2011
DOI: 10.1016/j.micromeso.2010.02.005
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Effect of hydrocarbon slip on NO removal activity of CuZSM5, FeZSM5 and V2O5/TiO2 catalysts by NH3

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Cited by 54 publications
(94 citation statements)
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“…Recalculation, taking into account the lower space velocity of 100 000 h -1 , of the data of Heo et al [24], gives values of 2.45 for a 2.2 % vanadia on titania catalyst at 375 °C and 2.37 at 500°C. Our catalyst A has about 2 times higher activity.…”
Section: Discussionmentioning
confidence: 95%
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“…Recalculation, taking into account the lower space velocity of 100 000 h -1 , of the data of Heo et al [24], gives values of 2.45 for a 2.2 % vanadia on titania catalyst at 375 °C and 2.37 at 500°C. Our catalyst A has about 2 times higher activity.…”
Section: Discussionmentioning
confidence: 95%
“…Activation energies were 38.6, 13.2 and 33.4 kJ/mol out of which at least the value for catalyst E is in the diffusion regime. Calculation of data given by Heo et al [24] gives rate constants in the region of 1.94 for 375 °C and 2.93 at 500…”
Section: Discussionmentioning
confidence: 99%
“…Unburned hydrocarbons are always present in real exhaust gas. Zeolite SCR catalyst can be deactivated by hydrocarbons as a result of active site poisoning and pore blockage [35][36][37][38][39]. Pore blockage is known to mainly take place on acid sites [35][36][37][38][39].…”
Section: Discussionmentioning
confidence: 99%
“…Thus, it is very important to understand how the HCs inhibit the activity of Fe-zeolite catalysts for the NH 3 -SCR reaction [53,[60][61][62][63]. The HC poisoning of Fe-based zeolite catalysts is closely related to the dimensional structure of the zeolite supports.…”
Section: Effects Of H 2 O So 2 and Hydrocarbons (Hc) On The Nh 3 -Scmentioning
confidence: 99%
“…The HC poisoning of Fe-based zeolite catalysts is closely related to the dimensional structure of the zeolite supports. For example, on Fe-ZSM-5 and Fe-BEA catalysts with three-dimensional structure, after HC poisoning the NH 3 -SCR activity was obviously decreased, especially at low temperatures, mainly due to carbonaceous deposition resulting in the decline of surface area and pore volume together with suppressed NO oxidation ability for blocked Fe 3+ sites, or the partial reduction of Fe 3+ species to Fe 2+ species by HC, or the competitive adsorption of HC with NH 3 / NO onto the catalyst surface [53,60,61]. The deactivation effect of HC on NH 3 -SCR activity was less on Fe-MOR catalysts with one-dimensional structure due to the difficulty in HC diffusion into the structure, and using this feature Ma et al [62] effectively improved the HC resistance of a modified Fe-BEA monolith catalyst by coating another layer of MOR zeolite on the outer surface.…”
Section: Effects Of H 2 O So 2 and Hydrocarbons (Hc) On The Nh 3 -Scmentioning
confidence: 99%