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Enabling direct CO2 electrolysis by alkali metal cation substituted membranes in a gas diffusion electrode reactor
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Enabling direct CO2 electrolysis by alkali metal cation substituted membranes in a gas diffusion electrode reactor

Wei-Chieh Liao, Ding-Huei Tsai, Wei-Ze Hong, Yi-Hong Huang, Liang-Chen LinYung-Tin Pan
Chemical Engineering Journal, 卷.434, 134765
04/2022

摘要

Cation exchange membrane Cesium CO2RR Copper Membrane electrode assembly Zero-gap Chemistry (all) Environmental Chemistry Chemical Engineering (all) Industrial and Manufacturing Engineering
Direct gas phase electrolysis using a membrane electrode assembly (MEA) reactor has been recognized as a promising direction for large scale continuous CO 2 conversion. The so called “zero-gap” CO 2 reduction was however seldom achieved when proton is the main charge carrier in the system due to the overwhelmed competing hydrogen evolution reaction (HER) taking place at the cathode. In this work, the suppression of HER is achieved by regulating the rate of proton transport through the membrane electrolytes and is realized by the modification of the sulfonic acid side chains with alkali metal cations. The MEA's CO 2 reduction reaction (CO 2 RR) faradaic efficiency (CO 2 RR-FE) is significantly improved as the alkali cations are varied sequentially from Li to Cs. Such improvement is attributed to the significantly hindered proton transport in the Cs-MEA, as reflected by the substantially larger high frequency resistance (HFR), which leads to enhanced competitive adsorption of CO 2 on the copper catalyst. In addition, the Cs-MEA showed the highest robustness for both the membrane cations and the copper cathode against leaching and corrosion. Moreover, the observed phase transition of copper metal into faceted cuprous oxide crystals exposing low index surfaces also favors CO 2 RR over HER. The collective desirable properties of the Cs-MEA result in the best CO 2 RR performance, exhibiting a maximum CO 2 RR-FE of 0.44% at −1.2 V vs RHE and a space time yield (STY) of 1.06 mmol·h −1 ·g cat -1 for methane (CH 4 ) and 2.02 mmol·h −1 ·g cat -1 for carbon monoxide (CO).

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