Small Pore Molecular Sieve Supported Copper Catalysts Durable Against Lean/Rich Aging for the Reduction of Nitrogen Oxides
US-2016038876-A1 · Feb 11, 2016 · US
US9561468B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9561468-B2 |
| Application number | US-201214391926-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 27, 2012 |
| Priority date | Apr 27, 2012 |
| Publication date | Feb 7, 2017 |
| Grant date | Feb 7, 2017 |
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The invention provides a method and system for the purification of exhaust gas from an internal combustion engine, comprising a filter and a SCR catalyst. The filter is periodically regenerated increasing the temperature of the exhaust gas up to 850° C. and the water vapor content up to 100% by volume. The SCR catalyst comprises a hydrothermally microporous stable zeolite and/or zeotype having the AEI type framework and being promoted with copper.
Opening claim text (preview).
The invention claimed is: 1. Method for the purification of exhaust gas from an internal combustion engine, comprising reducing the content of soot in the exhaust gas by passing the gas through a filter; subsequently reducing the content of nitrogen oxides in presence of ammonia or a precursor thereof in contact with a catalyst being active in NH 3 -SCR; periodically regenerating the filter by burning of soot captured in the filter and thereby increasing temperature of the exhaust gas up to 850° C. and water vapour content up to 100% by volume; and passing the exhaust gas from the filter through the catalyst during the regeneration of the filter, wherein the catalyst comprises a hydrothermally microporous stable zeolite and/or zeotype having the AEI type framework and being promoted with copper, and maintains 80% of the initial reduction of nitrogen oxides at 250° C. after the catalyst has been exposed to a water vapour content of 100% in the exhaust gas for 13 hours. 2. The method of claim 1 , wherein the atomic copper to aluminium ratio is between about 0.01 and about 1 for the zeolite and the atomic copper to silicon ratio is between 0.01 and about 1 for the zeotype. 3. The method of claim 1 , wherein the atomic ratio of silicon to aluminium is between 5 and 50 for the zeolite and between 0.02 and 0.5 for the zeotype. 4. The method of claim 1 , wherein 80% of the initial reduction of nitrogen oxides at 250° C. is maintained after the catalyst has been exposed to a temperature of 750° C. 5. The method of claim 1 , wherein at least 80 to 90% of the initial microporosity is maintained after aging at 600° C., and at least 30 to 40% is maintained after aging at 750° C. 6. The method of claim 3 , wherein the catalyst is an aluminosilicate zeolite SSZ-39 and/or silicoaluminum phosphate SAPO-18.
for removing nitrogen oxides by selective catalytic reduction [SCR] using a reducing agent in a lean exhaust gas · CPC title
Catalyst supported on particulate filters · CPC title
Nitrogen oxides other than dinitrogen oxide · CPC title
Exhaust gas flow channels or chambers being at least partly formed in the structural parts of the engine or machine (using structural parts of the vehicle B60K13/06) · CPC title
Copper · CPC title
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