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f292f5a
Add efficiency parameters for Haber-Bosch process
amos-schledorn Sep 23, 2025
65cd66f
Add efficiency-heat parameter for Fischer-Tropsch
amos-schledorn Sep 23, 2025
681e67c
Add methanation efficiency from PyPSA-Eur assumptions
amos-schledorn Sep 24, 2025
1928d62
Add methanolisation heat efficiency
amos-schledorn Sep 24, 2025
cace6c2
refactor to leaner code
amos-schledorn Sep 24, 2025
590c7f9
[pre-commit.ci] auto fixes from pre-commit.com hooks
pre-commit-ci[bot] Sep 24, 2025
8d92417
Use heat-losses instead of heat-efficiency for methanalisation and in…
amos-schledorn Sep 24, 2025
afc0f3a
Update release notes
amos-schledorn Sep 24, 2025
cce4007
Make reading of additional DEA data technology-dependent
amos-schledorn Sep 24, 2025
9eae93b
fix technology-dependent parameters, adjust test
amos-schledorn Sep 24, 2025
d1d3bfd
Remove breakpoint from order_data function
amos-schledorn Sep 24, 2025
7461f32
[pre-commit.ci] auto fixes from pre-commit.com hooks
pre-commit-ci[bot] Sep 24, 2025
7f95e97
re-add biogas plus hydrogen heat efficiency
amos-schledorn Sep 24, 2025
a0bc487
[pre-commit.ci] auto fixes from pre-commit.com hooks
pre-commit-ci[bot] Sep 24, 2025
0db3e9c
remove biogas plus hydrogen heating efficiency
amos-schledorn Sep 24, 2025
3eeec00
update US costs
amos-schledorn Sep 24, 2025
dd69abc
revert methanolisation edits
amos-schledorn Sep 25, 2025
b706d55
revert manual inputs to heat losses
amos-schledorn Sep 25, 2025
232e348
update release notes
amos-schledorn Sep 25, 2025
0a70932
update Haber-Bosch values and description
amos-schledorn Sep 25, 2025
89f9283
Merge branch 'master' into feat--add-waste-heat-from-renewable-fuels
amos-schledorn Oct 20, 2025
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1 change: 1 addition & 0 deletions .gitignore
Original file line number Diff line number Diff line change
Expand Up @@ -24,3 +24,4 @@ gurobi.log
*.cb
*.cb2
.*.lb
.claude/*
2 changes: 2 additions & 0 deletions docs/release_notes.rst
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Expand Up @@ -16,6 +16,8 @@ Upcoming Release
.. The features listed below are not released yet, but will be part of the next release!
.. To use the features already you have to use the ``master`` branch.

* Add excess heat output rates for renewable fuel production (methanation, methanolisation, Fischer-Tropsch, Haber-Bosch) and fuel cells.

* Updated indexing of DEA Excel data for PTES and revised capital cost and FOM assumptions for 2045 and 2050.


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2 changes: 2 additions & 0 deletions inputs/manual_input.csv
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Expand Up @@ -10,6 +10,8 @@ methanation,FOM,2030,3,%/year,2017,"Agora Energiewende (2018): The Future Cost o
methanation,investment,2050,500,EUR/kW_CH4,2017,"Agora Energiewende (2018): The Future Cost of Electricity-Based Synthetic Fuels (https://www.agora-energiewende.de/en/publications/the-future-cost-of-electricity-based-synthetic-fuels-1/), table 6: “Reference scenario”.",
methanation,lifetime,2050,20,years,2017,Guesstimate.,"Based on lifetime for methanolisation, Fischer-Tropsch plants."
methanation,FOM,2050,3,%/year,2017,"Agora Energiewende (2018): The Future Cost of Electricity-Based Synthetic Fuels (https://www.agora-energiewende.de/en/publications/the-future-cost-of-electricity-based-synthetic-fuels-1/), section 6.2.3.1",
methanation,heat-losses,2020,0.05,per unit,2017,Based on PyPSA-Eur assumptions (total efficiency of 0.95),
fuel cell,heat-losses,2020,0.05,per unit,2017,Based on PyPSA-Eur assumptions (total efficiency of 0.95),
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Outdated
H2 (g) pipeline,investment,2020,363.08,EUR/MW/km,2023,European Hydrogen Backbone Report (June 2021): https://gasforclimate2050.eu/wp-content/uploads/2021/06/EHB_Analysing-the-future-demand-supply-and-transport-of-hydrogen_June-2021.pdf Table 35. Implementation roadmap - Cross border projects and costs updates: https://ehb.eu/files/downloads/EHB-2023-20-Nov-FINAL-design.pdf Table 1,"Assumption for a 48 inch single line pipeline, incl. compressor investments, 16.9 GW (LHV) peak capacity (source 2), 4.4 MEUR/km base cost with additional investment for compressors of capacity 434 MWe/1000 km (source 1), at 4 MEUR/MWe for compressor (source 2)"
H2 (g) pipeline,lifetime,2020,50,years,2015,"Danish Energy Agency, Technology Data for Energy Transport (2021), Excel datasheet: H2 140.","Assumption for a 140 bar, > 6000 MW_HHV single line pipeline, incl. booster station investments. Considering LHV by scaling with LHV/HHV=0.8462623413."
