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In Situ DRIFTS Studies of NH(3)-SCR Mechanism over V(2)O(5)-CeO(2)/TiO(2)-ZrO(2) Catalysts for Selective Catalytic Reduction of NO(x)

TiO(2)-ZrO(2) (Ti-Zr) carrier was prepared by a co-precipitation method and 1 wt. % V(2)O(5) and 0.2 CeO(2) (the Mole ratio of Ce to Ti-Zr) was impregnated to obtain the V(2)O(5)-CeO(2)/TiO(2)-ZrO(2) catalyst for the selective catalytic reduction of NO(x) by NH(3). The transient activity tests and t...

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Autores principales: Zhang, Yaping, Yue, Xiupeng, Huang, Tianjiao, Shen, Kai, Lu, Bin
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2018
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6117643/
https://www.ncbi.nlm.nih.gov/pubmed/30060572
http://dx.doi.org/10.3390/ma11081307
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author Zhang, Yaping
Yue, Xiupeng
Huang, Tianjiao
Shen, Kai
Lu, Bin
author_facet Zhang, Yaping
Yue, Xiupeng
Huang, Tianjiao
Shen, Kai
Lu, Bin
author_sort Zhang, Yaping
collection PubMed
description TiO(2)-ZrO(2) (Ti-Zr) carrier was prepared by a co-precipitation method and 1 wt. % V(2)O(5) and 0.2 CeO(2) (the Mole ratio of Ce to Ti-Zr) was impregnated to obtain the V(2)O(5)-CeO(2)/TiO(2)-ZrO(2) catalyst for the selective catalytic reduction of NO(x) by NH(3). The transient activity tests and the in situ DRIFTS (diffuse reflectance infrared Fourier transform spectroscopy) analyses were employed to explore the NH(3)-SCR (selective catalytic reduction) mechanism systematically, and by designing various conditions of single or mixing feeding gas and pre-treatment ways, a possible pathway of NO(x) reduction was proposed. It was found that NH(3) exhibited a competitive advantage over NO in its adsorption on the catalyst surface, and could form an active intermediate substance of -NH(2). More acid sites and intermediate reaction species (-NH(2)), at lower temperatures, significantly promoted the SCR activity of the V(2)O(5)-0.2CeO(2)/TiO(2)-ZrO(2) catalyst. The presence of O(2) could promote the conversion of NO to NO(2), while NO(2) was easier to reduce. The co-existence of NH(3) and O(2) resulted in the NH(3) adsorption strength being lower, as compared to tests without O(2), since O(2) could occupy a part of the active site. Due to CeO(2’)s excellent oxygen storage-release capacity, NH(3) adsorption was weakened, in comparison to the 1 wt. % V(2)O(5)-0.2CeO(2)/TiO(2)-ZrO(2) catalyst. If NO(x) were to be pre-adsorbed in the catalyst, the formation of nitrate and nitro species would be difficult to desorb, which would greatly hinder the SCR reaction. All the findings concluded that NH(3)-SCR worked mainly through the Eley-Rideal (E-R) mechanism.
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spelling pubmed-61176432018-09-05 In Situ DRIFTS Studies of NH(3)-SCR Mechanism over V(2)O(5)-CeO(2)/TiO(2)-ZrO(2) Catalysts for Selective Catalytic Reduction of NO(x) Zhang, Yaping Yue, Xiupeng Huang, Tianjiao Shen, Kai Lu, Bin Materials (Basel) Article TiO(2)-ZrO(2) (Ti-Zr) carrier was prepared by a co-precipitation method and 1 wt. % V(2)O(5) and 0.2 CeO(2) (the Mole ratio of Ce to Ti-Zr) was impregnated to obtain the V(2)O(5)-CeO(2)/TiO(2)-ZrO(2) catalyst for the selective catalytic reduction of NO(x) by NH(3). The transient activity tests and the in situ DRIFTS (diffuse reflectance infrared Fourier transform spectroscopy) analyses were employed to explore the NH(3)-SCR (selective catalytic reduction) mechanism systematically, and by designing various conditions of single or mixing feeding gas and pre-treatment ways, a possible pathway of NO(x) reduction was proposed. It was found that NH(3) exhibited a competitive advantage over NO in its adsorption on the catalyst surface, and could form an active intermediate substance of -NH(2). More acid sites and intermediate reaction species (-NH(2)), at lower temperatures, significantly promoted the SCR activity of the V(2)O(5)-0.2CeO(2)/TiO(2)-ZrO(2) catalyst. The presence of O(2) could promote the conversion of NO to NO(2), while NO(2) was easier to reduce. The co-existence of NH(3) and O(2) resulted in the NH(3) adsorption strength being lower, as compared to tests without O(2), since O(2) could occupy a part of the active site. Due to CeO(2’)s excellent oxygen storage-release capacity, NH(3) adsorption was weakened, in comparison to the 1 wt. % V(2)O(5)-0.2CeO(2)/TiO(2)-ZrO(2) catalyst. If NO(x) were to be pre-adsorbed in the catalyst, the formation of nitrate and nitro species would be difficult to desorb, which would greatly hinder the SCR reaction. All the findings concluded that NH(3)-SCR worked mainly through the Eley-Rideal (E-R) mechanism. MDPI 2018-07-28 /pmc/articles/PMC6117643/ /pubmed/30060572 http://dx.doi.org/10.3390/ma11081307 Text en © 2018 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (http://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Zhang, Yaping
Yue, Xiupeng
Huang, Tianjiao
Shen, Kai
Lu, Bin
In Situ DRIFTS Studies of NH(3)-SCR Mechanism over V(2)O(5)-CeO(2)/TiO(2)-ZrO(2) Catalysts for Selective Catalytic Reduction of NO(x)
title In Situ DRIFTS Studies of NH(3)-SCR Mechanism over V(2)O(5)-CeO(2)/TiO(2)-ZrO(2) Catalysts for Selective Catalytic Reduction of NO(x)
title_full In Situ DRIFTS Studies of NH(3)-SCR Mechanism over V(2)O(5)-CeO(2)/TiO(2)-ZrO(2) Catalysts for Selective Catalytic Reduction of NO(x)
title_fullStr In Situ DRIFTS Studies of NH(3)-SCR Mechanism over V(2)O(5)-CeO(2)/TiO(2)-ZrO(2) Catalysts for Selective Catalytic Reduction of NO(x)
title_full_unstemmed In Situ DRIFTS Studies of NH(3)-SCR Mechanism over V(2)O(5)-CeO(2)/TiO(2)-ZrO(2) Catalysts for Selective Catalytic Reduction of NO(x)
title_short In Situ DRIFTS Studies of NH(3)-SCR Mechanism over V(2)O(5)-CeO(2)/TiO(2)-ZrO(2) Catalysts for Selective Catalytic Reduction of NO(x)
title_sort in situ drifts studies of nh(3)-scr mechanism over v(2)o(5)-ceo(2)/tio(2)-zro(2) catalysts for selective catalytic reduction of no(x)
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6117643/
https://www.ncbi.nlm.nih.gov/pubmed/30060572
http://dx.doi.org/10.3390/ma11081307
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