초록 ▼

Systems and methods for rejecting waste heat generated by one or more operating systems installed on an aircraft employ an endothermic fuel that can participate in endothermic catalytic cracking at temperatures below about 80° C. when exposed to a cracking catalyst that contains a superacid operativ

Systems and methods for rejecting waste heat generated by one or more operating systems installed on an aircraft employ an endothermic fuel that can participate in endothermic catalytic cracking at temperatures below about 80° C. when exposed to a cracking catalyst that contains a superacid operative to induce low-temperature catalytic cracking of the branched alkanes. The endothermic fuel contains an effective amount of the branched alkanes so that a net endothermic effect is realized when the fuel is exposed to the cracking catalyst. The low-temperature, heat-consuming cracking of the branched alkanes increases the heat sink capacity of the endothermic fuel.

대표청구항 ▼

1. A method for rejecting waste heat produced by one or more operating systems carried on an aircraft, the method comprising: supplying an endothermic fuel flow from an endothermic fuel reserve contained in a fuel reservoir, the endothermic fuel comprising an effective amount of branched alkanes so

1. A method for rejecting waste heat produced by one or more operating systems carried on an aircraft, the method comprising: supplying an endothermic fuel flow from an endothermic fuel reserve contained in a fuel reservoir, the endothermic fuel comprising an effective amount of branched alkanes so that the endothermic fuel achieves a net endothermic effect when the branched alkanes undergo endothermic catalytic cracking;bringing the endothermic fuel flow into thermal communication with one or more operating systems that generate waste heat while performing their intended functions during operation of the aircraft; andexposing the endothermic fuel flow to a cracking catalyst that comprises a superacid operative to catalytically crack the branched alkanes present in the endothermic fuel at a reaction temperature between about 20° C. to about 80° C., the superacid being present in an amount to drive cracking of the branched alkanes and to increase a heat sink capacity of the endothermic fuel flow at the reaction temperature. 2. The method of claim 1, wherein the branched alkanes included in the endothermic fuel comprise at least one of 2-methylpentane, 3-methylpentane, 2,2-dimethylbutane, 2,3-dimethylbutane, 2,2,4-trimethylpentane, 2,3,4-trimethylpentane, 2,2-dimethylpentane, 2,3-dimethylpentane, 2,4-dimethylpentane, 3-methylheptane, 2,2,4,4-tetramethylpentane, 2,4,7-trimethylnonane, branched isomers thereof that retain at least one tertiary or quaternary carbon bond, or mixtures thereof. 3. The method of claim 1, wherein the superacid comprises at least one of trifluoromethane sulfonic acid, 1,1,2,2-tetrafluoroethane sulfonic acid, perfluoro(2-ethoxyethane) sulfonic acid, fluorosulfonic acid, fluoroantimonic acid, magic acid, or mixtures thereof. 4. The method of claim 1, wherein the endothermic fuel comprises greater than 10 wt. % branched alkanes, less than 5 wt. % olefins, and less than 3000 ppm sulfur-containing compounds. 5. The method of claim 1, wherein the endothermic fuel comprises greater than 30 wt. % branched alkanes, less than 3 wt. % olefins, and less than 1000 ppm sulfur-containing compounds. 6. The method of claim 1, wherein the endothermic fuel comprises greater than 50 wt. % branched alkanes, less than 0.5 wt. % olefins, and less than 100 ppm sulfur-containing compounds. 7. The method of claim 1, wherein the superacid is present at about 150 grams or greater for every kilogram of the endothermic fuel that flows over the cracking catalyst per minute. 8. The method of claim 1, wherein the superacid is present at about 200 to about 400 grams for every kilogram of the endothermic fuel that flows over the cracking catalyst per minute. 9. The method of claim 1, wherein the cracking catalyst further comprises an inert support substrate that supports and immobilizes the superacid within a flow path of the endothermic fuel flow. 10. The method of claim 9, wherein the inert support substrate comprises silica particles that have been conditioned with at least one of trifluoromethansulfonic anhydride, hexamethyldisilazane, or a mixture thereof. 11. The method of claim 1, further comprising: delivering the endothermic fuel flow to a jet engine configured to receive and selectively combust at least some of the endothermic fuel flow either before or after being exposed to the cracking catalyst; anddelivering at least some of the endothermic fuel flow not combusted in the jet engine back to the fuel reservoir after the endothermic fuel flow has been exposed to the cracking catalyst. 12. The method of claim 1, wherein bringing the endothermic fuel flow into thermal communication with the one or more operating systems and exposing the endothermic fuel flow to the cracking catalyst comprises: passing the endothermic fuel flow through a fuel segment of a reactive heat exchanger, the fuel segment comprising a washcoat within a flow path of the endothermic fuel flow that includes the cracking catalyst; andcirculating a cooling fluid flow through the one or more operating systems, where waste heat is accepted, then through a cooling fluid segment of the reactive heat exchanger to transfer heat to the endothermic fuel flow in the fuel segment, and then back to the one or more operating systems. 