IP Library Granted Patent US 10,215,073
Granted Patent B2
US 10,215,073 · App. 15/574,910 · Granted Feb 26, 2019

Catalyzed soot filter for use in passive selective catalytic reduction

Inventors: Alfred Punke (Walle, DE); Gerd Grubert (Hannover, DE); Marcus Hilgendorff (Hannover, DE); Torsten Neubauer (Langenhagen, DE); Matthew Caudle (Hamilton, NJ); Yuejin Li (Edison, NJ)
Assignee: BASF Corporation
F01N3/2803B01D53/944B01D53/9418B01D53/9422B01D53/9477B01J23/42B01J23/44B01J29/763B01J29/783B01J35/0006B01J35/04B01J37/0234B01J37/0236B01J37/0244B01J37/04B01J37/08F01N3/035F01N3/2066F01N13/009B01D53/9481B01D2255/1021B01D2255/1023B01D2255/50B01D2255/9032B01D2255/9155B01D2255/9202F01N2510/068F01N2510/0682Y02T10/24
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Quick Facts
Patent No.
US 10,215,073
App. No.
15/574,910
Granted
Feb 26, 2019
Kind
B2
Abstract

The present invention relates to catalyzed soot filter comprising a porous wall flow substrate, a catalyst for selective catalytic reduction (SCR), a palladium component, and a platinum component, the wall flow substrate comprising an inlet end, an outlet end, a substrate axial length extending between the inlet end and the outlet end, and a plurality of channels defined by internal walls of the wall flow substrate, wherein the plurality of channels comprise inlet channels having an open inlet end and a closed outlet end, and outlet channels having a closed inlet end and an open outlet end, and the SCR catalyst is provided on the entire surface of the inlet channel walls and on at least a portion of the surface of the pores within the channel walls underneath the surface of the channel walls coated with the SCR catalyst.

Claims (30)

1. A catalyzed soot filter comprising a porous wall flow substrate, a catalyst for selective catalytic reduction (SCR), a palladium component, and a platinum component,

the wall flow substrate comprising an inlet end, an outlet end, a substrate axial length extending between the inlet end and the outlet end, and a plurality of channels defined by internal walls of the wall flow substrate, wherein the plurality of channels comprise inlet channels having an open inlet end and a closed outlet end, and outlet channels having a closed inlet end and an open outlet end,

wherein the SCR catalyst is on the entire surface of the inlet channel walls and on at least a portion of the surface of the pores within the channel walls underneath the surface of the channel walls coated with the SCR catalyst,

wherein the palladium component is on a portion of the surface of the inlet channel walls and on at least a portion of the surface of the pores within the channel walls underneath the surface of the portions of the channel walls coated with the palladium component,

wherein the portion of the inlet channel walls coated with the palladium component extends from the inlet end to x % of the substrate axial length with 0<x<100,

wherein the platinum component is on a portion of the surface of the outlet channel walls and on at least a portion of the surface of the pores within the channel walls within the surface of the portions of the channel walls coated with the platinum component, wherein the portion of the outlet channel walls coated with the platinum component extends from the outlet end to 100-x % of the substrate axial length.

2. The catalyzed soot filter of claim 1 , wherein x is in the range of from 5 to 95.

3. The catalyzed soot filter of claim 1 , wherein the porous wall flow substrate is a honeycomb substrate with alternately plugged inlet and outlet ends such that each wall of the wall flow substrate respectively has a first surface which is a surface of an inlet channel and a second surface which is a surface of an outlet channel.

4. The catalyzed soot filter of claim 1 , wherein the SCR catalyst comprises a zeolite.

5. The catalyzed soot filter of claim 4 , wherein the zeolite comprises a transition metal.

6. The catalyzed soot filter of claim 1 , wherein the average particle size D90 of the SCR catalyst is 25% or less of the average pore size of the walls of the substrate.

7. The catalyzed soot filter of claim 1 , wherein the catalyzed soot filter is contained in an emissions treatment system further comprising an internal combustion engine located upstream of the catalyzed soot filter, wherein the internal combustion engine is in fluid communication with the catalyzed soot filter.

