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A gas stream with a reduced oxygen concentration relative to ambient air is used to vaporize a liquid fuel or liquified higher hydrocarbon gas, or is mixed with a vaporized gas, and the reduced oxygen vaporized fuel gas is fed to a combustion device such as a premixed or diffusion combustor. Prefer

A gas stream with a reduced oxygen concentration relative to ambient air is used to vaporize a liquid fuel or liquified higher hydrocarbon gas, or is mixed with a vaporized gas, and the reduced oxygen vaporized fuel gas is fed to a combustion device such as a premixed or diffusion combustor. Preferably, the oxygen content of the gas stream is less than the limiting oxygen index. By mixing the fuel with a gas stream that has an appropriately reduced oxygen content, auto-ignition prior to the flame front can be avoided. In some embodiments, the reduced oxygen stream is generated from an air separator or taken from the exhaust of the combustion device.

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What is claimed is: 1. A method for operating a combustion device, the method comprising the steps of: producing a fuel gas using a liquid fuel comprising hydrocarbon molecules and a first gas stream with an oxygen content less than that of ambient air; premixing the fuel gas and a second gas to pr

What is claimed is: 1. A method for operating a combustion device, the method comprising the steps of: producing a fuel gas using a liquid fuel comprising hydrocarbon molecules and a first gas stream with an oxygen content less than that of ambient air; premixing the fuel gas and a second gas to produce a gas mixture at a location upstream of a combustion zone of a combustion device, the second gas including oxygen; and combusting the gas mixture in the combustion zone of the combustion device, whereby auto-ignition of the gas mixture upstream of the combustion zone is substantially suppressed. 2. The method of claim 1, wherein the gas mixture has an amount of oxygen sufficient to support combustion of the gas mixture. 3. The method of claim 1, wherein the gas mixture is a lean mixture with an equivalence ratio less than 1. 4. The method of claim 1, wherein at least 50 weight percent of the hydrocarbon molecules of the liquid fuel have at least two carbon atoms. 5. The method of claim 1, wherein the oxygen content of the first gas stream is below a limiting oxygen index of the liquid fuel. 6. The method of claim 1, wherein the combustion device includes a fuel metering system configured for natural gas. 7. The method of claim 1, wherein the first gas stream is supplied by an air separator. 8. The method of claim 7, wherein the air separator produces the first gas stream using adsorption. 9. The method of claim 1, wherein the reduced oxygen gas stream is supplied from an exhaust of a pre-burner. 10. The method of claim 1, wherein the reduced oxygen gas stream is supplied from an exhaust of the combustion device. 11. The method of claim 1, wherein an equivalence ratio of the gas mixture is less than a minimum equivalence ratio at which methane could be combusted under equivalent operating conditions. 12. The method of claim 1, wherein the liquid fuel is diesel fuel. 13. The method of claim 1, wherein the liquid fuel is heating oil. 14. The method of claim 1, wherein the liquid fuel is butane. 15. The method of claim 1, wherein the liquid fuel is propane. 16. The method of claim 1, wherein the liquid fuel is pentane. 17. The method of claim 1, wherein the liquid fuel is gasoline. 18. The method of claim 1, wherein the liquid fuel is a flammable liquid waste. 19. The method of claim 1, wherein the combustion device is a gas turbine engine. 20. The method of claim 1, wherein the gas mixture has an energy content approximately equal to that of natural gas. 21. The method of claim 20, wherein the energy content of the gas mixture has an energy content approximately equal to the energy content of natural gas on a volumetric basis. 22. The method of claim 20, wherein the energy content of the gas mixture has an energy content approximately equal to the energy content of natural gas on a mass basis. 23. A method for operating a combustion device configured to combust natural gas in a lean, premixed mode, the method comprising the steps of: vaporizing a higher hydrocarbon liquid fuel using a gas stream having a reduced oxygen content relative to ambient air to produce a reduced oxygen fuel gas; premixing the reduced oxygen fuel gas and a second gas to produce a gas mixture at a location upstream of a combustion zone of a combustion device, the gas mixture having an amount of oxygen sufficient to support combustion of the gas mixture, the gas mixture having an equivalence ratio less than one, the combustion device being configured to combust natural gas; and combusting the gas mixture in the combustion zone of the combustion device, whereby auto-ignition of the gas mixture upstream of the combustion zone is substantially suppressed. 24. The method of claim 23, wherein the gas stream is derived from an exhaust gas stream of the combustion device. 25. The method of claim 23, wherein the gas stream is provided by an air separator unit. 26. The method of claim 23, wherein an oxygen rich gas stream from the air separator unit is input to the combustion device. 27. The method of claim 23, wherein the gas mixture has an energy content approximately equal to that of natural gas. 28. The method of claim 27, wherein the energy content of the gas mixture has an energy content approximately equal to the energy content of natural gas on a volumetric basis. 29. The method of claim 27, wherein the energy content of the gas mixture has an energy content approximately equal to the energy content of natural gas on a mass basis. 30. A combustion system comprising: a combustion device, the combustor having an inlet for accepting a vaporized fuel, a combustion zone, and a premixing zone upstream of the combustion zone, the combustion device being configured to mix the vaporized fuel with an oxygenated gas stream in the premixing zone to produced a gas mixture and combust the gas mixture in the combustion zone; and a fuel vaporization unit connected to the inlet of the combustion device, the fuel vaporization unit being configured to supply a reduced oxygen vaporized fuel gas stream to the combustion device via the inlet, the fuel vaporization unit including a fuel vaporizer with a first inlet connectable to a liquid fuel source and a second inlet connectable to a reduced oxygen gas stream. 31. The system of claim 30, wherein the combustion device is configured combust the reduced oxygen vaporized fuel gas at an equivalence ratio less than 1. 32. The system of claim 30, wherein at least 50 weight percent of the hydrocarbon molecules of the liquid fuel from the liquid fuel source have at least two carbon atoms. 33. The system of claim 32, wherein the gas mixture has an energy content approximately equal to that of natural gas. 34. The system of claim 33, wherein the energy content of the gas mixture has an energy content approximately equal to the energy content of natural gas on a volumetric basis. 35. The system of claim 33, wherein the energy content of the gas mixture has an energy content approximately equal to the energy content of natural gas on a mass basis. 36. The system of claim 30, wherein the oxygen content of the reduced oxygen gas stream is below a limiting oxygen index of the liquid fuel. 37. The system of claim 30, wherein the combustion device includes a fuel metering system configured for natural gas. 38. The system of claim 30, wherein the fuel vaporization unit further comprising an air separation unit configured to produce a reduced oxygen stream at a first outlet, the first outlet being connected to the second inlet of the fuel vaporizer. 39. The system of claim 38, wherein the air separator produces the reduced oxygen stream by adsorption. 40. The system of claim 30, wherein the reduced oxygen gas stream is supplied from an exhaust gas stream output by the combustion device. 41. The system of claim 30, wherein the combustion device gas is configured to mix the vaporized fuel with the oxygenated gas stream such that the mixture has an equivalence ratio less than a minimum equivalence ratio at which methane could be combusted under equivalent operating conditions. 42. The system of claim 30, wherein the liquid fuel is a liquified gas, the liquified gas being of a composition that would be in a gaseous state at room temperature under atmospheric pressure. 43. The system of claim 30, wherein the liquid fuel is a fuel selected from the group consisting of diesel fuel, heating oil, liquified butane, liquified propane, liquified pentane, gasoline, and flammable liquid waste. 44. The system of claim 30, wherein the combustion device is a gas turbine engine.