METHOD TO MONITOR HC-SCR CATALYST NOX REDUCTION PERFORMANCE FOR LEAN EXHAUST APPLICATIONS

• US 20100307140A1
• Filed: 06/09/2009
• Published: 12/09/2010
• Est. Priority Date: 06/09/2009
• Status: Active Grant

• Current Assignee: GM Global Technology Operations LLC (General Motors Company)
• Original Assignee: GM Global Technology Operations Incorporated (General Motors Company)
• Inventors: Schmieg, Steven J., Sloane, Thompson M., Viola, Michael B., Mulawa, Patricia A., Hilden, David L., Lee, Jong H., Cheng, Shi-Wai S.
• Granted Patent: US 8,186,151 B2
• Time in Patent Office: Days
• US Class Current: 60/286
• CPC Class Codes: F01N 2250/12 absorption or adsorption, and catalytic conversion
• CPC Class Codes: F01N 2560/06 the means being a temperature sensor
• CPC Class Codes: F01N 2610/03 the substance being hydrocarbons, e.g. engine fuel
• CPC Class Codes: F01N 2610/146 Control thereof, e.g. control of injectors or injection valves
• CPC Class Codes: F01N 2900/0411 using a feed-forward control
• CPC Class Codes: F01N 2900/08 said parameters being related to the engine
• CPC Class Codes: F01N 3/208 Control of selective catalytic reduction [SCR], e.g. dosing of reducing agent
• CPC Class Codes: Y02T 10/12 Improving ICE efficiencies

Abstract

A method for initiating a regeneration mode in selective catalytic reduction device utilizing hydrocarbons as a reductant includes monitoring a temperature within the aftertreatment system, monitoring a fuel dosing rate to the selective catalytic reduction device, monitoring an initial conversion efficiency, selecting a determined equation to estimate changes in a conversion efficiency of the selective catalytic reduction device based upon the monitored temperature and the monitored fuel dosing rate, estimating changes in the conversion efficiency based upon the determined equation and the initial conversion efficiency, and initiating a regeneration mode for the selective catalytic reduction device based upon the estimated changes in conversion efficiency.

Claims

1. Method for initiating a regeneration mode in a selective catalytic reduction device of an aftertreatment system utilizing hydrocarbons as a reductant, comprising:

monitoring a temperature within said aftertreatment system;

monitoring a fuel dosing rate to said selective catalytic reduction device;

monitoring an initial conversion efficiency;

selecting an equation to estimate changes in a conversion efficiency of said selective catalytic reduction device based upon said monitored temperature and said monitored fuel dosing rate;

estimating changes in said conversion efficiency based upon said equation and said initial conversion efficiency; and

initiating a regeneration mode for said selective catalytic reduction device based upon said estimated changes in conversion efficiency.

2. The method of claim 1, wherein monitoring said initial conversion efficiency comprises:

resetting said initial conversion efficiency when said selective catalytic reduction device completes a full regeneration.

3. The method of claim 1, wherein monitoring said initial conversion efficiency comprises:

resetting said initial conversion efficiency to an estimated conversion efficiency when said selective catalytic reduction device undergoes a partial regeneration.

4. The method of claim 1, wherein estimating changes in said conversion efficiency comprises:

defining a time period through which said equation is operative based upon said monitored temperature and said fuel dosing rate; and

accumulatively estimating changes in said conversion efficiency through said time period.

5. The method of claim 4, further comprising:

defining a second time period through which a second equation is operative based upon said monitored temperature and said fuel dosing rate; and

accumulatively estimating changes in said conversion efficiency through said time period based upon said estimated conversion efficiency at a start of said new time period and said second equation through said second time period.

6. The method of claim 1, wherein initiating said regeneration mode is based upon said estimated conversion efficiency falling below a threshold conversion efficiency.

7. The method of claim 6, wherein monitoring said initial conversion efficiency comprises:

resetting said initial conversion efficiency when said selective catalytic reduction device completes a full regeneration; and

wherein said threshold conversion efficiency increases based upon increasing time of operation since said resetting.

8. The method of claim 6, wherein monitoring said initial conversion efficiency comprises:

resetting said initial conversion efficiency to an estimated conversion efficiency when said selective catalytic reduction device undergoes a partial regeneration; and

wherein said threshold conversion efficiency increases based upon increasing time of operation since said resetting.

9. The method of claim 1, wherein said monitored temperature comprises an exhaust gas flow temperature upstream of said selective catalytic reduction device.

10. The method of claim 1, wherein said monitored temperature comprises an exhaust gas flow temperature downstream of said selective catalytic reduction device.

11. The method of claim 1, wherein said monitored temperature comprises a catalyst temperature of said selective catalytic reduction device.

12. Method for estimating conversion efficiency for use in controlling a selective catalytic reduction device of an aftertreatment system utilizing hydrocarbons as a reductant, comprising:

monitoring a temperature within said aftertreatment system;

monitoring a fuel dosing rate to said selective catalytic reduction device;

monitoring an initial conversion efficiency;

selecting equations for different monitored temperature ranges to estimate changes in said conversion efficiency based upon said monitored temperature and said monitored fuel dosing rate;

accumulatively estimating changes in said conversion efficiency based upon said equations and said initial conversion efficiency; and

initiating a regeneration mode for said selective catalytic reduction device based upon said estimated changes in conversion efficiency.

13. The method of claim 12, wherein said monitored temperature comprises an exhaust gas flow temperature upstream of said selective catalytic reduction device.

14. The method of claim 12, wherein said monitored temperature comprises an exhaust gas flow temperature downstream of said selective catalytic reduction device.

15. The method of claim 12, wherein said monitored temperature comprises a catalyst temperature of said selective catalytic reduction device.

16. Method for estimating conversion efficiency for use in controlling an operative selective catalytic reduction device of an aftertreatment system utilizing hydrocarbons as a reductant, comprising:

testing an exemplary selective catalytic reduction device operatively similar to said operative selective catalytic reduction device, said testing comprising;

iteratively operating said exemplary selective catalytic reduction device through periods of operation with various temperatures and fuel dosing rates; and

monitoring conversion efficiency of said exemplary selective catalytic reduction device through each of said periods;

determining an equation representative of changes to said conversion efficiency for each of said periods;

utilizing said determined equations to track changes in conversion efficiency in said operative selective catalytic reduction device; and

controlling initiation of a regeneration mode in said operative selective catalytic reduction device based upon said tracked conversion efficiency.