-
Notifications
You must be signed in to change notification settings - Fork 52
DEA cost for Fischer-Tropsch, methanolisation #238
New issue
Have a question about this project? Sign up for a free GitHub account to open an issue and contact its maintainers and the community.
By clicking “Sign up for GitHub”, you agree to our terms of service and privacy statement. We’ll occasionally send you account related emails.
Already on GitHub? Sign in to your account
Open
millingermarkus
wants to merge
15
commits into
PyPSA:master
Choose a base branch
from
millingermarkus:revert_DEA_cost
base: master
Could not load branches
Branch not found: {{ refName }}
Loading
Could not load tags
Nothing to show
Loading
Are you sure you want to change the base?
Some commits from the old base branch may be removed from the timeline,
and old review comments may become outdated.
Open
Changes from 12 commits
Commits
Show all changes
15 commits
Select commit
Hold shift + click to select a range
0b1271b
Add in Fischer-Tropsch efficiency from DEA
5a69ce7
Remove Agora data from manual input (methanation, methanolisation, Fi…
c2da6d8
Cost update methanolisation, Fischer-Tropsch, methanation
ef28139
Remove lock file
4b80932
Added release note
a67b6f1
Correct Fischer-Tropsch Fixed cost
millingermarkus 5b2c182
Change unit for methanolisation to /kW_MeOH
millingermarkus f66ed97
Cleanup methanolisation data from DEA
millingermarkus 17f04e1
Methanolisation data from DEA
millingermarkus b7d918e
Add back methanation assumptions from Agora
millingermarkus 86dde7b
Merge branch 'master' into revert_DEA_cost
millingermarkus a384363
[pre-commit.ci] auto fixes from pre-commit.com hooks
pre-commit-ci[bot] ea4e844
remove redundant columns
millingermarkus 2162820
Minor cleanup
millingermarkus 8be62de
Remove old ebiofuel investment and VOM
millingermarkus File filter
Filter by extension
Conversations
Failed to load comments.
Loading
Jump to
Jump to file
Failed to load files.
Loading
Diff view
Diff view
There are no files selected for viewing
This file contains hidden or bidirectional Unicode text that may be interpreted or compiled differently than what appears below. To review, open the file in an editor that reveals hidden Unicode characters.
Learn more about bidirectional Unicode characters
Large diffs are not rendered by default.
Oops, something went wrong.
millingermarkus marked this conversation as resolved.
Outdated
Show resolved
Hide resolved
|
This file contains hidden or bidirectional Unicode text that may be interpreted or compiled differently than what appears below. To review, open the file in an editor that reveals hidden Unicode characters.
Learn more about bidirectional Unicode characters
| Original file line number | Diff line number | Diff line change |
|---|---|---|
| @@ -0,0 +1 @@ | ||
| ,markus,markus-Virtual-Machine,09.10.2025 14:54,file:///home/markus/.config/libreoffice/4; |
This file contains hidden or bidirectional Unicode text that may be interpreted or compiled differently than what appears below. To review, open the file in an editor that reveals hidden Unicode characters.
Learn more about bidirectional Unicode characters
| Original file line number | Diff line number | Diff line change |
|---|---|---|
|
|
@@ -3925,7 +3925,7 @@ electrobiofuels,VOM,4.957,EUR/MWh_th,combination of BtL and electrofuels,,2022.0 | |
| electrobiofuels,capture rate,0.9,per unit,Assumption based on doi:10.1016/j.biombioe.2015.01.006,,,, | ||
| electrobiofuels,efficiency-biomass,1.3183,per unit,Stoichiometric calculation,,,, | ||
| electrobiofuels,efficiency-hydrogen,1.0309,per unit,Stoichiometric calculation,,,, | ||
| electrobiofuels,efficiency-tot,0.6217,per unit,Stoichiometric calculation,,,, | ||
| electrobiofuels,efficiency-tot,0.5545,per unit,Stoichiometric calculation,,,, | ||
euronion marked this conversation as resolved.
Show resolved
Hide resolved
|
||
| electrobiofuels,investment,1155460.1124,EUR/kW_th,combination of BtL and electrofuels,,2022.0,, | ||
| electrolysis,FOM,4.0,%/year,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",86 AEC 100 MW: Fixed O&M ,2020.0,, | ||
| electrolysis,efficiency,0.5773,per unit,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",86 AEC 100 MW: Hydrogen Output,2020.0,, | ||
|
|
@@ -4079,12 +4079,12 @@ lignite,efficiency,0.33,p.u.,"Lazard's levelized cost of energy analysis - versi | |
| lignite,fuel,3.2985,EUR/MWh_th,"DIW (2013): Current and propsective costs of electricity generation until 2050, http://hdl.handle.net/10419/80348 , pg. 80 text below figure 10, accessed: 2023-12-14.","Based on IEA 2011 data, 10 USD/t.",2010.0,, | ||
| lignite,investment,3827.1629,EUR/kW_e,"Lazard's levelized cost of energy analysis - version 16.0 (2023): https://www.lazard.com/media/typdgxmm/lazards-lcoeplus-april-2023.pdf , pg. 49 (Levelized Cost of Energy - Key Assumptions), accessed: 2023-12-14.","Higher costs include coal plants with CCS, but since using here for calculating the average nevertheless. Calculated based on average of listed range, i.e. (3200+6775) USD/kW_e/2 / (1.09 USD/EUR). Note: Assume same costs as for hard coal, as cost structure is apparently comparable, see https://diglib.tugraz.at/download.php?id=6093e88b63f93&location=browse and https://iea.blob.core.windows.net/assets/ae17da3d-e8a5-4163-a3ec-2e6fb0b5677d/Projected-Costs-of-Generating-Electricity-2020.pdf .",2023.0,, | ||
| lignite,lifetime,40.0,years,"Lazard's levelized cost of energy analysis - version 16.0 (2023): https://www.lazard.com/media/typdgxmm/lazards-lcoeplus-april-2023.pdf , pg. 49 (Levelized Cost of Energy - Key Assumptions), accessed: 2023-12-14.","Note: Assume same costs as for hard coal, as cost structure is apparently comparable, see https://diglib.tugraz.at/download.php?id=6093e88b63f93&location=browse and https://iea.blob.core.windows.net/assets/ae17da3d-e8a5-4163-a3ec-2e6fb0b5677d/Projected-Costs-of-Generating-Electricity-2020.pdf . ",2023.0,, | ||
| 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,FOM,3.0,%/year,Schaber thesis, from old pypsa cost assumptions,2015.0,, | ||
euronion marked this conversation as resolved.
