Monometallic rhodium-containing four-way conversion catalysts for gasoline engine emissions treatment systems

1. An emission treatment system downstream of a gasoline direct injection engine for treatment of an exhaust stream comprising hydrocarbons, carbon monoxide, nitrogen oxides, and particulates, the emission treatment system comprising:

a close-coupled three-way conversion (TWC) composite comprising a first TWC catalytic material supported on a flow-through substrate; and

a catalyzed particulate filter located downstream of the close-coupled TWC composite, the catalyzed particulate filter comprising a second TWC catalytic material that permeates walls of a particulate filter,

wherein the second TWC catalytic material comprises rhodium as the only platinum group metal, and, relative to total support weight, a support comprising more than 20 wt. % ceria,

wherein the catalyzed particulate filter has a coated porosity that is less than an uncoated porosity of the particulate filter, and

wherein the coated porosity is in a range of from 75% to 98% of the uncoated porosity.

2. The system of claim 1 , wherein the particulate filter has a mean pore diameter in a range of from 13 μm to 25 μm.

3. The system of claim 1 wherein the particulate filter has a wall thickness in a range of from 6 mils (152 μm) to 14 mils (356 μm) and an uncoated porosity in a range of from 55% to 70%; and

wherein the uncoated porosity is a percentage of volume of pores of the particulate filter relative to volume of the particulate filter.

4. The system of claim 1 , having no layering of catalytic material on the surface of the walls of the particulate filter except optionally in areas of overlapped washcoat.

5. The system of claim 1 , wherein the coated porosity is linearly proportional to a washcoat loading of the TWC catalytic material.

6. The system of claim 1 , wherein the coated porosity is in a range of from 80% to 95% of the uncoated porosity.

7. The system of claim 1 , wherein a coated backpressure of the catalyzed particulate filter is non-detrimental to performance of the engine.

8. The system of claim 1 , wherein the second TWC catalytic material has a d90 average particle diameter of in a range of from 2.5 μm to 8 μm.

9. The system of claim 1 , wherein the second TWC catalytic material is formed from a single washcoat composition that permeates an inlet side, an outlet side, or both of the particulate filter.

10. The system of claim 1 , wherein a first single washcoat layer is present on the inlet side along up to a range of from 0 to 100% of the axial length of the particulate filter from the upstream end,

wherein a second single washcoat layer is present on the outlet side along up to a range of from 0% to 100% of the axial length of the particulate filter from the downstream end, and

wherein at least one of the first and single washcoat layers is present in an amount of >0%.

11. The system of claim 10 , wherein a first single washcoat layer is present on the inlet side along up to a range of from 50% to 100% of the axial length of the particulate filter from the upstream end, and

wherein a second single washcoat layer is present on the outlet side along up to a range of from 50% to 100% of the axial length of the particulate filter from the downstream end.

12. The system of claim 11 , wherein the first single washcoat layer is present on the inlet side along up to a range of from 50% to 55% of the axial length of the particulate filter from the upstream end, and

wherein the second single washcoat layer is present on the outlet side along up to a range of from 50% to 55% of the axial length of the particulate filter from the downstream end.

13. The system of claim 1 , wherein a single washcoat layer is present on the inlet side along up to 100% of the axial length of the particulate filter from the upstream end and there is not a washcoat layer on the outlet side.

14. The system of claim 1 , wherein a single washcoat layer is present on the outlet side along up to 100% of the axial length of the particulate filter from the downstream end and there is not a washcoat layer on the inlet side.

15. The system of claim 1 , comprising the second TWC catalytic material in an amount in a range of from 0.17 g/in 3 to 5 g/in 3 (10 g/L to 300 g/L).

16. The system of claim 1 , wherein the second TWC catalytic material consists essentially of rhodium, ceria or a ceria composite, and alumina.

17. The system of claim 1 , comprising the second TWC catalytic material in an amount in a range of from 0.25 g/in 3 to 1.5 g/in 3 .

18. The system of claim 1 , wherein the support of the second TWC comprises from 30 wt % to 60 wt. % ceria.

19. A catalyzed particulate filter located in an emission treatment system downstream of a gasoline direct injection engine for treatment of an exhaust stream comprising hydrocarbons, carbon monoxide, nitrogen oxides, and particulates and downstream of a three-way conversion (TWC) composite comprising a first TWC catalytic material on a flow-though substrate, the catalyzed particulate filter comprising:

a particulate filter having a wall thickness in a range of from 6 mils (152 μm) to 14 mils (356 μm) and a porosity in the range of from 55% to 70%; and

a second three-way conversion (TWC) catalytic material in an amount in a range of from 0.17 g/in 3 to 5 g/in 3 (10 g/L to 300 g/L), the second TWC catalytic material comprising rhodium as the only platinum group metal,

wherein the catalyzed particulate filter has a coated porosity that is less than an uncoated porosity of the particulate filter, the coated porosity is in a range from 75% to 98% of the uncoated porosity, and a coated backpressure that is substantially the same as an uncoated backpressure of the particulate filter.

20. The filter of claim 19 , wherein the wall thickness is 8 mils,

wherein the amount of the second three-way conversion (TWC) catalytic material is in a range of from 0.17 g/in 3 to 1.5 g/in 3 (10 g/L to 90 g/L), the second TWC catalytic material comprising rhodium as the only platinum group metal; and

the particulate filter has a mean pore size distribution in a range of from 13 μm to 25 μm.

21. A method of treating an exhaust gas comprising hydrocarbons, carbon monoxide, nitrogen oxides, and particulates, the method comprising situating the filter of claim 19 downstream of a gasoline direct injection engine and a three-way conversion (TWC) composite comprising a first TWC catalytic material on a flow-through substrate,

wherein upon operation of the engine, exhaust gas from the gasoline direct injection engine contacts the catalyzed particulate filter.

22. A method of making emission treatment system for a gasoline direct injection engine, the method comprising:

positioning a three-way conversion (TWC) composite comprising a first TWC catalytic material on a flow-through substrate downstream of the gasoline direct injection engine; and

positioning the catalyzed particulate filter downstream of the TWC composite,

wherein the catalyzed particulate filter comprises a second three-way conversion (TWC) catalytic material permeating walls of a particulate filter, the particulate filter having a wall thickness in a range of from 6 mils (152 μm) to 14 mils (356 μm) and a porosity in a range of from 55% to 70%,

wherein the second TWC catalytic material comprises rhodium as the only platinum group metal, and

wherein the catalyzed particulate filter has a coated porosity that is less than an uncoated porosity of the particulate filter, and wherein the coated porosity is in a range of from 75% to 98% of the uncoated porosity.