High-efficiency intermediate temperature solid oxide electrolyzer cells for the conversion of carbon dioxide to fuels
High-efficiency intermediate temperature solid oxide electrolyzer cells for the conversion of carbon dioxide to fuels
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DOI:
10.1016/j.jpowsour.2013.11.047
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发表时间:
2014-04
影响因子:
9.2
通讯作者:
Jingbo Yan;Jingbo Yan;Hao Chen;Emir Dogdibegovic;J. Stevenson;Mojie Cheng;Xiao-Dong Zhou
中科院分区:
文献类型:
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作者:
Jingbo Yan;Jingbo Yan;Hao Chen;Emir Dogdibegovic;J. Stevenson;Mojie Cheng;Xiao-Dong Zhou
Electrochemical reduction of carbon dioxide in the intermediate temperature region was investigated by utilizing a reversible solid oxide electrolysis cell (SOEC). The current–potential (i–V) curve exhibited a nonlinear characteristic at low current density. Differentiation ofi–Vcurves revealed that the cell area specific resistance (ASR) was current-dependent and had its maximum in electrolysis mode and minimum in fuel cell mode. Impedance measurements were performed under different current densities and gas compositions, and the results were analyzed by calculating the distribution of relaxation times. The ASR variation resulted from the difference in electrochemical reactions occurring on the Ni–YSZ electrode,i.e., Ni–YSZ is a better electrode for CO oxidation than for CO2reduction. Coke formation on Ni–YSZ played a crucial role in affecting its electrolysis performance in the intermediate temperature region. The ASR apex was associated with a decrease in cell temperature during electrolysis due to the endothermic nature of CO2reduction reaction. It was postulated that such a decrease in temperature and rise in CO concentration led to coke formation. As a consequence, higher temperature (>700 °C), higher CO2concentration (>50%), and the presence of hydrogen or steam are recommended for efficient CO2reduction in solid oxide electrochemical cells.