{"text_format":"1","workbook":"xlsx","n_sheets":5,"sheets":["Help","CCSbench","Calc","Sankey","Maps"],"not_rendered":{"charts":7,"images":13,"macros":1,"external_links":0,"defined_names":30,"comments":3,"pivot_tables":0},"unopened":[],"bounds":{"document_bytes":16777216,"sheet_cells":100000,"rows_first":2000,"rows_last":500,"rows_between":2000,"halvings":0,"cell_chars":16384,"cell_head_chars":4096},"cells_cut":0,"cells_raw":0,"read":"whole","date_system":"1900"}

{"sheet":"Help","index":0,"n_rows":26,"n_cols":3,"rows_kept":26,"cut":false,"hidden":false,"merged":[[25,1,25,2],[23,1,23,2],[15,1,15,2],[16,1,16,2],[5,1,5,2],[9,1,9,2],[10,1,10,2],[14,1,14,2],[22,1,22,2]]}
[]
[null,"CCS economic benchmarking"]
[]
[null,"Expected inputs"]
[]
[null,"The expected inputs from the user are in red. The related cells can be modified by the user, while all other cells are protected."]
[null,null,"* The type of carbon capture approach: post-combustion, oxy-combustion, or Ca-looping (which shares elements of post-combustion and oxy-combustion capture techniques).\n* The heat duty per unit mass of CO2 captured provided by steam bled from the turbine qCO2,capt (in MJth/kgCO2,capt) and the steam extraction pressure pbl.\n* The electric energy consumption of the CO2 separation technology per unit mass of CO2 wCO2,capt (in MJe/kgCO2,capt) excluding CO2 compression (e.g., solvent pumps, vacuum compressors, air separation unit, chillers).\n* The fraction ξ of the electric power consumed for CO2 capture that is released to the ambient environment through the plant cooling system. Values can range from 0% (for example for ID fans working on exhaust gases, where electric power is transferred to the flue gas emitted at the stack) to close to 100% (for example for intercooled compressors and solvent pumps, where electric power is almost totally transferred to the fluid and then released to the environment through the cooling water circuit).\n* The fraction of the total (thermal and electrical) energy input to the capture system that can be recovered by the steam cycle as low temperature heat and the expected heat recovery efficiency\n* The expected reduction in net electric efficiency of the plant compared to the efficiency of the benchmark plant without CO2 capture. If this value is not known, it can be estimated by the simplified mass and energy balance calculation by pressing the button \"Δη ESTIMATE\".\n* The carbon capture ratio (CCR).\n* The pressure at which the CO2 is delivered from the capture unit prior to final compression (pCO2) and its purity (xCO2).\n* The Capacity Factor, i.e. the ratio between the actual yearly electric energy production and the maximum theoretical energy produced with the nominal power output for 8760 hours per year."]
[null,null,"An estimate of the CAPEX and OPEX costs of the novel capture system may be provided in input to graphically show the position of the technology on the Capex-Opex chart with respect to the breakeven line. However, these data are not needed for the cost estimate."]
[null,null,"A components mapping section allows to exclude some components from the cost estimate of the well-established technologies section.\nIf YES is selected, the component cost is scaled according to the estimated mass and energy balance and included into the plant cost analysis.\nIf NO is selected (for instance, if the main boiler is totally substituted by the capture system), the component is not included in the cost estimation of the conventional components, but it has to be charged on the CAPEX/OPEX of the novel system."]
[null,"In the \"Calc\" sheet, the reference costs of the benchamark plants (with and without carbon capture) are listed and can be changed if a different economic framework has to be assumed as reference. In order to obtain a reliable estimate, please modify the energy and cost reference using consistent datasets."]
[null,"In the \"Maps\" sheet, the CO2 compressor consumption and the turbine gross power loss curves can be modified. The first gives the electric consumption of the CO2 compressor as a function of inlet pressure and purity, assuming that no further purification of the CO2 from incondensable gases is needed. The latter provides the electric energy loss as function of tne steam bleeding pressure."]
[]
[null,"Run the simulation"]
[]
[null,"If the efficiency penalty value is not available from process simulations, it can be estimated by the simplified mass and energy balance calculation by pressing the button \"Δη ESTIMATE\". The estimated mass and energy balances are graphically shown in the \"Sankey\" worksheet. A message in the \"Status\" section recalls wether the efficiency is estimated with the simplified H&M balance or if it is provided in input by the user."]
[null,"Once the inputs have been provided, the simulation can be run using the button \"Evaluate cost\".\n\n\n"]
[null,"The \"Evaluate costs\" button runs the model and prints the results for the specified input. The STATUS section provides an indication of the status of the results. \nThe first line indicates if the problem has been run after any change of the input values. \nThe second line provides information on the energy balance calculation:\n* \"Efficiency set by user\": the efficiency is provided by the user in the input section and gives a reasonable energy balance\n* \"Efficiency estimated by simplified H&M balance\": the estimated efficiency value is used and the energy balance is reasonable\n* \"WARNING\": an inconsistency in the energy balance is calculated, based on the estimation of the simplified model. Additional heat provided from an external source or additional losses must be assumed to close the balance. The user should increase (if \"heat recovery higher than consumption\" message) or reduce (if \"negative heat recovery\" message) the input efficiency penalty."]
[]
[null,"Results"]
[]
[null,null,"The first section of results provides the details of the additional consumptions due to the presence of the carbon capture section:\n* Expected CO2 compressor consumption (according to the curve in the \"Maps\" sheet)\n* The total electric consumption of the capture system (i.e. CO2 separation + CO2 compression)\n* The equivalent electricity loss per unit of thermal energy provided to the capture system by the steam bled from the turbine\n* The total equivalent electric consumption, which is the sum of the total electric consumption and the electric power output lost due to steam bleeding from the turbine\n* The ratio between the actual electricity consumption and the equivalent electric consumption of the CO2 capture technology\n* The actual net efficiency loss used in calculations\n"]
[null,null,"Cost estimates are reported in terms of breakeven CAPEX and OPEX, specific to the flow rate CO2 captured and to the nominal plant power output. CAPEX at null OPEX and OPEX at null CAPEX are also provided, which represent the intercepts of the breakeven line with the axes."]
[null,"In the graphs, the foreseen cost of the capture plant provided as input by the user are shown as red dots (with and without compressor cost included). The yellow line shows the breakeven line, considering the actual input data. Below this line, the technology is competitive with the benchmark (same cost of CO2 avoided). \nThe black lines show how the breakeven line would change if the same equivalent energy consumption of the CCS technology (i.e. the same efficiency penalty) were due to electric consumptions only or heat consumptions only (apart from CO2 compression consumption). The last graphs show the impact of equivalent electric consumption (and how it is shared between electricity and heat) on the efficiency loss, as well as the actual evaluated parameters for the CO2 compression and the steam turbine loss due to bleeding on the respective curves. "]
[null,"Additional graphs in the \"Maps\" sheet show a sensitivity analysis on the breakeven costs obtained by varying the efficiency loss and the equivalent electric consumption. The button \"Rebuild CAPEX/OPEX maps\" can be used to update the sensitivity analysis."]
[]
[null,"This work is licensed under the Creative Commons Attribution 4.0 International License. To view a copy of this license, visit http://creativecommons.org/licenses/by/4.0/ or send a letter to Creative Commons, PO Box 1866, Mountain View, CA 94042, USA."]

