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多孔介质内反应气的化学和热质非同性传递过程特性

HEAT AND MASS TRANSFER OF CHEMICAL REACTING GAS IN POROUS MEDIA
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摘要 针对集成扳式固体氧化物燃料电池,建立了数学物理模型,分析阳极侧多孔支撑层内富氢气体的内重整反应传递过程特性。讨论了操作温度、入口处H_2O:CH_4比值以及多孔材料的孔隙率对甲烷蒸汽重整转换率和氢气的生成量的影响,得到了在电池的一定运行工况范围内比较有利的反应条件。 The physico-mathematical model was established to analysis the transport phenomena during the methane steam reforming in the porous anode aside of the integrated planar solid oxide fuel cell (IP-SOFC). The kinetics study was conducted with numerical simulation to explore the influences of corresponding factors on the progress of reforming reaction and the distributing of the production, H2, includes that of operating temperature, ratio of H20 and CH4, and porosity of the supporting material. The operating and configuration conditions which benefit to the reforming reaction were also discussed.
出处 《工程热物理学报》 EI CAS CSCD 北大核心 2007年第5期838-840,共3页 Journal of Engineering Thermophysics
基金 国家自然科学基金(No.50576023) 教育部新世纪优秀人才支持计划资助项目(NCET-05-0216)
关键词 固体氧化物燃料电池 甲烷重整反应 多孔介质 solid oxide fuel cell methane steam reforming porous media
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参考文献7

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