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Tubular membrane electrode assembly for PEM electrolysis

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Tubular membrane electrode assembly for PEM electrolysis

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dc.contributor.author Laube, A. es_ES
dc.contributor.author Hofer, A. es_ES
dc.contributor.author Sánchez Batalla, B. es_ES
dc.contributor.author Ressel, S. es_ES
dc.contributor.author Chica, Antonio es_ES
dc.contributor.author Fischer, S. es_ES
dc.contributor.author Weidlich, C. es_ES
dc.contributor.author Bachmann, J. es_ES
dc.contributor.author Struckmann, T. es_ES
dc.date.accessioned 2024-01-29T19:01:30Z
dc.date.available 2024-01-29T19:01:30Z
dc.date.issued 2022-04-29 es_ES
dc.identifier.issn 0360-3199 es_ES
dc.identifier.uri http://hdl.handle.net/10251/202210
dc.description.abstract [EN] Polymer electrolyte membrane (PEM) water electrolysis is already widely used for hydrogen production but still needs further cost reductions. While tubular cell designs might reduce production costs by extrusion production of cell components and small sealing lengths, catalyst coating methods like atomic layer deposition (ALD) might reduce catalyst costs significantly. This study demonstrates the feasibility of a tubular PEM electrolyzer membrane electrode assembly (MEA) for the oxygen half cell with 5.0 mm diameter. An extruded perfluorosulfonic acid (PFSA) cation exchange membrane is combined with a porous transport electrode (PTE) consisting of a titanium felt with a low iridium catalyst loading obtained by ALD. The performance is experimentally characterized in a complete tubular cell setup by polarization curve and ohmic resistance measurements. Operation in sulphuric acid at a cell voltage of 1.7 V and a cell temperature of 60 °C results in an overall current density of 55 mA cm¿1 and an iridium mass activity 680 A g¿1 which is up to 3 times larger than literature values. The high frequency ohmic resistance of the cell turns out to be 0.96 ¿ cm¿2. Up to the knowledge of the authors, this is the first time, that a tubular PEM electrolysis cell is designed, assembled and characterized. es_ES
dc.description.sponsorship This work was done within the research project Tubulyze and was supported by the German Federal Ministry of Education and Research (BMBF FKZ: 03FS0564B). es_ES
dc.language Inglés es_ES
dc.publisher Elsevier es_ES
dc.relation.ispartof International Journal of Hydrogen Energy es_ES
dc.rights Reconocimiento - No comercial - Sin obra derivada (by-nc-nd) es_ES
dc.subject Cylindric cell design es_ES
dc.subject PEM water Electrolysis es_ES
dc.subject ALD catalyst Coating es_ES
dc.subject Porous transport electrodes es_ES
dc.title Tubular membrane electrode assembly for PEM electrolysis es_ES
dc.type Artículo es_ES
dc.identifier.doi 10.1016/j.ijhydene.2022.03.135 es_ES
dc.relation.projectID info:eu-repo/grantAgreement/BMBF//03FS0564B//Tubulyze/ es_ES
dc.rights.accessRights Abierto es_ES
dc.contributor.affiliation Universitat Politècnica de València. Instituto Universitario Mixto de Tecnología Química - Institut Universitari Mixt de Tecnologia Química es_ES
dc.description.bibliographicCitation Laube, A.; Hofer, A.; Sánchez Batalla, B.; Ressel, S.; Chica, A.; Fischer, S.; Weidlich, C.... (2022). Tubular membrane electrode assembly for PEM electrolysis. International Journal of Hydrogen Energy. 47(36):15943-15951. https://doi.org/10.1016/j.ijhydene.2022.03.135 es_ES
dc.description.accrualMethod S es_ES
dc.relation.publisherversion https://doi.org/10.1016/j.ijhydene.2022.03.135 es_ES
dc.description.upvformatpinicio 15943 es_ES
dc.description.upvformatpfin 15951 es_ES
dc.type.version info:eu-repo/semantics/publishedVersion es_ES
dc.description.volume 47 es_ES
dc.description.issue 36 es_ES
dc.relation.pasarela S\464839 es_ES
dc.contributor.funder Bundesministerium für Bildung und Forschung, Alemania es_ES


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