diff --git a/docs/release_notes.rst b/docs/release_notes.rst index 278b69b3..07290116 100644 --- a/docs/release_notes.rst +++ b/docs/release_notes.rst @@ -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 technology data for `CO2 dense phase compression` step for transport in large pipelines (https://github.com/PyPSA/technology-data/pull/273) which is different from the current `CO2 liquefaction` technology parameters that is take for ship transport. + * Add missing discount rate for OCGT in US-specific data. (https://github.com/PyPSA/technology-data/pull/269) `v0.14.0 `__ (13th February 2026) diff --git a/inputs/manual_input.csv b/inputs/manual_input.csv index c49112ee..57d482ac 100644 --- a/inputs/manual_input.csv +++ b/inputs/manual_input.csv @@ -192,6 +192,11 @@ NH3 (l) storage tank incl. liquefaction,lifetime,2020,20,years,2010,"Morgan E. 2 CO2 storage tank,investment,2050,2430,EUR/t_CO2,2013,"Lauri et al. 2014: doi: 10.1016/j.egypro.2014.11.297, Table 3.","Assuming a 3000m^3 pressurised steel cylinder tanks and a CO2 density of 1100 kg/m^3 (close to triple point at -56.6°C and 5.2 bar with max density of 1200kg/m^3 ). Lauri et al. report costs 3x higher per m^3 for steel tanks, which are consistent with other sources. The numbers reported are in rather difficult to pinpoint as systems can greatly vary." CO2 storage tank,FOM,2050,1,%/year,2013,"Lauri et al. 2014: doi: 10.1016/j.egypro.2014.11.297, pg. 2746 .","Assuming a 3000m^3 pressurised steel cylinder tanks and a CO2 density of 1100 kg/m^3 (close to triple point at -56.6°C and 5.2 bar with max density of 1200kg/m^3 ). Lauri et al. report costs 3x higher per m^3 for steel tanks, which are consistent with other sources. The numbers reported are in rather difficult to pinpoint as systems can greatly vary." CO2 storage tank,lifetime,2050,25,years,2013,"Lauri et al. 2014: doi: 10.1016/j.egypro.2014.11.297, pg. 2746 .","Assuming a 3000m^3 pressurised steel cylinder tanks and a CO2 density of 1100 kg/m^3 (close to triple point at -56.6°C and 5.2 bar with max density of 1200kg/m^3 ). Lauri et al. report costs 3x higher per m^3 for steel tanks, which are consistent with other sources. The numbers reported are in rather difficult to pinpoint as systems can greatly vary." +CO2 dense phase compression,investment,2024,33288,EUR/t_CO2/h,2024,"Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf", "Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h" +CO2 dense phase compression,FOM,2024,5,%/year,2024,"Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf", +CO2 dense phase compression,lifetime,2024,25,years,2024,"Guesstimate, based on CH4 liquefaction.", +CO2 dense phase compression,carbondioxide-input,0,1,t_CO2/t_CO2,-,, +CO2 dense phase compression,electricity-input,0,0.1051,MWh_el/t_CO2,-,"Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf", CO2 liquefaction,investment,2004,12.8928283642224,EUR/t_CO2/h,2004,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Plant capacity of 20 kt CO2 / d and an uptime of 85%. For a high purity, humid, low pressure input stream, includes drying and compression necessary for liquefaction." CO2 liquefaction,FOM,2004,5,%/year,2004,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf ., CO2 liquefaction,lifetime,2004,25,years,2004,"Guesstimate, based on CH4 liquefaction.", diff --git a/outputs/US/costs_2020.csv b/outputs/US/costs_2020.csv index 962739c9..bcd985a2 100644 --- a/outputs/US/costs_2020.csv +++ b/outputs/US/costs_2020.csv @@ -134,6 +134,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0,, CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0,, CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.",,, +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0,, +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0,, +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0,, CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0,, CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.",,, CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,,, diff --git a/outputs/US/costs_2025.csv b/outputs/US/costs_2025.csv index 1323c389..9cde2344 100644 --- a/outputs/US/costs_2025.csv +++ b/outputs/US/costs_2025.csv @@ -134,6 +134,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0,, CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0,, CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.",,, +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0,, +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0,, +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0,, CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0,, CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.",,, CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,,, diff --git a/outputs/US/costs_2030.csv b/outputs/US/costs_2030.csv index 7a853548..0ce92b44 100644 --- a/outputs/US/costs_2030.csv +++ b/outputs/US/costs_2030.csv @@ -134,6 +134,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0,, CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0,, CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.",,, +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0,, +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0,, +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0,, CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0,, CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.",,, CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,,, diff --git a/outputs/US/costs_2035.csv b/outputs/US/costs_2035.csv index ffecc32b..1c66a292 100644 --- a/outputs/US/costs_2035.csv +++ b/outputs/US/costs_2035.csv @@ -134,6 +134,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0,, CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0,, CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.",,, +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0,, +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0,, +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0,, CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0,, CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.",,, CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,,, diff --git a/outputs/US/costs_2040.csv b/outputs/US/costs_2040.csv index 79ee49bc..d67f442d 100644 --- a/outputs/US/costs_2040.csv +++ b/outputs/US/costs_2040.csv @@ -134,6 +134,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0,, CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0,, CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.",,, +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0,, +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0,, +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0,, CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0,, CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.",,, CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,,, diff --git a/outputs/US/costs_2045.csv b/outputs/US/costs_2045.csv index 23d4ac38..d98a5e26 100644 --- a/outputs/US/costs_2045.csv +++ b/outputs/US/costs_2045.csv @@ -134,6 +134,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0,, CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0,, CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.",,, +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0,, +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0,, +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0,, CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0,, CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.",,, CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,,, diff --git a/outputs/US/costs_2050.csv b/outputs/US/costs_2050.csv index c5d89281..0d84b9c9 100644 --- a/outputs/US/costs_2050.csv +++ b/outputs/US/costs_2050.csv @@ -134,6 +134,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0,, CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0,, CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.",,, +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0,, +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0,, +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0,, CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0,, CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.",,, CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,,, diff --git a/outputs/costs_2020.csv b/outputs/costs_2020.csv index 1dbe1cc7..f72ff7fe 100644 --- a/outputs/costs_2020.csv +++ b/outputs/costs_2020.csv @@ -103,6 +103,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0 CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0 CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.", +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0 +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0 +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0 CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0 CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.", CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,, diff --git a/outputs/costs_2025.csv b/outputs/costs_2025.csv index bb26c697..c5beb7f6 100644 --- a/outputs/costs_2025.csv +++ b/outputs/costs_2025.csv @@ -103,6 +103,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0 CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0 CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.", +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0 +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0 +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0 CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0 CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.", CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,, diff --git a/outputs/costs_2030.csv b/outputs/costs_2030.csv index aafd3b65..e23f138d 100644 --- a/outputs/costs_2030.csv +++ b/outputs/costs_2030.csv @@ -103,6 +103,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0 CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0 CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.", +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0 +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0 +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0 CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0 CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.", CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,, diff --git a/outputs/costs_2035.csv b/outputs/costs_2035.csv index 6b6cb09d..678a7fb2 100644 --- a/outputs/costs_2035.csv +++ b/outputs/costs_2035.csv @@ -103,6 +103,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0 CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0 CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.", +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0 +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0 +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0 CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0 CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.", CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,, diff --git a/outputs/costs_2040.csv b/outputs/costs_2040.csv index 61c88a65..58f2a387 100644 --- a/outputs/costs_2040.csv +++ b/outputs/costs_2040.csv @@ -103,6 +103,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0 CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0 CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.", +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0 +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0 +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0 CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0 CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.", CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,, diff --git a/outputs/costs_2045.csv b/outputs/costs_2045.csv index 0a04f69e..54167ca6 100644 --- a/outputs/costs_2045.csv +++ b/outputs/costs_2045.csv @@ -103,6 +103,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0 CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0 CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.", +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0 +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0 +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0 CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0 CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.", CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,, diff --git a/outputs/costs_2050.csv b/outputs/costs_2050.csv index f5570cf9..da06f436 100644 --- a/outputs/costs_2050.csv +++ b/outputs/costs_2050.csv @@ -103,6 +103,11 @@ CH4 liquefaction,electricity-input,0.036,MWh_el/MWh_CH4,"Pospíšil et al. (2019 CH4 liquefaction,investment,307.4924,EUR/kW_CH4,"Calculated, based on Lochner and Bothe (2009): https://doi.org/10.1016/j.enpol.2008.12.012 and Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306","based on 265 MUSD-2005/(1 bcm/a), 1 bcm = 10.6 TWh, currency exchange rate: 1.15 USD=1 EUR.",2005.0 CH4 liquefaction,lifetime,25.0,years,"Fasihi et al 2017, table 1, https://www.mdpi.com/2071-1050/9/2/306",,2005.0 CH4 liquefaction,methane-input,1.0,MWh_CH4/MWh_CH4,"Pospíšil et al. (2019): Energy demand of liquefaction and regasification of natural gas and the potential of LNG for operative thermal energy storage (https://doi.org/10.1016/j.rser.2018.09.027), Table 2 and Table 3. alternative source 2: https://encyclopedia.airliquide.com/methane (accessed 2021-02-10).","For refrigeration cycle, cleaning of gas presumed unnecessary as it should be nearly pure CH4 (=SNG). Assuming energy required is only electricity which is for Table 3 in the source provided with efficiencies of ~50% of LHV, making the numbers consistent with the numbers in Table 2.", +CO2 dense phase compression,FOM,5.0,%/year,Table 4-11 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,,2024.0 +CO2 dense phase compression,carbondioxide-input,1.0,t_CO2/t_CO2,,, +CO2 dense phase compression,electricity-input,0.1051,MWh_el/t_CO2,Table 4-10 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf,, +CO2 dense phase compression,investment,34120.2,EUR/t_CO2/h,Table 4-5 + 4-6 operation point 15 AIT Study https://www.ait.ac.at/fileadmin/user_upload/CO2Netz_Bericht_241007.pdf," ""Conversion: 19 Mio. EUR / (5 Mt/yr) = 19*1e6 EUR / (5*1e6 t * (1/8760) h) = 33 288 EUR/t/h""",2024.0 +CO2 dense phase compression,lifetime,25.0,years,"Guesstimate, based on CH4 liquefaction.",,2024.0 CO2 liquefaction,FOM,5.0,%/year,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,2004.0 CO2 liquefaction,carbondioxide-input,1.0,t_CO2/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,"Assuming a pure, humid, low-pressure input stream. Neglecting possible gross-effects of CO2 which might be cycled for the cooling process.", CO2 liquefaction,electricity-input,0.123,MWh_el/t_CO2,Mitsubish Heavy Industries Ltd. and IEA (2004): https://ieaghg.org/docs/General_Docs/Reports/PH4-30%20Ship%20Transport.pdf .,,