IP Library Granted Patent US 8,561,557
Granted Patent B2
US 8,561,557 · App. 12/571,187 · Granted Oct 22, 2013

Primary oxidant feed to oxy-fired circulating fluidized bed (CFB)

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Quick Facts
Patent No.
US 8,561,557
App. No.
12/571,187
Granted
Oct 22, 2013
Kind
B2
Abstract

A system for feeding a primary oxidant to an oxy-fired circulating fluidized bed (CFB) boiler. The system includes a plurality of bubble cap assemblies each comprising a stem and a bubble cap with at least one exit hole, each bubble cap connected via a stem to at least one windbox, the windbox containing at least one manifold. A plurality of pipes are provided, each pipe located within a bubble cap assembly with an open end located either at, above or below the exit holes of the bubble caps and an opposite end connected to the manifold located inside each windbox. Recycle gas is piped into the windbox, to the stem, and exiting from the exit holes located in the bubble cap into the CFB. Oxygen is piped into the manifold, through the pipes and exiting through the exit holes located in the bubble cap. The pipe may further contain means placed at its open end, to prevent accidental inlet of hot particles into the pipe, such as a debris shield placed above and proximate to the open end of the pipe or by having the open end oriented in a downward direction. An insulating gap may also be placed inside the bubble cap to reduce thermal conductance between the bubble cap outer surface that is exposed to hot bed material and the inner surface of the bubble cap, being in contact with oxygen.

Claims (51)

1. A system for feeding a primary oxidant to an oxy-fired circulating fluidized bed (CFB) boiler comprising:

a plurality of bubble cap assemblies, each bubble cap assembly including a bubble cap, a stem, one or more exit holes, and an inner and outer surface;

at least one windbox, wherein the at least one windbox has its own controlled oxidant feed and is connected to each of the stems of the plurality of bubble cap assemblies, and wherein the at least one windbox further comprises at least one manifold;

a plurality of pipes, each pipe being located within one of the plurality of bubble cap assemblies, each pipe having an open end that is located at, or below, each of the one or more exit holes of each of the plurality of bubble cap assemblies and each pipe being connected at an opposite end to the at least one manifold contained within its respective windbox;

a first controlled oxidant feed delivered independently to the at least one windbox, through the stem of each bubble cap assembly and through the one or more exit holes of each bubble cap assembly into the CFB and having a concentration of oxygen by volume not exceeding 28% oxygen by volume; and

a second controlled oxidant feed delivered independently through the at least one manifold, to the plurality of pipes and into the plurality of bubble cap assemblies wherein it mixes with the first controlled oxidant feed and exits through the one or more exit holes of the bubble cap and having a concentration of oxygen by volume of at least 28%;

wherein the direction of the exit of the second controlled oxidant feed from the open end of each of the plurality of pipes in each of the plurality of bubble cap assemblies is oriented in a downward direction.

2. The system according to claim 1 , wherein each windbox is equipped with an oxygen measurement probe.

3. The system according to claim 1 , wherein at least an inner surface of the plurality of the bubble caps and stems are coated with, or made from, stainless steel.

4. The system according to claim 1 , wherein at least an inner surface of the plurality of the bubble caps and stems are coated with, or made from, one or more non-metallic materials.

5. The system according to claim 1 , wherein the at least one windbox and the plurality of pipes are made from, or lined with, stainless steel.

6. The system according to claim 1 , wherein the at least one windbox and the plurality of pipes are made from, or lined with, one or more non-metallic materials.

7. The system according to claim 1 , wherein the direction of the exit from the open end of each of the plurality of pipes is oriented downwards by a debris shield attached to the open end of the pipe.

8. A system for feeding a primary oxidant to an oxy-fired circulating fluidized bed (CFB) boiler comprising:

a plurality of bubble cap assemblies, each bubble cap assembly including a bubble cap, a stem, one or more exit holes, and an inner and outer surface;

at least one windbox, wherein the at least one windbox has its own controlled oxidant feed and is connected to each of the stems of the plurality of bubble cap assemblies, and wherein the at least one windbox further comprises at least one manifold;

a plurality of pipes, each pipe being located within one of the plurality of bubble cap assemblies, each pipe having an open end that is located at, or above, each of the one or more exit holes of each of the plurality of bubble cap assemblies and each pipe being connected at an opposite end to the at least one manifold contained within its respective windbox;

a first controlled oxidant feed delivered independently to the at least one windbox, through the stem of each bubble cap assembly and through the one or more exit holes of each bubble cap assembly into the CFB and having a concentration of oxygen by volume not exceeding 28% oxygen by volume; and

a second controlled oxidant feed delivered independently through the at least one manifold, to the plurality of pipes and into the plurality of bubble cap assemblies wherein it mixes with the first controlled oxidant feed and exits through the one or more exit holes of the bubble cap and having a concentration of oxygen by volume of at least 28%;

wherein the direction of the exit of the second controlled oxidant feed from the open end of each of the plurality of pipes in each of the plurality of bubble cap assemblies is oriented in a downward direction.

9. The system according to claim 8 , wherein each windbox is equipped with an oxygen measurement probe.

10. The system according to claim 8 , wherein at least an inner surface of the plurality of the bubble caps and stems are coated with, or made from, stainless steel.

