Indicadores de Prod. Científica
Publicaciones Científicas
Patentes
Gaceta Electrónica de I+D
Ayuda
Descripción de Contenidos
Uso de la Página
Sugerencias y Propuestas
Convocatorias y
Documentos
Convocatorias y Ayudas de I+D
Documentos e Informes
Normativa
Recursos Investigación
Centros de Investigación
Grupos de Investigación
Investigadores
Equipamientos de I+D
Comités Eticos
Actividad Investigadora
Proyectos de Investigación
Ensayos Clínicos
Indicadores
Nuevos Proyectos
Resultados Investigación
Indicadores Prod. Científica
Publicaciones Científicas
Patentes
Gaceta Electrónica de I+D
Formación
Apoyo Metodológico
Oferta Formativa
Bibliografía Seleccionada
Recursos Metodológicos
Recursos Bibliográficos
Otros Recursos
Museo de la Sanidad
Enlaces de Interés
Ofertas de Trabajo
y Colaboración
Noticias
Eventos
Catalytic and kinetic analysis of the methane tri-reforming over a Ni-Mg/beta-SiC catalyst

Titulo

Catalytic and kinetic analysis of the methane tri-reforming over a Ni-Mg/beta-SiC catalyst 

Revista

INT J HYDROGEN ENERG 

Año

2015 

Volumen

40 

Página Inicial

8677 

Página Final

8687 

Autores

Garcia-Vargas, JM; Valverde, JL; Diez, J; Dorado, F; Sanchez, P

Centros Participantes

[Manuel Garcia-Vargas, Jesus; Luis Valverde, Jose; Diez, Javier; Dorado, Fernando; Sanchez, Paula] Univ Castilla La Mancha, Fac Ciencias Quim, Dept Ingn Quim, Ciudad Real 13005, Spain

Resumen

In this work, the influence of the temperature and feed composition on the catalytic behaviour of a Ni-Mg/beta-SiC catalyst in the methane tri-reforming was analysed and modelized. This catalyst was characterized by Atomic Absorption Spectrophotometry (AAS), Temperature Programmed Reduction (TPR), N-2 adsorption, Temperature Programmed Desortion of CO2 (TPD) and X-Ray Diffraction (XRD). 36 catalytic experiments at different temperatures and feed compositions were performed, modifying the quantity of CH4, CO2, H2O and O-2 present in the feed. The predominance of each one of the reactions that took place during the tri-reforming process was evaluated as a function of the temperature, finding at low temperatures a higher contribution of both the steam reforming and the water gas shift reactions. On the contrary, at higher temperatures, a higher contribution of the dry reforming was detected. Finally, a kinetic model was raised and experimental data were fitted to it. Steam reforming, dry reforming and water gas shift reactions were considered as the kinetically relevant equations. A good agreement between experimental and predicted data was observed. Copyright (C) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
Datos adjuntos
Tipo de contenido: PublicacionesCientificas
Creado el 11/05/2017 13:41  por Cuenta del sistema 
Última modificación realizada el 11/05/2017 13:41  por Cuenta del sistema