IP Library Granted Patent US 8,906,820
Granted Patent B2
US 8,906,820 · App. 13/567,705 · Granted Dec 9, 2014

Transition metal/zeolite SCR catalysts

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Quick Facts
Patent No.
US 8,906,820
App. No.
13/567,705
Granted
Dec 9, 2014
Kind
B2
Abstract

A method of converting nitrogen oxides in a gas to nitrogen by contacting the nitrogen oxides with a nitrogenous reducing agent in the presence of a zeolite catalyst containing at least one transition metal, wherein the zeolite is a small pore zeolite containing a maximum ring size of eight tetrahedral atoms, wherein the at least one transition metal is selected from the group consisting of Cr, Mn, Fe, Co, Ce, Ni, Cu, Zn, Ga, Mo, Ru, Rh, Pd, Ag, In, Sn, Re, Ir and Pt.

Claims (16)

1. A catalyst for treating exhaust gas comprising an aluminosilicate molecular sieve having a silica-to-alumina ratio of about 8 to about 150, having an AEI framework and containing from 0.5 to 5 wt %, based on the total weight of the molecular sieve, of at least one ion exchanged transition metal selected from Cr, Mn, Fe, Co, Ce, Ni, Cu, Zn, Ga, Mo, Ru, Rh, Pd, Ag, In, Sn, Re, Ir and Pt and combinations thereof, based on the total weight of the molecular sieve, the catalyst effective to promote the reaction of NH 3 with NO x to form nitrogen and water, selectively.

2. The catalyst of claim 1 , wherein said catalyst comprises a second molecular sieve having a second framework.

3. The catalyst of claim 2 , wherein said transition metal is selected from Cu and Fe.

4. The catalyst of claim 2 , wherein said second framework is CHA.

5. The catalyst of claim 4 , wherein said aluminosilicate molecular sieve comprising an AEI framework is SSZ-39.

6. The catalyst of claim 5 , wherein said second molecular sieve is a SAPO-34 isotype.

7. The catalyst of claim 4 , further comprising a medium, large, or meso-pore molecular sieve.

8. A catalytic washcoat comprising a catalyst according to claim 4 , and further comprising at least one binder selected from alumina, silica, non-zeolite silica-alumina, natural clay, TiO 2 , ZrO 2 , and SnO 2 .

9. A catalytic article comprising a catalytic washcoat according to claim 8 coated on a substrate selected from a metal flow-through substrate, a ceramic flow-through substrate, a wall-flow filter, a sintered metal filter, and a partial filter.

10. A catalytic article comprising an extruded-type flow through honeycomb formed from an extrudate comprising a catalyst according to claim 4 .

11. The catalytic article of claim 10 further comprising a transition metal promoted zeolite coating.

12. The catalyst of claim 1 , wherein said transition metal is selected from Cu and Fe.

13. A catalytic washcoat comprising a catalyst according to claim 1 , and further comprising at least one binder selected from alumina, silica, non-zeolite silica-alumina, natural clay, TiO 2 , ZrO 2 , and SnO 2 .

14. A catalytic article comprising a catalytic washcoat according to claim 13 coated on a substrate selected from a metal flow-through substrate, a ceramic flow-through substrate, a wall-flow filter, a sintered metal filter, and a partial filter.

15. The catalytic article of claim 13 further comprising a transition metal promoted zeolite coating.

16. A catalytic article comprising an extruded-type flow through honeycomb formed from an extrudate comprising a catalyst according to claim 1 .

Assignments (2)
CHANGE OF ADDRESS Recorded Jan 14, 2026
From: JOHNSON MATTHEY PUBLIC LIMITED COMPANY
To: JOHNSON MATTHEY PUBLIC LIMITED COMPANY
Reel/Frame 074703/0733 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 31, 2014
From: ANDERSEN, PAUL; CHEN, HAI-YING; FEDEYKO, JOSEPH; BAILIE, JILLIAN; RAJARAM, RAJ; CASCI, JOHN; FOO, RODNEY
To: JOHNSON MATTHEY PUBLIC LIMITED COMPANY
Reel/Frame 034077/0814 →