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A system and method for vaporizing a cryogenically stored fuel, particularly hydrogen, liquefied by cooling below the ambient temperature is provided. A system for vaporizing a cryogenically stored fuel uses heat arising in the area of a fuel consumer, and includes: a withdrawing line device for dra

A system and method for vaporizing a cryogenically stored fuel, particularly hydrogen, liquefied by cooling below the ambient temperature is provided. A system for vaporizing a cryogenically stored fuel uses heat arising in the area of a fuel consumer, and includes: a withdrawing line device for drawing fuel out of a tank device; a vaporizer device for vaporizing the fuel drawn via the withdrawing line, while introducing the vaporization heat; a gas line device for feeding the vaporized fuel to each consumer; a heat transfer system provided in the vicinity of the consumer while serving to absorb heat arising in the vicinity of the consumer, and; a fuel/heat exchanger device, through which a heat transfer fluid flows and which forms a part of the vaporizer device, for providing the vaporization heat via a heat flux drawn out of the heat transfer system. The coupling of the fuel/heat exchanger device to the heat transfer system is effected via a forward section and a return section such that the throughput of the heat transfer fluid, which is required for introducing the vaporization heat, through the fuel/heat exchanger device can be set in a varying manner by the fluid throughput through the forward section and/or the return section.

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What is claimed is: 1. A system for vaporizing a cryogenically stored fuel by utilizing heat generated in a vicinity of a fuel consumer, comprising: a vaporizing device for vaporizing fuel withdrawn from a fuel tank, introducing heat of vaporization; a gas line device for supplying the vaporized fu

