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质子交换膜燃料电池三维性能数值仿真
引用本文:邱彦樵,许逸达,苏艾. 质子交换膜燃料电池三维性能数值仿真[J]. 电池, 2004, 34(3): 229-231
作者姓名:邱彦樵  许逸达  苏艾
作者单位:元智大学机械工程学系,台湾省;元智大学机械工程学系,台湾省;元智大学机械工程学系,台湾省
摘    要:采用CFDResearchCorporation(CFDRC)Ver .2 0 0 3软件进行模型的建立及数值求解。比较了不同流道设计对电池性能的影响。结果发现 :在低操作电压下 ,气体补充速度比反应速度慢 ,容易产生浓度极化 ;栅状流道的气体分布非常不均匀 ,也会有传质极限的现象发生。蛇行流道的气体分布较均匀 ,传质也较好 ,性能比栅状流道好

关 键 词:质子交换膜燃料电池  栅状流道  蛇行流道  传质极限
文章编号:1001-1579(2004)03-0229-03
修稿时间:2003-12-10

Numerical analysis of PEMFC performance
QIU Yan-qiao,XU Yi-da,SU Ai. Numerical analysis of PEMFC performance[J]. Battery Bimonthly, 2004, 34(3): 229-231
Authors:QIU Yan-qiao  XU Yi-da  SU Ai
Abstract:Prediction of PEMFC gas concentration in mass transfer area and chemical reaction area were performed with CFD Research Corporation(CFDRC)Ver.2003 software. The influence of fuel cell performance with various flow channel design were studied. The results indicated that the gas compensation speed was lower than the reaction speed at low operating voltage, created the limit of mass transfer.The gas concentration of the straight flow pattern appeared excessive non-uniformity, created a mass transfer limit. On the other hand, the gas concentration was well distributed for the serpentine flow pattern, created a better mass transfer phenomena.
Keywords:PEMFC  straight flow pattern  serpentine flow pattern  mass transfer limit
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