Emission treatment catalysts, systems and methods

Patent metadata

Field	Value
Publication number	US-9993771-B2
Application number	US-48471009-A
Country	US
Kind code	B2
Filing date	Jun 15, 2009
Priority date	Dec 12, 2007
Publication date	Jun 12, 2018
Grant date	Jun 12, 2018

Abstract

Zoned diesel oxidation catalysts containing a higher precious metal loading in the inlet zone that the outlet zone and an equal or shorter length inlet zone are described. Emission treatment systems and methods of remediating nitrogen oxides (NOx), particulate matter, and gaseous hydrocarbons using zoned diesel oxidation catalysts are also described.

First claim

What is claimed:

1. A method of treating an exhaust stream from a diesel engine comprising NOx and particulate matter, the method comprising flowing the exhaust stream from the diesel engine through a diesel oxidation catalyst comprising an inlet zone with an axial length and an outlet zone with an axial length, the inlet zone comprising platinum and palladium in a first loading, the outlet zone comprising palladium in a second loading, the outlet zone comprises less than about 0.1 wt. % platinum, the first loading being greater than the second loading and the axial length of the inlet zone being less than or equal to the axial length of the outlet zone, and wherein upon passing a diesel exhaust stream through the diesel oxidation catalyst, substantially no additional NO 2 is produced over about 90% of the operating window of the diesel oxidation catalyst.

2. The method of claim 1 , wherein the axial length of the inlet zone is about half the axial length of the outlet zone.

3. The method of claim 1 , wherein the axial length of the inlet zone is about equal to the axial length of the outlet zone.

4. The method of claim 1 , wherein the axial length of inlet zone is at least about 10% of the total length of the diesel oxidation catalyst.

5. The method of claim 1 , wherein the axial length of the inlet zone is at least about 20% of the total length of the diesel oxidation catalyst.

6. The method of claim 1 , wherein the total length of the inlet zone is at least about 40% of the total length of the diesel oxidation catalyst.

7. The method of claim 1 , wherein the inlet zone has a platinum to palladium ratio equal to or greater than about 10:1.

8. The method of claim 1 , wherein the first loading is greater than about 30 g/ft 3 .

9. The method of claim 1 , wherein the second loading is less than about 30 g/ft 3 .

10. The method of claim 1 , wherein the diesel oxidation catalyst is disposed on a flow-through substrate.

11. The method of claim 1 , wherein one or more of the inlet zone and the outlet zone further comprises a base metal oxide.

12. The method of claim 1 , wherein one or more of the inlet zone and the outlet zone further comprises ceria.

13. The method of claim 1 , wherein the inlet zone comprises platinum and palladium in a ratio of at least 2:1 and the outlet zone comprises substantially only palladium.

14. The method of claim 1 , wherein the inlet zone comprises platinum and palladium in a ratio of about 10:1 with a loading of about 80 g/ft 3 and the outlet zone comprises substantially only palladium with a loading of about 5 g/ft 3 .

15. The method of claim 1 , wherein the inlet zone and the outlet zone comprise substantially only palladium.

16. The method of claim 1 , wherein one or more of the inlet zone and the outlet zone further comprises rhodium.

17. The method of claim 1 , wherein the axial length of the inlet zone is about half the axial length of the outlet zone and the first loading is greater than about 30 g/ft 3 and the second loading is less than about 30 g/ft 3 .

18. A system for treating an exhaust stream comprising NOx from an engine, the system comprising a diesel oxidation catalyst disposed downstream of a diesel engine, wherein the diesel oxidation catalyst comprises an inlet zone with an axial length and an outlet zone with an axial length, the inlet zone comprising platinum and palladium in a first loading, the outlet zone comprising palladium in a second loading, the outlet zone comprises less than about 0.1 wt. % platinum, the first loading being greater than the second loading and the axial length of the inlet zone being less than or equal to the axial length of the outlet zone, and wherein upon passing a diesel exhaust stream through the diesel oxidation catalyst, substantially no additional NO 2 is produced over about 90% of the operating window of the diesel oxidation catalyst.

19. The system of claim 18 , wherein the axial length of the inlet zone is less than about 35% of the total length of the diesel oxidation catalyst.

20. The system of claim 18 , further comprising a catalyzed soot filter disposed downstream of the diesel oxidation catalyst, the catalyzed soot filter having a plurality of longitudinally extending passages bounded by longitudinally extending walls, the passages comprising inlet passages having an open inlet end and a closed outlet end, and outlet passages having a closed inlet end and an open outlet end, the catalyzed soot filter comprising a catalyst composition on the walls, the catalyzed soot filter effective to optimize the ratio of NO to NO 2 exiting the filter.

21. The system of claim 20 , further comprising a selective catalytic reduction catalyst disposed downstream of the catalyzed soot filter.

Assignees

• Voss Kenneth E
• Hallstrom Kevin A
• Kumar Sanath V
• Stiebels Susanne
• Vaarkamp Marius
• Basf Corp

Inventors

• Voss Kenneth E
• Hallstrom Kevin A
• Kumar Sanath V
• Stiebels Susanne
• Vaarkamp Marius

Classifications

• B01D53/9418 Primary

  for removing nitrogen oxides by selective catalytic reduction [SCR] using a reducing agent in a lean exhaust gas · CPC title

• F01N3/2066

  Selective catalytic reduction [SCR] · CPC title

• F01N2610/02

  the substance being ammonia or urea · CPC title

• Y02T10/22

  Cross-Sectional Technologies · mapped topic

• B01D53/945

  characterised by a specific catalyst · CPC title