11. The system according to claim 8 , wherein at least an inner surface of the plurality of the bubble caps and stems are coated with, or made from, one or more non-metallic materials.

12. The system according to claim 8 , wherein the at least one windbox and the plurality of pipes are made from, or lined with, stainless steel.

13. The system according to claim 8 , wherein the at least one windbox and the plurality of pipes are made from, or lined with, one or more non-metallic materials.

14. The system according to claim 8 , wherein the direction of the exit from the open end of each of the plurality of pipes is oriented downwards by a debris shield attached to the open end of the pipe.

15. A system for feeding a primary oxidant to an oxy-fired circulating fluidized bed (CFB) boiler comprising:

a plurality of bubble cap assemblies, each bubble cap assembly including a bubble cap, a stem, one or more exit holes, an inner surface and an outer surface, and an insulating gap designed to reduce thermal conductance between the inner surface and the outer surface;

at least one windbox, wherein the at least one windbox has its own controlled oxidant feed and is connected to each of the stems of the plurality of bubble cap assemblies, and wherein the at least one windbox further comprises at least one manifold;

a plurality of pipes, each pipe being located within one of the plurality of bubble cap assemblies, each pipe having an open end that is located at, or below, each of the one or more exit holes of each of the plurality of bubble cap assemblies and each pipe being connected at an opposite end to the at least one manifold contained within its respective windbox;

a first controlled oxidant feed delivered independently to the at least one windbox, through the stem of each bubble cap assembly and through the one or more exit holes of each bubble cap assembly into the CFB and having a concentration of oxygen by volume not exceeding 28%; and

a second controlled oxidant feed delivered independently through the at least one manifold, to the plurality of pipes and into the plurality of bubble cap assemblies wherein it mixes with the first controlled oxidant feed and exits through the one or more exit holes of the bubble cap and having a concentration of oxygen by volume of at least 28%;

wherein the direction of the exit of the second controlled oxidant feed from the open end of each of the plurality of pipes in each of the plurality of bubble cap assemblies is oriented in a downward direction.

16. The system according to claim 15 , wherein each windbox is equipped with an oxygen measurement probe.

17. The system according to claim 15 , wherein at least an inner surface of the plurality of the bubble caps and stems are coated with, or made from, stainless steel.

18. The system according to claim 15 , wherein at least an inner surface of the plurality of the bubble caps and stems are coated with, or made from, one or more non-metallic materials.

19. The system according to claim 15 , wherein the at least one windbox and the plurality of pipes are made from, or lined with, stainless steel.

20. The system according to claim 15 , wherein the at least one windbox and the plurality of pipes are made from, or lined with, one or more non-metallic materials.

21. A system for feeding a primary oxidant to an oxy-fired circulating fluidized bed (CFB) boiler comprising:

a plurality of bubble cap assemblies, each bubble cap assembly including a bubble cap, a stem, one or more exit holes, and an inner and outer surface;

at least one windbox, wherein the at least one windbox has its own controlled oxidant feed and is connected to each of the stems of the plurality of bubble cap assemblies, and wherein the at least one windbox further comprises at least one manifold;

a plurality of pipes, each pipe being located within one of the plurality of bubble cap assemblies, each pipe having an open end that is located at, or above, each of the one or more exit holes of each of the plurality of bubble cap assemblies and each pipe being connected at an opposite end to the at least one manifold contained within its respective windbox;

an insulating gap designed to reduce thermal conductance between the inner and outer surfaces of each of the plurality of bubble caps, the insulating gap located within each of the bubble caps proper;

a first controlled oxidant feed delivered independently to the at least one windbox, through the stem of each bubble cap assembly and through the one or more exit holes of each bubble cap assembly into the CFB and having a concentration of oxygen by volume not exceeding 28% oxygen by volume; and

a second controlled oxidant feed delivered independently through the at least one manifold, to the plurality of pipes and into the plurality of bubble cap assemblies wherein it mixes with the first controlled oxidant feed and exits through the one or more exit holes of the bubble cap and having a concentration of oxygen by volume of at least 28%;

wherein the direction of the exit of the second controlled oxidant feed from the open end of each of the plurality of pipes in each of the plurality of bubble cap assemblies is oriented in a downward direction.

22. The system according to claim 21 , wherein each windbox is equipped with an oxygen measurement probe.

23. The system according to claim 21 , wherein at least an inner surface of the plurality of the bubble caps and stems are coated with, or made from, stainless steel.

24. The system according to claim 21 , wherein at least an inner surface of the plurality of the bubble caps and stems are coated with, or made from, one or more non-metallic materials.

25. The system according to claim 21 , wherein the at least one windbox and the plurality of pipes are made from, or lined with, stainless steel.

26. The system according to claim 21 , wherein the at least one windbox and the plurality of pipes are made from, or lined with, one or more non-metallic materials.

Assignments (13)
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 →
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 26, 2009
From: MARYAMCHIK, MIKHAIL; GODDEN, MARK C.; ALEXANDER, KIPLIN C.; KRAFT, DAVID L.
To: BABCOCK & WILCOX POWER GENERATION GROUP, INC.
Reel/Frame 023420/0446 →