13. A method for rejecting waste heat produced by one or more operating systems carried on an aircraft, the method comprising: bringing an endothermic fuel flow into thermal communication with one or more operating systems that generate waste heat while performing their intended functions during operation of the aircraft, the endothermic fuel comprising greater than 10 wt. % branched alkanes, less than 5 wt. % olefins, and less than 3000 ppm sulfur-containing compounds; andexposing the endothermic fuel flow to a cracking catalyst that is immobilized within a flow path of the endothermic fuel flow, the cracking catalyst comprising a superacid supported on an inert support substrate, the superacid being selected from the group consisting of trifluoromethane sulfonic acid, 1,1,2,2-tetrafluoroethane sulfonic acid, perfluoro(2-ethoxyethane) sulfonic acid, fluorosulfonic acid, fluoroantimonic acid, magic acid, or a mixture thereof, and being present at about 150 grams or greater for every kilogram of the endothermic fuel that flows over the cracking catalyst per minute. 14. The method of claim 13, wherein the inert support substrate comprises silica particles that have been conditioned with at least one of trifluoromethansulfonic anhydride, hexamethyldisilazane, or a mixture thereof. 15. The method of claim 13, wherein the branched alkanes included in the endothermic fuel comprise at least one of 2-methylpentane, 3-methylpentane, 2,2-dimethylbutane, 2,3-dimethylbutane, 2,2,4-trimethylpentane, 2,3,4-trimethylpentane, 2,2-dimethylpentane, 2,3-dimethylpentane, 2,4-dimethylpentane, 3-methylheptane, 2,2,4,4-tetramethylpentane, 2,4,7-trimethylnonane, branched isomers thereof that retain at least one tertiary or quaternary carbon bond, or mixtures thereof. 16. The method of claim 13, further comprising: supplying the endothermic fuel flow from an endothermic fuel reserve contained in a fuel reservoir;delivering the endothermic fuel flow to a jet engine configured to receive and selectively combust at least some of the endothermic fuel flow either before or after being exposed to the cracking catalyst; anddelivering at least some of the endothermic fuel flow not combusted in the jet engine back to the fuel reservoir after the endothermic fuel flow has been exposed to the cracking catalyst. 17. A fuel circulation system for rejecting waste heat produced by one or more operating systems carried on an aircraft, the system comprising: a fuel reservoir for storing a reserve of an endothermic fuel that contains an effective amount of branched alkanes so that the endothermic fuel achieves a net endothermic effect when the branched alkanes undergo in endothermic catalytic cracking;one or more operating systems that generate waste heat while performing their intended functions during operation of the aircraft;a jet engine configured to selectively receive and combust a variable quantity of the endothermic fuel contained in the fuel reservoir;a fuel delivery conduit for delivering an endothermic fuel flow originating in the fuel reservoir to the jet engine;a fuel return conduit for returning at least some of the endothermic fuel flow not combusted in the jet engine to the fuel reservoir; anda cracking catalyst cell in fluid communication with either the fuel delivery conduit or the fuel return conduit and exposed within a flow path of the endothermic fuel flow, the cracking catalyst cell comprising an immobilized compilation of a cracking catalyst that includes a superacid operative to induce catalytic cracking of the branched alkanes at a temperature between about 20° C. and about 80° C., and wherein the cracking catalyst cell includes an amount of the superacid to catalytically crack the branched alkanes present in the endothermic fuel and to increase a heat sink capacity of the endothermic fuel flow. 18. The fuel circulation system of claim 17, wherein the endothermic fuel comprises greater than 10 wt. % branched alkanes, less than 5 wt. % olefins, and less than 3000 ppm sulfur-containing compounds, and wherein the branched alkanes comprise at least one of 2-methylpentane, 3-methylpentane, 2,2-dimethylbutane, 2,3-dimethylbutane, 2,2,4-trimethylpentane, 2,3,4-trimethylpentane, 2,2-dimethylpentane, 2,3-dimethylpentane, 2,4-dimethylpentane, 3-methylheptane, 2,2,4,4-tetramethylpentane, 2,4,7-trimethylnonane, branched isomers thereof that retain at least one tertiary or quaternary carbon bond, or mixtures thereof. 19. The fuel circulation system of claim 17, wherein the superacid is present at about 150 grams or greater for every kilogram of the endothermic fuel that flows over the cracking catalyst per minute, and wherein the superacid comprises at least one of trifluoromethane sulfonic acid, 1,1,2,2-tetrafluoroethane sulfonic acid, perfluoro(2-ethoxyethane) sulfonic acid, fluorosulfonic acid, fluoroantimonic acid, magic acid, or mixtures thereof. 20. The fuel circulation system of claim 17, further comprising: a reactive heat exchanger in fluid communication with either the fuel delivery conduit or the fuel return conduit, the reactive heat exchanger comprising a fuel segment and a cooling fluid segment that are isolated from each other by a thermally-conductive material, the fuel segment being configured to communicate the endothermic fuel flow through the reactive heat exchanger, and the cooling fluid segment being configured to communicate a cooling fluid flow, which circulates between the one or more operating systems and the reactive heat exchanger, through the cooling fluid segment of the reactive heat exchanger to transfer heat to the endothermic fuel flow.