{"sheet":"CCSbench","index":1,"n_rows":78,"n_cols":16,"rows_kept":78,"cut":false,"hidden":false,"merged":[[7,1,9,1],[20,1,21,1],[60,14,60,15],[48,14,48,15],[3,1,3,5],[5,1,5,5],[29,1,29,5],[5,7,5,10],[15,7,15,10],[1,7,3,10]]}
[]
[null,"CCS economic benchmarking",null,null,null,"Version: 1.0",null,"This model is described and has been used in: \nG. Guandalini, M.C. Romano, M. Ho, D. Wiley, E.S. Rubin, J.C. Abanades, \"A sequential approach for the economic evaluation of new CO2 capture technologies for power plants\". International Journal of Greenhouse Gas Control, 2019.\nDOI: https://doi.org/10.​1016/​j.​ijggc.​2019.​03.​006\n\nRed values represent the model inputs to be changed by the user"]
[]
[null,"Authors: Giulio Guandalini, Matteo C. Romano\nPolitecnico di Milano, Department of Energy, Group of Energy Conversion Systems"]
[]
[null,"DATA",null,null,null,null,null,"Components mapping (cost)"]
[]
[null,"Capture system \nconsumptions","Type","POST",null,"Oxycombustion/Pre/Post-combustion",null,"Component","Included?"]
[null,null,"q CO2,capt",2000,"MJ/tonCO2","Heat consumed by the capture process",null,"Main Boiler","YES"]
[null,null,"@ pbl",5.0999999999999996,"bar","Steam pressure required by the capture process",null,"Equivalent oxy boiler for CaL","YES"]
[null,null,"w CO2,capt",120,"MJ/tonCO2","Electricity consumed by the capture process (without final CO2 compression)",null,"FGD","YES"]
[null,null,"@ cooling (ξ)",0.95,null,"Fraction of electricity dissipated by cooling system",null,"Other flue gas cleaning equipm.","YES","(e.g. SCR, filters)"]
[null,null,"q CO2,rec",0,null,"Fraction of low termperature heat recovered from capture system"]
[null,null,"ηC,LT",0.13,null,"Low temperature heat recovery efficiency"]
[null,null,"pCO2",2,"bar","Outlet pressure of pure CO2 at final intercooled compression inlet"]
[null,null,"Purity (xCO2)",1,null,"CO2 purity before compression",null,"Other specific parameters"]
[null,null,"Δη exp",7.176802064060428E-2,null,"Expected LHV efficiency reduction",null,"Coal to main boiler (CaL only)",1,null,"% of coal to the air combustion boiler"]
[null,null,"CCR",0.9,null,"Carbon capture ratio"]
[null,null,"CF",0.85,null,"Plant capacity factor"]
[]
[null,"Capture system: \nknown costs","CAPEX",1500,"k$/kgCO2/s","Capital cost of CCS technology (without final CO2 compression)"]
[null,null,"OPEX",15,"$/tonCO2","Operation cost of CCS technology (without final CO2 compression)"]
[]
[null,"Economics","CCF",0.10879999999999999,"%/y","Currency USD 2011",null,"Reference net plant output",550,"MWel"]
[]
[null,null,null,null,"STATUS","Run completed correctly",null,"ASU consumption per unit O2 produced",null,200,"kWhel/tonO2"]
[null,null,null,null,null,{"$f":"Calc!K16","v":"Efficiency estimated by simplified H&M balance"},null,"ASU consumption per unit CO2 captured",null,{"$f":"J26*3.6*2.41956/(Calc!C12*Calc!C9/1000)/CCRinp*IF(D8=\"Ca-L\",(1-I17),1)","v":828.58646136573259},"MJel/tonCO2"]
[]
[]
[null,"RESULTS"]
[]
[null,"Expected compressor power","WCO2,compr",{"$f":"Maps!H10","v":267.85833304019735},"MJ/tonCO2","Compression from pCO2 to 150 bar"]
[null,"Total electric consumption","Wel tot",{"$f":"D32+D11","v":387.85833304019735},"MJ/tonCO2","Includes compression from pCO2 to 150 bar"]
[null,"Equivalent electricity loss","Wel,eq/Q",{"$f":"Calc!F15","v":0.24276371669182278},"MJel/MJth","Equivalent electric energy loss due to steam bleeding"]
[null,"Total equivalent electric cons.","Weq tot",{"$f":"D33+D34*D9","v":873.38576642384294},"MJ/tonCO2","Total equivalent electric consumption of the capture plant"]
[null,"Electrical over total consumption","Wel,tot/Wel,eq,tot",{"$f":"D33/D35","v":0.4440859331018393},null,"Fraction of actual electric consumption over total equivalent consumption"]
[null,"Efficiency loss (LHV)","Δηel",{"$f":"Calc!F16","v":7.176802064060428E-2},"%pt","Plant efficiency loss with respect to the reference plant w/o CCS"]
[]
[null,"CAPEX break-even point","CAPEXBE",{"$f":"Calc!F20","v":5980.0520103776134},"k$/(kgCO2/s)","Break-even capital cost at null OPEX (ref. CCS)"]
[null,"OPEX break-even point","OPEXBE",{"$f":"Calc!F23","v":42.933888969076719},"$/tonCO2","Break-even operation cost at null CAPEX (ref. CCS)"]
[null,"CAPEX break-even point","CAPEXBE",{"$f":"Calc!G20","v":1372.8610552498624},"$/kWel","Break-even capital cost at null OPEX (ref. plant)"]
[null,"OPEX break-even point","OPEXBE",{"$f":"Calc!G23","v":35.483328648247415},"$/MWhel","Break-even operation cost at null CAPEX (ref. plant)"]
[]
[null,"Compressor CAPEX estimate","CAPEXCO",{"$f":"Calc!F25","v":754.01347074284411},"k$/(kgCO2/s)","Additional capital cost for CO2 compressor"]
[]
[null,"Expected CCA","CCA",{"$f":"Calc!F27","v":72.170598464922875},"$/tonCO2","Expected cost of avoided CO2"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,"GRAPHS DATA"]
[null,"Breakeven lines"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,"CO2 reference"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,"OPEX","CAPEX"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"\"Wel,tot/Wel,eq,tot = \"&TEXT(D33/D35,\"0.0%\")","v":"Wel,tot/Wel,eq,tot = 44.4%"},0,{"$f":"D39","v":5980.0520103776134}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"D40","v":42.933888969076719},0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,"EL only",0,{"$f":"Calc!L20","v":5656.3956346973246}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"Calc!L23","v":40.598062443955108},0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,"TH + compressor",0,{"$f":"Calc!O20","v":6074.2785021898799}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"Calc!O23","v":43.614262577731822},0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,"Benchmark",{"$f":"Calc!C25","v":2.3703099972272539},{"$f":"Calc!C24","v":4817.0270367012599}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,"Technology",{"$f":"D22","v":15},{"$f":"D21","v":1500}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,"Technology + compr",{"$f":"O58","v":15},{"$f":"P58+D44","v":2254.0134707428442}]
