IP Library Granted Patent US 8,434,430
Granted Patent B2
US 8,434,430 · App. 12/570,823 · Granted May 7, 2013

In-bed solids control valve

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Quick Facts
Patent No.
US 8,434,430
App. No.
12/570,823
Granted
May 7, 2013
Kind
B2
Abstract

A circulating fluidized bed (CFB) boiler comprising a reaction chamber. A bubbling fluidized bed (BFB) is contained within an enclosure within the lower portion of the reaction chamber and contains an in-bed heat exchanger (IBHX) that occupies part of the reaction chamber floor. At least one non-mechanical valve, which includes an opening between the CFB and BFB and independently controlled fluidizing means located both upstream and downstream of the opening, is used to control the heat transfer to the IBHX by controlling the solids discharge from the BFB to the CFB. The elevation of the bottom of the opening is at or above the elevation of the fluidizing means. A flow control barrier may be located downstream of the opening.

Claims (35)

1. A circulating fluidized bed (CFB) boiler comprising:

a CFB reaction chamber having side walls and a grid defining a floor at a lower end of the CFB reaction chamber for providing fluidizing gas into the CFB reaction chamber;

a bubbling fluidized bed (BFB) located within a lower portion of the CFB reaction chamber and being bound by enclosure walls and the floor of the CFB reaction chamber;

at least one controllable in-bed heat exchanger (IBHX), the IBHX occupying part of the lower end of the CFB reaction chamber and being surrounded by the enclosure walls of the BFB;

at least one non-mechanical valve designed to permit the control of solids discharge from the BFB into the CFB reaction chamber, the valve including at least one opening in the enclosure wall of the BFB, at least one independently controlled first fluidizing means located upstream of the at least one opening in the enclosure wall, at least one independently controlled second fluidizing means located downstream of the at least one opening in the enclosure wall, and

at least one flow control barrier that is located downstream of the at least one opening in the enclosure wall, wherein the elevation of the top of the flow control barrier is at or above the elevation of the bottom of the at least one opening in the enclosure wall;

wherein the elevation of the bottom of the at least one non-mechanical valve opening in the enclosure wall being at or above the top of both of the independently controlled first and second fluidizing means.

2. The CFB boiler according to claim 1 , wherein the at least one flow control barrier is located downstream of the at least one independently controlled second fluidizing means.

3. The CFB boiler according to claim 1 , wherein the at least one flow control barrier is located upstream of the at least one independently controlled second fluidizing means.

4. The CFB boiler according to claim 1 , wherein the at least one flow control barrier is made of an abrasion resistant material.

5. The CFB boiler according to claim 1 , wherein the at least one flow control barrier is made of refractory-covered tubes.

6. The CFB boiler according to claim 1 , wherein the at least one IBHX is selected from one or more of a superheater, a reheater, an economizer or an evaporative surface.

7. The CFB boiler according to claim 1 , wherein tubes of the at least one IBHX are arranged so that they are not in the vicinity of the at least one opening in order to reduce erosion of the tubes.

8. The CFB boiler according to claim 1 , wherein the tubes of the at least one IBHX are protected by a layer of erosion-resistant material formed on the surface of the tubes in the vicinity of the at least one opening.

9. A circulating fluidized bed (CFB) boiler comprising:

a CFB reaction chamber having side walls and a grid defining a floor at a lower end of the CFB reaction chamber for providing fluidizing gas into the CFB reaction chamber;

a bubbling fluidized bed (BFB) located within a lower portion of the CFB reaction chamber, the BFB being above a grid for providing fluidizing gas into the BFB, and being bound by enclosure walls and the floor of the CFB reaction chamber;

at least one controllable in-bed heat exchanger (IBHX), the IBHX occupying a lower part of the CFB reaction chamber and being surrounded by the enclosure walls of the BFB; and

at least one non-mechanical valve designed to permit the control of solids discharge from the BFB into the CFB reaction chamber, the valve including at least one opening in the enclosure wall of the BFB, at least one independently controlled first fluidizing means located upstream of the at least one opening in the enclosure wall, at least one independently controlled second fluidizing means located downstream of the at least one opening in the enclosure wall,

wherein the first and second independently controlled fluidizing means are separately controllable from the at least one grid;

wherein the elevation of the bottom of the at least one non-mechanical valve opening in the enclosure wall being at or above the top of both of the independently controlled first and second fluidizing means,

wherein the at least one IBHX is selected from one or more of a superheater, a reheater, an economizer or an evaporative surface, and

wherein the tubes of the at least one IBHX are protected by a layer of erosion- resistant material formed on the surface of the tubes in the vicinity of the at least one opening.

10. The CFB boiler according to claim 9 , further comprising at least one flow control barrier that is located downstream of the at least one opening in the enclosure wall, wherein the elevation of the top of the flow control barrier is at or above the elevation of the bottom of the at least one opening in the enclosure wall.

11. The CFB boiler according to claim 10 , wherein the at least one flow control barrier is located downstream of the at least one independently controlled second fluidizing means.

12. The CFB boiler according to claim 10 , wherein the at least one flow control barrier is located upstream of the at least one independently controlled second fluidizing means.

13. The CFB boiler according to claim 10 , wherein the at least one flow control barrier is made of an abrasion resistant material.

14. The CFB boiler according to claim 10 , wherein the at least one flow control barrier is made of refractory-covered tubes.

15. The CFB boiler according to claim 9 , wherein tubes of the at least one IBHX are arranged so that they are not in the vicinity of the at least one opening in order to reduce erosion of the tubes.

16. A circulating fluidized bed (CFB) boiler comprising:

a CFB reaction chamber having side walls and a grid defining a floor at a lower end of the CFB reaction chamber for providing fluidizing gas into the CFB reaction chamber;

a bubbling fluidized bed (BFB) located within a lower portion of the CFB reaction chamber and being bound by enclosure walls and the floor of the CFB reaction chamber;

at least one controllable in-bed heat exchanger (IBHX), the IBHX occupying part of the lower end of the CFB reaction chamber and being surrounded by the enclosure walls of the BFB;

at least one non-mechanical valve designed to permit the control of solids discharge from the BFB into the CFB reaction chamber, the valve including at least one opening in the enclosure wall of the BFB, at least one independently controlled first fluidizing means located upstream of the at least one opening in the enclosure wall, at least one independently controlled second fluidizing means located downstream of the at least one opening in the enclosure wall, and

at least one flow control barrier that is located downstream of the at least one opening in the enclosure wall, wherein the elevation of the top of the flow control barrier is at or above the elevation of the bottom of the at least one opening in the enclosure wall.

Assignments (8)
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 →
NOTICE OF GRANT OF SECURITY INTEREST IN PATENTS Recorded Sep 30, 2010
From: BABCOCK & WILCOX POWER GENERATION GROUP, INC. (F.K.A. THE BABCOCK & WILCOX COMPANY)
To: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 025066/0080 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 20, 2009
From: MARYAMCHIK, MIKHAIL; GODDEN, MARK C.; ALEXANDER, KIPLIN C.; KRAFT, DAVID L.
To: BABCOCK & WILCOX POWER GENERATION GROUP, INC.
Reel/Frame 023393/0531 →