Oxy-fuel combustion oxidant heater internal arrangement

Patent metadata

Field	Value
Publication number	US-9581330-B2
Application number	US-201414462531-A
Country	US
Kind code	B2
Filing date	Aug 18, 2014
Priority date	Jul 10, 2007
Publication date	Feb 28, 2017
Grant date	Feb 28, 2017

Abstract

A regenerative oxidant preheater internal arrangement, including a system and method for use thereof, utilizing a unique recycle oxy-combustion methodology which includes at least two primary combustion oxidant sectors placed adjacent to both the flue gas side as well as a secondary oxidant sector positioned between the two primary sectors. A tri-sector regenerative oxidant preheater apparatus, method and arrangement for utilization with oxy-fired pulverized coal combustion power plants.

First claim

What is claimed is:

1. A tri-sector rotary regenerative oxidant preheater including a stationary housing, a rotor rotatably mounted in the housing, sector plates located at the axial ends of the rotor for dividing the preheater into a flue gas sector, a secondary oxidant sector, and two primary oxidant sectors, the secondary oxidant sector being interposed between the primary oxidant sectors, and wherein during operation of the preheater, the flue gas sector and the primary oxidant sectors have a negative pressure environment, and the secondary oxidant sector has a positive pressure environment.

2. The preheater according to claim 1 , wherein there is substantially no pressure differential between the environments of the flue gas sector and the primary oxidant sectors.

3. The preheater according to claim 1 , wherein the environments in the flue gas sector and the primary oxidant sectors are at a negative pressure of about 5 inches wg.

4. The preheater according to claim 1 , wherein the environment in the secondary oxidant sector is at a positive pressure of about 20 inches wg.

5. The preheater according to claim 1 , wherein the primary oxidant sector bordering the three o'clock side of the flue gas sector is larger than the primary oxidant sector bordering the nine o'clock side of the flue gas sector.

6. The preheater according to claim 1 , wherein the primary oxidant sector bordering the three o'clock side of the flue gas sector is smaller than the primary oxidant sector bordering the nine o'clock side of the flue gas sector.

7. The preheater according to claim 1 , wherein the primary oxidant sectors are of substantially equal size.

8. An oxidant preheater internal sector arrangement comprising:
a flue gas side consisting of a sector, through which a flue gas stream having an air pressure, flows away from a boiler having a gas exit as the flue gas stream leaves the gas exit; and
a counterflowing combustion oxidant side, the combustion oxidant side being comprised of:
at least one secondary combustion oxidant sector through which an oxygenated secondary combustion oxidant stream flows toward the boiler, the secondary combustion oxidant stream having an air pressure; and
at least two primary combustion oxidant sectors through which a pressurized cold primary combustion oxidant stream flows toward the boiler, the primary combustion oxidant stream having an air pressure greater than that of the secondary combustion oxidant stream and the flue gas stream;

wherein two of the at least two primary combustion oxidant sectors are positioned adjacent to both the flue gas side and to the at least one secondary combustion oxidant sector; and
wherein the at least one secondary combustion oxidant sector is located between the at least two primary combustion oxidant sectors.

9. The oxidant preheater internal arrangement as claimed in claim 8 , comprising two secondary combustion oxidant sectors.

10. The oxidant preheater internal arrangement as claimed in claim 9 , comprising three primary combustion oxidant sectors.

11. The oxidant preheater internal arrangement as claimed in claim 8 , wherein the primary combustion oxidant stream has an air pressure between +40 to +45 inches water gauge, the secondary combustion oxidant stream has an air pressure between +20 to +25 inches water gauge and the flue gas stream has an air pressure between 0 to −5 inches water gauge.

12. A system for warm-recycle oxy-fuel combustion comprising:
an oxidant preheater for recycling waste heat from a boiler and cooling flue gas from the boiler, the oxidant preheater having an internal arrangement as claimed in claim 8 ;
a primary oxidant fan for feeding primary oxidant flow to the oxidant preheater positioned upstream from the oxidant heater; and
a primary oxidant mixer for introducing an oxidant into the primary combustion oxidant stream positioned downstream from the oxidant heater.

13. The system for warm-recycle oxy-fuel combustion as claimed in claim 12 , wherein the oxidant preheater comprises two secondary combustion oxidant sectors.

14. The system for warm-recycle oxy-fuel combustion as claimed in claim 12 , wherein the oxidant introduced into the primary combustion oxidant stream is pure oxygen or atmospheric air.

15. The system for warm-recycle oxy-fuel combustion as claimed in claim 14 , wherein oxygen is introduced into the primary combustion oxidant stream and before it is introduced the oxygen is preheated.

16. The system for warm recycle oxy-fuel combustion as claimed in claim 12 , wherein the primary combustion oxidant stream has a pressure of about +40 to +45 inches water gauge, the secondary combustion oxidant stream has a pressure of about +20 to +25 inches water gauge and the flue gas stream has a pressure of about 0 to −5 inches water gauge.

17. The system for warm recycle oxy-fuel combustion as claimed in claim 12 , comprising three primary combustion oxidant sectors.

18. The system for warm recycle oxy-fuel combustion as claimed in claim 12 , further comprising:
a secondary oxidant fan for feeding secondary oxidant flow to the oxidant preheater positioned upstream from the oxidant heater; and
a secondary oxidant mixer for introducing an oxidant into the secondary combustion oxidant stream positioned upstream from the oxidant preheater and downstream from the secondary oxidant fan.

19. The system for warm-recycle oxy-fuel combustion as claimed in claim 18 , wherein the secondary oxidant fan operates at a temperature of at least 300° F. and the primary oxidant fan operates at a temperature of 170° F. or lower.

20. The system for warm recycle oxy-fuel combustion as claimed in claim 19 , wherein after passing through the oxidant preheater the secondary combustion oxidant stream flows to a windbox which is connected to the boiler, and wherein after passing through the oxidant heater, the primary combustion oxidant stream flows to a coal pulverizer.

21. The system for warm-recycle oxy-fuel combustion as claimed in claim 20 , further comprising:
a particulate removal unit for removing particulate matter from the secondary combustion oxidant stream position upstream from the secondary oxidant fan;
an analytical quality control services (AQCS) unit located on an intermediate flue gas stream; and
a portion of the flue gas stream which exits the oxidant heater, wherein the portion is divided and forms the secondary combustion oxidant stream as well as the intermediate flu gas stream,
wherein after passing through the AQCS unit, the intermediate flue gas stream is divided and forms the primary combustion oxidant stream, and a compression and purification stream which leads to a compression and purification unit.

Assignees

• Babcock & Wilcox Power Generat
• Babcock & Wilcox Co

Inventors

• Mcdonald Dennis K
• Alexander Kiplin C
• Kraft David L

Classifications

• Y02E20/344

  Cross-Sectional Technologies · mapped topic

• F23N3/002

  using electronic means (F23N3/02 - F23N3/08 take precedence) · CPC title

• F23L15/02

  Arrangements of regenerators · CPC title

• F23D1/00

  Burners for combustion of pulverulent fuel · CPC title

• F28D19/044

  shaped in sector form, e.g. with baskets · CPC title