IP Library Granted Patent US 9,874,350
Granted Patent B2
US 9,874,350 · App. 14/246,380 · Granted Jan 23, 2018

System and method for increasing the service life and/or catalytic activity of an SCR catalyst and control of multiple emissions

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Quick Facts
Patent No.
US 9,874,350
App. No.
14/246,380
Granted
Jan 23, 2018
Kind
B2
Abstract

The present invention relates generally to the field of emission control equipment for boilers, heaters, kilns, or other flue gas-, or combustion gas-, generating devices (e.g., those located at power plants, processing plants, etc.) and, in particular to a new and useful method and apparatus for reducing or preventing the poisoning and/or contamination of an SCR catalyst. In another embodiment, the method and apparatus of the present invention is designed to protect the SCR catalyst. In still another embodiment, the present invention relates to a method and apparatus for increasing the service life and/or catalytic activity of an SCR catalyst while simultaneously controlling various emissions.

Claims (75)

1. A method for increasing the active life of an SCR catalyst, the method comprising the steps of:

(a) providing a fuel to a furnace, or boiler, wherein the fuel is selected from a form of biomass;

(b) subjecting the fuel to a combustion process, wherein the combustion process produces at least one gaseous phosphorus compound and/or at least one gaseous phosphorus-containing compound;

(c) providing at least one iron-bearing compound to a combustion zone or flue gas stream of the furnace, or boiler, prior to entry of the flue gas into an SCR, wherein the SCR is located upstream of at least one air heater; and

(d) permitting the at least one iron-bearing compound to react with the at least one gaseous phosphorus compound and/or the at least one gaseous phosphorus-containing compound present in the combustion zone or flue gas prior to the entry of the flue gas into the SCR to form an iron phosphorus-containing compound.

2. The method of claim 1 , wherein the at least one iron-bearing compound is selected from metallic iron, one or more iron oxides, iron carbonate, or mixtures of two or more thereof.

3. The method of claim 1 , wherein the at least one iron-bearing compound is selected from iron (III) oxide, iron (II) carbonate, iron (II) oxide, or mixtures of two or more thereof.

4. The method of claim 1 , wherein the at least one iron-bearing compound is selected from iron (III) oxide, iron (II) carbonate, or a mixture thereof.

5. The method of claim 1 , wherein the at least one iron-bearing compound is provided to the combustion zone via addition to the biomass.

6. The method of claim 1 , wherein the at least one iron-bearing compound is provided to the combustion zone via a dedicated supply line.

7. The method of claim 1 , wherein the at least one iron-bearing compound is a water soluble iron-bearing compound.

8. The method of claim 1 , wherein the at least one iron-bearing compound is a water soluble iron-bearing compound that is supplied in the form of an aqueous solution.

9. The method of claim 1 , wherein the at least one iron-bearing compound is a water insoluble iron-bearing compound that is supplied in the form of an aqueous suspension or emulsion.

10. The method of claim 1 , wherein the at least one iron-bearing compound is at least one iron-bearing halide, and wherein Step (d) involves:

permitting the iron portion of the at least one iron-bearing halide compound to react with the at least one gaseous phosphorus compound and/or the at least one gaseous phosphorus-containing compound present in the combustion zone or flue gas prior to the entry of the flue gas into the SCR to form an iron phosphorus-containing compound; and

wherein the method further includes the step of:

(e) permitting the halide portion of the at least one iron-bearing halide compound to react with any gaseous mercury compounds, or mercury-containing compounds, present in the combustion zone or flue gas.

11. The method of claim 10 , wherein the at least one iron-bearing halide compound is selected from iron (II) bromide, iron (III) bromide, iron (II) chloride, iron (III) chloride, iron (II) iodide, iron (III) iodate, or mixtures of two or more thereof.

12. The method of claim 10 , wherein the at least one iron-bearing halide compound is iron (II) bromide.

13. The method of claim 10 , wherein the at least one iron-bearing halide compound is provided at an amount sufficient to yield a halide concentration of between about 10 ppm to about 200 ppm.

