Single or dual layer ammonia slip catalyst

Patent metadata

Field	Value
Publication number	US-9789441-B2
Application number	US-201615184267-A
Country	US
Kind code	B2
Filing date	Jun 16, 2016
Priority date	Jun 18, 2015
Publication date	Oct 17, 2017
Grant date	Oct 17, 2017

Abstract

A catalyst article having an extruded support having a plurality of channels through which exhaust gas flows during operation of an engine, and a single layer coating or a bi-layer coating on the support, where the extruded support contains a third SCR catalyst, the single layer coating and the bilayer-coating contain platinum on a support with low ammonia storage and a first SCR catalyst. The catalytic articles are useful for selective catalytic reduction (SCR) of NOx in exhaust gases and in reducing the amount of ammonia slip. Methods for producing such articles are described. Methods of using the catalytic articles in an SCR process, where the amount of ammonia slip is reduced, are also described.

First claim

We claim:

1. A catalyst article comprising: (a) an extruded support having an inlet, an outlet and a plurality of channels through which exhaust gas flows during operation of an engine, and (b) a single layer coating or a bi-layer coating on the support, where, the single layer coating comprises a blend of platinum on a support with low ammonia storage with a first SCR catalyst, and the bi-layer coating comprises a bottom layer and a top layer, where the bottom layer is located between the top layer and the extruded support, the bottom layer comprises a blend of platinum on a support with low ammonia storage with a first SCR catalyst, the top layer comprises a second SCR catalyst, and the extruded support comprises a third SCR catalyst.

2. The catalyst of claim 1 , where the support with low ammonia storage is a siliceous support.

3. The catalyst of claim 1 , where the ratio of the amount of the first SCR catalyst to the amount of platinum on the support with low ammonia storage is in the range of at least one of: (a) 0:1 to 300:1, (b) 3:1 to 300:1, (c) 7:1 to 100:1; and (d) 10:1 to 50:1, inclusive, based on the weight of these components.

4. The catalyst of claim 1 , where the first SCR catalyst is a Cu-SCR catalyst comprising copper and a small pore molecular sieve, an Fe-SCR catalyst comprising iron and a small pore molecular sieve, or a mixed oxide.

5. The catalyst article of claim 1 , where the second SCR catalyst and the third SCR catalyst are, independent of each other, a base metal, an oxide of a base metal, a molecular sieve, a metal exchanged molecular sieve or a mixture thereof.

6. The catalyst article of claim 5 , where the molecular sieve or the metal exchanged molecular sieve is small pore, medium pore, large pore or a mixture thereof.

7. The catalyst article of claim 1 , where the catalyst provides an improvement in N 2 yield from ammonia at a temperature from about 250° C. to about 300° C. compared to a catalyst comprising a comparable formulation in which the first SCR catalyst is present as a first layer and the platinum on a siliceous support is present in a second layer and gas comprising NH 3 passes through the first layer before passing through the second layer.

8. The catalyst article of claim 1 , where, when the first SCR catalyst comprises vanadium, the catalyst article provides reduced deactivation compared to a catalyst comprising a comparable formulation in which the first SCR catalyst is present as a first layer and the platinum on a siliceous support is present in a second layer and gas comprising NH 3 passes through the first layer before passing through the second layer.

9. An exhaust system comprising the catalyst article of claim 1 and a means for forming NH 3 in the exhaust gas.

10. An exhaust system comprising the catalyst of claim 1 , an SCR catalyst and DOC catalyst, where the SCR catalyst is located between the catalyst of claim 1 and the DOC catalyst.

11. The exhaust system of claim 9 , where the exhaust system comprises a platinum group metal before an SCR catalyst and the amount of the platinum group metal is sufficient to generate an exotherm.

12. A method of improving the N 2 yield from ammonia in an exhaust gas at a temperature from about 250° C. to about 300° C., the method comprising contacting an exhaust gas comprising ammonia with a catalyst of claim 1 .

13. The method of claim 12 , where the improvement in yield is about 10% to about 20% compared to a catalyst comprising a comparable formulation in which the first SCR catalyst is present as a first layer and the platinum on a siliceous support is present in a second layer and gas comprising NH 3 passes through the first layer before passing through the second layer.

14. A method of reducing N 2 O formation from NH 3 in an exhaust gas, the method comprising contacting an exhaust gas comprising ammonia with a catalyst of claim 1 .

15. The method of claim 14 , where the reduction in N 2 O formation is about 20% to about 40% compared to a catalyst comprising a comparable formulation in which the first SCR catalyst is present as a first layer and the platinum on a siliceous support is present in a second layer and gas comprising NH 3 passes through the first layer before passing through the second layer.

Assignees

• Johnson Matthey Plc

Inventors

• Larsson Mikael
• Micallef David
• Lu Jing

Classifications

• B01J29/82

  Phosphates {(B01J29/005 takes precedence)} · CPC title

• B01J29/763

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

• F01N3/2828

  Ceramic multi-channel monoliths, e.g. honeycombs · CPC title

• B01D2255/911

  NH3-storage component incorporated in the catalyst · CPC title

• F01N2570/14

  Nitrogen oxides · CPC title