacity 9.98 gpmTotal Developed Head 100.00 ft H2OStandard Motor Size .50 hpWaste Water PumpsSparing 2@100%Type Horizontal Split CageCapacity 99.45 gpmTotal Developed Head 200.00 ft H2OStandard Motor Size 10.00 hpWater Treatment System Makeup PumpsSparing 2@100%Type Horizontal Split CageCapacity 342.65 gpmTotal Developed Head 200.00 ft H2OStandard Motor Size 30.00 hpWater Treatment System Raw Water PumpsSparing 1@100%Type VerticalCapacity 967.65 gpmTotal Developed Head 300.00 ft H2OStandard Motor Size 100.00 hpBOP EQUIPMENT DATAInstrument & Station Air CompressorsType Screw

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SOAPP-CT.25 WorkStation 11/1/00

Equipment ListProject: Sample OutputsConceptual Design: Cogen, 1 x 27 MW, NG, Quarterly

Variable Value UnitsNumber 3@50%Capacity 200.00 ft3/min-stdDischarge Pressure 125.00 psigStandard Motor Size 40.00 hpNumber of Receivers 2.00 Volume of Receivers 20.00 ft3Instrument Air Dryers Type DessicantAftercoolers & Moisture Separators Included YesWater Treatment SystemNumber of Parallel Trains 2@100%Water Treatment System Auxiliary Power 61.00 kWTotal Water Treatment System Capacity 18,481.67 gphTANKSTreated Water Storage TankNumber 1 Tank Capacity 277,225.00 galTank Diameter 44.34 ftTank Height 24.00 ftNeutralization Tank and AgitatorNumber 1 Neutralization Tank Capacity 20,354.26 galNeutralization Tank Diameter 16.00 ftNeutralization Tank Height 14.00 ftNumber of Neutralization Tank Agitators 1@100%Neutralization Tank Agitator Standard Motor Size 2.000 hpOil/Water SeparatorsNumber 1 Type Corrugated PlateCapacity 54.60 gpmPIPING DATAFuel Oil PipingNatural Gas PipingPlant Nat Gas Header Pipe Size 12.00 inPlant Nat Gas Header Pipe Schedule 40.00 Plant Nat Gas Header Pipe Length 187.00 ftCT Nat Gas Header Pipe Size 2.00 inCT Nat Gas Header Pipe Schedule 80.00 CT Nat Gas Header Pipe Length 56.00 ftCT Nat Gas Branch Pipe Size 2.00 inCT Nat Gas Branch Pipe Schedule 80.00 CT Nat Gas Branch Pipe Length 38.00 ftHRSG Nat Gas Header Pipe Size 4.00 inHRSG Nat Gas Header Pipe Schedule 40.00 HRSG Nat Gas Header Pipe Length 56.00 ftHRSG Nat Gas Branch Pipe Size 2.00 inHRSG Nat Gas Branch Pipe Schedule 80.00 HRSG Nat Gas Branch Pipe Length 174.00 ftHigh Pressure Steam Piping

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SOAPP-CT.25 WorkStation 11/1/00

Equipment ListProject: Sample OutputsConceptual Design: Cogen, 1 x 27 MW, NG, Quarterly

Variable Value UnitsMass Flow, per HRSG 119,421.65 lb/hPressure at HRSG 549.78 psiaTemperature at HRSG 485.00 FPlant Header Diameter 6.00 inPlant Header Length 56.00 ftPlant Header Material A106 Gr. BPlant Header Thickness .28 inHRSG Leads Diameter 6.00 inHRSG Leads Length 174.00 ftHRSG Leads Material A106 Gr. BHRSG Leads Thickness .28 inHigh Pressure Feedwater PipingHigh Pressure Feedwater Mass Flow, per HRSG 151,816.91 lb/hHigh Pressure Feedwater Pressure 739.44 psiaHigh Pressure Feedwater Temperature 319.93 FHigh Pressure Feedwater Piping Header Diameter 4.00 inHigh Pressure Feedwater Piping Header Length 248.00 ftHigh Pressure Feedwater Piping Header Material A106 Gr. BHigh Pressure Feedwater Piping Header Thickness .24 inHigh Pressure Feedwater Piping Leads Diameter 4.00 inHigh Pressure Feedwater Piping Leads Length 270.00 ftHigh Pressure Feedwater Piping Leads Material A106 Gr. BHigh Pressure Feedwater Piping Leads Thickness .24 inLow Pressure Feedwater PipingLow Pressure Feedwater Mass Flow, per HRSG 6,022.99 lb/hLow Pressure Feedwater Pressure 88.00 psiaLow Pressure Feedwater Temperature 318.69 FLow Pressure Feedwater Piping Header Diameter 4.00 inLow Pressure Feedwater Piping Header Length 248.00 ftLow Pressure Feedwater Piping Header Material A106 Gr. BLow Pressure Feedwater Piping Header Thickness .24 inLow Pressure Feedwater Piping Leads Diameter 4.00 inLow Pressure Feedwater Piping Leads Length 270.00 ftLow Pressure Feedwater Piping Leads Material A106 Gr. BLow Pressure Feedwater Piping Leads Thickness .24 inCondensate PipingCondensate Piping Header Diameter 4.00 inCondensate Piping Header Length 211.00 ftCondensate Piping Header Material A106 Gr. BCondensate Piping Header Thickness .24 inELECTRICAL EQUIPMENT DATAMain Power Transformer - Combustion Turbine 33,000.00 kVAUnit Auxiliary Transformer - Combustion Turbine 1,620.00 kVAUnit Substation Transformer 1,500.00 kVAMain Power Transformer - Combustion Turbine - Quantity 1 Unit Auxiliary Transformer - Combustion Turbine - Quantity 1 Unit Substation Transformer - Combustion Turbine - Quantity 4 Non-segregated Bus Duct - CT MPT to Generator 1,800.00 A

