Electrochemical reduction of CO2 in solid oxide electrolysis cells

被引:150
|
作者
Zhan, Zhongliang [1 ]
Zhao, Lin [1 ]
机构
[1] Chinese Acad Sci, Shanghai Inst Ceram, CAS Key Lab Mat Energy Convers, Shanghai 200050, Peoples R China
关键词
Solid oxide electrolysis cells; Solid oxide fuel cells; Electrochemical reduction; Carbon dioxide; CARBON-DIOXIDE ELECTROLYSIS; FUEL-CELLS; ELECTRODE/ELECTROLYTE INTERFACE; INTERMEDIATE TEMPERATURE; HYDROGEN-PRODUCTION; PARTIAL OXIDATION; PERFORMANCE; METHANE; SYNGAS;
D O I
10.1016/j.jpowsour.2010.05.037
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
This paper describes results on the electrochemical reduction of carbon dioxide using the same device as the typical planar nickel-YSZ cermet electrode supported solid oxide fuel cells (H-2-CO2, Ni-YSZ vertical bar YSZ vertical bar LSCF-GDC, LSCF. air). Operation in both the fuel cell and the electrolysis mode indicates that the electrodes could work reversibly for the charge transfer processes. An electrolysis current density of approximate to 1 A cm(-2) is observed at 800 degrees C and 1.3V for an inlet mixtures of 25% H-2-75% CO2. Mass spectra measurement suggests that the nickel-YSZ cermet electrode is highly effective for reduction of CO2 to CO. Analysis of the gas transport in the porous electrode and the adsorption/desorption process over the nickel surface indicates that the cathodic reactions are probably dominated by the reduction of steam to hydrogen, whereas carbon monoxide is mainly produced via the reverse water gas shift reaction. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:7250 / 7254
页数:5
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