14. A method for sequestering one or more gaseous phosphorus compounds, or gaseous phosphorus-containing compounds, in the form of one or more less reactive iron-phosphorus-containing compounds, the method comprising the steps of:

(i) providing a fuel to a furnace, or boiler, wherein the fuel is selected from a form of biomass;

(ii) subjecting the fuel to a combustion process, wherein the combustion process produces at least one gaseous phosphorus compound and/or at least one gaseous phosphorus-containing compound;

(iii) providing at least one iron-bearing compound to a combustion zone or flue gas stream of the furnace, or boiler; and

(iv) permitting the at least one iron-bearing compound to react with the at least one gaseous phosphorus compound and/or the at least one gaseous phosphorus-containing compound present in the combustion zone or flue gas to form one or more less reactive iron-phosphorus-containing compounds.

15. The method of claim 14 , wherein the at least one iron-bearing compound is selected from metallic iron, one or more iron oxides, iron carbonate, or mixtures of two or more thereof.

16. The method of claim 14 , wherein the at least one iron-bearing compound is selected from iron (III) oxide, iron (II) carbonate, iron (II) oxide, or mixtures of two or more thereof.

17. The method of claim 14 , wherein the at least one iron-bearing compound is selected from iron (III) oxide, iron (II) carbonate, or a mixture thereof.

18. The method of claim 14 , wherein the at least one iron-bearing compound is provided to the combustion zone via addition to the biomass.

19. The method of claim 14 , wherein the at least one iron-bearing compound is provided to the combustion zone via a dedicated supply line.

20. The method of claim 14 , wherein the at least one iron-bearing compound is a water soluble iron-bearing compound.

21. The method of claim 14 , wherein the at least one iron-bearing compound is a water soluble iron-bearing compound that is supplied in the form of an aqueous solution.

22. The method of claim 14 , wherein the at least one iron-bearing compound is a water insoluble iron-bearing compound that is supplied in the form of an aqueous suspension or emulsion.

23. The method of claim 14 , wherein the at least one iron-bearing compound is at least one iron-bearing halide, and wherein Step (iv) involves:

permitting the iron portion of the at least one iron-bearing halide compound to react with the at least one gaseous phosphorus compound and/or the at least one gaseous phosphorus-containing compound present in the combustion zone or flue gas to form an iron phosphorus-containing compound; and

wherein the method further includes the step of:

(v) permitting the halide portion of the at least one iron-bearing halide compound to react with any gaseous mercury compounds, or mercury-containing compounds, present in the combustion zone or flue gas.

24. The method of claim 23 , wherein the at least one iron-bearing halide compound is selected from iron (II) bromide, iron (III) bromide, iron (II) chloride, iron (III) chloride, iron (II) iodide, iron (III) iodate, or mixtures of two or more thereof.

25. The method of claim 23 , wherein the at least one iron-bearing halide compound is iron (II) bromide.

26. The method of claim 23 , wherein the at least one iron-bearing halide-bearing compound is provided at an amount sufficient to yield a halide concentration of between about 10 ppm to about 200 ppm.

27. A method for increasing the active life of an SCR catalyst, the method comprising the steps of:

(A) providing a fuel to a furnace, or boiler, wherein the fuel is selected from a form of biomass;

(B) subjecting the fuel to a combustion process, wherein the combustion process produces at least one gaseous phosphorus compound and/or at least one gaseous phosphorus-containing compound;

(C) providing at least one iron-bearing compound to a combustion zone or flue gas stream of the furnace, or boiler, prior to entry of the flue gas into an SCR, wherein the SCR is located upstream of at least one air heater; and

(D) permitting the at least one iron-bearing compound to react with the at least one gaseous phosphorus compound and/or the at least one gaseous phosphorus-containing compound present in the combustion zone or flue gas prior to the entry of the flue gas into the SCR to form an iron phosphorus-containing compound,

wherein the method achieves an increase in either one, or both, of a catalytic activity and/or a catalytic lifespan of at least about 10 percent at an operational time of at least about 4,000 hours.

28. The method of claim 27 , wherein the at least one iron-bearing compound is selected from metallic iron, one or more iron oxides, iron carbonate, or mixtures of two or more thereof.

29. The method of claim 27 , wherein the at least one iron-bearing compound is selected from iron (III) oxide, iron (II) carbonate, iron (II) oxide, or mixtures of two or more thereof.

30. The method of claim 27 , wherein the at least one iron-bearing compound is selected from iron (III) oxide, iron (II) carbonate, or a mixture thereof.

31. The method of claim 27 , wherein the at least one iron-bearing compound is provided to the combustion zone via addition to the biomass.

