催化作用
臭氧
化学
氧化剂
分解
镍
无机化学
一氧化碳
吸附
氧气
催化氧化
氧化物
X射线光电子能谱
化学工程
有机化学
工程类
作者
M. Stoyanova,P. Konova,P. Nikolov,A. Naydenov,St. Christoskova,D. Mehandjiev
标识
DOI:10.1016/j.cej.2006.05.018
摘要
An alumina-supported nickel oxide system with overstoichiometric oxygen (NiOx/Al2O3) was investigated with respect to heterogeneous catalytic decomposition of ozone, complete oxidation of volatile organic compounds (VOCs) and oxidation of CO. The catalyst was prepared by a deposition oxidation–precipitation method and was characterized by chemical analysis, XPS, XRD, IR techniques, magnetic and adsorption measurements. The experiments were performed in the temperature range of −50 to 250 °C in an isothermal plug-flow reactor. A very high activity of the catalyst towards ozone decomposition was observed even at temperatures below −45 °C and at the same time the catalyst remained active for a long time. The activity of the catalyst with respect to complete oxidation of VOCs and oxidation of carbon monoxide was studied in presence of different oxidizing agents (ozone or oxygen). A significant increase in catalytic activity and decrease in reaction temperature were observed using ozone as an oxidant. Two main reasons for this behaviour were found: (i) the high content of active and mobile oxygen obtained during the synthesis on the catalyst surface, and (ii) the catalytically active complex of Ni4+O(OH)2, formed during the reaction of ozone decomposition and able to oxidize VOCs at room temperature.
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