{"text_format":"2","workbook":"xlsx","n_sheets":5,"sheets":["A1","A2","A3","B","C"],"not_rendered":{"charts":0,"images":0,"macros":0,"external_links":0,"defined_names":0,"comments":0,"pivot_tables":0},"unopened":[],"bounds":{"document_bytes":16777216,"sheet_cells":100000,"run_cost":"one","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":"A1","index":0,"n_rows":73,"n_cols":6,"rows_kept":73,"cut":false,"hidden":false,"merged":[[4,1,4,2],[4,3,4,5],[63,1,63,5],[68,1,68,5],[27,1,27,5],[43,1,43,5],[47,1,47,5],[14,0,14,5]]}
["Biological Upgrading Technologies for Advanced Biofuels & Products"]
[]
[]
[]
["Table A1","Example ",null,"From Applicant"]
["Parameter/Performance","Benchmark","Target","Benchmark (Current)","Intermediate Target","Final Target"]
["Feed (hydrolysate of what feed, conditioning process)","Corn stover hydrolysate","Corn stover hydrolysate"]
["Process type (e.g., SSF, Ferm, HHF)","SSF","HHF"]
["Biofuel or product","Biofuel","Biofuel"]
["Enzyme loading "]
["Inoculation level (g dry cell mass/L)"]
["Temperature (C)"]
["pH (pH units)"]
["Scale demonstrated (>1L, >10L, >100L, etc.)",">1L",">100L"]
["Final Product"]
["Type of product (biofuel or product)","Biofuel","Biofuel"]
["Specific product type (alcohol, hydrocarbon, specialty, etc.)","Alcohol","Alcohol"]
["Biofuel or product name","n-butanol","n-butanol"]
["Type(s) of subsequent separation(s) required","Distillation","Distillation"]
["Biofuel quality (please fill out for biofuels only):"]
["Btu content (Btu/gal)",100000,110000]
["Oxygen content (wt%)",0.25,0.22]
["TAN (total acid number) "]
["   Net biofuel yield (gal fuel/ton dry biomass)",90,95]
["Product quality (please fill out for non-biofuel products only):"]
["Product purity (%)","N/A","N/A"]
["   Net product yield (kg product/ton dry biomass)","N/A","N/A"]
["Initial concentrations:"]
["Total Solids (%)",0.2,0.2]
["Insoluble Solids (%)"]
["Catalyst loading (g/L)"]
["Glucose (g/L)",66,66]
["Xylose (g/L)",25,25]
["Arabinose (g/L)",7,7]
["Other monomeric sugar (g/L)",2,2]
["Gluc + C6-oligomers (g/L)"]
["Xylo + C5-oligomers (g/L)"]
["Furfural (g/L)"]
["HMF (g/L)"]
["Other sugar-derived oxygenates, convertible (g/L)"]
["Solubilized lignin (g/L)"]
["Acetate (g/L)"]
["Other organics, non-convertible (g/L)",{"$f":"4229*1000/418163","v":10.113281184609829},{"$f":"4629*1000/433898","v":10.668405938722925}]
["Sugar Utilization"]
["Glucose (%)",100,100]
["Xylose (%)",85,94]
["Other sugars (%)",0,90]
["Final Concentrations"]
["Total Solids (%)"]
["Insoluble Solids (%)"]
["Catalyst loading (g/L)"]
["Glucose (g/L)",63,60]
["Xylose (g/L)",24,20]
["Arabinose (g/L)",7,5]
["Other monomeric sugar (g/L)",2,2]
["Gluc + C6-oligomers (g/L)"]
["Xylo + C5-oligomers (g/L)"]
["Furfural (g/L)"]
["HMF (g/L)"]
["Other sugar-derived oxygenates, convertible (g/L)"]
["Solubilized lignin (g/L)"]
["Acetate (g/L)"]
["Other organics, non-convertible (g/L)"]
["Biofuel Yields (% theoretical)"]
["Glucose to fuel (%)",95,95]
["Xylose to fuel (%)",75,85]
["Other sugars to fuel (%)",0,85]
["Final fuel titer (g/L)",50,62]
["Robustness"]
["Reaction rate (time to achieve yields above) (hours)","84-168","36-48"]
