IP Library Granted Patent US 9,097,158
Granted Patent B2
US 9,097,158 · App. 14/219,586 · Granted Aug 4, 2015

Solids transport in flue gas desulfurization system

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Quick Facts
Patent No.
US 9,097,158
App. No.
14/219,586
Granted
Aug 4, 2015
Kind
B2
Abstract

A solids transport system for use in a flue gas desulfurization system is disclosed. Flue gas can be recycled from downstream and used as a fluidizing gas for transporting solids between different locations. Exemplary systems include fluidization slide gravity conveyors, fluidization pads in bins, and in hoppers. The flue gas is generally already at an elevated temperature, reducing power consumption needed to heat the fluidizing gas.

Claims (44)

1. A flue gas desulfurization system, comprising:

a main flue gas path that extends through an absorber vessel, a particle collection device downstream of the absorber vessel, and a stack;

a solids transport system for recycling solid alkaline particles from the particle collection device to the absorber vessel, the solids transport system including at least one fluidized surface, wherein the at least one fluidized surface is created using flue gas, or a combination of flue gas and fluidization air, such that the capacity of at least one air heater and/or at least fan/blower is reduced or is eliminated; and

a flue gas recycle path having at least one take-off point that sends flue gas from the main flue gas path to the solids transport system, the flue gas being used as a fluidizing gas to produce the at least one fluidized surface.

2. The system of claim 1 , wherein the at least one take-off point is located upstream of the absorber vessel in the main flue gas path.

3. The system of claim 1 , wherein the at least one take off point is located downstream of the absorber vessel and upstream of the particle collection device in the main flue gas path.

4. The system of claim 1 , wherein the main flue gas path includes a fan downstream of the particle collection device and upstream of the stack.

5. The system of claim 4 , wherein the at least one take-off point is located downstream of the particle collection device and upstream of the fan in the main flue gas path.

6. The system of claim 4 , wherein the at least one take off point is located downstream of the fan and upstream of the stack in the main flue gas path.

7. The system of claim 1 , wherein the main flue gas path includes an air preheater that is downstream of a boiler and upstream of the absorber vessel, and the at least one take-off point is located upstream of the air preheater.

8. The system of claim 1 , wherein the solids transport system includes a slide leading from the particle collection device, the slide having the at least one fluidized surface.

9. The system of claim 1 , wherein the solids transport system includes a distribution bin that receives recycled solid particles from the particle collection device, the wherein at least one fluidized surface being located in the distribution bin.

10. The system of claim 1 , wherein the solids transport system includes a slide leading from the particle collection device to a distribution bin, the slide and the distribution bin each having a fluidized surface.

11. The system of claim 1 , wherein the solids transport system includes a hopper, the hopper having a fluidized surface.

12. The system of claim 1 , further comprising an air stream that is mixed with the flue gas recycle path so that a mixture of flue gas and air is used as the fluidizing gas.

13. The system of claim 1 , wherein the flue gas recycle path has a plurality of take-off points.

14. A method for recycling solid particles in a flue gas desulfurization system that has a main flue gas path extending through an absorber vessel and a particle collection device downstream of the absorber vessel, comprising:

separating solid particles from clean gas in the particle collection device;

recycling solid alkaline particles from the particle collection device to the absorber vessel using a solids transport system that includes at least one fluidized surface, wherein the at least one fluidized surface is created using flue gas, or a combination of flue gas and fluidization air, such that the capacity of at least one air heater and/or at least fan/blower is reduced or is eliminated;

wherein recycled flue gas is sent from the main flue gas path to the solids transport system through a flue gas recycle path comprising at least one take-off point, and the recycled flue gas is used as a fluidizing gas to produce the at least one fluidized surface upon which the solid particles travel.

15. The method of claim 14 , wherein the at least one take-off point is located upstream of the absorber vessel in the main flue gas path.

16. The method of claim 14 , wherein the at least one take-off point is located downstream of the absorber vessel and upstream of the particle collection device in the main flue gas path.

17. The method of claim 14 , wherein the main flue gas path includes a fan downstream of the particle collection device and upstream of a stack.

18. The method of claim 17 , wherein the at least one take-off point is located downstream of the particle collection device and upstream of the fan in the main flue gas path.

19. The method of claim 17 , wherein the at least one take-off point is located downstream of the fan and upstream of the stack in the main flue gas path.