[]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,"Energy reference"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,"OPEX","CAPEX"]
[null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"\"Wel,tot/Wel,eq,tot  = \"&TEXT(D33/D35,\"0.0%\")","v":"Wel,tot/Wel,eq,tot  = 44.4%"},0,{"$f":"D41","v":1372.8610552498624}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"D42","v":35.483328648247415},0]
[null,"Relation between equivalent electric consumption and efficiency loss",null,null,null,null,"Heat-to-power conversion factor",null,null,null,null,null,null,"EL only",0,{"$f":"Calc!M20","v":1298.558150746072}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"Calc!M23","v":33.552851296990447},0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,"TH + compressor",0,{"$f":"Calc!P20","v":1394.4929542295692}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,null,{"$f":"Calc!P23","v":36.045633180615575},0]
[null,null,null,null,null,null,null,null,null,null,null,null,null,"Benchmark",{"$f":"Calc!C25*Calc!L26/1000","v":1.9589767116232832},{"$f":"Calc!C24*Calc!L26/1000/3.6","v":1105.8614221576345}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,"Technology",{"$f":"$D$22*Calc!L26/1000","v":12.396965252951253},{"$f":"$D$21*Calc!L26/1000/3.6","v":344.36014591531261}]
[null,null,null,null,null,null,null,null,null,null,null,null,null,"Technology + compr",{"$f":"$O$58*Calc!L26/1000","v":12.396965252951253},{"$f":"($P$58+$D$44)*Calc!L26/1000/3.6","v":517.46160512005736}]
[]
[]
[]
[]
[]
[]
[null,null,null,null,null,null,"Estimated CO2 compressor consumption"]

{"sheet":"Calc","index":2,"n_rows":156,"n_cols":16,"rows_kept":156,"cut":false,"hidden":false,"merged":[]}
["CCS economic benchmarking"]
["Reference capture plant implemented:","USC+MEA"]
[]
["References","[1] NETL/DOE, 2012. Updated Costs (June 2011 Basis) for Selected Bituminous Baseline Cases. DOE/NETL-341/082312"]
[null,"[2] NETL/DOE, 2015. Cost and Performance Baseline for Fossil Energy Plants Volume 1a: Bituminous Coal and Natural Gas to Electricity. Revision 3. DOE/NETL-2015/1723"]
[]
["General data",null,null,null,null,null,"Conversion"]
["Heating value LHV","MJ/kg - Btu/lb",26.151,11252,"[2] pg. 27",null,"1 ton",{"$f":"42.09/38.18","v":1.102409638554217},"tonne",null,null,"reference case input"]
["Heating value HHV","MJ/kg - Btu/lb",27.113,11666,"[2] pg. 28",null,"1 kg",{"$f":"1/453.59237*1000","v":2.2046226218487757},"lb",null,null,"case input (from CCSbench sheet)"]
["Fuel cost (HHV)","$/GJ - $/MMBtu",{"$f":"D10*H10*1000","v":1.5544139669781813},1.64,"[2] pg. 26",null,"1 J",{"$f":"1/1055.06","v":9.4781339449889106E-4},"Btu"]
[null,"$/t - $/lb",{"$f":"C10*C9","v":42.144825886679428},{"$f":"D10*D9/1000000","v":1.9132239999999998E-2}]
["Emission factor (ECO2,fuel)","kg/GJ HHV",{"$f":"0.6375/12.01*44.01/C9*1000","v":86.161048681662351},null,"[2] pg. 32 - complete combustion"]
[]
["Capture system data",null,null,null,"Results"]
["CCS type",null,{"$f":"CCSbench!D8","v":"POST"},null,"Weq/Q",{"$f":"C84","v":0.24276371669182278},"MJel/MJth"]
["CO2 capture efficiency (ηcapt)","%",{"$f":"CCSbench!D18","v":0.9},null,"Δηel",{"$f":"CCSbench!D17","v":7.176802064060428E-2},"%pt",null,null,"STATUS",{"$f":"IF(ABS(C69-QrecFrac*(QCCS+WCCS))<5,\"Efficiency estimated by simplified H&M balance\",IF(AND(C69>0,C69<QCCS+WCCS),\"Efficiency set by user\",IF(C69>0,\"WARNING: Heat recovery higher than consumption\",\"WARNING: Negative heat recovery\")))","v":"Efficiency estimated by simplified H&M balance"}]
["Compressor consumption (wCO2,comp)","MJ/tonCO2",{"$f":"CCSbench!D32","v":267.85833304019735}]
["Total electric consumption","MJ/tonCO2",{"$f":"CCSbench!D33","v":387.85833304019735},null,"Actual","k$/(kgCO2/s)","$/kWe",null,"Breakeven results",null,"Only EL","k$/(kgCO2/s)","$/kWe","TH+compr","k$/(kgCO2/s)","$/kWe"]
["Thermal consumption (qCO2,comp)","MJ/tonCO2",{"$f":"CCSbench!D9","v":2000},null,"CAPEX break",5226.0512019700573,1199.7625029808694,null,"without compression",null,"CAPEX break",4902.3887628892717,1125.4582064814258,"CAPEX break",5320.2747116904729,1221.3937173515194]
["Bleeding pressure","bar",{"$f":"CCSbench!D10","v":5.0999999999999996},null,null,5980.0520103776134,1372.8610552498624,null,"with compression",null,null,5656.3956346973246,1298.558150746072,null,6074.2785021898799,1394.4929542295692]
["CCS EE consumption to cooling system","% ",{"$f":"CCSbench!D12","v":0.95},null,null,"$/tonCO2","$/MWhe",null,null,null,null,"$/tonCO2","$/MWhe",null,"$/tonCO2","$/MWhe"]
["CCF","%/y",{"$f":"CCSbench!D24","v":0.10879999999999999},null,"OPEX break",37.49493270052578,30.988225190010922,null,"without compression",null,"OPEX break",35.163028372415155,29.060989394757982,"OPEX break",38.174127357079335,31.549555360496559]
[null,null,null,null,null,42.933888969076719,35.483328648247415,null,"with compression",null,null,40.598062443955108,33.552851296990447,null,43.614262577731822,36.045633180615575]
["Benchmark CAPEX","k$/(kgCO2/s)",{"$f":"(E97+E98)/E39","v":4817.0270367012599}]
["Benchmark OPEX","$/tonCO2",{"$f":"E124/E40*1000","v":2.3703099972272539},null,"Compressor",{"$f":"C98/C39","v":754.01347074284411},"k$/(kgCO2/s)",null,null,null,"Weqtot",{"$f":"C18+C19*F15","v":873.38576642384294},"MJ/tonCO2"]
["Expected CAPEX","k$/(kgCO2/s)",{"$f":"CCSbench!D21","v":1500},null,null,null,null,null,null,null,"CO2 spec",{"$f":"C40","v":826.46435019675027},"kg/MWh"]
["Expected OPEX","$/tonCO2",{"$f":"CCSbench!D22","v":15},null,"CCA",{"$f":"C143","v":72.170598464922875},"$/tonCO2"]
