Ammonia oxidation catalyst for diesel applications

1. An ammonia oxidation catalyst for the treatment of an exhaust gas stream, the catalyst comprising a coating disposed on a substrate, wherein the coating comprises:

(i) a selective catalytic reduction component of a zeolite material comprising one or more of copper and iron; and

(ii) an oxidation catalytic component comprising platinum supported on a porous non-zeolite oxide support, wherein the oxidation catalytic component further comprises a first oxide material supported on the porous non-zeolite oxide support supporting platinum, wherein the first oxide material comprises titania,

wherein from 65 wt.-% to 95 wt.-%, of the oxidation catalytic component consist of the porous non-zeolite oxide support.

2. The catalyst of claim 1 , wherein the selective catalytic reduction component according to (i) is a 8-membered ring pore zeolite material.

3. The catalyst of claim 1 , wherein the coating further comprises an oxide binder, wherein the oxide binder comprises an oxide selected from the group consisting of zirconia, alumina, titania, silica, and a combination of any two or more thereof.

4. The catalyst of claim 1 , wherein the porous non-zeolite oxide support comprises a non-zeolite selected from the group consisting of alumina, silica, zirconia, zirconia-alumina, silica-alumina, and a combination of any two or more thereof.

5. The catalyst of claim 1 , wherein the coating comprises the selective catalytic reduction component (i) at a loading 11 , (11), and the porous non-zeolite oxide support at a loading 13 , (13), wherein the loading ratio of the selective catalytic reduction component (i) relative to the porous non-zeolite oxide support, expressed as (11):(13), ranges from 1:1 to 25:1.

6. The catalyst of claim 1 , wherein the coating comprises platinum, calculated as elemental platinum, at an amount ranging from 0.2 wt.-% to 1.5 wt-%, based on the weight of the porous non-zeolite oxide support.

7. The catalyst of claim 1 , wherein the oxidation catalytic component further comprises one or more platinum group metals other than platinum.

8. The catalyst of claim 1 , wherein the coating comprises the first oxide material at an amount ranging from 1 wt.-% to 20 wt,-%, based on the weight of the porous non-zeolite oxide support.

9. The catalyst of claim 1 , wherein the oxidation catalytic component further comprises a second oxide material supported on the porous non-zeolite oxide support, the second oxide material comprising an element selected from the group consisting of manganese, cerium, tungsten, molybdenum, praseodymium, europium, chromium, cobalt, technetium, rhenium, ruthenium, vanadium, indium and a combination of any two or more thereof.

10. A process for preparing the ammonia oxidation catalyst according to claim 1 , the process comprising

(a) preparing a first mixture comprising water and a selective catalytic reduction component a zeolite material comprising one or more of copper and iron;

(b) preparing a second mixture comprising water and a source of the oxidation catalytic component comprising a source of platinum, a porous non-zeolite oxide support and a first oxide material comprising titania;

(c) mixing the first mixture obtained in (a) and the second mixture obtained in (b);

(d) disposing the mixture obtained in (c) on a substrate; and optionally drying the substrate comprising the mixture disposed thereon; and

(e) calcining the substrate obtained in (d), wherein from 65 wt % to 95 wt %, of the oxidation catalytic component consist of the porous non-zeolite oxide support.

11. The process of claim 10 , wherein (a) further comprises

(a.1) preparing a mixture comprising water and a precursor of an oxide binder;

(a.2) adding the selective catalytic reduction component of the zeolite material comprising one or more of copper and iron to the mixture obtained in (a.1).

12. The process of claim 10 , wherein (b) further comprises

(b.1) impregnating the source of platinum onto the porous non-zeolite oxide support with an adjuvant;

(b.2) optionally, impregnating a source of one or more platinum group metals other than platinum onto the impregnated porous non-zeolite oxide support obtained in (b.1);

(b.3) impregnating a solution comprising a source of the first oxide material comprising titania onto the impregnated porous non-zeolite oxide support obtained in (b.1), obtaining a mixture;

(b.4) optionally adding a source of a second oxide material to the mixture obtained in (b.3);

(b.5) drying, calcining, or both the mixture obtained in (b.3), optionally the mixture obtained in (b.4), obtaining a powder;

(b.6) preparing a mixture comprising water and the powder obtained in (b.5);

(b.7) optionally, milling the particles of the mixture obtained in (b.6); or

wherein (b) further comprises

(b.1′) impregnating the source of platinum onto the porous non-zeolite oxide support with an adjuvant;

(b.2′) impregnating a solution comprising a source of the first oxide material comprising titania onto the impregnated porous non-zeolite oxide support obtained in (b.1), obtaining a mixture;

(b.3′) impregnating a source of one or more platinum group metals other than platinum onto the impregnated porous non-zeolite oxide support obtained in (b.2′);

(b.4′) drying and calcining the mixture obtained in (b.3′), obtaining a powder;

(b.5′) preparing a mixture comprising water and the powder obtained in (b.4′); and

(b.6′) optionally, milling the particles of the mixture obtained in (b.5′).

13. The process of claim 10 , wherein the porous non-zeolite oxide support provided in (b) has an average pore volume ranging from 0.6 ml/cm 3 to 2 ml/cm 3 .

14. A method for oxidizing ammonia, wherein ammonia is comprised in an exhaust gas stream, the method comprising

(1) providing the exhaust gas stream;

(2) passing the exhaust gas stream provided in (1) through a catalyst according to claim 1 .