Life cycle analysis of a combined CO2 capture and conversion membrane reactor

被引:20
作者
Fang, Jie [1 ]
Jin, Xinfang [1 ]
Huang, Kevin [1 ]
机构
[1] Univ South Carolina, Dept Mech Engn, Columbia, SC 29201 USA
基金
美国国家科学基金会;
关键词
Membrane; Reactor; CO2; capture; Electrolysis; Synthetic fuel; HYDROGEN-PRODUCTION; CARBON CAPTURE; FLUE-GAS; WATER; DIOXIDE; PERFORMANCE; INTEGRATION; TECHNOLOGY; ABSORPTION; SEPARATION;
D O I
10.1016/j.memsci.2017.12.006
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper reports a life cycle analysis of a combined CO2 capture and conversion "all-in-one" membrane reactor system. The reactor is composed of a high-temperature mixed electronic and carbonate-ion conductor (MECC) membrane for CO2 capture and a solid oxide electrolysis cell (SOEC) for CO2/H2O co-reduction. The results show that the parasitic energy (PE) using MECC membrane to capture CO2 is 321 kJ for every kilogram CO2 captured, less than half of the consumption of the stat-of the-art MEA plant. The energy efficiency of the combined system can reach 82%. A cost analysis further shows that the cost of electricity dictates the price of synthetic fuel produced by the reactor at a lower SOEC area (lower capital cost), while both electricity cost and SOEC capital cost play an important role for higher SOEC area (higher capital cost). Finally, the synthetic fuel produced from Ag-based MECC and NiO-based MECC capture/conversion systems are comparable to that of biomass derived liquids (carbon neutral) when the electricity cost is < $0.059/kWh and < $0.096/ kWh, respectively.
引用
收藏
页码:142 / 150
页数:9
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