32. The method of claim 27 , wherein the at least one iron-bearing compound is provided to the combustion zone via a dedicated supply line.

33. The method of claim 27 , wherein the at least one iron-bearing compound is a water soluble iron-bearing compound.

34. The method of claim 27 , wherein the at least one iron-bearing compound is a water soluble iron-bearing compound that is supplied in the form of an aqueous solution.

35. The method of claim 27 , wherein the at least one iron-bearing compound is a water insoluble iron-bearing compound that is supplied in the form of an aqueous suspension or emulsion.

36. The method of claim 27 , wherein the method further includes the step of:

(E) providing at least one halide-bearing compound to a combustion zone or flue gas stream of a furnace, or boiler, prior to entry of the flue gas into an SCR, with the proviso that halide-bearing compound is not an iron halide; and

(F) permitting the at least one halide-bearing compound to react with and/or oxidize any mercury present in the combustion zone or flue gas.

37. The method of claim 36 , wherein the at least one halide-bearing compound is selected from potassium bromide, potassium chloride, potassium fluoride, potassium iodide, sodium bromide, sodium chloride, sodium fluoride, sodium iodide, calcium bromide, calcium chloride, calcium fluoride, calcium iodide, aluminum bromide, aluminum chloride, aluminum fluoride, aluminum iodide, transition metal halides with the proviso that the transition metal is not iron, or any mixture of two or more thereof or mixtures of two or more thereof.

38. The method of claim 36 , wherein the at least one iron-bearing compound is selected from iron (II) carbonate and the at least one halide-bearing compound is selected from calcium bromide.

39. The method of claim 36 , wherein the at least one halide-bearing compound is provided at an amount sufficient to yield a halide concentration of between about 10 ppm to about 200 ppm.

40. A method for increasing the active life of an SCR catalyst, the method comprising the steps of:

(I) providing a fuel to a furnace, or boiler, wherein the fuel is selected from a form of biomass;

(II) subjecting the fuel to a combustion process, wherein the combustion process produces at least one gaseous phosphorus compound and/or at least one gaseous phosphorus-containing compound;

(III) providing at least one iron-bearing compound to a combustion zone or flue gas stream of the furnace, or boiler, prior to entry of the flue gas into an SCR, wherein the SCR is located upstream of at least one air heater;

(IV) permitting the at least one iron-bearing compound to react with the at least one gaseous phosphorus compound and/or the at least one gaseous phosphorus-containing compound present in the combustion zone or flue gas prior to the entry of the flue gas into the SCR to form an iron phosphorus-containing compound;

(V) providing at least one halide-bearing compound to a combustion zone or flue gas stream of a furnace, or boiler, prior to entry of the flue gas into an SCR, with the proviso that halide-bearing compound is not an iron halide; and

(VI) permitting the at least one halide-bearing compound to react with and/or oxidize any mercury present in the combustion zone or flue gas.

41. The method of claim 40 , wherein the at least one iron-bearing compound is selected from metallic iron, one or more iron oxides, iron carbonate, or mixtures of two or more thereof.

42. The method of claim 40 , wherein the at least one iron-bearing compound is selected from iron (III) oxide, iron (II) carbonate, iron (II) oxide, or mixtures of two or more thereof.

43. The method of claim 40 , wherein the at least one iron-bearing compound is selected from iron (III) oxide, iron (II) carbonate, or a mixture thereof.

44. The method of claim 40 , wherein the at least one halide-bearing compound is selected from potassium bromide, potassium chloride, potassium fluoride, potassium iodide, sodium bromide, sodium chloride, sodium fluoride, sodium iodide, calcium bromide, calcium chloride, calcium fluoride, calcium iodide, aluminum bromide, aluminum chloride, aluminum fluoride, aluminum iodide, transition metal halides with the proviso that the transition metal is not iron, or any mixture of two or more thereof or mixtures of two or more thereof.

45. The method of claim 40 , wherein the at least one iron-bearing compound is selected from iron (II) carbonate and the at least one halide-bearing compound is selected from calcium bromide.

46. The method of claim 40 , wherein the at least one iron-bearing compound is a water soluble iron-bearing compound.

47. The method of claim 40 , wherein the at least one iron-bearing compound is a water soluble iron-bearing compound that is supplied in the form of an aqueous solution.

48. The method of claim 40 , wherein the at least one iron-bearing compound is a water insoluble iron-bearing compound that is supplied in the form of an aqueous suspension or emulsion.