Outdated
Show resolved
Hide resolved
|
||
| 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,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,, | ||
| methanation,investment,1058.2216,EUR/kWH2,Schaber thesis, from old pypsa cost assumptions,2015.0,, | ||
| methanation,lifetime,25.0,years,Schaber thesis, from old pypsa cost assumptions,2015.0,, | ||
euronion marked this conversation as resolved.
Outdated
Show resolved
Hide resolved
|
||
| methane storage tank incl. compressor,FOM,1.9,%/year,"Guesstimate, based on hydrogen storage tank type 1 including compressor by DEA.",Based on assumptions for hydrogen storage tank type 1 including compressor (by DEA).,2014.0,, | ||
| methane storage tank incl. compressor,investment,8961.5075,EUR/m^3,Storage costs per l: https://www.compositesworld.com/articles/pressure-vessels-for-alternative-fuels-2014-2023 (2021-02-10).,"Assume 5USD/l (= 4.23 EUR/l at 1.17 USD/EUR exchange rate) for type 1 pressure vessel for 200 bar storage and 100% surplus costs for including compressor costs with storage, based on similar assumptions by DEA for compressed hydrogen storage tanks.",2014.0,, | ||
| methane storage tank incl. compressor,lifetime,30.0,years,"Guesstimate, based on hydrogen storage tank type 1 including compressor by DEA.",Based on assumptions for hydrogen storage tank 1 including compressor (by DEA).,2014.0,, | ||
|
|
@@ -4102,14 +4102,14 @@ methanol-to-olefins/aromatics,electricity-input,1.3889,MWh_el/t_HVC,"DECHEMA 201 | |
| methanol-to-olefins/aromatics,investment,2781006.4359,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).,2015.0,, | ||
| 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.",,2017.0,, | ||
|
Collaborator
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. FOM is missing for methanolisation in your new dataset
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. added |
||
| methanolisation,FOM,2.9032,%/year,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",98 Methanol from hydrogen: Fixed O&M,2020.0,, | ||
| 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,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,,, | ||
fneum marked this conversation as resolved.
Outdated
Show resolved
Hide resolved
|
||
| methanolisation,investment,819108.478,EUR/MW_MeOH,"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 8: “Reference scenario”.","Well developed technology, no significant learning expected.",2017.0,, | ||
| methanolisation,lifetime,20.0,years,"Danish Energy Agency, Technology Data for Renewable Fuels (04/2022), Data sheet “Methanol to Power”.",,2017.0,, | ||
| methanolisation,investment,1345.9296,EUR/kW_MeOH,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",98 Methanol from hydrogen: Specific investment,2020.0,, | ||
| methanolisation,lifetime,30.0,years,"Danish Energy Agency, inputs/data_sheets_for_renewable_fuels.xlsx",98 Methanol from hydrogen: Technical lifetime,2020.0,, | ||
| micro CHP,FOM,6.6667,%/year,"Danish Energy Agency, inputs/technologydatafor_heating_installations_marts_2018.xlsx",219 LT-PEMFC mCHP - natural gas: Fixed O&M,2015.0,, | ||
| micro CHP,efficiency,0.351,per unit,"Danish Energy Agency, inputs/technologydatafor_heating_installations_marts_2018.xlsx","219 LT-PEMFC mCHP - natural gas: Electric efficiency, annual average, net",2015.0,, | ||
| micro CHP,efficiency-heat,0.599,per unit,"Danish Energy Agency, inputs/technologydatafor_heating_installations_marts_2018.xlsx","219 LT-PEMFC mCHP - natural gas: Heat efficiency, annual average, net",2015.0,, | ||
|
|
||
This file contains hidden or bidirectional Unicode text that may be interpreted or compiled differently than what appears below. To review, open the file in an editor that reveals hidden Unicode characters.
Learn more about bidirectional Unicode characters
Oops, something went wrong.
Oops, something went wrong.
Add this suggestion to a batch that can be applied as a single commit.
This suggestion is invalid because no changes were made to the code.
Suggestions cannot be applied while the pull request is closed.
Suggestions cannot be applied while viewing a subset of changes.
Only one suggestion per line can be applied in a batch.
Add this suggestion to a batch that can be applied as a single commit.
Applying suggestions on deleted lines is not supported.
You must change the existing code in this line in order to create a valid suggestion.
Outdated suggestions cannot be applied.
This suggestion has been applied or marked resolved.
Suggestions cannot be applied from pending reviews.
Suggestions cannot be applied on multi-line comments.
Suggestions cannot be applied while the pull request is queued to merge.
Suggestion cannot be applied right now. Please check back later.
Uh oh!
There was an error while loading. Please reload this page.