IP Library Granted Patent US 7,707,824
Granted Patent B2
US 7,707,824 · App. 11/786,036 · Granted May 4, 2010

Excess NH3 storage control for SCR catalysts

Assignee: GM Global Technology Operations, Inc.
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Quick Facts
Patent No.
US 7,707,824
App. No.
11/786,036
Granted
May 4, 2010
Kind
B2
Abstract

A method of regulating an amount of NH3 stored in a catalyst of an exhaust after-treatment system includes determining a mass of NH3 into the catalyst based on a dosing rate of a dosing agent that is injected into an exhaust stream upstream of the catalyst and determining a mass of NH3 out of the catalyst. An accumulated mass of NH3 within the catalyst is calculated based on the mass of NH3 into the catalyst and the mass of NH3 out of the catalyst. The dosing rate is regulated based on the accumulated mass of NH3 within the catalyst.

Claims (40)

1. A method of regulating an amount of NH3 stored in a catalyst of an exhaust after-treatment system, comprising:

determining a mass of NH3 into the catalyst based on a dosing rate of a dosing agent that is injected into an exhaust stream upstream of the catalyst;

determining a mass of NH3 out of the catalyst;

calculating an accumulated mass of NH3 within the catalyst based on said mass of NH3 into the catalyst and said mass of NH3 out of the catalyst; and

regulating said dosing rate based on said accumulated mass of NH3 within the catalyst.

2. The method of claim 1 wherein said mass of NH3 out of the catalyst is determined based on signals generated by NOx sensors that are located upstream and downstream of the catalyst, respectively.

3. The method of claim 1 further comprising determining a conversion efficiency of the catalyst based on a temperature of the catalyst, wherein said mass of NH3 out of the catalyst is determined based on a base dosing rate and said conversion efficiency.

4. The method of claim 1 further comprising:

monitoring a catalyst temperature; and

setting said accumulated mass of NH3 within the catalyst equal to zero when said catalyst temperature exceeds a threshold temperature.

5. The method of claim 1 further comprising determining a maximum NH3 storage mass of the catalyst based on a catalyst temperature, wherein said dosing rate is regulated based on said maximum NH3 storage mass.

6. The method of claim 5 further comprising calculating an excess NH3 storage ratio based on said accumulated mass of NH3 within the catalyst and said maximum NH3 storage mass, wherein said dosing rate is regulated based on said excess NH3 storage ratio.

7. The method of claim 6 further comprising determining an adjustment factor based on said excess NH3 storage ratio, wherein said dosing rate is regulated based said adjustment factor.

8. The method of claim 6 wherein said dosing agent is regulated to maintain said excess NH3 storage ratio to be less than 1.

9. An exhaust after-treatment system that regulates an amount of NH3 stored in a catalyst thereof, comprising:

a first module that determines a mass of NH3 into the catalyst based on a dosing rate of a dosing agent that is injected into an exhaust stream upstream of the catalyst;

a second module that determines a mass of NH3 out of the catalyst;

a third module that calculates an accumulated mass of NH3 within the catalyst based on said mass of NH3 into the catalyst and said mass of NH3 out of the catalyst; and

a fourth module that regulates said dosing rate based on said accumulated mass of NH3 within the catalyst.

10. The exhaust after-treatment system of claim 9 wherein said mass of NH3 out of the catalyst is determined based on signals generated by NOx sensors that are located upstream and downstream of the catalyst, respectively.

11. The exhaust after-treatment system of claim 9 further comprising a fifth module that determines a conversion efficiency of the catalyst based on a temperature of the catalyst, wherein said mass of NH3 out of the catalyst is determined based on a base dosing rate and said conversion efficiency.

12. The exhaust after-treatment system of claim 9 further comprising a temperature sensor that monitors a catalyst temperature, wherein said fourth module sets said accumulated mass of NH3 within the catalyst equal to zero when said catalyst temperature exceeds a threshold temperature.

13. The exhaust after-treatment system of claim 9 further comprising a fifth module that determines a maximum NH3 storage mass of the catalyst based on a catalyst temperature, wherein said dosing rate is regulated based on said maximum NH3 storage mass.

14. The exhaust after-treatment system of claim 13 further comprising a sixth module that calculates an excess NH3 storage ratio based on said accumulated mass of NH3 within the catalyst and said maximum NH3 storage mass, wherein said dosing rate is regulated based on said excess NH3 storage ratio.

