Microporous structure flowing integrated with electrolytic water splitting based on stacked mesh electrode for hydrogen production

被引:6
作者
Chen, Yu [1 ]
Chen, Jiaojiao [1 ]
Bai, Ke [1 ]
Liu, Jingyun [1 ]
Xiao, Zeyi [1 ]
Fan, Senqing [1 ]
机构
[1] Sichuan Univ, Sch Chem Engn, 24 South Sect 1,Yihuan Rd, Chengdu 610065, Peoples R China
关键词
Electrolytic water splitting; Hydrogen production; Stacked mesh electrode; Microporous structure flowing; Flow-through electrolyzer; BUBBLE FORMATION; EVOLUTION; AREA;
D O I
10.1016/j.fuel.2023.130317
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In order to promote gas bubble transport during water splitting for hydrogen production, stacked mesh elec-trodes integrated microporous structure flowing and electrolytic water splitting have been fabricated by elec-trodepositing CoFe alloy. The average size of the bubble on the mesh electrode surface is 40 mu m 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.
引用
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页数:10
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