Oxygen fired steam generator

Patent metadata

Field	Value
Publication number	US-9638418-B2
Application number	US-46829009-A
Country	US
Kind code	B2
Filing date	May 19, 2009
Priority date	May 19, 2009
Publication date	May 2, 2017
Grant date	May 2, 2017

Abstract

In a method for operating a steam generator, a transport reactor is provided. Only a substantially pure oxygen feed stream is introduced into the transport reactor in an amount sufficient to maintain the transport reactor at or above a specific system load. The specific load is the system load when only the substantially pure oxygen feed stream is provided to the transport reactor at a minimum flow velocity for operating the transport reactor. A fuel is combusted in the presence of the substantially pure oxygen feed stream to produce a flue gas, which contains solid material. The solid material is separated from the flue gas and passed to a heat exchanger. The heat exchange may be one of a moving bed heat exchanger or a fluidized bed heat exchanger. The solid material is directed to the transport reactor to contribute to the combustion process.

First claim

What is claimed is:

1. A method for operating a steam generator comprising:
providing a transport reactor;
introducing only a substantially pure oxygen feed stream into said transport reactor in an amount sufficient to maintain the transport reactor at or above a specific system load, whereby the specific system load is the system load when only the substantially pure oxygen feed stream is provided to the transport reactor at a minimum flow velocity for operating said transport reactor;
introducing a fuel into the transport reactor, wherein the fuel and the substantially pure oxygen are mixed prior to being introduced into the transport reactor and the resulting mixture is introduced into the transport reactor via the same inlet;
combusting the fuel in the presence of said substantially pure oxygen feed stream to produce a flue gas, said flue gas containing solid material;
separating said solid material from the flue gas;
passing the solid material to a heat exchanger;
mixing the solid material with the substantially pure oxygen feed stream and fuel prior to directing the mixture of the solid material, the substantially pure oxygen feed stream, and the fuel to said transport reactor to contribute to the combustion process occurring within the transport reactor; and
directing the mixture of the fuel, substantially pure oxygen feed stream, and solid material into said transport reactor to contribute to the combustion process.

2. A method as defined by claim 1 wherein said substantially pure oxygen feed stream consists of 90-100% oxygen.

3. A method as defined by claim 1 wherein subsequent to separating said flue gas, said method further includes passing separated flue gas portion through an oxygen preheater at which heat from the flue gas is transferred to said substantially pure oxygen feed stream.

4. A method as defined by claim 3 wherein said separator is a cyclone and said method further includes subsequent to said separating and prior to passing said separated flue gas product portion through said oxygen preheater, said separated flue gas portion of said flue gas is directed into a backpass volume having at least one heat exchanger in communication therewith at which heat from said separated flue gas portion is transferred to a working fluid flowing through said at least one heat exchanger.

5. A method as defined by claim 1 further comprising:
providing an inlet into said transport reactor;
providing at least one of supplemental air and supplemental inert gas through said inlet and thereby into said transport reactor when said transport reactor is operating at a velocity below a minimum threshold flow velocity in an amount sufficient to raise said flow velocity through said transport reactor at least to said minimum threshold velocity.

6. A method as defined by claim 1 wherein the heat exchanger is a fluidized bed heat exchanger and said method further includes providing an inlet into said fluidized bed heat exchanger; and introducing a fluidizing gas, via said inlet, into said inlet of said fluidized bed heat exchanger.

7. A method as defined by claim 6 wherein said fluidizing gas is at least one of flue gas, air, and substantially pure oxygen.

8. A method as defined by claim 1 wherein the heat exchanger is one of a moving bed heat exchanger and a fluid bed heat exchanger which include a bypass for allowing at least a portion of said solid material to flow therethrough, and said method further includes controlling temperature in said transport reactor by operating said bypass.

9. A method as defined by claim 8 wherein said heat exchanger is a fluid bed heat exchanger, said method includes providing a throttle valve in fluid communication with said bypass and in fluid communication with said transport reactor; and
operating said throttle valve to control the rate at which said solid material portion is directed into said transport reactor, thereby controlling the temperature within said transport reactor.

10. A method as defined by claim 1 wherein said transport reactor operates at a flow rate of between about 30 ft/sec. to about 50 ft/sec.

11. A method as defined by claim 1 wherein the combusting of the fuel includes operating said transport reactor at a temperature approaching an ash fusion temperature defined by said fuel.

12. A method as defined by claim 11 wherein said substantially pure oxygen feed stream comprises 90-100% oxygen.

13. A method as defined by claim 11 wherein introducing a substantially pure oxygen feed stream into said transport reactor occurs when said transport reactor is operating at substantially full load, the method comprising introducing said substantially pure oxygen feed stream into said transport reactor at a rate and pressure sufficient to cause said substantially pure oxygen feed stream to function as a primary draft source for the steam generator.

14. A method as defined by claim 1 wherein the heat exchanger is a moving bed heat exchanger.

15. A method for operating a steam generator, said method comprising:
providing a transport reactor;
introducing only a substantially pure oxygen feed stream into said transport reactor in an amount sufficient to maintain a desired flow velocity, above a minimum threshold velocity through said transport reactor;
introducing a fuel into the transport reactor, wherein the fuel and the substantially pure oxygen are mixed prior to being introduced into the transport reactor and the resulting mixture is introduced into the transport reactor through an inlet in the transport reactor;
combusting the fuel in the presence of said substantially pure oxygen feed stream to produce a flue gas, said flue gas containing solid material, at least a portion of which is hot ash;
providing a cyclone having an inlet in fluid communication with an exit defined by said transport reactor so that said flue gas is directed into said cyclone;
said cyclone operating to separate said flue gas into an end product portion and a recycled product portion;
passing the recycled product portion which includes at least a portion of said hot ash of said solid material, through a moving bed heat exchanger in fluid communication with an outlet of said cyclone;
passing the end product portion through an oxygen preheater at which heat from the flue gas is transferred to the substantially pure oxygen feed stream;
mixing the recycled product portion with the substantially pure oxygen feed stream and fuel to form a mixture prior to the mixture being directed to the transport reactor for further combustion; and
directing the mixture of the fuel, substantially pure oxygen feed stream, and the recycled product portion into the transport reactor to contribute to the combustion process.

16. A method as defined by claim 15 wherein said substantially pure oxygen feed stream consists of 95-100% oxygen.

17. A method as defined by claim 16 further comprising providing an inlet into said transport reactor; and providing at least one of supplemental air and supplemental inert gas through said inlet and thereby into said transport reactor when said transport reactor is operating at a velocity below a minimum threshold velocity in an amount sufficient to raise said flow velocity through said transport reactor at least to said minimum threshold velocity.

18. A method as defined by claim 16 wherein said transport reactor operates at a flow rate of between about 30 ft/sec. to about 50 ft/sec.

19. A method as defined by claim 15 wherein said method includes, subsequent to separating said flue

Assignees

• Chiu John H
• Mylchreest George D
• General Electric Technology Gmbh

Inventors

• Chiu John H
• Mylchreest George D

Classifications

• F23C2206/103

  Cooling recirculating particles · CPC title

• Y02E20/344

  Cross-Sectional Technologies · mapped topic

• F23C10/10 Primary

  the separation apparatus being located outside the combustion chamber · CPC title

• F23L7/007 Primary

  Supplying oxygen or oxygen-enriched air · CPC title

• F23L7/00

  Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam · CPC title