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add methanol-to-olefins/aromatics and naphtha steam cracker
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fneum committed Aug 9, 2023
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2 changes: 2 additions & 0 deletions docs/release_notes.rst
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Expand Up @@ -11,6 +11,8 @@ Upcoming Release

* Add methanol-to-kerosene from `Concawe report <https://www.concawe.eu/wp-content/uploads/Rpt_22-17.pdf>`_.

* Add methanol-to-olefins/aromatics and steam cracker mostly from `DECHEMA report <https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry.pdf>`_.

Technology-Data 0.6.2 (7 August 2023)
=====================================

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14 changes: 14 additions & 0 deletions inputs/manual_input.csv
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Expand Up @@ -174,6 +174,20 @@ Ammonia cracker,investment,2050,527592.22,EUR/MW_H2,2015,"Ishimoto et al. (2020)
Ammonia cracker,lifetime,2050,25,years,2015,"Ishimoto et al. (2020): 10.1016/j.ijhydene.2020.09.017 , table 7.",
Ammonia cracker,FOM,2050,4.3,%/year,2015,"Ishimoto et al. (2020): 10.1016/j.ijhydene.2020.09.017 , table 7.","Estimated based on Labour cost rate, Maintenance cost rate, Insurance rate, Admin. cost rate and Chemical & other consumables cost rate."
Ammonia cracker,ammonia-input,0,1.46,MWh_NH3/MWh_H2,,"ENGIE et al (2020): Ammonia to Green Hydrogen Feasibility Study (https://assets.publishing.service.gov.uk/government/uploads/system/uploads/attachment_data/file/880826/HS420_-_Ecuity_-_Ammonia_to_Green_Hydrogen.pdf), Fig. 10.",Assuming a integrated 200t/d cracking and purification facility. Electricity demand (316 MWh per 2186 MWh_LHV H2 output) is assumed to also be ammonia LHV input which seems a fair assumption as the facility has options for a higher degree of integration according to the report).
methanol-to-olefins/aromatics,investment,2015,2628000,EUR/(t_HVC/h),2015,"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 35","Assuming CAPEX of 1200 €/t actually given in €/(t/a)."
methanol-to-olefins/aromatics,lifetime,2015,30,years,-,"Guesstimate","same as steam cracker"
methanol-to-olefins/aromatics,FOM,2015,3,%/year,-,"Guesstimate","same as steam cracker"
methanol-to-olefins/aromatics,VOM,2015,30,€/t_HVC,2015,"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 35",""
methanol-to-olefins/aromatics,electricity-input,2015,1.3889,MWh_el/t_HVC,-,"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), page 69","5 GJ/t_HVC"
methanol-to-olefins/aromatics,methanol-input,2015,18.03,MWh_MeOH/t_HVC,-,"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), Sections 4.5 (for ethylene and propylene) and 4.6 (for BTX)","Weighted average: 2.83 t_MeOH/t_ethylene+propylene for 21.7 Mt of ethylene and 17 Mt of propylene, 4.2 t_MeOH/t_BTX for 15.7 Mt of BTX. Assuming 5.54 MWh_MeOH/t_MeOH."
methanol-to-olefins/aromatics,carbondioxide-output,2015,0.6107,t_CO2/t_HVC,-,"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), Sections 4.5 (for ethylene and propylene) and 4.6 (for BTX)","Weighted average: 0.4 t_MeOH/t_ethylene+propylene for 21.7 Mt of ethylene and 17 Mt of propylene, 1.13 t_CO2/t_BTX for 15.7 Mt of BTX. The report also refere"
steam cracker,investment,2015,10512000,EUR/(t_HVC/h),2015,"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 35","Assuming CAPEX of 1200 €/t actually given in €/(t/a)."
