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A system for supplying a gaseous fuel to a gas turbine includes a liquefied fuel source for supplying a liquefied fuel to a liquid fuel pump that is disposed downstream from the liquefied fuel source. The liquid fuel pump is sufficient to raise the pressure of the liquefied fuel to a substantially s

A system for supplying a gaseous fuel to a gas turbine includes a liquefied fuel source for supplying a liquefied fuel to a liquid fuel pump that is disposed downstream from the liquefied fuel source. The liquid fuel pump is sufficient to raise the pressure of the liquefied fuel to a substantially supercritical pressure. A supercritical liquefied fuel vaporizer is disposed downstream from the liquid fuel pump. A heat recovery system is in thermal communication with the liquefied fuel. The heat recovery system is positioned between the liquid fuel source and the supercritical liquefied fuel vaporizer.

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1. A system for supplying a gaseous fuel to a gas turbine, comprising: a. a liquefied fuel source for supplying a liquefied fuel;b. a liquid fuel pump disposed downstream from the liquefied fuel source, wherein the liquid fuel pump raises the pressure of the liquefied fuel to a substantially supercr

1. A system for supplying a gaseous fuel to a gas turbine, comprising: a. a liquefied fuel source for supplying a liquefied fuel;b. a liquid fuel pump disposed downstream from the liquefied fuel source, wherein the liquid fuel pump raises the pressure of the liquefied fuel to a substantially supercritical pressure;c. a supercritical liquefied fuel vaporizer disposed downstream from the liquid fuel pump, wherein the supercritical liquefied fuel vaporizer comprises an outer wall, an inner wall and a fluid conduit that extends therebetween, an inlet end of the fluid conduit receiving the liquefied fuel pressurized to the substantially supercritical pressure, the fluid conduit in thermal communication with the inner wall, the inner wall enclosing a trapezoid shaped high pressure plenum, the inner wall comprising a top wall, a bottom wall, a left-side wall and a right-side wall, a length of the to wall is greater than a length of the bottom wall, a left end of the to wall connected to a left end of the bottom wall by the left-side wall, a right end of the top wall connected to a right end of the bottom wall by the right-side wall, wherein the left-side wall and the right-side wall converge toward each other as the left-side wall and the right-side wall extend from the to wall to the bottom wall;d. a heat recovery system that is in thermal communication with the liquefied fuel, wherein the heat recovery system is disposed between the liquid fuel pump and the supercritical liquefied fuel vaporizer, wherein the heat recovery system superheats the liquefied fuel upstream from the inlet end of the fluid conduit and the superheated liquefied fuel heats the inner wall of the supercritical liquefied fuel vaporizer; ande. an outlet end of the fluid conduit connected to a liquefied fuel injector positioned in the to wall, the liquefied fuel injector injecting the superheated liquefied fuel, wherein a portion of the superheated liquefied fuel flashes into a fuel vapor inside the trapezoid shaped high pressure plenum and a remaining liquid portion of the superheated liquefied fuel evaporates as the remaining liquid portion falls onto the inner wall heated by the superheated liquefied fuel in the fluid conduit. 2. The system as in claim 1, wherein the liquefied fuel is at least one of propane, butane, liquefied petroleum gas, pentane, methanol, ethanol, or dimethyl ether. 3. The system as in claim 1, wherein the heat recovery system is in thermal communication with an exhaust gas stream. 4. The system as in claim 1, wherein the heat recovery system is in thermal communication with an exhaust gas stream of the gas turbine. 5. The system as in claim 1, wherein the heat recovery system superheats the liquefied fuel to a supercritical temperature. 6. The system as in claim 1, wherein the supercritical liquefied fuel vaporizer includes a diluent injector positioned in the bottom wall. 7. The system as in claim 1, further comprising a diluent supply for supplying a diluent to the supercritical liquefied fuel vaporizer, wherein the diluent supply includes a compressor fluidly connected to a gas turbine. 8. A gas turbine, comprising: a. a combustor;b. a primary fuel supply for providing a primary fuel to the combustor;c. a backup fuel supply in fluid communication with the combustor, the backup fuel supply including a system for supplying a gaseous fuel to the combustor; andd. wherein the system for supplying the gaseous fuel to the gas turbine comprises: i. a liquefied fuel source for supplying a liquefied fuel;ii. a liquid fuel pump disposed downstream from the liquefied fuel source, wherein the liquid fuel pump raises the pressure of the liquefied fuel to a substantially supercritical pressure;iii. a supercritical liquefied fuel vaporizer disposed downstream from the liquid fuel pump, wherein the supercritical liquefied fuel vaporizer comprises an outer wall, an inner wall and a fluid conduit that extends therebetween, an inlet end of the fluid conduit receiving the liquefied fuel pressurized to the substantially