Filter substrate comprising zone-coated catalyst washcoat

Patent metadata

Field	Value
Publication number	US-9366166-B2
Application number	US-201414260405-A
Country	US
Kind code	B2
Filing date	Apr 24, 2014
Priority date	Apr 24, 2013
Publication date	Jun 14, 2016
Grant date	Jun 14, 2016

Abstract

A catalyzed filter for filtering particulate matter from exhaust gas emitted from a positive ignition internal combustion engine comprises a ceramic porous wall-flow filter substrate having a total substrate length and having inlet channels defined in part by ceramic inlet wall surfaces and outlet channels defined in part by ceramic outlet wall surfaces, wherein the inlet surfaces are separated from the outlet surfaces by a first porous structure containing pores of a first mean pore size, wherein the porous substrate is coated in part with a catalyst washcoat composition, wherein a second porous structure of a washcoated part of the porous substrate contains pores of a second mean pore size, wherein the second mean pore size is less than the first mean pore size, which catalyst washcoat composition being disposed in a first zone comprising the inlet surfaces of a first substrate length less than the total substrate length, wherein a second zone comprising the outlet surfaces of a second substrate length contains no washcoat and wherein the sum of the substrate length in the first zone and the substrate length in the second zone is >100%.

First claim

The invention claimed is:

1. A catalysed filter for filtering particulate matter from exhaust gas emitted from a positive ignition internal combustion engine, which filter comprising a ceramic porous wall-flow filter substrate having a total substrate length and having inlet channels defined in part by ceramic inlet wall surfaces and outlet channels defined in part by ceramic outlet wall surfaces, wherein the inlet surfaces are separated from the outlet surfaces by a first porous structure containing pores of a first mean pore size, wherein the porous substrate is coated in part with a catalyst washcoat composition, wherein a second porous structure of a washcoated part of the porous substrate contains pores of a second mean pore size, wherein the second mean pore size is less than the first mean pore size, which catalyst washcoat composition being disposed in a first zone comprising the inlet surfaces of a first substrate length less than the total substrate length, wherein a second zone comprising the outlet surfaces of a second substrate length contains no washcoat and wherein the sum of the substrate length in the first zone and the substrate length in the second zone is >100%.

2. A filter according to claim 1 , wherein the catalyst washcoat composition is selected from the group consisting of a three-way catalyst washcoat composition, an oxidation catalyst washcoat composition, a NO x absorber catalyst washcoat composition and a selective catalytic reduction (SCR) catalyst washcoat composition.

3. A filter according to claim 2 , wherein the NO absorber catalyst washcoat composition comprises: a mixture of rhodium supported on a zirconia-based mixed oxide, a ceria-zirconia mixed oxide or an optionally stabilised alumina; and platinum and/or palladium supported on an alumina-based high surface area support and ceria or a mixed oxide comprising ceria and an alkaline earth metal, an alkali metal or a lanthanide is supported on the ceria or mixed oxide comprising ceria.

4. A filter according to claim 2 , wherein the SCR catalyst washcoat composition comprises Cu, Fe and/or Ce supported on or exchanged into a synthetic aluminosilicate zeolite molecular sieve selected from the group consisting of AEI, MFI (ZSM-5), ERI, mordenite, ferrierite, BEA, Y, CHA and LEV.

5. A filter according to claim 2 , wherein the catalyst washcoat composition is a three-way catalyst washcoat composition, an oxidation catalyst washcoat composition or a NO absorber catalyst washcoat composition, wherein a total platinum group metal loading in the first zone is >50 gft −3 .

6. A filter according to claim 1 , wherein the catalyst washcoat composition is a three-way catalyst washcoat composition.

7. A filter according to claim 6 , wherein the three-way catalyst washcoat composition comprises at least one platinum group metal supported on a high surface area oxide, and an oxygen storage component.

8. A filter according to claim 7 , wherein the at least one platinum group metal is selected from the group consisting of (i) platinum and rhodium; (ii) palladium and rhodium; (iii) platinum, palladium and rhodium; (iv) palladium only; and (v) rhodium only.

