催化作用
分解
化学
吸附
氧气
无机化学
降水
化学工程
有机化学
物理
气象学
工程类
作者
Tianqi Zhao,Yulin Li,Qiang Gao,Zhiying Liu,Xiufeng Xu
标识
DOI:10.1016/j.catcom.2020.105948
摘要
A Y2O3-Co3O4 catalyst was prepared by an innovative co-precipitation method at the solution boiling temperature, and tested for the N2O decomposition reaction. The catalyst exhibited a higher catalytic activity than that prepared by the common co-precipitation method at 90 °C. In addition, the catalytic performance of the Y2O3-Co3O4 catalyst was further enhanced by K-promoter, which might be related to the weakening of CoO bond and higher concentration of adsorbed oxygen (Oα) on the catalyst surface. Even under the co-presence of oxygen and steam in the feed stream, the K/Y2O3-Co3O4 catalyst showed good catalytic stability and maintained 100% conversion of N2O after a continuous reaction at 400 °C for 30 h.
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