H2 (g) pipeline,FOM,2020,4,%/year,2015,"Danish Energy Agency, Technology Data for Energy Transport (2021), Excel datasheet: H2 140.","Assumption for a 140 bar, > 6000 MW_HHV single line pipeline, incl. booster station investments. Considering LHV by scaling with LHV/HHV=0.8462623413."
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6 changes: 6 additions & 0 deletions outputs/US/costs_2020.csv
Original file line number Diff line number Diff line change
Expand Up @@ -826,6 +826,7 @@ Fischer-Tropsch,VOM,5.636,EUR/MWh_FT,"Danish Energy Agency, inputs/data_sheets_f
Fischer-Tropsch,capture rate,0.9,per unit,Assumption based on doi:10.1016/j.biombioe.2015.01.006,,,,
Fischer-Tropsch,carbondioxide-input,0.32,t_CO2/MWh_FT,ICCT IRA e-fuels assumptions ,"Input per 1t FT liquid fuels output, carbon efficiency increases with years (4.3, 3.9, 3.6, 3.3 t_CO2/t_FT from 2020-2050 with LHV 11.95 MWh_th/t_FT).",,,
Fischer-Tropsch,efficiency,0.7,per unit,ICCT IRA e-fuels assumptions ,,,,
Fischer-Tropsch,efficiency-heat,0.25,per unit,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx","102 Hydrogen to Jet: District Heat Output,",2020.0,,
Fischer-Tropsch,electricity-input,0.04,MWh_el/MWh_FT,ICCT IRA e-fuels assumptions ,"0.005 MWh_el input per FT output, output increasing from 2020 to 2050 (0.65, 0.7, 0.73, 0.75 MWh liquid FT output).",,,
Fischer-Tropsch,hydrogen-input,1.43,MWh_H2/MWh_FT,ICCT IRA e-fuels assumptions ,"0.995 MWh_H2 per output, output increasing from 2020 to 2050 (0.65, 0.7, 0.73, 0.75 MWh liquid FT output).",,,
Fischer-Tropsch,investment,1482100.9059,USD/MW_FT,ICCT IRA e-fuels assumptions ,,2022.0,,
Expand Down Expand Up @@ -1049,6 +1050,7 @@ HVDC underground,investment,1008.2934,EUR/MW/km,Härtel et al. (2017): https://d
HVDC underground,lifetime,40.0,years,Purvins et al. (2018): https://doi.org/10.1016/j.jclepro.2018.03.095 .,"Based on estimated costs for a NA-EU connector (bidirectional,4 GW, 3000km length and ca. 3000m depth). Costs in return based on existing/currently under construction undersea cables. (same as for HVDC submarine)",2018.0,,
Haber-Bosch,FOM,3.0,%/year,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",103 Hydrogen to Ammonia: Fixed O&M,2015.0,,
Haber-Bosch,VOM,0.0225,EUR/MWh_NH3,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",103 Hydrogen to Ammonia: Variable O&M,2015.0,,
Haber-Bosch,efficiency-heat,0.0015,per unit,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",103 Hydrogen to Ammonia: High value heat Output,2015.0,,
Haber-Bosch,electricity-input,0.2473,MWh_el/MWh_NH3,"DECHEMA 2017: DECHEMA: Low carbon energy and feedstock for the European chemical industry (https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf), table 11.",Assume 5 GJ/t_NH3 for compressors and NH3 LHV = 5.16666 MWh/t_NH3.,,,
Haber-Bosch,hydrogen-input,1.1484,MWh_H2/MWh_NH3,"DECHEMA 2017: DECHEMA: Low carbon energy and feedstock for the European chemical industry (https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf), pg. 57.","178 kg_H2 per t_NH3, LHV for both assumed.",,,
Haber-Bosch,investment,1785.0713,EUR/kW_NH3,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",103 Hydrogen to Ammonia: Specific investment,2015.0,,
Expand Down Expand Up @@ -3955,6 +3957,7 @@ ethanol from sugar crops,lifetime,20.0,years,"JRC, 01_JRC-EU-TIMES Full model, h
fuel cell,FOM,5.0,%/year,"Danish Energy Agency, inputs/technology_data_for_el_and_dh.xlsx",12 LT-PEMFC CHP: Fixed O&M,2015.0,,
fuel cell,c_b,1.25,50oC/100oC,"Danish Energy Agency, inputs/technology_data_for_el_and_dh.xlsx",12 LT-PEMFC CHP: Cb coefficient,2015.0,,
fuel cell,efficiency,0.5,per unit,"Danish Energy Agency, inputs/technology_data_for_el_and_dh.xlsx","12 LT-PEMFC CHP: Electricity efficiency, annual average",2015.0,,
fuel cell,heat-losses,0.05,per unit,Based on PyPSA-Eur assumptions (total efficiency of 0.95),,2017.0,,
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Don't full understand the energy balance of the fuel cell:
Is it 1u of hydrogen --> 0.5u electricity + 0.05u heat losses + 0.45u high value heat?