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SOAPP-CT.25 WorkStation 11/1/00

Equipment ListProject: Sample OutputsConceptual Design: Cogen, 1 x 27 MW, NG, Quarterly

Variable Value UnitsNon-segregated Phase Bus Duct - Length 100.00 ftNon-segregated Phase Bus Duct - CT UAT to non-seg bus ducts 300.00 ANon-segregated Phase Bus Duct - Length 150.00 ftNon-segregated Bus Duct 1,800.00 ANon-segregated Bus Duct, Length 84.00 ftCircuit Breaker - CT, Quantity 1 Circuit Breaker - CT Generator 1,400.00 AMedium Voltage Breaker - CT UAT, Quantity 1 Medium Voltage Breaker - CT UAT 300.00 AMedium Voltage Breaker - CT Starter, Quantity 1 Medium Voltage Breaker - CT Starter 120.00 AMedium Voltage Breaker - BFW Pump, Quantity 0 Medium Voltage Breaker - BFW Pump .00 AMedium Voltage Breaker - Unit Substation, Quantity 2 Medium Voltage Breaker - Unit Substation 200.00 ALow Voltage Breaker - Unit Substation, Quantity 2 Low Voltage Breaker - Unit Substation 1,800.00 ALow Voltage Breaker - Bus Coupler, Quantity 1 Low Voltage Breaker - Bus Coupler 1,800.00 ALow Voltage Breaker - Power Centers, Quantity 2 Low Voltage Breaker - Power Centers 500.00 ALow Voltage Breaker - Motor Control Center, Quantity 2 Low Voltage Breaker - Motor Control Center 100.00 ASwitchyard Voltage 115.00 kV

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SOAPP-CT.25 WorkStation 11/1/00

Performance SummaryProject: Sample OutputsConceptual Design: Cogen, 1 x 27 MW, NG, Quarterly

Variable Period #1 Period #2 Period #3 Period #4 UnitsPLANT DESIGN BASISAmbient Air Temperature 57.00 64.00 68.50 59.50 FSite Elevation 600.00 600.00 600.00 600.00 ftCompressor Inlet Air Temperature 57.00 64.00 68.50 59.50 FCompressor Inlet Air Pressure Drop 4.75 4.75 4.75 4.75 in H2OExhaust Gas Pressure Drop 12.50 12.50 12.50 12.50 in H2OCOMBUSTION TURBINE DATANumber of CT's Operating 1 1 1 1 CT Primary Fuel Type Natural Gas Natural Gas Natural Gas Natural GasCT Gross Output per CT 28,939.02 27,813.27 27,185.09 28,442.98 kWCT Gross Heat Rate (LHV) 9,268.00 9,338.77 9,380.32 9,297.22 Btu/kWhCT Heat Input - HHV 297.71 288.31 283.06 293.53 MBtu/hCT Fuel Flow Rate (LHV) per CT 14,116.14 13,670.61 13,421.31 13,917.93 lb/hCT Exhaust Flow per CT 665,765.75 648,005.94 638,045.69 657,969.88 lb/hCT Exhaust Temperature 909.20 911.03 912.05 910.02 FCT NOx Emissions 25.00 25.00 25.00 25.00 ppmvd @ 15% O2HRSG DATAHP Steam Flow per HRSG 119,421.65 118,966.34 119,202.56 118,033.80 lb/hHP Steam Pressure at HRSG 549.78 549.78 549.78 549.78 psiaHP Steam Temperature at HRSG 485.00 485.00 485.00 485.00 FHP Steam Enthalpy at HRSG 1,211.33 1,211.33 1,211.33 1,211.33 Btu/lbDB Primary Fuel Type Natural Gas Natural Gas Natural Gas Natural GasDB Status In Use In Use In Use In UseDB Heat Input - HHV 43.05 44.49 47.18 43.78 MBtu/hDB Fuel Flow (LHV) 2,041.03 2,109.74 2,236.87 2,076.07 lb/hStack Exhaust Flow 667,806.75 650,115.69 640,282.56 660,045.94 lb/hStack Exhaust Temperature 333.69 333.69 333.69 333.69 FPLANT DATAGross Output 28,939.02 27,813.27 27,185.09 28,442.98 kWAuxiliary Power 672.12 672.12 672.12 672.12 kWNet Output 28,266.90 27,141.15 26,512.97 27,770.86 kWTotal Plant Heat Input - HHV 340.75 332.81 330.23 337.31 MBtu/hNet Plant Process Heat Rate (HHV) at 100% Load 4,822.00 4,797.00 4,798.00 4,841.00 Btu/kWhNet Plant Process Heat Rate (LHV) at 100% Load 4,344.00 4,322.00 4,322.00 4,362.00 Btu/kWhNet Plant Electric Heat Rate (HHV) at 100% Load 12,055.00 12,262.00 12,455.00 12,146.00 Btu/kWhNet Plant Electric Heat Rate (LHV) at 100% Load 10,860.00 11,047.00 11,221.00 10,943.00 Btu/kWh

