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[null,"Capital Costs for SCR and Water Injection on the Simple Cycle Gas Turbines (EU IDs 1 and 2)"]
[]
[null,null,null,null,null,null,null,null,null,"Shaded cells indicate user inputs."]
[null,"Total Capital Investment Determination - Water Injection + SCR",null,null,null,null,null,null,null,"Date:"]
[null,"Project: ",null,"GVEA Zehnder PM2.5 BACT Analysis - Frame 5 CTs (EU ID 1 and 2, cost per turbine)",null,null,null,null,null,"Prepared By:"]
[null,null,null,null,null,null,null,null,null,"Checked By:"]
[null,"*Notes regarding pertinent cost information and cost exclusion reasoning is included on the separate footnote reference page.",null,null,null,null,null,null,null,"Rev:"]
[null,"Capital Costs"]
[null,"DIRECT COSTS",null,null,"QTY","UNIT","UNIT COST"," TOTAL MATERIALS COST"," TOTAL LABOR COST"]
[]
[null,"(1)","Purchased equipment and material costs"]
[null,null,"(a)","Basic equipment"]
[null,null,null,"Water Injection1",1,"EA",1250000,{"$f":"E13*G13","v":1250000}]
[null,null,null,"SCR2,3",1,"EA",3000000,{"$f":"E14*G14","v":3000000}]
[null,null,null,"Reagent Prep/Water Treatment/Structure",1,"EA",{"$f":"4387000/2","v":2193500},{"$f":"E15*G15","v":2193500},null,"TOTAL =",{"$f":"SUM(H13:H15)","v":6443500}]
[]
[null,null,"(b)","Instrumentation"]
[null,null,null,"Total Instrumentation4",null,"EA",null,{"$f":"E18*G18","v":0}]
[null,null,null,null,null,null,null,null,null,"TOTAL =",{"$f":"SUM(H18:H18)","v":0}]
[null,null,"(c)","Freight"]
[null,null,null,"Injection System Freight",null,"% MATL COST",null,null,{"$f":"G21*H13","v":0}]
[null,null,null,null,null,null,null,null,null,"TOTAL =",{"$f":"SUM(I21:I21)","v":0}]
[null,null,"(d)","Labor"]
[null,null,null,"Labor - offsite fab",null,"MH",null,null,{"$f":"E24*G24","v":0}]
[null,null,null,"Labor - onsite",null,"MH",null,null,{"$f":"E25*G25","v":0}]
[]
[null,null,"(e )","Startup Spares"]
[null,null,null,"Startup Spare Parts for SCR",5.0000000000000001E-3,"%",null,{"$f":"E28*G14","v":15000}]
[null,null,null,null,null,null,null,null,null,"TOTAL =",{"$f":"H28","v":15000}]
[null,null,"(f)","Vendor representatives fees"]
[null,null,null,"Fab Site Vendor Representatives fees (enter no. of days and daily rate)",10,"Days",1800,null,{"$f":"G31*E31","v":18000}]
[null,null,null,"Onsite Vendor Representatives fees (enter no. of days and daily rate)",8,"Days",2500,null,{"$f":"G32*E32","v":20000}]
[null,null,null,null,null,null,null,null,null,"TOTAL =",{"$f":"SUM(I31:I32)","v":38000}]
[null,"Purchased Equipment and Material Cost (PEMC)",null,null,"All above costs included in vendor scope except SCR spares and SCR vendor rep. fees",null,null,null,null," PEMC   =",{"$f":"SUM(K15:K33)","v":6496500}]
[]
[null,"(2)","Direct Installation Costs5,6"]
[null,null,"(a)","Concrete",null,"CY",null,{"$f":"E37*G37","v":0},null,null,{"$f":"H37+I37","v":0}]
[null,null,"(b)","Piling",null,"TON",null,0,null,null,0]
[null,null,"(c)","Structural steel",null,"TON",null,0,null,null,0]
[null,null,"(d)","Electrical",null,"LOT",null,0,null,null,0]
[null,null,"(e )","Painting",null,"SF",null,0,null,null,0]
[null,null,"(f)","Insulation",null,"LOT",null,0,null,null,0]
[null,null,"(g)","Abovegrade piping",null,"LF",null,0,null,null,0]
[null,null,"(h)","Functional Checkouts"]
[null,null,null,"Functional Checkout  - fab site, enter %:",null,"% offsite fab labor",null,null,{"$f":"G45*I24","v":0},null,{"$f":"H45+I45","v":0}]
