Multilayered catalyst compositions
A layered three-way conversion catalyst having the capability of simultaneously catalyzing the oxidation of hydrocarbons and carbon monoxide and the reduction of nitrogen oxides is disclosed. Engine exhaust treatment system and methods of using the same are also provided. In one or more embodiments, the catalyst supported on a carrier has three layers, where at least two of the layers are zoned to have an oxygen storage component being present in an upstream zone in an amount that is less than the oxygen storage component present in the downstream zone.
1. An exhaust gas treatment system comprising:
a catalytic material deposited on a carrier, the carrier comprising a longitudinal axis, an upstream end, a downstream end, having a length extending between the inlet end to the outlet end;
the catalytic material comprising:
an inner layer having an inner layer upstream zone and an inner layer downstream zone deposited on the carrier, the inner layer comprising a first support, being substantially free of precious metals, and, optionally, comprising a first oxygen storage component;
a middle layer having a middle layer upstream zone and a middle layer downstream zone, the middle layer comprising a second support, a palladium component, and, optionally, a second oxygen storage component; and
an outer layer having an outer layer upstream zone and an outer layer downstream zone, the outer layer comprising a third support, a rhodium component, and, optionally, a third oxygen storage component;
wherein at least two of the first oxygen storage component, the second oxygen storage component, and the third oxygen storage component are present in the inner layer downstream zone, the middle layer downstream zone, and the outer layer downstream zone, respectively, in amounts greater than in the inner layer upstream zone, the middle layer upstream zone, and the outer layer upstream zone, respectively.
2. The exhaust gas treatment system of claim 1 , wherein the middle layer upstream zone comprises a palladium component in an amount in the range of 50-90% by weight of the zone and the middle layer downstream zone comprises the palladium component in an amount in the range of 10-50% by weight of the zone.
3. The exhaust gas treatment system of claim 1 , wherein the outer layer upstream zone comprises a rhodium component in an amount in the range of 50-80% by weight of the zone and the middle layer downstream zone comprises the rhodium component in an amount in the range of 20-50% by weight of the zone.
4. The exhaust gas treatment system of claim 1 , wherein
the inner layer upstream zone is substantially free of an oxygen storage component and the inner layer downstream zone comprises the first oxygen storage component in an amount in the range of 10 to 50% by weight in the zone.
5. The exhaust gas treatment system of claim 1 , wherein
the first oxygen storage component is present in the inner layer upstream zone in an amount in the range of 0.1 to 20% by weight in the zone and in the inner layer downstream zone in an amount in the range of 10 to 50% by weight in the zone.
6. The exhaust gas treatment system of claim 1 , wherein
the middle layer upstream zone is substantially free of an oxygen storage component and the middle layer downstream zone comprises the second oxygen storage component in an amount in the range of 10 to 25% by weight in the zone.
7. The exhaust gas treatment system of claim 1 , wherein
the second oxygen storage component is present in the middle layer upstream zone in an amount in the range of 0.1 to 20% by weight in the zone and in the middle layer downstream zone in an amount in the range of 10 to 25% by weight in the zone.
8. The exhaust gas treatment system of claim 1 , wherein both the inner layer upstream zone and the outer layer downstream zone are substantially free of an oxygen storage component.
9. The exhaust gas treatment system of claim 8 , wherein the outer layer upstream zone comprises the third oxygen storage component in an amount in the range of 0.1 to 20% by weight in the zone.
10. The exhaust gas treatment system of claim 1 , wherein
the inner layer upstream zone is substantially free of an oxygen storage component; the middle layer upstream zone comprises the second oxygen storage component in an amount in the range of 0 to 25% by weight of the layer; and the outer layer upstream zone comprises the third oxygen storage component in an amount in the range of 0 to 20% by weight in the zone.
11. The exhaust gas treatment system of claim 1 , wherein
the inner layer upstream zone comprises the first oxygen storage component in an amount in the range of 0.1 to 20% by weight in the zone; the middle layer upstream zone comprises the second oxygen storage component in an amount in the range of 0 to 25% by weight of the layer; and the outer layer upstream zone comprises the third oxygen storage component in an amount in the range of 0 to 20% by weight in the zone.
