8-ring small pore molecular sieve with promoter to improve low temperature performance
Described is a selective catalytic reduction catalyst comprising an 8-ring small pore molecular sieve promoted with copper and an alkaline earth component. The catalyst is effective to catalyze the reduction of nitrogen oxides (NOx) in the presence of a reductant. A method for selectively reducing nitrogen oxides is also described.
1. A selective catalytic reduction catalyst comprising an 8-ring small pore molecular sieve promoted with copper and an alkaline earth component, wherein the catalyst is effective to catalyze the reduction of nitrogen oxides in the presence of a reductant, wherein the 8-ring small more molecular sieve has a crystallite size in the range of from 10 nanometers to 100 micrometers, and wherein the alkaline earth component is present in an amount of less than 5% by weight.
2. The catalyst of claim 1 , wherein the 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.
3. The catalyst of claim 2 , wherein the 8-ring small pore molecular sieve has the CHA crystal structure.
4. The catalyst of claim 3 , wherein the 8-ring small pore molecular sieve having the CHA crystal structure is selected from the group consisting of aluminosilicate zeolite, a borosilicate, a gallosilicate, a SAPO, an ALPO, a MEAPSO and a MeAPO.
5. The catalyst of claim 4 , wherein the 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 catalyst of claim 3 , wherein the 8-ring small pore molecular sieve having the CHA crystal structure is an aluminosilicate zeolite.
7. The catalyst of claim 5 , wherein the aluminosilicate zeolite is selected from SSZ-13 and SSZ-62.
8. The catalyst of claim 3 , wherein the 8-ring small pore molecular sieve having the CHA crystal structure is a SAPO.
9. The catalyst of claim 1 , wherein the alkaline earth component is selected from barium, magnesium, calcium, strontium, and combinations thereof.
10. The catalyst of claim 9 , wherein the alkaline earth component is selected from barium, magnesium, calcium, and combinations thereof.
11. The catalyst of claim 1 , wherein the alkaline earth component is barium.
12. The catalyst composite of claim 1 , wherein the copper and alkaline earth component are exchanged into the 8-ring small pore molecular sieve.
13. The catalyst of claim 12 , wherein the catalyst exhibits higher NO x conversion at 200° C. than a catalyst comprising copper promoted aluminosilicate zeolite that is not promoted with an alkaline earth component tested under similar conditions.
14. The catalyst of claim 12 wherein the copper loading is in the range of 1 and 10% by weight and the alkaline earth component loading is less than 5% by weight.
15. The catalyst of claim 12 , wherein the copper loading is in the range of 2 and 8% by weight and the alkaline earth component loading is less than 2.5% by weight.
16. The catalyst of claim 12 , wherein the copper loading is in the range of 2 and 4% and the alkaline earth component loading is less than 1.5% by weight.
17. The catalyst of claim 7 , wherein the zeolite has a silica to alumina molar ratio is in the range of 5 and 100.
18. The catalyst 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 550° C.
19. 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 catalyst comprising an 8-ring small pore molecular sieve promoted with copper and an alkaline earth component, wherein the 8-ring small more molecular sieve has a crystallite size in the range of from 10 nanometers to 100 micrometers, and wherein the alkaline earth component is present in an amount of less than 5% by weight.
20. The method of claim 19 , wherein the 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.