Tunable AIG for Improved SCR Performance

• US 20150093315A1
• Filed: 09/29/2014
• Published: 04/02/2015
• Est. Priority Date: 09/27/2013
• Status: Abandoned Application

• Current Assignee: Peerless Manufacturing Company (CECO Environmental Corp.)
• Original Assignee: Peerless Manufacturing Company (CECO Environmental Corp.)
• Inventors: Broderick, Jeffrey Michael, Lindemann, Scott H., Broderick, R. Gifford, Schindler, Edmund S., Valentine, James M.
• Application Number:
  US14/500,358
• Publication Number:
  US 20150093315A1
• Time in Patent Office: Days
• US Class Current: 423/239.1
• CPC Class Codes: B01D 2251/2062 Ammonia
• CPC Class Codes: F01N 2610/02 the substance being ammonia or urea
• CPC Class Codes: F01N 2610/10 the substance being heated, e.g. by heating tank or supply line of the added substance
• CPC Class Codes: F01N 2610/105 Control thereof
• CPC Class Codes: F01N 2610/1453 Sprayers or atomisers; Arrangement thereof in the exhaust apparatus
• 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 system for controlling reagent flow to an exhaust of a lean burn combustion source includes a plurality of decomposition ducts each being connected to at least one injection lance of a reagent injection grid and supplying reagent and hot carrier gas to the injection lance, and at least one metering valve in communication with each of the plurality of decomposition ducts that controls reagent injection rate to the injection lance. A method of controlling a reagent flow to an exhaust of a lean burn combustion source includes providing a reagent injection grid having at least one injection lance, supplying the reagent and hot carrier gas to the reagent injection grid from a plurality of decomposition ducts coupled to the injection grid, and controlling reagent injection rate to the injection grid via at least one metering valve in communication with each of the plurality of decomposition ducts.

Claims

1. A system for controlling a reagent flow to an exhaust of a lean burn combustion source equipped with a catalyst, comprising:

a plurality of decomposition ducts, wherein each decomposition duct is connected to at least one injection lance of a reagent injection grid and supplies reagent and hot carrier gas to said at least one injection lance; and

at least one metering valve in communication with each of said plurality of decomposition ducts, wherein said at least one metering valve controls reagent injection rate to said at least one injection lance of said injection grid.

2. The system of claim 1, wherein each of said plurality of decomposition ducts feeds a plurality of injection lances of said reagent injection grid.

3. The system of claim 1, wherein said plurality of decomposition ducts connect to a common header that supplies a mixture of hot gas and vaporized reagent to said reagent injection grid.

4. The system of claim 1, wherein each of said plurality of decomposition ducts is connected to one injection lance, and wherein the individual lances receive hot carrier gas from a supply header connected to inlet ends of said plurality of decomposition ducts.

5. The system of claim 1, wherein each of said plurality of decomposition ducts has two or more metering valves in communication with the decomposition ducts.

6. The system of claim 1, wherein the hot carrier gas supplied to said reagent injection grid is exhaust gas.

7. The system of claim 1, wherein the hot gas supplied to said reagent injection grid is ambient air heated by a supplemental heater.

8. The system of claim 7, wherein the supplemental heater comprises at least one of an electric heater, heat exchanger and burner.

9. The system of claim 1, wherein the injection rate to the at least one decomposition duct is between about 0.2 and about 40 gallons per hour of aqueous reagent.

10. The system of claim 1, wherein a residence time from a point of reagent injection in the decomposition ducts to an outlet of the injection grid is less than 1 second.

11. The system of claim 1, wherein the hot carrier gas flow to said plurality of decomposition ducts is controlled by at least one flow control valve positioned in each decomposition duct upstream of the at least one metering valve.

12. The system of claim 11, wherein the at least one flow control valve is manually adjusted.

13. The system of claim 11, wherein the at least one flow control valve is automatically adjusted.

14. The system of claim 1, wherein the system further comprises a fan connected to said plurality of decomposition ducts and wherein the hot carrier gas flow is regulated by a variable frequency drive coupled to the fan.

15. The system of claim 1, wherein the system further comprises a fan connected to said plurality of decomposition ducts and wherein the hot carrier gas flow is regulated by a damper positioned at an outlet of the fan.

16. The system of claim 1, wherein said injection grid comprises a plurality of injection lances and wherein the plurality of injection lances flow the same injection rate of the carrier gas, the reagent or a blend thereof at any given operating condition of the combustion source.

17. The system of claim 1, wherein said injection grid comprises a plurality of injection lances and wherein at least one of the plurality of injection lances flows a different rate of injection of the carrier gas, the reagent or a blend thereof at any given operating condition of the combustion source.

18. The system of claim 1, wherein the reagent is urea, and wherein the carrier gas flow rate and gas temperature in said plurality of decomposition ducts before a point of reagent injection are maintained so that a gas temperature of a blended flow after the reagent injection is maintained at about 600 F or greater at an inlet to said reagent injection grid.

