{"text_format":"2","workbook":"xlsx","n_sheets":4,"sheets":["Subtopic 1a","Subtopic 1b","Subtopic 1c","Subtopic 1d"],"not_rendered":{"charts":0,"images":0,"macros":0,"external_links":1,"defined_names":3,"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":"Subtopic 1a","index":0,"n_rows":25,"n_cols":6,"rows_kept":25,"cut":false,"hidden":false,"merged":[]}
["Metric","Units","Current State of the Art","Status of Proposed Approach (if available)","Metric Target for end of project","Commercialization Target"]
[]
["Blue cells are to be edited by the applicant. Green cells are automatically calcuated based on applicant input."]
[]
["Feedstock","[use consistant units for feedstock ]","[Define target feedstock]","[Define target feedstock]","[Define target feedstock]","[Define target feedstock]"]
["Molar yield (optional)","[e.g., mol H2/mol glucose]"]
["Hydrogen yield from feedstock under study (required)","[g H2/unit feedstock]"]
["Hydrogen Production Rate","L/L/Day*"]
["Feedstock concentration in reactor","[unit feedstock/liter]"]
["Feedstock costs","[$/unit feedstock]**"]
[null,"*Liters hydrogen under standard conditions, per liter reactor volume, per day"]
[null,"** Souce (for feedstock costs not from the H2A Hydrogen Production Cost Analysis tool, below): "]
["Calculated Values "]
["Minimum feedstock cost contribution","$/kg",{"$f":"C10/C7*1000","v":{"$error":"#DIV/0!"}},{"$f":"D10/D7*1000","v":{"$error":"#DIV/0!"}},{"$f":"E10/E7*1000","v":{"$error":"#DIV/0!"}},{"$f":"F10/F7*1000","v":{"$error":"#DIV/0!"}}]
["Reactor size for 1,000 kg per day","1000 L",{"$f":"(1000/(C8/12000))/1000","v":{"$error":"#DIV/0!"}},{"$f":"(1000/(D8/12000))/1000","v":{"$error":"#DIV/0!"}},{"$f":"(1000/(E8/12000))/1000","v":{"$error":"#DIV/0!"}},{"$f":"(1000/(F8/12000))/1000","v":{"$error":"#DIV/0!"}}]
[]
[]
["Feedstock Type","Unit","$(2007)/unit","Source"]
["Woody Biomass","kg",2.7828237281268226E-2,"H2A Hydrogen Production Cost Analysis tool (http://www.hydrogen.energy.gov/h2a_production.html) "]
["Woody Biomass B2A","kg",5.5889788385402865E-2,"H2A Hydrogen Production Cost Analysis tool (http://www.hydrogen.energy.gov/h2a_production.html) "]
["Woody Biomass MYPP (2011)","kg",7.2892857142857148E-2,"H2A Hydrogen Production Cost Analysis tool (http://www.hydrogen.energy.gov/h2a_production.html) "]
["Woody Biomass MYPP (2014)","Dry Metric Ton",80,"Bioenergy Technology Office Multiyear Program Plan (http://energy.gov/sites/prod/files/2015/01/f19/mypp_beto_november_2014_0.pdf)"]
["Bio Methane","mmBtu",13.11,"H2A Hydrogen Production Cost Analysis tool (http://www.hydrogen.energy.gov/h2a_production.html) "]
[]
["NOTE: The Formula for \"Minimum feedstock cost contribution\" has been update to fix an error."]

{"sheet":"Subtopic 1b","index":1,"n_rows":18,"n_cols":6,"rows_kept":18,"cut":false,"hidden":false,"merged":[]}
["Metric","Units","Current State of the Art","Status of Proposed Approach (if available)","Metric Target for the end of the project","MYRD&D Target or Commercialization Target"]
[]
["Platinum group metal (PGM) total content (both electrodes) ","g/kW",null,null,null,"<0.125"]
[]
["PGM total loading (both electrodes) ","mg/cm2",null,null,null,"<0.125"]
[]
["Loss in catalytic (mass) activitya,b","% loss",null,null,null,"<40"]
[]
["Loss in performance at 0.8 A/cm2 a ","mV",null,null,null,30]
[]
["Loss in performance at 1.5 A/cm2 b","mV",null,null,null,30]
[]
["Mass activity @ 900 mViR-freec","A/mgPGM",null,null,null,0.44]
[]
[]
["a.       Durability testing performed according to Table E1 of Appendix E."]
["b.      Durability testing performed according to Table E2 of Appendix E."]
["c.       Test at 80°C H2/O2 in MEA; fully humidified with total outlet pressure of 150 kPa (abs); anode stoichiometry 2; cathode stoichiometry 9.5 (Gasteiger et al., Applied Catalysis B: Environmental, 56 (2005) 9-35)."]

{"sheet":"Subtopic 1c","index":2,"n_rows":8,"n_cols":5,"rows_kept":8,"cut":false,"hidden":false,"merged":[]}
["Metric","Current State of the Art","Status of Proposed Approach (if available)","Metric Target for the end of the project","MYRD&D Target or Commercialization Target"]
[]
["Dispensing Accuracy at:"]
["          -40 C",null,null,null,1.4999999999999999E-2]
["           25 C",null,null,null,1.4999999999999999E-2]
["           85 C",null,null,null,1.4999999999999999E-2]
[]
["Dispenser High Volume Capital Cost",null,null,null,40000]

{"sheet":"Subtopic 1d","index":3,"n_rows":5,"n_cols":5,"rows_kept":5,"cut":false,"hidden":false,"merged":[]}
["Metric","Current State of the Art","Status of Proposed Approach (if available)","Target for the end of the project","MYRD&D Target or Commercialization Target"]
[]
["Cost to install pipeline per mile per inch ID of pipe - per mile, excluding right of way",null,null,null,"$320,000/inch-mile"]
[]
["Maximum leak rate of pipeline",null,null,null,"6 kg H2/mile-year"]