Efficient and Stable Proton Exchange Membrane Water Electrolysis Enabled by Stress Optimization

被引:31
作者
Liu, Jiawei [1 ,2 ,3 ]
Liu, Han [1 ,2 ,3 ]
Yang, Yang [1 ,2 ,3 ]
Tao, Yongbing [3 ]
Zhao, Lanjun [4 ]
Li, Shuirong [5 ]
Fang, Xiaoliang [5 ]
Lin, Zhiwei [1 ,2 ,3 ]
Wang, Huakun [6 ]
Tao, Hua Bing [1 ,2 ,3 ]
Zheng, Nanfeng [1 ,2 ,3 ]
机构
[1] Xiamen Univ, Collaborat Innovat Ctr Chem Energy Mat, State Key Lab Phys Chem Solid Surfaces, Xiamen 361005, Peoples R China
[2] Xiamen Univ, Coll Chem & Chem Engn, Xiamen 361005, Peoples R China
[3] Innovat Lab Sci & Technol Energy Mat Fujian Prov I, Xiamen 361005, Peoples R China
[4] Amoy Isl Hydrogen Xiamen Technol Co ltd, Xiamen 361101, Peoples R China
[5] Xiamen Univ, Coll Energy, Xiamen 361005, Peoples R China
[6] Xiamen Univ, Fujian Key Lab Digital Simulat Coastal Civil Engn, Xiamen 361005, Peoples R China
基金
国家重点研发计划;
关键词
OXYGEN EVOLUTION REACTION; PERFORMANCE;
D O I
10.1021/acscentsci.4c00037
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Proton exchange membrane water electrolysis (PEMWE) is a promising solution for the conversion and storage of fluctuating renewable energy sources. Although tremendously efficient materials have been developed, commercial PEMWE products still cannot fulfill industrial demands regarding efficiency and stability. In this work, we demonstrate that the stress distribution, a purely mechanical parameter in electrolyzer assembly, plays a critical role in overall efficiency and stability. The conventional cell structure, which usually adopts a serpentine flow channel (S-FC) to deliver and distribute reactants and products, resulted in highly uneven stress distribution. Consequently, the anode catalyst layer (ACL) under the high stress region was severely deformed, whereas the low stress region was not as active due to poor electrical contact. To address these issues, we proposed a Ti mesh flow channel (TM-FC) with gradient pores to reduce the stress inhomogeneity. Consequently, the ACL with TM-FC exhibited 27 mV lower voltage initially and an 8-fold reduction in voltage degradation rate compared to that with S-FC at 2.0 A/cm(2). Additionally, the applicability of the TM-FC was demonstrated in cross-scale electrolyzers up to 100 kW, showing a voltage increase of only 20 mV (accounting for less than 2% of overall voltage) after three orders of magnitude scaleup.
引用
收藏
页码:852 / 859
页数:8
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