Catalysts for gasoline lean burn engines with improved NH3-formation activity

Patent metadata

Field	Value
Publication number	US-8950174-B2
Application number	US-201113224675-A
Country	US
Kind code	B2
Filing date	Sep 2, 2011
Priority date	Sep 2, 2010
Publication date	Feb 10, 2015
Grant date	Feb 10, 2015

Abstract

Described is a catalyst comprising a substrate and a catalyst coating of two or more layers: (a) a first layer comprising Pd and Rh on the substrate; and (b) a second layer comprising Pt and/or Pd on the first layer; these layers each further comprising: one or more particulate support materials; one or more oxygen storage component (OSC) materials; and one or more nitrogen oxide storage materials comprising one or more elements selected from the group of alkali and/or alkaline earth metals, wherein the total amount of alkali and alkaline earth metals ranges from 0.18 to 2.0 g/in 3 calculated as the respective alkali metal oxides M 2 O and alkaline earth metal oxides MO. Also described is a method for the production of a catalyst, as well as a process for the treatment of a gas stream, in particular of an exhaust gas stream resulting from an internal combustion engine.

First claim

The invention claimed is:

1. A catalyst comprising a substrate and a catalyst coating, the catalyst coating comprising two or more layers, said layers comprising:
(a) a first layer provided on the substrate, said first layer comprising:
(a′) a layer containing Pd; and
(a″) a layer containing Rh; and

(b) a second layer provided on the first layer, said second layer comprising Pt and Pd;
the layers (a′), (a″) and second layers each further comprising:
one or more particulate support materials;
one or more oxygen storage component (OSC) materials; and
one or more nitrogen oxide storage materials comprising one or more elements selected from the group of alkali metals, alkaline earth metals and combinations thereof,

wherein the total amount of alkali and alkaline earth metals comprised in the one or more nitrogen oxide storage materials contained in the catalyst ranges from 0.18 to 2.0 g/in 3 calculated as the respective alkali metal oxides M 2 O and alkaline earth metal oxides MO,
wherein the layer (a′) comprises less than 500 ppm of Pt and Rh,
wherein the layer (a″) comprises less than 500 ppm of Pt and Pd, and
wherein the second layer comprises less than 500 ppm of Rh.

2. The catalyst of claim 1 , wherein at least part of the Pd, Rh and Pt is supported on the one or more particulate support materials.

3. The catalyst of claim 1 , wherein Pd and Rh comprised in the first layer are at least in part supported on separate particulate support materials.

4. The catalyst of claim 1 , wherein the second layer contains less than 500 ppm of Ba.

5. The catalyst of claim 1 , wherein the one or more particulate support materials comprise metal oxide support particles.

6. The catalyst of claim 1 , wherein the one or more OSC materials contained in the catalyst comprise one or more compounds selected from the group consisting of zirconia, ceria, lanthana, praseodymia, neodymia, and mixtures thereof.

7. The catalyst of claim 1 , wherein the alkali metals, alkaline earth metals or combinations thereof contained in the catalyst are selected from the group consisting of Li, Na, K, Rb, Cs, Mg, Ca, Sr, and Ba.

8. The catalyst of claim 1 , wherein the alkali metals, alkaline earth metals or combinations thereof contained in the catalyst are comprised in the one or more oxygen storage materials as their respective carbonates, oxides or combinations thereof.

9. The catalyst of claim 1 , wherein the catalyst coating comprises Pt and Pd in a Pt:Pd weight ratio comprised in the range of from 1:100 to 10:1.

10. The catalyst of claim 1 , wherein the catalyst comprises Rh in a loading of from 0.1 to 10 g/ft 3 .

11. The catalyst of claim 1 , wherein the catalyst comprises Pt in a loading of from 0.5 to 50 g/ft 3 .

12. The catalyst of claim 1 , wherein the catalyst comprises Pd in a loading of from 20 to 200 g/ft 3 .

13. The catalyst of claim 1 , wherein the one or more OSC materials comprised in layer (a′) comprise a ceria-zirconia composite with 30 to 85 wt.-% CeO 2 ,
or,

wherein the one or more OSC materials comprised in layer (a″) or in the second layer or both comprise a ceria-zirconia composite with 10 to 39 wt.-% CeO 2 .

14. The catalyst of claim 1 , wherein layer (a′) contains 50 wt.-% or more of the one or more nitrogen oxide storage materials.

15. An exhaust gas treatment system comprising an internal combustion engine and an exhaust gas conduit in fluid communication with the internal combustion engine, wherein the catalyst according to claim 1 is present in the exhaust gas conduit.

16. The exhaust gas treatment system of claim 15 , wherein the exhaust gas treatment system further contains a selective catalytic reduction (SCR) catalyst in the exhaust gas conduit.

17. A method for producing a catalyst according to claim 1 , comprising the steps of:
(i) providing a substrate;
(ii) impregnating one or more particulate support materials with at least one Pd-source;
(iii) adding one or more oxygen storage component (OSC) materials, one or more nitrogen oxide storage materials comprising one or more elements selected from the group of alkali metals, alkaline earth metals and combinations thereof, and a solvent to the product obtained in step (ii) to obtain a slurry;
(iv) milling the slurry obtained in step (iii);
(v) providing the resulting slurry of step (iv) onto the substrate in one or more coating steps as a layer;
(vi) impregnating one or more particulate support materials with at least one Rh-source;
(vii) adding one or more oxygen storage component (OSC) materials, one or more nitrogen oxide storage materials comprising one or more elements selected from the group of alkali metals, alkaline earth metals and combinations thereof, and a solvent to the product obtained in step (vi) to obtain a slurry;
(viii) milling the slurry obtained in step (vii);
(ix) providing the resulting slurry of step (viii) onto the substrate in one or more coating steps as a layer;
(x) impregnating one or more particulate support materials with at least one Pt- and at least one Pd-source;
(xi) adding one or more oxygen storage component (OSC) materials, one or more nitrogen oxide storage materials comprising one or more elements selected from the group of alkali metals, alkaline earth metals and combinations thereof, and a solvent to the product obtained in step (x) to obtain a slurry;
(xii) milling the slurry obtained in step (xi);
(xiii) providing the resulting slurry of step (xii) onto the substrate in one or more coating steps as a layer;

wherein the total amount of alkali and alkaline earth metals comprised in the one or more nitrogen oxide storage materials contained in the catalyst ranges from 0.18 to 2.0 g/in 3 calculated as the respective alkali metal oxides M 2 O and alkaline earth metal oxides MO.

18. A process for the treatment of a gas stream comprising conducting said gas stream over or through a catalyst according to claim 1 .

19. A method comprising a step of contacting an exhaust gas comprising CO, unburned hydrocarbons, and nitrogen oxides with a catalyst according to claim 1 for conversion of said compounds to CO 2 , N 2 , and water.

Assignees

• Hilgendorff Marcus
• Basf Se

Inventors

• Hilgendorff Marcus

Classifications

• B01J35/40

  characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title

• B01D2255/2042

  Barium · CPC title

• B01J23/58

  with alkali- or alkaline earth metals · CPC title

• B01D53/945

  characterised by a specific catalyst · CPC title

• Y02T10/24

  Cross-Sectional Technologies · mapped topic