[null,null,null,"Functional Checkout - onsite, enter %",null,"% onsite fab labor",null,null,{"$f":"G46*I25","v":0},null,{"$f":"H46+I46","v":0}]
[null,null,null,"Contractor Commissioning, enter %:",null,"% of equipment  total cost",null,null,{"$f":"G47*K15","v":0},null,{"$f":"H47+I47","v":0}]
[null,"Direct Installation Costs (DIC)",null,null,null,null,null,null,null," DIC   =",{"$f":"H13+(H14*2)","v":7250000}]
[]
[]
[null,"Total Direct Costs (TDC)",null,null,null,null,null,null,null,"TDC = (PEMC) + (DIC)  =",{"$f":"K34+K48","v":13746500}]
[]
[]
[null,"INDIRECT COSTS"]
[null,"(3)","Engineering, Procurement & Construction Support Services",null,0.22,"% TDC",null,null,{"$f":"E55*K51","v":3024230}]
[null,"(4)","Performance tests",null,1,"EA",10000,null,{"$f":"E56*G56","v":10000}]
[null,"Total Indirect Costs (TIC)",null,null,null,null,null,null,null,"TIC   =",{"$f":"SUM(I55:I56)","v":3034230}]
[]
[]
[null,"MANAGEMENT AND CONTINGENCY COSTS"]
[null,"(5)","Unit Operator Costs7",null,null,"% TDC",null,null,null,null,"Excluded in this estimate."]
[null,"(6)","Contingency",null,0.3,"% PEMC",null,null,{"$f":"E62*K34","v":1948950}]
[null,"Total Management and Contingency Costs (TM&CC)",null,null,null,null,null,null,null,"TM & CC   =   ",{"$f":"SUM(I61:I62)","v":1948950}]
[]
[]
[null,"TOTAL CAPITAL INVESTMENT (TCI)",null,null,null,null,null,null,null,"TCI  =  (TDC)+(TIC)+(TM&CC)  = ",{"$f":"K51+K57+K63","v":18729680}]
[]
[null,"Footnotes:"]
[null,1,"For the water injection option, costs have been included for a water treatment system. Zehnder does not have any water treatment system, thus would need reverse osmosis, electro de-ionization, storage tanks, small pumps, and interconnecting piping. It is unlikely this equipment and reagent preparation equipment would fit inside the existing turbine building as it is all essential for normal maintenance and operation.  "]
[null,2,"Source of SCR Capital Costs: ATCO Emissions Management. These were supply-only costs given in a range for the Frame 5s. The highpoint of the range provided ($2 – $3 million) was used."]
[null,3,"Costs for reagent prep equipment and additional structures are discussed in a separately submitted CBI package."]
[null,4,"Continuous emissions monitoring system is included in capital costs under Reagent Prep/Water Treatment/Structure."]
[null,5,"Construction costs associated directly with SCR installation were conservatively estimated at double the capital cost. This seems reasonable given the current footprint of the turbine building. Additional structure costs were included under part (1)(a) This should be viewed as an engineering estimate only."]
[null,6,"Construction costs associated directly with water injection installation was conservatively estimated at half the capital cost. This is based on the assumption that some water treatment system work in addition to SCR treated water needs will be required to add water injection. This should be viewed as an engineering estimate only."]
[null,7,"Unit operator costs were excluded as these costs were not specified in vendor quotes and/or appropriate literature."]
[null,8,"Annual direct cost for SCR power consumption were excluded as vendor quotes did not specify system power requirements. However the reagent solutions will require continual heating to keep them in liquid form and a notable station load compared to the unit actual operation is expected."]