steam cracker,lifetime,2015,30,years,-,"Guesstimate",""
steam cracker,FOM,2015,3,%/year,-,"Guesstimate",""
steam cracker,VOM,2015,180,€/t_HVC,2015,"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 35",""
steam cracker,naphtha-input,2015,14.8,MWh_naphtha/t_HVC,-,"Lechtenböhmer et al. (2016): 10.1016/j.energy.2016.07.110, Section 4.3, page 6.",""
steam cracker,electricity-input,2015,2.7,MWh_el/t_HVC,-,"Lechtenböhmer et al. (2016): 10.1016/j.energy.2016.07.110, Section 4.3, page 6.","Assuming electrified processing."
steam cracker,carbondioxide-output,2015,0.55,t_CO2/t_HVC,-,"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), ","The report also references another source with 0.76 t_CO2/t_HVC"
Steam methane reforming,investment,2015,470085.47008547,EUR/MW_H2,2015,"International Energy Agency (2015): Technology Roadmap Hydrogen and Fuel Cells , table 15.",Large scale SMR facility (150-300 MW). Currency conversion 1.17 USD = 1 EUR.
Steam methane reforming,lifetime,2015,30,years,2015,"International Energy Agency (2015): Technology Roadmap Hydrogen and Fuel Cells , table 15.",Large scale SMR facility (150-300 MW).
Steam methane reforming,FOM,2015,3,%/year,2015,"International Energy Agency (2015): Technology Roadmap Hydrogen and Fuel Cells , table 15.",Large scale SMR facility (150-300 MW).
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14 changes: 14 additions & 0 deletions outputs/costs_2020.csv
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Expand Up @@ -751,6 +751,13 @@ methane storage tank incl. compressor,lifetime,30.0,years,"Guesstimate, based on
methanol,CO2 intensity,0.25,tCO2/MWh_th,,
methanol-to-kerosene,hydrogen-input,0.03,MWh_H2/MWh_kerosene,"Concawe (2022): E-Fuels: A technoeconomic assessment of European domestic production and imports towards 2050 (https://www.concawe.eu/wp-content/uploads/Rpt_22-17.pdf), table 6.","Assuming LHV 11.94 kWh/kg for kerosene, 5.54 kWh/kg for methanol, 33.3 kWh/kg for hydrogen."
methanol-to-kerosene,methanol-input,1.08,MWh_MeOH/MWh_kerosene,"Concawe (2022): E-Fuels: A technoeconomic assessment of European domestic production and imports towards 2050 (https://www.concawe.eu/wp-content/uploads/Rpt_22-17.pdf), table 6.","Assuming LHV 11.94 kWh/kg for kerosene, 5.54 kWh/kg for methanol, 33.3 kWh/kg for hydrogen."
methanol-to-olefins/aromatics,FOM,3.0,%/year,Guesstimate,same as steam cracker
methanol-to-olefins/aromatics,VOM,30.0,€/t_HVC,"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 35",
methanol-to-olefins/aromatics,carbondioxide-output,0.61,t_CO2/t_HVC,"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), Sections 4.5 (for ethylene and propylene) and 4.6 (for BTX)","Weighted average: 0.4 t_MeOH/t_ethylene+propylene for 21.7 Mt of ethylene and 17 Mt of propylene, 1.13 t_CO2/t_BTX for 15.7 Mt of BTX. The report also refere "
methanol-to-olefins/aromatics,electricity-input,1.39,MWh_el/t_HVC,"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), page 69",5 GJ/t_HVC
methanol-to-olefins/aromatics,investment,2628000.0,EUR/(t_HVC/h),"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 35",Assuming CAPEX of 1200 €/t actually given in €/(t/a).
