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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/catal9050411</dc:identifier><dc:language>eng</dc:language><dc:creator>Charisiou, Nikolaos D.</dc:creator><dc:creator>Siakavelas, Georgios I.</dc:creator><dc:creator>Dou, Binlin</dc:creator><dc:creator>Sebastian, Víctor</dc:creator><dc:creator>Hinder, Steven J.</dc:creator><dc:creator>Baker, Mark A.</dc:creator><dc:creator>Polychronopoulou, Kyriaki</dc:creator><dc:creator>Goula, Maria A.</dc:creator><dc:title>Nickel supported on AlCeO3 as a highly selective and stable catalyst for hydrogen production via the glycerol steam reforming reaction</dc:title><dc:identifier>ART-2019-115095</dc:identifier><dc:description>In this study, a critical comparison between two low metal (Ni) loading catalysts is presented, namely Ni/Al2O3 and Ni/AlCeO3 for the glycerol steam reforming (GSR) reaction. The surface and bulk properties of the catalysts were evaluated using a plethora of techniques, such as N2 adsorption/desorption, Inductively Coupled Plasma Atomic Emission Spectroscopy (ICP-AES), X-ray Diffraction (XRD), X-ray Photoelectron Spectroscopy (XPS), Scanning Electron Microscopy / Energy Dispersive X-Ray Spectroscopy (SEM/EDX, Transmission Electron Microscopy (TEM), CO2 and NH3-Temperature Programmed Desorption (TPD), and Temperature Programmed Reduction (H2-TPR). Carbon deposited on the catalyst’s surfaces was probed using Temperature Programmed Oxidation (TPO), SEM, and TEM. It is demonstrated that Ce-modification of Al2O3 induces an increase of the surface basicity and Ni dispersion. These features lead to a higher conversion of glycerol to gaseous products (60% to 80%), particularly H2 and CO2, enhancement of WGS reaction, and a higher resistance to coke deposition. Allyl alcohol was found to be the main liquid product for the Ni/AlCeO3 catalyst, the production of which ceases over 700 °C. It is also highly significant that the Ni/AlCeO3 catalyst demonstrated stable values for H2 yield (2.9-2.3) and selectivity (89-81%), in addition to CO2 (75-67%) and CO (23-29%) selectivity during a (20 h) long time-on-stream study. Following the reaction, SEM/EDX and TEM analysis showed heavy coke deposition over the Ni/Al2O3 catalyst, whereas for the Ni/AlCeO3 catalyst TPO studies showed the formation of more defective coke, the latter being more easily oxidized.</dc:description><dc:date>2019</dc:date><dc:source>http://zaguan.unizar.es/record/86404</dc:source><dc:doi>10.3390/catal9050411</dc:doi><dc:identifier>http://zaguan.unizar.es/record/86404</dc:identifier><dc:identifier>oai:zaguan.unizar.es:86404</dc:identifier><dc:identifier.citation>CATALYSTS 9, 5 (2019), 411  [21 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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