1998
DOI: 10.1016/s0926-3373(97)00089-1
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Deactivation by SO2 of MnOx/Al2O3 catalysts used for the selective catalytic reduction of NO with NH3 at low temperatures

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Cited by 244 publications
(26 citation statements)
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“…The conversion of NO was stable for 300 min at 433 K in the absence of SO 2 gas, as we reported previously [14]. In the presence of SO 2 at 433 K, the conversion of NO decreased with the reaction time, which indicates that the SO 2 poisoned the catalyst, as in the case of the Mn-based catalysts [9]. The reaction temperature had a significant effect on the deactivation rate of the TiO 2 photocatalyst.…”
Section: Resultssupporting
confidence: 77%
See 1 more Smart Citation
“…The conversion of NO was stable for 300 min at 433 K in the absence of SO 2 gas, as we reported previously [14]. In the presence of SO 2 at 433 K, the conversion of NO decreased with the reaction time, which indicates that the SO 2 poisoned the catalyst, as in the case of the Mn-based catalysts [9]. The reaction temperature had a significant effect on the deactivation rate of the TiO 2 photocatalyst.…”
Section: Resultssupporting
confidence: 77%
“…The problem with Mn-based catalysts is low resistance to SO 2 poisoning. Kijlstra et al [9] proposed that the formation of MnSO 4 is the main reason for the deactivation of MnO x /Al 2 O 3 catalysts. The formed sulfates decomposed at 1020 K, which means regeneration of the catalysts is only possible at much higher temperatures than the reaction temperature.…”
Section: Introductionmentioning
confidence: 99%
“…This suggests that NO or SO 2 molecules and Hg 0 vapor could be competitively adsorbed on the surface of 12Co 3 O 4 /CNNS [9]. In addition, the adsorbed SO 2 may react with Co 3 O 4 to produce thermally-stable metal sulfates, i.e., cobalt sulfate, leading to the decline of the active phases [42]. Thus, the competitive adsorption and side reactions contribute to the remarkable suppressive influences of NO and SO 2 towards Hg 0 adsorption.…”
Section: Impact Of Flue Gasmentioning
confidence: 99%
“…At coal-fired power stations, V2O5-WO3/TiO2 is the most commonly used SCR catalyst. However, the high operating temperature window of 300 -400°C is associated with a variety of problems [6,7], such as the possible oxidation of SO2 and the high energy consumption [8,9]. Therefore, there is a need for the development of low temperature SCR catalysts, which has attracted a wide attention in recent years [10,11].…”
Section: Introductionmentioning
confidence: 99%