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In operating a gas turbine, there can be a difference between the desired heating value of the fuel and the actual needs of the fuel for the supplied fuel to be ignited. In one aspect, fuel parameters related to the molecular weight of the fuel such as specific gravity and pressure drop are determin

In operating a gas turbine, there can be a difference between the desired heating value of the fuel and the actual needs of the fuel for the supplied fuel to be ignited. In one aspect, fuel parameters related to the molecular weight of the fuel such as specific gravity and pressure drop are determined. Ignitability of the fuel is calculated based on the fuel parameters and adjusted as necessary to bring the fuel's ignitability to designed values. The fuel's ignitability can be calculated without actually igniting the fuel and also without direct knowledge of the fuel's calorific value or its composition.

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1. A method performed by a controller for delivering fuel-oxidizer mixture to a gas turbine for ignition, wherein the fuel is a composition of one or more fuel components, the method comprising: calculating an ignitability of the mixture based on one or more fuel parameters related to molecular weig

1. A method performed by a controller for delivering fuel-oxidizer mixture to a gas turbine for ignition, wherein the fuel is a composition of one or more fuel components, the method comprising: calculating an ignitability of the mixture based on one or more fuel parameters related to molecular weight of the fuel, one or more fuel flow parameters, and one or more oxidizer flow parameters; andadjusting the fuel and oxidizer in mixture such that the ignitability of the mixture after the adjustment is within a reference ignitability range,wherein the step of calculating the ignitability of the mixture and the step of adjusting the fuel and oxidizer mixture are performed before igniting the mixture,wherein the step of calculating the ignitability of the mixture is performed without directly measuring a Wobbe index and calorific value of the fuel, and without directly measuring a composition of the fuel,wherein the step of calculating the ignitability of the mixture comprises: determining a specific gravity of the fuel, determining a pressure drop across a predetermined reference piping section, or both;determining one or more ignitability indicators of the fuel based on the specific gravity of the fuel, the pressure drop, or both; anddetermining a lean limit of ignitability based on the one or more ignitability indicators,wherein the ignitability indicators of the fuel include parameters related to a flammability, heat capacity, and/or reactivity of the fuel, andwherein the lean limit of ignitability is a minimum ignition energy required to ignite the mixture. 2. The method of claim 1, wherein the step of determining the specific gravity of the fuel comprises: determining the specific gravity based on measurements from any one or more of a fuel specific gravity sensor and a fuel pressure sensor. 3. The method of claim 1, wherein the step of determining one or more ignitability indicators includes determining a combustible lean limit of the mixture by applying a transfer function that models a relationship between the specific gravity of the fuel and/or the pressure drop, the temperature of the mixture, and the combustible lean limit of the mixture, the combustible lean limit being a flammability limit of the mixture below which a lean blow out will not be prevented. 4. The method of claim 1, wherein the step of determining one or more ignitability indicators include determining a lower heating value of the mixture by applying a transfer function that models a relationship between the specific gravity of the fuel and/or the pressure drop and the lower heating value of the fuel. 5. The method of claim 1, wherein the step of determining one or more ignitability indicators include determining a rate of reaction of the mixture by applying a transfer function that models a relationship between the specific gravity of the fuel and/or the pressure drop and the rate of reaction of the fuel. 6. The method of claim 1, wherein the step of determining the lean limit of ignitability comprises: determining a lean limit flame temperature of the fuel based on the one or more ignitability indicators; anddetermining the lean limit of ignitability based on the lean limit flame temperature corresponding to the lean limit of ignitability. 7. The method of claim 1, wherein the fuel flow parameters include fuel pressure, fuel pressure drop, fuel flow rate, fuel flow velocity, and fuel temperature,wherein the oxidizer flow parameters include oxidizer pressure, oxidizer pressure drop, oxidizer flow rate, oxidizer flow velocity, oxidizer temperature, andwherein the step of adjusting the fuel and oxidizer in the mixture comprises controlling any combination of the fuel flow parameters, the oxidizer flow parameters, and turbulence. 8. The method of claim 7, wherein the step of adjusting the fuel and oxidizer in the mixture comprises controlling the fuel flow parameters, the oxidizer flow parameters, or both based on measurements from a fuel composition sensor, a fuel calorific value sensor, or both. 9. The method of claim 1, further comprising setting one or more gas turbine ignition parameters based on one or both of the ignitability of the mixture and the lean limit of ignitability, wherein the gas turbine ignition parameters include spark ignition duration, spark ignition frequency, and rotor speed. 10. The method of claim 1, further comprising determining a minimum fuel setting for a first ignition attempt with combustible lean limits correction, and a maximum fuel setting for the first ignition attempt with combustible rich limits correction. 11. The method of claim 1, wherein the step of calculating the ignitability of the mixture comprises rotating the gas turbine to a predetermined speed to enable measurements of the fuel parameters related to the molecular weight of the fuel, the fuel flow parameters, and the oxidizer flow parameters. 