Iron-containing aluminosilicate zeolites and methods of making and using same
View Patent ↗There is disclosed iron-containing aluminosilicate zeolites having both framework iron and iron cations on the ion-exchange sites. There is also disclosed a direct synthesis method of making an iron-containing aluminosilicate zeolite, which does not require the use of an intermediate step, such as ion-exchange or impregnation. In addition, there is disclosed a method of using the iron-containing aluminosilicate zeolite disclosed herein in a selective catalytic reduction reaction, typically in the presence of ammonia, to reduce or remove nitric oxides from exhaust emissions.
1. A method of selective catalytic reduction of nitrogen oxides in exhaust gases, said method comprising:
at least partially contacting said exhaust gases with an iron-containing aluminosilicate zeolite, chosen from Beta, Y, mordenite, ferrierite and chabazite type zeolites, comprising both framework iron and extra-framework iron cations, wherein said zeolite has a silica-to-alumina ratio (SAR) of less than 60.
2. The method of claim 1 , wherein said selective catalytic reduction occurs in the presence of ammonia, urea, or sources thereof.
3. The method of claim 1 , wherein said iron is present in an amount ranging from 1 to 5% by weight of said zeolite.
4. The method of claim 1 , wherein said selective catalytic reduction of nitrogen oxides improves after hydrothermal aging said zeolite at 300 ° C. or higher.
5. The method of claim 1 , wherein said exhaust gas is automotive exhaust.
6. The method of claim 1 , wherein said exhaust gas is from a stationary source chosen from a power generation plant or a stationary diesel engine.
7. A method of selective catalytic reduction of nitrogen oxides in exhaust gases, said method comprising:
at least partially contacting said exhaust gases with an iron-containing aluminosilicate zeolite, chosen from Beta, Y, mordenite, ferrierite and chabazite type zeolites, comprising both framework iron and extra-framework iron cations, wherein said method exhibits a selective catalytic reduction of nitrogen oxides with NH 3 or urea of greater than 40% conversion at 250-300 ° C. in exhaust gases prior to aging or exposure to steam.
8. The method of claim 7 , wherein said iron is present in an amount ranging from 1 to 5% by weight of said zeolite.
9. The method of claim 7 , wherein said selective catalytic reduction of nitrogen oxides improves after hydrothermal aging said zeolite at 300 ° C. or higher.
10. The method of claim 7 , wherein said zeolite has a silica-to-alumina ratio (SAR) of less than 60.
11. The method of claim 7 , wherein said exhaust gas is automotive exhaust.
12. The method of claim 7 , wherein said exhaust gas is from a stationary source chosen from a power generation plant or a stationary diesel engine.
13. A method of selective catalytic reduction of nitrogen oxides in exhaust gases, said method comprising:
at least partially contacting said exhaust gases with an iron-containing aluminosilicate zeolite, chosen from Beta, Y, mordenite, ferrierite and chabazite type zeolites, comprising both framework iron and extra-framework iron cations,
wherein said zeolite has a silica-to-alumina ratio (SAR) of less than 60, and exhibits a selective catalytic reduction of nitrogen oxides with NH 3 or urea of greater than 40% conversion at 250-300 ° C. in exhaust gases prior to aging or exposure to steam.
14. The method of claim 13 , wherein said iron is present in an amount ranging from 1 to 5% by weight of said zeolite.
15. The method of claim 13 , wherein said selective catalytic reduction of nitrogen oxides improves after hydrothermal aging said zeolite at 300 ° C. or higher.
16. The method of claim 1 , wherein said exhaust gas is automotive exhaust, or said exhaust gas is chosen from a stationary source including a power generation plant or a stationary diesel engine.