Method for the preparation of a catalysed particulate filter and catalysed particulate filter
US-9073047-B2 · Jul 7, 2015 · US
US9339844B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9339844-B2 |
| Application number | US-201113881787-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 1, 2011 |
| Priority date | Nov 2, 2010 |
| Publication date | May 17, 2016 |
| Grant date | May 17, 2016 |
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Method for the preparation of a catalysed particulate filter and a particulate filter prepared by the method.
Opening claim text (preview).
The invention claimed is: 1. Method for the preparation of a catalysed particulate filter comprising the steps of: a) providing a porous filter body having a dispersion side and a permeation side; b) providing a catalyst washcoat containing particles of a first catalyst composition being active in selective catalytic reduction of nitrogen oxides together with particles of second catalyst composition being active in oxidation of carbon monoxide and hydrocarbons and ammonia and particles of a third catalyst composition being active in selective oxidation of ammonia to nitrogen in combination with the second catalyst composition, wherein the particles of the first catalyst composition have a mode particle size less than mean pore size of the particulate filter, and wherein the particles of the second and third catalyst composition have a mode particle size larger than mean pore size of the particulate filter; c) coating the filter body with the catalyst washcoat by introduction of the washcoat into outlet end of the permeation side; and d) drying and heat treating the coated filter body to obtain the catalysed particulate filter, wherein the first catalyst composition comprises at least one of an iron and/or copper promoted zeolite, a silica aluminum phosphate, an ion exchanged zeolite or a silica aluminum phosphate, one or more base metal oxides and a catalyst support of at least one of cerium oxide mixed with tungsten oxide on a titania support, an alumina support, a zirconia support or a silica support and mixtures thereof. 2. The method of claim 1 , wherein the zeolite is beta zeolite or a chabazite zeolite. 3. The method of claim 1 , wherein the silica alumina phosphate with chabazite structure is SAPO 34 catalyst promoted with copper. 4. The method of claim 1 , wherein the second catalyst composition comprises a mixture of platinum and palladium supported on at least one of alumina, titania, ceria, silica and zirconia support. 5. The method of claim 1 , wherein the third catalyst composition comprises a copper and/or iron promoted zeolite or a copper and/or iron promoted silica alumina phosphate with chabazite structure. 6. The method of claim 5 , wherein the zeolite is a beta zeolite or zeolite with chabazite structure. 7. The method according to claim 1 , wherein the filter is in form of a wall flow monolith with a plurality of longitudinal passages divided by longitudinal porous walls, dispersion side of the passages having an open inlet end and plugged outlet end, and permeation side of the passages having a plugged inlet end and an open outlet end. 8. The method according to claim 1 , wherein the washcoat is introduced from the outlet end of the permeation side. 9. The method according to claim 1 , wherein the washcoat is applied prior to plugging the inlet end of the permeation side.
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