[null,null,null,null,null,null,null,null,"Low T heat recovery efficency",null,{"$f":"CCSbench!D14","v":0.13},null,"Recovered low T heat fraction",null,{"$f":"QrecCCS/(C68+C60)","v":-5.0919458571481246E-7}]
[null,null,null,"DOE Cases B12A / B12B"]
["Plant energy balance",null,"Actual","USC","USC+MEA",null,"Reference",null,"Proportional to"]
["Net power output (Pel)","MWe",{"$f":"CCSbench!I24","v":550},550,550,null,"[2] p. 15",null,null,null,null,null,null,{"$f":"C31/E31-1","v":0}]
["Electric efficiency (ηel)","%HHV",{"$f":"C33*C8/C9","v":0.33777839015334182},0.40699999999999997,0.32500000000000001,null,"[2] p. 15",null,null,null,null,null,null,{"$f":"C32/E32-1","v":3.9318123548744088E-2}]
[null,"%LHV",{"$f":"D33-F16","v":0.35020402631744701},{"$f":"D32*$C$9/$C$8","v":0.42197204695805129},{"$f":"E32*$C$9/$C$8","v":0.33695556575274371},null,null,null,null,null,null,null,null,3.9318123548743866E-2]
["Carbon capture efficiency (ηcapt)","%",{"$f":"C16","v":0.9},0,0.9,null,"[2] p. 15",null,null,null,null,null,null,0]
["Fuel input (HHV) (Qfuel)","MWHHV",{"$f":"C31/C32","v":1628.2865216756927},{"$f":"D31/D32","v":1351.3513513513515},{"$f":"E31/E32","v":1692.3076923076922},null,null,null,null,null,null,null,null,-3.7830691737090527E-2]
["Fuel to main boiler","MWHHV",{"$f":"IF($C$15=\"CA-L\",CCSbench!$I$17,1)*C35","v":1628.2865216756927},{"$f":"D35","v":1351.3513513513515},{"$f":"E35","v":1692.3076923076922},null,null,null,null,null,null,null,null,-3.7830691737090527E-2]
[]
["CO2 total flow","kg/s",{"$f":"C35*$C$12/1000","v":140.29487426179404},{"$f":"D35*$C$12/1000","v":116.433849569814},{"$f":"E35*$C$12/1000","v":145.81100546127473},null,null,null,null,null,null,null,null,-3.7830691737090416E-2]
["CO2 to storage (GCO2,capt)","kg/s",{"$f":"C38*C34","v":126.26538683561463},{"$f":"D38*D34","v":0},{"$f":"E38*E34","v":131.22990491514727},null,null,null,null,null,null,null,null,-3.7830691737090527E-2]
[null,"kg/MWhe",{"$f":"C39*3600/C31","v":826.46435019675027},{"$f":"D39*3600/D31","v":0},{"$f":"E39*3600/E31","v":858.95937762641859},null,null,null,null,null,null,null,null,-3.7830691737090638E-2]
["CO2 emitted (GCO2,emit)","kg/s",{"$f":"C38*(1-C34)","v":14.029487426179401},{"$f":"D38*(1-D34)","v":116.433849569814},{"$f":"E38*(1-E34)","v":14.58110054612747},null,null,null,null,null,null,null,null,-3.7830691737090416E-2]
[null,"kg/MWhe",{"$f":"C41*3600/C31","v":91.829372244083345},{"$f":"D41*3600/D31","v":762.11246991150983},{"$f":"E41*3600/E31","v":95.439930847379813},null,null,null,null,null,null,null,null,-3.7830691737090527E-2]
[]
["Combustion flue gases","kg/s",{"$f":"IF($C$15=\"OXY\",C38/0.825*3.19,E44/E35*C35)*IF($C$15=\"CA-L\",CCSbench!$I$17,1)","v":682.14020585797437},{"$f":"D45","v":601.46751455217782},{"$f":"E45+E39","v":708.96067874946391},null,null,null,null,null,null,null,null,-3.7830691737090638E-2]
["Stack flow","kg/s",{"$f":"IF($C$15=\"OXY\",1/3.19,1)*C44-C39","v":555.8748190223597},{"$f":"4773632/3600/$H$9","v":601.46751455217782},{"$f":"4585242/3600/$H$9","v":577.73077383431666},null,"[2] p. 124+146",null,"Fuel input - CO2 removed",null,null,null,null,-3.783069173709086E-2]
["Stack/flue gas cooling power (Qstack)","MWth",{"$f":"(C35+C49+C50)-(C57+C51)","v":253.09370233697769},{"$f":"(D35+D49+D50)-(D57+D51)","v":183.40840840840838},{"$f":"(E35+E49+E50)-(E57+E51)","v":263.0448717948716},null,null,null,null,null,null,null,null,-3.7830691737089084E-2]
["Gas treatment flow","kg/s",{"$f":"C44","v":682.14020585797437},{"$f":"D44","v":601.46751455217782},{"$f":"E44","v":708.96067874946391},null,null,null,"Combustion flue gases",null,null,null,null,-3.7830691737090638E-2]
[]
["Air in (Qenth,air)","MWth",{"$f":"E49/E35*C35","v":19.216659240028665},{"$f":"57.3/3.6","v":15.916666666666666},{"$f":"71.9/3.6","v":19.972222222222225},null,"[2] p. 126+148",null,"Fuel input",null,null,null,null,-3.7830691737090638E-2]
["Raw water in (Qenth,water)","MWth",{"$f":"E50/E35*C35","v":29.987610107527342},{"$f":"72.7/3.6","v":20.194444444444446},{"$f":"112.2/3.6","v":31.166666666666668},null,"[2] p. 126+148",null,"Fuel input",null,null,null,null,-3.7830691737090638E-2]
["CO2 enthalpy (Qenth,CO2)","MWth",{"$f":"E51/E40*C40","v":-26.406202126770953},0,{"$f":"-98.8/3.6","v":-27.444444444444443},null,"[2] p. 126+148",null,"CO2 removed",null,null,null,null,-3.7830691737090749E-2]
[]
["Other cooling tower duty (Qcool,fix)","MWth",{"$f":"E53/E31*C31","v":29.444444444444443},{"$f":"106/3.6","v":29.444444444444443},{"$f":"106/3.6","v":29.444444444444443},null,"[2] p. 126+148",null,"Plant size",null,null,null,null,0]
["Heat losses to environment (Qenv)","MWth",{"$f":"E54/E35*C35","v":35.680445181416225},{"$f":"104.7/3.6","v":29.083333333333332},{"$f":"133.5/3.6","v":37.083333333333336},null,"[2] p. 126+148",null,"Fuel input",null,null,null,null,-3.7830691737090638E-2]
[]
["Boiler efficiency","%",{"$f":"E56","v":0.89100000000000001},0.89100000000000001,{"$f":"D56","v":0.89100000000000001},null,"[2] p. 126+148",null,"Constant",null,null,null,null,0]
["Cycle input (Qcycle)","MWth",{"$f":"C35*C56","v":1450.8032908130422},{"$f":"D35*D56","v":1204.0540540540542},{"$f":"E35*E56","v":1507.8461538461538},null,null,null,null,null,null,null,null,-3.7830691737090638E-2]
[]
["Aux consumption BOP (Waux)","MWe",{"$f":"E59/E57*C57-IF(CCSbench!I11=\"NO\",0.0022*Calc!$C$35,0)","v":38.10190460721121},{"$f":"107/3.6","v":29.722222222222221},39.6,null,"[2] p. 120+142",null,"Cycle input",null,null,null,null,-3.7830691737090638E-2]
["Aux consumption CO2 removal (to CT) (WCO2,capt)","MWe",{"$f":"C21*(C18-C17)*C39/1000","v":14.394254099260069},0,16,null,"[2] p. 142"]
["Aux consumption CO2 removal (dissip)  (WCO2,capt)","MWe",{"$f":"(C18-C17)*(1-C21)*C39/1000","v":0.75759232101368845},0,0]
