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SPDX-FileCopyrightText: Contributors to technology-data <https://github.com/pypsa/technology-data>
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SPDX-License-Identifier: GPL-3.0-only
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##########################################
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.. The features listed below are not released yet, but will be part of the next release!
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.. To use the features already you have to use the ``master`` branch.
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* Updated Biochar pyrolysis: units updated with rebase on CO2 sequestered, biomass properties aligned with other biomass technolgies, 0.7 coefficient applied to calculate final CO2 sequestration beyond 100 years.
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* Updated Biochar pyrolysis: units updated with rebase on CO2 sequestered, biomass properties aligned with other biomass technolgies, 0.7 coefficient applied to calculate final CO2 sequestration beyond 100 years. (https://github.com/PyPSA/technology-data/pull/258)
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`v0.15.0 <https://github.com/PyPSA/technology-data/releases/tag/v0.15.0>`__ (9th June 2026)
* Renamed ``electricity grid connection`` to ``distribution grid reinforcement`` and updated description for more clarity on the technology and consistency with the source.
* Added VOM for carbon capture retrofits: ``biomass CHP capture`` and ``cement capture`` (https://github.com/PyPSA/technology-data/pull/253).
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* Added technology data for ``CO2 dense phase compression`` step for transport in large pipelines which is different from the current ``CO2 liquefaction`` technology parameters that is taken for ship transport (https://github.com/PyPSA/technology-data/pull/273).
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* Added missing discount rate for OCGT in US-specific data. (https://github.com/PyPSA/technology-data/pull/269)
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* The ``currency_year`` column will now reflect the inflation adjusted currency year instead of the original currency year of the input data. (https://github.com/PyPSA/technology-data/pull/275)
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`v0.14.0 <https://github.com/PyPSA/technology-data/releases/tag/v0.14.0>`__ (13th February 2026)
distribution grid reinforcement,investment,2025,150,EUR/kW,2020,DEA - Technology Data Catalogue for el and DH - v17 - Page 15 - Paragraph 'Cost of grid expansion',"The costs of grid expansion from adding a new electricity generator or a new large consumer - related to strengthening or expansion of the local grid and/or substations (voltage transformation, pumping or compression/expansion)"
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distribution grid reinforcement,lifetime,2025,40,years,2020,same as 'electricity distribution grid',
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distribution grid reinforcement,FOM,2025,2,%/year,2020,same as 'electricity distribution grid',
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methanation,investment,2020,748,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”.",
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methanation,lifetime,2020,20,years,2017,Guesstimate.,"Based on lifetime for methanolisation, Fischer-Tropsch plants."
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methanation,FOM,2020,3,%/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",
@@ -192,6 +195,11 @@ NH3 (l) storage tank incl. liquefaction,lifetime,2020,20,years,2010,"Morgan E. 2
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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."
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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."
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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."
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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"
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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",
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CO2 dense phase compression,lifetime,2024,25,years,2024,"Guesstimate, based on CH4 liquefaction.",
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CO2 dense phase compression,carbondioxide-input,0,1,t_CO2/t_CO2,-,,
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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",
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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."
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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 .,
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CO2 liquefaction,lifetime,2004,25,years,2004,"Guesstimate, based on CH4 liquefaction.",
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