Assignments (10)
SECURITY INTEREST Recorded Jul 18, 2025
From: BABCOCK & WILCOX ENTERPRISES, INC.; THE BABCOCK & WILCOX COMPANY; DIAMOND POWER INTERNATIONAL, LLC; BABCOCK & WILCOX SPIG, INC.; BABCOCK & WILCOX CANADA CORP.; BABCOCK & WILCOX FPS INC.
To: B. RILEY FINANCIAL, INC.
Reel/Frame 072053/0943 →
SECURITY INTEREST Recorded May 23, 2025
From: BABCOCK & WILCOX ENTERPRISES, INC.; THE BABCOCK & WILCOX COMPANY; DIAMOND POWER INTERNATIONAL, LLC; BABCOCK & WILCOX SPIG, INC.; BABCOCK & WILCOX CANADA CORP.; BABCOCK & WILCOX FPS INC.
To: GLAS TRUST COMPANY LLC
Reel/Frame 071371/0835 →
SECURITY INTEREST Recorded Mar 3, 2025
From: BABCOCK & WILCOX ENTERPRISES, INC.; THE BABCOCK & WILCOX COMPANY; DIAMOND POWER INTERNATIONAL, LLC; BABCOCK & WILCOX SPIG, INC.; BABCOCK & WILCOX CANADA CORP.; BABCOCK & WILCOX FPS INC.
To: PENSION BENEFIT GUARANTY CORPORATION
Reel/Frame 070380/0647 →
RELEASE OF SECURITY INTEREST Recorded Sep 13, 2024
From: MSD PCOF PARTNERS XLV, LLC
To: THE BABCOCK & WILCOX COMPANY; DIAMOND POWER INTERNATIONAL, LLC; AMERICON LLC
Reel/Frame 069017/0362 →
SECURITY INTEREST Recorded Jan 19, 2024
From: BABCOCK & WILCOX ENTERPRISES, INC.; THE BABCOCK & WILCOX COMPANY; DIAMOND POWER INTERNATIONAL, LLC; BABCOCK & WILCOX SPIG, INC.; BABCOCK & WILCOX CANADA CORP.; BABCOCK & WILCOX FPS INC.
To: AXOS BANK, AS ADMINISTRATIVE AGENT
Reel/Frame 066354/0765 →
SECURITY INTEREST Recorded Jul 22, 2021
From: THE BABCOCK & WILCOX COMPANY (F/K/A BABCOCK & WILCOX POWER GENERATION GROUP, INC.); BABCOCK & WILCOX SPIG, INC.; BABCOCK & WILCOX TECHNOLOGY, LLC; DIAMOND POWER INTERNATIONAL, LLC (F/K/A DIAMOND POWER INTERNATIONAL, INC.)
To: MSD PCOF PARTNERS XLV, LLC, AS AGENT
Reel/Frame 056962/0486 →
RELEASE OF SECURITY INTEREST Recorded Jul 1, 2021
From: BANK OF AMERICA, N.A.
To: DIAMOND POWER INTERNATIONAL, LLC (F/K/A DIAMOND POWER INTERNATIONAL, INC.); MEGTEC TURBOSONIC TECHNOLOGIES, INC.; THE BABCOCK & WILCOX COMPANY (F/K/A BABCOCK & WILCOX POWER GENERATION GROUP, INC.); BABCOCK & WILCOX SPIG, INC.; BABCOCK & WILCOX TECHNOLOGY, LLC (F/K/A MCDERMOTT TECHNOLOGY, INC.); SOFCO-EFS HOLDINGS LLC; BABCOCK & WILCOX MEGTEC, LLC
Reel/Frame 057337/0823 →
CHANGE OF NAME Recorded Sep 24, 2015
From: BABCOCK & WILCOX POWER GENERATION GROUP, INC.
To: THE BABCOCK & WILCOX COMPANY
Reel/Frame 036675/0434 →
SECURITY INTEREST Recorded Jul 28, 2015
From: BABCOCK & WILCOX POWER GENERATION GROUP, INC. (TO BE RENAMED THE BABCOCK AND WILCOX COMPANY)
To: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 036201/0598 →
SECURITY INTEREST Recorded Jul 22, 2014
From: BABCOCK & WILCOX POWER GENERATION GROUP, INC.
To: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 033380/0744 →