Coking resistant Ni/ZrO2@SiO2 catalyst for the partial oxidation of methane to synthesis gas. (8th June 2015)

• Record Type: Journal Article
• Authors: Ding, Chuanmin; Ai, Ganggang; Zhang, Kan; Yuan, Qinbo; Han, Yulin; Ma, Xishun; Wang, Junwen; Liu, Shibin
• Is Part Of: International journal of hydrogen energy. Volume 40:Number 21(2015)
• Page Start: 6835
• Page End: 6843
• Publication Date: 2015-06-08
• Subjects: Hydrogen as fuel -- Periodicals; Hydrogène (Combustible) -- Périodiques; Hydrogen as fuel; Periodicals; 665.81
• DOI: 10.1016/j.ijhydene.2015.03.094
• Languages: English
• ISSNs: 0360-3199

Abstract

<abstract xml:lang="en" abstract-type="author" id="abs0010"> <title id="sectitle0010">Abstract</title> <sec> <p id="abspara0010">Carbon deposition, which may reduce the number of active sites or remove metal particles from the catalyst surface, is an urgent issue for the partial oxidation of methane (POM) to synthesis gas. To solve this problem, Ni/ZrO₂@SiO₂ catalysts were prepared by a modified Stöber method. The investigation was focused mainly on the role of ZrO₂ addition and mesopore silica shell in preventing carbon deposition. The structural properties and carbon deposition of catalysts were characterized by XRD, TEM, N₂ adsorption and TG techniques. The oxygen transfer capacity and reducibility of catalysts were evaluated by oxygen storage capacity (OSC) and temperature programmed reduction (TPR). Inspiringly, the Ni/ZrO₂@SiO₂ catalyst was proved to be more active and possessed less carbon deposition due to the higher reducibility and oxygen storage/release capacity. Importantly, compared with the support catalysts, the catalysts coated by mesopore silica shell showed exceptional resistance to coking, because the edge and corner atoms favor to carbon deposition were selectively blocked by silica shell, in addition, the size of the pore channel prevented growth up of carbon filament.</p> </sec> </abstract>