9. A filter according to claim 1 , wherein the washcoat loading in the first zone is greater than 1.60 gin −3 .

10. A filter according to claim 1 , wherein the substrate zone length in the first zone is 25 to 75% of the total substrate length.

11. A filter according to claim 10 , wherein the substrate zone length in the first zone is <45% of the total substrate length.

12. A filter according to claim 1 , comprising a surface catalyst washcoat composition comprising solid washcoat particles, wherein a catalyst washcoat composition layer substantially covers surface pores of the porous structure and the pores of the second mean pore size of the washcoated porous substrate are defined in part by spaces between the particles (interparticle pores) in the catalyst washcoat composition.

13. A filter according to claim 12 , wherein a D90 size of the solid washcoat particles is in the range 10 to 40 μm.

14. A filter according to claim 12 , wherein a mean particle size (D50) of solid washcoat particles is in the range 1 to 20 μm.

15. A filter according to claim 1 , wherein the washcoat comprises solid washcoat particles, wherein the pores at a surface of the porous structure comprise a pore opening and the washcoat causes a narrowing of substantially all the surface pore openings.

16. A filter according to claim 15 , wherein a mean size (D50) of solid washcoat particles is less than a mean pore size of the porous substrate.

17. A filter according to claim 15 , wherein a D90 size of solid washcoat particles is in the range 4 to 6 μm.

18. A filter according to claim 15 , wherein a mean size (D50) of solid washcoat particles is in the range 1 to 3 μm.

19. A filter according to claim 1 , wherein the uncoated porous substrate has a porosity of >40%.

20. A filter according to claim 1 , wherein a first mean pore size of the porous structure of the porous substrate is from 8 to 45 μm.

21. A filter according to claim 1 , wherein the washcoat comprises solid washcoat particles, wherein the washcoat locates substantially within the porous structure of the porous substrate.

22. An exhaust system for a positive ignition internal combustion engine comprising a catalysed filter according to claim 1 , wherein the first zone is disposed upstream of the second zone.

23. An exhaust system according to claim 22 , wherein the exhaust system comprises a flow through monolith substrate comprising a three-way catalyst composition or a NO x absorber catalyst composition disposed upstream of the catalysed filter.

24. An exhaust system according to claim 22 , wherein the catalyst washcoat composition is a selective catalytic reduction (SCR) catalyst washcoat composition, which system comprising an injector means for injecting a nitrogenous reductant into flowing exhaust gas upstream of the catalysed filter.

25. A positive ignition engine comprising an exhaust system according to claim 22 .

26. A positive ignition engine comprising an exhaust system according to claim 25 , wherein the catalyst washcoat composition is a selective catalytic reduction (SCR) catalyst washcoat composition, which system comprising engine management means for controlling at least one engine cylinder to emit enriched exhaust gas for generating ammonia in situ on the flow through monolith substrate comprising a three-way catalyst composition or a NO x absorber catalyst composition disposed upstream of the catalysed filter.

27. A vehicle comprising a positive ignition engine according to claim 25 .

28. A method of simultaneously converting oxides of nitrogen and particulate matter in the exhaust gas of a positive ignition internal combustion engine, which method comprising the step of contacting the gas with a catalysed filter comprising a porous substrate having a total substrate length and having inlet surfaces and outlet surfaces, wherein the inlet surfaces are separated from the outlet surfaces by a first porous structure containing pores of a first mean pore size, wherein the porous substrate is coated in part with a catalyst washcoat composition, wherein a second porous structure of a washcoated part of the porous substrate contains pores of a second mean pore size, wherein the second mean pore size is less than the f

Assignees

• Johnson Matthey Plc

Inventors

• Blakeman Philip Gerald
• Greenwell David Robert

Classifications

• F01N2510/0682

  having a discontinuous, uneven or partially overlapping coating of catalytic material, e.g. higher amount of material upstream than downstream or vice versa · CPC title

• F01N2330/06

  Ceramic, e.g. monoliths · CPC title

• F01N3/2828

  Ceramic multi-channel monoliths, e.g. honeycombs · CPC title

• F01N3/103

  Oxidation catalysts for HC and CO only · CPC title

• F01N3/101

  Three-way catalysts · CPC title