The critical role of the anode porous transport layer/catalyst layer interface of polymer electrolyte membrane water electrolyzers: A parametric analysis

dc.contributor.authorGarcía-Salaberri, Pablo A.
dc.contributor.authorChang , Hung-Ming
dc.contributor.authorLang, Jack Todd
dc.contributor.authorFiras, Nausir
dc.contributor.authorShazhad , Hasan
dc.contributor.authorMorimoto, Yu
dc.contributor.authorZenyuk, Iryna V.
dc.date.accessioned2025-05-19T12:06:46Z
dc.date.available2025-05-19T12:06:46Z
dc.date.issued2025-04-01
dc.descriptionThis work was supported by project TED2021-131620B-C21 of the Spanish Research Council. The authors acknowledge the use of facilities and instrumentation at the UC Irvine Materials Research Institute (IMRI), which is supported in part by the National Science Foundation through the UC Irvine Materials Research Science and Engineering Center (DMR-2011967). SEM work was performed using instrumentation funded in part by the National Science Foundation Center for Chemistry at the Space-Time Limit (CHE-0802913).
dc.description.abstractReducing the dependency of proton exchange membrane water electrolyzers (PEMWE) on precious metals, such as iridium (Ir), is necessary to develop a widespread green hydrogen system. This challenge requires a careful design of the interface between the anode porous transport layer (PTL) and the catalyst layer (CL). A comprehensive numerical analysis of relevant parameters that govern the behavior of the anode PTL/CL interface is presented. Calculations are also combined with an experimental characterization of the thickness and electrical conductivity of an unsupported CL as a function of Ir loading. The results show that the in-plane electrical resistance at the anode PTL/CL interface plays a critical role in cell performance. Reaching an acceptable electrical resistance at low Ir loading (𝐿Ir ≃ 0.1 mgIr , cm−2) can be accomplished through the incorporation of a micrometer-sized microporous layer (MPL) onto the PTL or the preparation of bimodal CLs with a secondary conductive phase. Further reduction of the Ir loading to the ultra-low regime (𝐿Ir ≲ 0.1 mgIr , cm−2) may require the use of nanometer-sized MPLs with unsupported CLs or micrometer-sized MPLs with bimodal CLs. Furthermore, the decline of the volume reactive area at ultra-low Ir loading needs a maximization of the exchange current density and the specific electrochemical surface area, and a decrease of the catalyst oxygen coverage factor in the anode CL.
dc.identifier.citationPablo A. García-Salaberri, Hung-Ming Chang, Jack Todd Lang, Nausir Firas, Hasan Shazhad, Yu Morimoto, Iryna V. Zenyuk, The critical role of the anode porous transport layer/catalyst layer interface of polymer electrolyte membrane water electrolyzers: A parametric analysis, Chemical Engineering Journal, Volume 509, 2025, 160722, ISSN 1385-8947, https://doi.org/10.1016/j.cej.2025.160722
dc.identifier.doihttps://doi.org/10.1016/j.cej.2025.160722
dc.identifier.issn1385-8947 (print)
dc.identifier.issn1873-3212 (online)
dc.identifier.urihttps://hdl.handle.net/10115/86337
dc.language.isoen
dc.publisherElsevier
dc.rightsAttribution 4.0 Internationalen
dc.rights.accessRightsinfo:eu-repo/semantics/openAccess
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/
dc.subjectPTL/CL interface
dc.subjectPerformance
dc.subjectIr loading
dc.subjectElectrical conductivity
dc.subjectModeling
dc.subjectPEMWE
dc.titleThe critical role of the anode porous transport layer/catalyst layer interface of polymer electrolyte membrane water electrolyzers: A parametric analysis
dc.typeArticle

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