Understanding the impact of the gas diffusion layer structure on catalyst utilization in the PEM water electrolyzer

A multiphysics half-cell model of a polymer electrolyte membrane water electrolyzer (PEMWE) was developed to probe impacts of the detailed 3-dimensional pore structure of the gas diffusion layer (GDL) on performance characteristics. We show that pores in the titanium GDL mesh led to significant unde...

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Main Authors: Yuyao Huang, Samuel Williams, Tae Wook Heo, Aaron Marshall, Brandon Wood, John Kennedy, James Metson, Meng Wai Woo, Jingjing Liu
Format: Article
Language:English
Published: Elsevier 2025-07-01
Series:Next Energy
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Online Access:http://www.sciencedirect.com/science/article/pii/S2949821X25000821
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author Yuyao Huang
Samuel Williams
Tae Wook Heo
Aaron Marshall
Brandon Wood
John Kennedy
James Metson
Meng Wai Woo
Jingjing Liu
author_facet Yuyao Huang
Samuel Williams
Tae Wook Heo
Aaron Marshall
Brandon Wood
John Kennedy
James Metson
Meng Wai Woo
Jingjing Liu
author_sort Yuyao Huang
collection DOAJ
description A multiphysics half-cell model of a polymer electrolyte membrane water electrolyzer (PEMWE) was developed to probe impacts of the detailed 3-dimensional pore structure of the gas diffusion layer (GDL) on performance characteristics. We show that pores in the titanium GDL mesh led to significant underutilization of the catalyst layer (CL), with only 45% of the catalyst effectively utilized. This contradicts the assumption of uniform electron flow across the CL, as shown in graphical abstract (a), as near-zero current was observed near GDL pore regions and the current distribution in CL was influenced by GDL structure, as shown in graphical abstract (b). Instead, oxygen generation was primarily concentrated under the solid titanium regions, diffusing out around the pore walls. High current density peaks were also noted at the GDL-catalyst contact, correlating with degradation hotspots that were directly observed in companion experiments, as shown in graphical abstract (c). Collectively, these findings point to the critical importance of the heterogeneous GDL porous architecture not only for PEMWE efficiency but also for uneven degradation of the CL.
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series Next Energy
spelling doaj-art-7b3779ad7da647d79428aba0b1c2f7be2025-08-20T02:17:33ZengElsevierNext Energy2949-821X2025-07-01810031910.1016/j.nxener.2025.100319Understanding the impact of the gas diffusion layer structure on catalyst utilization in the PEM water electrolyzerYuyao Huang0Samuel Williams1Tae Wook Heo2Aaron Marshall3Brandon Wood4John Kennedy5James Metson6Meng Wai Woo7Jingjing Liu8Department of Chemical and Materials Engineering, Faculty of Engineering, University of Auckland, Auckland, New ZealandDepartment of Chemical and Materials Engineering, Faculty of Engineering, University of Auckland, Auckland, New ZealandLawrence Livermore National Laboratory, Livermore, CA, United StatesUniversity of Canterbury, Department of Chemical and Process Engineering, 20 Kirkwood Avenue, Upper Riccarton, Christchurch 8041, New ZealandLawrence Livermore National Laboratory, Livermore, CA, United StatesNational Isotope Center, GNS Science, 30 Gracefield Road, Gracefield, Lower Hutt 5010, New ZealandUniversity of Auckland, Faculty of Science, Auckland, 1010, New ZealandDepartment of Chemical and Materials Engineering, Faculty of Engineering, University of Auckland, Auckland, New ZealandDepartment of Chemical and Materials Engineering, Faculty of Engineering, University of Auckland, Auckland, New Zealand; Corresponding author.A multiphysics half-cell model of a polymer electrolyte membrane water electrolyzer (PEMWE) was developed to probe impacts of the detailed 3-dimensional pore structure of the gas diffusion layer (GDL) on performance characteristics. We show that pores in the titanium GDL mesh led to significant underutilization of the catalyst layer (CL), with only 45% of the catalyst effectively utilized. This contradicts the assumption of uniform electron flow across the CL, as shown in graphical abstract (a), as near-zero current was observed near GDL pore regions and the current distribution in CL was influenced by GDL structure, as shown in graphical abstract (b). Instead, oxygen generation was primarily concentrated under the solid titanium regions, diffusing out around the pore walls. High current density peaks were also noted at the GDL-catalyst contact, correlating with degradation hotspots that were directly observed in companion experiments, as shown in graphical abstract (c). Collectively, these findings point to the critical importance of the heterogeneous GDL porous architecture not only for PEMWE efficiency but also for uneven degradation of the CL.http://www.sciencedirect.com/science/article/pii/S2949821X25000821PEM water electrolyzerElectron distributionCOMSOLOxygen generationCatalyst efficiency
spellingShingle Yuyao Huang
Samuel Williams
Tae Wook Heo
Aaron Marshall
Brandon Wood
John Kennedy
James Metson
Meng Wai Woo
Jingjing Liu
Understanding the impact of the gas diffusion layer structure on catalyst utilization in the PEM water electrolyzer
Next Energy
PEM water electrolyzer
Electron distribution
COMSOL
Oxygen generation
Catalyst efficiency
title Understanding the impact of the gas diffusion layer structure on catalyst utilization in the PEM water electrolyzer
title_full Understanding the impact of the gas diffusion layer structure on catalyst utilization in the PEM water electrolyzer
title_fullStr Understanding the impact of the gas diffusion layer structure on catalyst utilization in the PEM water electrolyzer
title_full_unstemmed Understanding the impact of the gas diffusion layer structure on catalyst utilization in the PEM water electrolyzer
title_short Understanding the impact of the gas diffusion layer structure on catalyst utilization in the PEM water electrolyzer
title_sort understanding the impact of the gas diffusion layer structure on catalyst utilization in the pem water electrolyzer
topic PEM water electrolyzer
Electron distribution
COMSOL
Oxygen generation
Catalyst efficiency
url http://www.sciencedirect.com/science/article/pii/S2949821X25000821
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