Electrochemical Conversion of CO2 to CO into a Microchannel Reactor System in the Case of Aqueous ElectrolyteClick to copy article linkArticle link copied!
- Fanghua ZhangFanghua ZhangState Key Laboratory of Chemical Engineering, School of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, ChinaMore by Fanghua Zhang
- Zhichao JinZhichao JinState Key Laboratory of Chemical Engineering, School of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, ChinaMore by Zhichao Jin
- Chengzhen ChenChengzhen ChenState Key Laboratory of Chemical Engineering, School of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, ChinaMore by Chengzhen Chen
- Yanling TangYanling TangState Key Laboratory of Chemical Engineering, School of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, ChinaMore by Yanling Tang
- Samah A. MahyoubSamah A. MahyoubState Key Laboratory of Chemical Engineering, School of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, ChinaMore by Samah A. Mahyoub
- Shenglin YanShenglin YanState Key Laboratory of Chemical Engineering, School of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, ChinaMore by Shenglin Yan
- Zhenmin Cheng*Zhenmin Cheng*Email: [email protected]State Key Laboratory of Chemical Engineering, School of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, ChinaMore by Zhenmin Cheng
Abstract

A microchannel electrochemical reactor system was designed to facilitate the reduction of CO2 to CO, which is composed of a premixing section in the upstream consisting of a circular microchannel for the presaturation of CO2 in the electrolyte and a reacting section in the downstream consisting of an annular microchannel containing a Ag rod as the catalyst. Such a combined structure exhibited an ultrahigh CO faradaic efficiency of 95.3% due to the efficient mass transfer under Taylor flow. It is interesting to find that CO2 conversion was increased from 0.94 to 3.66% when the length of the microchannel was increased by connection in series due to the prolonged contacting time between CO2 and the electrocatalyst. Furthermore, “scale-up” experiments demonstrated that the faradaic efficiency for CO could keep all above 95.0% at a current density of 7.5 mA cm2 when the microchannel number was increased in parallel, revealing that the microchannel electrochemical reactor is efficient to conduct the electroreduction of CO2.
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