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PEMFC阴极面带增湿槽道的模拟分析
引用本文:丁刚强,罗志平,潘牧.PEMFC阴极面带增湿槽道的模拟分析[J].电池工业,2007,12(5):320-324.
作者姓名:丁刚强  罗志平  潘牧
作者单位:1. 中国船舶重工集团公司第712研究所,湖北,武汉,430064
2. 武汉理工大学材料复合新技术国家重点实验室,湖北,武汉,430070
摘    要:对阴极面为带增湿槽道流场的单电池使用FLUENT软件建立了一个完整的三维数学模型。通过耦合气体控制方程、电化学反应Butler-Volmer方程、膜中水传递方程和水的相变方程,以及分析膜的水含量、阴极催化层水浓度、氧气浓度和膜中电流密度分布;结果表明,最后得到增湿槽道在实现阴极增湿的同时损失了其对应的活性面积。

关 键 词:质子交换膜燃料电池  数学模型  增湿技术  CFD
文章编号:1008-7923(2007)05-0320-05
修稿时间:2006-05-23

Modeling of cathode with increased wet channel PEMFC
DING Gang-qiang,LUO Zhi-ping,PAN Mu.Modeling of cathode with increased wet channel PEMFC[J].Chinese Battery Industry,2007,12(5):320-324.
Authors:DING Gang-qiang  LUO Zhi-ping  PAN Mu
Affiliation:1.The 712 Research Institute, CSIC, Wuhan, Hubei 430064, China; 2. State Key Laboratory of Advanced Technology for Materials Synthesis and Progressing, Wuhan University of Technology, Wuhan, Hubei 430070, China
Abstract:A three-dimensional mathematical model of cathode in single cell increased wet channel had been developed with FLUENT software.In this model,the gas governing equation,electrochemistry reactions Butler-Volmer equation,membrane water transport equation and liquid water formation and vaporization equation were solved.By analyzing the membrane water content,cathode catalysis layer water density and oxygen density and distribution of current density in the membrane,we can get the results that the increased wet channel way achieves cathode humidity.And at the same time,it lose its corresponding active area.
Keywords:PEM fuel cell  mathematical model  humidifying technology  CFD
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