Mixed metal 8-ring small pore molecular sieve catalyst compositions, catalytic articles, systems, and methods
Described are compositions and catalytic articles comprising a copper-promoted 8-ring small pore molecular sieve and an iron-promoted 8-ring small pore molecular sieve. The catalytic articles are useful in methods and systems to catalyze the reduction of nitrogen oxides in the presence of a reductant.
1. A selective catalytic reduction article comprising a washcoat containing both a first 8-ring small pore molecular sieve promoted with copper and a second 8-ring small pore molecular sieve promoted with iron, the catalyst effective to catalyze the reduction of nitrogen oxides in the presence of a reductant.
2. The article of claim 1 , wherein the first and second 8-ring small pore molecular sieves are selected from the group consisting of copper-promoted zeolite having a structure type selected from AEI, AFT, AFX, CHA, EAB, ERI, KFI, LEV, SAS, SAT, and SAV.
3. The article of claim 2 , wherein the first and second 8-ring small pore molecular sieves have the CHA crystal structure.
4. The article of claim 2 , wherein the 8-ring small pore molecular sieve having the CHA crystal structure is selected from an aluminosilicate zeolite, a borosilicate, a gallosilicate, a SAPO, an AlPO, a MeAPSO, and a MeAPO.
5. The article of claim 3 , wherein the 8-ring small pore molecular sieve is selected from the group consisting of SSZ-13, SSZ-62, natural chabazite, zeolite K-G, Linde D, Linde R, LZ-218, LZ-235, LZ-236, ZK-14, SAPO-34, SAPO-44, SAPO-47, and ZYT-6.
6. The article of claim 1 , wherein the first 8-ring small pore molecular sieve promoted with copper further comprises a barium component.
7. The article of claim 1 , wherein the washcoat layer is disposed on a substrate.
8. The article of claim 1 , wherein first 8-ring small pore molecular sieve promoted with copper and the second 8-ring small pore molecular sieve promoted with copper are present in a ratio in the range of 1:1 to 10:1 of the first 8-ring small pore molecular sieve material to the second 8-ring small pore molecular sieve.
9. The article of claim 1 , wherein the first 8-ring small pore molecular sieve and second 8-ring small pore molecular sieve each are selected from SSZ-13 and SSZ-62 and are present in a ratio in the range of 1:1 to 10:1 of the copper-promoted 8-ring small pore molecular sieve to the iron-promoted 8-ring small pore molecular sieve.
10. The article of claim 9 , wherein the first 8-ring small pore molecular sieve further comprises a barium component.
11. The article of claim 1 , wherein the catalyst is effective to catalyze the selective catalytic reduction of nitrogen oxides in the presence of a reductant at temperatures between 200° C. and 600° C.
12. The article of claim 3 , wherein zeolite has a silica to alumina ratio is in the range of 20 and 50.
13. A method for selectively reducing nitrogen oxides (NO x ), the method comprising contacting an exhaust gas stream containing NO x with a selective catalytic reduction catalytic article comprising a washcoat containing a first 8-ring small pore molecular sieve promoted with copper and a second 8-ring small pore molecular sieve promoted with iron.
14. The method of claim 13 , wherein the first and second 8-ring small pore molecular sieves are selected from the group consisting of AEI, AFT, AFX, CHA, EAB, ERI, KFI, LEV, SAS, SAT, and SAV.
15. The method of claim 14 , wherein the first and second 8-ring small pore molecular sieves have the CHA crystal structure and is selected from the group consisting of aluminosilicate zeolite, SAPO, AlPO, and MeAPO.
16. The method of claim 15 , wherein first and second 8-ring small pore molecular sieves having the CHA crystal structure are selected from the group consisting of SSZ-13, SSZ-62, natural chabazite, zeolite K-G, Linde D, Linde R, LZ-218, LZ-235, LZ-236, ZK-14, SAPO-34, SAPO-44, SAPO-47, and ZYT-6.
17. The method of claim 16 , wherein the first 8-ring small pore molecular sieve having the CHA crystal structure is an aluminosilicate zeolite.
18. The method of claim 17 , wherein the aluminosilicate zeolite is selected from SSZ-13 and SSZ-62.
19. The method of claim 13 , wherein second 8-ring small pore molecular sieve is selected from the group consisting of AEI, AFT, AFX, CHA, EAB, ERI, KFI, LEV, SAS, SAT, and SAV.
20. The method of claim 19 , wherein the second 8-ring small pore molecular sieve has the CHA crystal structure and is selected from the group consisting of SSZ-13, SSZ-62, natural chabazite, zeolite K-G, Linde D, Linde R, LZ-218, LZ-235, LZ-236, ZK-14, SAPO-34, SAPO-44, SAPO-47, and ZYT-6.