["Aux consumption CO2 compr (WCO2,comp)","MWe",{"$f":"C17*C39/1000","v":33.821236038463418},0,35.69,null,"[2] p. 142",null,"CO2 removed",null,null,null,null,-5.2360996400576676E-2]
["Total aux","MWe",{"$f":"SUM(C59:C62)","v":87.074987065948392},{"$f":"SUM(D59:D62)","v":29.722222222222221},{"$f":"SUM(E59:E62)","v":91.289999999999992},null,"[2] p. 120+142",null,null,null,null,null,null,-4.6171682923119683E-2]
["Recovered fraction of BOP aux (ω)","%",{"$f":"E64","v":0.22700000000000001},0.25,0.22700000000000001]
[]
["Turbine gross power (WT,gross)","MWe",{"$f":"C63+C31","v":637.07498706594833},{"$f":"2087/3.6","v":579.72222222222217},{"$f":"2309/3.6","v":641.38888888888891},null,"[2] p. 120+142",null,null,null,null,null,null,-6.7258755143292381E-3]
["Gross efficiency","%",{"$f":"C66/(C57+C64*C59+QrecCCS)","v":0.43651648816133415},{"$f":"D66/(D57+D64*D59)","v":0.47852215176636254},{"$f":"E66/(E57+E64*E59)","v":0.42284674289965307},null,null,null,null,null,"CO2 specific heat consumption",null,null,3.2327895369233195E-2]
["CO2 capture thermal  (QCO2,capt)","MWth",{"$f":"C19*C39/1000","v":252.53077367122927},0,332,null,null,null,null,null,{"$f":"C68*1000/CO2flow","v":2000},"MJth/tonCO2"]
["CO2 capture heat recovery  (QCO2,H)","MWth",{"$f":"(C74*C68+C66-(D67*(C57+C64*C59)))/$K$28","v":-1.3591677893250913E-4},null,null,null,null,null,null,null,{"$f":"QrecCCS*1000/CO2flow","v":-1.0764373542011137E-3},"MJth/tonCO2"]
["Condenser duty (Qcond)","MWth",{"$f":"C57-(C66-C64*C59)-C68+QrecCCS-C54-C53","v":504.72163687906186},{"$f":"D57-(D66-D64*D59)","v":631.76238738738755},{"$f":"1867/3.6","v":518.61111111111109},null,"[2] p. 126+148",null,null,null,null,null,null,-2.6782060650978656E-2]
["Cooling tower blowdown","MWth",{"$f":"C72*E71/E72","v":13.114330672337749},{"$f":"29.4/3.6","v":8.1666666666666661},{"$f":"50.4/3.6","v":14},null,"[2] p. 126+148",null,"Cooling tower duty",null,null,null,null,-6.3262094833017923E-2]
["Cooling tower duty (Qcool)","MWth",{"$f":"(C53+(C68-QrecCCS)+C70+C60+C62+C73)/(1-E71/E72)","v":1016.6420487930695},{"$f":"D53+D68+D70+D71+D60","v":669.37349849849863},{"$f":"E53+E68+E70+E71+E60+E73","v":1085.3004273504271},null,null,null,null,null,null,null,null,-6.3262094833017923E-2]
["Flue gas sensible heat rejected from CC system","MWth",{"$f":"E73/E45*C45","v":168.61523707149379},null,{"$f":"E46-87.8","v":175.24487179487159},null,null,null,"Flue gases"]
["CO2 removal ΔW/Q","-",{"$f":"C84","v":0.24276371669182278},null,{"$f":"(D67*(E57+E59)-E66)/E68","v":0.29848907949444053},null,null,null,null,null,null,null,null,-0.18669146253860069]
[]
["Low pressure turbine losses"]
[]
["Saturation pressure",{"$f":"CCSbench!D10","v":5.0999999999999996},"bar",null,"Assumption:","Steam cycle performance obtained from model fitted on “DOE-NETL, 2012. Cost and Performance Baseline for Fossil Energy Plants –  Volume 1: Bituminous Coal and Natural Gas to Electricity, DOE/NETL-2010/1397, Revision 2, November 2010.”"]
["Saturation temperature",{"$f":"3885.7/(16.3872-LN(B78*100))-230.17","v":152.55241204128967},"°C",null,null,"Condensate from the capture plant is returned as saturated liquid to the optimal injection point in the feed water pre-heating line."]
[]
["Parameters","A",6.0125999999999999E-2]
["A*ln(p)+B","B",0.14480399999999999]
[]
[null,"ΔW/Q",{"$f":"C81*LN(B78)+C82","v":0.24276371669182278}]
[]
["Costing","$2011","Actual","USC","USC+MEA",null,"Reference",null,"Proportional to","Exp","Cella","Active"]
["CAPEX",null,null,null,null,null,"[2] p. 132+155"]
["Coal & sorbent handling","k$",{"$f":"D88*(OFFSET(INDIRECT(K88),0,2)/OFFSET(INDIRECT(K88),0,3))^J88*L88","v":50960.478838403826},45398,52286,null,"IT 1",null,"Fuel input (HHV) (Qfuel)",0.62,{"$f":"ADDRESS(MATCH(I88,A:A,0),1)","v":"$A$35"},{"$f":"TRUE","v":true},null,{"$f":"C88/E88-1","v":-2.5351359094139436E-2}]
["Coal and sorbent prep and feed","k$",24350.028980626295,21531,24983,null,"IT 2",null,"Fuel input (HHV) (Qfuel)",0.66,"$A$35",{"$f":"TRUE","v":true},null,{"$f":"C89/E89-1","v":-2.5336069302073549E-2}]
["Feedwater and misc BOP systems (3.1+3.3+3.5)","k$",78198.44348612662,68888,80373,null,"IT 3a",null,"Fuel input (HHV) (Qfuel)",0.68,"$A$35",{"$f":"TRUE","v":true},null,-2.7055808715282237E-2]
["Feedwater and misc BOP systems (3.2+3.4+3.7)","k$",24267.729056172622,18328,24953,null,"IT 3b",null,"Raw water in (Qenth,water)",0.71,"$A$50",{"$f":"TRUE","v":true},null,-2.7462467191414985E-2]
["Feedwater and misc BOP systems (others)","k$",6734.6728679110165,6428,6824,null,"IT 3c",null,"Fuel input (HHV) (Qfuel)",0.25,"$A$35",{"$f":"TRUE","v":true},null,-1.3090142451492315E-2]
["PC boiler","k$",388630.69334991946,341722,400793,null,"IT 4",null,"Fuel to main boiler",0.69,"$A$36",{"$f":"CCSbench!$I$9=\"YES\"","v":true},null,-3.0345606460393637E-2]
["Secondary combustor","k$",{"$f":"D94*((OFFSET(INDIRECT(K94),0,2)-OFFSET(INDIRECT(K93),0,2))/OFFSET(INDIRECT(K94),0,3))^J94*L94","v":0},341722,400793,null,"IT 4",null,"Fuel input (HHV) (Qfuel)",0.69,"$A$35",{"$f":"CCSbench!$I$10=\"YES\"","v":true}]
["Flue gas cleanup (other)","k$",{"$f":"D95*(OFFSET(INDIRECT(K95),0,2)/OFFSET(INDIRECT(K95),0,3))^J95*L95","v":62385.027855908047},59322,70064,null,"IT 5Aa",null,"Gas treatment flow",0.4,"$A$47",{"$f":"CCSbench!$I$12=\"YES\"","v":true},null,-0.10959939689558051]
["Flue gas cleanup (FGD)","k$",{"$f":"D96*(OFFSET(INDIRECT(K96),0,2)/OFFSET(INDIRECT(K96),0,3))^J96*L96","v":113523.88248955319},107950,127411,null,"IT 5Ab",null,"Gas treatment flow",0.4,"$A$47",{"$f":"CCSbench!$I$11=\"YES\"","v":true},null,-0.10899465125025953]
["CO2 removal","k$",189398.08025342194,0,533757,null,"IT 5B"]