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[null,"SCR and Water Injection on the Simple Cycle Gas Turbines (EU IDs 1 and 2)"]
[]
[null,null,null,null,null,null,null,null,"Shaded cells indicate user inputs"]
[null,"Cost Effectiveness Determination - Water Injection + SCR",null,null,null,null,null,null,null,"Date:"]
[null,"Project:  ",null,"GVEA Zehnder PM2.5 BACT Analysis - Frame 5 CTs (EU ID 1 and 2, cost per turbine)",null,null,null,null,null,"Prepared By:"]
[null,null,null,null,null,null,null,null,null,"Checked By:"]
[null,"*Notes regarding pertinent cost information and cost exclusion reasoning is included on the separate footnote reference page.",null,null,null,null,null,null,null,"Rev:"]
[null,"Annualized Costs"]
[null,"DIRECT ANNUAL COSTS",null,null,"QTY","UNIT","UNIT COST"," TOTAL MATERIALS COST"," TOTAL LABOR COST",null,"TOTAL"]
[null,"(1)","Operating Labor",null,{"$f":"E13*2","v":730},"MH",105,null,{"$f":"E10*G10","v":76650},null,{"$f":"I10","v":76650}]
[null,"(2)","Supervisory Labor",null,183,"MH",125,null,{"$f":"E11*G11","v":22875},null,{"$f":"I11","v":22875}]
[null,"(3)","Maintenance Labor (water treatment)",null,{"$f":"E16*1.29","v":13950.832279367751},"1000 GALS",{"$f":"0.7*(1.05^25)","v":2.37044845862957},null,{"$f":"E12*G12","v":33069.728873226937},null,{"$f":"I12","v":33069.728873226937}]
[null,"(4)","Maintenance Labor (SCR system)",null,{"$f":"365*E55/100","v":365},"MH",105,null,{"$f":"E13*G13","v":38325},null,{"$f":"I13","v":38325}]
[null,"(5)","Maintenance Materials",null,null,"LOT",null,{"$f":"E14*G14","v":0},"Included in water treatment below",null,{"$f":"H14","v":0}]
[null,"(6)","Utilities"]
[null,null,"a)","Water Use:",{"$f":"E18*0.73*7.21/(8.34*1000)","v":10814.598666176551},"1000 GALS",{"$f":"0.384*(1.05^25)","v":1.3003602973053643},{"$f":"E16*G16","v":14062.874736787537},null,null,{"$f":"H16","v":14062.874736787537}]
[null,null,"b)","Water Pump Energy:",{"$f":"23.8*0.161*8760","v":33566.567999999999},"kWh",0.18,{"$f":"E17*G17","v":6041.9822399999994},null,null,{"$f":"H17","v":6041.9822399999994}]
[null,null,"c)","CT Fuel Use:",{"$f":"268/137*1000*8760","v":17136350.364963505},"GALS"]
[null,null,"d)","Fuel Penalty:",{"$f":"E18*0.035*0.73","v":437833.75182481762},"GALS",1.7,{"$f":"E19*G19","v":744317.37810218998},null,null,{"$f":"H19","v":744317.37810218998}]
[null,null,"e)","Water Treatment Capacity:",{"$f":"E16*1.3*1.29","v":18136.081963178076},"1000 GALS",{"$f":"1.97*(1.05^25)","v":6.6711192335717904},{"$f":"E20*G20","v":120987.9652061917},null,null,{"$f":"H20","v":120987.9652061917}]
[null,null,"f)","Water Waste Disposal:",{"$f":"E20*0.29","v":5259.4637693216418},"1000 GALS",{"$f":"3.82*(1.05^25)","v":12.935875874235654},{"$f":"E21*G21","v":68035.770484984343},null,null,{"$f":"H21","v":68035.770484984343}]
[null,null,"g)","Urea/DEF:",{"$f":"(929.7-795.4)*(60)*2*2.2/2000","v":17.72760000000001},"TON",356,{"$f":"E22*G22","v":6311.0256000000036},null,null,{"$f":"H22","v":6311.0256000000036}]
[null,null,"h)","SCR Energy Use8:",null,"kWh",0.18,"Excluded in this estimate.",null,null,{"$f":"G23*E23","v":0}]
[null,"(7)","Catalyst Replacement Costs (every 3 years)"]
[null,null,"(a)","Replacement of SCR Catalyst: % of total equipment cost",0.3,"% total equip ",{"$f":"'SCR+Water Injection TCI'!G14","v":3000000},{"$f":"G25*E25","v":900000},null,null,{"$f":"H25*E30","v":279946.49911350262}]
[null,null,"(b)","Replacement labor for SCR Catalyst",180,"MH",105,null,{"$f":"E26*G26","v":18900},null,{"$f":"I26*E30","v":5878.8764813835551}]
[null,null,"(c)","Transport cost direct to site (SCR catalyst)",0.13,"% replacement",null,null,{"$f":"E27*(H25)","v":117000},null,{"$f":"I27*E30","v":36393.044884755342}]
[null,null,"(d)","Transport cost for spent SCR catalyst",0.13,"% replacement",null,null,{"$f":"E28*H25","v":117000},null,{"$f":"I28*E30","v":36393.044884755342}]
[]