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See above.

fuel cell,investment,1375.6881,EUR/kW_e,"Danish Energy Agency, inputs/technology_data_for_el_and_dh.xlsx",12 LT-PEMFC CHP: Nominal investment,2015.0,,
fuel cell,lifetime,10.0,years,"Danish Energy Agency, inputs/technology_data_for_el_and_dh.xlsx",12 LT-PEMFC CHP: Technical lifetime,2015.0,,
fuelwood,fuel,15.9997,EUR/MWhth,"JRC ENSPRESO ca avg for MINBIOWOO (FuelwoodRW), ENS_BaU_GFTM",,2010.0,,
Expand Down Expand Up @@ -4082,6 +4085,7 @@ lignite,lifetime,40.0,years,"Lazard's levelized cost of energy analysis - versio
methanation,FOM,3.0,%/year,"Agora Energiewende (2018): The Future Cost of Electricity-Based Synthetic Fuels (https://www.agora-energiewende.de/en/publications/the-future-cost-of-electricity-based-synthetic-fuels-1/), section 6.2.3.1",,2017.0,,
methanation,carbondioxide-input,0.198,t_CO2/MWh_CH4,"Götz et al. (2016): Renewable Power-to-Gas: A technological and economic review (https://doi.org/10.1016/j.renene.2015.07.066), Fig. 11 .",Additional H2 required for methanation process (2x H2 amount compared to stochiometric conversion).,,,
methanation,efficiency,0.8,per unit,Palzer and Schaber thesis, from old pypsa cost assumptions,2015.0,,
methanation,heat-losses,0.05,per unit,Based on PyPSA-Eur assumptions (total efficiency of 0.95),,2017.0,,
methanation,hydrogen-input,1.282,MWh_H2/MWh_CH4,,Based on ideal conversion process of stochiometric composition (1 t CH4 contains 750 kg of carbon).,,,
methanation,investment,777.5294,EUR/kW_CH4,"Agora Energiewende (2018): The Future Cost of Electricity-Based Synthetic Fuels (https://www.agora-energiewende.de/en/publications/the-future-cost-of-electricity-based-synthetic-fuels-1/), table 6: “Reference scenario”.",,2017.0,,
methanation,lifetime,20.0,years,Guesstimate.,"Based on lifetime for methanolisation, Fischer-Tropsch plants.",2017.0,,
Expand All @@ -4105,6 +4109,8 @@ methanol-to-olefins/aromatics,methanol-input,18.03,MWh_MeOH/t_HVC,"DECHEMA 2017:
methanolisation,FOM,3.0,%/year,"Agora Energiewende (2018): The Future Cost of Electricity-Based Synthetic Fuels (https://www.agora-energiewende.de/en/publications/the-future-cost-of-electricity-based-synthetic-fuels-1/), section 6.3.2.1.",,2017.0,,
methanolisation,capture rate,0.9,per unit,Assumption based on doi:10.1016/j.biombioe.2015.01.006,,,,
methanolisation,carbondioxide-input,0.248,t_CO2/MWh_MeOH,"DECHEMA 2017: DECHEMA: Low carbon energy and feedstock for the European chemical industry (https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf) , pg. 66.",,,,
methanolisation,efficiency,0.002,per unit,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",98 Methanol from hydrogen: District heating,2020.0,,
methanolisation,efficiency-heat,0.002,per unit,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",98 Methanol from hydrogen: District heating,2020.0,,
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methanolisation,electricity-input,0.271,MWh_e/MWh_MeOH,"DECHEMA 2017: DECHEMA: Low carbon energy and feedstock for the European chemical industry (https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf) , pg. 65.",,,,
methanolisation,heat-output,0.1,MWh_th/MWh_MeOH,"DECHEMA 2017: DECHEMA: Low carbon energy and feedstock for the European chemical industry (https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf) , pg. 65.",steam generation of 2 GJ/t_MeOH,,,
methanolisation,hydrogen-input,1.138,MWh_H2/MWh_MeOH,"DECHEMA 2017: DECHEMA: Low carbon energy and feedstock for the European chemical industry (https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf) , pg. 64.",189 kg_H2 per t_MeOH,,,
