Aftertreatment system including preheating oxidation catalyst

Patent metadata

Field	Value
Publication number	US-2024418113-A1
Application number	US-202418816735-A
Country	US
Kind code	A1
Filing date	Aug 27, 2024
Priority date	Sep 13, 2019
Publication date	Dec 19, 2024
Grant date	—

Abstract

An aftertreatment system for treating exhaust gas includes: an exhaust conduit configured to receive the exhaust gas; a preheating oxidation catalyst disposed in the exhaust conduit; a primary oxidation catalyst disposed in the exhaust conduit downstream of the preheating oxidation catalyst; a selective catalytic reduction system disposed in the exhaust conduit downstream of the primary oxidation catalyst; and a controller configured to: determine a temperature of the exhaust gas at an inlet of the selective catalytic reduction system, and in response to the temperature of the exhaust gas at the inlet of the selective catalytic reduction system being below a threshold temperature, cause hydrocarbons to be provided to the preheating oxidation catalyst or to the exhaust conduit at a location upstream of the preheating oxidation catalyst. The preheating oxidation catalyst catalyzes combustion of the hydrocarbons so as to increase the temperature of the exhaust gas to above the threshold temperature.

First claim

What is claimed is:

1 . An aftertreatment system for treating exhaust gas, the aftertreatment system comprising:
an exhaust conduit configured to receive the exhaust gas; a preheating oxidation catalyst disposed in the exhaust conduit; a primary oxidation catalyst disposed in the exhaust conduit downstream of the preheating oxidation catalyst; a selective catalytic reduction system disposed in the exhaust conduit downstream of the primary oxidation catalyst; and a controller configured to:
determine a temperature of the exhaust gas at an inlet of the selective catalytic reduction system, and
in response to the temperature of the exhaust gas at the inlet of the selective catalytic reduction system being below a threshold temperature, cause hydrocarbons to be provided to the preheating oxidation catalyst or to the exhaust conduit at a location upstream of the preheating oxidation catalyst;
wherein the preheating oxidation catalyst is configured to catalyze combustion of the hydrocarbons so as to increase the temperature of the exhaust gas to above the threshold temperature.

2 . A system comprising:
an engine; and the aftertreatment system of claim 1 ; wherein the controller is configured to cause the engine to provide the hydrocarbons in response to the temperature of the exhaust gas being greater than a light off temperature of the preheating oxidation catalyst.

3 . The aftertreatment system of claim 2 , further comprising a heater operatively coupled to the preheating oxidation catalyst, wherein the controller is configured to selectively activate the heater in response to the temperature of the exhaust gas being less than the light off temperature of the preheating oxidation catalyst.

4 . The system of claim 2 , wherein the controller is further configured to:
in response to the temperature of the exhaust gas increasing to be equal to or greater than an upper threshold temperature that is greater than the threshold temperature, cause the engine to stop providing the hydrocarbons.

5 . The aftertreatment system of claim 1 , further comprising a hydrocarbon injector disposed between the preheating oxidation catalyst and the primary oxidation catalyst;
wherein the controller is further configured to:
in response to the temperature of the exhaust gas reaching a light off temperature of the primary oxidation catalyst but still being below the threshold temperature, cause the hydrocarbon injector to insert second hydrocarbons into the exhaust gas between the preheating oxidation catalyst and the primary oxidation catalyst.

6 . The aftertreatment system of claim 1 , wherein the selective catalytic reduction system comprises an upstream catalyst and a downstream catalyst disposed downstream of the upstream catalyst.

7 . The aftertreatment system of claim 6 , wherein the upstream catalyst comprises a FeZ catalyst.

8 . The aftertreatment system of claim 6 , wherein the downstream catalyst comprises a CuZ catalyst.

9 . The aftertreatment system of claim 1 , wherein the preheating oxidation catalyst has a light off temperature that is lower than a light off temperature of the primary oxidation catalyst.

10 . The aftertreatment system of claim 1 , further comprising a hydrocarbon injector disposed between the preheating oxidation catalyst and the primary oxidation catalyst.

