Metal phosphide catalysts for the hydrotreatment of non-edible vegetable oils

[EN] Silica-supported catalysts of nickel, cobalt, iron, molybdenum, and tungsten metal phosphides (NiP/SiO, CoP/SiO, FeP/SiO, MoP/SiO, and WP/SiO) with a metal-loading of 15 wt%, were synthesized by reduction of the corresponding phosphite precursors. The catalysts were characterized by N adsorptio...

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Detalles Bibliográficos
Autores: Álvarez Galván, María Consuelo, Blanco Brieva, Gema, Capel Sánchez, María del Carmen, Morales-delaRosa, Silvia, Campos Martín, José Miguel, García Fierro, José Luis
Tipo de recurso: artículo
Estado:Versión aceptada para publicación
Fecha de publicación:2018
País:España
Institución:Consejo Superior de Investigaciones Científicas (CSIC)
Repositorio:DIGITAL.CSIC. Repositorio Institucional del CSIC
OAI Identifier:oai:digital.csic.es:10261/202744
Acceso en línea:http://hdl.handle.net/10261/202744
Access Level:acceso abierto
Palabra clave:Green Diesel
Hydrogenation
Vegetable oil
Metal phosphides
hydrotreatment
Descripción
Sumario:[EN] Silica-supported catalysts of nickel, cobalt, iron, molybdenum, and tungsten metal phosphides (NiP/SiO, CoP/SiO, FeP/SiO, MoP/SiO, and WP/SiO) with a metal-loading of 15 wt%, were synthesized by reduction of the corresponding phosphite precursors. The catalysts were characterized by N adsorption–desorption, X-ray diffraction (XRD), CO pulse chemisorption, NH temperature programmed desorption (NH-TPD), and X-ray photoelectron spectroscopy (XPS). The activity of these catalysts was measured at 573 K, a liquid flow of 0.3 mL min, a pressure of 2.0 MPa and a H/liquid ratio of 300 in a three-phase, trickle-bed reactor in the hydrotreatment of methyl laurate. The MoP/SiO catalyst was found to exhibit the best catalytic performance based on its higher active phase dispersion as measured by XRD, CO chemisorption and XPS analyses, along with its moderate acidity, which is higher with respect to the other studied catalysts. The reaction conditions using the MoP/SiO catalyst, the most active and selective to C and C hydrocarbons, were optimized. Optimal results can be obtained under the following conditions: 573 K, 2.0 MPa, and a liquid flow of 0.3 mL min. Moreover, long-run experiments showed that the MoP/SiO catalyst exhibits stable catalytic behavior for at least 96 h.