["Avg. Volumetric Productivity (g/L-h)"]
["Max. Vol. Productivity (g/L-h)"]
["References/Notes","An example only. ","An example only. "]

{"sheet":"A2","index":1,"n_rows":93,"n_cols":6,"rows_kept":93,"cut":false,"hidden":false,"merged":[[5,1,5,2],[5,3,5,5],[83,0,83,5],[88,1,88,5],[14,0,14,5],[34,0,34,5],[47,0,47,5],[67,0,67,5],[63,0,63,5]]}
["Chemical Upgrading Technologies for Advanced Biofuels & Products"]
[]
[]
[]
[]
["Table A2","Example ",null,"From Applicant"]
["Parameter/Performance","Benchmark","Target","Benchmark (Current)","Intermediate Target","Final Target"]
["Feed type (hydrolysate of what feedstock, what conditioning, etc.)","Corn stover hydrolysate","Corn stover hydrolysate"]
["Production mode (batch, continuous, other)","SSF","HHF"]
["Scale demonstrated (>1L, >10L, >100L, etc.)",">1L",">100L"]
["Catalyst loading level (g catalyst/g biomass or g sugar)"]
["Additional re-agent loading (g/g biomass or g sugar)"]
["Temperature (C)"]
["Pressure (psi)"]
["Catalyst Description/Performance"]
["Catalyst Economics"]
["Catalyst Production Cost ($/kg)",120,110]
["Catayst Regeneration Cost ($/kg)",80,80]
["Catalyst On-stream Time (%)",0.7,0.75]
["Catalyst Lifetime (yr)",0.1,0.125]
["Catalyst Performance"]
["Selectivity (molar selectivity)"]
["Activity (WHSV)"]
["Stability (hrs on stream between regenerations)",0.75,0.8]
["Catalyst type:"]
["Homogeneous:"]
["metal","X","X"]
["ligand"]
["catalyst-product separation"]
["solvent system"]
["Heterogeneous:"]
["gas/liquid phase"]
["solvent system (if liquid)"]
["metals/supports"]
["Final Product"]
["Type of product (biofuel or product)","Biofuel","Biofuel"]
["Specific product type (alcohol, hydrocarbon, specialty, etc.)","Alcohol","Alcohol"]
["Biofuel or product name","n-butanol","n-butanol"]
["Type(s) of subsequent separation(s) required","Distillation","Distillation"]
["Biofuel quality (please fill out for biofuels only):"]
["Btu content (Btu/gal)",100000,110000]
["Oxygen content (wt%)",0.25,0.22]
["TAN (total acid number) "]
["   Net biofuel yield (gal fuel/ton dry biomass)",90,95]
["Product quality (please fill out for non-biofuel products only):"]
["Product purity (%)","N/A","N/A"]
["   Net product yield (kg product/ton dry biomass)","N/A","N/A"]
["Initial Concentrations"]
["Total Solids (%)",0.2,0.2]
["Insoluble Solids (%)"]
["Catalyst loading (g/L)",60,60]
["Glucose (g/L)",66,66]
["Xylose (g/L)",25,25]
["Arabinose (g/L)",7,7]
["Other monomeric sugar (g/L)",2,2]
["Gluc + C6-oligomers (g/L)"]
["Xylo + C5-oligomers (g/L)"]
["Furfural (g/L)"]
["HMF (g/L)"]
["Other sugar-derived oxygenates, convertible (g/L)"]
["Solubilized lignin (g/L)"]
["Acetate (g/L)"]
["Other organics, non-convertible (g/L)"]
["Sugar Utilization"]
["Glucose (%)",100,100]
["Xylose (%)",85,94]
["Other sugars (%)",0,30]
["Final Concentrations"]
["Total Solids (%)",0.2,0.18]
["Insoluble Solids (%)"]
["Catalyst loading (g/L)",50,53]
["Glucose (g/L)",63,60]
["Xylose (g/L)",24,20]
["Arabinose (g/L)",7,5]
["Other monomeric sugar (g/L)",2,2]
["Gluc + C6-oligomers (g/L)"]
["Xylo + C5-oligomers (g/L)"]
["Furfural (g/L)"]
