Ammonia oxidation catalyst

Patent metadata

Field	Value
Publication number	US-9227176-B2
Application number	US-201314091967-A
Country	US
Kind code	B2
Filing date	Nov 27, 2013
Priority date	Nov 30, 2012
Publication date	Jan 5, 2016
Grant date	Jan 5, 2016

Abstract

Provided is a catalyst article for treating an emission gas comprising (a) a noble metal catalyst layer comprising one or more noble metals disposed on a first refractory metal oxide support; and (b) a vanadium catalyst layer comprising vanadium pre-fixed on a second refractory metal oxide support selected from alumina, titania, zirconia, ceria, silica, and mixtures of these, wherein the first catalyst layer is in physical contact with said second catalyst layer. Also provided is a method for making such a catalyst article, a method for treating gas emissions using such an article, and an emission gas treatment system incorporating such an article.

First claim

What is claimed is:

1. A catalyst article for treating an emission gas comprising:
a. a noble metal catalyst layer comprising one or more noble metals disposed on a first refractory metal oxide support; and
b. a vanadium catalyst layer comprising vanadium pre-fixed on a second refractory metal oxide support selected from the group consisting of alumina, titania, zirconia, ceria, silica, and mixtures thereof,
wherein the noble metal catalyst layer is in physical contact with the vanadium catalyst layer.

2. The catalyst article of claim 1 , wherein said noble metal catalyst layer is a coating applied to an inert substrate selected from the group consisting of honeycomb flow-through monoliths, honeycomb wall-flow monoliths, and corrugated metal plates, and wherein said vanadium catalyst layer is a coating applied to said inert substrate.

3. The catalyst article of claim 2 , Wherein said noble metal catalyst layer is a first layer and said vanadium catalyst layer is a second layer.

4. The catalytic article of claim 3 , wherein said first layer is substantially free of vanadium and said second layer is substantially free of noble metals.

5. The catalytic article of claim 4 , wherein said article is calcined.

6. The catalyst article of claim 4 , wherein said second layer comprises vanadia pre-fixed to a titania support, wherein said vanadia is present in an amount of about 0.1-10 weight percent based on the weight of the titania.

7. The catalyst article of claim 6 , wherein said second layer further comprises an oxide of tungsten.

8. The catalyst article of claim 6 , wherein said first layer comprises at least one of platinum and palladium on an alumina support, wherein said platinum group metal is present in an amount of about 0.05-0.50 weight percent based on the weight of the alumina support.

9. The catalyst article of claim 3 , wherein said second layer is applied over at least a portion of said first layer.

10. The catalyst article of claim 3 , wherein said inert substrate is a flow-through honeycomb brick.

11. The catalyst article of claim 10 , further comprising a selective catalytic reduction (SCR) catalyst disposed on or in said flow-through brick upstream of said first and second layers.

12. The catalyst article of claim 3 , wherein said inert substrate is a corrugated metal plate.

13. The catalyst article of claim 3 , wherein said inert substrate is a wall flow honeycomb filter.

14. The catalyst article of claim 1 , wherein said second catalyst layer is an extruded substrate and said first catalyst layer is a coating on said extruded substrate.

15. The catalyst article of claim 1 , wherein the catalyst article provides an increase in the amount of NH 3 conversion over a temperature range of about 250° C. to about 400° C., compared to a comparable article having vanadia that was not prefixed.

16. A method for treating an emission gas comprising:
a. contacting a emission gas derived combusting hydrocarbons in a stoichiometric excess of oxygen, wherein the emission gas contains ammonia, with a catalyst article according to claim 1 ; and
b. oxidizing a least a portion of said ammonia to form N 2 and/or NO x .

17. The method of claim 16 , further comprising providing a process for the upstream selective catalytic reduction of NO x .

18. A system for treating an emission gas comprising an SCR catalyst and an ammonia slip catalyst according to claim 1 .

19. A method for preparing a catalyst article comprising:
a. loading vanadium onto a refractory metal oxide support selected from the group consisting of alumina, titania, zirconia, ceria, silica, and mixtures thereof;
b. subsequent to step (a), calcining the vanadium loaded refractory metal oxide support to form a prefixed catalyst;
c. coating an inert substrate with supported noble metal catalyst to form a first layer; and
d. coating said inert substrate with said prefixed alyst to form a second layer.

20. The method of claim 19 , wherein said inert substrate containing said first layer and said second layer is calcined at a temperature of about 400-600° C. for about 1-10 hours.

21. The method of claim 20 , wherein said first layer is substantially free of vanadium and said second layer is substantially free of noble metals.

22. The method of claim 19 , wherein said first layer comprises vanadia on a titania support and said second layer comprises at least one noble mctal selected from platinum and palladium supported on alumina.

Assignees

• Johnson Matthey Plc

Inventors

• Andersen Paul Joseph
• Doura Kevin

Classifications

• B01J37/0244 Primary

  Coatings comprising several layers · CPC title

• B01D2251/2062

  Ammonia · CPC title

• B01J23/40

  of the platinum group metals · CPC title

• F01N3/20

  specially adapted for catalytic conversion (F01N3/22 takes precedence) · CPC title

• B01J23/42

  Platinum · CPC title