DIESEL OXIDATION CATALYST WITH NOx ADSORBER ACTIVITY

Patent metadata

Field	Value
Publication number	US-2015273452-A1
Application number	US-201514676175-A
Country	US
Kind code	A1
Filing date	Apr 1, 2015
Priority date	Apr 1, 2014
Publication date	Oct 1, 2015
Grant date	—

Abstract

An oxidation catalyst for treating an exhaust gas from a diesel engine and an exhaust system comprising the oxidation catalyst are described. The oxidation catalyst comprises: a first washcoat region for adsorbing NO x , wherein the first washcoat region comprises a zeolite catalyst, wherein the zeolite catalyst comprises a noble metal and a zeolite; a second washcoat region for oxidising nitric oxide (NO), wherein the second washcoat region comprises platinum (Pt) and a support material; and a substrate having an inlet end and an outlet end.

First claim

1 . An oxidation catalyst for treating an exhaust gas from a diesel engine, which oxidation catalyst comprises:
a first washcoat region for adsorbing NO x , wherein the first washcoat region comprises a zeolite catalyst, wherein the zeolite catalyst comprises a noble metal and a zeolite; a second washcoat region for oxidising nitric oxide (NO), wherein the second washcoat region comprises platinum (Pt) and a support material; and a substrate having an inlet end and an outlet end.

2 . An oxidation catalyst according to claim 1 , wherein the noble metal is selected from the group consisting of palladium (Pd), platinum (Pt), rhodium (Rh), gold (Au), silver (Ag), iridium (Ir), ruthenium (Ru), osmium (Os) and mixtures of two or more thereof.

3 . An oxidation catalyst according to claim 1 , wherein the zeolite catalyst has at least 1% by weight of the noble metal located inside pores of the zeolite.

4 . An oxidation catalyst according to claim 1 , wherein the zeolite is a small pore zeolite having a Framework Type selected from the group consisting of ACO, AEI, AEN, AFN, AFT, AFX, ANA, APC, APD, ATT, CDO, CHA, DDR, DFT, EAB, EDI, EPI, ERI, GIS, GOO, IHW, ITE, ITW, LEV, KFI, MER, MON, NSI, OWE, PAU, PHI, RHO, RTH, SAT, SAV, SIV, THO, TSC, UEI, UFI, VNI, YUG, ZON and a mixture or intergrowth of any two or more thereof.

5 . An oxidation catalyst according to claim 1 , wherein the zeolite has a silica to alumina molar ratio of 10 to 200.

6 . An oxidation catalyst according to claim 1 , wherein the second washcoat region comprises platinum (Pt) as the only platinum group metal.

7 . An oxidation catalyst according to claim 1 , wherein the support material comprises a refractory metal oxide selected from the group consisting of alumina, silica, titania, zirconia, ceria and a mixed or composite oxide of two or more thereof.

8 . An oxidation catalyst according to claim 7 , wherein the support material comprises alumina doped with silica.

9 . An oxidation catalyst according to claim 1 , wherein the second washcoat region further comprises an alkaline earth metal or manganese.

10 . An oxidation catalyst according to claim 1 , wherein the first washcoat region is arranged to contact the exhaust gas at the outlet end of the substrate and after contact of the exhaust gas with the second washcoat region.

11 . An oxidation catalyst according to claim 10 , wherein the first washcoat region is a first washcoat zone disposed at an outlet end of the substrate and the second washcoat region is a second washcoat zone disposed at an inlet end of the substrate.

12 . An oxidation catalyst according to claim 10 , the second washcoat region is a second washcoat layer and the first washcoat region is a first washcoat zone, and wherein the first washcoat zone is disposed on the second washcoat layer at an outlet end of the substrate.

13 . An oxidation catalyst according to claim 10 , wherein the second washcoat region is a second washcoat layer and the first washcoat region is a first washcoat layer, and wherein the second washcoat layer is disposed on the first washcoat layer.

14 . An oxidation catalyst according to claim 1 , wherein the second washcoat region is arranged to contact the exhaust gas at or near the outlet end of the substrate and after contact of the exhaust gas with the first washcoat region.

15 . An oxidation catalyst according to claim 14 , wherein the second washcoat region is a second washcoat zone disposed at an outlet end of the substrate and the first washcoat region is a first washcoat zone disposed at an inlet end of the substrate.

16 . An oxidation catalyst according to claim 14 , wherein the first washcoat region is a first washcoat layer and the second washcoat region is a second washcoat zone, and wherein the second washcoat zone is disposed on the first washcoat layer at an outlet end of the substrate.

17 . An oxidation catalyst according to claim 14 , wherein the first washcoat region is a first washcoat layer and the second washcoat region is a second washcoat layer, and wherein the second washcoat layer is disposed on the first washcoat layer.

18 . An oxidation catalyst according to claim 1 , wherein the substrate is a through-flow substrate.

19 . An exhaust system comprising an oxidation catalyst as defined in claim 1 and an emissions control device.

20 . A method of treating an exhaust gas from a diesel engine, which method comprises either contacting the exhaust gas with an oxidation catalyst as defined in claim 1 .

Assignees

• Johnson Matthey Plc

Inventors

• Chiffey Andrew Francis
• Phillips Paul Richard
• Moreau Francois
• Daly Christopher
• O'Brien Matthew

Classifications

• B01J29/7415

  Zeolite Beta · CPC title

• B01J37/0248

  Coatings comprising impregnated particles · CPC title

• B01J37/0246

  Coatings comprising a zeolite · CPC title

• B01J37/0244

  Coatings comprising several layers · CPC title

• B01D53/944

  Simultaneously removing carbon monoxide, hydrocarbons or carbon making use of oxidation catalysts (three-way-catalysts [TWC] B01D53/9445) · CPC title