19. The system of claim 1, wherein the reagent is aqueous ammonia, and wherein the hot carrier gas flow rate and gas temperature in said plurality of decomposition ducts before a point of reagent injection are maintained so that a gas temperature of a blended flow after the reagent injection is maintained at greater than about 250 F at an inlet to said reagent injection grid.

20. The system of claim 1, wherein the at least one metering valve comprises a pulse width modulated solenoid valve.

21. The system of claim 1, wherein the at least one metering valve comprises a variable speed chemical feed pump.

22. The system of claim 1, wherein the at least one metering valve atomizes the reagent such that it is injected into the decomposition ducts with droplet sizes between about 10 microns and about 70 microns.

23. The system of claim 1, wherein the system further comprises at least one sensor positioned in a primary exhaust duct after a catalyst chamber, and wherein a quantity of the reagent injected into said plurality of decomposition ducts is based at least in part on a measurement of at least one of NOx concentration and ammonia slip received from said at least one sensor.

24. The system of claim 1, further comprising at least one atomizer affixed to each of said plurality of decomposition ducts for supplying atomized reagent to the decomposition ducts.

25. The system of claim 24, wherein said at least one atomizer and said at least one metering valve are formed as an integral unit that defines an atomizing injector.

26. A system for controlling a reagent flow to an exhaust of a lean burn combustion source equipped with a catalyst, comprising:

a reagent injection grid;

at least one decomposition duct coupled to said reagent injection grid, wherein the at least one decomposition duct supplies reagent and hot carrier gas to said reagent grid; and

a plurality of metering valves in communication with said at least one decomposition duct, wherein said plurality of metering valves control reagent injection rate to said injection grid.

27. A method of controlling a reagent flow to an exhaust of a lean burn combustion source equipped with a catalyst, comprising the steps of:

providing a reagent injection grid comprising at least one injection lance;

supplying the reagent and hot carrier gas to said reagent injection grid from a plurality of decomposition ducts coupled to said reagent injection grid; and

controlling reagent injection rate to said at least one injection lance of said injection grid via at least one metering valve in communication with said at least one decomposition duct.

28. The method of claim 27, wherein each of the plurality of decomposition ducts feeds a plurality of injection lances of said reagent injection grid.

29. The method of claim 27, wherein the plurality of decomposition ducts connect to a common header that supplies a mixture of hot gas and vaporized reagent to said reagent injection grid.

30. The method of claim 27, wherein each of the plurality of decomposition ducts is connected to an injection lance, and wherein the hot carrier gas is supplied to the individual lances from a supply header connected to inlet ends of the plurality of decomposition ducts.

31. The method of claim 27, wherein each of said plurality of decomposition ducts has two or more metering valves in communication with the decomposition ducts.

32. The method of claim 27, wherein the hot carrier gas supplied to said reagent injection grid is exhaust gas.

33. The method of claim 27, wherein the hot carrier gas supplied to said reagent injection grid is ambient air and wherein the method further comprises the step of heating the ambient air by a supplemental heater before it is supplied to said reagent injection grid.

34. The method of claim 27, wherein the reagent is injected to the at least one decomposition duct at a rate between about 0.2 and about 40 gallons per hour of aqueous reagent.

35. The method of claim 27, further comprising the step of controlling the hot carrier gas flow to the plurality of decomposition ducts feeding said reagent injection grid via at least one flow control valve positioned in each of the plurality of decomposition ducts upstream of the at least one metering valve.

36. The method of claim 27, wherein said injection grid comprises a plurality of injection lances and wherein the plurality of injection lances flow the same injection rate of the carrier gas, the reagent or a blend thereof at any given operating condition of the combustion source.

37. The method of claim 27, wherein said injection grid comprises a plurality of injection lances and wherein the plurality of injection lances flow a different rate of injection of the carrier gas, the reagent or a blend thereof at any given operating condition of the combustion source.

38. The method of claim 27, wherein the reagent is urea, and wherein the method further comprises the step of setting the carrier gas flow rate and gas temperature in the plurality of decomposition ducts before a point of reagent injection such that a gas temperature of a blended flow after the reagent injection is maintained at about 600 F or greater at an inlet to said reagent injection grid.

39. The method of claim 27, wherein the reagent is aqueous ammonia, and the method further comprises the step of setting the hot carrier gas flow rate and gas temperature in the plurality of decomposition ducts before a point of reagent injection such that a gas temperature of a blended flow after the reagent injection is maintained at greater than about 250 F at an inlet to said reagent injection grid.

40. The method of claim 27, wherein the method further comprises the step of measuring at least one of NOx concentration and ammonia slip via at least one sensor positioned in a primary exhaust duct after a catalyst chamber, wherein a quantity of the reagent injected into the plurality of decomposition ducts is based at least in part on the measurements received from the at least one sensor.

41. The method of claim 27, wherein a residence time from a point of reagent injection in the decomposition ducts to an outlet of the injection grid is less than 1 second.