IP Library Granted Patent US 8,268,274
Granted Patent B2
US 8,268,274 · App. 12/907,217 · Granted Sep 18, 2012

Catalyst combinations and methods and systems for oxidizing nitric oxide in a gas stream

Assignee: GM Global Technology Operations LLC
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Quick Facts
Patent No.
US 8,268,274
App. No.
12/907,217
Filed
Oct 19, 2010
Granted
Sep 18, 2012
Kind
B2
Art Unit
1734
USPC
423/239.1
Abstract

One embodiment of the invention may include a product comprising a catalyst combination comprising a perovskite catalyst and a second catalyst that is not a perovskite catalyst.

Claims (83)

1. A product comprising:

a catalyst combination comprising a perovskite catalyst and a second non-perovskite catalyst, the perovskite catalyst having 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, and a particulate filter.

2. A product as set forth in claim 1 , 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.

3. A product as set forth in of claim 2 , wherein A′ comprises Strontium.

4. A product as set forth in claim 1 , 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.

5. A product as set forth in claim 1 , 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.

6. A product as set forth in claim 1 , wherein A is Lanthanum.

7. A product as set forth in claim 6 , wherein B is Cobalt or Manganese or Iron.

8. A product as set forth in claim 1 further comprising a catalytic oxidation reactor and wherein the catalyst combination is received in the reactor, wherein the catalyst combination is coupled to a substrate comprising at least one of reactor packing structures and materials, beads, pellets, fluidized bed powders or other solid particulate material suspendable in a flow of gas, a flow-through monolith, a wall-flow monolith, a metal monolith, a ceramic monolith, metal or ceramic fabricated supports.

9. A product as set forth in claim 8 wherein the catalyst combination has a loading of about 1-100 g/ft 3 .

10. A product as set forth in claim 8 wherein the second non-perovskite catalyst comprises palladium having a loading of 5-100 g/ft 3 .

11. A product as set forth in claim 8 wherein the second non-perovskite catalyst comprises platinum having a loading of 1-60 g/ft 3 .

12. A product as set forth in claim 1 further comprising a catalytic oxidation reactor and wherein the catalyst combination is received in the reactor, wherein the catalyst combination is not coupled to a substrate.

13. A product as set forth in claim 12 wherein the catalyst combination has a loading of about 1-100 g/ft 3 .

14. A product as set forth in claim 1 further comprising a catalytic oxidation reactor and wherein the catalyst combination is received in the reactor, wherein the catalyst combination has a form or shape comprising at least one of flat panels, beads, pellets, flow-through or wall-flow monoliths, or reactor packing material shapes.

15. A product as set forth in claim 1 further comprising a catalytic oxidation reactor and wherein the catalyst combination is received in the reactor, wherein the catalyst combination has a form or shape comprising at least one of, rings, saddles, hollow cylinders or Raschig rings.

16. A product as set forth in claim 1 wherein the second non-perovskite catalyst comprises at least one metal from the precious metal or nobel metal group of the periodic table.

17. A product as set forth in claim 1 wherein the second non-perovskite catalyt comprises at least one of palladium, platinum, rhodium or ruthenium, or catalyst systems including the same.

18. A product as set forth in claim 1 wherein the second non-perovskite catalyst comprises at least one of palladium or platinum, or catalyst systems including the same.

19. A system for reducing NO x and particulate matter emissions in an exhaust stream comprising:

a catalytic oxidation reactor comprising a perovskite catalyst and a non-perovskite catalyst, the perovskite catalyst having 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;

a particulate filter; and

a catalytic reduction reactor having a selective catalytic reduction catalyst.

20. The system of claim 19 , wherein said perovskite catalyst 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.

21. A system as set forth in claim 19 , wherein said perovskite catalyst 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.

22. A system as set forth in claim 19 , wherein said perovskite catalyst 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.

23. A system as set forth in claim 19 , wherein said catalytic oxidation reactor further comprises:

a platinum based catalyst or a palladium based catalyst or a platinum and palladium based catalyst coupled to another portion of said substrate material.

24. A system as set forth in claim 19 , wherein said catalytic oxidation reactor further comprises:

a platinum based catalyst or a palladium based catalyst or a platinum and palladium based catalyst coupled to said portion of said substrate material.

25. A system as set forth in claim 19 further comprising:

an injector device for injecting ammonia or urea to the exhaust stream before said catalytic reduction reactor.

26. A system as set forth in claim 25 further comprising:

a NO x sensor contained within the exhaust stream and coupled to said injector device, said NO x sensor located upstream of said catalytic reduction reactor.

