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A Numerical Model Predicting Liquid Water Saturation within the Cathode Electrode of a Proton Exchange Membrane Fuel Cell

机译:预测质子交换膜燃料电池的阴极电极内液体水饱和的数值模型

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A two-phase, half cell, model of a proton exchange membrane fuel cell cathode has been developed with emphasis on the liquid water saturation within the three porous layer structure, i.e. the catalyst layer, the micro-porous layer and the gas-diffusion layer. The model was run under varying current density, operating temperature, relative humidity and gaseous flow rate. The results show that the calculated liquid saturation profiles strongly depends on the local distribution of these variables which are highly coupled. For example, an under-humidified gas feed entering into the cell, first undergoes through the evaporation regime at low current densities, followed by liquid-water generation at moderate current densities, and finally evaporation of the liquid-water at higher current densities due to increase in the cell temperature. The increase in air flow rate enhances the liquid-water saturation within the catalyst layer, near the channel area, and reduces its amount under the ribs. The reduced liquid-saturation under the ribs is due to higher local temperature because of increased reactant transport that results in its evaporation. In summary, prediction of liquid-water saturation within the cathode is a highly complicated phenomenon that is strongly coupled to the above variables.
机译:已经开发了一种两相,半电池的质子交换膜燃料电池阴极的模型,其强调三个多孔层结构内的液体水饱和度,即催化剂层,微多孔层和气体扩散层。该模型在不同电流密度,工作温度,相对湿度和气体流速下运行。结果表明,计算出的液体饱和轮廓强烈取决于这些变量的局部分布,这些变量高耦合。例如,进入细胞的欠加湿气体进料,首先通过低电流密度通过蒸发状态进行,然后在中等电流密度下产生液体水,并且最终在由于较高的电流密度下蒸发液态水细胞温度增加。空气流量的增加增强了催化剂层内的液体水饱和度,靠近通道区域,并降低其在肋骨下的量。肋骨下的液体饱和度降低是由于较高的局部温度,因为导致其蒸发的反应性转运增加。总之,阴极内的液体饱和度的预测是高度复杂的现象,其强烈地偶联到上述变量。

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