pypsa-eur/doc/configtables/industry.csv

1		Unit	Values	Description
2	St_primary_fraction	--	Dictionary with planning horizons as keys.	The fraction of steel produced via primary route versus secondary route (scrap+EAF). Current fraction is 0.6
3	DRI_fraction	--	Dictionary with planning horizons as keys.	The fraction of the primary route DRI + EAF
4
5	H2_DRI	--	float	The hydrogen consumption in Direct Reduced Iron (DRI) Mwh_H2 LHV/ton_Steel from 51kgH2/tSt in `Vogl et al (2018) <https://doi.org/10.1016/j.jclepro.2018.08.279>`_
6	elec_DRI	MWh/tSt	float	The electricity consumed in Direct Reduced Iron (DRI) shaft. From `HYBRIT brochure <https://ssabwebsitecdn.azureedge.net/-/media/hybrit/files/hybrit_brochure.pdf>`_
7	Al_primary_fraction	--	Dictionary with planning horizons as keys.	The fraction of aluminium produced via the primary route versus scrap. Current fraction is 0.4
8	MWh_NH3_per_tNH3	LHV	float	The energy amount per ton of ammonia.
9	MWh_CH4_per_tNH3_SMR	--	float	The energy amount of methane needed to produce a ton of ammonia using steam methane reforming (SMR). Value derived from 2012's demand from `Center for European Policy Studies (2008) <https://ec.europa.eu/docsroom/documents/4165/attachments/1/translations/en/renditions/pdf>`_
10	MWh_elec_per_tNH3_SMR	--	float	The energy amount of electricity needed to produce a ton of ammonia using steam methane reforming (SMR). same source, assuming 94-6% split methane-elec of total energy demand 11.5 MWh/tNH3
11	Mwh_H2_per_tNH3 _electrolysis	--	float	The energy amount of hydrogen needed to produce a ton of ammonia using Haber–Bosch process. From `Wang et al (2018) <https://doi.org/10.1016/j.joule.2018.04.017>`_, Base value assumed around 0.197 tH2/tHN3 (>3/17 since some H2 lost and used for energy)
12	Mwh_elec_per_tNH3 _electrolysis	--	float	The energy amount of electricity needed to produce a ton of ammonia using Haber–Bosch process. From `Wang et al (2018) <https://doi.org/10.1016/j.joule.2018.04.017>`_, Table 13 (air separation and HB)
13	Mwh_NH3_per_MWh _H2_cracker	--	float	The energy amount of amonia needed to produce an energy amount hydrogen using ammonia cracker
14	NH3_process_emissions	MtCO2/a	float	The emission of ammonia production from steam methane reforming (SMR). From UNFCCC for 2015 for EU28
15	petrochemical_process _emissions	MtCO2/a	float	The emission of petrochemical production. From UNFCCC for 2015 for EU28
16	HVC_primary_fraction	--	float	The fraction of high value chemicals (HVC) produced via primary route
17	HVC_mechanical_recycling _fraction	--	float	The fraction of high value chemicals (HVC) produced using mechanical recycling
18	HVC_chemical_recycling _fraction	--	float	The fraction of high value chemicals (HVC) produced using chemical recycling
19	HVC_environment_sequestration_fraction	--	float	The fraction of high value chemicals (HVC) put into landfill resulting in additional carbon sequestration. The default value is 0.
20	waste_to_energy	--	bool	Switch to enable expansion of waste to energy CHPs for conversion of plastics. Default is false.
21	waste_to_energy_cc	--	bool	Switch to enable expansion of waste to energy CHPs for conversion of plastics with carbon capture. Default is false.
22
23	sector_ratios_fraction_future	--	Dictionary with planning horizons as keys.	The fraction of total progress in fuel and process switching achieved in the industry sector.
24	basic_chemicals_without_NH3_production_today	Mt/a	float	The amount of basic chemicals produced without ammonia (= 86 Mtethylene-equiv - 17 MtNH3).
25	HVC_production_today	MtHVC/a	float	The amount of high value chemicals (HVC) produced. This includes ethylene, propylene and BTX. From `DECHEMA (2017) <https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry-p-20002750.pdf>`_, Figure 16, page 107
26	Mwh_elec_per_tHVC _mechanical_recycling	MWh/tHVC	float	The energy amount of electricity needed to produce a ton of high value chemical (HVC) using mechanical recycling. From SI of `Meys et al (2020) <https://doi.org/10.1016/j.resconrec.2020.105010>`_, Table S5, for HDPE, PP, PS, PET. LDPE would be 0.756.
27	Mwh_elec_per_tHVC _chemical_recycling	MWh/tHVC	float	The energy amount of electricity needed to produce a ton of high value chemical (HVC) using chemical recycling. The default value is based on pyrolysis and electric steam cracking. From `Material Economics (2019) <https://materialeconomics.com/latest-updates/industrial-transformation-2050>`_, page 125
28
29	chlorine_production _today	MtCl/a	float	The amount of chlorine produced. From `DECHEMA (2017) <https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry-p-20002750.pdf>`_, Table 7, page 43
30	MWh_elec_per_tCl	MWh/tCl	float	The energy amount of electricity needed to produce a ton of chlorine. From `DECHEMA (2017) <https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry-p-20002750.pdf>`_, Table 6 page 43
31	MWh_H2_per_tCl	MWhH2/tCl	float	The energy amount of hydrogen needed to produce a ton of chlorine. The value is negative since hydrogen produced in chloralkali process. From `DECHEMA (2017) <https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry-p-20002750.pdf>`_, page 43
32	methanol_production _today	MtMeOH/a	float	The amount of methanol produced. From `DECHEMA (2017) <https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry-p-20002750.pdf>`_, page 62
33	MWh_elec_per_tMeOH	MWh/tMeOH	float	The energy amount of electricity needed to produce a ton of methanol. From `DECHEMA (2017) <https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry-p-20002750.pdf>`_, Table 14, page 65
34	MWh_CH4_per_tMeOH	MWhCH4/tMeOH	float	The energy amount of methane needed to produce a ton of methanol. From `DECHEMA (2017) <https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry-p-20002750.pdf>`_, Table 14, page 65
35	MWh_MeOH_per_tMeOH	LHV	float	The energy amount per ton of methanol. From `DECHEMA (2017) <https://dechema.de/dechema_media/Downloads/Positionspapiere/Technology_study_Low_carbon_energy_and_feedstock_for_the_European_chemical_industry-p-20002750.pdf>`_, page 74.
36	hotmaps_locate_missing	--	{true,false}	Locate industrial sites without valid locations based on city and countries.
37	reference_year	year	YYYY	The year used as the baseline for industrial energy demand and production. Data extracted from `JRC-IDEES 2015 <https://data.jrc.ec.europa.eu/dataset/jrc-10110-10001>`_
38	oil_refining_emissions	tCO2/MWh	float	The emissions from oil fuel processing (e.g. oil in petrochemical refinieries). The default value of 0.013 tCO2/MWh is based on DE statistics for 2019; the EU value is very similar.