Disordered molecular sieve supports for the selective catalytic reduction of NO

1. A catalyst for selective catalytic reduction of NO x comprising:

a. 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

b. a support comprising a molecular sieve having at least one intergrowth phase consisting of an aluminosilicate, a silico-aluminophosphate, or aluminosilicate/silico-aluminophosphate combination having two different small-pore, three-dimensional framework structures,

wherein the first framework structure is AEI and the second framework structure is CHA,

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.

2. The catalyst of claim 1 , 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.

3. The catalyst of claim 1 , wherein said support comprises one aluminosilicate and one or more silico-aluminophosphates.

4. The catalyst of claim 1 , wherein said molecular sieve comprises an intergrowth of a first material selected from the group consisting of SAPO-34, SSZ-13, SAPO-47, CAL-1, SSZ-62, and ZYT-6, and a second material selected from the group consisting of SAPO-18, SIZ-8, and SSZ-39.

5. The catalyst of claim 1 , wherein said first and second framework structures are silico-aluminophosphates.

6. The catalyst of claim 5 , wherein said mole ratio is about 1:99 to about 50:50.

7. The catalyst of claim 6 , wherein said mole ratio is about 5:95 to about 20:80.

8. The catalyst of claim 5 , wherein said molecular sieve is a SAPO-18/SAPO-34 intergrowth.

9. The catalyst of claim 8 , wherein said mole ratio is about 1:99 to about 50:50.

10. The catalyst of claim 8 , wherein said mole ratio is about 5:95 to about 15:85.

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

12. The catalyst of claim 1 , wherein said transition metal is Cu.

13. The catalyst of claim 5 , 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.

14. The catalyst of claim 13 , wherein said transition metal is selected from the group consisting of Cu and Fe.

15. The catalyst of claim 9 , 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.

16. The catalyst of claim 1 , wherein said transition metal is Cu and is present in an amount of about 1.5 to about 2.5 weight percent based on the total weight of the support, and wherein said support comprises an intergrowth of SAPO-18 and SAPO-34 in a mole ratio of SAPO-18 to SAPO-34 of about 5:95 to about 15:85.

17. A catalyst composition comprising:

a. 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 consisting of an aluminosilicate, a silico-aluminophosphate, or aluminosilicate/silico-aluminophosphate combination having two different small-pore, three-dimensional framework structures,

wherein the first framework structure is AEI and the second framework structure is CHA,

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; and

b. a binder selected from the group consisting of TiO 2 , ZrO 2 , SnO 2 , CeO 2 , alumina, silica, non molecular sieve silica-alumina, a naturally occurring clay, or mixtures thereof, wherein said supported metal catalyst and said binder are combined to form a washcoat.

18. The catalyst composition of claim 17 , wherein said binder is selected from the group consisting of TiO 2 , ZrO 2 , SnO 2 , and CeO 2 .

19. The catalyst composition of claim 1 , wherein said first and second framework structures are aluminosilicates.

20. The catalyst of claim 19 , wherein said mole ratio is about 1:99 to about 50:50.

21. The catalyst of claim 20 , wherein said mole ratio is about 5:95 to about 20:80.

22. The catalyst of claim 20 , wherein said molecular sieve is an SSZ-13/SSZ-39 intergrowth.

23. The catalyst of claim 22 , wherein said transition metal is selected from the group consisting of Cu, Fe, Co, Pt, and Mn.

24. The catalyst of claim 23 , wherein said transition metal is Cu.

25. The catalyst of claim 23 , 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.