PRODUCTION OF SYNTHETIC FUELS BY CO-ELECTROLYSIS OF STEAM AND CARBON DIOXIDE

被引:232
作者
Ebbesen, Sune Dalgaard [1 ]
Graves, Christopher [1 ,2 ,3 ]
Mogensen, Mogens [1 ]
机构
[1] Tech Univ Denmark, Riso Natl Lab Sustainable Energy, Fuel Cells & Solid State Chem Div, DK-4000 Roskilde, Denmark
[2] Columbia Univ, Lenfest Ctr Sustainable Energy, New York, NY USA
[3] Columbia Univ, Dept Earth & Environm Engn, New York, NY USA
关键词
Electrolysis; Steam; Carbon dioxide; Solid oxide cell; Synthesis gas; ANODE-SUPPORTED SOFCS; TEMPERATURE; IMPEDANCE; GAS; PERFORMANCE; DEGRADATION; CONVERSION; REDUCTION; HYDROGEN; CELLS;
D O I
10.1080/15435070903372577
中图分类号
O414.1 [热力学];
学科分类号
摘要
Co-electrolysis of H2O and CO2 was studied in solid oxide cells (SOCs) supported by nickel-/yittria-stabilized zirconia (Ni/YSZ) electrode. Polarization characterization indicates that electrochemical reduction of both CO2 and H2O occurs during co-electrolysis. In parallel with the electrochemical reactions, the equilibrium of the water-gas shift reaction is reached, and moreover, CO is produced via the water-gas shift reaction. The degradation observed when performing co-electrolysis in these SOCs occurs mainly at the Ni/YSZ cathode and may be a consequence of impurities in the gas stream, adsorbing on active sites in the SOC. The low degradation is most likely acceptable for long-time operation.
引用
收藏
页码:646 / 660
页数:15
相关论文
共 32 条
[31]   Isotopic and kinetic assessment of the mechanism of reactions of CH4 with CO2 or H2O to form synthesis gas and carbon on nickel catalysts [J].
Wei, JM ;
Iglesia, E .
JOURNAL OF CATALYSIS, 2004, 224 (02) :370-383
[32]  
Wendt H., 1990, ELECTROCHEMICAL HYDR, V2nd