Reducing the crossover of carbonate and liquid products during carbon dioxide electroreduction

被引:55
作者
McCallum, Christopher [1 ]
Gabardo, Christine M. [1 ]
O'Brien, Colin P. [1 ]
Edwards, Jonathan P. [1 ]
Wicks, Joshua [2 ]
Xu, Yi [1 ]
Sargent, Edward H. [2 ]
Sinton, David [1 ]
机构
[1] Univ Toronto, Dept Mech & Ind Engn, Toronto, ON M5S 3G8, Canada
[2] Univ Toronto, Dept Elect & Comp Engn, Toronto, ON M5S 1A4, Canada
基金
加拿大自然科学与工程研究理事会; 加拿大创新基金会;
关键词
ELECTROCHEMICAL REDUCTION; CO2; REDUCTION; GAS-PHASE; ELECTROLYTE; FUEL; CELL; CONVERSION; ALCOHOLS; ETHYLENE; INSIGHTS;
D O I
10.1016/j.xcrp.2021.100522
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Membrane electrode assembly (MEA) electrolyzers can perform stable, high-rate carbon dioxide (CO2) electroreduction for renewable fuels and chemicals, thereby realizing effective carbon utilization to mitigate anthropogenic CO2 emissions. Here, we present a numerical, multiphysics model, computationally intensified 60-fold with a machine learning analysis of computational and experimental data, to address the most urgent systems challenges in CO2 MEA electrolyzers: mitigating carbonate and liquid product crossover to increase CO2 utilization and energy efficiency. We explore the effect of varying the applied potential, CO2 partial pressure, ion-exchange membrane thickness, membrane porosity, and membrane charge on these three metrics. By selectively tuning these physical system parameters, we identify conditions that realize negligible CO2 reactant loss, a 2-fold enhancement in CO2 utilization, and a 2-fold decrease in Nernstian overpotential, corresponding to a multi-carbon, full-cell energy efficiency of 21%. These results may direct future MEA system designs and motivate thin anion-exchange membrane structures.
引用
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页数:17
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