Design of an electrochemical cell making syngas (CO+H2) from CO2 and H2O reduction at room temperature

被引:362
|
作者
Delacourt, Charles [1 ]
Ridgway, Paul L. [1 ]
Kerr, John B. [1 ]
Newman, John [1 ]
机构
[1] Lawrence Berkeley Natl Lab, Environm Energy Technol Div, Berkeley, CA 94720 USA
关键词
D O I
10.1149/1.2801871
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
An electrolysis-cell design for simultaneous electrochemical reduction of CO2 and H2O to make syngas (CO + H-2) at room temperature (25 degrees C) was developed, based on a technology very close to that of proton-exchange-membrane fuel cells (PEMFC), i.e., based on the use of gas-diffusion electrodes so as to achieve high current densities. While a configuration involving a proton-exchange membrane (Nafion) as electrolyte was shown to be unfavorable for CO2 reduction, a modified configuration based on the insertion of a pH-buffer layer (aqueous KHCO3) between the silver-based cathode catalyst layer and the Nafion membrane allows for a great enhancement of the cathode selectivity for CO2 reduction to CO [ca. 30 mA/cm(2) at a potential of -1.7 to -1.75 V vs SCE (saturated-calomel reference electrode)]. A CO/H-2 ratio of 1/2, suitable for methanol synthesis, is obtained at a potential of ca. -2 V vs SCE and a total current density of ca. 80 mA/cm(2). An issue that has been identified is the change in product selectivity upon long-term electrolysis. Results obtained with two other cell designs are also presented and compared. (c) 2007 The Electrochemical Society.
引用
收藏
页码:B42 / B49
页数:8
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