methanol-to-olefins/aromatics,lifetime,30.0,years,Guesstimate,same as steam cracker
methanol-to-olefins/aromatics,methanol-input,18.03,MWh_MeOH/t_HVC,"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), Sections 4.5 (for ethylene and propylene) and 4.6 (for BTX)","Weighted average: 2.83 t_MeOH/t_ethylene+propylene for 21.7 Mt of ethylene and 17 Mt of propylene, 4.2 t_MeOH/t_BTX for 15.7 Mt of BTX. Assuming 5.54 MWh_MeOH/t_MeOH. "
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.",
methanolisation,VOM,6.27,EUR/MWh_MeOH,"Danish Energy Agency, data_sheets_for_renewable_fuels.xlsx",98 Methanol from power: Variable O&M
methanolisation,capture rate,0.9,per unit,Assumption based on doi:10.1016/j.biombioe.2015.01.006,
Expand Down Expand Up @@ -839,6 +846,13 @@ solid biomass to hydrogen,FOM,4.25,%/year,"Zech et.al. DBFZ Report Nr. 19. Hy-NO
solid biomass to hydrogen,capture rate,0.9,per unit,Assumption based on doi:10.1016/j.biombioe.2015.01.006,
solid biomass to hydrogen,efficiency,0.56,per unit,"Zech et.al. DBFZ Report Nr. 19. Hy-NOW - Evaluierung der Verfahren und Technologien für die Bereitstellung von Wasserstoff auf Basis von Biomasse, DBFZ, 2014",
solid biomass to hydrogen,investment,4000.0,EUR/kW_th,"Zech et.al. DBFZ Report Nr. 19. Hy-NOW - Evaluierung der Verfahren und Technologien für die Bereitstellung von Wasserstoff auf Basis von Biomasse, DBFZ, 2014",
steam cracker,FOM,3.0,%/year,Guesstimate,
steam cracker,VOM,180.0,€/t_HVC,"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 35",
steam cracker,carbondioxide-output,0.55,t_CO2/t_HVC,"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), ",The report also references another source with 0.76 t_CO2/t_HVC
steam cracker,electricity-input,2.7,MWh_el/t_HVC,"Lechtenböhmer et al. (2016): 10.1016/j.energy.2016.07.110, Section 4.3, page 6.",Assuming electrified processing.
steam cracker,investment,10512000.0,EUR/(t_HVC/h),"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 35",Assuming CAPEX of 1200 €/t actually given in €/(t/a).
steam cracker,lifetime,30.0,years,Guesstimate,
steam cracker,naphtha-input,14.8,MWh_naphtha/t_HVC,"Lechtenböhmer et al. (2016): 10.1016/j.energy.2016.07.110, Section 4.3, page 6.",
uranium,fuel,2.6,EUR/MWh_th,Lazard s Levelized Cost of Energy Analysis - Version 13.0,
waste CHP,FOM,2.4,%/year,"Danish Energy Agency, technology_data_for_el_and_dh.xlsx","08 WtE CHP, Large, 50 degree: Fixed O&M"
waste CHP,VOM,27.28,EUR/MWh_e,"Danish Energy Agency, technology_data_for_el_and_dh.xlsx","08 WtE CHP, Large, 50 degree: Variable O&M "
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14 changes: 14 additions & 0 deletions outputs/costs_2025.csv
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Expand Up @@ -751,6 +751,13 @@ methane storage tank incl. compressor,lifetime,30.0,years,"Guesstimate, based on
methanol,CO2 intensity,0.25,tCO2/MWh_th,,
methanol-to-kerosene,hydrogen-input,0.03,MWh_H2/MWh_kerosene,"Concawe (2022): E-Fuels: A technoeconomic assessment of European domestic production and imports towards 2050 (https://www.concawe.eu/wp-content/uploads/Rpt_22-17.pdf), table 6.","Assuming LHV 11.94 kWh/kg for kerosene, 5.54 kWh/kg for methanol, 33.3 kWh/kg for hydrogen."
methanol-to-kerosene,methanol-input,1.08,MWh_MeOH/MWh_kerosene,"Concawe (2022): E-Fuels: A technoeconomic assessment of European domestic production and imports towards 2050 (https://www.concawe.eu/wp-content/uploads/Rpt_22-17.pdf), table 6.","Assuming LHV 11.94 kWh/kg for kerosene, 5.54 kWh/kg for methanol, 33.3 kWh/kg for hydrogen."
