2008
DOI: 10.1016/j.apcatb.2007.07.032
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Chemical deactivation of V2O5/WO3–TiO2 SCR catalysts by additives and impurities from fuels, lubrication oils and urea solution

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Cited by 247 publications
(105 citation statements)
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“…ZnCl 2 , or molten K Zn double salts). The surface area with (65 m 2 /g at 400 °C degassing temperature) and the pore structure of the fresh catalyst are in agreement similar catalysts [28]. The total pore volume and the micropore volume, 0.271 and 0.0028 cm 3 /g are also in agreement with similar catalysts.…”
Section: Discussionsupporting
confidence: 73%
“…ZnCl 2 , or molten K Zn double salts). The surface area with (65 m 2 /g at 400 °C degassing temperature) and the pore structure of the fresh catalyst are in agreement similar catalysts [28]. The total pore volume and the micropore volume, 0.271 and 0.0028 cm 3 /g are also in agreement with similar catalysts.…”
Section: Discussionsupporting
confidence: 73%
“…Unfortunately, in practice, many kinds of toxic components such as alkali metal, CaO, As 2 O 3 and SO 2 under complex flue gas conditions often result in the deactivation and lifetime reduction of catalysts, thus its replacement cycle in practical application is shortened dramatically [3][4][5]. Since direct landfill not only endangers environment, brings hazard (V, As, Hg, etc.)…”
Section: Introductionmentioning
confidence: 99%
“…severest poisoning effect on the vanadia-based catalysts [15]. Several authors [4,7,8,15,16] concluded that potassium compounds strongly interacted with the dispersed vanadia species and neutralized the Brønsted acid sites, leading to a decrease of adsorption sites for ammonia, which played a crucial role in the NH 3 -SCR mechanism. Potassium doping would result in severe deactivation.…”
mentioning
confidence: 98%