초록 ▼

A gas stream with a reduced oxygen concentration relative to ambient air is used to vaporize a liquid fuel or liquefied 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. Prefera

A gas stream with a reduced oxygen concentration relative to ambient air is used to vaporize a liquid fuel or liquefied 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 desired flame location in the combustor 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.

대표청구항 ▼

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 diluent gas; premixing the fuel gas with a second gas containing oxygen to produce a gas mixture in a premixing zone

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 diluent gas; premixing the fuel gas with a second gas containing oxygen to produce a gas mixture in a premixing zone located upstream of a combustion zone of a combustion device, the combustion device being configured such that autoignition of the gas mixture would occur upstream of the combustion zone in the absence of the diluent gas; and combusting the gas mixture in the combustion zone of the combustion device; wherein the diluent gas is inert and present in an amount such that reaction of the fuel gas upstream of the combustion zone is 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 diluent gas is below a limiting oxygen index of the liquid fuel. 6. The method of claim 1, wherein the combustion device includes a fuel metering apparatus configured for natural gas. 7. 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. 8. The method of claim 1, wherein the combustion device is a gas turbine engine. 9. The apparatus of claim 1, wherein the liquid fuel is a liquefied gas, the liquefied gas being of a composition that would be in a gaseous state at room temperature under atmospheric pressure. 10. A combustion apparatus comprising: a combustor, the combustor having a first inlet for accepting fuel gas, a second inlet for accepting oxygenated gas for supporting combustion of the fuel gas, a combustion zone, and a premixing zone upstream of the combustion zone, the combustion device being configured to premix the fuel gas with at least some of the oxygenated gas in the premixing zone to produce a gas mixture, and to combust the gas mixture in the combustion zone; and a fuel vaporization unit in fluid communication with the first inlet of the combustor, the fuel vaporization unit being configured to produce fuel gas using a liquid fuel comprising hydrocarbon molecules and a diluent gas; wherein the combustion apparatus is configured such that autoignition of the gas mixture would occur upstream of the combustion zone in the absence of the diluent gas and wherein the diluent gas is inert and present in the fuel gas in an amount such that reaction of the fuel gas upstream of the combustion zone is suppressed. 11. The combustion apparatus of claim 10, further comprising a fuel gas metering apparatus for controlling the supply of fuel gas to the first inlet, the fuel gas metering apparatus being configured for natural gas. 12. The apparatus of claim 10, wherein the combustion device is configured to combust the gas mixture at an equivalence ratio less than 1. 13. The apparatus of claim 10, wherein at least 50 weight percent of the hydrocarbon molecules of the liquid fuel have at least two carbon atoms. 14. The apparatus of claim 10, wherein an oxygen content of the diluent gas is below a limiting oxygen index of the liquid fuel. 15. The apparatus of claim 10, 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. 16. The apparatus of claim 10, 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. 17. The apparatus of claim 10, wherein the combustion device is a gas turbine engine. 18. The apparatus of claim 10, wherein the combustion device is configured such that an amount of the oxygenated gas sufficient to support combustion is premixed with the fuel gas in the premixing zone.