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Single-step hydrogen production from NH3, CH4, and biogas in stacked proton ceramic reactors

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Single-step hydrogen production from NH3, CH4, and biogas in stacked proton ceramic reactors

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dc.contributor.author Clark, Daniel es_ES
dc.contributor.author Malerod-Fjeld, Harald es_ES
dc.contributor.author Budd, Michael es_ES
dc.contributor.author Yuste-Tirados, Irene es_ES
dc.contributor.author Beeaff, Dustin es_ES
dc.contributor.author Aamodt, Simen es_ES
dc.contributor.author Nguyen, Kevin es_ES
dc.contributor.author Ansaloni, Luca es_ES
dc.contributor.author Peters, Thijs es_ES
dc.contributor.author Vestre, Per K. es_ES
dc.contributor.author Pappas, Dimitrios K. es_ES
dc.contributor.author Valls-Esteve, María Inmaculada es_ES
dc.contributor.author Remiro-Buenamañana, Sonia es_ES
dc.contributor.author Norby, Truls es_ES
dc.contributor.author Bjorheim, Tor S. es_ES
dc.contributor.author Serra Alfaro, José Manuel es_ES
dc.contributor.author Kjolseth, Christian es_ES
dc.date.accessioned 2023-11-15T19:01:31Z
dc.date.available 2023-11-15T19:01:31Z
dc.date.issued 2022-04-22 es_ES
dc.identifier.issn 0036-8075 es_ES
dc.identifier.uri http://hdl.handle.net/10251/199843
dc.description.abstract [EN] Proton ceramic reactors offer efficient extraction of hydrogen from ammonia, methane, and biogas by coupling endothermic reforming reactions with heat from electrochemical gas separation and compression. Preserving this efficiency in scale-up from cell to stack level poses challenges to the distribution of heat and gas flows and electric current throughout a robust functional design. Here, we demonstrate a 36-cell well-balanced reactor stack enabled by a new interconnect that achieves complete conversion of methane with more than 99% recovery to pressurized hydrogen, leaving a concentrated stream of carbon dioxide. Comparable cell performance was also achieved with ammonia, and the operation was confirmed at pressures exceeding 140 bars. The stacking of proton ceramic reactors into practical thermo-electrochemical devices demonstrates their potential in efficient hydrogen production. es_ES
dc.description.sponsorship This work was supported by Norway's Ministry of Petroleum and Energy through the Gassnova project CLIMIT grant 618191 in partnership with Engie SA, Equinor, ExxonMobil, Saudi Aramco, Shell, and TotalEnergies and the Research Council of Norway NANO2021 project DynaPro grant 296548. es_ES
dc.language Inglés es_ES
dc.publisher American Association for the Advancement of Science (AAAS) es_ES
dc.relation.ispartof Science es_ES
dc.rights Reserva de todos los derechos es_ES
dc.title Single-step hydrogen production from NH3, CH4, and biogas in stacked proton ceramic reactors es_ES
dc.type Artículo es_ES
dc.identifier.doi 10.1126/science.abj3951 es_ES
dc.relation.projectID info:eu-repo/grantAgreement/RCN//296548//DynaPro/ es_ES
dc.relation.projectID info:eu-repo/grantAgreement/Gassnova//618191//CLIMIT/ 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 Clark, D.; Malerod-Fjeld, H.; Budd, M.; Yuste-Tirados, I.; Beeaff, D.; Aamodt, S.; Nguyen, K.... (2022). Single-step hydrogen production from NH3, CH4, and biogas in stacked proton ceramic reactors. Science. 376(6591):390-393. https://doi.org/10.1126/science.abj3951 es_ES
dc.description.accrualMethod S es_ES
dc.relation.publisherversion https://doi.org/10.1126/science.abj3951 es_ES
dc.description.upvformatpinicio 390 es_ES
dc.description.upvformatpfin 393 es_ES
dc.type.version info:eu-repo/semantics/publishedVersion es_ES
dc.description.volume 376 es_ES
dc.description.issue 6591 es_ES
dc.identifier.pmid 35446633 es_ES
dc.relation.pasarela S\488151 es_ES
dc.contributor.funder Gassnova es_ES
dc.contributor.funder Saudi Aramco es_ES
dc.contributor.funder Research Council of Norway es_ES
dc.contributor.funder Ministry of Petroleum and Energy, Norway es_ES


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