Hybrid lean premixing catalytic combustion system for gas turbines

• US 6,658,856 B2
• Filed: 01/17/2002
• Issued: 12/09/2003
• Est. Priority Date: 01/17/2002
• Status: Expired due to Fees

• Current Assignee: Vericor Power Systems
• Original Assignee: Vericor Power Systems LLC (MTU)
• Inventors: Critchley, Ian L.
• Primary Examiner(s): Freay, Charles G.
• Assistant Examiner(s): Belena, John F.
• Application Number:
  US10/052,976
• Publication Number:
  US 20030134240A1
• Time in Patent Office: 691 Days
• Field of Search: 60/393.7, 602/62, 607/23, 607/37, 607/72, 607/77, 607/94
• US Class Current: 60/777
• CPC Class Codes: F02C 9/16 Control of working fluid flow F02C9/48 takes precedence; control of air-intake flow F02C7/057
• CPC Class Codes: F23R 3/26 Controlling the air flow
• CPC Class Codes: F23R 3/346 for staged combustion
• CPC Class Codes: F23R 3/40 characterised by the use of catalytic means

Abstract

A system and method of combusting a hydrocarbon fuel is disclosed. The system combines the accuracy and controllability of an air staging system with the ultra-low emissions achieved by catalytic combustion systems without the need for a pre-heater. The result is a system and method that is mechanically simple and offers ultra-low emissions over a wide range of power levels, fuel properties and ambient operating conditions.

Claims

1. A method of combusting hydrocarbon fuel, comprising:

compressing an air stream in a compressor;

dividing the air stream into at least one air staging valve air stream and at least one secondary air stream;

controllably dividing said air staging valve air stream into at least one bypass flow stream, and at least one primary air stream;

introducing said bypass flow stream into a bypass manifold, wherein the output is an output bypass flow stream;

introducing said primary air stream into a fuel preparation and mixing section, wherein fuel is injected and mixed to form a fuel/air mixture stream;

introducing said fuel/air mixture stream into a catalyst section, wherein a catalyst is located, thereby generating a heat of reaction and a product stream of partially oxidized hydrocarbons, carbon monoxide and excess air;

combusting said product stream, in a main combustor, at a condition at which appreciable quantities of thermal NO_x are not formed, thereby generating an effluent gas stream; and

combining said effluent gas stream with said output bypass flow stream and secondary air stream to form an exit effluent gas stream, wherein the temperature and composition of the product stream are selected to control simultaneously the amounts of NO_x formed in the main combustor and the stability of the flame in the main combustor, thereby controlling the total amount of NO_x in the exit effluent gas stream.

2. A method as in claim 1, further comprising a valve for controllably dividing said air staging valve air stream.

3. A method as in claim 1, wherein the step of controllably dividing said air staging valve air stream into at least one bypass flow stream, and at least one primary air stream is accomplished by controlling the air valve schedules through a predetermined schedule.

4. A method as in claim 1, wherein the temperature and composition of said product stream are selected to control simultaneously the amount of thermal NO_x and prompt NO_x formed in the main combustor.

5. A method as in claim 1, wherein said catalyst is selected from the group consisting of platinum, rhodium, iridium, ruthenium, palladium, chromium oxides, cobalt oxides, alumina and mixtures thereof.

6. A method as in claim 1, wherein said fuel is in liquid form.

7. A method as in claim 1, wherein said fuel is in gaseous form.

8. A method as in claim 1, further comprising the step of delivering said exit effluent gas stream to a turbine.

9. A method of combusting hydrocarbon fuel, comprising:

compressing an air stream in a compressor;

dividing the air stream into at least one air staging valve air stream and at least one secondary air stream;

controllably dividing said air staging valve air stream into at least one bypass flow stream, and at least one primary air stream;

introducing said bypass flow stream into a bypass manifold;

introducing said primary air stream into a fuel preparation and mixing section, wherein fuel is injected and mixed to form a fuel/air mixture stream;

introducing said fuel/air mixture stream into a catalyst section, wherein a catalyst is located and partially oxidizes the fuel by contacting the fuel/air mixture with an oxidation catalyst in a catalytic oxidation stage, thereby generating a heat of reaction and a partial oxidation product stream comprising partially oxidized hydrocarbons, carbon monoxide and excess air;

combusting the partial oxidation product stream, in a main combustor, at a condition at which appreciable quantities of thermal NO_x are not formed, thereby generating an effluent gas stream; and

combining said effluent gas stream with said bypass flow stream and secondary air streams to form an exit effluent gas stream,

wherein the temperature and composition of the partial oxidation product stream are selected to control simultaneously the amounts of NO_x formed in the main combustor and the stability of the flame in the main combustor, thereby controlling the total amount of NO_x in the exit effluent gas stream.

10. A method as in claim 9, further comprising a valve for controllably dividing said air staging valve air stream.

11. A method as in claim 9, wherein the step of controllably dividing said air staging valve air stream into at least one bypass flow stream, and at least one primary air stream is accomplished by controlling the air valve schedules through a predetermined schedule.

