Catalyst for purifying motor vehicle exhaust gases and process for producing the catalyst

Claim 2

A catalyst for purifying exhaust gases essentially comprising a substantially catalytically inert, refractory monolithic support, an inside layer containing a catalytically active refractory oxide formed on the support, and an outside layer containing a catalytically active refractory oxide formed on the inside layer, characterized in that the support has continuous longitudinal unobstructed flow channels each extending through the support and defined by a thin wall, the inside layer is deposited on the walls of the channels, contains cerium oxide and platinum and has a weight of 10 to 200 g per liter of the catalyst, the outside layer is deposited on the inside layer, contains a zirconium compound and rhodium and has a weight of 5 to 60 g per liter of the catalyst, and the catalytically active refractory oxide is finely divided and has a specific surface area of at least about 10 m 2 /g.

Claim 3

The catalyst set forth in claim 1 wherein the inside layer has a thickness of 5 to 110 microns, and the outside layer has a thickness of 3 to 35 microns.

Claim 4

The catalyst set forth in claim 1 or 2 wherein the catalytically active refractory oxide is active alumina.

Claim 5

The catalyst set forth in any one of claims 1 to 3 wherein the support is composed of cordierite.

Claim 6

The catalyst set forth in any one of claims 1 to 3 wherein the support is composed of refractory metal.

Claim 7

The catalyst set forth in any one of claims 1 to 5 wherein the weight of cerium oxide is 15 to 40% by weight based on the weight of the inside layer.

Claim 8

The catalyst set forth in any one of claims 1 to 6 wherein the weight of platinum is 0.01 to 10 g per liter of the catalyst.

Claim 9

The catalyst set forth in any one of claims 1 to 7 wherein the zirconium compound is zirconium oxide.

Claim 10

The catalyst set forth in any one of claims 1 to 8 wherein the weight of the zirconium compound is 10 to 30% by weight based on the weight of the outside layer.

Claim 11

The catalyst set forth in any one of claims 1 to 9 wherein the weight of rhodium is 0.002 to 2 g per liter of the catalyst.

Claim 12

A process for producing a catalyst for purifying exhaust gases essentially comprising a substantially catalytically inert, refractory monolithic support, an inside layer containing a catalytically active refractory oxide formed on the support, and an outside layer containing a catalytically active refractory oxide formed on the inside layer, wherein the support has a continuous longitudinal unobstructed flow channels each extending through the support and defined by a thin wall, the inside layer is deposited on the walls of the channels, contains cerium oxide and platinum and has a weight of 10 to 200 g per liter of the catalyst, the outside layer is deposited on the inside layer, contains a zirconium compound and rhodium and has a weight of 5 to 60 g per liter of the catalyst, and the catalytically active refractory oxide is finely divided and has a specific surface area of at least about 10 m 2 /g; which comprises depositing a slurry containing a finely divided catalytically active refractory oxide and/or its precursor, cerium oxide or another cerium compound, and platinum or a platinum compound on a substantially catalytically inert refractory monolithic support, thereafter depositing a slurry containing a finely divided catalytically active refractory oxide and/or or its precursor, zirconium oxide or another zirconium compound and rhodium or a rhodium compound on the support, and calcining the support having the slurries deposited thereon.

Claim 13

A process for producing a catalyst for purifying exhaust gases essentially comprising a substantially catalytically inert, refractory monolithic support, an inside layer containing a catalytically active refractory oxide formed on the support, and an outside layer containing a catalytically active refractory oxide formed on the inside layer, wherein the support has a continuous longitudinal unobstructed flow channels each extending through the support and defined by a thin wall, the inside layer is deposited on the walls of the channels, contains cerium oxide and platinum and has a weight of 10 to 200 g per liter of the catalyst, the outside layer is deposited on the inside layer, contains a zirconium compound and rhodium and has a weight of 5 to 60 g per liter of the catalyst, and the catalytically active refractory oxide is finely divided and has a specific surface area of at least about 10 m 2 /g; which comprises depositing a slurry containing a finely divided catalytically active refractory oxide and/or its precursor, cerium oxide or another cerium compound, and platinum or a platinum compound on a substantially catalytically inert refractory monolithic support, thereafter depositing a slurry containing a finely divided catalytically active refractory oxide and/or or its precursor, zirconium oxide or another zirconium compound and rhodium or a rhodium compound on the support, and calcining the support having the slurries deposited thereon.

Claim 14

The process set forth in claim 11 wherein the inside layer has a thickness of 5 to 110 microns, and the outside layer has a thickness of 3 to 35 microns.

Claim 15

The process set forth in claim 11 or 12 wherein the catalytically active refractory oxide is active alumina.

Claim 16

The process set forth in any one of claims 11 to 13 wherein the support is composed of cordierite.

Claim 17

The process of any one of claims 11 to 13 wherein the support is composed of refractory metal.

Claim 18

The process set forth in any one of claims 11 to wherein the weight of cerium oxide is 15 to 40% by weight . based on the weight of the inside layer.

Claim 19

The process set forth in any one of claims 11 to 16 wherein the weight of platinum is 0.01 to 10 g per liter of the catalyst.

Claim 20

The process set forth in any one of claims 11 to 17 wherein the zirconium compound is zirconium oxide.

Claim 21

The process set forth in any one of claims 11 to 18 wherein the weight of the zirconium compound is 10 to 30% by weight based on the weight of the outside layer.

Claim 22

The process set forth in any one of claims 11 to 19 wherein the weight of rhodium is 0.002 to 2 g per liter of the catalyst.

Claim 23

The process set forth in any one of claims 11 to 20 wherein the platinum compound in the slurry is hexahydroxoplatinic acid.

Claim 24

The process set forth in any one of claims 11 to 21 wherein the rhodium compound in the slurry is rhodium nitrate.

Claim 25

The process set forth in any one of claims 11 to 22 wherein the zirconium compound in the slurry is zirconyl acetate.