27. A system as set forth in claim 25 further comprising:

a temperature sensor coupled to said catalytic reduction reactor and said injector device, said temperature sensor measuring a temperature of a selective catalytic reduction catalyst contained in said catalytic reduction reactor.

28. A product as set forth in claim 19 wherein the second non-perovskite catalyst comprises palladium having a loading of 5-100 g/ft 3 .

29. A product as set forth in claim 19 wherein the second non-perovskite catalyst comprises platinum having a loading of 1-60 g/ft 3 .

30. A method for oxidizing nitric oxide in a gas stream from a hydrocarbon fueled power source operated with a fuel lean combustion mixture, the method comprising:

passing the gas stream through a catalytic oxidation reactor, the catalytic oxidation reactor comprising a perovskite catalyst and a non-perovskite catalyst, the perovskite catalyst having the general formula ABO 3 , AA′BO 3 AA′BB′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, and a particulate filter.

31. A method as set forth in claim 30 further comprising:

forming a catalytic oxidation reactor comprising a perovskite catalyst has the general formula AA′BO 3 coupled to a substrate material, 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.

32. A method as set forth in 30 further comprising:

forming a catalytic oxidation reactor comprising a perovskite catalyst has the general formula ABB′O 3 coupled to a substrate material, 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.

33. A method as set forth in claim 30 further comprising:

forming a catalytic oxidation reactor comprising a perovskite catalyst has the general formula AA′BB′O 3 coupled to a substrate material, 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.

34. A method as set forth in claim 30 wherein the perovskite catalyst is coupled to a substrate comprising at least one of reactor packing structures and materials, beads, pellets, fluidized bed powders or other solid particulate material suspendable in a flow of gas, a flow-through monolith, a wall-flow monolith, a metal monolith, a ceramic monolith, metal or ceramic fabricated supports.

35. A method as set forth in claim 30 wherein the perovskite catalyst is not coupled to a substrate.

36. A method as set forth in claim 30 wherein the perovskite catalyst includes a form or shape comprising at least one of flat panels, beads, pellets, flow-through or wall-flow monoliths, or reactor packing material shapes.

37. A method as set forth in claim 30 wherein the perovskite catalyst includes a form or shape comprising at least one of, rings, saddles, hollow cylinders or Raschig rings.

38. A product comprising:

a catalyst combination comprising a perovskite catalyst and a second non-perovskite catalyst, the perovskite catalyst having 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, and further comprising a catalytic oxidation reactor and wherein the catalyst combination is received in the reactor, wherein the catalyst combination has a form or shape comprising at least one of, rings, saddles, hollow cylinders or Raschig rings.

39. A product comprising:

a catalyst combination comprising a perovskite catalyst and a second non-perovskite catalyst, 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.

40. A method as set forth in 39 , further comprising:

forming a catalytic oxidation reactor comprising a perovskite catalyst has the general formula ABB′O 3 coupled to a substrate material, 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.

41. A method for oxidizing nitric oxide in a gas stream from a hydrocarbon fueled power source operated with a fuel lean combustion mixture, the method comprising:

passing the gas stream through a catalytic oxidation reactor, the catalytic oxidation reactor comprising a perovskite catalyst and a non-perovskite catalyst, the perovskite catalyst having the general formula AA′BO 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, and wherein A′ comprises a substitution of a promoter material for a portion of A.

42. A product comprising:

a substrate having a first catalyst washcoat thereon and a second catalyst washcoat thereon, the first catalyst washcoat comprising a perovskite catalyst, the second catalyst comprising a second non-perovskite catalyst, the perovskite catalyst having the general formula ABO 3 , AA′BO 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.

Assignments (4)
RELEASE OF SECURITY INTEREST Recorded Nov 7, 2014
From: WILMINGTON TRUST COMPANY
To: GM GLOBAL TECHNOLOGY OPERATIONS LLC
Reel/Frame 034287/0159 →
CHANGE OF NAME Recorded Feb 10, 2011
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: GM GLOBAL TECHNOLOGY OPERATIONS LLC
Reel/Frame 025780/0482 →
SECURITY AGREEMENT Recorded Nov 8, 2010
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: WILMINGTON TRUST COMPANY
Reel/Frame 025324/0658 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 19, 2010
From: KIM, CHANG H.; BROWN, DAVID B.; LI, WEI; SCHMIEG, STEVEN J.; QI, GONGSHIN
To: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
Reel/Frame 025158/0404 →
Continuity (3)
Continuation In Part 12563345 · Sep 21, 2009
Provisional Application 61102462 · Oct 3, 2008
Related Publication 20110070139A1 · Mar 24, 2011