15. The exhaust after-treatment system of claim 14 further comprising a seventh module that determines an adjustment factor based on said excess NH3 storage ratio, wherein said dosing rate is regulated based said adjustment factor.

16. The exhaust after-treatment system of claim 14 wherein said dosing agent is regulated to maintain said excess NH3 storage ratio to be less than 1.

17. A method of regulating an amount of NH3 stored in a catalyst of an exhaust after-treatment system, comprising:

determining a mass of NH3 into the catalyst based on a dosing rate of a dosing agent that is injected into an exhaust stream upstream of the catalyst;

determining a mass of NH3 out of the catalyst;

calculating an accumulated mass of NH3 within the catalyst based on said mass of NH3 into the catalyst and said mass of NH3 out of the catalyst;

determining a maximum NH3 storage mass of the catalyst;

calculating an excess NH3 storage ratio based on said maximum NH3 storage mass and said accumulated mass of NH3 within the catalyst; and

regulating said dosing rate based on said excess NH3 storage ratio to maintain said excess NH3 storage ratio to be less than 1.

18. The method of claim 17 wherein said mass of NH3 out of the catalyst is determined based on signals generated by NOx sensors that are located upstream and downstream of the catalyst, respectively.

19. The method of claim 17 further comprising determining a conversion efficiency of the catalyst based on a temperature of the catalyst, wherein said mass of NH3 out of the catalyst is determined based on a base dosing rate and said conversion efficiency.

20. The method of claim 17 further comprising:

monitoring a catalyst temperature; and

setting said accumulated mass of NH3 within the catalyst equal to zero when said catalyst temperature exceeds a threshold temperature.

21. The method of claim 17 further comprising determining said maximum NH3 storage mass of the catalyst based on at least one of a catalyst temperature and a catalyst volume.

22. The method of claim 21 further comprising determining an adjustment factor based on said excess NH3 storage ratio, wherein said dosing rate is regulated based said adjustment factor.

Assignments (12)
RELEASE OF SECURITY INTEREST Recorded Nov 7, 2014
From: WILMINGTON TRUST COMPANY
To: GM GLOBAL TECHNOLOGY OPERATIONS LLC
Reel/Frame 034185/0587 →
CHANGE OF NAME Recorded Feb 10, 2011
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: GM GLOBAL TECHNOLOGY OPERATIONS LLC
Reel/Frame 025781/0035 →
SECURITY AGREEMENT Recorded Nov 8, 2010
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: WILMINGTON TRUST COMPANY
Reel/Frame 025324/0057 →
RELEASE OF SECURITY INTEREST Recorded Nov 5, 2010
From: UAW RETIREE MEDICAL BENEFITS TRUST
To: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
Reel/Frame 025314/0946 →
RELEASE OF SECURITY INTEREST Recorded Nov 4, 2010
From: UNITED STATES DEPARTMENT OF THE TREASURY
To: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
Reel/Frame 025245/0656 →
SECURITY AGREEMENT Recorded Aug 28, 2009
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: UAW RETIREE MEDICAL BENEFITS TRUST
Reel/Frame 023162/0140 →
SECURITY AGREEMENT Recorded Aug 27, 2009
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: UNITED STATES DEPARTMENT OF THE TREASURY
Reel/Frame 023156/0264 →
RELEASE OF SECURITY INTEREST Recorded Aug 21, 2009
From: CITICORP USA, INC. AS AGENT FOR BANK PRIORITY SECURED PARTIES; CITICORP USA, INC. AS AGENT FOR HEDGE PRIORITY SECURED PARTIES
To: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
Reel/Frame 023155/0663 →
RELEASE OF SECURITY INTEREST Recorded Aug 20, 2009
From: UNITED STATES DEPARTMENT OF THE TREASURY
To: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
Reel/Frame 023124/0563 →
SECURITY AGREEMENT Recorded Apr 16, 2009
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: CITICORP USA, INC. AS AGENT FOR BANK PRIORITY SECURED PARTIES; CITICORP USA, INC. AS AGENT FOR HEDGE PRIORITY SECURED PARTIES
Reel/Frame 022553/0540 →
SECURITY AGREEMENT Recorded Feb 3, 2009
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: UNITED STATES DEPARTMENT OF THE TREASURY
Reel/Frame 022201/0363 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 14, 2007
From: SOLBRIG, CHARLES E.
To: GM GLOBAL TECHNOLOGY OPERATIONS, INC
Reel/Frame 019558/0112 →
Continuity (1)
Related Publication 20080250778A1 · Oct 16, 2008