SCR catalytic converter having improved NOx conversion

Patent metadata

Field	Value
Publication number	US-9694320-B2
Application number	US-201414768961-A
Country	US
Kind code	B2
Filing date	Feb 21, 2014
Priority date	Feb 25, 2013
Publication date	Jul 4, 2017
Grant date	Jul 4, 2017

Abstract

The invention relates to the possibility of improving selective catalytic reduction (SCR), which is the selective reaction of nitrogen oxides with ammonia in the exhaust gas of combustion processes on an exhaust-gas catalytic converter suitable therefor—the SCR catalytic converter. For this purpose, materials used in the catalytic converter for storing ammonia are distributed on the catalyst carrier in such a way that, viewed in the flow direction, a region having low ammonia storage capacity is followed by a region of higher ammonia storage capacity.

First claim

The invention claimed is:

1. A method for the reduction of nitrogen oxides in the exhaust gas of a combustion process of lean-mixture-combustion engines by reaction with ammonia across an exhaust gas catalytic converter, the exhaust gas being guided across an exhaust gas catalytic converter in the presence of ammonia and the exhaust gas catalytic converter having one or several supporting bodies comprising one or several storage materials for ammonia, in which a material with ammonia storage capacity is distributed on the supporting body/bodies in such a way that, when viewed in the flow direction, an area with lower ammonia storage capacity is followed by an area of higher ammonia storage capacity, wherein the material determining the catalytic activity of the contemplated reaction is made of a material which has ammonia storage capacity and, as the latter, compounds selected from the group comprising zeolites, zeolite-like materials, or mixtures thereof are used, wherein a particulate filter as a supporting body in itself is not to have an increase in the catalytically active material.

2. The method according to claim 1 , wherein the area of lower ammonia storage capacity has only 30-70% of the ammonia storage capacity of the area of higher ammonia storage capacity.

3. The method according to claim 1 wherein zeolite or zeolite-like materials selected from the group comprising chabazite, SAPO-34, ALPO-4 and Zeolite β are used as storage material for ammonia.

4. The method according to claim 1 wherein at, on or under its outlet end, there is an ammonia oxidation catalytic converter.

5. The method according to claim 2 , wherein zeolite or zeolite-like materials selected from the group comprising chabazite, SAPO-34, ALPO-4 and Zeolite β are used as storage material for ammonia.

6. The method according to claim 5 , wherein at, on or under its outlet end, there is an ammonia oxidation catalytic converter.

7. The method according to claim 2 , wherein at, on or under its outlet end, there is an ammonia oxidation catalytic converter.

8. The method according to claim 3 , wherein at, on or under its outlet end, there is an ammonia oxidation catalytic converter.

9. The method according to claim 1 , wherein the storage material for ammonia comprises a zeolite-like material that is SAPO-34, ALPO-4 or both.

10. The method according to claim 1 , wherein the storage material for ammonia comprises a zeolite that is chabazite, Zeolite β, or both.

11. The method according to claim 1 , wherein the storage material for ammonia comprises a zeolite that is mordenite (MOR), Y-zeolite (FAU), ZSM-5 (MFI), ferrierite (FER), chabazite (CHA), β-zeolite (BEA) or a mixture of two or more thereof.

12. The method according to claim 1 , wherein the storage material for ammonia comprises a zeolite-like material that is aluminum phosphate (AlPO), silicon aluminum phosphate (SAPO) or a mixture thereof.

13. The method according to claim 12 , wherein the storage material for ammonia is SAPO-34, ALPO-4 or a mixture thereof.

14. The method according to claim 1 , wherein the storage material for ammonia is a), b) or a mixture of a) and b) with:
a) being mordenite (MOR), Y-zeolite (EAU), ZSM-5 (MFI), ferrierite (FER), chabazite (CHA), β-zeolite (BEA) or a mixture of two or more thereof; and
b) being aluminum phosphate (AlPO), silicon aluminum phosphate (SAPO) or a mixture thereof.

15. The method according to claim 14 , wherein the storage material for ammonia includes a).

16. The method of claim 15 wherein a) is one of chabazite, Zeolite β, or a mixture thereof.

17. The method according to claim 14 , wherein the storage material for ammonia includes h).

18. The method of claim 14 wherein at least one storage material is provided with a transition material that is iron, copper, manganese, silver or a mixture of any two or more thereof.

19. The method of claim 1 wherein at least one storage material is provided with a transition material that is iron, copper, manganese, silver or a mixture of any two or more thereof.

20. The method of claim 1 wherein the exhaust is passed over or through each of a diesel oxidation catalyst, the particulate filter, and one or more SCR catalysts.

Assignees

• Umicore Ag & Co Kg

Inventors

• Reith Christoph
• Seyler Michael

Classifications

• B01D53/9477

  with catalysts positioned on separate bricks, e.g. exhaust systems · CPC title

• B01J29/7015

  CHA-type, e.g. Chabazite, LZ-218 · CPC title

• F01N2510/0682

  having a discontinuous, uneven or partially overlapping coating of catalytic material, e.g. higher amount of material upstream than downstream or vice versa · CPC title

• Y02T10/24

  Cross-Sectional Technologies · mapped topic

• F01N3/106

  Auxiliary oxidation catalysts · CPC title