2012
DOI: 10.1039/c2cy20140b
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Catalytic performance and hydrothermal durability of CeO2–V2O5–ZrO2/WO3–TiO2 based NH3-SCR catalysts

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Cited by 67 publications
(32 citation statements)
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“…However, the reaction activity of adsorbed NH 3 and nitrate species over CeNb 3.0 Zr 2 O x was higher than that over CeZr 2 O x , and both of them could participate in the NH 3 -SCR reaction according to the in-situ DRIFTS results. It was likely to conclude that the adsorbed NH 3 species could react with adsorbed nitrate to form N 2 and The hydrothermal stability of NH 3 -SCR catalysts is required in the long deNO x for practical applications, as the diesel engine exhaust temperature can reach as high as 700 • C during the regeneration process of DPF system [41]. Accordingly, the catalysts were hydrothermally aged at various temperatures for 8 h and the results are illustrated in Fig.…”
Section: Reactivity Of Adsorbed No X Speciesmentioning
confidence: 99%
“…However, the reaction activity of adsorbed NH 3 and nitrate species over CeNb 3.0 Zr 2 O x was higher than that over CeZr 2 O x , and both of them could participate in the NH 3 -SCR reaction according to the in-situ DRIFTS results. It was likely to conclude that the adsorbed NH 3 species could react with adsorbed nitrate to form N 2 and The hydrothermal stability of NH 3 -SCR catalysts is required in the long deNO x for practical applications, as the diesel engine exhaust temperature can reach as high as 700 • C during the regeneration process of DPF system [41]. Accordingly, the catalysts were hydrothermally aged at various temperatures for 8 h and the results are illustrated in Fig.…”
Section: Reactivity Of Adsorbed No X Speciesmentioning
confidence: 99%
“…In contrast, the thermal stabilities of the oxide catalysts with CeO2-ZrO2 as the support or Ce as the main active component are generally lower than those of zeolite catalysts. This is especially true of the recently developed Cu-based small-pore zeolite catalysts [13,48]. In addition, although the combination of CeO2 and WO3 has been shown to be very effective for the NH3-SCR reaction and can form the basis for high efficiency catalysts, the high cost of WO3 implies that there is a need for reducing or eliminating WO3 in such systems.…”
Section: Perspectivesmentioning
confidence: 99%
“…Moreover, the Ce additive on V2O5-WO3/TiO2 could provide stronger and more active Brönsted acid sites, which were beneficial for the SCR reaction. Ceria-modified V2O5-ZrO2/WO3-TiO2 catalyst was also evaluated for the NH3-SCR of NOx in diesel engines [13]. Compared with the V2O5/WO3-TiO2 catalysts having only Zr addition, the co-addition of Ce greatly enhanced the low-temperature activity of the catalyst, but the material obviously deactivated with age.…”
Section: Ceria As An Nh3-scr Catalyst Promotermentioning
confidence: 99%
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“…9,10 The V 2 O 5 -WO 3 (MoO 3 )/TiO 2 catalyst is a commonly used commercial SCR catalyst for NO x removal with an active temperature range of 300-400 °C. 11,12 However, this catalyst has many disadvantages including the toxicity of vanadium at high temperatures.13 Therefore, significant efforts should be devoted towards the development of non-vanadium catalysts for NH 3 -SCR processes. Mn-based catalysts have been studied due to their inherent environmentfriendly characteristics and excellent SCR activity at low temperatures.…”
mentioning
confidence: 99%