Exhaust gas treatment system for ultra low NOx and cold start

Patent metadata

Field	Value
Publication number	US-11779906-B2
Application number	US-202017594773-A
Country	US
Kind code	B2
Filing date	Apr 27, 2020
Priority date	Apr 29, 2019
Publication date	Oct 10, 2023
Grant date	Oct 10, 2023

Abstract

The present disclosure relates to an exhaust gas treatment system for treating an exhaust gas stream leaving an internal combustion engine, wherein said exhaust gas treatment system comprises (i) a first catalyst comprising a coating and a first substrate, wherein the coating comprises a vanadium oxide supported on a first oxidic support comprising titanium; (ii) a hydrocarbon injector for injecting a fluid comprising hydrocarbons into the exhaust gas stream exiting the outlet end of the first catalyst according to (i); (iii) a second catalyst comprising a coating and a second substrate, wherein the coating comprises palladium on a second oxidic support comprising one or more of zirconium, silicon, aluminum and titanium.

First claim

The invention claimed is:

1. An exhaust gas treatment system for treating an exhaust gas stream leaving an internal combustion engine, the exhaust gas treatment system having an upstream end for introducing the exhaust gas stream into the exhaust gas treatment system, wherein the exhaust gas treatment system comprises
(i) a first catalyst having an inlet end and an outlet end and comprising a coating and a first substrate, wherein the first substrate has an inlet end, an outlet end and a substrate axial length extending from the inlet end to the outlet end of the first substrate and comprises a plurality of passages defined by internal walls, wherein the interface between the passages and the internal walls is defined by the surface of the internal walls, wherein the coating is disposed on the surface of the internal walls of the first substrate and the coating comprises a vanadium oxide supported on a first oxidic support comprising titanium;
(ii) a hydrocarbon injector for injecting a fluid comprising hydrocarbons into the exhaust gas stream exiting the outlet end of the first catalyst according to (i); and
(iii) a second catalyst having an inlet end and an outlet end and comprising a coating and a second substrate, wherein the second substrate has an inlet end, an outlet end and a substrate axial length extending from the inlet end to the outlet end of the second substrate and comprises a plurality of passages defined by internal walls, wherein the interface between the passages and the internal walls is defined by the surface of the internal walls, wherein the coating is disposed on the surface of the internal walls of the second substrate and the coating comprises palladium on a second oxidic support comprising one or more of zirconium, silicon, aluminum and titanium;
wherein the first catalyst according to (i) is the first catalyst of the exhaust gas treatment system downstream of the upstream end of the exhaust gas treatment system and wherein the inlet end of the first catalyst is arranged upstream of the outlet end of the first catalyst;
wherein in the exhaust gas treatment system, the second catalyst according to (iii) is located downstream of the first catalyst according to (i) and downstream of the hydrocarbon injector according to (ii) and wherein the inlet end of the second catalyst is arranged upstream of the outlet end of the second catalyst; and
wherein the coating of the second catalyst according to (iii) further comprises a zeolitic material, the zeolitic material comprising one or more of Cu and Fe, and the coating of the second catalyst according to (iii) further comprises from 0.5 weight-% to 10 weight-% of an oxidic binder, based on the total weight of the zeolitic material.

2. The system of claim 1 , wherein the coating of the first catalyst comprises the vanadium oxide at an amount ranging from 1.0 weight-% to 10 weight-%, based on the weight of the first oxidic support.

3. The system of claim 1 , wherein the first oxidic support further comprises one or more of tungsten, silicon, zirconium, and antimony;
wherein the first oxidic support has from 80 weight-% to 98 weight-% titania, calculated as WO 3 .

4. The system of claim 1 wherein the second oxidic support comprises one or more of zirconium and aluminum;
wherein the second oxidic support has a total of from 90 weight-% to 100 weight-%, aluminum, oxygen and optionally zirconium.

5. The system of claim 1 , wherein the coating of the second catalyst according to (iii) comprises palladium ranging from 5 g/ft 3 to 90 g/ft 3 .

