2012
DOI: 10.1016/j.cattod.2011.10.035
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Improved high temperature stability of NH3-SCR catalysts based on rare earth vanadates supported on TiO2WO3SiO2

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Cited by 72 publications
(34 citation statements)
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“…[3][4][5][6] Although this catalyst system has been utilized for several decades in industry, some disadvantages still exist such as a narrow operation temperature window, low N 2 selectivity and poor stability at high temperatures, and, more importantly, the biological toxicity of the active V 2 O 5 phase, restricting its further application especially for the NO x reduction process for mobile sources such as diesel engines. [3,7,8] Therefore, more and more researchers now devote themselves to the development of new, highly efficient and environmentally friendly NH 3 -SCR catalysts with improved low-temperature deNO x efficiency, hydrothermal stability or resistance to co-existing pollutants, including zeolite catalysts promoted by metal cations (e.g., Fe-ZSM-5, Fe-BEA, Cu-ZSM-5, Cu-beta, Cu-CHA) [9][10][11][12][13][14][15][16][17][18][19][20] and single metal oxide, supported type, or mixed oxide catalysts (e.g., g-Fe 2 O 3 nanorods, Fe 2 O 3 / WO 3 /ZrO 2 , Ti 0.9 Fe 0.1 O 2Àd , Ce-P-O, CeTiO x , CeWO x , MnO x , (Fe 3Àx Mn x ) 1Àd O 4 ). [21][22][23][24][25][26][27][28][29] In our previous study, we reported a novel, environmentally benign iron titanate (FeTiO x ) catalyst for NH 3 -SCR of NO x prepared by a facile coprecipitation method, achieving high deNO x efficiency, N 2 selectivity, and H 2 O/SO 2 durability in the medium temperature range.…”
Section: Introductionmentioning
confidence: 98%
“…[3][4][5][6] Although this catalyst system has been utilized for several decades in industry, some disadvantages still exist such as a narrow operation temperature window, low N 2 selectivity and poor stability at high temperatures, and, more importantly, the biological toxicity of the active V 2 O 5 phase, restricting its further application especially for the NO x reduction process for mobile sources such as diesel engines. [3,7,8] Therefore, more and more researchers now devote themselves to the development of new, highly efficient and environmentally friendly NH 3 -SCR catalysts with improved low-temperature deNO x efficiency, hydrothermal stability or resistance to co-existing pollutants, including zeolite catalysts promoted by metal cations (e.g., Fe-ZSM-5, Fe-BEA, Cu-ZSM-5, Cu-beta, Cu-CHA) [9][10][11][12][13][14][15][16][17][18][19][20] and single metal oxide, supported type, or mixed oxide catalysts (e.g., g-Fe 2 O 3 nanorods, Fe 2 O 3 / WO 3 /ZrO 2 , Ti 0.9 Fe 0.1 O 2Àd , Ce-P-O, CeTiO x , CeWO x , MnO x , (Fe 3Àx Mn x ) 1Àd O 4 ). [21][22][23][24][25][26][27][28][29] In our previous study, we reported a novel, environmentally benign iron titanate (FeTiO x ) catalyst for NH 3 -SCR of NO x prepared by a facile coprecipitation method, achieving high deNO x efficiency, N 2 selectivity, and H 2 O/SO 2 durability in the medium temperature range.…”
Section: Introductionmentioning
confidence: 98%
“…The vanadium-based catalysts have also been successfully used in the deNO x process for heavy duty diesel engines in 2005 using urea as an efficient reductant [3]. However, although it has been utilized industrially for several decades, some disadvantages still remain for this catalyst system, such as a narrow operation temperature window, low N 2 selectivity, and sublimation of V 2 O 5 at high reaction temperatures [1,4,5], which greatly restrict its further application in the deNO x process for mobile sources. Accordingly, the in-depth study and improvement of vanadium-based catalysts for the NH 3 -SCR process is still of great concern in the field of environmental catalysis [5][6][7][8][9][10][11][12][13].…”
Section: Introductionmentioning
confidence: 99%
“…For this purpose, an active SCR catalyst formulation has been loaded over supports showing different soot oxidation functionalities. SCR catalyst materials were selected among metal/rare earth vanadates that have been shown to act as efficient catalyst precursors for NH 3 -SCR reaction [11][12][13][14][15][16], while among the different supports, standard TiO 2 -WO 3 -SiO 2 (TWS) was used and compared with more efficient carbon oxidation carriers like CeO 2 and Ce 0.75 Zr 0.25 O 2 [17]. In particular, this work investigates FeVO 4 and Fe 0.5 Er 0.5 VO 4 supported on TWS, CeO 2 , Ce 0.75 Zr 0.25 O 2 (CeZrO 2 ), and Al 2 O 3 in the simultaneous soot oxidation and NH 3 -SCR reactions.…”
Section: Introductionmentioning
confidence: 99%