methanol-to-olefins/aromatics,FOM,3.0,%/year,Guesstimate,same as steam cracker
methanol-to-olefins/aromatics,VOM,30.0,€/t_HVC,"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 35",
methanol-to-olefins/aromatics,carbondioxide-output,0.61,t_CO2/t_HVC,"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), Sections 4.5 (for ethylene and propylene) and 4.6 (for BTX)","Weighted average: 0.4 t_MeOH/t_ethylene+propylene for 21.7 Mt of ethylene and 17 Mt of propylene, 1.13 t_CO2/t_BTX for 15.7 Mt of BTX. The report also refere "
methanol-to-olefins/aromatics,electricity-input,1.39,MWh_el/t_HVC,"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), page 69",5 GJ/t_HVC
methanol-to-olefins/aromatics,investment,2628000.0,EUR/(t_HVC/h),"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 35",Assuming CAPEX of 1200 €/t actually given in €/(t/a).
methanol-to-olefins/aromatics,lifetime,30.0,years,Guesstimate,same as steam cracker
methanol-to-olefins/aromatics,methanol-input,18.03,MWh_MeOH/t_HVC,"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), Sections 4.5 (for ethylene and propylene) and 4.6 (for BTX)","Weighted average: 2.83 t_MeOH/t_ethylene+propylene for 21.7 Mt of ethylene and 17 Mt of propylene, 4.2 t_MeOH/t_BTX for 15.7 Mt of BTX. Assuming 5.54 MWh_MeOH/t_MeOH. "
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.",
methanolisation,VOM,6.27,EUR/MWh_MeOH,"Danish Energy Agency, data_sheets_for_renewable_fuels.xlsx",98 Methanol from power: Variable O&M
methanolisation,capture rate,0.9,per unit,Assumption based on doi:10.1016/j.biombioe.2015.01.006,
Expand Down Expand Up @@ -839,6 +846,13 @@ solid biomass to hydrogen,FOM,4.25,%/year,"Zech et.al. DBFZ Report Nr. 19. Hy-NO
solid biomass to hydrogen,capture rate,0.9,per unit,Assumption based on doi:10.1016/j.biombioe.2015.01.006,
solid biomass to hydrogen,efficiency,0.56,per unit,"Zech et.al. DBFZ Report Nr. 19. Hy-NOW - Evaluierung der Verfahren und Technologien für die Bereitstellung von Wasserstoff auf Basis von Biomasse, DBFZ, 2014",
solid biomass to hydrogen,investment,3750.0,EUR/kW_th,"Zech et.al. DBFZ Report Nr. 19. Hy-NOW - Evaluierung der Verfahren und Technologien für die Bereitstellung von Wasserstoff auf Basis von Biomasse, DBFZ, 2014",
steam cracker,FOM,3.0,%/year,Guesstimate,
steam cracker,VOM,180.0,€/t_HVC,"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 35",
steam cracker,carbondioxide-output,0.55,t_CO2/t_HVC,"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), ",The report also references another source with 0.76 t_CO2/t_HVC
steam cracker,electricity-input,2.7,MWh_el/t_HVC,"Lechtenböhmer et al. (2016): 10.1016/j.energy.2016.07.110, Section 4.3, page 6.",Assuming electrified processing.
steam cracker,investment,10512000.0,EUR/(t_HVC/h),"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 35",Assuming CAPEX of 1200 €/t actually given in €/(t/a).
steam cracker,lifetime,30.0,years,Guesstimate,
steam cracker,naphtha-input,14.8,MWh_naphtha/t_HVC,"Lechtenböhmer et al. (2016): 10.1016/j.energy.2016.07.110, Section 4.3, page 6.",
uranium,fuel,2.6,EUR/MWh_th,Lazard s Levelized Cost of Energy Analysis - Version 13.0,
waste CHP,FOM,2.38,%/year,"Danish Energy Agency, technology_data_for_el_and_dh.xlsx","08 WtE CHP, Large, 50 degree: Fixed O&M"
waste CHP,VOM,26.9,EUR/MWh_e,"Danish Energy Agency, technology_data_for_el_and_dh.xlsx","08 WtE CHP, Large, 50 degree: Variable O&M "
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