Systems and methods for reducing reductant deposit formation in a decomposition reactor of an exhaust gas aftertreatment system for an internal combustion engine

Patent metadata

Field	Value
Publication number	US-11300025-B2
Application number	US-201917291205-A
Country	US
Kind code	B2
Filing date	Nov 5, 2019
Priority date	Nov 6, 2018
Publication date	Apr 12, 2022
Grant date	Apr 12, 2022

Abstract

An exhaust gas aftertreatment system includes a decomposition reactor, an injector, and a processor. The decomposition reactor includes a body, an impingement structure, and a heater. Exhaust gas is flowable through the body. The body includes an inlet and an outlet. The inlet is configured to receive the exhaust gas at a first temperature. The outlet is configured to selectively expel the exhaust gas at a second temperature greater than the first temperature. The impingement structure is disposed within the body between the inlet and the outlet. The impingement structure extends into the body and is located such that the exhaust gas flowing through the body impinges on the impingement structure. The heater is coupled to the impingement structure and configured to selectively heat the impingement structure. The injector is configured to inject reductant into the body. The processor is programmed to control the heater.

First claim

What is claimed is:

1. An exhaust gas aftertreatment system comprising:
a decomposition reactor comprising:
a body through which exhaust gas is flowable, the body comprising:
an inlet configured to receive the exhaust gas at a first temperature, and
an outlet configured to selectively expel the exhaust gas at a second temperature greater than the first temperature,

an impingement structure disposed within the body between the inlet and the outlet, the impingement structure extending into the body and being located such that the exhaust gas flowing through the body impinges on the impingement structure,
a heater coupled to the impingement structure and configured to selectively heat the impingement structure, and
a guide coupled to the body downstream of the inlet, the guide comprising a plurality of guide apertures configured to receive the exhaust gas from the inlet;

an injector configured to inject reductant into the body; and
a processor programmed to control the heater so as to heat the impingement structure to a third temperature that is greater than a Leidenfrost temperature of the reductant.

2. The exhaust gas aftertreatment system of claim 1 , wherein:
the decomposition reactor comprises a splash plate, a swirl plate, or a mixer; and
the impingement structure comprises a surface of the splash plate, the swirl plate, or the mixer.

3. The exhaust gas aftertreatment system of claim 1 , wherein the injector is located upstream of the impingement structure.

4. The exhaust gas aftertreatment system of claim 1 , further comprising a swirl mixer coupled to the body downstream of the impingement structure and upstream of the outlet, the swirl mixer configured to swirl the exhaust gas passing therethrough.

5. The exhaust gas aftertreatment system of claim 1 , further comprising:
a flange coupled to the body downstream of the guide; and
an inner tube coupled to the flange and the guide, the inner tube being configured to separately receive the exhaust gas from the inlet and the guide, and to provide the exhaust gas through the flange and towards the outlet.

6. The exhaust gas aftertreatment system of claim 5 , wherein the flange comprises a plurality of flange apertures configured to receive the exhaust gas from the inlet and to provide the exhaust gas through the flange and towards the outlet.

7. The exhaust gas aftertreatment system of claim 5 , wherein the impingement structure is at least partially disposed within at least one of the inner tube or the guide.

8. The exhaust gas aftertreatment system of claim 7 , wherein the impingement structure is coupled to at least one of the inner tube or the guide.

9. An exhaust gas aftertreatment system comprising:
a decomposition reactor comprising:
a body through which exhaust gas is flowable, the body comprising:
an inlet configured to receive the exhaust gas, and
an outlet configured to selectively expel the exhaust gas;

a guide coupled to the body downstream of the inlet, the guide extending into the body and comprising a plurality of guide apertures configured to receive the exhaust gas from the inlet;
a flange coupled to the body downstream of the guide;
an inner tube coupled to the flange and the guide, the inner tube being configured to separately receive the exhaust gas from the inlet and the guide, and to provide the exhaust gas through the flange and towards the outlet;
a temperature controlled catalyst disposed within the inner tube downstream of the guide, the temperature controlled catalyst being located such that the exhaust gas passing through the inner tube towards the outlet impinges on the temperature controlled catalyst; and
a heater coupled to the temperature controlled catalyst and configured to selectively heat the temperature controlled catalyst; and

a processor programmed to control the heater so as to heat the temperature controlled catalyst to perform hydrolysis of the exhaust gas that impinges on the temperature controlled catalyst.

10. The exhaust gas aftertreatment system of claim 9 , wherein the inner tube and the body are coaxial such that the temperature controlled catalyst is centered on a central axis of the body.

11. The exhaust gas aftertreatment system of claim 9 , wherein the guide, the inner tube, the flange, the temperature controlled catalyst, and the heater are contained within the body.

12. The exhaust gas aftertreatment system of claim 9 , further comprising a swirl mixer coupled to the body downstream of the inner tube and upstream of the outlet, the swirl mixer configured to swirl the exhaust gas passing therethrough.

13. A decomposition reactor for an exhaust gas aftertreatment system, the decomposition reactor comprising:
an inlet configured to receive an exhaust gas;
an outlet configured to provide the exhaust gas;
a body extending between the inlet and the outlet;
an inner tube positioned within the body such that at least a portion of the inner tube is separated from the body by an air gap extending around the inner tube, the inner tube comprising an impingement structure positioned proximate the inlet;
a distribution plate coupled to the impingement structure; and
a first heater coupled to the distribution plate;
wherein the distribution plate separates the first heater from the impingement structure.

14. The decomposition reactor of claim 13 , further comprising:
a second heater coupled to the distribution plate, the second heater separated from the first heater by a gap;
wherein the distribution plate separates the second heater from the impingement structure; and
wherein the distribution plate extends between the first heater and the second heater.

15. The decomposition reactor of claim 13 , further comprising:
a plurality of vanes, each of the plurality of vanes coupled to the inner tube proximate a downstream end of the inner tube;
wherein the inner tube further comprises an injector aperture that is located between the downstream end and the impingement structure; and
wherein the injector aperture is configured to receive an injector.

16. The decomposition reactor of claim 13 , further comprising:
a mixing plate coupled to the inner tube, the mixing plate comprising a mixing plate aperture configured to facilitate passage of the exhaust gas through the mixing plate and a mixing plate channel configured to facilitate passage of the exhaust gas through the mixing plate, the mixing plate channel configured to cause the exhaust gas exiting the mixing plate channel to swirl downstream of the mixing plate;
wherein the inner tube further comprises:
an upstream end; and
a downstream end opposite the upstream end; and

wherein the impingement structure is disposed between the upstream end and the mixing plate.

17. The decomposition reactor of claim 16 , wherein the inner tube further comprises an injector aperture disposed between the upstream end and the mixing plate.

18. The decomposition reactor of claim 17 , wherein the injector aperture is aligned with the impingement structure.

19. The decomposition reactor of claim 16 , wherein the first heater is configured to heat the impingement structure to a temperature that is between 120 degrees Celsius and 151 degrees Celsius, inclusive.

Assignees

• Cummins Emission Solutions Inc

Inventors

• Volmerding Matthew K
• Pandit Gaurav Hemant

Classifications

• F01N2900/1631

  Heat amount provided to exhaust apparatus · CPC title

• F01N2900/1626

  Catalyst activation temperature · CPC title

• F01N2900/1602

  Temperature of exhaust gas apparatus · CPC title

• F01N2470/24

  Concentric tubes or tubes being concentric to housing, e.g. telescopically assembled · CPC title

• F01N2470/08

  Exhaust gas passages being formed between the walls of an outer shell and an inner chamber · CPC title