What is claimed is: 1. A system for vaporizing a cryogenically stored fuel by utilizing heat generated in a vicinity of a fuel consumer, comprising: a vaporizing device for vaporizing fuel withdrawn from a fuel tank, introducing heat of vaporization; a gas line device for supplying the vaporized fuel to the consumer; a heat transfer system provided in the vicinity of the consumer for absorbing heat generated in the vicinity of the consumer; and a fuel-heat exchanger device through which a heat transfer fluid passes, forming part of the vaporizer device for supplying the heat of vaporization through a heat stream withdrawn from the heat transfer system; wherein the coupling of the fuel-heat exchanger device with the heat transfer system is accomplished via a forward flow section and a return flow section such that the throughput of heat transfer fluid through the fuel-heat exchanger device, as is required for introducing the heat of vaporization, is adjustable in deviation by the fluid throughput through at least one of the forward flow section and the return flow section, independently of the other one. 2. The system as claimed in claim 1, wherein a thermal coupling of the fuel-heat exchanger device with the heat transfer system on the consumer end is accomplished via an intermediate heat exchanger. 3. A system for vaporizing a cryogenically stored fuel by utilizing heat generated in a vicinity of a fuel consumer, comprising: a vaporizing device for vaporizing fuel withdrawn from a fuel tank, introducing heat of vaporization; a gas line device for supplying the vaporized fuel to the consumer; a heat transfer system provided in the vicinity of the consumer for absorbing heat generated in the vicinity of the consumer; and a fuel-heat exchanger device through which a heat transfer fluid passes, forming part of the vaporizer device for supplying the heat of vaporization through a heat stream withdrawn from the heat transfer system; wherein the coupling of the fuel-heat exchanger device with the heat transfer system is accomplished via a forward flow section and a return flow section such that the throughput of heat transfer fluid through the fuel-heat exchanger device, as is required for introducing the heat of vaporization, is adjustable in deviation by the fluid throughout through at least one of the forward flow section and the return flow section, wherein the coupling of the fuel-heat exchanger device is accomplished with separation of the fluid circuits into one primary circuit of the heat transfer system and at least one secondary circuit coupling the primary circuit to the fuel heat exchanger device. 4. The system as claimed in claim 2, wherein the coupling of the fuel-heat exchanger device is accomplished with separation of the fluid circuits into one primary circuit and at least one secondary circuit. 5. The system as claimed in claim 3, wherein for the separate fluid circuits, different heat transfer of fluids are accommodated in the respective fluid circuits. 6. The system as claimed in claim 4, wherein for the separate fluid circuits, different heat transfer of fluids are accommodated in the respective fluid circuits. 7. The system as claimed in claim 1, wherein the coupling is accomplished with the inclusion of a bridge line which permits partial recycling of a heat transfer fluid stream flowing out of the fuel-heat exchanger device to the input side of the fuel-heat exchanger device. 8. The system as claimed in claim 1, wherein the coupling is accomplished with the inclusion of a bypass line device for creating a fluid connection between the forward flow section and the return flow section, bypassing the fuel-heat exchanger device. 9. The system as claimed in claim 7, wherein the coupling is accomplished with the inclusion of a bypass line device for creating a fluid connection between the forward flow section and the return flow section, bypassing the fuel-heat exchanger device. 10. The system as claimed in claim 1, wherein an input temperature detecting sensor is provided for detecting the input temperature of the heat transfer fluid at the inlet of the fuel-heating device. 11. The system as claimed in claim 1, wherein an output temperature detecting sensor is provided for detecting the output temperature of the heat transfer fluid at the output of the fuel-heat exchanger device. 12. The system as claimed in claim 10, wherein an output temperature detecting sensor is provided for detecting the output temperature of the heat transfer fluid at the output of the fuel-heat exchanger device. 13. The system as claimed in claim 1, wherein a pump device is provided for conveying the heat transfer fluid through the fuel-heat exchanger system. 14. The system as claimed in claim 1, wherein final controlling valves are provided for adjusting flow-through conditions through the fuel-heat exchanger device. 15. The system as claimed in claim 9, wherein actuator valves are provided for adjusting flow-through conditions through the bypass line or the bridge line. 16. The system as claimed in claim 1, wherein a control unit is provided for adjusting the fluid throughput through the forward flow and return flow sections and/or through the fuel-heat exchanger device so as to result in system settings tailored to an instantaneous operating state of the consumer. 17. The system as claimed in claim 1, wherein the fuel-heat exchanger device is operated such that a cooling potential is made available for the consumer, which consumer comprises at least one of: an engine, an exhaust gas recirculation system, a charging air cooling system, a vehicle air-conditioning system, and transmission systems, through the heat transfer fluid stream flowing out on an output end of the heat exchanger device. 18. The system as claimed in claim 1, wherein the heat transfer fluid is withdrawn from an area of the consumer which makes available a sufficiently high temperature potential for applying a vaporization capacity through the fuel-heat exchanger device. 19. The system as claimed in claim 18, wherein the heat transfer fluid is withdrawn from a fast-heating and/or high-temperature section of the heat transfer system on the consumer end. 20. The system as claimed in claim 1, wherein the heat transfer fluid stream cooled by heat withdrawn from the fuel-heat exchanger device is fed into a cooling fluid stream upstream from a cooling-water heat exchanger. 21. The system as claimed in claim 1, wherein the consumer is a combustion engine. 22. The system as claimed in claim 1, wherein the consumer is a fuel cell. 23. The system as claimed in claim 1, wherein the heat transfer system forms a coolant circuit of the consumer. 24. The system as claimed in claim 1, wherein the heat transfer system cooperates with an exhaust gas recirculation system. 25. The system as claimed in claim 1, wherein a waste heat system comprises a lubricant system of the consumer or drive train components. 26. The system as claimed in claim 1, wherein the heat transfer takes places in the fuel-heat exchanger device selectively according to the co-current or counter-current principle. 27. The system as claimed in claim 1, wherein the fuel is at least temporarily in a liquid state when entering the heat exchanger. 28. The system as claimed in claim 1, wherein hydrogen is used as the fuel. 29. The system as claimed in claim 1, wherein the fuel stored in a tank has a temperature of less than 150 K. 30. A method for vaporizing a cryogenically stored fuel, the method comprising the acts of: withdrawing the fuel from a tank device; heating and vaporizing the fuel via a vaporizer device designed as a heat exchanger, wherein a heat stream required for continuous vaporization of the fuel is withdrawn via a thermally regulated heat transfer fluid stream which is withdrawn from a heat transfer system provided on the consumer end; and adjusting the fluid stream withdrawn from the heat transfer fluid system on the consumer end and a vaporizer fluid stream passed through the vaporizer device to various levels in at least some phases as a function of the operating state of the consumer, by adjusting a forward flow independently of a return flow of the heat transfer system. 31. The method as claimed in claim 30, wherein the fluid streams are adjusted with the provision that a quantity of heat required for supplying gaseous hydrogen is to be made available in the range of preselected temperature gradients. 32. The method as claimed in claim 30, wherein the fluid streams are adjusted with the provision that the quantity of heat required for supplying the fuel is to be made available at a preselected inlet temperature of the vaporizer fluid stream. 33. The method as claimed in claim 30, wherein the fluid streams are adjusted with the provision that the quantity of heat required for supplying the fuel is to be made available on reaching a preselected outlet temperature of the vaporizer fluid stream. 34. The system as claimed in claim 28, wherein the fuel is stored in a tank at a temperature of less than about 20 K. 35. The method as claimed in claim 30, wherein the fuel comprises gaseous hydrogen.