Bipolar membrane electrolyzers enable high single-pass CO2 electroreduction to multicarbon products

被引:129
|
作者
Xie, Ke [1 ]
Miao, Rui Kai [2 ]
Ozden, Adnan [2 ]
Liu, Shijie [2 ]
Chen, Zhu [1 ]
Dinh, Cao-Thang [3 ]
Huang, Jianan Erick [1 ]
Xu, Qiucheng [4 ]
Gabardo, Christine M. [2 ]
Lee, Geonhui [1 ]
Edwards, Jonathan P. [2 ]
O'Brien, Colin P. [2 ]
Boettcher, Shannon W. [4 ]
Sinton, David [2 ]
Sargent, Edward H. [1 ]
机构
[1] Univ Toronto, Dept Elect & Comp Engn, 10 Kings Coll Rd, Toronto, ON M5S 3G4, Canada
[2] Univ Toronto, Dept Mech & Ind Engn, 5 Kings Coll Rd, Toronto, ON M5S 3G8, Canada
[3] Queens Univ, Dept Chem Engn, 19 Div St, Kingston, ON K7L 3N6, Canada
[4] Univ Oregon, Dept Chem & Biochem, Eugene, OR 97403 USA
基金
加拿大自然科学与工程研究理事会;
关键词
ELECTROCHEMICAL REDUCTION; CARBON BALANCE; COEFFICIENTS; TRANSPORT; INSIGHTS; CATALYST; ETHYLENE;
D O I
10.1038/s41467-022-31295-3
中图分类号
O [数理科学和化学]; P [天文学、地球科学]; Q [生物科学]; N [自然科学总论];
学科分类号
07 ; 0710 ; 09 ;
摘要
In alkaline and neutral MEA CO2 electrolyzers, CO2 rapidly converts to (bi)carbonate, imposing a significant energy penalty arising from separating CO2 from the anode gas outlets. Here we report a CO2 electrolyzer uses a bipolar membrane (BPM) to convert (bi)carbonate back to CO2, preventing crossover; and that surpasses the single-pass utilization (SPU) limit (25% for multi-carbon products, C2+) suffered by previous neutral-media electrolyzers. We employ a stationary unbuffered catholyte layer between BPM and cathode to promote C2+ products while ensuring that (bi)carbonate is converted back, in situ, to CO2 near the cathode. We develop a model that enables the design of the catholyte layer, finding that limiting the diffusion path length of reverted CO2 to similar to 10 mu m balances the CO2 diffusion flux with the regeneration rate. We report a single-pass CO2 utilization of 78%, which lowers the energy associated with downstream separation of CO2 by 10x compared with past systems.
引用
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页数:12
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