Energy analysis of a power-to-jet-fuel plant

被引:3
|
作者
Boilley, J. H. [1 ,2 ]
Berrady, A. [2 ]
Bin Shahrel, H. [2 ]
Gurbuz, E. [2 ]
Gallucci, F. [1 ]
机构
[1] Eindhoven Univ Technol, Sustainable Proc Engn Chem Engn & Chem, Eindhoven, Netherlands
[2] ENGIE LAB CRIGEN, Hydrogen Lab, 4 Rue Josephine Baker, F-93240 Stains, France
关键词
Power-to-fuels; Hydrogen; Energy analysis; Synthetic fuels; Carbon capture and utilisation; Fischer-tropsch; SOEC; SOLID OXIDE ELECTROLYZER; FISCHER-TROPSCH; TECHNOECONOMIC ANALYSIS; LIQUID FUELS; GAS HOLDUP; SCALE-UP; HYDROCRACKING; STACK; PERFORMANCE; REACTOR;
D O I
10.1016/j.ijhydene.2024.01.262
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Sustainable aviation fuel (SAF) production from captured carbon dioxide and green hydrogen, is referred to as the key to decarbonize the hard-to-abate aviation sector. Fischer-Tropsch is a mature and reliable pathway for hydrocarbon synthesis, with a wide spectrum of technological options and high plant efficiency extending to more than 80 % of e-kerosene selectivity. In this work, an Aspen Hysys model, coupled with different Matlab simulations for Fischer-Tropsch, Hydrocracker and SOEC, was set up to estimate efficiency and selectivity. The results show that global efficiency is mainly linked to the efficiency of the production of H2. Energetic efficiency reaches 48.06 % using the already existing commercial electrolyte supported cell in a SOEC electrolyser, but it could increase to 65.74 % if cathode supported cell was considered.
引用
收藏
页码:1160 / 1176
页数:17
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