12. The exhaust gas treatment system of claim 1 , wherein
the inner layer downstream zone comprises the first oxygen storage component in an amount in the range of 10 to 50% by weight of the layer; the middle layer downstream zone comprises the second oxygen storage component in an amount in the range of 10 to 25% by weight of the layer; and the outer layer downstream zone comprises the third oxygen storage component in an amount in the range of 0 to 20% by weight in the zone.
13. The exhaust gas treatment system of claim 1 , wherein the inner layer upstream zone, the middle layer upstream zone, the outer layer upstream zone, or combinations thereof begins from the upstream end and extends for no more than 50% of the substrate's length.
14. The exhaust gas treatment system of claim 1 , wherein the inner layer downstream zone, the middle layer downstream zone, or combinations thereof begins from the downstream end and extends for no more than 50% of the substrate's length.
15. The exhaust gas treatment system of claim 1 , wherein:
the first support of the inner layer comprises alumina in an amount in the range of 20 to 90% by weight of the layer; the first oxygen storage component comprises ceria; and the inner layer downstream zone comprises the first oxygen storage component in an amount in the range of 10 to 50% by weight of the zone;
the second support of the middle layer comprises alumina in an amount in the range of 20 to 70% by weight of the layer and palladium in an amount of 2% or less by weight of the layer; the second oxygen storage component comprises ceria; and the middle layer downstream zone comprises the second oxygen storage component in an amount in the range of 0.1 to 25% by weight of the zone; and
the third support of the outer layer comprises alumina in an amount in the range of 50 to 80% by weight of the layer and rhodium in an amount of 0.5% or less by weight of the layer; the third oxygen storage component comprises ceria; and the outer layer downstream zone comprises the third oxygen storage component in an amount in the range of 0.1 to 20% by weight of the zone.
16. The exhaust gas treatment system of claim 1 , wherein the inner layer, the middle layer, the outer layer, or combinations thereof further independently comprise platinum, palladium, rhodium, or combinations thereof.
17. The exhaust gas treatment system of claim 1 , wherein the inner layer, the middle layer, the outer layer, or combinations thereof are independently supported by an activated compound selected from the group consisting of alumina, silica-alumina, alumino-silicates, alumina-zirconia, and alumina-ceria.
18. The exhaust gas treatment system of claim 1 , wherein the outer layer upstream zone and the outer layer downstream zone have the same composition.
19. The exhaust gas treatment system of claim 1 , wherein the middle layer upstream zone and the middle layer downstream zone have the same composition.
20. The exhaust gas treatment system of claim 1 , wherein the inner layer upstream zone and the inner layer downstream zone have the same composition.
21. A method for oxidizing hydrocarbons, carbon monoxide, and nitrogen oxides comprising:
contacting a gaseous stream comprising the hydrocarbons, carbon monoxide, and nitrogen oxides with an exhaust gas treatment system comprising:
a catalytic material deposited on a carrier, the carrier comprising a longitudinal axis, an upstream end, a downstream end, having a length extending between the inlet end to the outlet end;
the catalytic material comprising:
an inner layer having an inner layer upstream zone and an inner layer downstream zone deposited on the carrier, the inner layer comprising a first support, being substantially free of precious metals, and, optionally, comprising a first oxygen storage component;
a middle layer having a middle layer upstream zone and a middle layer downstream zone, the middle layer comprising a second support, a palladium component, and, optionally, a second oxygen storage component; and
an outer layer having an outer layer upstream zone and an outer layer downstream zone, the outer layer comprising a third support, a rhodium component, and, optionally, a third oxygen storage component;
wherein at least two of the first oxygen storage component, the second oxygen storage component, and the third oxygen storage component are present in the inner layer downstream zone, the middle layer downstream zone, and the outer layer downstream zone, respectively, in amounts greater than in the inner layer upstream zone, the middle layer upstream zone, and the outer layer upstream zone, respectively.
22. The method of claim 21 , wherein the inner layer upstream zone, the middle layer upstream zone, the outer layer upstream zone, or combinations thereof begins from the upstream end and extends for no more than 50% of the substrate's length.
23. The method of claim 21 , wherein the inner layer downstream zone, the middle layer downstream zone, or combinations thereof begins from the downstream end and extends for no more than 50% of the substrate's length.