质子交换膜燃料电池
压力降
限制电流
多孔性
堆栈(抽象数据类型)
气体扩散
化学
扩散
饱和(图论)
材料科学
膜
复合材料
传质
磁导率
化学工程
色谱法
燃料电池
机械
电极
热力学
工程类
电化学
计算机科学
组合数学
物理
数学
物理化学
生物化学
程序设计语言
作者
Yong Zhang,Shirong He,Xiaohui Jiang,Zhuo Wang,Xi Yang,Haoyan Fang,Qiming Li,Jing Cao
出处
期刊:Energy
[Elsevier BV]
日期:2023-11-16
卷期号:287: 129664-129664
被引量:26
标识
DOI:10.1016/j.energy.2023.129664
摘要
Aiming at the problems of inconsistent local distribution of reactant gas and easy blockage of water in the traditional “bipolar plate (BP) + gas diffusion layer (GDL)” structure flow field (FF). A new type of porous foam flow field (PFFF) with integrated BP/GDL (taking the pore of decahedral structure as matrix) is proposed. Firstly, three-dimensional (3D) proton exchange membrane fuel cell (PEMFC) saturation model is applied to analyze the influence of the availability of GDL components and different channel (CH) widths. GDL is essential for channel-rib (CR) FF because its elimination leads to the non-uniform mass distribution in fuel cell (FC). Secondly, by comparing CRFF and PFF with “BP + GDL” structure and PFFF with integrated BP/GDL, it is found that the limiting current density of PFF increases by 49.9 % compared with CRFF, and the mass transmission loss is reduced. Compared with PFF, the performance of PFFF is greatly enhanced, the pressure drop is moderate, and the amount of liquid water in CH is reduced by 39.1 %. Therefore, GDL component that eliminate PFF is extremely beneficial to improve FC efficiency and reduce stack volume. Finally, the output performance of FC under various porosities and pore number is explored.
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