阴极
质子交换膜燃料电池
电解
机械
流量(数学)
化学
等温过程
压力降
电流密度
电解水
聚合物电解质膜电解
分析化学(期刊)
材料科学
膜
电极
热力学
电解质
色谱法
物理
量子力学
生物化学
物理化学
作者
Yufeng Zhuang,Pan Cui,Rui Long,Wei Liu,Zhichun Liu
标识
DOI:10.1016/j.ijhydene.2023.08.026
摘要
The flow field dominates the process of mass transport and distribution inside the proton exchange membrane water electrolysis cell (PEMEC). Initially, a three-dimensional and non-isothermal PEMEC channel model was estimated to investigate the impact of channel height and width. Based on these results, a complete PEMEC model with a parallel flow-field pattern was developed, and the channel heights and widths of the model were optimized using a genetic algorithm (GA). Compared to the original model, the optimized model decreased the pressure drop by 34.97% at a lower voltage. In addition, because of the optimized flow-field pattern, the optimized model improves the current density on the proton exchange membrane as well as the gas holdup situation in a partial position in the cathode gas diffusion layer.
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