Hydrocarbon trap catalyst

Patent metadata

Field	Value
Publication number	US-10828623-B2
Application number	US-201815983246-A
Country	US
Kind code	B2
Filing date	May 18, 2018
Priority date	May 18, 2018
Publication date	Nov 10, 2020
Grant date	Nov 10, 2020

Abstract

The present invention relates to a catalyst comprising a carrier substrate of the length L extending between substrate ends a and b and two washcoat zones A and B, wherein washcoat zone A comprises a redox active base metal and palladium supported on a zeolite and/or refractory oxide support and extends starting from substrate end a over a part of the length L, and washcoat zone B comprises the same components as washcoat A and an additional amount of palladium and extends from substrate end b over a part of the length L, wherein L=L A +L B , wherein L A is the length of washcoat zone A and L B is the length of substrate length B.

First claim

The invention claimed is:

1. Catalyst comprising a carrier substrate of the length L extending between substrate ends a and b and two washcoat zones A and B, wherein washcoat zone A comprises a compound of a redox active base metal, selected from the group consisting of Cu, Ni, Co, Mn, Fe, Cr, Ce, Pr, Tb, Sn and In, and palladium, with one or both of the compound and palladium being supported on a zeolite and/or a support oxide, and wherein washcoat zone A extends, starting from substrate end a, over a part of the length L, and washcoat zone B comprises the same components as washcoat zone A and an additional amount of palladium and extends from substrate end b over a part of the length L, wherein L=L A +L B , wherein L A is the length of washcoat zone A and L B is the length of washcoat zone B.

2. Catalyst according to claim 1 , wherein
washcoat zone A comprises two layers A1 and A2, which both extend over the length L A ,
wherein layer A1 comprises zeolite, the compound of a redox active base metal selected from the group consisting of Cu, Ni, Co, Mn, Fe, Cr, Ce, Pr, Tb, Sn and In, and palladium, with the compound being supported on the zeolite, and layer A2 comprises rhodium, and
washcoat zone B comprises two layers B1 and B2, which both extend over the length L B ,
wherein layer B1 comprises the same components as layer A1 and layer B2 comprises the same components as layer A2 and
wherein layers B1 and B2 comprise an additional amount of palladium compared to layers A1 and A2.

3. Catalyst according to claim 1 , wherein the redox active base metal is copper, manganese or iron.

4. Catalyst according to claim 1 , wherein the redox active base metal is iron.

5. Catalyst according to claim 4 , wherein the iron compound is in washcoat zones A and B in an amount of 1.0 to 30 g/l, based on the volume of the carrier substrate zone and calculated as Fe 2 O 3 .

6. Catalyst according to claim 4 , wherein the zeolite is present and the iron compound and palladium in washcoat zone A are both supported on the zeolite.

7. Catalyst according to claim 6 , wherein the iron compound and palladium are present in cationic form within the zeolite structure or in oxidic and metallic form, respectively, within and/or on the surface of the zeolite.

8. Catalyst according to claim 1 , wherein the redox active base metal is present in cationic or in oxidic form.

9. Catalyst according to claim 1 , wherein the zeolite is present and the zeolite belongs to the structure type code BEA, FAU, FER, MFI or MOR.

10. Catalyst according to claim 1 , wherein the zeolite is present and the zeolite is beta zeolite.

11. Catalyst according to claim 1 , wherein the zeolite is present in washcoat zones A and B in an amount of 120 to 340 g/l based on the volume of the carrier substrate.

12. Catalyst according to claim 1 , wherein the support oxide is present and the support oxide is alumina, silica, magnesia, titania, ceria, zirconia or mixtures or mixed oxides comprising at least two of these materials.

13. Catalyst according to claim 1 , wherein palladium is present in cationic, metallic or oxidic form.

14. Catalyst according to claim 1 , wherein it comprises palladium is present in washcoat zone A in an amount of 0.04 to 4.0 g/l, based on the volume of the carrier substrate and calculated as palladium metal.

15. Catalyst according to claim 14 , wherein palladium is present in washcoat zone B in an amount of 2 to 20 g/l, based on the volume of the carrier substrate and calculated as palladium metal.

16. Catalyst according to claim 15 , wherein the compound is an iron compound that is in washcoat zones A and B in an amount of 1.0 to 30 g/l, based on the volume of the carrier substrate zone and calculated as Fe 2 O 3 , and wherein both the zeolite and the support oxide are present with each providing support to one or both of the iron compound and the palladium.

17. Catalyst according to claim 1 , wherein palladium is present in washcoat zone B in an amount of 2 to 20 g/l, based on the volume of the carrier substrate and calculated as palladium metal.

18. Catalyst according to claim 1 , wherein washcoat zone A extends over 70 to 95% of the length L of the carrier substrate and washcoat zone B extends over 5 to 30% of the length L of the carrier substrate.

19. Catalyst according to claim 1 , wherein the carrier substrate of the length L is a flow-through or filter substrate.

20. Method of treating exhaust gases of a combustion engine, wherein the exhaust gas is passed over the catalyst of claim 1 , and wherein the exhaust gas enters the catalyst at substrate end a and exits at substrate end b.

Assignees

• Umicore Ag & Co Kg

Inventors

• Nunan John
• Moser David
• Alltizer Chad

Classifications

• B01J35/56

  Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional [3D] monoliths · CPC title

• B01J21/04 Primary

  Alumina · CPC title

• F01N3/101

  Three-way catalysts · CPC title

• B01D53/945

  characterised by a specific catalyst · CPC title

• B01J29/18

  of the mordenite type · CPC title