20. The method of claim 14 , wherein the solids transport system includes a slide leading from the particle collection device, or a distribution bin that receives recycled solid particles from the particle collection device, or a fluidized hopper, and wherein the at least one fluidized surface is located in the slide, the distribution bin, or the hopper.

21. The method of claim 14 , further comprising the step of mixing the recycled flue gas with air to form a mixture of flue gas and air that is used as the fluidizing gas.

22. The method of claim 14 , wherein the flue gas recycle path has a plurality of take-off paths.

23. A flue gas desulfurization system, comprising:

a main flue gas path that extends through a circulating dry scrubber absorber vessel, a particle collection device downstream of the absorber vessel, and a stack;

a solids transport system for recycling solid alkaline particles from the particle collection device to the circulating dry scrubber absorber vessel, the solids transport system including at least one fluidized surface, wherein the at least one fluidized surface is created using flue gas, or a combination of flue gas and fluidization air, such that the capacity of at least one air heater and/or at least fan/blower is reduced or is eliminated; and

a flue gas recycle path having at least one take-off point that sends flue gas from the main flue gas path to the solids transport system, the flue gas being used as a fluidizing gas to produce the at least one fluidized surface.

24. The system of claim 23 , wherein the at least one take-off point is located upstream of the circulating dry scrubber absorber vessel in the main flue gas path.

25. The system of claim 23 , wherein the at least one take-off point is located downstream of the circulating dry scrubber absorber vessel and upstream of the particle collection device in the main flue gas path.

26. The system of claim 23 , wherein the main flue gas path includes a fan downstream of the particle collection device and upstream of the stack.

27. The system of claim 26 , wherein the at least one take-off point is located downstream of the particle collection device and upstream of the fan in the main flue gas path.

28. The system of claim 26 , wherein the at least one take-off point is located downstream of the fan and upstream of the stack in the main flue gas path.

29. The system of claim 23 , wherein the main flue gas path includes an air preheater that is downstream of a boiler and upstream of the absorber vessel, and the at least one take-off point is located upstream of the air preheater.

30. The system of claim 23 , wherein the solids transport system includes a slide leading from the particle collection device, the slide having the at least one fluidized surface.

31. The system of claim 23 , wherein the solids transport system includes a distribution bin that receives recycled solid particles from the particle collection device, the at least one fluidized surface being located in distribution bin.

32. The system of claim 23 , wherein the solids transport system includes a slide leading from the particle collection device to a distribution bin, the slide and the distribution bin each having a fluidized surface.

33. The system of claim 23 , wherein the solids transport system includes a hopper, the hopper having a fluidized surface.

34. The system of claim 23 , further comprising an air stream that is mixed with the flue gas recycle path so that a mixture of flue gas and air is used as the fluidizing gas.

35. The system of claim 23 , wherein the flue gas recycle path has a plurality of take-off points.

Assignments (12)
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 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 →
RELEASE OF SECURITY INTEREST Recorded May 17, 2018
From: LIGHTSHIP CAPITAL LLC
To: BABCOCK & WILCOX ENTERPRISES, INC.; THE BABCOCK & WILCOX COMPANY; DIAMOND POWER INTERNATIONAL, LLC; BABCOCK & WILCOX MEGTEC, LLC; MEGTEC TURBOSONIC TECHNOLOGIES, INC.; BABCOCK & WILCOX UNIVERSAL, INC.; BABCOCK & WILCOX TECHNOLOGY, LLC
Reel/Frame 046182/0829 →
SECURITY INTEREST Recorded Aug 10, 2017
From: THE BABCOCK & WILCOX COMPANY; DIAMOND POWER INTERNATIONAL, LLC; BABCOCK & WILCOX MEGTEC, LLC; MEGTEC TURBOSONIC TECHNOLOGIES, INC.; BABCOCK & WILCOX UNIVERSAL, INC.; BABCOCK & WILCOX TECHNOLOGY, LLC
To: LIGHTSHIP CAPITAL LLC
Reel/Frame 043515/0001 →
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 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 2, 2014
From: GAYHEART, JEB W; LORENZ, DOUGLAS R; MACINNIS, JAMES M; MILLER, ERIC S; ROTH, JONATHAN C
To: BABCOCK & WILCOX POWER GENERATION GROUP, INC.
Reel/Frame 033228/0653 →