平板式重整器构型中微通道乙醇重整的优化

S. Roychowdhury, P. Vivekanand, Sarit K. Das, T. Sundararajan
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引用次数: 2

摘要

为了解乙醇转化为燃料电池用氢的流体力学、传热和动力学,研究了乙醇在板式重整器微通道中的蒸汽重整过程。考虑了燃烧烟气和蒸汽-乙醇混合物交替通道之间的热交换,包括共流或逆流配置。燃烧反应在接近入口时完成。这导致了更高的转化率为共流配置,由于更高的传热率在入口。结果表明,末端效应仅在最外层的通道中才会出现,因此对称的重整器通道分析足以预测多通道重整器系统的性能。在轴向上,气流场、温度场和浓度场在离进口较近的地方达到充分发育的廓形。在较大的轴向距离上,由于气体密度的变化,速度剖面发生了轻微的变化。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Optimization of Ethanol Reforming with micro-channels in Plate type reformer configuration
The study of steam reforming of ethanol in micro-channels in a plate-type reformer has been carried out to understand the fluid mechanics, heat transfer and kinetics of ethanol conversion to hydrogen for fuel-cell applications. Heat exchange between alternate channels of combustion flue gas and steam-ethanol mixture has been considered, involving co-flow or counter-flow configurations. Combustion reactions are observed to be completed close to the entry. This results in higher rates of conversion for the co-flow configuration, owing to higher heat transfer rates at the entry. It is shown that end effects are felt only in the outer-most channels and hence a symmetric reformer channel analysis is adequate to predict the performance of a multi-channel reformer system. In the axial direction, the flow, temperature and concentration fields attain fully developed profile form at a short distance from the inlet. At larger axial distances, the velocity profile undergoes mild variations due to changes in the gas d...
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