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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:10.1007/s13399-023-04937-9</dc:identifier><dc:language>eng</dc:language><dc:creator>Afailal, Zainab</dc:creator><dc:creator>Gil-Lalaguna, Noemí</dc:creator><dc:creator>Høj, Martin</dc:creator><dc:creator>Cornejo, Alfonso</dc:creator><dc:creator>Sánchez, José Luis</dc:creator><dc:creator>Jensen, Anker Degn</dc:creator><dc:title>Production of phenolic compounds from argan shell waste by reductive catalytic fractionation</dc:title><dc:identifier>ART-2023-135091</dc:identifier><dc:description>For efficient utilization of lignocellulosic biomass components, reductive catalytic fractionation appears as a promising biorefinery strategy. In this work, this concept of biomass valorization was used to study the potential of an unexplored feedstock, argan shells. This material was processed in a non-catalytic route and over a Pd/C catalyst in two different reaction media. The effects of the treatment temperature (250, 275, and 300 °C), as well as the catalyst loading (catalyst/argan shells mass ratio of 0.05 and 0.1 g/g), were also studied. The main product (lignin-derived oil) was thoroughly characterized using GC/MS/FID, SEC, and NMR. The highest monomer yields of 48–49 wt% based on the lignin content were obtained for n-butanol/water reaction medium at 300 °C using a Pd/C catalyst load of 0.1 g/g and for methanol reaction medium at 275 °C and 0.05 g/g. Significantly lower monomeric phenol yields were obtained in the non-catalytic route (4–19 wt% for n-butanol/water and 9–16 wt% for methanol). The main phenolic monomers in the catalytic pathway were 4-n-propanolguaiacol, 4-n-propanolsyringol, and 4-alkyl guaiacols and syringols, with some differences in the selectivities from one solvent to another.</dc:description><dc:date>2023</dc:date><dc:source>http://zaguan.unizar.es/record/127929</dc:source><dc:doi>10.1007/s13399-023-04937-9</dc:doi><dc:identifier>http://zaguan.unizar.es/record/127929</dc:identifier><dc:identifier>oai:zaguan.unizar.es:127929</dc:identifier><dc:relation>info:eu-repo/grantAgreement/ES/AEI/PID2020-114936RB-I00</dc:relation><dc:relation>info:eu-repo/grantAgreement/ES/DGA-FEDER/T22-23R</dc:relation><dc:identifier.citation>Biomass Conversion and Biorefinery (2023), [20 pp.]</dc:identifier.citation><dc:rights>by</dc:rights><dc:rights>http://creativecommons.org/licenses/by/3.0/es/</dc:rights><dc:rights>info:eu-repo/semantics/openAccess</dc:rights></dc:dc>

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