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6 changes: 6 additions & 0 deletions outputs/US/costs_2025.csv
Original file line number Diff line number Diff line change
Expand Up @@ -862,6 +862,7 @@ Fischer-Tropsch,VOM,5.0512,EUR/MWh_FT,"Danish Energy Agency, inputs/data_sheets_
Fischer-Tropsch,capture rate,0.9,per unit,Assumption based on doi:10.1016/j.biombioe.2015.01.006,,,,
Fischer-Tropsch,carbondioxide-input,0.32,t_CO2/MWh_FT,ICCT IRA e-fuels assumptions ,"Input per 1t FT liquid fuels output, carbon efficiency increases with years (4.3, 3.9, 3.6, 3.3 t_CO2/t_FT from 2020-2050 with LHV 11.95 MWh_th/t_FT).",,,
Fischer-Tropsch,efficiency,0.7,per unit,ICCT IRA e-fuels assumptions ,,,,
Fischer-Tropsch,efficiency-heat,0.225,per unit,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx","102 Hydrogen to Jet: District Heat Output,",2020.0,,
Fischer-Tropsch,electricity-input,0.04,MWh_el/MWh_FT,ICCT IRA e-fuels assumptions ,"0.005 MWh_el input per FT output, output increasing from 2020 to 2050 (0.65, 0.7, 0.73, 0.75 MWh liquid FT output).",,,
Fischer-Tropsch,hydrogen-input,1.43,MWh_H2/MWh_FT,ICCT IRA e-fuels assumptions ,"0.995 MWh_H2 per output, output increasing from 2020 to 2050 (0.65, 0.7, 0.73, 0.75 MWh liquid FT output).",,,
Fischer-Tropsch,investment,1482100.9059,USD/MW_FT,ICCT IRA e-fuels assumptions ,,2022.0,,
Expand Down Expand Up @@ -1085,6 +1086,7 @@ HVDC underground,investment,1008.2934,EUR/MW/km,Härtel et al. (2017): https://d
HVDC underground,lifetime,40.0,years,Purvins et al. (2018): https://doi.org/10.1016/j.jclepro.2018.03.095 .,"Based on estimated costs for a NA-EU connector (bidirectional,4 GW, 3000km length and ca. 3000m depth). Costs in return based on existing/currently under construction undersea cables. (same as for HVDC submarine)",2018.0,,
Haber-Bosch,FOM,3.0,%/year,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",103 Hydrogen to Ammonia: Fixed O&M,2015.0,,
Haber-Bosch,VOM,0.0225,EUR/MWh_NH3,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",103 Hydrogen to Ammonia: Variable O&M,2015.0,,
Haber-Bosch,efficiency-heat,0.0015,per unit,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",103 Hydrogen to Ammonia: High value heat Output,2015.0,,
Haber-Bosch,electricity-input,0.2473,MWh_el/MWh_NH3,"DECHEMA 2017: DECHEMA: Low carbon energy and feedstock for the European chemical industry (https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf), table 11.",Assume 5 GJ/t_NH3 for compressors and NH3 LHV = 5.16666 MWh/t_NH3.,,,
Haber-Bosch,hydrogen-input,1.1484,MWh_H2/MWh_NH3,"DECHEMA 2017: DECHEMA: Low carbon energy and feedstock for the European chemical industry (https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf), pg. 57.","178 kg_H2 per t_NH3, LHV for both assumed.",,,
Haber-Bosch,investment,1622.5424,EUR/kW_NH3,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",103 Hydrogen to Ammonia: Specific investment,2015.0,,
Expand Down Expand Up @@ -4041,6 +4043,7 @@ ethanol from sugar crops,lifetime,20.0,years,"JRC, 01_JRC-EU-TIMES Full model, h
fuel cell,FOM,5.0,%/year,"Danish Energy Agency, inputs/technology_data_for_el_and_dh.xlsx",12 LT-PEMFC CHP: Fixed O&M,2015.0,,
fuel cell,c_b,1.25,50oC/100oC,"Danish Energy Agency, inputs/technology_data_for_el_and_dh.xlsx",12 LT-PEMFC CHP: Cb coefficient,2015.0,,
fuel cell,efficiency,0.5,per unit,"Danish Energy Agency, inputs/technology_data_for_el_and_dh.xlsx","12 LT-PEMFC CHP: Electricity efficiency, annual average",2015.0,,
fuel cell,heat-losses,0.05,per unit,Based on PyPSA-Eur assumptions (total efficiency of 0.95),,2017.0,,