12. The method of claim 1, wherein the step of calculating the ignitability of the mixture comprises: pumping the fuel using one or more fuel pumps fluidly attached to fuel delivery piping, to enable measurements of the fuel parameters related to the molecular weight of the fuel and the fuel flow parameters; andpumping the oxidizer using one or more oxidizer pumps fluidly attached to oxidizer delivery piping, to enable measurements of the oxidizer flow parameters,wherein when the fuel and oxidizer are pumped using the fuel and oxidizer pumps, the turbine is not rotated. 13. The method of claim 7, wherein the step of adjusting the fuel and oxidizer in the mixture comprises controlling the fuel flow parameters, the oxidizer flow parameters, or both without directly measuring the Wobbe index, the calorific value of the fuel, and the composition of the fuel. 14. A controller configured to control delivery of fuel and oxidizer mixture to a gas turbine for ignition, wherein the fuel is a composition of one or more fuel components, the controller comprising: a parameter receiving unit arranged to receive any combination of on one or more fuel parameters related to molecular weight of the fuel, one or more fuel flow parameters, and one or more oxidizer flow parameters;an ignitability calculating unit arranged to calculate an ignitability of the mixture based on parameters received by the parameter receiving unit; andan ignitability adjusting unit arranged to adjust the fuel and oxidizer in the mixture such that the ignitability of the mixture after the adjustment is within a reference ignitability range,wherein the ignitability calculating unit performs the calculation and the ignitability adjusting unit performs the adjustment before the mixture is ignited so as to reduce a number of ignition attempts,wherein the ignitability calculating unit calculates the ignitability of the mixture without information on a Wobbe index, calorific value, and composition of the fuel,wherein the ignitability calculating unit calculates the ignitability of the mixture by: determining one or more ignitability indicators based on a specific gravity of the fuel, a pressure drop of the fuel across a predetermined reference piping section, or both, anddetermining a lean limit of ignitability based on the one or more ignitability indicators,wherein the ignitability indicators of the fuel include parameters related to a flammability, heat capacity, and/or reactivity of the fuel, andwherein the lean limit of ignitability is a minimum ignition energy required to ignite the mixture. 15. The controller of claim 14, wherein the ignitability calculating unit is configured to determine the specific gravity based on measurements from any one or more of a fuel specific gravity sensor and a fuel pressure sensor. 16. The controller of claim 14, wherein the ignitability calculating unit is configured to determine a combustible lean limit of the mixture by applying a transfer function that models a relationship between the specific gravity of the fuel and/or the pressure drop, the temperature of the mixture, and the combustible lean limit of the mixture, the combustible lean limit being a flammability limit of the mixture below which a lean blow out will not be prevented. 17. The controller of claim 14, wherein the ignitability calculating unit is configured to determine a lower heating value of the mixture by applying a transfer function that models a relationship between the specific gravity of the fuel and/or the pressure drop and the lower heating value of the fuel. 18. The controller of claim 14, wherein the ignitability calculating unit is configured to determine a rate of reaction of the mixture by applying a transfer function that models a relationship between the specific gravity of the fuel and/or the pressure drop and the rate of reaction of the fuel. 19. The controller of claim 14, wherein the ignitability calculating unit is configured to determine the lean limit of ignitability by: determining a lean limit flame temperature of the fuel based on the one or more ignitability indicators; anddetermining the lean limit of ignitability based on the lean limit flame temperature corresponding to the lean limit of ignitability. 20. The controller of claim 14, wherein the fuel flow parameters include fuel pressure, fuel pressure drop, fuel flow rate, fuel flow velocity, and fuel temperature,wherein the oxidizer flow parameters include oxidizer pressure, oxidizer pressure drop, oxidizer flow rate, oxidizer flow velocity, oxidizer temperature, andwherein the ignitability adjusting unit is configured to adjust the fuel and oxidizer in the mixture by controlling any combination of the fuel flow parameters, the oxidizer flow parameters, and turbulence. 21. The controller of claim 20, wherein the ignitability adjusting unit is configured to adjust the fuel and oxidizer in the mixture by controlling the fuel flow parameters, oxidizer flow parameters, or both based on measurements from a fuel composition sensor, a fuel calorific value sensor, or both. 22. The controller of claim 14, further comprising an ignition parameters setting unit configured to set one or more gas turbine ignition parameters based on one or both of the ignitability of the mixture and the lean limit of ignitability, wherein the gas turbine ignition parameters include spark ignition duration, spark ignition frequency, and rotor speed. 23. The controller of claim 14, wherein the ignition parameters setting unit is configured to control a minimum fuel setting for a first ignition attempt with combustible lean limits correction, and a maximum fuel setting for the first ignition attempt with combustible rich limits correction. 24. The controller of claim 20, wherein the ignitability adjusting unit is configured to adjust the fuel and oxidizer in the mixture by controlling the fuel flow parameters, oxidizer flow parameters, or both without information on a Wobbe index, calorific value, and composition of the fuel.