IP Library Granted Patent US 8,226,915
Granted Patent B2
US 8,226,915 · App. 12/955,317 · Granted Jul 24, 2012

Coated perovskite-based catalysts, catalyst combinations and methods of treating a gas stream

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Quick Facts
Patent No.
US 8,226,915
App. No.
12/955,317
Granted
Jul 24, 2012
Kind
B2
Abstract

One embodiment of the invention includes a method of treating a gas stream comprising flowing the gas stream over a hydrocarbon reduction and NO x reduction catalyst first, and thereafter flowing the gas over a perovskite and NO x trap material for NO x oxidation and storage. In one embodiment, the hydrocarbon reduction and NO x reduction catalyst may include palladium. In one embodiment, the perovskite catalyst may have the general formula ABO 3 , AA′BO 3 , ABB′O 3 , or AA′BB′O 3 . The perovskite catalyst may be the only catalyst or a second non-perovskite catalyst may include at least one of palladium, platinum, rhodium, ruthenium or a catalyst system including one or more of the same or alloys thereof. In one embodiment, the NO x trap material may include at least one of alkali metals, alkaline earth metals such as barium, calcium, potassium, or sodium.

Claims (50)

1. A method comprising:

treating an exhaust steam including NO x comprising:

flowing the exhaust stream first over a hydrocarbon reduction and NO x reduction catalyst;

and thereafter flowing the exhaust stream over a perovskite catalyst and a NO x trap material for NO x oxidation and storage.

2. A method as set forth in claim 1 wherein the perovskite catalyst and NO x trap material comprises a layer on or over a support substrate, and wherein the hydrocarbon reduction and NO x reduction catalyst comprises a layer on or over the layer including the perovskite catalyst then NO x trap material.

3. A method as set forth in claim 1 wherein the hydrocarbon reduction and NO x reduction catalyst comprises a first layer or zone on or over a first portion of a substrate and wherein the perovskite catalyst and a NO x trap material comprise a layer or zone on or over a second portion of the substrate and wherein the hydrocarbon reduction and NO x reduction catalyst is not on the perovskite catalyst and NO x trap material.

4. A method as set forth in claim 1 wherein the hydrocarbon reduction and NO x reduction catalyst and the perovskite catalyst and NO x trap material are supported by a substrate.

5. A method as set forth in claim 4 wherein the substrate is substantially flat.

6. A method as set forth in claim 4 wherein the substrate comprises a bead or pellet.

7. A method as set forth in claim 4 wherein the substrate is constructed and arranged to have a ring, saddle, hollow cylinder or Raschig ring shape.

8. A method as set forth in claim 4 wherein the substrate is porous.

9. A method as set forth in claim 4 wherein the substrate is solid.

10. A method as set forth in claim 4 wherein the substrate comprises a gas flow through monolith having a plurality of through-holes formed therein.

11. A method as set forth in claim 10 wherein the monolith comprises a ceramic or metal material.

12. A method as set forth in claim 4 wherein the substrate comprises a wall flow filter.

13. A method as set forth in claim 1 wherein the perovskite catalyst and NO x trap material are constructed and arranged as a support substrate not carried by another substrate and wherein the hydrocarbon reduction and NO x reduction catalyst is coated on or over the substrate.

14. A method as set forth in claim 13 wherein the perovskite catalyst and NO x reduction material is porous.

15. A method as set forth in claim 1 wherein the perovskite catalyst has the general formula ABO 3 , AA′BO 3 , ABB′O 3 , or AA′BB′O 3 , wherein A comprises a rare earth metal from the Lanthanide Series and/or an alkaline-earth metal and wherein B comprises a transition metal.

16. A method as set forth in claim 15 , wherein said perovskite catalyst has the general formula AA′BO 3 ;

wherein A comprises a rare earth metal from the Lanthanide Series and/or an alkaline-earth metal;

wherein B comprises a transition metal; and

wherein A′ comprises a substitution of a promoter material for a portion of A.

17. A method as set forth in claim 15 , wherein said perovskite catalyst has the general formula ABB′O 3 ,

wherein A comprises a rare earth metal from the Lanthanide Series and/or an alkaline-earth metal;

wherein B comprises a transition metal; and

wherein B′ comprises a substitution of a promoter material for a portion of B.

18. A method as set forth in claim 15 , wherein said perovskite catalyst has the general formula AA′BB′O 3 ,

wherein A comprises a rare earth metal from the Lanthanide Series and/or an alkaline-earth metal;

wherein B comprises a transition metal;

wherein A′ comprises a substitution of a promoter material for a portion of A; and

wherein B′ comprises a substitution of a promoter material for a portion of B.

19. A method as set forth in of claim 18 , wherein A′ comprises Strontium.

20. A method as set forth in claim 15 , wherein A is Lanthanum.

21. A method as set forth in claim 15 , wherein B is Cobalt or Manganese or Iron.

22. A system for reducing NO x in a gas stream comprising:

a catalytic oxidation reactor comprising a first reaction zone comprising a hydrocarbon reduction and NO x reduction catalyst; and a second zone downstream of the first zone, the second zone comprising a perovskite catalyst and a NO x trap material for NO x oxidation and storage.

23. A system as set forth in claim 22 wherein the perovskite catalyst has the general formula ABO 3 , AA′BO 3 ABB′O 3 , or AA′BB′O 3 , wherein A comprises a rare earth metal from the Lanthanide Series and/or an alkaline-earth metal and wherein B comprises a transition metal.

24. The system of claim 22 , wherein said perovskite catalyst is of the general formula AA′BO 3 ;

wherein A comprises a rare earth metal from the Lanthanide Series and/or an alkaline-earth metal;

wherein B comprises a transition metal; and

wherein A′ comprises a substitution of a promoter material for a portion of A.

25. A system as set forth in claim 22 , wherein said perovskite catalyst is of the general formula ABB′O 3 ;

wherein A comprises a rare earth metal from the Lanthanide Series and/or an alkaline-earth metal;

wherein B comprises a transition metal; and

wherein B′ comprises a substitution of a promoter material for a portion of B.

26. A system as set forth in claim 22 , wherein said perovskite catalyst is of the general formula AA′BB′O 3 ;

wherein A comprises a rare earth metal from the Lanthanide Series and/or an alkaline-earth metal;

wherein B comprises a transition metal;

wherein A′ comprises a substitution of a promoter material for a portion of A; and

wherein B′ comprises a substitution of a promoter material for a portion of B.

Assignments (4)
RELEASE OF SECURITY INTEREST Recorded Nov 7, 2014
From: WILMINGTON TRUST COMPANY
To: GM GLOBAL TECHNOLOGY OPERATIONS LLC
Reel/Frame 034287/0159 →
SECURITY AGREEMENT Recorded Jun 24, 2011
From: GM GLOBAL TECHNOLOGY OPERATIONS LLC
To: WILMINGTON TRUST COMPANY
Reel/Frame 026499/0267 →
CHANGE OF NAME Recorded Feb 10, 2011
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: GM GLOBAL TECHNOLOGY OPERATIONS LLC
Reel/Frame 025780/0482 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 29, 2010
From: QI, GONGSHIN; KIM, CHANG H.; LI, WEI
To: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
Reel/Frame 025427/0423 →