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SOAPP-CT.25 WorkStation 11/1/00

Emissions SummaryProject: Sample OutputsConceptual Design: Cogen, 1 x 27 MW, NG, Quarterly

Variable Value UnitsPLANT DESIGN BASISCycle Type CogenerationNumber of Combustion Turbines 1 Number of HRSG's 1 Primary Fuel Type Natural GasCT NOx Control Type - Primary Fuel Water InjectionDuct Burner YesBypass Stack YesAIR EMISSIONS - HEAT RECOVERY STEAM GENERATORSFiring Primary FuelCO2 mass flow per HRSG stack 47,661.50 lb/hCO mass flow per HRSG stack 54.57 lb/hNOx (as NO2) mass flow per HRSG stack 38.91 lb/hNH3 mass flow per HRSG stack .00 lb/hSO2 mass flow per HRSG stack .00 lb/hCO concentration 64.54 ppmvd @ 15% O2NOx concentration 42.95 ppmvd @ 15% O2NH3 concentration .00 ppmvd @ 15% O2SO2 concentration .00 ppmvd @ 15% O2Volumetric Flow Rate per HRSG stack 270,383.06 ft3/min-actCO2 mass flow total plant 47,661.50 lb/hCO mass flow total plant 54.57 lb/hNOx (as NO2) mass flow total plant 38.91 lb/hNH3 mass flow total plant .00 lb/hSO2 mass flow total plant .00 lb/hAIR EMISSIONS - BYPASS STACKS - IN BYPASS MODEFiring Primary FuelCO2 mass flow per Bypass stack 42,015.79 lb/hCO mass flow per Bypass stack 49.53 lb/hNOx (as NO2) mass flow per Bypass stack 21.06 lb/hSO2 mass flow per Bypass stack .00 lb/hCO concentration 63.00 ppmvd @ 15% O2NOx concentration 25.00 ppmvd @ 15% O2SO2 concentration .00 ppmvd @ 15% O2Volumetric Flow Rate per Bypass stack 459,410.03 ft3/min-actCO2 mass flow total plant 42,015.79 lb/hCO mass flow total plant 49.53 lb/hNOx (as NO2) mass flow total plant 21.06 lb/hSO2 mass flow total plant .00 lb/hLIQUID DISCHARGESRaw Cycle Water Make-up Average Flow 342.65 gpmRaw Cycle Water Make-up Peak Flow 308.43 gpmPretreatment Waste Average Flow 8.98 gpmPretreatment Waste Peak Flow 9.98 gpmPretreatment Outlet Average Flow 299.45 gpmPretreatment Outlet Peak Flow 332.67 gpmDemineralizer Waste Average Flow 22.18 gpmDemineralizer Waste Peak Flow 24.64 gpm

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SOAPP-CT.25 WorkStation 11/1/00

Emissions SummaryProject: Sample OutputsConceptual Design: Cogen, 1 x 27 MW, NG, Quarterly

