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An analytical model for hydrogen alkaline anion exchange membrane fuel cell

机译:氢碱性阴离子交换膜燃料电池的分析模型

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An analytical model for hydrogen alkaline anion exchange membrane fuel cell (AAEMFC) is developed in this study. The results show that due to both the electrochemical reaction and electro-osmotic drag, water in cathode is consumed faster than oxygen. Proper liquid humidification in cathode is favorable for performance improvement, especially at low operating temperatures; on the other hand, without liquid humidification, high reactant flow rate is needed. If there is no liquid humidification and the oxygen stoichiometry ratio is fixed, a higher operating pressure increases both the activation loss and ohmic loss, leading to lower cell performance. With the increment of catalyst layer (CL) thickness, the reactant concentration in CL decreases, and the ohmic resistance of electron and ion increases. Decreasing the membrane thickness reduces both the ohmic resistance and activation loss, because more water can transfer from anode to cathode. Copyright (C) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
机译:本研究建立了氢碱性阴离子交换膜燃料电池(AAEMFC)的分析模型。结果表明,由于电化学反应和电渗透阻力,阴极中的水消耗速度快于氧气。阴极中适当的液体加湿有利于提高性能,尤其是在较低的工作温度下;另一方面,在没有液体加湿的情况下,需要高的反应物流速。如果没有液体加湿并且氧气化学计量比固定,则较高的工作压力会同时增加活化损失和欧姆损失,从而导致电池性能下降。随着催化剂层(CL)厚度的增加,CL中的反应物浓度降低,电子和离子的欧姆电阻增加。减小膜厚度可同时降低欧姆电阻和活化损失,因为更多的水可以从阳极转移到阴极。 Hydrogen Energy Publications,LLC版权所有(C)2015。由Elsevier Ltd.出版。保留所有权利。

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