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Homogeneous and highly dispersed Ni–Ru on a silica support as an effective CO methanation catalyst

The highly dispersed SiO(2)-supported nickel-based catalysts for CO methanation were prepared by an ethylene glycol (EG) modified wet-impregnation method. The results indicate that the highly dispersed 20Ni/SiO(2) (EG) catalyst realized good stability and higher catalytic activity than the catalyst...

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Detalles Bibliográficos
Autores principales: Liu, Yi, Sheng, Wei, Hou, Zhanggui, Zhang, Yi
Formato: Online Artículo Texto
Lenguaje:English
Publicado: The Royal Society of Chemistry 2018
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9077448/
https://www.ncbi.nlm.nih.gov/pubmed/35542588
http://dx.doi.org/10.1039/c7ra13147j
Descripción
Sumario:The highly dispersed SiO(2)-supported nickel-based catalysts for CO methanation were prepared by an ethylene glycol (EG) modified wet-impregnation method. The results indicate that the highly dispersed 20Ni/SiO(2) (EG) catalyst realized good stability and higher catalytic activity than the catalyst obtained from a non-pretreated silica support (20Ni/SiO(2)) in CO methanation, due to the smaller nickel particles and strong nickel–silica interaction. By the addition of a small amount of noble metal promoter (Ru, Pt, Pd), the catalytic activity for CO methanation was further improved dramatically and follows the order Ru > Pt > Pd. The added noble metal promoter enhanced the reduction of the nickel oxide by spill-over-hydrogen during reduction treatment, and provided more active species for the methanation reaction, resulting in 7 times higher CO conversion than the non-pretreated 20Ni/SiO(2) catalyst. The 20Ni–0.5Ru/SiO(2) (EG) catalyst presents superb catalytic performance in CO methanation with high activity (CO conv. 80.2%) as well as high methane selectivity (90.3%) at 275 °C without any deactivation during 50 h reaction. The obtained catalysts were characterized by XRD, TG/DTA, TEM, XPS, TPR, H(2) chemisorption, and in situ DRIFTS.