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@@ -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,, | ||
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@@ -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,, | ||
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@@ -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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Contributor
There was a problem hiding this comment. Choose a reason for hiding this commentThe reason will be displayed to describe this comment to others. Learn more. Don't full understand the energy balance of the fuel cell:
Contributor
Author
There was a problem hiding this comment. Choose a reason for hiding this commentThe reason will be displayed to describe this comment to others. Learn more. See above. |
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| 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,, | ||
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@@ -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,, | ||
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@@ -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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cpschau marked this conversation as resolved.
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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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