["HMF (g/L)"]
["Other sugar-derived oxygenates, convertible (g/L)"]
["Solubilized lignin (g/L)"]
["Acetate (g/L)"]
["Other organics, non-convertible (g/L)"]
["Biofuel Yields (% theoretical)"]
["Glucose to fuel (%)",95,95]
["Xylose to fuel (%)",75,85]
["Other sugars to fuel (%)",0,85]
["Final fuel titer (g/L)",50,62]
["Robustness"]
["Total Reaction Time (h)","84-167","36-47"]
["Avg. Volumetric Productivity (g/L-h)"]
["Max. Vol. Productivity (g/L-h)"]
["References/Notes","An example only. ","An example only. "]

{"sheet":"A3","index":2,"n_rows":95,"n_cols":6,"rows_kept":95,"cut":false,"hidden":false,"merged":[[87,1,87,5],[4,1,4,2],[4,3,4,5],[13,0,13,5],[33,0,33,5],[46,0,46,5],[62,0,62,5],[66,0,66,5],[82,0,82,5]]}
["Hybrid (combination biological & chemical) Upgrading Technologies for Advanced Biofuels or Products"]
[]
[]
[]
["Table A3","Example ",null,"From Applicant"]
["Parameter/Performance","Benchmark","Target","Benchmark (Current)","Intermediate Target","Final Target"]
["Feed type (hydrolysate of what feedstock, what conditioning, etc.)","Corn stover hydrolysate","Corn stover hydrolysate"]
["Production mode (batch, continuous, other)","SSF","HHF"]
["Scale demonstrated (>1L, >10L, >100L, etc.)",">1L",">100L"]
["Catalyst loading level (g catalyst/g biomass or g sugar)"]
["Additional re-agent loading (g/g biomass or g sugar)"]
["Temperature (C)"]
["Pressure (psi)"]
["Catalyst Description/Performance"]
["Catalyst Economics"]
["Catalyst Production Cost ($/kg)",120,110]
["Catayst Regeneration Cost ($/kg)",80,80]
["Catalyst On-stream Time (%)",0.7,0.75]
["Catalyst Lifetime (yr)",0.1,0.125]
["Catalyst Performance"]
["Selectivity (molar selectivity)"]
["Activity (WHSV)"]
["Stability (hrs on stream between regenerations)",0.75,0.8]
["Catalyst type:"]
["Homogeneous:"]
["metal","X","X"]
["ligand"]
["catalyst-product separation"]
["solvent system"]
["Heterogeneous:"]
["gas/liquid phase"]
["solvent system (if liquid)"]
["metals/supports"]
["Final Product"]
["Type of product (biofuel or product)","Biofuel","Biofuel"]
["Specific product type (alcohol, hydrocarbon, specialty, etc.)","Alcohol","Alcohol"]
["Biofuel or product name","n-butanol","n-butanol"]
["Type(s) of subsequent separation(s) required","Distillation","Distillation"]
["Biofuel quality (please fill out for biofuels only):"]
["Btu content (Btu/gal)",100000,110000]
["Oxygen content (wt%)",0.25,0.22]
["TAN (total acid number) "]
["   Net biofuel yield (gal fuel/ton dry biomass)",90,95]
["Product quality (please fill out for non-biofuel products only):"]
["Product purity (%)","N/A","N/A"]
["   Net product yield (kg product/ton dry biomass)","N/A","N/A"]
["Initial Concentrations"]
["Total Solids (%)",0.2,0.2]
["Insoluble Solids (%)"]
["Catalyst loading (g/L)",60,60]
["Glucose (g/L)",66,66]
["Xylose (g/L)",25,25]
["Arabinose (g/L)",7,7]
["Other monomeric sugar (g/L)",2,2]
["Gluc + C6-oligomers (g/L)"]
["Xylo + C5-oligomers (g/L)"]
["Furfural (g/L)"]
["HMF (g/L)"]
["Other sugar-derived oxygenates, convertible (g/L)"]
["Solubilized lignin (g/L)"]
["Acetate (g/L)"]
["Other organics, non-convertible (g/L)"]
["Sugar Utilization"]
