分解水
电极
微型多孔材料
电解质
电解
制氢
材料科学
电解水
析氧
碱性水电解
氢
气泡
化学工程
复合材料
化学
电化学
催化作用
并行计算
计算机科学
生物化学
有机化学
物理化学
光催化
工程类
作者
Yu Chen,Jiaojiao Chen,Ke Bai,Jingyun Liu,Zeyi Xiao,Senqing Fan
出处
期刊:Fuel
[Elsevier]
日期:2024-02-01
卷期号:358: 130317-130317
被引量:1
标识
DOI:10.1016/j.fuel.2023.130317
摘要
In order to promote gas bubble transport during water splitting for hydrogen production, stacked mesh electrodes integrated microporous structure flowing and electrolytic water splitting have been fabricated by electrodepositing CoFe alloy. The average size of the bubble on the mesh electrode surface is 40 μm and the release time of trapped bubbles in the pores of the electrode is 2.11 s during the process of water splitting at 50 mA cm−2 and 1 M KOH. The electrodes show excellent performance in both hydrogen evolution reaction (HER, 247 mV at 1000 mA cm−2) and oxygen evolution reaction (OER, 350 mV at 1000 mA cm−2). The required cell voltage at 1000 mA cm−2 for flow-through electrolyzer assembled with the stacked mesh electrodes is only 2 V under the condition of 6 M KOH, and 343 K. The voltage caused by the bubble in the flow-through electrolyzer assembled with stacked mesh electrodes is just about 50 mV at the current density of 1000 mA cm−2. The energy required for hydrogen production is only 4.04 kWh Nm−3 and 4.78 kWh Nm−3 under the current density of 200 mA cm−2 and 1000 mA cm−2, respectively. Besides, the flow-through electrolyzer assembled with the stacked mesh electrodes shows excellent stability with only a 60 mV increase in cell voltage after continuing electrolytic water splitting for 100 h at 1000 mA cm−2.
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