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首页> 外文期刊>Journal of Chemical Engineering of Japan >Modeling of Heat Transfer in Single Cell of Polymer Electrolyte Fuel Cell by Means of Temperature Data Measured by Thermograph
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Modeling of Heat Transfer in Single Cell of Polymer Electrolyte Fuel Cell by Means of Temperature Data Measured by Thermograph

机译:借助热成像仪测量温度数据的聚合物电解质燃料电池单电池传热建模

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References(17) Cited-By(1) The aim of this study is to construct a simple heat-transfer model to present the temperature of the interface between the polymer electrolyte membrane (PEM) and the catalyst layer at the cathode, i.e., the reaction surface, in a single cell of polymer electrolyte fuel cell (PEFC). The model is based on the temperature data of the separator measured by thermograph in a power-generation experiment. In addition, this study also aims to investigate the effect of the operation condition on the temperature of the reaction surface using the heat-transfer model developed. The heat-transfer model is constructed by assuming multi plate heat transfer for components of a single cell of PEFC. In this model, the temperature of the reaction surface under the rib of separator and that under the gas channel of the separator are assumed to be the same. The result shows that the temperature of the reaction surface is higher with increasing gas channel pitch. The impact of the flow rate of the supply gas on the temperature of the reaction surface is small when O2 is used as the cathode supply gas. When air is used as the cathode supply gas, the temperature of the reaction surface is higher than that when O2 is used. The temperature of the reaction surface at the inlet is lower than that at the middle and outlet of the cell. This study can explain these temperature characteristics under several conditions by power-generation performance and energy conversion of the fuel cell.
机译:参考文献(17)Cited-By(1)这项研究的目的是构建一个简单的传热模型,以显示聚合物电解质膜(PEM)与阴极处催化剂层之间的界面温度,即反应表面,位于聚合物电解质燃料电池(PEFC)的单个电池中。该模型基于在发电实验中通过热像仪测量的隔板温度数据。此外,本研究还旨在使用开发的传热模型研究操作条件对反应表面温度的影响。传热模型是通过假设PEFC单电池组件的多板传热来构建的。在该模型中,假定分离器肋下方的反应表面温度和分离器气体通道下方的反应表面温度相同。结果表明,随着气体通道间距的增加,反应表面温度升高。当将O 2用作阴极供应气体时,供应气体的流量对反应表面温度的影响很小。当使用空气作为阴极供应气体时,反应表面的温度高于使用O2时的温度。入口处的反应表面温度低于池中部和出口的温度。这项研究可以通过燃料电池的发电性能和能量转换来解释几种条件下的这些温度特性。

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