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Analytical modeling of liquid saturation jump effect for hydrogen alkaline anion exchange membrane fuel cell

机译:氢碱性阴离子交换膜燃料电池液相饱和跃迁效应的解析模型

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Alkaline anion exchange membrane fuel cell (AEMFC) has been recognized as a promising zero-emission power source for portable, mobile and stationary application in recent years. To ensure high ionic conductivity and efficient reactants delivery, water management is regarded as one of the most critical issues for AEMFC. In this study, an analytical model is formulated to investigate the effect of electrode wetta-bility on the water transport and resultant AEMFC performance. The pressure continuity method is considered to simulate liquid saturation jump on the interfaces of adjacent electrode layers. The results show that decreasing the cathode catalyst layer (CL) contact angle improves the performance because more water can be kept in the cathode CL decreasing polarization losses. The anode micro porous layer (MPL) is generally helpful, by forcing the liquid water to back-diffuse to the cathode. However, cathode MPL hinders the water transport to the cathode CL, leading to a lower reaction rate and membrane conductivity. The liquid water injection into the cathode has great potential to further improve the performance of AEMFC, however it may cause flooding in the flow channel and GDL The cathode reaction kinetics should be considered as one of the most significant factors dragging the cell performance.
机译:近年来,碱性阴离子交换膜燃料电池(AEMFC)被公认为是便携式,移动式和固定式应用的有希望的零排放电源。为了确保高离子电导率和有效的反应物输送,水管理被视为AEMFC的最关键问题之一。在这项研究中,建立了一个分析模型来研究电极润湿性对水传输和所得AEMFC性能的影响。考虑采用压力连续性方法来模拟相邻电极层界面上的液体饱和跃变。结果表明,减小阴极催化剂层(CL)的接触角可改善性能,因为可以在阴极CL中保留更多的水,从而减少极化损耗。阳极微孔层(MPL)通常是有用的,它可以迫使液态水向后扩散到阴极。然而,阴极MPL阻碍了水向阴极CL的传输,导致较低的反应速率和膜电导率。注入阴极的液态水具有进一步改善AEMFC性能的巨大潜力,但是它可能导致流道和GDL泛滥。应将阴极反应动力学视为拖累电池性能的最重要因素之一。

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