<?xml version="1.0" encoding="UTF-8"?><?xml-stylesheet type="text/xsl" href="static/style.xsl"?><OAI-PMH xmlns="http://www.openarchives.org/OAI/2.0/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/ http://www.openarchives.org/OAI/2.0/OAI-PMH.xsd"><responseDate>2026-05-28T19:47:12Z</responseDate><request verb="GetRecord" identifier="oai:riuma.uma.es:10630/26489" metadataPrefix="rdf">https://riuma.uma.es/rest/oai/request</request><GetRecord><record><header><identifier>oai:riuma.uma.es:10630/26489</identifier><datestamp>2026-02-03T11:18:54Z</datestamp><setSpec>com_10630_2254</setSpec><setSpec>col_10630_37953</setSpec></header><metadata><rdf:RDF xmlns:dc="http://purl.org/dc/elements/1.1/" xmlns:doc="http://www.lyncode.com/xoai" xmlns:ds="http://dspace.org/ds/elements/1.1/" xmlns:ow="http://www.ontoweb.org/ontology/1#" xmlns:rdf="http://www.openarchives.org/OAI/2.0/rdf/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/rdf/ http://www.openarchives.org/OAI/2.0/rdf.xsd">
   <ow:Publication rdf:about="oai:riuma.uma.es:10630/26489">
      <dc:title>Bi-reforming of Biogas for Hydrogen Production with Sulfur-Resistant Multimetallic Catalyst</dc:title>
      <dc:creator>Poggio-Fraccari, Eduardo</dc:creator>
      <dc:creator>Mariño, Fernando</dc:creator>
      <dc:creator>Herrera-Delgado, María Concepción</dc:creator>
      <dc:creator>Larrubia-Vargas, María Ángeles</dc:creator>
      <dc:creator>Alemany-Arrebola, Luis José</dc:creator>
      <dc:subject>Biogas</dc:subject>
      <dc:subject>Hidrógeno -- Industria</dc:subject>
      <dc:description>A multimetallic sample, NiCeSnRh/Al2O3, was tested in methane reforming with a CH4:H2O:CO2 molar ratio equal to 3:2:1. A very stable methane conversion with the time-on-stream was achieved during 20 h. Dimethyl sulfide served as a model&#xd;
sulfur molecule and a sulfurized sample was also tested. This achieved slightly lower conversion with a stable performance for more than 10 h and a minor but continuous decrease of its activity, after this period. The carbon dioxide conversion was always higher than the methane conversion in agreement with the lower H2/CO ratio observed with respect to the theoretical value, 2/1, indicating the sulfur might block the active sites for H2O activation. The analysis of the used catalysts showed graphitic and disordered carbon deposits</dc:description>
      <dc:date>2023-05-05T11:37:49Z</dc:date>
      <dc:date>2023-05-05T11:37:49Z</dc:date>
      <dc:date>2023</dc:date>
      <dc:type>journal article</dc:type>
      <dc:identifier>Poggio-Fraccari, Mariño, F., Herrera, C., Larrubia-Vargas, M. Á., &amp; Alemany, L. (2023). Bi‐reforming of biogas for hydrogen production with sulfur‐resistant multi‐metallic catalyst. Chemical Engineering &amp; Technology. https://doi.org/10.1002/ceat.202200525</dc:identifier>
      <dc:identifier>https://hdl.handle.net/10630/26489</dc:identifier>
      <dc:identifier>https://doi.org/10.1002/ceat.202200525</dc:identifier>
      <dc:language>eng</dc:language>
      <dc:rights>http://creativecommons.org/licenses/by-nc-nd/4.0/</dc:rights>
      <dc:rights>open access</dc:rights>
      <dc:rights>Attribution-NonCommercial-NoDerivatives 4.0 Internacional</dc:rights>
      <dc:publisher>Wiley</dc:publisher>
   </ow:Publication>
</rdf:RDF>
</metadata></record></GetRecord></OAI-PMH>