2014
DOI: 10.1016/j.apcatb.2014.04.037
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New insights into sulfur poisoning on a vanadia SCR catalyst under simulated diesel engine operating conditions

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Cited by 78 publications
(41 citation statements)
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“…1 Recently, developing low-temperature SCR systems is signicant, because ue gas becomes much cleaner aer passing through desulfurized and particulate control devices, which could protect catalysts from being deactivated by high concentrations of ash and SO 2 in the ue gas, thereby prolonging the catalyst lifespan. 6 Therefore, investigating the key factor in the NH 4 HSO 4 decomposition and reactivity behaviors on the catalysts constitutes the vital step in industrializing lowtemperature SCR systems. [2][3][4][5] However, certain amount of SO 2 and H 2 O in the ue gas leads to the deposition of NH 4 HSO 4 on the catalysts, which adversely affects the SCR reaction; formation of that product is the main barrier to the commercialization of low-temperature SCR systems.…”
Section: Introductionmentioning
confidence: 99%
“…1 Recently, developing low-temperature SCR systems is signicant, because ue gas becomes much cleaner aer passing through desulfurized and particulate control devices, which could protect catalysts from being deactivated by high concentrations of ash and SO 2 in the ue gas, thereby prolonging the catalyst lifespan. 6 Therefore, investigating the key factor in the NH 4 HSO 4 decomposition and reactivity behaviors on the catalysts constitutes the vital step in industrializing lowtemperature SCR systems. [2][3][4][5] However, certain amount of SO 2 and H 2 O in the ue gas leads to the deposition of NH 4 HSO 4 on the catalysts, which adversely affects the SCR reaction; formation of that product is the main barrier to the commercialization of low-temperature SCR systems.…”
Section: Introductionmentioning
confidence: 99%
“…For the V 2 O 5 -WO 3 /TiO 2 catalyst, anatase TiO 2 acts as a carrier, V 2 O 5 is the active component, and WO 3 performs as the promoter to stabilize the catalyst and prevents the catalyst from sintering. In coal-fired power plants, the SCR catalyst suffers from gradual deactivation during the operation period because of poisoning, sintering, fouling, surface masking, attrition/crushing, and loss of vanadium or change in ratio value of the vanadium in different valence states [3][4][5][6][7][8].…”
Section: Introductionmentioning
confidence: 99%
“…However, under continuous low temperature operation (T<400°C), significant catalyst deterioration can occur. Xi, et al, (42) quantified the formation of ammonia sulfate species on vanadia SCR catalysts. They and others (review in 43) found that if SCR catalysts are exposed to cold start conditions without going up to ammonia sulfate decomposition temperatures (∼350-400°C) the ammonia sulfates can build up and block catalyst activity.…”
Section: Scrmentioning
confidence: 99%