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The invention is a method and apparatus for use therewith for a main burner of a gas turbine. The method employs catalytic combustion to support main combustion. More specifically, a rich fuel/air mixture is catalytically oxidized with the resulting reacted mixture being made lean by having addition

The invention is a method and apparatus for use therewith for a main burner of a gas turbine. The method employs catalytic combustion to support main combustion. More specifically, a rich fuel/air mixture is catalytically oxidized with the resulting reacted mixture being made lean by having additional air added thereto. The resulting lean mixture is then combusted in the presence of the main mixture that is also lean thereby supporting combustion of the main mixture. The method allows for enhanced turndown of a lean main mixture.

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1. A method of combustion comprising the steps of: providing a first, second, and third oxidant; providing a first and second fuel, the first, second and third oxidants and the first and second fuels being of such proportions that the first fuel and the first oxidant have a fuel/oxidant equiva

1. A method of combustion comprising the steps of: providing a first, second, and third oxidant; providing a first and second fuel, the first, second and third oxidants and the first and second fuels being of such proportions that the first fuel and the first oxidant have a fuel/oxidant equivalence ratio greater than 1.0,the first fuel in combination with the first and second oxidant have a fuel/oxidant equivalence ratio less than 1.0, andthe second fuel and third oxidant have a fuel/oxidant equivalence ratio less than 1.0; introducing the first oxidant and the first fuel into a first common area so the first oxidant and the first fuel travel together and intermix to form a first mixture; oxidizing a portion of the first fuel with the first oxidant within the first mixture by flowing the first mixture over and in contact with a catalyst thereby generating a heat of reaction and a first reacted mixture; ducting the first reacted mixture and separately ducting the second oxidant into a second common area so the first reacted mixture and the second oxidant travel together and intermix to form a second mixture; combusting the second mixture; introducing the third oxidant and the second fuel into a third common area so that the third oxidant and the second fuel travel together and intermix to create a third mixture; and combusting the third mixture in contact with the combusting second mixture. 2. The method of claim 1 wherein after the step of generating a heat of reaction, the method includes having the further step of transferring a portion of the heat of reaction into the second oxidant.3. The method of claim 2 wherein in the step of introducing the first reacted mixture and the second oxidant the first reacted mixture and the second oxidant are intermixed such that second mixture is substantially premixed.4. The method of claim 3 wherein in the step of introducing the third oxidant and the second fuel the second fuel and the third air are intermixed such that the third mixture is substantially premixed.5. The method of claim 1 wherein in the step of providing the first, second, and third oxidant the first oxidant, second oxidant, and third oxidant are flows divided from a primary oxidant.6. The method of claim 1 wherein in the step of providing a first and second fuel the first fuel is of a first type and second fuel is of a second type, the first and second type being the same.7. The method of claim 1 wherein in the step of providing a first and second fuel the first fuel and second fuel are in a ratio less than about 1:1 and greater than about 1:19.8. The method of claim 7 wherein the ratio is less than about 1:4 and greater than about 1:9.9. The method of claim 1 wherein in the step of providing a first, second, and third oxidant the oxidant comprises oxygen.10. The method of claim 9 wherein the oxidant comprises air and in the step of providing a first and second fuel the first and second fuels are a hydrocarbon.11. A main burner comprising: a housing defining an interior area; a main mixer for introducing a fuel and an oxidant, the main mixer having an exit and being disposed in the interior area; a first duct defining a chamber and having an exit, the chamber of the first duct in fluid communication with the main mixer exit, the first duct having a length that permits the fuel and the oxidant to mix therein creating a fuel/oxidant mixture; a catalytic pilot comprising a catalytic reactor having an exit and a catalyst positioned therein for oxidizing a first mixture in the presence of the catalyst creating a reacted mixture, and a second duct defining a chamber and having a first entrance, a second entrance, and an exit, the first entrance being coincident with or relatively upstream of the second entrance, the first entrance in fluid communication with the catalytic reactor exit, and a third duct having an exit in fluid communication with the second entrance for introducing an other oxidant into the chamber of the second duct, the second duct having a length that permits the reacted mixture and the other oxidant to be mixed therein creating a reacted/other oxidant mixture, the chamber of the second duct being isolated from the chamber of the first duct whereby the reacted mixture and the other oxidant flow exclusively in the second duct and the fuel and the oxidant flow exclusively in the first duct; and the first duct exit and the second duct exit being positioned relative one to another such that a first flame resulting from the fuel/oxidant mixture is supported by a second flame resulting from the reacted/other oxidant mixture. 12. The main burner of claim 11 wherein the main mixer defines a passage extending therethrough, and the catalytic pilot is positioned therein.13. The main burner of claim 11 wherein the main mixer defines a passage extending therethrough, and the second duct is positioned therein.14. The main burner of claim 11 wherein the first duct length is sufficient to permit premixing of the fuel and oxidant.15. The main burner of claim 14 wherein the first duct has a cross-section that tapers in the direction of flow.16. The main burner of claim 14 wherein the second duct length is sufficient to permit premixing of the reacted mixture and other oxidant.17. The main burner of claim 11 wherein the catalytic reactor comprises a substrate having a first and second side and a catalyst, the catalyst positioned on the first side and the first side isolated from the second side whereby the first mixture will flow over the first side exclusive of the second side and the other oxidant will flow over the second side exclusive of the first side.18. The main burner of claim 17 wherein the catalytic reactor has a housing defining an interior area and an inlet adapted to allow the first mixture to pass therethrough, the inlet being in fluid communication with the interior area; a plurality of tubes positioned in the interior area, each defining an inlet positioned to receive during operation the other oxidant exclusive of the first mixture and an exterior surface and a passage, the passages collectively defining the third duct; the plurality of tubes and the interior area cooperating to define a flow channel through which during operation the first mixture exclusive of the other oxidant will flow; and a catalyst positioned with the flow channel on the exterior surface of at least one tube.19. The main burner of claim 18 wherein the second duct exit is spatially downstream of the main mixer exit based on the normal flow of the fuel therethrough.20. The main burner of claim 18 wherein the catalytic reactor further comprises a plenum in fluid communication with the flow channel.21. The main burner of claim 20 wherein each tube has an exit and the exits are flared whereby the flares secure the tubes within the housing.22. The main burner of claim 11 wherein the length of the first duct is sufficient to permit mixing such that the second mixture has an unmixedness less than 20 percent.23. The main burner of claim 22 wherein the length of the second duct is sufficient to permit mixing such that the third mixture has an unmixedness less than about 20 percent.24. The main burner of claim 23 wherein the unmixedness of the second mixture and first mixture is less than about 10 percent and greater than about 2 percent.