12. A method as in claim 9, wherein the temperature and composition of the partial oxidation product stream are selected to control simultaneously the amount of thermal NO_x and prompt NO_x formed in the main combustor.

13. A method as in claim 9, wherein said catalyst is selected from the group consisting of platinum, rhodium, iridium, ruthenium, palladium, chromium oxides, cobalt oxides, alumina and mixtures thereof.

14. A method as in claim 9, wherein said fuel is in liquid form.

15. A method as in claim 9, wherein said fuel is in gaseous form.

16. A method as in claim 9, further comprising the step of delivering said exit effluent gas stream to a turbine.

17. A method of combusting hydrocarbon fuel, comprising:

compressing an air stream in a compressor;

dividing the air stream into a first air staging valve air stream, a second air staging valve air stream and one secondary air stream;

utilizing an air staging valve to controllably divide said first air staging valve air stream into one bypass flow stream and one primary air stream;

introducing said bypass flow stream into a bypass manifold, wherein the output is an output bypass flow stream;

introducing said primary air stream into a fuel preparation and mixing section, wherein fuel is injected and mixed to form a fuel/air mixture stream;

introducing said fuel/air mixture stream into a catalyst section, wherein a catalyst is located and partially oxidizes the fuel by contacting the catalyst mixture with an oxidation catalyst in a catalytic oxidation stage, thereby generating a heat of reaction and a partial oxidation product stream comprising partially oxidized hydrocarbons, carbon monoxide and excess air;

combusting the partial oxidation product stream, in a main combustor, at a condition at which appreciable quantities of thermal NO_x are not formed, thereby generating an effluent gas stream; and

combining said effluent gas stream with said output bypass flow stream, and said secondary air stream to form an exit effluent gas stream,

wherein the temperature and composition of the partial oxidation product stream are selected to control simultaneously the amounts of NO_x formed in the main combustor and the stability of the flame in the main combustor, thereby controlling the total amount of NO_x in the exit effluent gas stream.

18. A method as in claim 17, wherein the temperature and composition of the partial oxidation product stream are selected to control simultaneously the amount of thermal NO_x and prompt NO_x formed in the main combustor.

19. A method as in claim 17, wherein said catalyst is selected from the group consisting of platinum, rhodium, iridium, ruthenium, palladium, chromium oxides, cobalt oxides, alumina and mixtures thereof.

20. A method as in claim 17, wherein said fuel is in liquid form.

21. A method as in claim 17, wherein said fuel is in gaseous form.

22. A method as in claim 17, wherein said step of controllably dividing said air staging valve air stream into at least one bypass flow stream, and at least one primary air stream is accomplished by controlling the air valve schedules through a predetermined schedule.

23. A method as in claim 17, further comprising the step of delivering said exit effluent gas stream to a turbine.

24. A method of combusting hydrocarbon fuel, comprising:

compressing an air stream in a compressor;

dividing the air stream into a first air staging valve air stream, a second air staging valve air stream and one secondary air stream;

utilizing an air staging valve to controllably divide said first air staging valve air stream into one bypass flow stream and one primary air stream;

introducing said bypass flow stream into a bypass manifold, wherein the output is an output bypass flow stream;

introducing said primary air stream into a fuel preparation and mixing section, wherein fuel is injected and mixed to form a fuel/air mixture stream;

introducing said fuel/air mixture stream into a catalyst section, wherein a catalyst is introduced and partially oxidizes the fuel by contacting the catalyst mixture with an oxidation catalyst in a catalytic oxidation stage, thereby generating a heat of reaction and a partial oxidation product stream comprising hydrocarbons, carbon monoxide and excess air;

combusting the partial oxidation product stream, in a main combustor, at a condition at which appreciable quantities of thermal NO_x are not formed, thereby generating an effluent gas stream;

controlling the flame in the main combustor to a flame temperature between 1700 and 2000 K by varying the position of said air staging valve;

combining said effluent gas stream with said bypass air stream, and said secondary air stream to form an exit effluent gas stream, wherein the temperature and composition of the partial oxidation product stream are selected to control simultaneously the amounts of NO_x formed in the main combustor and the stability of the flame in the main combustor, thereby controlling the total amount of NO_x in the exit effluent gas stream.

25. A method as in claim 24, wherein the temperature and composition of the partial oxidation product stream are selected to control simultaneously the amount of thermal NO_x and prompt NO_x formed in the main combustor.

26. A method as in claim 24, wherein said catalyst is selected from the group consisting of platinum, rhodium, iridium, ruthenium, palladium, chromium oxides, cobalt oxides, alumina and mixtures thereof.

27. A method as in claim 24, wherein said fuel is in liquid form.

28. A method as in claim 24, wherein said fuel is in gaseous form.

29. A method as in claim 24, further comprising the step of delivering said exit effluent gas stream to a turbine.