Production of syngas plus oxygen from CO2 in a gas-diffusion electrode-based electrolytic cell

被引:73
作者
Yamamoto, T
Tryk, DA
Fujishima, A [1 ]
Ohata, H
机构
[1] Univ Tokyo, Sch Engn, Dept Appl Chem, Bunkyo Ku, Tokyo 1138656, Japan
[2] Elect Power Dev Co Ltd, Chuo Ku, Tokyo 1048165, Japan
关键词
CO2; reduction; full cell; gas diffusion electrode;
D O I
10.1016/S0013-4686(02)00253-0
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
Most of the research published in electrochemical CO2 reduction has been reported for half-cells, with little consideration of the overall system. However, it is necessary to consider the eventual involvement of full cells. We conducted CO2 reduction and water oxidation in a CO2-reducing full cell with larger geometric surface area (2 x 2 cm 2) and with a relatively small inter-electrode gap (1-2 mm) in order to minimize ohmic losses. The result was an ca. 1:1 CO/H-2 (v/v) gas ratio at a current density of 10 mA cm(-2) and a cell voltage of 3.05 V, producing O-2 at the counter electrode. Based on an enthalpic voltage of 1.36 V, this constitutes an overall energy efficiency of 44.6%. (C) 2002 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:3327 / 3334
页数:8
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