Design Strategies for Alkaline Exchange Membrane–Electrode Assemblies: Optimization for Fuel Cells and Electrolyzers

Production of hydrocarbon-based, alkaline exchange, membrane–electrode assemblies (MEA’s) for fuel cells and electrolyzers is examined via catalyst-coated membrane (CCM) and gas-diffusion electrode (GDE) fabrication routes. The inability effectively to hot-press hydrocarbon-based ion-exchange polyme...

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Main Authors: Aviv Ashdot, Mordechai Kattan, Anna Kitayev, Ervin Tal-Gutelmacher, Alina Amel, Miles Page
Format: Article
Language:English
Published: MDPI AG 2021-09-01
Series:Membranes
Subjects:
Online Access:https://www.mdpi.com/2077-0375/11/9/686
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author Aviv Ashdot
Mordechai Kattan
Anna Kitayev
Ervin Tal-Gutelmacher
Alina Amel
Miles Page
author_facet Aviv Ashdot
Mordechai Kattan
Anna Kitayev
Ervin Tal-Gutelmacher
Alina Amel
Miles Page
author_sort Aviv Ashdot
collection DOAJ
description Production of hydrocarbon-based, alkaline exchange, membrane–electrode assemblies (MEA’s) for fuel cells and electrolyzers is examined via catalyst-coated membrane (CCM) and gas-diffusion electrode (GDE) fabrication routes. The inability effectively to hot-press hydrocarbon-based ion-exchange polymers (ionomers) risks performance limitations due to poor interfacial contact, especially between GDE and membrane. The addition of an ionomeric interlayer is shown greatly to improve the intimacy of contact between GDE and membrane, as determined by ex situ through-plane MEA impedance measurements, indicated by a strong decrease in the frequency of the high-frequency zero phase angle of the complex impedance, and confirmed in situ with device performance tests. The best interfacial contact is achieved with CCM’s, with the contact impedance decreasing, and device performance increasing, in the order GDE >> GDE+Interlayer > CCM. The GDE+interlayer fabrication approach is further examined with respect to hydrogen crossover and alkaline membrane electrolyzer cell performance. An interlayer strongly reduces the rate of hydrogen crossover without strongly decreasing electrolyzer performance, while crosslinking the ionomeric layer further reduces the crossover rate though also limiting device performance. The approach can be applied and built upon to improve the design and production of alkaline, and more generally, hydrocarbon-based MEA’s and exchange membrane devices.
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spelling doaj.art-b2126e10d90d447cb40e4d462d5dc68e2023-11-22T14:10:24ZengMDPI AGMembranes2077-03752021-09-0111968610.3390/membranes11090686Design Strategies for Alkaline Exchange Membrane–Electrode Assemblies: Optimization for Fuel Cells and ElectrolyzersAviv Ashdot0Mordechai Kattan1Anna Kitayev2Ervin Tal-Gutelmacher3Alina Amel4Miles Page5Hydrolite Ltd., 2 Hatochen St., Caesaria 38900, IsraelHydrolite Ltd., 2 Hatochen St., Caesaria 38900, IsraelHydrolite Ltd., 2 Hatochen St., Caesaria 38900, IsraelHydrolite Ltd., 2 Hatochen St., Caesaria 38900, IsraelHydrolite Ltd., 2 Hatochen St., Caesaria 38900, IsraelHydrolite Ltd., 2 Hatochen St., Caesaria 38900, IsraelProduction of hydrocarbon-based, alkaline exchange, membrane–electrode assemblies (MEA’s) for fuel cells and electrolyzers is examined via catalyst-coated membrane (CCM) and gas-diffusion electrode (GDE) fabrication routes. The inability effectively to hot-press hydrocarbon-based ion-exchange polymers (ionomers) risks performance limitations due to poor interfacial contact, especially between GDE and membrane. The addition of an ionomeric interlayer is shown greatly to improve the intimacy of contact between GDE and membrane, as determined by ex situ through-plane MEA impedance measurements, indicated by a strong decrease in the frequency of the high-frequency zero phase angle of the complex impedance, and confirmed in situ with device performance tests. The best interfacial contact is achieved with CCM’s, with the contact impedance decreasing, and device performance increasing, in the order GDE >> GDE+Interlayer > CCM. The GDE+interlayer fabrication approach is further examined with respect to hydrogen crossover and alkaline membrane electrolyzer cell performance. An interlayer strongly reduces the rate of hydrogen crossover without strongly decreasing electrolyzer performance, while crosslinking the ionomeric layer further reduces the crossover rate though also limiting device performance. The approach can be applied and built upon to improve the design and production of alkaline, and more generally, hydrocarbon-based MEA’s and exchange membrane devices.https://www.mdpi.com/2077-0375/11/9/686alkaline exchange membranesfuel cellselectrolyzersmembrane–electrode assembly
spellingShingle Aviv Ashdot
Mordechai Kattan
Anna Kitayev
Ervin Tal-Gutelmacher
Alina Amel
Miles Page
Design Strategies for Alkaline Exchange Membrane–Electrode Assemblies: Optimization for Fuel Cells and Electrolyzers
Membranes
alkaline exchange membranes
fuel cells
electrolyzers
membrane–electrode assembly
title Design Strategies for Alkaline Exchange Membrane–Electrode Assemblies: Optimization for Fuel Cells and Electrolyzers
title_full Design Strategies for Alkaline Exchange Membrane–Electrode Assemblies: Optimization for Fuel Cells and Electrolyzers
title_fullStr Design Strategies for Alkaline Exchange Membrane–Electrode Assemblies: Optimization for Fuel Cells and Electrolyzers
title_full_unstemmed Design Strategies for Alkaline Exchange Membrane–Electrode Assemblies: Optimization for Fuel Cells and Electrolyzers
title_short Design Strategies for Alkaline Exchange Membrane–Electrode Assemblies: Optimization for Fuel Cells and Electrolyzers
title_sort design strategies for alkaline exchange membrane electrode assemblies optimization for fuel cells and electrolyzers
topic alkaline exchange membranes
fuel cells
electrolyzers
membrane–electrode assembly
url https://www.mdpi.com/2077-0375/11/9/686
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