Disordered molecular sieve supports for the selective catalytic reduction of NOx

Patent metadata

Field	Value
Publication number	US-8932973-B2
Application number	US-201213353873-A
Country	US
Kind code	B2
Filing date	Jan 19, 2012
Priority date	Mar 11, 2010
Publication date	Jan 13, 2015
Grant date	Jan 13, 2015

Abstract

A catalyst for selective catalytic reduction of NO x having one or more transition metals selected from Cr, Mn, Fe, Co, Ce, Ni, Cu, Zn, Ga, Mo, Ru, Rh, Pd, Ag, In, Sn, Re, Ir, Pt, and mixtures thereof supported on a support, wherein the support has a molecular sieve having at least one intergrowth phase having at least two different small-pore, three-dimensional framework structures.

First claim

What is claimed is:

1. A method for treating an exhaust gas comprising:
a. contacting an exhaust gas stream comprising NOx and a reducing agent with a supported metal catalyst comprising:
i. one or more transition metals selected from the group consisting of Cr, Mn, Fe, Co, Ce, Ni, Cu, Zn, Ga, Mo, Ru, Rh, Pd, Ag, In, Sn, Re, Ir, Pt, and mixtures thereof, and
ii. a support comprising a molecular sieve having at least one intergrowth phase comprising at least two different small-pore, three-dimensional framework structures,
wherein each framework structure in said intergrowth has a maximum of eight ring members,
wherein the one or more transition metals are disposed inside the pores of the molecular sieve, on the external surface of the molecular sieve, or both inside the pores and on the external surface of the molecular sieve and
wherein said transition metal is present in an amount of about 0.01 to about 6 weight percent, based on the total weight of the molecular sieve;

b. selectively reducing at least a portion of said NO x with said reducing agent to produce N 2 and H 2 O.

2. The method of claim 1 , wherein said exhaust gas stream is generated by a lean-burn engine.

3. The method of claim 1 , wherein said reducing agent is ammonia.

4. The method of claim 1 , wherein said reducing agent is a hydrocarbon.

5. The method of claim 1 , wherein said contacting occurs at a temperature of about 150° C. to about 750° C.

6. The method of claim 1 wherein said contacting occurs at a temperature of at least 900° C.

7. The method of claim 2 , wherein said intergrowth phase consists essentially of a first small-pore, three-dimensional framework structure and a second small-pore, three-dimensional framework structure, wherein said first and second framework structures are present in a mole ratio of said first framework structure to said second framework structure of about 1:99 to about 99:1.

8. The method of claim 7 , wherein one of said first or second framework structures is selected from the group consisting of AEI, GME, AFX, AFT, and LEV, and the other of said first or second framework structures is CHA.

9. The method of claim 8 , wherein said one framework structure is an aluminosilicate and one framework structure is a silico-aluminophosphate.

10. The method of claim 8 , wherein said first framework structure is AEI and said second framework structure is CHA.

11. The method of claim 10 , wherein said first and second framework structures are silicoaluminophosphates.

12. The method of claim 11 , wherein said mole ratio is about 1:99 to about 50:50.

13. The method of claim 12 , wherein said mole ratio is about 5:95 to about 20:80.

14. The method of claim 10 , wherein said molecular sieve comprises SAPO-18 and SAPO-34 and said mole ratio is about 1:99 to about 50:50.

15. The method of claim 14 , wherein said mole ratio is about 5:95 to about 15:85.

16. The method of claim 1 , wherein said transition metal is selected from the group consisting of Cu, Fe, Co, Pt, and Mn.

17. The method of claim 1 , wherein said transition metal is Cu.

18. The method of claim 11 , wherein said transition metal is present in an amount of about 1 to about 3 weight percent based on the total weight of the molecular sieve, and is selected from the group consisting of Cu, Fe, Co, Pt, and Mn.

19. The method of claim 18 , wherein said transition metal is selected from the group consisting of Cu and Fe.

Assignees

• Andersen Paul J
• Casci John Leonello
• Chen Hai-Ying
• Fedeyko Joseph M
• Johnson Matthey Plc

Inventors

• Andersen Paul J
• Casci John Leonello
• Chen Hai-Ying
• Fedeyko Joseph M

Classifications

• B01D2258/012

  Diesel engines and lean burn gasoline engines · CPC title

• B01D2251/2062

  Ammonia · CPC title

• B01J2229/18

  to introduce other elements into or onto the molecular sieve itself · CPC title

• B01D2255/20746

  Cobalt · CPC title

• B01D2255/20761

  Copper · CPC title