Variable Value UnitsDemineralizer Outlet Average Flow 277.26 gpmDemineralizer Outlet Peak Flow 308.03 gpmEvaporative Cooler Make-up Average Flow .00 gpmEvaporative Cooler Make-up Peak Flow .00 gpmCT Water Injection Average Flow 31.58 gpmCT Water Injection Peak Flow 33.68 gpmSteam Cycle Make-up Average Flow 245.68 gpmSteam Cycle Make-up Peak Flow 274.35 gpmSteam Export Average Flow 238.84 gpmSteam Export Peak Flow 264.09 gpmCT Steam Injection Average Flow .00 gpmCT Steam Injection Peak Flow .00 gpmSteam Cycle Blowdown Average Flow 6.84 gpmSteam Cycle Blowdown Peak Flow 10.26 gpmFire Water Supply Average Flow .00 gpmFire Water Supply Peak Flow 1,250.00 gpmTotal Waste Water Discharge Average Flow 38.67 gpmTotal Waste Water Discharge Peak Flow 99.45 gpmSettling Basin Discharge Average Flow 38.67 gpmSettling Basin Discharge Peak Flow 99.45 gpmTransformer and Switchyard Area Runoff Average Flow .66 gpmTransformer and Switchyard Area Runoff Peak Flow 54.57 gpmFuel Oil Area Runoff Average Flow .00 gpmFuel Oil Area Runoff Peak Flow .00 gpm

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SOAPP-CT.25 WorkStation 11/1/00

Motor List/Aux PowerProject: Sample OutputsConceptual Design: Cogen, 1 x 27 MW, NG, Quarterly

System / Component Number Design hp Each Number Operating Operating Auxiliary Power (kW)CONDENSATE/FEEDWATER SYSTEMCondensate Pumps 1@100% 10.000 1 6.85High Pressure Feedwater Pumps 1@100% 250.000 1 182.58Low Pressure Feedwater Pumps 1@100% 1.000 1 .67WATER TREATMENT SYSTEMWater Treatment System N/A N/A N/A 61.00Raw Water Pumps 1@100% 100.000 1 25.99Water Treatment Make-up Pumps 2@100% 30.000 1 17.33Pretreatment Backwash Pumps 2@100% .500 1 .32Waste Water Pumps 2@100% 10.000 1 2.43Waste Water Neutralization Tank Agitator 1@100% 2.000 1 1.14BALANCE OF PLANT EQUIPMENTStation Air Compressors 3@50% 40.000 2 51.62Bypass Stack/Diverter Valve Seal Air Fans 1 10.000 1 7.00Service Water Pump 2@100% 15.000 1 11.19OTHER LOSSESCombustion Turbine Auxiliaries N/A N/A N/A 126.00Transformer Losses N/A N/A N/A 113.00Miscellaneous Auxiliaries N/A N/A N/A 65.00Total Auxiliary Power Consumption 672.12

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SOAPP-CT.25 WorkStation 11/1/00

Site Parameters ListProject: Sample OutputsConceptual Design: Cogen, 1 x 27 MW, NG, Quarterly

Variable Length (x-dir) (ft) Width (y-dir) (ft) Height (z-dir) (ft) Perimeter(ft) Surface Area(sq ft)Site Entrance 10.00 20.00 .00 60.00 200.00Parking 115.00 115.70 .00 461.40 13,305.00Control Building 60.00 90.00 40.00 300.00 5,400.00Maintenance Building 60.00 90.00 20.00 300.00 5,400.00Combustion Turbine Bay 76.00 56.00 34.00 264.00 4,256.00Rack Connection 25.00 10.00 10.00 70.00 250.00Transformers 60.00 56.00 .00 232.00 3,360.00Bypass Stack/Diverter valve 1 13.00 11.00 15.00 48.00 143.00Exhaust Ductwork 1 40.00 7.00 20.00 94.00 280.00Heat Recovery Steam Generator 1 96.00 29.00 64.00 250.00 2,784.00Main Stack 1 9.78 9.78 80.00 39.11 96.00Standard Deaerator 18.00 15.00 71.00 66.00 270.00Water Treatment 77.28 80.40 20.00 315.36 6,213.00Waste Neutralization Tank 16.00 16.00 14.00 64.00 256.00Treated Water Tank 44.34 44.34 24.00 177.37 1,966.00Site Boundry 319.78 311.70 .00 1,262.96 99,675.00Natural Gas Interface 10.00 10.00 8.00 40.00 100.00Steam Interface 10.00 10.00 8.00 40.00 100.00

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SOAPP-CT.25 WorkStation 11/1/00

Site Parameters ListProject: Sample OutputsConceptual Design: Cogen, 1 x 27 MW, NG, Quarterly

Variable Volume(cu ft)Site Entrance .00Parking .00Control Building 216,000.00Maintenance Building 108,000.00Combustion Turbine Bay 144,704.00Rack Connection 2,500.00Transformers .00Bypass Stack/Diverter valve 1 2,145.00Exhaust Ductwork 1 5,600.00Heat Recovery Steam Generator 1 178,176.00Main Stack 1 7,649.00Standard Deaerator 19,170.00Water Treatment 124,270.00Waste Neutralization Tank 3,584.00Treated Water Tank 47,189.00Site Boundry .00Natural Gas Interface 800.00Steam Interface 800.00

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