["CO2 compression","k$",{"$f":"E98*(OFFSET(INDIRECT(K98),0,2)/OFFSET(INDIRECT(K98),0,4))^J98*L98","v":95205.802562609606},0,98381,null,"IT 5B",null,"Aux consumption CO2 compr (WCO2,comp)",0.61,{"$f":"ADDRESS(MATCH(I98,A:A,0),1)","v":"$A$62"},{"$f":"TRUE","v":true},null,-3.2274498504694993E-2]
["Ducting (7.3+7.9)","k$",{"$f":"D99*(OFFSET(INDIRECT(K99),0,2)/OFFSET(INDIRECT(K99),0,3))^J99*L99","v":26011.087233247054},25341,25928,null,"IT 7a",null,"Fuel input (HHV) (Qfuel)",0.14000000000000001,"$A$35",{"$f":"TRUE","v":true},null,3.2045369194328988E-3]
["Stack (7.4)","k$",19533.719419706875,20287,19099,null,"IT 7b",null,"Stack flow",0.48,"$A$45",{"$f":"TRUE","v":true},null,2.2761370737047759E-2]
["Steam turbine generator","k$",164671.07413467026,154148,166838,null,"IT 8a",null,"Turbine gross power (WT,gross)",0.7,"$A$66",{"$f":"TRUE","v":true},null,-1.2988203318966551E-2]
["Steam turbine generator (8.3 condenser)","k$",11000.399688124009,12786,11338,null,"IT 8b",null,"Condenser duty (Qcond)",0.67,"$A$70",{"$f":"TRUE","v":true},null,-2.9776002105837973E-2]
["Cooling water system","k$",59406.744614888878,44037,62254,null,"IT 9",null,"Cooling tower duty (Qcool)",{"$f":"LN(E103/D103)/LN(OFFSET(INDIRECT(K103),0,4)/OFFSET(INDIRECT(K103),0,3))","v":0.71635453710502905},"$A$72",{"$f":"TRUE","v":true},null,-4.573610346501622E-2]
["Ash/spent sorbent handling system","k$",18624.268185924742,16778,19028,null,"IT 10",null,"Fuel input (HHV) (Qfuel)",0.56000000000000005,"$A$35",{"$f":"TRUE","v":true},null,-2.1217774546734125E-2]
["Accessory electric plant","k$",{"$f":"D105*(OFFSET(INDIRECT(K105),0,2)/OFFSET(INDIRECT(K105),0,3))^J105","v":98007.80740216226},61735,93584,null,"IT 11",null,"Total aux",0.43,"$A$63",null,null,4.7270980105170279E-2]
["Instrumentation and control","k$",{"$f":"D106*(OFFSET(INDIRECT(K106),0,2)/OFFSET(INDIRECT(K106),0,3))^J106","v":30262.545550915202},26316,31654,null,"IT 12",null,"Total aux",0.13,"$A$63",null,null,-4.3958250113249497E-2]
["BEC","k$",{"$f":"SUM(C88:C106)","v":1461172.4859702918},{"$f":"SUM(D88:D106)-D94","v":1030995},{"$f":"SUM(E88:E106)-E94","v":1849548},null,null,null,null,null,null,null,null,-0.20998401448878767]
["Improvements to site","k$",{"$f":"D108*(OFFSET(INDIRECT(K108),0,2)/OFFSET(INDIRECT(K108),0,3))^J108","v":17578.180355043482},16394,18063,null,"IT 13",null,"BEC",0.2,{"$f":"ADDRESS(MATCH(I108,A:A,0),1)","v":"$A$107"},null,null,-2.6840483029204387E-2]
["Buildings and structures","k$",{"$f":"D109*(OFFSET(INDIRECT(K109),0,2)/OFFSET(INDIRECT(K109),0,3))^J109","v":69347.574607562565},66971,71531,null,"IT 14",null,"BEC",0.1,{"$f":"ADDRESS(MATCH(I109,A:A,0),1)","v":"$A$107"},null,null,-3.0524183814534034E-2]
["Total capital cost","k$",{"$f":"SUM(C107:C109)","v":1548098.2409328977},{"$f":"SUM(D107:D109)","v":1114360},{"$f":"SUM(E107:E109)","v":1939142},null,null,null,null,null,null,null,null,-0.20165813492106421]
["Total Overnight Cost (TOC)","k$",{"$f":"E111/E110*C110","v":1903528.0226846908},1378634,2384352,null,"[2] p. 135+158",null,"Total capital cost",1,{"$f":"ADDRESS(MATCH(I111,A:A,0),1)","v":"$A$110"},null,null,-0.20165813492106421]
["Total As Spent Cost (TASC)","k$",{"$f":"E112/E110*C110","v":2170021.7223248254},1563371,2718161,null,"[2] p. 135+158",null,"Total Overnight Cost (TOC)",1,{"$f":"ADDRESS(MATCH(I112,A:A,0),1)","v":"$A$111"},null,null,-0.2016581349210641]
["FIXED OPEX",null,null,null,null,null,"[2] p. 136+159"]
["Labour","k$/y",{"$f":"D114*(OFFSET(INDIRECT(K114),0,2)/OFFSET(INDIRECT(K114),0,3))^J114","v":20994.920402561394},{"$f":"6329.5+7284.5+3403","v":17017},{"$f":"7384+12065+4862","v":24311},null,null,null,"Total Overnight Cost (TOC)",{"$f":"LN(E114/D114)/LN(OFFSET(INDIRECT(K114),0,4)/OFFSET(INDIRECT(K114),0,3))","v":0.65113871194799566},{"$f":"ADDRESS(MATCH(I114,A:A,0),1)","v":"$A$111"},null,null,-0.13640243500631832]
["Property taxes and insurance","k$/y",{"$f":"D115*(OFFSET(INDIRECT(K115),0,2)/OFFSET(INDIRECT(K115),0,3))^J115","v":30883.514169590875},22287,38782,null,null,null,"Total Overnight Cost (TOC)",{"$f":"LN(E115/D115)/LN(OFFSET(INDIRECT(K115),0,4)/OFFSET(INDIRECT(K115),0,3))","v":1.0111684096810749},{"$f":"ADDRESS(MATCH(I115,A:A,0),1)","v":"$A$111"},null,null,-0.20366370559561464]
["Total fixed  Opex","k$/y",{"$f":"SUM(C114:C115)","v":51878.43457215227},{"$f":"SUM(D114:D115)","v":39304},{"$f":"SUM(E114:E115)","v":63093},null,null,null,null,null,null,null,null,-0.1777465872259637]
["VARIABLE OPEX",null,null,null,null,null,"[2] p. 136+159"]
["Maintenance material cost","$/MWhe",{"$f":"D118*$D$31/$C$31*(OFFSET(INDIRECT(K118),0,2)/OFFSET(INDIRECT(K118),0,3))^J118*L118","v":3.6865620756256732},2.67,4.4174199999999999,null,null,null,"Total Overnight Cost (TOC)",1,{"$f":"ADDRESS(MATCH(I118,A:A,0),1)","v":"$A$111"},{"$f":"TRUE","v":true},null,-0.16544904590786624]
["Water","$/MWhe",0.69792347045304337,0.47,0.72,null,null,null,"Raw water in (Qenth,water)",1,"$A$50",{"$f":"TRUE","v":true},null,-3.0661846592995312E-2]
["MU & WT chemicals","$/MWhe",0.53457967949594809,0.36,0.55600000000000005,null,null,null,"Raw water in (Qenth,water)",1,"$A$50",{"$f":"TRUE","v":true},null,-3.8525756302251746E-2]
["Limestone+hydrated lime","$/MWhe",2.6175638035786655,2.3079999999999998,2.8970000000000002,null,null,null,"Gas treatment flow",1,"$A$47",{"$f":"L96","v":true},null,-9.6457092309746195E-2]
["Activated carbon","$/MWhe",0.29487287215357588,0.26,0.32900000000000001,null,null,null,"Gas treatment flow",1,"$A$47",{"$f":"TRUE","v":true},null,-0.10372987187362959]
["Ammonia","$/MWhe",1.9291490597432019,1.7010000000000001,2.1829999999999998,null,null,null,"Gas treatment flow",1,"$A$47",{"$f":"TRUE","v":true},null,-0.11628535971452036]
["CO2 related variable opex","$/MWhe",12.396965252951253,0,2.036,null,null,null,null,null,null,{"$f":"TRUE","v":true}]
