WALL-FLOW FILTER COMPRISING CATALYTIC WASHCOAT

• US 20150152768A1
• Filed: 12/02/2014
• Published: 06/04/2015
• Est. Priority Date: 12/02/2013
• Status: Abandoned Application

• Current Assignee: Johnson Matthey PLC
• Original Assignee: Johnson Matthey PLC
• Inventors: CHANDLER, Guy Richard, COLLINS, Neil Robert, PHILLIPS, Paul Richard, ARULRAJ, Kaneshalingham, PREST, David William
• Application Number:
  US14/558,270
• Publication Number:
  US 20150152768A1
• Time in Patent Office: Days
• US Class Current: 1/1
• CPC Class Codes: B01D 2255/20761 Copper
• CPC Class Codes: B01D 2255/50 Zeolites
• CPC Class Codes: B01D 2255/504 ZSM 5 zeolites
• CPC Class Codes: B01D 2255/91 NOx-storage component incorporated in the catalyst
• CPC Class Codes: B01D 2255/912 HC-storage component incorporated in the catalyst
• CPC Class Codes: B01D 2255/9155 Wall flow filters
• CPC Class Codes: B01D 2258/012 Diesel engines and lean burn gasoline engines
• CPC Class Codes: B01D 46/247 of the cells
• CPC Class Codes: B01D 46/2476 Monolithic structures
• CPC Class Codes: B01D 46/2482 Thickness, height, width, length or diameter
• CPC Class Codes: B01D 53/94 by catalytic processes
• CPC Class Codes: B01D 53/9418 for removing nitrogen oxides by selective catalytic reduction [SCR] using a reducing agent in a lean exhaust gas
• CPC Class Codes: B01J 29/072 Iron group metals or copper
• CPC Class Codes: B01J 29/084 Y-type faujasite
• CPC Class Codes: B01J 29/146 Y-type faujasite
• CPC Class Codes: B01J 29/18 of the mordenite type
• CPC Class Codes: B01J 29/24 Iron group metals or copper
• CPC Class Codes: B01J 29/40 of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
• CPC Class Codes: B01J 29/46 Iron group metals or copper
• CPC Class Codes: B01J 29/50 of the erionite or offretite type, e.g. zeolite T, as exemplified by patent document US2950952
• CPC Class Codes: B01J 29/56 : Iron group metals or copper
• CPC Class Codes: B01J 29/7007 : Zeolite Beta
• CPC Class Codes: B01J 29/7015 : CHA-type, e.g. Chabazite, LZ-218
• CPC Class Codes: B01J 29/7023 : EUO-type, e.g. EU-1, TPZ-3 or ZSM-50
• CPC Class Codes: B01J 29/7038 : MWW-type, e.g. MCM-22, ERB-1, ITQ-1, PSH-3 or SSZ-25
• CPC Class Codes: B01J 29/7615 : Zeolite Beta
• CPC Class Codes: B01J 29/763 : CHA-type, e.g. Chabazite, LZ-218
• CPC Class Codes: B01J 29/7646 : EUO-type, e.g. EU-1, TPZ-3 or ZSM-50
• CPC Class Codes: B01J 29/7676 : MWW-type, e.g. MCM-22, ERB-1, ITQ-1, PSH-3 or SSZ-25
• CPC Class Codes: B01J 37/0246 : Coatings comprising a zeolite
• CPC Class Codes: C04B 2111/00793 : as filters or diaphragms
• CPC Class Codes: C04B 41/0072 : Heat treatment
• CPC Class Codes: C04B 41/4515 : application under vacuum or reduced pressure
• CPC Class Codes: C04B 41/4535 : applied as a solution, emulsion, dispersion or suspension
• CPC Class Codes: F01N 2330/06 : Ceramic, e.g. monoliths
• CPC Class Codes: F01N 3/2828 : Ceramic multi-channel monoliths, e.g. honeycombs
• CPC Class Codes: Y02A 50/20 : Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
• CPC Class Codes: Y02T 10/12 : Improving ICE efficiencies
• CPC Class Codes: Y10T 428/24157 : Filled honeycomb cells [e.g., solid substance in cavities, etc.]

