Systems and methods for desulfation of catalysts included in aftertreatment systems

Patent metadata

Field	Value
Publication number	US-11698011-B2
Application number	US-202017602233-A
Country	US
Kind code	B2
Filing date	Mar 30, 2020
Priority date	Apr 9, 2019
Publication date	Jul 11, 2023
Grant date	Jul 11, 2023

Abstract

An aftertreatment system for reducing constituents of an exhaust gas having a sulfur content includes: an oxidation catalyst; a filter disposed downstream of the oxidation catalyst; and a controller configured, in response to determining that the filter is to be regenerated and a desulfation condition being satisfied, to: cause a temperature of the oxidation catalyst to increase to a first regeneration temperature that is greater than or equal to 400 degrees Celsius and less than 550 degrees Celsius; cause the temperature of the oxidation catalyst to be maintained at the first regeneration temperature for a first time period; and after the first time period, cause the temperature of the oxidation catalyst to increase to a second regeneration temperature equal to or greater than 550 degrees Celsius.

First claim

What is claimed is:

1. An aftertreatment system for reducing constituents of an exhaust gas having a sulfur content, comprising:
a selective catalytic reduction catalyst; and
a controller configured to:
determine a NO X conversion efficiency of the selective catalytic reduction catalyst;
in response to the NO X conversion efficiency being less than a predetermined threshold, cause a temperature of the selective catalytic reduction catalyst to increase to a first regeneration temperature that is greater than or equal to 400 degrees Celsius and less than 550 degrees Celsius;
cause the temperature of the selective catalytic reduction catalyst to be maintained at the first regeneration temperature for a first time period;
after the first time period, cause the temperature of the selective catalytic reduction catalyst to increase to a second regeneration temperature greater than the first regeneration temperature and less than 550 degrees Celsius; and
cause the temperature of the selective catalytic reduction catalyst to be maintained at the second regeneration temperature for a second time period.

2. The aftertreatment system of claim 1 , wherein the controller is further configured to:
in response to a time interval between regeneration events not satisfying a time interval threshold, cause the temperature of the selective catalytic reduction catalyst to increase to a third regeneration temperature in a subsequent regeneration event, the third regeneration temperature being greater than the first regeneration temperature and less than 550 degrees Celsius; and
cause the temperature of the selective catalytic reduction catalyst to be maintained at the third regeneration temperature for a predetermined third time period.

3. The aftertreatment system of claim 2 , wherein the time interval threshold is in a range of 10 hours to 12 hours.

4. The aftertreatment system of claim 2 , wherein the controller is further configured to:
in response to the time interval between regeneration events not satisfying a critical time interval, cause the temperature of the selective catalytic reduction catalyst to increase to a fourth regeneration temperature in a subsequent regeneration event, the fourth regeneration temperature being equal to or greater than 550 degrees Celsius.

5. The aftertreatment system of claim 4 , wherein the critical time interval is 1 hour.

6. The aftertreatment system of claim 4 , wherein the controller is further configured to:
in response to the time interval between regeneration events continuing to not satisfy the critical time interval after the subsequent regeneration event, generate a fault code.

7. The aftertreatment system of claim 1 , wherein a ratio of ammonia generated by a reductant inserted into the exhaust gas to an amount of NO X gases included in the exhaust gas flowing through the aftertreatment system is greater than 1.0.

8. The aftertreatment system of claim 1 , further comprising:
an oxidation catalyst disposed upstream of the selective catalytic reduction catalyst; and
a hydrocarbon insertion assembly configured to insert hydrocarbons into the oxidation catalyst,
wherein the controller is configured to cause the temperature of the selective catalytic reduction catalyst to increase by instructing the hydrocarbon insertion assembly to insert hydrocarbons into the oxidation catalyst.

9. The aftertreatment system of claim 1 , further comprising:
a selective catalytic reduction catalyst heater operatively coupled to the selective catalytic reduction catalyst,
wherein the controller is configured to instruct the selective catalytic reduction heater to increase and maintain the temperature of the selective catalytic reduction catalyst.

10. The aftertreatment system of claim 1 , wherein the predetermined threshold comprises the NO X conversion efficiency being 90%.

11. An aftertreatment system for reducing constituents of an exhaust gas having a sulfur content, comprising:
a selective catalytic reduction catalyst; and
a controller configured to:
determine a NO X conversion efficiency of the selective catalytic reduction catalyst;
in response to the NO X conversion efficiency being less than a first predetermined threshold, cause a temperature of the selective catalytic reduction catalyst to increase to a first regeneration temperature that is greater than or equal to 400 degrees Celsius and less than 550 degrees Celsius;
cause the temperature of the selective catalytic reduction catalyst to be maintained at the first regeneration temperature for a first time period;
in response to the NO X conversion efficiency being less than a second predetermined threshold that is less than the first predetermined threshold or a time interval between subsequent regeneration events at the first temperature being less than a time interval threshold, cause the temperature of the selective catalytic reduction catalyst to increase to a second regeneration temperature that is equal to or greater than 550 degrees Celsius;
cause the temperature of the selective catalytic reduction catalyst to be maintained at the second regeneration temperature for a second time period; and
in response to the NO X conversion efficiency being less than a third predetermined threshold that is less than the second predetermined threshold, or the time interval between subsequent regeneration events at the second temperature being less than a time interval threshold, generate a fault code.

12. The aftertreatment system of claim 11 , wherein the first predetermined threshold corresponds to a 90% NO X conversion efficiency, the second predetermined threshold corresponds to an 80% NO X conversion efficiency, and the third predetermined threshold corresponds a 70% NO X conversion efficiency.

13. The aftertreatment system of claim 11 , wherein the controller is further configured to:
in response to a fuel tank associated with an engine that is generating the exhaust gas being refilled or a predetermined amount of fuel having been consumed, increase the temperature of the selective catalytic reduction catalyst to the first regeneration temperature.

Assignees

• Cummins Emission Solutions Inc

Inventors

• Cunningham Michael J
• Yezerets Aleksey
• Li Junhui
• Cramer James A

Classifications

• B01D53/9495

  Controlling the catalytic process · CPC title

• F01N9/002

  of filter regeneration · CPC title

• F01N2570/04

  Sulfur or sulfur oxides · CPC title

• F01N2900/1612

  SOx amount trapped in catalyst · CPC title

• B01D53/96

  Regeneration, reactivation or recycling of reactants · CPC title