Zoned catalyst for treating exhaust gas

1. A system for treating an exhaust gas comprising:

a. a first SCR catalyst zone comprising vanadium loaded on a metal oxide selected from TiO 2 , ZrO 2 , SiO 2 , CeO 2 , and Al 2 O 3 ; and

b. a second SCR catalyst zone comprising a copper loaded small-pore molecular sieve, wherein the first SCR catalyst zone is disposed upstream of the second SCR catalyst zone with respect to normal exhaust gas flow through the system.

2. The system of claim 1 wherein the first SCR catalyst zone has a higher washcoat loading relative to the second SCR catalyst zone and the overall copper loading is higher than the overall vanadium loading.

3. The system of claim 1 , wherein the first SCR catalyst zone comprises about 0.5-4 weight percent vanadium (based on the total weight of the metal oxide) and the second SCR catalyst zone comprises about 1-4 weight percent copper (based on the total weight of the molecular sieve).

4. The system of claim 1 wherein the second SCR catalyst zone is free of iron.

5. The system of claim 1 , wherein the second SCR catalyst zone is free of transition metals other than copper.

6. The system of claim 1 , wherein the first and second SCR catalyst zones are free of platinum group metals.

7. The system of claim 1 , wherein the first SCR catalyst zone comprises an iron vanadate.

8. The system of claim 7 , wherein the first SCR catalyst zone further comprises tungsten.

9. The system of claim 1 , wherein the system is free of any exhaust gas treatment catalysts disposed between the first and second SCR catalyst zones.

10. The system of claim 1 , wherein the second SCR catalyst zone comprises a copper loaded molecular sieve having a framework selected from CHA, AEI, AFX and AFT.

11. The system of claim 1 , wherein the first and second SCR catalyst zones are coated on a flow-through honeycomb substrate having an inlet end, an outlet end, and an axial length measured from the inlet end to the outlet end, and the first and second SCR catalyst zones are adjacent or at least partially overlapping.

12. The system of claim 11 , wherein first zone extends from the inlet end to a first end point that is position about 10 to 40 percent of the axial length and wherein the second zone is about 20 to 90 percent of the axial length, provided that the first and second zones are adjacent or overlap by less than 90 percent of the axial length.

13. The system of claim 11 , further comprising an oxidation catalyst zone downstream of the second SCR catalyst zone.

14. The system of claim 13 , wherein the second SCR catalyst zone completely overlaps the oxidation catalyst zone.

15. The system of claim 1 , wherein the first SCR catalyst zone is an extruded vanadium catalyst honeycomb having an axial length and the second SCR zone is a washcoat that covers about 10 to 90 percent of the axial length.

16. The system of claim 15 , wherein the second SCR zone washcoat that covers about 60 to 90 percent of the axial length of the honeycomb.

17. The system of claim 1 , wherein the first SCR catalyst zone is on a wall-flow filter having an inlet side and an outlet side, and the second SCR catalyst zone is on a flow-through honeycomb substrate, provided that there are no intervening catalyst between the first SCR catalyst zone and the second SCR catalyst zone.

18. The system of claim 17 , further comprising a partial NOx absorber disposed upstream of the first SCR catalyst zone.

19. The system of claim 17 , further comprising an ammonia slip catalyst coated on the flow-through substrate downstream of the second SCR catalyst zone.

20. A method for treating an exhaust gas comprising the step of contacting, in series, a mixture of ammonia and exhaust gas derived from an internal combustion engine with (a) a first SCR zone comprising vanadium loaded on a metal oxide selected from TiO 2 , ZrO 2 , SiO 2 , CeO 2 , and Al 2 O 3 , and (b) a second SCR zone comprising a copper-loaded small pore molecular sieve.