2006
DOI: 10.1016/j.cattod.2006.01.035
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Outstanding low temperature HC-SCR of NOx over platinum-group catalysts supported on mesoporous materials expecting diesel-auto emission regulation

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Cited by 29 publications
(16 citation statements)
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“…The present zeolites are not solid bases, such as BaO usually used as LNT-agents, therefore, the materials have no problems such as deactivation with several ppm SOx (SOx poisoning or stoichiometric sufation). Zeolites, such as HZSM-5 and MCM-41, produce low-temperature activities in the catalyst, as previously reported (Komatsu et al, 2006). These results strongly suggest that the support effect is due to the incorporated metals.…”
Section: The Support Effect On Nox-conversion Vs Temperature Profilesupporting
confidence: 85%
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“…The present zeolites are not solid bases, such as BaO usually used as LNT-agents, therefore, the materials have no problems such as deactivation with several ppm SOx (SOx poisoning or stoichiometric sufation). Zeolites, such as HZSM-5 and MCM-41, produce low-temperature activities in the catalyst, as previously reported (Komatsu et al, 2006). These results strongly suggest that the support effect is due to the incorporated metals.…”
Section: The Support Effect On Nox-conversion Vs Temperature Profilesupporting
confidence: 85%
“…The silica/metal atom ratio was adjusted to 20/1. The experimental details were described in the previous report (Komatsu et al, 2006). The Pt-catalyst supported on MPS (Pt/MPS) and on the silicates (Pt/metal-silicate) were prepared by impregnating each support-material with an aqueous solution of H 2 PtCl 4 and RhCl 3 ·3H 2 O, evaporated to dryness at 110 , followed by reduction with hydrogen at 300 for 1 h. The precious metal loading of the Pt-catalysts was adjusted at a 5 mass % Pt-0.3 mass % Rh.…”
Section: Sample Preparationmentioning
confidence: 99%
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“…This research is focused on HC-SCR which could eliminate the need for a secondary fuel tank [8]- [12] and the use of expensive platinum group metal (pgm) loadings. A hydrocarbon (HC) containing reactant is injected into the exhaust gas upstream the HC-SCR catalyst and those hydrocarbons then react with the NOx on the catalyst's active sites to reduce the NOx levels downstream the catalysis.…”
Section: Introductionmentioning
confidence: 99%
“…Figure 6a, b shows the NO x conversion and N 2 selectivity, respectively, of the 0.2 wt% Pd/(60+20)−20 and 0.05 wt% Pd/(60+20)−20 catalysts tested before and after aging. The aging procedure simulated at least 80,000 km of on-road usage [44]. The maximum NO x conversion of 0.05 wt% Pd/ (60+20)−20 shifted to higher temperature and decreased from approximately 90 % at 200°C to circa 51 % at 310°C after aging.…”
Section: Aged Catalystsmentioning
confidence: 99%