Abstract

A catalysed honeycomb wall-flow filter for treating exhaust gas comprising particulate matter emitted from an internal combustion engine, which filter comprising a honeycomb substrate having a first end and a second end and comprising an array of interconnecting porous walls defining an array of longitudinally extending first channels and second channels, wherein the first channels are bordered on their sides by the second channels and have a larger hydraulic diameter than the second channels, wherein the first channels are end-plugged at a first end of the honeycomb substrate and the second channels are end-plugged at a second end of the honeycomb substrate, wherein channel wall surfaces of the first channels comprise an on-wall-type catalytic washcoat. The invention also relates to an exhaust system comprising the catalysed filter and to methods of making it.

Claims

1. A catalysed honeycomb wall-flow filter for treating exhaust gas comprising particulate matter emitted from an internal combustion engine, which filter comprising a honeycomb substrate having a first end and a second end and comprising an array of interconnecting porous walls defining an array of longitudinally extending first channels and second channels, wherein the first channels are bordered on their sides by the second channels and have a larger hydraulic diameter than the second channels, wherein the first channels are end-plugged at a first end of the honeycomb substrate and the second channels are end-plugged at a second end of the honeycomb substrate, wherein channel wall surfaces of the first channels comprise an on-wall-type catalytic washcoat.

2. A catalysed filter according to claim 1, wherein the catalytic washcoat on channel wall surfaces of the first channels additionally permeates the interconnecting porous walls thereof.

3. A catalysed filter according to claim 1, wherein a catalytic washcoat is located at on-wall surfaces, permeates the interconnecting porous wall or both at on-wall surfaces and permeating the interconnecting porous wall of the second channel walls.

4. A catalysed honeycomb substrate having a first end and a second end and comprising an array of interconnecting porous walls defining an array of longitudinally extending first channels and second channels, wherein the first channels are bordered on their sides by the second channels, wherein the first channels of the honeycomb substrate are open at both the first end and the second end of the honeycomb substrate and wherein the second channels are open at the first end of the honeycomb substrate but are blocked with end plugs at the second end of the honeycomb substrate;

and a first catalytic washcoat is disposed on surfaces of the porous channel walls of the first channels, permeates the porous channel walls of the first channels or is both disposed on a surface of the porous channel walls and permeates the porous channel walls of the first channels, which first catalytic washcoat being defined at one end by the second end of the honeycomb substrate.

5. A catalysed honeycomb wall-flow filter comprising the catalysed honeycomb substrate according to claim 4 having end plugs inserted in first channels at a first end of the honeycomb substrate and a second catalytic washcoat, which is disposed on surfaces of the porous channel walls of the second channels, permeates the porous channel walls of the second channels or is both disposed on a surface of the porous channel walls and permeates the porous channel walls of the second channels, which second catalytic washcoat being defined at one end by the first end of the wall-flow filter substrate.

6. A catalysed honeycomb substrate according to claim 4, wherein the first channels have a larger hydraulic diameter than the second channels.

7. A catalysed honeycomb substrate according to claim 4, wherein the first channels and the second channels have substantially the same hydraulic diameter.

8. A catalysed honeycomb substrate according to claim 4, wherein catalytic washcoat in the first channels or the second channels, is each selected from the group consisting of a hydrocarbon trap, a three-way catalyst, a NO_x absorber, an oxidation catalyst, a selective catalytic reduction (SCR) catalyst, a H₂S trap, an ammonia slip catalyst (ASC) and a lean NO_x catalyst.

9. A catalysed honeycomb substrate according to claim 4, wherein the catalytic washcoat of the first channels is a SCR catalyst.

10. A catalysed honeycomb substrate according to claim 8, wherein the or each catalytic washcoat comprises one or more molecular sieve.

11. A catalysed honeycomb substrate according to claim 10, wherein the at least one molecular sieve is a small, medium or large pore molecular sieve.

12. A catalysed honeycomb substrate according to claim 10, wherein the at least one molecular sieve is selected from the group consisting of AEI, ZSM-5, ZSM-20, ERI, LEV, mordenite, BEA, Y, CHA, MCM-22 and EU-1.

13. A catalysed honeycomb substrate according to claim 10, wherein the molecular sieve is un-metallised or is metallised with at least one metal selected from the group consisting of groups IB, IIB, IIIA, IIIB, IVB, VB, VIB, VIB and VIII of the periodic table.

