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NO(x) reduction by CO over ASC catalysts in a simulated rotary reactor: effect of CO(2), H(2)O and SO(2)

The influence of CO(2), H(2)O and SO(2) on the NO reduction by CO over Fe/Co activated semi-coke catalyst was investigated in a simulated rotary reactor. The results showed that, in the simulated rotary reactor, the influence of CO(2) and H(2)O on the NO adsorption was significant at low temperature...

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Detalles Bibliográficos
Autores principales: Sun, Peiliang, Cheng, Xingxing, Lai, Yanhua, Wang, Zhiqiang, Ma, Chunyuan, Chang, Jingcai
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/PMC9088861/
https://www.ncbi.nlm.nih.gov/pubmed/35558965
http://dx.doi.org/10.1039/c8ra07658h
Descripción
Sumario:The influence of CO(2), H(2)O and SO(2) on the NO reduction by CO over Fe/Co activated semi-coke catalyst was investigated in a simulated rotary reactor. The results showed that, in the simulated rotary reactor, the influence of CO(2) and H(2)O on the NO adsorption was significant at low temperatures, and the inhibition became weak when increasing the temperature. However, the NO adsorption efficiency could not be improved by increasing temperature after catalyst sulfur poisoning. The heavily inhibited NO adsorption process, which was due to the competitive adsorption and formation of the sulfate, resulted in a low NO reduction efficiency in the presence of CO(2), H(2)O or SO(2). The in situ DRIFT study showed that the dominant effect of CO(2), H(2)O and SO(2) on the NO adsorption was the inhibition of the free nitrate ions formation. In addition, the introduction of CO(2), H(2)O and SO(2) could not change the route of NO reduction, but just reduced the degree of the NO + CO reduction.