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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:10.1016/j.biombioe.2025.108273</dc:identifier><dc:language>eng</dc:language><dc:creator>Lete, Alejandro</dc:creator><dc:creator>García, Lucía</dc:creator><dc:creator>Ruiz, Joaquín</dc:creator><dc:creator>Arauzo, Jesús</dc:creator><dc:title>Valorization of pure and biodiesel-derived refined crude glycerol to renewable acetol over copper-based catalyst: Effect of operating conditions and catalyst stability</dc:title><dc:identifier>ART-2025-145809</dc:identifier><dc:description>Acetol is a key intermediate in the aldol condensation of biomass-derived furans, enabling the production of carbon chains within the aviation fuel range. This work proposes glycerol, a biomass-derived by-product from biodiesel production, as a renewable feedstock for acetol production. The catalytic performance of a CuAl catalyst was evaluated in the gas phase dehydration of glycerol, focusing on the influence of temperature (200–300 °C), catalyst weight to glycerol mass flow ratio (10–50 gCatalyst min gGlycerol−1), and carrier gas to liquid ratio (200–600 m3GasSTP m3Liquid−1). Both pure and biodiesel-derived refined crude glycerol were used as feedstock. Long-term stability experiments assessed the evolution of catalytic activity and physicochemical properties over time. A great activity was obtained under conditions of 250 °C, 30 gCatalyst min gGlycerol−1, and 400 m3GasSTP m3Liquid−1 with pure glycerol after a time-on-stream (TOS) of 2 h (95.1 % glycerol conversion and 564 mgAcetol gGlycerol−1). Stability studies provided good catalytic results after a TOS of 52 h using pure glycerol (72 % glycerol conversion and 266 mgAcetol gGlycerol−1) and demonstrated that coke deposition was responsible for catalyst deactivation. The use of refined crude glycerol proved to be highly effective in the first hours of the reaction (98.7 % glycerol conversion and 570 mgAcetol gGlycerol−1 for a TOS of 2 h), however, rapid deactivation was observed due to solids deposition. This catalytic route highlights the feasibility of valorization of biomass residues for producing renewable acetol, a promising precursor for sustainable aviation fuel (SAF).</dc:description><dc:date>2025</dc:date><dc:source>http://zaguan.unizar.es/record/163709</dc:source><dc:doi>10.1016/j.biombioe.2025.108273</dc:doi><dc:identifier>http://zaguan.unizar.es/record/163709</dc:identifier><dc:identifier>oai:zaguan.unizar.es:163709</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:identifier.citation>BIOMASS &amp; BIOENERGY 203 (2025), 108273 [15 pp.]</dc:identifier.citation><dc:rights>by-nc-nd</dc:rights><dc:rights>https://creativecommons.org/licenses/by-nc-nd/4.0/deed.es</dc:rights><dc:rights>info:eu-repo/semantics/openAccess</dc:rights></dc:dc>

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