supercritical pressure, the fluid conduit in thermal communication with the inner wall, the inner wall enclosing a trapezoid shaped high pressure plenum, the inner wall comprising a to wall, a bottom wall, a left-side wall and a right-side wall, a length of the top wall is greater than a length of the bottom wall, a left end of the top wall connected to a left end of the bottom wall by the left-side wall, a right end of the top wall connected to a right end of the bottom wall by the right-side wall, wherein the left-side wall and the right-side wall converge toward each other as the left-side wall and the right-side wall extend from the to wall to the bottom wall;iv. a heat recovery system that is in thermal communication with the liquefied fuel, wherein the heat recovery system is disposed between the liquid fuel pump and the supercritical liquefied fuel vaporizer, wherein the heat recovery system superheats the liquefied fuel upstream from the inlet end of the fluid conduit and the superheated liquefied fuel heats the inner wall of the supercritical liquefied fuel vaporizer; andv. an outlet end of the fluid conduit connected to a liquefied fuel injector positioned in the to wall, the liquefied fuel injector injecting the superheated liquefied fuel, wherein a portion of the superheated liquefied fuel flashes into a fuel vapor inside the trapezoid shaped high pressure plenum and a remaining liquid portion of the superheated liquefied fuel evaporates as the remaining liquid portion falls onto the inner wall heated by the superheated liquefied fuel in the fluid conduit. 9. The gas turbine as in claim 8, wherein the primary fuel comprises at least one of a liquid fuel or a gaseous fuel. 10. The gas turbine as in claim 8, wherein the liquefied fuel is at least one of propane, butane, liquefied petroleum gas, pentane, methanol, ethanol, and dimethyl ether. 11. The gas turbine as in claim 8, wherein the heat recovery system is in thermal communication with an exhaust gas stream. 12. The gas turbine as in claim 8, Wherein the heat recovery system is in thermal communication with an exhaust gas stream of the gas turbine. 13. The gas turbine as in claim 8, wherein the heat recovery system superheats the liquefied fuel to a supercritical temperature. 14. The system as in claim 8, wherein the supercritical liquefied fuel vaporizer includes a diluent injector positioned in the bottom wall. 15. The gas turbine as in claim 8, further comprising a diluent supply for supplying a diluent to the supercritical liquefied fuel vaporizer, wherein the diluent supply includes a compressor fluidly connected to a gas turbine. 16. A gas turbine, comprising: a. a compressor;b. a combustor disposed downstream from the compressor;c. a turbine disposed downstream from the combustor; andd. a system for supplying a gaseous fuel to the combustor, the system comprising: i. a liquid fuel source for supplying a liquefied fuel;ii. a liquid fuel pump disposed downstream from the liquefied fuel source, wherein the liquid fuel pump raises the pressure of the liquefied fuel to a substantially supercritical pressure;iii. a supercritical liquefied fuel vaporizer disposed downstream from the liquid fuel pump wherein the supercritical liquefied fuel vaporizer comprises an outer wall, an inner wall and a fluid conduit that extends therebetween, an inlet end of the fluid conduit receiving the liquefied fuel pressurized to the substantially supercritical pressure, the fluid conduit in thermal communication with the inner wall, the inner wall enclosing a trapezoid shaped high pressure plenum, the inner wall comprising a top wall, a bottom wall, a left-side wall and a right-side wall, a length of the to wall is greater than a length of the bottom wall, a left end of the top wall connected to a left end of the bottom wall by the left-side wall, a right end of the to wall connected to a right end of the bottom wall by the right-side wall, wherein the left-side wall and the right-side wall converge toward each other as the left-side wall and the right-side wall extend from the to wall to the bottom wall;iv. a heat recovery system that is in thermal communication with the liquefied fuel upstream from the supercritical liquefied fuel vaporizer, wherein the heat recovery system superheats the liquefied fuel upstream from the inlet end of the fluid conduit and the superheated liquefied fuel heats the inner wall of the supercritical liquefied fuel vaporizer; andv. an outlet end of the fluid conduit connected to a liquefied fuel injector positioned in the top wall, the liquefied fuel injector injecting the superheated liquefied fuel, wherein a portion of the superheated liquefied fuel flashes into a fuel vapor inside the trapezoid shaped high pressure plenum and a remaining liquid portion of the superheated liquefied fuel evaporates as the remaining liquid portion falls onto the inner wall heated by the superheated liquefied fuel in the fluid conduit, the fuel vapor supplied as the gaseous fuel to the combustor. 17. The gas turbine as in claim 16, wherein the liquefied fuel comprises at least one of propane, butane, liquefied petroleum gas, pentane, methanol, ethanol, and dimethyl ether. 18. The gas turbine as in claim 16, wherein the heat recovery system is in thermal communication with an exhaust gas stream flowing from the turbine.