[null,"Sinking Fund Factor  [see inputs below]:",null,null,{"$f":"($E$52/100)/(POWER(1+($E$52/100),($E$54)/($E$55/100))-1)","v":0.31105166568166959}]
[]
[null,"Total Direct Annual Costs (TDAC)",null,null,null,null,null,null,null," TDAC   =",{"$f":"SUM(K10:K31)","v":1489288.1906077773}]
[]
[null,"INDIRECT ANNUAL COSTS"]
[null,"(8)","Overhead",null,0.3,"% WT Labor",null,null,{"$f":"E35*I12","v":9920.9186619680804},null,{"$f":"I35","v":9920.9186619680804}]
[null,"(9)","Administrative Charges, Property Taxes, Insurance",null,0.04,"% total capital",null,null,{"$f":"E36*'SCR+Water Injection TCI'!K66","v":749187.20000000007},null,{"$f":"I36","v":749187.20000000007}]
[null,null,"Capital Recovery Factor [see inputs below]",null,{"$f":"($E$52/100*POWER((1+($E$52/100)),$E$53))/((POWER(((1+$E$52/100)),$E$53))-1)","v":9.4392925743255696E-2}]
[null,"(10)","Capital Recovery",null,null,null,null,null,null,"CRF * TCI  = ",{"$f":"E37*'SCR+Water Injection TCI'!K66","v":1767949.2934349414}]
[]
[null,"Total Indirect Annual Costs (TIAC)",null,null,null,null,null,null,null," TIAC   =",{"$f":"SUM(K33:K38)","v":2527057.4120969097}]
[]
[null,"TOTAL ANNUALIZED COSTS (TAC)",null,null,null,null,null,null,null,"TAC = (TDAC) + (TIAC)  =",{"$f":"K32+K40","v":4016345.602704687}]
[]
[null,"Cost Effectiveness Summary"]
[]
[null,"TOTAL TONS NOx AVOIDED PER YEAR",null,null,null,null,null,null,null,"=",{"$f":"1033*0.95","v":981.34999999999991}]
[]
[null,"COST EFFECTIVENESS ($ PER TON AVOIDED)",null,null,null,null,null,null,null,"(TAC)/(TPY)   = ",{"$f":"K42/K46","v":4092.673972287856}]
[]
[]
[null,null,null,"Data Inputs for Capital Recovery Factor:"]
[null,null,null,"Annual Interest Rate (EPA OAQPS Control Cost Manual) ",7,"%"]
[null,null,null,"Project Life (EPA OAQPS Control Cost Manual) ",20,"years"]
[null,null,null,"Catalyst Life ",3,"years"]
[null,null,null,"Asset Utilization",100,"%"]
[]
[null,"Footnotes:"]
[null,1,"For the water injection option, costs have been included for a water treatment system. Zehnder does not have any water treatment system, thus would need reverse osmosis, electro de-ionization, storage tanks, small pumps, and interconnecting piping. It is unlikely this equipment and reagent preparation equipment would fit inside the existing turbine building as it is all essential for normal maintenance and operation.  "]
[null,2,"Source of SCR Capital Costs: ATCO Emissions Management. These were supply-only costs given in a range for the Frame 5s. The highpoint of the range provided ($2 – $3 million) was used."]
[null,3,"Costs for reagent prep equipment and additional structures are discussed in a separately submitted CBI package."]
[null,4,"Continuous emissions monitoring system is included in capital costs under Reagent Prep/Water Treatment/Structure."]
[null,5,"Construction costs associated directly with SCR installation were conservatively estimated at double the capital cost. This seems reasonable given the current footprint of the turbine building. Additional structure costs were included under part (1)(a) This should be viewed as an engineering estimate only."]
[null,6,"Construction costs associated directly with water injection installation was conservatively estimated at half the capital cost. This is based on the assumption that some water treatment system work in addition to SCR treated water needs will be required to add water injection. This should be viewed as an engineering estimate only."]
[null,7,"Unit operator costs were excluded as these costs were not specified in vendor quotes and/or appropriate literature."]
[null,8,"Annual direct cost for SCR power consumption were excluded as vendor quotes did not specify system power requirements. However the reagent solutions will require continual heating to keep them in liquid form and a notable station load compared to the unit actual operation is expected."]