14. A method of making a catalysed wall-flow filter substrate for treating exhaust gas comprising particulate matter emitted from an internal combustion engine, which method comprising providing a honeycomb flow-through substrate monolith having a first end and a second end, having physical properties and parameters pre-selected for use in a honeycomb wall-flow filter substrate and comprising an array of interconnecting porous walls defining an array of longitudinally extending first and second channels which are open at both the first end and the second end of the honeycomb flow-through substrate monolith, wherein the first channels are bordered on their sides by the second channels and have a larger hydraulic diameter than the second channels, contacting at least porous channel wall surfaces which define the first channels of the honeycomb flow-through substrate monolith with a liquid catalytic washcoat, wherein at least one of:

a liquid catalytic washcoat solids content;

a liquid catalytic washcoat rheology;

a porosity of the flow-through substrate monolith;

a mean pore size of the flow-through substrate monolith;

a liquid catalytic washcoat volumetric mean particle size; and

a liquid catalytic washcoat D90 (by volume), is pre-selected so that the liquid catalytic washcoat remains on a surface of the porous channel walls of the first channels or both remains on the surface of the porous channel walls and permeates the porous channel walls of the first channels;

drying and calcining the coated honeycomb flow-through substrate monolith; and

inserting end plugs into open ends of the first channels at the first end of the honeycomb flow-through substrate monolith and into open ends of the second channels at a second end of the honeycomb flow-through substrate monolith to form the catalysed wall-flow filter substrate.

18. A method according to claim 14, wherein the step of contacting the porous channel walls of the first channels is done by orienting the honeycomb substrate monolith such that the channels thereof are substantially vertical and introducing liquid catalytic washcoat into the channels from a lower end thereof.

19. A method according to claim 18, wherein the step of introducing the liquid catalytic washcoat from a lower end of the honeycomb substrate monolith is done by dipping the honeycomb substrate monolith into a bath of liquid catalytic washcoat.

20. A method according to claim 18, wherein the step of introducing the liquid catalytic washcoat from a lower end of the honeycomb substrate monolith is done by pushing a predefined quantity of liquid catalytic washcoat up into the honeycomb substrate monolith.

21. A method according to claim 18, wherein the step of introducing the liquid catalytic washcoat from a lower end of the honeycomb substrate is done by drawing liquid catalytic washcoat into the channels by application of a vacuum at an upper end of the honeycomb substrate monolith.

15. A method of making a catalysed wall-flow filter substrate for treating exhaust gas comprising particulate matter emitted from an internal combustion engine, which method comprising providing a honeycomb substrate monolith having a first end and a second end, having physical properties and parameters pre-selected for use in a honeycomb wall-flow filter substrate and comprising an array of interconnecting porous walls defining an array of longitudinally extending first and second channels, wherein the first channels are bordered on their sides by the second channels, wherein the first channels are open at both the first and the second end of the honeycomb substrate monolith and the second channels are open at the first end of the honeycomb substrate monolith but are blocked with end plugs at the second end thereof, contacting porous channel wall surfaces which define the first channels of the honeycomb substrate monolith with a liquid catalytic washcoat to produce a coated honeycomb substrate monolith, wherein at least one of:

a liquid catalytic washcoat solids content;

a liquid catalytic washcoat rheology;

a porosity of the honeycomb substrate monolith;

a mean pore size of the honeycomb substrate monolith;

a liquid catalytic washcoat volumetric mean particle size; and

a liquid catalytic washcoat D90 (by volume), is pre-selected so that at least some of the liquid catalytic washcoat remains on a surface of the porous channel walls of the first channels, permeates the porous channel walls of the first channels or both remains on the surface of the porous channel walls and permeates the porous channel walls of the first channels;

drying and calcining the coated honeycomb substrate monolith; and

inserting end plugs into open ends of the first channels at the first end of the honeycomb substrate monolith to form the catalysed wall-flow filter substrate.

16. A method according to claim 15, wherein the first channels have a larger hydraulic diameter than the second channels.

17. A method according to claim 15, wherein the first channels and the second channels have substantially the same hydraulic diameter.