["Glucose (%)",100,100]
["Xylose (%)",85,94]
["Other sugars (%)",0,30]
["Final Concentrations"]
["Total Solids (%)"]
["Insoluble Solids (%)"]
["Catalyst loading (g/L)",50,53]
["Glucose (g/L)",63,60]
["Xylose (g/L)",24,20]
["Arabinose (g/L)",7,5]
["Other monomeric sugar (g/L)",2,2]
["Gluc + C6-oligomers (g/L)"]
["Xylo + C5-oligomers (g/L)"]
["Furfural (g/L)"]
["HMF (g/L)"]
["Other sugar-derived oxygenates, convertible (g/L)"]
["Solubilized lignin (g/L)"]
["Acetate (g/L)"]
["Other organics, non-convertible (g/L)"]
["Biofuel Yields (% theoretical)"]
["Glucose to fuel (%)",95,95]
["Xylose to fuel (%)",75,85]
["Other sugars to fuel (%)",0,85]
["Final fuel titer (g/L)",50,62]
["Processing Steps Used"]
["Process Step 1","Acid pretreatment","Acid pretreatment"]
["Process Step 2","Fermentation","Combined fermentation & catalytic upgrading"]
["Process Step 3","Catalytic upgrading","Distillation"]
["Process Step 4","Distillation","N/A"]
["Process Step 5","N/A","N/A"]
["Process Step 6","N/A","N/A"]
["References/Notes","An example only. ","An example only. "]

{"sheet":"B","index":3,"n_rows":46,"n_cols":9,"rows_kept":46,"cut":false,"hidden":false,"merged":[[43,0,43,7],[2,1,2,3],[2,4,2,7],[30,2,30,3],[5,8,42,8],[18,2,18,3],[5,0,5,7],[17,0,17,7]]}
["Separations Technologies for Advanced Biofuels or Products"]
[]
["Table B","Example ",null,null,"From Applicant"]
["Parameter/Performance","Component Names","Benchmark","Target","Component Names","Benchmark (Current)","Intermediate Target","Final Target"]
["Preceeding Process Step"]
["Feed Stream data",{"$nulls":7},"Please add rows here as appropriate for ALL feed and output streams, and/or for multi-stage processes"]
["Composition by component (mol%)"]
["Component A:","C2H6",0.5,0.5]
["Component B:","C3H8",0.3,0.3]
["Component C:","iC4H10",0.2,0.2]
["Component D:","N/A"]
["Component E:","N/A"]
["Component F:","N/A"]
["Flow rate (L/h)",null,100,100]
["Temperature (oC)"]
["Pressure (psi)"]
["Phase/state"]
["Output Stream(s) data"]
["Stream Reference ID:",null,"Propane (C3)"]
["Composition by component (mol%)"]
["Component A:","C2H6",0.1,0.02]
["Component B:","C3H8",0.86,0.97]
["Component C:","iC4H10",0.04,0.01]
["Component D:","N/A"]
["Component E:","N/A"]
["Component F:","N/A"]
["Flow rate (L/h)",null,20,25]
["Temperature (oC)"]
["Pressure (psi)"]
["Phase/state"]
["Stream Reference ID:",null,"Other"]
["Composition by component (mol%)"]
["Component A:","C2H6",0.6,0.66]
["Component B:","C3H8",0.16,7.6666999999999999E-2]
["Component C:","iC4H10",0.24,0.26333299999999998]
["Component D:","N/A"]
["Component E:","N/A"]
["Component F:","N/A"]
["Flow rate (L/h)",null,80,75]
["Temperature (oC)"]
["Pressure (psi)"]
["Phase/state"]
["Product/Fuel Purity",null,0.86,0.97]
[]
["Proceeding Process Step"]
["References/Notes"]

{"sheet":"C","index":4,"n_rows":62,"n_cols":6,"rows_kept":62,"cut":false,"hidden":false,"merged":[[48,0,48,5],[47,0,47,5],[1,5,2,5],[3,0,3,1],[6,0,6,1],[1,2,2,2],[1,3,2,3],[1,4,2,4],[5,0,5,1],[56,2,56,4],[51,2,51,4],[52,2,52,4],[53,2,53,4],[54,2,54,4],[55,2,55,4],[57,2,57,4],[58,2,58,4],[59,2,59,4],[61,2,61,4],[60,2,60,4]]}