["SCR catalyst","$/MWhe",{"$f":"D125*$D$31/$C$31*(OFFSET(INDIRECT(K125),0,2)/OFFSET(INDIRECT(K125),0,3))^J125*L125","v":0.25665052154652263},0.21299999999999999,0.26700000000000002,null,null,null,"Fuel input (HHV) (Qfuel)",1,{"$f":"ADDRESS(MATCH(I125,A:A,0),1)","v":"$A$35"},{"$f":"TRUE","v":true},null,-3.876209158605759E-2]
["Waste disposal","$/MWhe",{"$f":"D126*$D$31/$C$31*(OFFSET(INDIRECT(K126),0,2)/OFFSET(INDIRECT(K126),0,3))^J126*L126","v":1.2892772678628135},1.07,1.34,null,null,null,"Fuel input (HHV) (Qfuel)",1,{"$f":"ADDRESS(MATCH(I126,A:A,0),1)","v":"$A$35"},{"$f":"TRUE","v":true},null,-3.7852785177004966E-2]
["Total variable Opex","$/MWhe",{"$f":"SUM(C118:C126)","v":23.703544003410695},{"$f":"SUM(D118:D126)","v":9.0519999999999996},{"$f":"SUM(E118:E126)","v":14.745419999999999},null,null,null,null,null,null,null,null,0.60751908073223393]
["Fuel","$/MWhe",{"$f":"$C$10/$C$32*3.6","v":16.566750402774666},{"$f":"$C$10/$D$32*3.6","v":13.749116169831581},{"$f":"$C$10/$E$32*3.6","v":17.218123941912165},null,null,null,null,null,null,null,null,-3.7830691737090638E-2]
[]
["CO2 transport and storage","$/MWh",{"$f":"E130*$D$31/$C$31*(OFFSET(INDIRECT(K130),0,2)/OFFSET(INDIRECT(K130),0,4))^J130","v":9.2368253593239302},0,9.6,null,"[2] p. 136+159",null,"CO2 to storage (GCO2,capt)",1,{"$f":"ADDRESS(MATCH(I130,A:A,0),1)","v":"$A$39"},null,null,-3.7830691737090527E-2]
[]
["Capacity factor","%",{"$f":"CCSbench!D19","v":0.85},{"$f":"C132","v":0.85},{"$f":"D132","v":0.85},null,"[2] p. 136+159",null,null,null,null,null,null,0]
["Operating hours","h/y",{"$f":"8760*C132","v":7446},{"$f":"8760*D132","v":7446},{"$f":"8760*E132","v":7446},null,null,null,null,null,null,null,null,0]
["Yearly electricity production","GWh",{"$f":"$C$31*C133/1000","v":4095.3},{"$f":"$D$31*D133/1000","v":4095.3},{"$f":"$E$31*E133/1000","v":4095.3},null,null,null,null,null,null,null,null,0]
["CCF","%/y",{"$f":"C22","v":0.10879999999999999},0.1023,0.10879999999999999,null,null,null,null,null,null,null,null,0]
["COE Capex","$/MWh",{"$f":"C112*C135/C134","v":57.651054474383066},{"$f":"D112*D135/D134","v":39.052780821917814},{"$f":"E112*E135/E134","v":72.213492735574931},null,null,null,null,null,null,null,null,-0.20165813492106432]
["COE Fixed Opex","$/MWh",{"$f":"C116/C134","v":12.667798347410999},{"$f":"D116/D134","v":9.5973432959734328},{"$f":"E116/E134","v":15.406197348179619},null,null,null,null,null,null,null,null,-0.1777465872259637]
["COE Variable Opex","$/MWh",{"$f":"C127","v":23.703544003410695},9.0519999999999996,14.745419999999999,null,null,null,null,null,null,null,null,0.60751908073223393]
["COE Fuel","$/MWh",16.566750402774666,13.749116169831581,17.218123941912165,null,null,null,null,null,null,null,null,-3.7830691737090638E-2]
["CO2 transport and storage","$/MWh",{"$f":"C130","v":9.2368253593239302},{"$f":"D130","v":0},{"$f":"E130","v":9.6},null,null,null,null,null,null,null,null,-3.7830691737090527E-2]
["1st y COE","$/MWh",{"$f":"SUM(C136:C140)","v":119.82597258730335},{"$f":"SUM(D136:D140)","v":71.451240287722825},{"$f":"SUM(E136:E140)","v":129.18323402566671},null,null,null,null,null,null,null,null,-7.2434023725588159E-2]
[]
["CCA","$/ton",{"$f":"(C141-$D$141)/($D$42-C42)*1000","v":72.170598464922875},"NA",{"$f":"(E141-$D$141)/($D$42-E42)*1000","v":86.597227806904471},null,null,null,null,null,null,null,null,-0.16659458630881652]
[]
["Delta CCA","$/ton",{"$f":"C143-E143","v":-14.426629341981595}]
[]
[]
[]
["CCA breakdown"]
[]
["COE Capex","$/ton",{"$f":"(C136-D136)/($D$42-$C$42)*1000","v":27.746893390549335}]
["COE Fixed Opex","$/ton",{"$f":"(C137-D137)/($D$42-$C$42)*1000","v":4.5808331764931802}]
["COE Variable Opex","$/ton",{"$f":"(C138-D138)/($D$42-$C$42)*1000","v":21.85874006729069}]
["COE Fuel","$/ton",{"$f":"(C139-D139)/($D$42-$C$42)*1000","v":4.2036480447566156}]
["CO2 transport and storage","$/ton",{"$f":"(C140-D140)/($D$42-$C$42)*1000","v":13.780483785833061}]
["CCA","$/ton",{"$f":"SUM(C151:C155)","v":72.170598464922875}]

{"sheet":"Sankey","index":3,"n_rows":36,"n_cols":5,"rows_kept":36,"cut":false,"hidden":false,"merged":[]}
[]
[null,"Sankey diagram: USC+CCS"]
[]
[]
[]
[null,null,"Fuel input (HHV)",{"$f":"Calc!C35","v":1628.2865216756927},"MWHHV"]
[null,null,"Air in",{"$f":"Calc!C49","v":19.216659240028665},"MWth"]
[null,null,"Raw water in",{"$f":"Calc!C50","v":29.987610107527342},"MWth"]
[]
[null,null,"Ambient losses",{"$f":"-Calc!C54","v":-35.680445181416225},"MWth"]
[null,null,"Stack power",{"$f":"-Calc!C46+Calc!C73","v":-84.478465265483891},"MWth"]
[null,null,"Other cooling tower duty",{"$f":"-Calc!C53","v":-29.444444444444443},"MWth"]
[null,null,"Cycle input",{"$f":"SUM(D6:D12)","v":1527.8874361319045},"MWth"]
[]
[null,null,"Aux consumption BOP",{"$f":"Calc!C59","v":38.10190460721121},"MWe"]
[null,null,"Aux consumption CO2 removal (to CT)",{"$f":"Calc!C60","v":14.394254099260069},"MWe"]
[null,null,"Aux consumption CO2 removal (dissip)",{"$f":"Calc!C61","v":0.75759232101368845},"MWe"]
[null,null,"Aux consumption CO2 compr",{"$f":"Calc!C62","v":33.821236038463418},"MWe"]
[]
[null,null,"Turbine gross power",{"$f":"Calc!C66","v":637.07498706594833},"MWe"]
[]
[null,null,"CO2 capture thermal requirement",{"$f":"Calc!C68","v":252.53077367122927},"MWth"]
[null,null,"CO2 capture heat recovery",{"$f":"QrecCCS","v":-1.3591677893250913E-4},"MWth"]
[null,null,"Condenser duty",{"$f":"Calc!C70","v":504.72163687906186},"MWth"]
[null,null,"CO2 entalphy",{"$f":"-Calc!C51","v":26.406202126770953},"MWth"]
[]
[null,null,"Other dissipations",{"$f":"Calc!C59*(1-Calc!C64)","v":29.452772261374268},"MWth"]
[null,null,"Cooling tower blowdown",{"$f":"Calc!C71","v":13.114330672337749},"MWth"]
[null,null,"Cooling tower duty",{"$f":"Calc!C72","v":1016.6420487930695},"MWth"]
[]
[null,null,"Net power output",{"$f":"D20-SUM(D15:D18)","v":550},"MWe"]
[]
[]
[null,null,"Balance check"]
