聚合物电解质膜电解
电解
阳极
电解水
电解质
极化(电化学)
制氢
电流密度
质子交换膜燃料电池
输运现象
氢
材料科学
化学工程
多孔性
氧气输送
浓差极化
水运
电化学
机械
化学
膜
电极
水流
氧气
环境科学
复合材料
环境工程
工程类
物理
有机化学
物理化学
量子力学
生物化学
作者
Hassan Salihi,Hyunchul Ju
出处
期刊:Energies
[Multidisciplinary Digital Publishing Institute]
日期:2023-01-09
卷期号:16 (2): 766-766
被引量:10
摘要
Polymer electrolyte membrane (PEM) electrolysis has a promising future for large-scale hydrogen production. As PEM electrolysis technology develops, larger operating current densities are required. In order to increase current density, more water should be available at the reaction sites. Moreover, the removal rate of oxygen and hydrogen needs to be effectively improved. This, in turn, necessitates a better understanding of the main mass transport and electrochemical processes. On the anode side, mass transport is particularly crucial because water must be supplied to the catalyst layer (CL) while, at the same time, oxygen bubbles must be eliminated in a parallel flow from the reaction sites into the flow channels. Hence, simulating the two-phase bubbly flow across the cell thickness is necessary to predict PEM electrolysis performance more accurately as a function of the operating current density. This study provides a systematic understanding of how morphological and geometrical features contribute to the polarization curve and performance characteristics of a PEM electrolysis cell. Hence, a multi-phase PEM electrolysis model has been implemented using MATLAB R2022a. Polarization curves have been calibrated against experimental data and then assessed to provide a fundamental understanding of the relationship between the two-phase flow and cell performance.
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