首页> 外文会议>4th International Conference on Fuel Cell Science, Engineering, and Technology 2006 pt.B >SIMULATION OF WATER VAPOR TRANSPORT PHENOMENA IN PROTON EXCHANGE MEMBRANE FUEL CELLS (PEMFCs)
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SIMULATION OF WATER VAPOR TRANSPORT PHENOMENA IN PROTON EXCHANGE MEMBRANE FUEL CELLS (PEMFCs)

机译:质子交换膜燃料电池(PEMFCs)中水汽传输现象的模拟。

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摘要

The objective of this paper is to study the influences of water vapor concentration in membrane and flow channels under the different operation conditions. The studied flow channels by CFDRC code include serpentine and interdigitated flow channels which have different gas transportation mechanisms. At the same time, the computer code, based upon Okada's one dimensional model, was built to predict the influences of the electro-osmosis effect, the foreign impurity cations and the water balance time on water concentration in the membrane by Fortran 90. Both of interdigitated and serpentine flow fields show that water vapor accumulates near the cathode outlet of the membrane. And, the serpentine flow field accumulates more water vapor than interdigitated flow field does. As the inlet water mass fraction below 10%, the drying out problem may happen to reduce current density. In addition, the foreign impurity cations may induce the stronger electro-osmosis effect and reduce the effect of water back diffusion; hence, cause the accumulating of water in the cathode. It needs more water balance time and decreases the membrane performance.
机译:本文的目的是研究在不同操作条件下膜和流道中水蒸气浓度的影响。通过CFDRC代码研究的流道包括具有不同气体传输机制的蛇形和指状流道。同时,基于Okada的一维模型建立了计算机代码,以预测Fortran 90电渗效应,外来杂质阳离子和水平衡时间对膜中水浓度的影响。交错的和蜿蜒的流场表明,水蒸气聚集在膜的阴极出口附近。并且,蛇形流场比叉指流场累积更多的水蒸气。当进水质量分数低于10%时,可能会发生干燥问题,从而降低电流密度。另外,外来杂质阳离子可引起更强的电渗透作用并减少水的回扩散作用。因此,导致阴极中积水。它需要更多的水平衡时间并降低膜性能。

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