8. The catalyzed soot filter of claim 7 , wherein the emissions treatment system further comprises a lean NO x , trap (LNT) in fluid communication with the catalyzed soot filter, wherein the LNT is located upstream of the catalyzed soot filter.

9. A method of preparing a catalyzed soot filter comprising

(i) providing a porous wall flow substrate comprising an inlet end, an outlet end, a substrate axial length extending between the inlet end and the outlet end, and a plurality of channels defined by internal walls of the wall flow substrate, wherein the plurality of channels comprise inlet channels having an open inlet end and a closed outlet end, and outlet channels having a closed inlet end and an open outlet end,

(ii) mixing a particulate support material with distilled water and subsequently adding an aqueous solution of a palladium compound thereto, wherein the resulting mixture is optionally milled for providing a first slurry comprising a palladium component, wherein said first slurry displays an average particle size D90 which is 25% or less of the average pore size of the walls of the porous wall flow substrate,

(iii) mixing a particulate support material with distilled water and subsequently adding an aqueous solution of a platinum compound thereto, wherein the resulting mixture is optionally milled for providing a second slurry comprising a platinum component, wherein said second slurry displays an average particle size D90 which is 25% or less of the average pore size of the walls of the porous wall flow substrate,

(iv) suspending a solid SCR catalyst in distilled water and optionally milling the resulting mixture for providing a third slurry, wherein said third slurry displays an average particle size D90 which is 25% or less of the average pore size of the walls of the porous wall flow substrate,

(v) coating a portion of the inlet channel walls of the wall flow substrate by immersing the inlet end of the wall flow substrate into the first slurry up to x % of the substrate axial length extending from the inlet end with 0<x<100,

(vi) removing the wall flow substrate from the first slurry and removing excess slurry from the inlet channels,

(vii) coating a portion of the outlet channel walls of the wall flow substrate by immersing the outlet end of the wall flow substrate into the second slurry up to 100-x % of the substrate axial length extending from the outlet end,

(viii) removing the wall flow substrate from the second slurry and removing excess slurry from the outlet channels,

(ix) coating the inlet channel walls of the wall flow substrate by immersing the inlet end of the wall flow substrate into the third slurry along the entire axial length of the substrate yet without allowing slurry to contact the face of the outlet end of the wall flow substrate,

(x) removing the wall flow substrate from the third slurry and removing excess slurry from the inlet channels, and

(xi) optionally drying and/or calcining the coated wall flow substrate.

10. A catalyzed soot filter, which is obtained according to a method of claim 9 .

11. A process for the treatment of emissions from an internal combustion engine, comprising:

directing exhaust gas from an internal combustion engine through the inlet channels of a catalyzed soot filter according to claim 1 .

12. The process of claim 11 , wherein prior to directing the exhaust gas stream into the catalyzed soot filter, the exhaust gas stream is contacted with a diesel oxidation catalyst (DOC).

13. The process of claim 12 , wherein prior to directing the exhaust gas stream into the catalyzed soot filter, the exhaust gas stream is contacted with a lean NO x trap (LNT).

Assignments (4)
NUNC PRO TUNC ASSIGNMENT Recorded Aug 8, 2024
From: BASF CORPORATION
To: BASF MOBILE EMISSIONS CATALYSTS LLC
Reel/Frame 068518/0394 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 11, 2018
From: BASF CATALYSTS GERMANY GMBH
To: BASF CORPORATION
Reel/Frame 047742/0597 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 25, 2018
From: CAUDLE, MATTHEW; LI, YUEJIN
To: BASF CORPORATION
Reel/Frame 047315/0827 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 25, 2018
From: PUNKE, ALFRED; GRUBERT, GERD; HILGENDORFF, MARCUS; NEUBAUER, TORSTEN
To: BASF CATALYSTS GERMANY GMBH
Reel/Frame 047315/0830 →
Continuity (2)
Provisional Application 62163396 · May 19, 2015
Related Publication 20180163596A1 · Jun 14, 2018