Feasibility study and techno-economic assessment of power-to-gas (P2G) technology based on solid oxide electrolysis (SOE)

被引:2
|
作者
Martsinchyk, Katsiaryna [3 ]
Martsinchyk, Aliaksandr [3 ]
Lazor, Monika [1 ,2 ,4 ,6 ]
Shuhayeu, Pavel [3 ]
Kupecki, Jakub [1 ,2 ,5 ]
Niemczyk, Anna [1 ,2 ]
Blesznowski, Marcin [1 ,2 ]
Milewskic, Jaroslaw [3 ]
机构
[1] Natl Res Inst, Inst Power Engn, Mory 8, PL-01330 Warsaw, Poland
[2] Natl Res Inst, Inst Power Engn, Ctr Hydrogen Technol CTH 2, Augustowka 36, PL-02981 Warsaw, Poland
[3] Warsaw Univ Technol, Inst Heat Engn, Nowowiejska 21-25, PL-00665 Warsaw, Poland
[4] Warsaw Univ Technol, Fac Chem, Noakowskiego 3, PL-00664 Warsaw, Poland
[5] Univ Calif Irvine, Natl Fuel Cell Res Ctr NFCRC, Engn Lab Facil, Irvine, CA 92697 USA
[6] Augustowka 36, PL-02981 Warsaw, Poland
关键词
Power-to-gas; Techno-economic assessment; solid oxide electrolysis; hydrogen; Syngas; Feasibility study; CARBON-DIOXIDE SEPARATION; FUEL-CELL; CO2; METHANATION; ENERGY; CAPTURE; OPTIMIZATION; ABSORPTION; STORAGE; COST;
D O I
10.1016/j.jenvman.2024.120425
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Power-to-Gas (P2G) is considered as a promising energy storage technology in a long-time horizon. The rapid growth in the share of intermittent renewables in the energy mix is driving forward research and development in large-scale energy storage. This paper presents a feasibility analysis of a power-to-gas system in terms of various operating points and capacities. The analysis was performed using a system model, which features a solid oxide electrolyzer (SOE), a CO2 separation unit, and a methanation reactor as the key components. For the purposes of the techno-economic assessment (TEA) of the system, the CAPEX/OPEX estimation was performed and the cost structure defined. The model proposed in the study enables system-level optimization, including technical and economic criteria, considering two nominal scales: 10 kW and 40 GW, which corresponds to the nominal capacity of SOE in each case. According to the study, in an SOE-based P2G system, the cost of synthetic natural gas (SNG) production will fall by 15-21% by 2030 and 29-37% by 2050. SNG production would cost 3.15-3.75 EUR2023/kg(SNG) in 2030 and 2.6-3.0 EUR2023/kg(SNG) in 2050 for systems with SOE power >10 MW. Generally, product cost reductions occur as a result of material development and large-scale production, which influences the system's CAPEX. According to the research, the technology will break even by 2050. The large-scale power-to-gas system with a total of 40 GW installed capacity delivers a product price of 2.4 EUR2023/kg(SNG) with the average conversion efficiency of 68%.
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页数:14
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