Catalyst blends
US-2015375215-A1 · Dec 31, 2015 · US
US9868115B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9868115-B2 |
| Application number | US-201514676207-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 1, 2015 |
| Priority date | Oct 6, 2011 |
| Publication date | Jan 16, 2018 |
| Grant date | Jan 16, 2018 |
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The invention provides an exhaust gas cleaning oxidation catalyst and in particular to an oxidation catalyst for cleaning the exhaust gas discharged from internal combustion engines of compression ignition type (particularly diesel engines). The invention further relates to a catalysed substrate monolith comprising an oxidising catalyst on a substrate monolith for use in treating exhaust gas emitted from a lean-burn internal combustion engine. In particular, the invention relates to a catalysed substrate monolith comprising a first washcoat coating and a second washcoat coating, wherein the second washcoat coating is disposed in a layer above the first washcoat coating.
Opening claim text (preview).
The invention claimed is: 1. An oxidation catalyst for the oxidative treatment of a hydrocarbon (HC) and carbon monoxide (CO) in an exhaust gas, which is a catalysed substrate monolith, the oxidation catalyst comprising a supporting substrate and a plurality of catalyst layers supported on the supporting substrate, wherein the plurality of catalyst layers comprise a washcoat material, an active metal and a hydrocarbon adsorbent, and wherein one catalyst layer lies on the catalyst surface layer side and is a first washcoat coating, and one or more other catalyst layers lie on the side lower than the one catalyst layer, wherein one of the one or more other catalyst layers is a second washcoat coating; and wherein: (a) the amount of hydrocarbon adsorbent in the one catalyst layer is greater than the amount of hydrocarbon adsorbent in the one or more other catalyst layers, and the concentration of active metal in the one catalyst layer is the same as or less than the concentration of active metal in the one or more other catalyst layers; or (b) the amount of hydrocarbon adsorbent in the one catalyst layer is the same as the amount of hydrocarbon adsorbent in the one or more other catalyst layers, and the concentration of active metal in the one catalyst layer is less than the concentration of active metal in the one or more other catalyst layers; and wherein a Pt:Pd weight ratio of both the first washcoat coating and the second washcoat coating combined is ≧1:1, and wherein the supporting substrate is a substrate monolith. 2. An oxidation catalyst according to claim 1 , which consists of two catalyst layers. 3. An oxidation catalyst according to claim 1 , wherein the hydrocarbon adsorbent is a zeolite. 4. An oxidation catalyst according to claim 1 , wherein the one catalyst layer has a concentration of hydrocarbon adsorbent of 0.05 to 3.00 gin −3 . 5. An oxidation catalyst according to claim 1 , wherein the ratio by amount of hydrocarbon adsorbent in the one catalyst layer to the one or more other catalyst layers is 10:1 to 1.1:1. 6. An oxidation catalyst according to claim 1 , wherein there is no hydrocarbon adsorbent in the one or more other catalyst layers. 7. An oxidation catalyst according to claim 1 , wherein the one catalyst layer has a concentration of hydrocarbon adsorbent of 10 to 50% by weight of the layer. 8. An oxidation catalyst according to claim 1 , wherein the active metal is platinum, palladium or a mixture thereof. 9. An oxidation catalyst according to claim 1 , wherein the one or more other catalyst layers have a concentration of active metal of 0.05 to 3.5 gin −3 . 10. An oxidation catalyst according to claim 1 , wherein the ratio by concentration of active metal in the one catalyst layer to the one or more other catalyst layers is 1:50 to 1:1.1. 11. An oxidation catalyst according to claim 1 , wherein the one catalyst layer has a concentration of active metal of 0.01 to 5% by weight. 12. An oxidation catalyst according to claim 1 , wherein the substrate monolith is a flow-through substrate monolith. 13. An oxidation catalyst according to claim 1 , wherein the second washcoat coating comprises both platinum and palladium and wherein the first washcoat coating comprises both platinum and palladium at a higher Pt:Pd weight ratio than in the second washcoat coating. 14. An oxidation catalyst according to claim 1 , wherein a Pt:Pd weight ratio of both the first washcoat coating and the second washcoat coating combined is ≦10:1. 15. An oxidation catalyst according to claim 1 , wherein the first washcoat coating comprises 25-75% by weight of a total platinum group metal present in the first washcoat coating and the second washcoat coating combined. 16. An oxidation catalyst according to claim 1 , wherein at least one of the first washcoat coating and the second washcoat coating comprises a molecular sieve at ≦30% by weight of the individual washcoat coating layer. 17. An oxidation catalyst according to claim 1 , wherein the oxidation catalyst is a diesel oxidation catalyst or a NO x adsorber catalyst. 18. An oxidation catalyst according to claim 1 , wherein each active metal is (i) a base metal selected from nickel, copper, manganese, iron, cobalt and zinc, or (ii) a platinum group metal selected from platinum, palladium and a mixture thereof. 19. An oxidation catalyst according to claim 1 , wherein the washcoat material is a support material for the active metal. 20. An oxidation catalyst according to claim 19 , wherein the support material comprises SiO 2 , Al 2 O 3 , CeO 2 or TiO 2 as its main constituent. 21. An exhaust system for a lean-burn internal combustion engine, which system comprises an oxidation catalyst according to claim 1 .
Iron · CPC title
Beta zeolites · CPC title
CHA-type, e.g. Chabazite, LZ-218 · CPC title
Noble metals · CPC title
characterised by structure, by material or by manufacturing of catalyst support · CPC title
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