质子交换膜燃料电池
电解质
材料科学
水运
氧气输送
电解
浮力
化学工程
化学
电解水
气泡
氧气
聚合物电解质膜电解
膜
阳极
分析化学(期刊)
电极
水流
色谱法
机械
环境工程
工程类
物理化学
物理
有机化学
生物化学
作者
Hironori Nakajima,Vediyappan Veeramani,Hiroshige Matsumoto,Motohiko Sato,Omar Samuel Mendoza-Hernandez,Asuka Shima,Yoshitsugu Sone
出处
期刊:Electrochemistry
[The Electrochemical Society of Japan]
日期:2021-10-01
卷期号:90 (1): 017002-017002
被引量:3
标识
DOI:10.5796/electrochemistry.21-00097
摘要
A novel interdigitated flow field design for polymer electrolyte electrolysis cells (proton exchange membrane water electrolysis cells) composed of oxygen exhaust channels apart from liquid water feed channels has been developed for ground and space applications because the design is advantageous in terms of oxygen/water separation without buoyancy, and dispenses with water circulators for bubble removal in a cell and external separators by natural or centrifugal buoyancy. Finite element modeling of water transport in the polymer electrolyte (proton exchange) membrane in a cell with the interdigitated flow fields is conducted. Current-voltage (I–V) measurement of the cell is also performed for comparison with numerical modeling. Deviation of the experimental I–V characteristics from those of the numerical model indicates a possible water transport path in the in-plane direction of hydrophobic microporous layers (MPLs) coated on gas diffusion layers installed between the anode catalyst layers (CLs) and oxygen flow channels in the cell. Analysis of the deviation associated with the limitation of water transport also suggests fractional bubble coverage of produced oxygen gas at the CLs. The hydrophobic MPL acts to separate oxygen gas and pressurized liquid water due to the capillary pressure, while it determines the limitation of water transport to the CLs with the oxygen bubble coverage.
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