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Catalytic modification of conventional SOFC anodes with a view to reducing their activity for direct internal reforming of natural gas
Affiliation:1. Politecnico di Milano, Department of Energy, Via Lambruschini 4, 20156, Milano, Italy;2. ETHZ – Institute of Process Engineering, Sonneggstrasse 3, 8092, Zurich, Switzerland;1. Union Research Center of Fuel Cell, School of Chemical and Environmental Engineering, China University of Mining and Technology, Beijing 100083, PR China;2. State Key Laboratory of Power Systems, Department of Thermal Engineering, Tsinghua University, Beijing 100084, PR China;3. Tsinghua Innovation Center in Dongguan, Dongguan, 523808, PR China;1. Marine Engineering College, Dalian Maritime University, Dalian, Liaoning 116026, China;2. Marine Engineering College, Jimei University, Xiamen, Fujian 361021, China;3. Ningbo Institute of Material Technology and Engineering (NIMTE), Chinese Academy of Science, Ningbo 315201, China;4. Department of Energy Sciences, Lund University, Box 118, 22100 Lund, Sweden;5. Transportation Equipment and Ocean Engineering College, Dalian Maritime University, Dalian, Liaoning 116026, China
Abstract:When using natural gas as fuel for the solid oxide fuel cell (SOFC), direct internal reforming lowers the requirement for cell cooling and, theoretically, offers advantages with respect to capital cost and efficiency. The high metal content of a nickel/zirconia anode and the high temperature, however, cause the endothermic reforming reaction to take place very fast. The resulting drop of temperature at the inlet produces thermal stresses, which may lower the system efficiency and limit the stack lifetime. To reduce the reforming rate without lowering the electrochemical activity of the cell, a wet impregnation procedure for modifying conventional cermets by coverage with a less active metal was developed. As the coating material copper was chosen. Copper is affordable, catalytically inert for the reforming reaction and exhibits excellent electronic conductivity. The current density–voltage characteristics of the modified units showed that it is possible to maintain a good electrochemical performance of the cells despite the catalytic modification. A copper to nickel ratio of 1:3 resulted in a strong diminution of the catalytic reaction rate. This indicates that the modification could be a promising method to improve the performance of solid oxide fuel cells with direct internal reforming of hydrocarbons.
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