电解
电化学
阴极
气体扩散电极
化学工程
选择性
铜
气体扩散
催化作用
膜电极组件
无机化学
材料科学
化学
电极
冶金
物理化学
阳极
电解质
工程类
生物化学
作者
Yi Xu,Jonathan P. Edwards,Shijie Liu,Rui Kai Miao,Jianan Erick Huang,Christine M. Gabardo,Colin P. O’Brien,Jun Li,Edward H. Sargent,David Sinton
出处
期刊:ACS energy letters
[American Chemical Society]
日期:2021-02-02
卷期号:6 (2): 809-815
被引量:397
标识
DOI:10.1021/acsenergylett.0c02401
摘要
The electrochemical conversion of CO 2 produces valuable chemicals and fuels. However, operating at high reaction rates produces locally alkaline conditions that convert reactant CO 2 into cell-damaging carbonate salts. These salts precipitate in the porous cathode structure, block CO 2 transport, reduce reaction efficiency, and render CO 2 electrolysis inherently unstable. We propose a self-cleaning CO 2 reduction strategy with short, periodic reductions in applied voltage, which avoids saturation and prevents carbonate salt formation. We demonstrate this approach in a membrane electrode assembly (MEA) with silver and copper catalysts, on carbon and polytetrafluoroethylene (PTFE)-based gas diffusion electrodes, respectively. When operated continuously, the C 2 selectivity of the copper–PTFE system started to decline rapidly after only ∼10 h. With the self-cleaning strategy, the same electrode operated for 157 h (236 h total duration), maintaining 80% C 2 product selectivity and 138 mA cm –2 of C 2 partial current density, at a cost of <1% additional energy input.
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