Role of Reaction Intermediate Diffusion on the Performance of Platinum Electrodes in Solid Acid Fuel Cells

dc.bibliographicCitation.firstPage1065eng
dc.bibliographicCitation.issue9eng
dc.bibliographicCitation.volume11eng
dc.contributor.authorLorenz, Oliver
dc.contributor.authorKühne, Alexander
dc.contributor.authorRudolph, Martin
dc.contributor.authorDiyatmika, Wahyu
dc.contributor.authorPrager, Andrea
dc.contributor.authorGerlach, Jürgen W.
dc.contributor.authorGriebel, Jan
dc.contributor.authorWinkler, Sara
dc.contributor.authorLotnyk, Andriy
dc.contributor.authorAnders, André
dc.contributor.authorAbel, Bernd
dc.date.accessioned2022-03-25T07:36:59Z
dc.date.available2022-03-25T07:36:59Z
dc.date.issued2021
dc.description.abstractUnderstanding the reaction pathways for the hydrogen oxidation reaction (HOR) and the oxygen reduction reaction (ORR) is the key to design electrodes for solid acid fuel cells (SAFCs). In general, electrochemical reactions of a fuel cell are considered to occur at the triple-phase boundary where an electrocatalyst, electrolyte and gas phase are in contact. In this concept, diffusion processes of reaction intermediates from the catalyst to the electrolyte remain unconsidered. Here, we unravel the reaction pathways for open-structured Pt electrodes with various electrode thicknesses from 15 to 240 nm. These electrodes are characterized by a triple-phase boundary length and a thickness-depending double-phase boundary area. We reveal that the double-phase boundary is the active catalytic interface for the HOR. For Pt layers ≤ 60 nm, the HOR rate is rate-limited by the processes at the gas/catalyst and/or the catalyst/electrolyte interface while the hydrogen surface diffusion step is fast. For thicker layers (>60 nm), the diffusion of reaction intermediates on the surface of Pt be-comes the limiting process. For the ORR, the predominant reaction pathway is via the triple-phase boundary. The double-phase boundary contributes additionally with a diffusion length of a few nanometers. Based on our results, we propose that the molecular reaction mechanism at the electrode interfaces based upon the triple-phase boundary concept may need to be extended to an effective area near the triple-phase boundary length to include all catalytically relevant diffusion processes of the reaction intermediates. © 2021 by the authors. Licensee MDPI, Basel, Switzerland.eng
dc.description.versionpublishedVersioneng
dc.identifier.urihttps://oa.tib.eu/renate/handle/123456789/8379
dc.identifier.urihttps://doi.org/10.34657/7417
dc.language.isoengeng
dc.publisherBasel : MDPIeng
dc.relation.doihttps://doi.org/10.3390/catal11091065
dc.relation.essn2073-4344
dc.relation.ispartofseriesCatalysts 11 (2021), Nr. 9eng
dc.rights.licenseCC BY 4.0 Unportedeng
dc.rights.urihttps://creativecommons.org/licenses/by/4.0/eng
dc.subjectDouble-phase boundaryeng
dc.subjectHydrogen oxidation reactioneng
dc.subjectMagnetron sputteringeng
dc.subjectOxygen reduction reactioneng
dc.subjectPlatinum thin filmseng
dc.subjectReaction pathwayeng
dc.subjectSolid acid fuel cellseng
dc.subjectTriple-phase boundaryeng
dc.subject.ddc540eng
dc.titleRole of Reaction Intermediate Diffusion on the Performance of Platinum Electrodes in Solid Acid Fuel Cellseng
dc.typearticleeng
dc.typeTexteng
dcterms.bibliographicCitation.journalTitleCatalystseng
tib.accessRightsopenAccesseng
wgl.contributorIOMeng
wgl.subjectChemieeng
wgl.typeZeitschriftenartikeleng
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