Manganese-containing diesel oxidation catalyst
An oxidation catalyst composite, methods, and systems for the treatment of exhaust gas emissions from a diesel engine are described. More particularly, an oxidation catalyst composite including a first washcoat comprising a zeolite, Pt, and first refractory metal oxide support containing manganese, a second washcoat comprising a second refractory metal oxide support, a Pt component and a Pd component, and a third washcoat comprising palladium and a rare earth oxide component is described.
1. An oxidation catalyst composite for abatement of exhaust gas emissions from a lean bum engine comprising:
a carrier substrate having a length, an inlet end and an outlet end, an oxidation catalyst catalytic material on the carrier substrate, the oxidation catalyst catalytic material comprising:
a first washcoat including a mixture of a zeolite and a first refractory metal oxide support, the first refractory metal oxide impregnated with Pt and optionally Pd, wherein the first refractory metal oxide support further contains Mn that is present in the first refractory metal oxide support as surface-dispersed manganese oxide or as discrete manganese oxide particles;
a second washcoat including a second refractory metal oxide support, a platinum (Pt) component and a palladium (Pd) component in a ratio of Pt:Pd in the range of about 10:1 to 1:10; and
a third washcoat comprising palladium and a rare earth oxide component, the third washcoat being substantially free of platinum;
wherein the oxidation catalyst composite is effective to abate hydrocarbon and carbon monoxide, and to oxidize NO to NO 2 in the lean burn engine exhaust.
2. The oxidation catalyst composite of claim 1 , wherein the Pt:Pd ratio of the first washcoat is in the range of 1:0 to 10:1.
3. The oxidation catalyst composite of claim 1 , wherein the first washcoat is substantially free of palladium.
4. The oxidation catalyst composite of claim 2 , wherein the palladium component is present in an amount in the range of about 0.1 g/ft 3 to about 10 g/ft 3 .
5. The oxidation catalyst composite of claim 1 , wherein the Mn content of the first washcoat is in the range of 0.1% to 20% by weight.
6. The oxidation catalyst composite of claim 5 , wherein the Mn content is in the range of 3 to 10% by weight.
7. The oxidation catalyst composite of claim 1 , wherein the Mn oxide is derived from a soluble Mn species or from bulk Mn oxides.
8. The oxidation catalyst composite of claim 7 , wherein the soluble Mn species is selected from the group consisting of Mn acetate, Mn nitrate, Mn sulfate, and combinations thereof.
9. The oxidation catalyst composite of claim 7 , wherein the bulk Mn oxide is selected from the group consisting of MnO, MnO 3 , MnO 2 , and combinations thereof.
10. The oxidation catalyst of claim 1 , wherein the first refractory metal oxide support comprises alumina, silica, zirconia, titania, ceria, or combinations thereof.
11. The oxidation catalyst composite of claim 1 , wherein the first washcoat comprises Pt in an amount in the range of about 10 g/ft 3 to 100 g/ft 3 .
12. The oxidation catalyst composite of claim 11 , wherein the first washcoat comprises Pd in an amount in the range of about 0.1 g/ft 3 to about 10 g/ft 3 .
13. The oxidation catalyst composite of claim 1 , wherein the first washcoat comprises a hydrothermally stable zeolite in the form of 6 to 12 member ring structures selected from the group consisting of ZSM-5, beta, mordenite, Y zeolite, chabazite, ferrierite, and combinations thereof.
14. The oxidation catalyst composite of claim 1 , wherein the second refractory metal oxide support comprises alumina, silica, zirconia, titania, ceria, or combinations thereof.
15. The oxidation catalyst composite of claim 14 , wherein the second washcoat comprises a Pt component in an amount in the range of about 10 g/ft 3 to 100 g/ft 3 .
16. The oxidation catalyst composite of claim 14 , wherein the second washcoat comprises a Pd component in an amount in the range of about 10 g/ft 3 to 100 g/ft 3 .
17. The oxidation catalyst composite of claim 1 , wherein the first washcoat is substantially free of barium, and the second washcoat is substantially free of zeolite.
18. The oxidation catalyst composite of claim 1 , wherein the third washcoat comprises a rare earth oxide component selected from the group consisting of Ce, Nd, Y, Pr, Zr, La, and combinations thereof.
19. The oxidation catalyst composite of claim 18 , wherein the rare earth oxide component comprises ceria and is present in an amount of at least 80% by weight.
20. The oxidation catalyst composite of claim 19 , wherein ceria is present in an amount of at least 99% by weight.
21. The oxidation catalyst composite of claim 20 , wherein the third washcoat comprises a Pd component in an amount in the range of about 10 g/ft 3 to 100 g/ft 3 supported on the rare earth oxide component.
22. The oxidation catalyst composite of claim 1 , wherein the first, second and third washcoats of the catalyst composite can be layered or zoned, and wherein the carrier substrate is a flow-through monolith substrate.
23. The oxidation catalyst composite of claim 22 , wherein the third washcoat is coated on the carrier substrate, the second washcoat is coated on top of the third washcoat, and the first washcoat is coated on top of the second washcoat.
24. The oxidation catalyst composite of claim 22 , wherein the second washcoat is coated on the inlet end of the carrier substrate, the third washcoat is coated on the outlet end of the carrier substrate, and the first washcoat is coated on top of the second washcoat and the third washcoat.
25. The oxidation catalyst composite of claim 1 , wherein the carrier substrate comprises a flow-through monolith.
26. A method for treating a diesel engine exhaust gas stream, the method comprising contacting the diesel engine exhaust gas stream with the oxidation catalyst composite of claim 1 .
27. The method of claim 26 , further comprising passing the diesel engine exhaust gas stream to an SCR catalyst composition immediately downstream from the oxidation catalyst.
28. The method of claim 27 , wherein the SCR catalyst composition is disposed on a wall flow monolith.
29. A system for treatment of a lean burn engine exhaust gas stream including hydrocarbons, carbon monoxide, and other exhaust components, the system comprising:
an exhaust conduit in fluid communication with the lean bum engine via an exhaust manifold;
the oxidation catalyst composite of claim 1 , wherein the carrier substrate is a flow through substrate; and
a catalyzed soot filter and an SCR catalyst located downstream from the oxidation catalyst.
30. The system of claim 29 , wherein the SCR catalyst is coated onto the catalyzed soot filter.
31. The system of claim 29 , wherein the SCR catalyst is on a flow through substrate immediately downstream from the oxidation catalyst composite and the catalyzed soot filter is downstream from the SCR catalyst.