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首页> 外文期刊>Journal of Chemical Engineering of Japan >Clarification on Temperature Distribution in Single Cell of Polymer Electrolyte Fuel Cell under Different Operation Conditions by Means of 1D Multi-Plate Heat-Transfer Model
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Clarification on Temperature Distribution in Single Cell of Polymer Electrolyte Fuel Cell under Different Operation Conditions by Means of 1D Multi-Plate Heat-Transfer Model

机译:利用一维多层板传热模型澄清不同运行条件下聚合物电解质燃料电池单电池的温度分布

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This study focused on understanding the impact of operating conditions on the temperature profile of the interface between the polymer electrolyte membrane (PEM) and the catalyst layer at the cathode (i.e., the reaction surface) in a single polymer electrolyte fuel cell (PEFC). A 1D multi-plate heat-transfer model based on the temperature data of the separator measured by the thermograph in a power-generation experiment was developed to evaluate the temperature profile of the reaction surface. The in-plane temperature distributions on the reaction surface, which was analyzed at twenty points were investigated in detail with the relative humidity, flow rate of the supply gas, and gas channel pitch of the separator as variables. The results showed that the temperature of the reaction surface increased with the gas channel pitch except when the flow rate and relative humidity of supply gas were low. The temperature of the reaction surface measured along the gas-flow direction from the inlet to the outlet of the cell by 1-2 K under all experimental conditions. The impact of the relative humidity of the supply gas on the temperature of the reaction surface was insignificant compared to that of the gas channel pitch. The results of this study suggest that the temperature of the supply gas should be set higher by 2 K and that the accumulated water should be removed from the turn-round part of the gas channel in order to realize an even in-plane temperature distribution on the reaction surface.
机译:这项研究着重于了解操作条件对单个聚合物电解质燃料电池(PEFC)中阴极(即反应表面)处的聚合物电解质膜(PEM)和催化剂层之间的界面温度分布的影响。基于在发电实验中通过热像仪测量的隔板温度数据,建立了一维多板传热模型,以评估反应表面的温度分布。以相对湿度,供应气体的流速和分离器的气体通道间距为变量,详细研究了在20个点分析的反应表面的面内温度分布。结果表明,除了供给气体的流量和相对湿度较低时,反应表面的温度均随气体通道间距的增加而升高。在所有实验条件下,沿着从电池的进口到出口的气流方向测量的反应表面温度为1-2K。与气体通道间距相比,供给气体的相对湿度对反应表面温度的影响微不足道。该研究结果表明,应将供气温度设置为2 K,并应从气体通道的转弯部分清除积聚的水,以实现平面上均匀的面内温度分布。反应表面。

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