Degradation of proton exchange membrane (PEM) water electrolysis cells: Looking beyond the cell voltage increase

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dc.identifier.uri http://dx.doi.org/10.15488/10219
dc.identifier.uri https://www.repo.uni-hannover.de/handle/123456789/10291
dc.contributor.author Suermann, Michel
dc.contributor.author Bensmann, Boris
dc.contributor.author Hanke-Rauschenbach, Richard
dc.date.accessioned 2020-12-02T13:04:25Z
dc.date.available 2020-12-02T13:04:25Z
dc.date.issued 2019
dc.identifier.citation Suermann, M.; Bensmann, B.; Hanke-Rauschenbach, R.: Degradation of proton exchange membrane (PEM) water electrolysis cells: Looking beyond the cell voltage increase. In: Journal of the Electrochemical Society 166 (2019), Nr. 10, S. F645-F652. DOI: https://doi.org/10.1149/2.1451910jes
dc.description.abstract The degradation of proton exchange membrane water electrolysis cells is usually measured in a temporal increase of the cell voltage. Although this is sufficient to evaluate the stability of a system, it is less suitable for targeted material development. Thus, an overpotential-specific and temporally resolved electrochemical characterization protocol is proposed. In this the ohmic overpotential is determined with high frequency resistance measurements. These are also used in combination with polarization curves to distinguish between the kinetic and mass transport overpotentials and to determine kinetic key parameters, according to the Butler-Volmer and transition state theory. Complementary electrochemical impedance spectroscopy measurements further unravel the individual resistances. On this basis, the following statements can already be issued. The major share of the measured cell voltage increase, i.e. degradation, is of apparent nature as it is recovered once lower potentials are applied. It is suggested that this is due to changes in the oxidation states of the iridium-based catalyst. Real degradation occurs in the ohmic and mass transport overpotential mainly at higher current densities and longer operating times. The increasing kinetic overpotential with increasing operating time is primarily potential-driven. Interestingly, both the Tafel slope and the apparent exchange current density slightly increase over time. © 2019 The Author(s). Published by ECS. eng
dc.language.iso eng
dc.publisher Bristol : IOP Publishing Ltd.
dc.relation.ispartofseries Journal of the Electrochemical Society 166 (2019), Nr. 10
dc.rights CC BY 4.0 Unported
dc.rights.uri https://creativecommons.org/licenses/by/4.0/
dc.subject Cells eng
dc.subject Cytology eng
dc.subject Electrochemical impedance spectroscopy eng
dc.subject Electrolysis eng
dc.subject Electrolytic cells eng
dc.subject Kinetics eng
dc.subject Electrochemical characterizations eng
dc.subject Electrochemical impedance spectroscopy measurements eng
dc.subject Exchange current densities eng
dc.subject High frequency resistance eng
dc.subject Material development eng
dc.subject Proton exchange membranes eng
dc.subject Proton-exchange membrane eng
dc.subject Transition state theories eng
dc.subject Proton exchange membrane fuel cells (PEMFC) eng
dc.subject.ddc 540 | Chemie ger
dc.subject.ddc 660 | Technische Chemie ger
dc.subject.ddc 620 | Ingenieurwissenschaften und Maschinenbau ger
dc.title Degradation of proton exchange membrane (PEM) water electrolysis cells: Looking beyond the cell voltage increase
dc.type Article
dc.type Text
dc.relation.issn 0013-4651
dc.relation.doi https://doi.org/10.1149/2.1451910jes
dc.bibliographicCitation.issue 10
dc.bibliographicCitation.volume 166
dc.bibliographicCitation.firstPage F645
dc.bibliographicCitation.lastPage F652
dc.description.version publishedVersion
tib.accessRights frei zug�nglich


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