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In relation to this article, we declare that there is no conflict of interest.
Publication history
Received October 14, 2025
Revised January 17, 2026
Accepted January 26, 2026
Available online April 25, 2026
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Effects of the Electrode Supporter Structures for Achieving Optimum Hydrodynamic Performance for a Zero-gap Alkaline Water Electrolysis Cell

Department of Energy Engineering, Future Convergence Technology Research Institute , Gyeongsang National University 1Department of Energy Engineering , Dankook University 2Department of Energy System Engineering , Gyeongsang National University
chp@gnu.ac.kr, chlee@dankook.ac.kr
Korean Journal of Chemical Engineering, April 2026, 43(5), 1447-1461(15)
https://doi.org/10.1007/s11814-026-00664-9

Abstract

Water electrolysis, a hydrogen energy production method, can generate pure hydrogen and oxygen without emitting 

carbon-based molecules; thus, it is an environmentally friendly technology. Zero-gap alkaline water electrolyzer (ZGAWE) 

can produce hydrogen economically and effi ciently. Here, we developed a ZGAWE hydrodynamic model and investigated 

the changes in cell performance according to the input power and diff erent electrode supporter structures, such as wavy 

mesh, foam, and serpentine, under actual operating conditions. Owing to its high hydrogen conversion rate and low 

operation costs, the wavy mesh supporter design had the highest effi ciency. Additionally, as the system size increased, the 

operation costs decreased; thus, the wavy mesh supporter design was also applicable for large-scale ZGAWE systems. 

Foam supporter fl ow fi eld design shows a very similar trend and can compete with the wavy mesh supporter. Conversely, 

diff erent hydrodynamic performance and high operation costs of the serpentine fl ow fi eld design made it unsuitable for 

the ZGAWE system, but it could be used for the proton/anion exchange membrane water electrolyzer. The results provide 

signifi cant insights into the hydrodynamic eff ects to operate ZGAWEs at diff erent cell voltages; additionally, the results 

can be used to develop high-performance water electrolyzer systems.

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