["Process Details and Costs "]
["Feedstock Type",null,"Benchmark or Current Process","Intermediate Target","Final Target Process\n(36 months)","Anticipated cost improvements are due to:"]
["Feed Rate (dry ton/day)"]
["Biofuel Yield (gallons/dry ton)"]
["BioProduct Yield (if applicable, gal/dry ton)"]
["Line 1:  Annual Biofuel of Product Production (MM gallons)"]
["Line 1a:  Annual BioProduct Production (MM gallons)"]
["Equipment Costs (2013$) (Biochemical)","Description","Installed Capital Cost (MM$)",null,"Installed Capital Cost (MM$)"]
["Feedstock Storage and Handling"]
["Pretreatment and Conditioning"]
["Enzymatic Hydrolysis, Hydrolysate Conditioning, & Bioconversion"]
["Cellulase Enzyme Production"]
["Product Recovery and Upgrading"]
["Wastewater Treatment"]
["Product and Feed Chemical Storage"]
["Combustor, Boiler, and Turbogenerator"]
["Utilities (include steam/electricity here or in operating costs)"]
["Line 2:  Total Installed Capital"]
["Total Installed Capital per Annual Gallon (line 2 divided by line 1)"]
["Operating Costs (2013$)","Description","MM$/yr",null,"MM$/yr"]
["Feedstock Storage and Handling"]
["Pretreatment and Conditioning"]
["Enzymatic Hydrolysis, Hydrolysate Conditioning, & Bioconversion"]
["Cellulase Enzyme Production"]
["Product Recovery and Upgrading"]
["Wastewater Treatment"]
["Product and Feed Chemical Storage"]
["Combustor, Boiler, and Turbogenerator"]
["Waste Disposal"]
["Steam"]
["Electricity"]
["Labor and Maintenance"]
["Line 3:  Total Operating Costs"]
["Line 4:  Co-product Credits"]
["Line 5:  Net Operating Costs (line 3 minus line 4)"]
["Net Biofuel or Product Production Costs ($/gal) (line 5 divided by line 1)"]
["Energy1 Balance Information",null,"Annual Value/Units","Annual Value/Units","Annual Value/Units"]
["Inputs:2","Purchased Electricity"]
[null,"Purchased Steam or Hot Water"]
[null,"Coal"]
[null,"Natural Gas"]
[null,"Diesel"]
[null,"CHP"]
[null,"Others (specify):"]
["Outputs:","Excess Electricity Generated"]
[null,"Others (specify):"]
[]
["1Energy balance information should include a list of any energy and process heat inputs and outputs used in the pathway, including such sources produced off site or by another entity.   "]
["2Energy input information should include fuels used by type, including purchased electricity.  Indicate the source, type of fuel required, efficiency, and temperature/pressure for any steam or hot water purchased for the fuel production process."]
[]
[]
["Fixed costs (utilize as appropriate):","Feedstock Storage and Handling",26.9,null,null,"Installed Costs MM(2013$)"]
["(Source: NREL Design Report (2013))","Pretreatment and Conditioning",53.6]
[null,"Enzymatic Hydrolysis, Hydrolysate Conditioning, & Bioconversion",73.400000000000006]
[null,"Cellulase Enzyme Production",12.4]
[null,"Product Recovery and Upgrading",26.6]
[null,"Wastewater Treatment",60.1]
[null,"Product and Feed Chemical Storage",3.4]
[null,"Combustor, Boiler, and Turbogenerator",76]
[null,"Utilities",8.8000000000000007]
[null,"Feedstock","$80/dry ton"]
[null,"Enzymes (Cellulase)","$0.39/gallon of renewable diesel blendstock"]