[null,null,"IN",{"$f":"D6+D7+D8","v":1677.4907910232489},"MW"]
[null,null,"OUT",{"$f":"-(D10+D11)+D29+D17+D31-D25-D28+D27","v":1677.4907910232489},"MW"]

{"sheet":"Maps","index":4,"n_rows":57,"n_cols":15,"rows_kept":57,"cut":false,"hidden":false,"merged":[[28,6,29,18],[30,6,30,18],[48,8,48,11]]}
["CO2 Compression Map"]
[]
[null,"CO2 purity","A","B"]
["Params",1,316.96622856203396,-70.84771733784703]
[null,0.95,325.79852246340153,-72.40819795464833,null,"[kJ/kg]","[bar]"]
[]
["Compression work",null,"W [kJ/kg]",null,null,null,null,"Oper Point"]
["Data","p [bar]","Pure CO2","95% CO2","@ oper cond",null,"Pressure",{"$f":"CCSbench!$D$15","v":2}]
[null,1,{"$f":"($C$4+$D$4*LN($B9))","v":316.96622856203396},{"$f":"($C$5+$D$5*LN($B9))","v":325.79852246340153},{"$f":"($C9-$D9)/($B$4-$B$5)*($H$9-$B$5)+$D9","v":316.96622856203396},null,"Purity",{"$f":"CCSbench!D16","v":1}]
[null,{"$f":"B9*1.5","v":1.5},288.23995119242716,296.43952465180269,{"$f":"($C10-$D10)/($B$4-$B$5)*($H$9-$B$5)+$D10","v":288.23995119242716},null,"Consumption",{"$f":"(($C$4+$D$4*LN($H8))-($C$5+$D$5*LN($H8)))/($B$4-$B$5)*($H$9-$B$5)+($C$5+$D$5*LN($H8))","v":267.85833304019735}]
[null,{"$f":"B10*1.5","v":2.25},259.51367382282035,267.08052684020385,259.51367382282035]
[null,3.375,230.78739645321349,237.72152902860495,230.78739645321349,null,"Assumption:","Outlet pressure 150 bar"]
[null,5.0625,202.06111908360668,208.36253121700611,202.06111908360668,null,null,"6 compressor stages + 1 pump stage"]
[null,7.59375,173.33484171399988,179.00353340540727,173.33484171399988,null,null,"Isentropic efficiency: 84% compressors, 80% pump"]
[null,11.390625,144.60856434439305,149.6445355938084,144.60856434439305,null,null,"Intercooling to 30 °C"]
[null,17.0859375,115.88228697478624,120.28553778220959,115.88228697478624,null,null,"Max T out compressors: 100°C"]
[null,25.62890625,87.156009605179406,90.926539970610719,87.156009605179406]
[null,38.443359375,58.429732235572601,61.56754215901185,58.429732235572601]
[null,57.6650390625,29.703454865965796,32.20854434741301,29.703454865965796]
[]
[]
[]
["Lost work ratio Map"]
[]
[null,"p [bar]","T [°C]","W/Q",null,null,"A",6.0125999999999999E-2]
[null,1,{"$f":"3885.7/(16.3872-LN(B26*100))-230.17","v":99.628859902636549},{"$f":"$H$25*LN(B26)+$H$26","v":0.14480399999999999},null,null,"B",0.14480399999999999]
[null,2,{"$f":"3885.7/(16.3872-LN(B27*100))-230.17","v":120.24402533001503},{"$f":"$H$25*LN(B27)+$H$26","v":0.18648016737834727}]
[null,{"$f":"B27*1.5","v":3},133.54320233269229,0.21085916246845876,null,null,"Mapped from a USC cycle with optimal reinjection point"]
[null,5,151.80737976663673,0.2415730639230127,null,null,"Steam cycle performance obtained from model fitted on “DOE-NETL, 2012. Cost and Performance Baseline for Fossil Energy Plants –  Volume 1: Bituminous Coal and Natural Gas to Electricity, DOE/NETL-2010/1397, Revision 2, November 2010.”"]
[null,7,164.87399421284866,0.26180379362209977]
[null,10,179.73797608478165,0.28324923130135998,null,null,"Condensate from the capture plant is returned as saturated liquid to the optimal injection point in the feed water pre-heating line."]
[null,15,198.05445781911951,0.30762822639147147]
[null,20,212.07543752447154,0.32492539867970727]
[null,50,263.56527806378688,0.38001829522437269]
[]
["Efficiency loss map"]
[]
["Δη [%]","Equivalent electric consumption [MJe/tonCO2]"]
["CCR",100,500,1000,1500,2000,2500]
[0.75,8.2497563059878432E-3,3.5048917447338124E-2,6.8547931379336291E-2,0.10204679661800653,0.13554584238192846,0.16904481579952302,null,{"$f":"\"CCR = \"&TEXT(A40,\"0%\")","v":"CCR = 75%"}]
[0.8,8.6964080806606336E-3,3.7282182421798371E-2,7.3014428543723198E-2,0.10874666233481539,0.14447890991025797,0.18021114166409274,null,"CCR = 80%"]
[0.85,9.1430599226672848E-3,3.9515497210839412E-2,7.748095257123544E-2,0.11544645876276527,0.153411962021965,0.19137745516806934,null,"CCR = 85%"]
[0.9,9.5897118290065864E-3,4.1748730572849169E-2,8.1947484662895587E-2,0.12214625056253137,0.16234502183726546,0.20254379998276717,null,"CCR = 90%"]
[0.95,1.0036363796778303E-2,4.3981982140903542E-2,8.6413963983236475E-2,0.12884597847757273,0.17127807979152149,0.21371011671549783,null,"CCR = 95%"]
[1,1.0483015823180841E-2,4.6215245466930732E-2,9.0880542191167146E-2,0.13554584238192846,0.18021114166409274,0.22487643355048326,null,"CCR = 100%"]
[]
["CAPEX/OPEX maps"]
[]
["CCR",0.9,null,{"$f":"CONCATENATE(\"CCR = \",TEXT(B49,\"0%\"))","v":"CCR = 90%"},null,"TYPE","POST",null,{"$f":" IF(OR(Maps!B49 <> CCSbench!D18,Maps!G49 <> CCSbench!D8), \"Data changed: Rebuild maps\", \"CAPEX/OPEX Maps: Ok\")","v":"CAPEX/OPEX Maps: Ok"}]
[]
["CAPEX break-even",null,null,null,null,null,null,null,"OPEX break-even"]
[null,"W/Weq",null,null,null,null,null,null,null,"W/Weq"]
["Delta eta",0,0.2,0.4,0.6,0.8,1,null,null,0,0.2,0.4,0.6,0.8,1]
[0.03,8457.5368667485673,8378.2064919358563,8305.9912754235775,8239.1202350305466,8176.4483158699913,8117.1866342392495,null,0.03,60.736472079402404,60.162543689976033,59.640198584602601,59.156590479649381,58.703420746888739,58.274972015623291]
[0.06,6914.8412154783682,6766.8546440962918,6640.2688574545509,6527.1826432290827,6423.586153214811,6327.1331621042391,null,0.06,49.660419382663186,48.590340630894346,47.675783814018132,46.858997535320825,46.110946772635913,45.414642068638742]
[0.09,5386.0325598932959,5179.3982480471041,5010.3619220260962,4862.2670340910827,4728.0195978592892,4603.8248089784674,null,0.09,38.68330282390027,37.191532870525322,35.971773395105124,34.903540648082028,33.935517879043097,33.040252173237974]
[0.12,3873.5841049001656,3616.366432954143,3412.9597067999744,3236.955878396433,3078.3846699445612,2932.1251602232783,null,0.12,27.824212877516537,25.969415457669662,24.503509115228429,23.235680070956235,22.093880736819678,21.041696496533707]