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<dc:dc xmlns:dc="http://purl.org/dc/elements/1.1/" xmlns:invenio="http://invenio-software.org/elements/1.0" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xsi:schemaLocation="http://www.openarchives.org/OAI/2.0/oai_dc/ http://www.openarchives.org/OAI/2.0/oai_dc.xsd"><dc:identifier>doi:10.3390/catal15040348</dc:identifier><dc:language>eng</dc:language><dc:creator>Maldonado-Martín, Francisco</dc:creator><dc:creator>García, Lucía</dc:creator><dc:creator>Ruiz, Joaquín</dc:creator><dc:creator>Oliva, Miriam</dc:creator><dc:creator>Arauzo, Jesús</dc:creator><dc:title>Selective Conversion of Glycerol to Acetol: Effect of the Preparation Method of CuAl Catalysts and Reaction Phase</dc:title><dc:identifier>ART-2025-144134</dc:identifier><dc:description>A group of CuAl catalysts were synthesized with a Cu/Al molar ratio of 1:1 using different preparation methods: coprecipitation, surfactant assisted coprecipitation, polymeric precursor, and self-combustion and then screened for the selective dehydration of glycerol to acetol. The catalysts were employed in glycerol conversion at the same temperature (227 °C) in two different laboratory-scale systems, the first one at atmospheric pressure (gas phase) and the second one in a pressurized system at 34 absolute bar (liquid phase). The preparation method of the CuAl catalysts influenced the carbon yield to liquids and acetol selectivity. However, the reaction phase had a greater influence than the preparation method of the catalyst. In the gas phase, the carbon yield to liquids reached values above 40% and the carbon selectivity to acetol was higher than 90%. The highest acetol yield, 462.6 mgacetol/gglycerol, was obtained with the CuAl catalyst prepared by the surfactant-assisted coprecipitation method. This study provides a new perspective on catalyst design by highlighting the crucial role of preparation techniques in determining CuAl catalyst performance in the liquid and gas phases.</dc:description><dc:date>2025</dc:date><dc:source>http://zaguan.unizar.es/record/160886</dc:source><dc:doi>10.3390/catal15040348</dc:doi><dc:identifier>http://zaguan.unizar.es/record/160886</dc:identifier><dc:identifier>oai:zaguan.unizar.es:160886</dc:identifier><dc:relation>info:eu-repo/grantAgreement/ES/DGA/T22-23R</dc:relation><dc:relation>info:eu-repo/grantAgreement/ES/MCINN/PID2020-114985RB-I00</dc:relation><dc:relation>info:eu-repo/grantAgreement/ES/MICINN PRE2021-100578</dc:relation><dc:identifier.citation>Catalysts 15, 4 (2025), 348 [31 pp.]</dc:identifier.citation><dc:rights>by</dc:rights><dc:rights>https://creativecommons.org/licenses/by/4.0/deed.es</dc:rights><dc:rights>info:eu-repo/semantics/openAccess</dc:rights></dc:dc>

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