11 . A method for controlling operations of an aftertreatment system that includes an exhaust conduit, a preheating oxidation catalyst disposed in the exhaust conduit, a primary oxidation catalyst disposed in the exhaust conduit downstream of the preheating oxidation catalyst, and a selective catalytic reduction system disposed in the exhaust conduit downstream of the primary oxidation catalyst, the preheating oxidation catalyst being configured to catalyze combustion of hydrocarbons so as to increase a temperature of exhaust gas to be above a threshold temperature, the method comprising:
determining, by a controller, the temperature of the exhaust gas at an inlet of the selective catalytic reduction system; and in response to the temperature of the exhaust gas being below the threshold temperature, causing, by the controller, the hydrocarbons to be provided to the preheating oxidation catalyst or to the exhaust conduit at a location upstream of the preheating oxidation catalyst.

12 . The method of claim 11 , wherein the controller causes an engine to provide the hydrocarbons in response to the temperature of the exhaust gas being greater than a light off temperature of the preheating oxidation catalyst.

13 . The method of claim 12 , further comprising:
in response to the temperature of the exhaust gas increasing to be equal to or greater than an upper threshold temperature that is greater than the threshold temperature, causing, by the controller, the engine to stop providing of the hydrocarbons.

14 . The method of claim 12 , wherein the aftertreatment system further comprises a heater operatively coupled to the preheating oxidation catalyst, and wherein the method further comprises:
causing activation of the heater, by the controller, in response to the temperature of the exhaust gas being less than the light off temperature of the preheating oxidation catalyst.

15 . The method of claim 11 , further comprising:
in response to the temperature of the exhaust gas reaching a light off temperature of the primary oxidation catalyst but still being below the threshold temperature, causing, by the controller, a hydrocarbon injector disposed between the preheating oxidation catalyst and the primary oxidation catalyst to insert second hydrocarbons.

16 . A controller for controlling operations of a system that comprises an aftertreatment system that includes, an exhaust conduit, a preheating oxidation catalyst disposed in the exhaust conduit, a primary oxidation catalyst disposed in the exhaust conduit downstream of the preheating oxidation catalyst, and a selective catalytic reduction system disposed in the exhaust conduit downstream of the primary oxidation catalyst, the preheating oxidation catalyst being configured to catalyze combustion of hydrocarbons so as to increase a temperature of exhaust gas to above a threshold temperature, the controller configured to:
determine the temperature of the exhaust gas at an inlet of the selective catalytic reduction system; and in response to the temperature of the exhaust gas at being below the threshold temperature, cause the hydrocarbons to be provided to the preheating oxidation catalyst or to the exhaust conduit at a location upstream of the preheating oxidation catalyst, the preheating oxidation catalyst being configured to catalyze combustion of the hydrocarbons so as to increase the temperature of the exhaust gas to above the threshold temperature.

17 . The controller of claim 16 , wherein the controller causes the hydrocarbons to be provided in response to the temperature of the exhaust gas being greater than a light off temperature of the preheating oxidation catalyst.

18 . The controller of claim 17 , wherein the aftertreatment system further comprises a heater operatively coupled to the preheating oxidation catalyst, and wherein the controller is further configured to:
selectively activate the heater in response to the temperature of the exhaust gas being less than the light off temperature of the preheating oxidation catalyst.

19 . The controller of claim 17 , further configured to:
in response to the temperature of the exhaust gas reaching a light off temperature of th

Assignees

• Cummins Emission Solutions Inc

Inventors

• Punde Shirish S
• Dabhoiwala Rayomand
• Reynolds James Nicholas

Classifications

• F01N2900/0602

  Electrical exhaust heater signals · CPC title

• F01N2900/1602

  Temperature of exhaust gas apparatus · CPC title

• F01N11/002 Primary

  the diagnostic devices measuring or estimating temperature or pressure in, or downstream of the exhaust apparatus · CPC title

• F01N9/002

  of filter regeneration · CPC title

• F01N3/208

  Control of selective catalytic reduction [SCR], e.g. by adjusting the dosing of reducing agent · CPC title