Diesel oxidation catalyst having a capture region for sulfur containing impurities

Patent metadata

Field	Value
Publication number	US-10137413-B2
Application number	US-201715668829-A
Country	US
Kind code	B2
Filing date	Aug 4, 2017
Priority date	Aug 5, 2016
Publication date	Nov 27, 2018
Grant date	Nov 27, 2018

Abstract

An oxidation catalyst is described for treating an exhaust gas produced by a diesel engine. The oxidation catalyst comprises: a substrate; a capture material for capturing at least one sulfur containing impurity in the exhaust gas produced by the diesel engine; wherein the capture material comprises a metal for reacting with an oxide of sulfur in the exhaust gas and particles of a refractory oxide, wherein the particles of the refractory oxide have a mean specific surface area ≤50 m2/g; and a catalytic region disposed on the substrate; wherein the catalytic region comprises a catalytic material comprising a platinum group metal (PGM) selected from the group consisting of platinum (Pt), palladium (Pd) and a combination of platinum (Pt) and palladium (Pd).

First claim

The invention claimed is:

1. An oxidation catalyst for treating an exhaust gas produced by a diesel engine, wherein the oxidation catalyst comprises:
a substrate;
a capture material for capturing at least one sulfur containing impurity in the exhaust gas produced by the diesel engine; wherein the capture material comprises a metal for reacting with an oxide of sulfur in the exhaust gas and particles of a refractory oxide, and
wherein the particles of the refractory oxide have a mean specific surface area less than or equal to 50 m 2 /g; and
a catalytic region disposed on the substrate;
wherein the catalytic region comprises a catalytic material comprising a platinum group metal (PGM) selected from the group consisting of platinum (Pt), palladium (Pd) and a combination of platinum (Pt) and palladium (Pd).

2. The oxidation catalyst of claim 1 , wherein the metal for reacting with an oxide of sulfur in the exhaust gas is palladium (Pd), magnesium (Mg), cerium (Ce) or a combination of any two or more thereof.

3. The oxidation catalyst of claim 1 , wherein the capture material comprises particles of the metal for reacting with an oxide of sulfur in the exhaust gas having a mean particle size of from about about 10 nm to about 5 microns.

4. The oxidation catalyst of claim 1 , wherein the refractory oxide of the capture material is alumina.

5. The oxidation catalyst of claim 1 , wherein the platinum group metal (PGM) is platinum (Pt), palladium (Pd) or a combination of platinum (Pt) and palladium (Pd).

6. The oxidation catalyst of claim 1 , wherein the catalytic material further comprises a support material, and wherein the platinum group metal (PGM) is supported on the support material, and wherein the support material comprises a refractory oxide selected from the group consisting of alumina, silica, titania, zirconia, ceria, silica-alumina, titania-alumina, zirconia-alumina, ceria-alumina, titania-silica, zirconia-silica, zirconia-titania, ceria-zirconia and alumina-magnesium oxide.

7. The oxidation catalyst of claim 6 , wherein the refractory oxide of the support material supporting the PGM is alumina, silica or silica-alumina.

8. The oxidation catalyst of claim 6 , wherein the refractory oxide of the support material supporting the PGM is titania.

9. The oxidation catalyst of claim 1 further comprising a capture region, wherein the capture region comprises the capture material.

10. The oxidation catalyst of claim 9 , wherein the capture region is a capture layer.

11. The oxidation catalyst of claim 10 , wherein the catalytic region is a catalytic layer, and wherein the capture layer is disposed on the catalytic layer, and the catalytic layer is disposed on the substrate.

12. The oxidation catalyst of claim 10 wherein the catalytic region is a first catalytic zone and a second catalytic zone, and the capture layer is disposed on both the first catalytic zone and the second catalytic zone, and wherein the first catalytic zone and the second catalytic zone are disposed on the substrate.

13. The oxidation catalyst of claim 9 , wherein the capture region is a capture zone.

14. The oxidation catalyst of claim 13 , wherein the catalytic region is either:
(a) a catalytic layer, and the capture zone is disposed on the catalytic layer; or
(b) a catalytic zone, wherein the catalytic zone is disposed at an outlet end of the substrate and the capture zone is disposed at an inlet end of the substrate; or
(c) a catalytic zone, wherein the catalytic zone is disposed at an inlet end of the substrate and the capture zone is disposed at an outlet end of the substrate.

15. The oxidation catalyst of claim 9 , wherein the substrate comprises an inlet end surface and an outlet end surface, and the capture region is a capture face, which is disposed on the inlet end surface and/or the outlet end surface, and optionally wherein the capture face has a mean length from the inlet end surface of the substrate of <25 mm.

16. The oxidation catalyst of claim 15 , wherein the catalytic region is either:
(a) a catalytic layer disposed on the substrate; or
(b) a first catalytic layer and a second catalytic layer, wherein the first catalytic layer is disposed on the second catalytic layer, and the second catalytic layer is disposed on the substrate; or
(c) a first catalytic zone and a second catalytic zone, wherein the first catalytic zone is disposed upstream of the second catalytic zone.

17. The oxidation catalyst of claim 1 , wherein the substrate is a flow-through monolith substrate or a filtering monolith substrate, which is a wall-flow filter.

18. The oxidation catalyst of claim 1 , wherein the substrate has a diameter of greater than or equal to 7 inches (17.8 cm).

19. An exhaust system for treating an exhaust gas produced by a diesel engine, wherein the exhaust system comprises an oxidation catalyst according to claim 1 and an emissions control device.

20. The oxidation catalyst of claim 1 , wherein the particles of the refractory oxide are coated with particles of the metal for reacting with an oxide of sulfur in the exhaust gas.

21. The oxidation catalyst of claim 1 , wherein the particles of the refractory oxide of the capture material comprise alumina, silica, titania, zirconia, silica-alumina, titania-alumina, zirconia-alumina, titania-silica, zirconia-silica, zirconia-titania, or alumina-magnesium oxide.

22. The oxidation catalyst of claim 1 , wherein the particles of the refractory oxide of the capture material comprise alumina, silica, or silica-alumina.

23. The oxidation catalyst of claim 1 , wherein the particles of the refractory oxide of the capture material have a mean specific surface area of less than or equal to 30 m 2 /g.

24. The oxidation catalyst of claim 1 , wherein the particles of the refractory oxide of the capture material have a mean specific surface area of less than or equal to 20 m 2 /g.

25. The oxidation catalyst of claim 1 , wherein the capture material comprises particles of the metal for reacting with an oxide of sulfur in the exhaust gas having a mean particle size in a range of from 50 nm to 5 microns.

26. The oxidation catalyst of claim 1 , wherein the capture material comprises particles of the metal for reacting with an oxide of sulfur in the exhaust gas having a mean particle size in a range of from 75 nm to 3 microns.

Assignees

• Johnson Matthey Plc

Inventors

• Cole Kieran
• Hofmann Lothar
• Robertson Calum

Classifications

• B01D2255/9025

  Three layers · CPC title

• F01N2570/12

  Hydrocarbons · CPC title

• B01J23/44

  Palladium · CPC title

• F01N2570/10

  Carbon or carbon oxides · CPC title

• F01N3/106

  Auxiliary oxidation catalysts · CPC title