Systems and methods to reduce reductant consumption in exhaust aftertreatment systems

Patent metadata

Field	Value
Publication number	US-10113465-B2
Application number	US-201615389625-A
Country	US
Kind code	B2
Filing date	Dec 23, 2016
Priority date	Mar 27, 2014
Publication date	Oct 30, 2018
Grant date	Oct 30, 2018

Abstract

Systems, apparatus and methods are provided for reducing reductant consumption in an exhaust aftertreatment system that includes a first SCR device and a downstream second SCR device, a first reductant injector upstream of the first SCR device, and a second reductant injector between the first and second SCR devices. NOx conversion occurs with reductant injection by the first reductant injector to the first SCR device in a first temperature range and with reductant injection by the second reductant injector to the second SCR device when the temperature of the first SCR device is above a reductant oxidation conversion threshold.

First claim

What is claimed is:

1. A system, comprising:
an internal combustion engine operable to produce an exhaust gas;
an exhaust conduit fluidly coupled to the internal combustion engine to receive the exhaust gas;
an oxidation catalyst connected to the exhaust conduit to receive the exhaust gas;
a particulate filter and a first selective catalytic reduction (SCR) device fluidly coupled to the exhaust conduit downstream of the oxidation catalyst;
a second SCR device fluidly coupled to the exhaust conduit downstream of the particulate filter and the first SCR device, wherein the second SCR device is located in a lower temperature operating region than the first SCR device;
a controller operably connected to a first reductant injector and a second reductant injector;
wherein the first reductant injector is upstream of the first SCR device and is controlled by the controller to inject a reductant into the exhaust gas during a first temperature range of operation of the first SCR device to reduce NOx primarily over the first SCR device, and the first reductant injector is disabled by the controller in response to a temperature of the first SCR device being above a reductant oxidation conversion threshold; and
wherein the second reductant injector is downstream of the first SCR device and upstream of the second SCR device and is controlled by the controller to inject the reductant into the exhaust gas to reduce NOx over the second SCR device in response to the temperature of the first SCR device being above the first temperature range and the second SCR device being above a minimum temperature threshold.

2. The system of claim 1 , further comprising at least one storage device fluidly coupled to the exhaust conduit upstream of the oxidation catalyst, wherein the at least one storage device is configured to provide a storage location for hydrocarbons and oxides of nitrogen in the exhaust gas produced by the internal combustion engine during low temperature operating conditions.

3. The system of claim 2 , wherein the at least one storage device includes a separate device for each of hydrocarbon storage and oxides of nitrogen storage.

4. The system of claim 1 , further comprising the first SCR device and the second SCR device being connected by an exhaust conduit portion configured to provide exhaust cooling from the first SCR device to the second SCR device.

5. The system of claim 1 , further comprising, a source of liquid reductant coupled to at least one of the first and second reductant injectors.

6. The system of claim 1 , further comprising a source of gaseous reductant coupled at least to the first reductant injector.

7. The system of claim 6 , wherein the source of gaseous reductant is coupled to each of the first and second reductant injectors.

8. The system of claim 1 , wherein the first SCR device is included as a washcoat on the particulate filter.

9. The system of claim 1 , wherein the particulate filter is upstream of the first SCR device.

10. The system of claim 1 , wherein the first reductant injector is between the the particulate filter and the first SCR device.

11. The system of claim 1 , wherein the second SCR device includes a first SCR element upstream of a second SCR element.

12. The system of claim 1 , wherein the controller comprises:
a NO x determination module structured to determine a NO x amount upstream of the first SCR device;
a temperature determination module structured to determine a temperature of the first SCR device and a temperature of the second SCR device;
an injector selection module structured to select at least one of the first reductant injector and. the second reductant injector in response to the temperature of the first SCR device and the temperature of the second SCR device; and
a reductant control module structured to determine a reductant injector command to the selected ones of the first reductant injector and the second reductant injector in response to the NO x amount to achieve a desired NO x conversion by the first SCR device and the second SCR device.

13. The system of claim 12 , wherein the controller further comprises an ammonia storage depletion module structured to determine an ammonia storage amount on the first SCR device, the ammonia storage depletion module further being structured to enable the first reductant injector to inject a reductant amount when the ammonia storage amount on the first SCR device is less than an ammonia depletion threshold.

14. The system of claim 1 , wherein the first temperature range includes a low temperature threshold associated with a NOx conversion efficiency of the first SCR device and a high temperature threshold associated with the reductant oxidation conversion threshold of the first SCR device.

15. A system, comprising:
an exhaust conduit for receiving an exhaust gas from an internal combustion engine;
a first selective catalytic reduction (SCR) device fluidly coupled to the exhaust conduit to receive the exhaust gas;
a second SCR device fluidly coupled to the exhaust conduit downstream, of the first SCR device, wherein the second SCR device is located in a lower temperature operating region than the first SCR device;
a controller operably connected to a first reductant injector and a second reductant injector;
wherein the first reductant injector is upstream of the first SCR device and in response to the controller injects a reductant into the exhaust gas during a first temperature range of operation of the first SCR device to reduce NOx primarily over the first SCR device, wherein the first reductant injector is disabled by the controller in response to a temperature of the first SCR device being above a reductant oxidation conversion threshold; and
wherein the second reductant injector is downstream of the first SCR device and upstream of the second SCR device and in response to the controller injects the reductant into the exhaust gas to reduce NOx over the second SCR device in response to the temperature of the first SCR device being above the first temperature range and the second SCR device being above a minimum temperature threshold.

16. The system of claim 15 , further comprising:
an oxidation catalyst connected to the exhaust conduit to receive the exhaust gas; and
a particulate filter fluidly coupled to the exhaust conduit downstream of the oxidation catalyst.

17. The system of claim 16 , further comprising at least one storage device fluidly coupled to the exhaust conduit upstream of the oxidation catalyst, wherein the at least one storage device is configured to provide a storage location for hydrocarbons and oxides of nitrogen in the exhaust gas during low temperature operating conditions.

18. The system of claim 17 , wherein the at least one storage device includes a single device for hydrocarbon storage and oxides of nitrogen storage.

Assignees

• Cummins Inc

Inventors

• Gupta Aniket
• Cunningham Michael J

Classifications

• F01N3/208 Primary

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

• B01D53/9418

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

• F01N3/0842

  Nitrogen oxides · CPC title

• F01N2610/02

  the substance being ammonia or urea · CPC title

• F01N3/0835

  Hydrocarbons · CPC title