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      <dc:title>Coupling of glycerol-APR and in situ hydrodeoxygenation of fatty acid to produce hydrocarbons</dc:title>
      <dc:creator>Domínguez-Barroso, María Vanesa</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>Hidrocarburos</dc:subject>
      <dc:description>Glycerol valorization by coupling APR to yield hydrogen with hydrogenation of a model compound as tandem reactions is approached using Pt-Ni/Al2O3 as efficient catalyst. Oleic acid is used as a C18 fatty acid model compound for in situ hydrogenation reaction. The combination of the two catalytic transformations to a single tandem process appears particularly interesting since this protocol reduces the number of synthetic steps towards the target compound and avoids external hydrogen supply. Glycerol reforming is carried out in a catalytic fixed bed batch reactor under subcritical water condition between 175 and 275°C (2–6.21MPa as autogenous pressure). The coupled reactions were carried out using 1wt %of catalyst, adding oleic acid to the mixture of water/glycerol and without any external hydrogen supply. In APR, maximum glycerol conversion of 80.3% was achieved using Pt-Ni/Al2O3 catalyst at 200°C with H2-selectivity close to 80% and CO formation below to 3.7%. In the coupled reactions, no hydrogen is observed in the gas-off, which is associated to the hydrogen consumption by oleic acid at 275°C; reaching a hydrogenation conversion value close to 91.3% and deoxygenation conversion of 32% giving a C17 paraffinic like-hydrocarbon.</dc:description>
      <dc:date>2025-01-20T12:47:00Z</dc:date>
      <dc:date>2025-01-20T12:47:00Z</dc:date>
      <dc:date>2019-07-22</dc:date>
      <dc:type>journal article</dc:type>
      <dc:identifier>Vanesa Domínguez-Barroso, Concepción Herrera, María Ángeles Larrubia, Luis J. Alemany, Coupling of glycerol-APR and in situ hydrodeoxygenation of fatty acid to produce hydrocarbons, Fuel Processing Technology, Volume 190, 2019, Pages 21-28, ISSN 0378-3820, https://doi.org/10.1016/j.fuproc.2019.03.011. (https://www.sciencedirect.com/science/article/pii/S037838201832280X)</dc:identifier>
      <dc:identifier>https://hdl.handle.net/10630/36577</dc:identifier>
      <dc:identifier>10.1016/j.fuproc.2019.03.011</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>Elsevier</dc:publisher>
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