8-ring small pore molecular sieve with promoter to improve low temperature performance
US-8961914-B2 · Feb 24, 2015 · US
US9561469B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9561469-B2 |
| Application number | US-201514665051-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 23, 2015 |
| Priority date | Mar 24, 2014 |
| Publication date | Feb 7, 2017 |
| Grant date | Feb 7, 2017 |
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Provided is a method for reducing N 2 O emissions in an exhaust gas comprising contacting an exhaust gas containing NH 3 and an inlet NO concentration with an SCR catalyst composition containing small pore zeolite having an SAR of about 3 to about 15 and having about 1-5 wt. % of an exchanged transition metal.
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What is claimed is: 1. A method for reducing N 2 O emissions in an exhaust gas comprising contacting an exhaust gas containing NH 3 and an inlet NO concentration with an SCR catalyst composition containing small pore zeolite having an SAR of about 3 to about 15 and having about 1 - 5 wt. % of an exchanged transition metal to produce a purified gas containing an outlet NO concentration and an outlet N 2 O concentration, a. wherein the inlet NO concentration and outlet NO concentration have a relative ratio of > about 4, b. wherein the inlet NO concentration and outlet N 2 O concentration have a relative ratio of > about 50, and c. wherein the small pore zeolite has a framework selected from AD, AFT, and AFX. 2. The method of claim 1 , wherein the inlet NO concentration and outlet NO concentration have a relative ratio of > about 5. 3. The method of claim 1 , wherein the inlet NO concentration and outlet NO concentration have a relative ratio of > about 10. 4. The method of claim 1 , wherein the inlet NO concentration and outlet N 2 O concentration have a relative ratio of > about 80. 5. The method of claim 4 , wherein the inlet NO concentration and outlet N 2 O concentration have a relative ratio of > about 100. 6. The method of claim 1 , wherein the transition metal is copper. 7. The method of claim 1 , wherein the small pore zeolite has a SAR of about 5 to about 9. 8. The method of claim 1 , wherein the small pore zeolite has a SAR of about 10 to about 15. 9. The method of claim 1 , wherein the small pore zeolite has a framework selected from AFT and AFX. 10. The method of claim 1 , wherein the small pore zeolite has an AEI framework. 11. The method of claim 1 , wherein the NO and NO 2 are present in a ratio of about 4:1 to about 1:3by volume. 12. The method of claim 1 , wherein the NH 3 is present in exhaust gas entering the SCR catalyst at an NH 3 /NO ratio of about 0.5:1 to about 1:2 and an NH 3 /NO 2 ratio of about 1:1 to about 6:3. 13. A system for treating an exhaust gas comprising, in series and in fluid communication, a diesel oxidation catalyst, a source of nitrogen-based reductant, and an SCR catalyst, wherein the SCR catalyst comprises a small pore zeolite having a framework selected from AEI, AFX and AFT, having an SAR of about 3 to about 15and having about 1 - 5 wt. % of an exchanged transition metal, and wherein the SCR catalyst is coated on a honeycomb wall-flow filter or flow-through monolith or is an extruded honeycomb body.
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