6. The system of claim 5 , wherein palladium is the only platinum group metal present in the coating of the second catalyst according to (iii).

7. The system of claim 1 , wherein the coating of the second catalyst has from 98 weight-% to 100 weight-% palladium supported on the second oxidic support; wherein the second oxidic support comprises one or more of zirconium, silicon, aluminum, and titanium.

8. The system of claim 1 , further comprising an injector for injecting a fluid into the exhaust gas stream exiting the internal combustion engine, the injector being located upstream of the first catalyst and downstream of the upstream end of the exhaust gas treatment system;
wherein no hydrocarbon injector is located upstream of the first catalyst and downstream of the upstream end of the exhaust gas treatment system.

9. An exhaust gas treatment system for treating an exhaust gas stream leaving an internal combustion engine, the exhaust gas treatment system having an upstream end for introducing the exhaust gas stream into the exhaust gas treatment system, wherein the exhaust gas treatment system comprises:
(i) a first catalyst having an inlet end and an outlet end and comprising a coating and a first substrate, wherein the first substrate has an inlet end, an outlet end and a substrate axial length extending from the inlet end to the outlet end of the first substrate and comprises a plurality of passages defined by internal walls, wherein the interface between the passages and the internal walls is defined by the surface of the internal walls, wherein the coating is disposed on the surface of the internal walls of the first substrate and the coating comprises a vanadium oxide supported on a first oxidic support comprising titanium;
(ii) a hydrocarbon injector for injecting a fluid comprising hydrocarbons into the exhaust gas stream exiting the outlet end of the first catalyst according to (i); and
(iii) a second catalyst having an inlet end and an outlet end and comprising a coating and a second substrate, wherein the second substrate has an inlet end, an outlet end and a substrate axial length extending from the inlet end to the outlet end of the second substrate and comprises a plurality of passages defined by internal walls, wherein the interface between the passages and the internal walls is defined by the surface of the internal walls, wherein the coating is disposed on the surface of the internal walls of the second substrate and the coating comprises palladium on a second oxidic support comprising one or more of zirconium, silicon, aluminum and titanium; and
(iv) a third catalyst having an inlet end and an outlet end and comprising a coating and a third substrate, wherein the third substrate has an inlet end, an outlet end and a substrate axial length extending from the inlet end to the outlet end of the third substrate and comprises a plurality of passages defined by internal walls, wherein the interface between the passages and the internal walls is defined by the surface of the internal walls, wherein the coating is disposed on the surface of the internal walls of the third substrate and the coating comprises one or more of a vanadium oxide and a zeolitic material comprising one or more of Cu and Fe;
wherein the first catalyst according to (i) is the first catalyst of the exhaust gas treatment system downstream of the upstream end of the exhaust gas treatment system and wherein the inlet end of the first catalyst is arranged upstream of the outlet end of the first catalyst
wherein in the exhaust gas treatment system, the second catalyst according to (iii) is located downstream of the first catalyst according to (i) and downstream of the hydrocarbon injector according to (ii) and wherein the inlet end of the second catalyst is arranged upstream of the outlet end of the second catalyst
wherein in the exhaust gas treatment system, the third catalyst according to (iv) is located downstream of the second catalyst according to (iii) and wherein the inlet end of the third catalyst is arranged upstream of the outlet end of the third catalyst;
wherein the outlet end of the second catalyst according to (iii) is in fluid communication with

Assignees

• Basf Corp

Inventors

• Dorner Robert

Classifications

• B01J35/56

  Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional [3D] monoliths · CPC title

• B01J23/44 Primary

  Palladium · CPC title

• B01D53/944

  Simultaneously removing carbon monoxide, hydrocarbons or carbon making use of oxidation catalysts (three-way-catalysts [TWC] B01D53/9445) · CPC title

• B01D53/9418

  for removing nitrogen oxides by selective catalytic reduction [SCR] using a reducing agent in a lean exhaust gas · CPC title

• B01D53/9431

  Processes characterised by a specific device · CPC title