Exhaust gas purification catalyst
US-2017298797-A1 · Oct 19, 2017 · US
US2022016601A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2022016601-A1 |
| Application number | US-201917295683-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 14, 2019 |
| Priority date | Nov 21, 2018 |
| Publication date | Jan 20, 2022 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
An exhaust-gas purification apparatus includes: a honeycomb base material including a plurality of exhaust-gas flow paths partitioned by a porous wall; and one or more catalyst noble metals carried by the honeycomb base material. The catalyst noble metals are selected from the group consisting of platinum, palladium, and rhodium. The honeycomb base material has a noble metal concentrated surface section in which a 50%-by-mass noble metal carry depth for a specific noble metal that is one type among one or two catalyst noble metals is less than 50% of the distance from the surface to the center of the inside of the porous wall. The 50%-by-mass noble metal carry depth is the depth at which, when the amount of the specific noble metal carried between the surface and the center of the inside of porous wall is used as a reference, 50% by mass of specific noble metal is carried.
Opening claim text (preview).
1 . An exhaust gas purification device comprising a honeycomb substrate having a plurality of exhaust gas flow paths separated by a porous wall, and one or more catalyst noble metals which are carried by the honeycomb substrate, wherein the honeycomb substrate includes ceria-zirconia composite oxide particles as a constituent material, the catalyst noble metals are selected from the group consisting of platinum, palladium, and rhodium, the honeycomb substrate has: a noble metal-enriched surface part in which a 50 mass % noble metal carrying depth of a specific noble metal, which is one of the one or more catalyst noble metals, is less than 50% of the distance from a surface of the porous wall to a center of an interior of the porous wall, and the 50 mass % noble metal carrying depth is a depth in which 50 mass % of the specific noble metal is carried based on a quantity of the specific noble metal carried from the surface of the porous wall to the center of the interior of the porous wall. 2 . The exhaust gas purification device according to claim 1 , wherein the specific noble metal is platinum or palladium. 3 . The exhaust gas purification device according to claim 2 , wherein the specific noble metal is platinum or palladium, and the catalyst noble metals include rhodium. 4 . The exhaust gas purification device according to claim 1 , wherein the honeycomb substrate is constituted by an inlet-side part which is 60% or less of a total length of the honeycomb substrate from an inlet side of the exhaust gas flow path, and a main part constituting the remainder of the honeycomb substrate, and the noble metal-enriched surface part is present at least in the main part. 5 . The exhaust gas purification device according to claim 4 , wherein a length of the inlet-side part constituting the honeycomb substrate is 10% or more of the total length of the honeycomb substrate. 6 . The exhaust gas purification device according to claim 1 , wherein the honeycomb substrate is constituted by an inlet-side part which is 30 mm or less from an inlet side of the exhaust gas flow path and a main part constituting the remainder of the honeycomb substrate, and the noble metal-enriched surface part is present at least in the main part. 7 . The exhaust gas purification device according to claim 6 , wherein a length of the inlet-side part constituting the honeycomb substrate is 10 mm or more. 8 . The exhaust gas purification device according to claim 4 , wherein a quantity of the specific noble metal carried by the inlet-side part of the honeycomb substrate is greater than a quantity of the specific noble metal carried by the main part. 9 . The exhaust gas purification device according to claim 4 , wherein in the inlet-side part of the honeycomb substrate, the 50 mass % noble metal carrying depth of the specific noble metal is greater than the 50 mass % noble metal carrying depth of the specific noble metal of the main part. 10 . The exhaust gas purification device according to claim 1 , wherein a porosity of the honeycomb substrate is 30% to 70%. 11 . The exhaust gas purification device according to claim 1 , wherein at least a part of the exhaust gas flow path does not have a catalyst layer. 12 . A method for the production of an exhaust gas purification device, comprising at least the following (a) to (c): (a) supplying a solution containing salts of one or more catalyst noble metals and a thickening agent from one open side of a honeycomb substrate having a plurality of exhaust gas flow paths separated by a porous wall, the solution having a viscosity of 10 to 400 mPa at a shear rate of 380 s −1 and the catalyst noble metals being selected from the group consisting of platinum, palladium, and rhodium; (b) suctioning the supplied solution from an opening side of the honeycomb substrate opposite the side to which the solution was supplied and/or pumping the supplied solution from the opening side of the honeycomb substrate to which the solution was supplied; and (c) drying and/or firing the honeycomb substrate. 13 . The method according to claim 12 , further comprising the following (d): (d) immersing the honeycomb substrate in a solution containing salts of the catalyst noble metals so that at least a part of an inlet-side part which is 30 mm or less of a total length from an inlet of the exhaust gas flow path of the honeycomb substrate is immersed, and subsequently drying and/or firing the honeycomb substrate, whereby a quantity of the catalyst noble metal carried by the inlet-side part is greater than a quantity of the catalyst noble metal carried by a main part excluding the inlet-side part. 14 . The exhaust gas purification device according to claim 2 , wherein the honeycomb substrate is constituted by an inlet-side part which is 60% or less of a total length of the honeycomb substrate from an inlet side of the exhaust gas flow path, and a main part constituting the remainder of the honeycomb substrate, and the noble metal-enriched surface part is present at least in the main part. 15 . The exhaust gas purification device according to claim 14 , wherein a length of the inlet-side part constituting the honeycomb substrate is 10% or more of the total length of the honeycomb substrate. 16 . The exhaust gas purification device according to claim 14 , wherein in the inlet-side part of the honeycomb substrate, the 50 mass % noble metal carrying depth of the specific noble metal is greater than the 50 mass % noble metal carrying depth of the specific noble metal of the main part. 17 . The exhaust gas purification device according to claim 3 , wherein the honeycomb substrate is constituted by an inlet-side part which is 60% or less of a total length of the honeycomb substrate from an inlet side of the exhaust gas flow path, and a main part constituting the remainder of the honeycomb substrate, and the noble metal-enriched surface part is present at least in the main part. 18 . The exhaust gas purification device according to claim 17 , wherein a length of the inlet-side part constituting the honeycomb substrate is 10% or more of the total length of the honeycomb substrate. 19 . The exhaust gas purification device according to claim 17 , wherein in the inlet-side part of the honeycomb substrate, the 50 mass % noble metal carrying depth of the specific noble metal is greater than the 50 mass % noble metal carrying depth of the specific noble metal of the main part.
Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional [3D] monoliths · CPC title
Two zones · CPC title
used in catalytic reactors · CPC title
Catalysts having a gradually changing coating · CPC title
Zr-Ce mixed oxides · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.