fuel cell,investment,1269.866,EUR/kW_e,"Danish Energy Agency, inputs/technology_data_for_el_and_dh.xlsx",12 LT-PEMFC CHP: Nominal investment,2015.0,,
fuel cell,lifetime,10.0,years,"Danish Energy Agency, inputs/technology_data_for_el_and_dh.xlsx",12 LT-PEMFC CHP: Technical lifetime,2015.0,,
fuelwood,fuel,15.261,EUR/MWhth,"JRC ENSPRESO ca avg for MINBIOWOO (FuelwoodRW), ENS_BaU_GFTM",,2010.0,,
Expand Down Expand Up @@ -4168,6 +4171,7 @@ lignite,lifetime,40.0,years,"Lazard's levelized cost of energy analysis - versio
methanation,FOM,3.0,%/year,"Agora Energiewende (2018): The Future Cost of Electricity-Based Synthetic Fuels (https://www.agora-energiewende.de/en/publications/the-future-cost-of-electricity-based-synthetic-fuels-1/), section 6.2.3.1",,2017.0,,
methanation,carbondioxide-input,0.198,t_CO2/MWh_CH4,"Götz et al. (2016): Renewable Power-to-Gas: A technological and economic review (https://doi.org/10.1016/j.renene.2015.07.066), Fig. 11 .",Additional H2 required for methanation process (2x H2 amount compared to stochiometric conversion).,,,
methanation,efficiency,0.8,per unit,Palzer and Schaber thesis, from old pypsa cost assumptions,2015.0,,
methanation,heat-losses,0.05,per unit,Based on PyPSA-Eur assumptions (total efficiency of 0.95),,2017.0,,
methanation,hydrogen-input,1.282,MWh_H2/MWh_CH4,,Based on ideal conversion process of stochiometric composition (1 t CH4 contains 750 kg of carbon).,,,
methanation,investment,728.6739,EUR/kW_CH4,"Agora Energiewende (2018): The Future Cost of Electricity-Based Synthetic Fuels (https://www.agora-energiewende.de/en/publications/the-future-cost-of-electricity-based-synthetic-fuels-1/), table 6: “Reference scenario”.",,2017.0,,
methanation,lifetime,20.0,years,Guesstimate.,"Based on lifetime for methanolisation, Fischer-Tropsch plants.",2017.0,,
Expand All @@ -4191,6 +4195,8 @@ methanol-to-olefins/aromatics,methanol-input,18.03,MWh_MeOH/t_HVC,"DECHEMA 2017:
methanolisation,FOM,3.0,%/year,"Agora Energiewende (2018): The Future Cost of Electricity-Based Synthetic Fuels (https://www.agora-energiewende.de/en/publications/the-future-cost-of-electricity-based-synthetic-fuels-1/), section 6.3.2.1.",,2017.0,,
methanolisation,capture rate,0.9,per unit,Assumption based on doi:10.1016/j.biombioe.2015.01.006,,,,
methanolisation,carbondioxide-input,0.248,t_CO2/MWh_MeOH,"DECHEMA 2017: DECHEMA: Low carbon energy and feedstock for the European chemical industry (https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf) , pg. 66.",,,,
methanolisation,efficiency,0.002,per unit,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",98 Methanol from hydrogen: District heating,2020.0,,
methanolisation,efficiency-heat,0.002,per unit,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",98 Methanol from hydrogen: District heating,2020.0,,
methanolisation,electricity-input,0.271,MWh_e/MWh_MeOH,"DECHEMA 2017: DECHEMA: Low carbon energy and feedstock for the European chemical industry (https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf) , pg. 65.",,,,
methanolisation,heat-output,0.1,MWh_th/MWh_MeOH,"DECHEMA 2017: DECHEMA: Low carbon energy and feedstock for the European chemical industry (https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf) , pg. 65.",steam generation of 2 GJ/t_MeOH,,,
methanolisation,hydrogen-input,1.138,MWh_H2/MWh_MeOH,"DECHEMA 2017: DECHEMA: Low carbon energy and feedstock for the European chemical industry (https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf) , pg. 64.",189 kg_H2 per t_MeOH,,,
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