Precipitated and calcined composition based on zirconium oxide and cerium oxide
US-2015375203-A1 · Dec 31, 2015 · US
US9630146B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9630146-B2 |
| Application number | US-201313908475-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 3, 2013 |
| Priority date | Jun 3, 2013 |
| Publication date | Apr 25, 2017 |
| Grant date | Apr 25, 2017 |
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A particulate filter for use in a vehicle engine exhaust is provided which includes a catalyst containing a mixture of nickel and copper. The catalyst is impregnated into the filter substrate, which is non-reactive with nickel and copper. When used in a vehicle exhaust gas treatment system, the catalyst on the filter improves soot burn-off at low temperatures, provides improved efficiency in reducing CO and NO x emissions over the use of conventional three-way-catalyst washcoats, and provides enhanced oxygen storage capacity (OSC) and water-gas-shift (WGS) functions.
Opening claim text (preview).
What is claimed is: 1. A particulate filter comprising: a filter substrate; and a catalyst comprising a mixture of nickel and copper impregnated in said substrate; wherein said filter substrate is non-reactive with nickel and copper; wherein said catalyst is substantially uniformly distributed through the substrate; and wherein said catalyst is directly loaded without a metal oxide washcoat. 2. An exhaust treatment system comprising: a particulate filter positioned in an exhaust stream; said particulate filter including an inlet, an outlet, and a plurality of porous walls; said particulate filter comprising a substrate including a catalyst impregnated therein comprising a mixture of nickel and copper; wherein said catalyst is substantially uniformly distributed through the substrate; and wherein said particulate filter substrate is non-reactive with copper and nickel; and wherein said catalyst is directly loaded without a metal oxide washcoat. 3. The exhaust treatment system of claim 2 having a CO conversion efficiency of at least 90% at a temperature between about 200° C. to about 1000° C. 4. The exhaust treatment system of claim 2 wherein said particulate filter includes a plurality of channels separated by the plurality of porous walls; wherein said channels are open at one end and plugged at an opposite end to trap particulates therein. 5. The exhaust treatment system of claim 2 wherein said catalyst provides a supplemental oxygen storage capacity of about 0.3 mole O to about 350.0 mole O per cubic feet. 6. The exhaust treatment system of claim 2 wherein said catalyst provides a water-gas-shift activity of 50 to 100% equilibrium conversion of CO at about 200° C. to 800° C. 7. The exhaust treatment system of claim 2 wherein said catalyst provides regeneration of said particulate filter at a temperature of between about 200° C. to 1000° C. and burns off from about 90% to 100% of soot deposited on said particulate filter. 8. The exhaust treatment system of claim 2 wherein said catalyst provides substantially complete oxidation of soot to CO 2 . 9. The exhaust treatment system of claim 2 wherein said catalyst provides sufficient oxygen storage capacity for soot and CO oxidation under oxygen-deficient conditions at a temperature between about 200° C. and 1000° C. 10. The exhaust treatment system of claim 2 wherein said catalyst provides sufficient oxygen storage capacity for NO x removal at a temperature between about 250° C. to 1000° C. 11. The exhaust treatment system of claim 2 wherein said substrate consists of a material selected from the group consisting of cordierite, aluminum titanate, silicon carbide, and mullites. 12. The exhaust treatment system of claim 2 wherein the catalyst is impregnated directly into the particulate filter, the catalyst permeates particulate filter walls and directly contacts deposited particulates. 13. The exhaust treatment system of claim 2 wherein said catalyst is substantially free of precious metals. 14. The exhaust treatment system of claim 2 wherein said mixture of nickel and copper is impregnated in said substrate at a loading of between about 1.0 and 50 wt. %. 15. The exhaust treatment system of claim 2 wherein said nickel is impregnated in said substrate at a loading of between about 0.1 to about 99 wt. %. 16. The exhaust treatment system of claim 15 wherein said nickel is impregnated in said substrate at a loading of about 10 wt. %. 17. The exhaust treatment system of claim 2 wherein said copper is contained on said substrate at a loading of between about 0.1 to about 99 wt. %. 18. The exhaust treatment system of claim 17 wherein said copper is impregnated in said substrate at a loading of about 10 wt. %. 19. The exhaust treatment system of claim 2 wherein a weight ratio of nickel to copper is from about 99:1 to 50:50. 20. The exhaust treatment system of claim 2 wherein said catalyst is directly impregnated in a material selected from the group consisting of cordierite, aluminum titanate, silicon carbide, and mullites.
Cross-Sectional Technologies · mapped topic
Nickel · CPC title
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characterised by a specific catalyst · CPC title
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