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An apparatus for producing power from a source of liquid fuel. The apparatus includes at least one capillary flow passage, the at least one capillary flow passage having an inlet end and an outlet end, the inlet end in fluid communication with the source of liquid fuel, a heat source arranged along

An apparatus for producing power from a source of liquid fuel. The apparatus includes at least one capillary flow passage, the at least one capillary flow passage having an inlet end and an outlet end, the inlet end in fluid communication with the source of liquid fuel, a heat source arranged along the at least one capillary flow passage, the heat source operable to heat the liquid fuel in the at least one capillary flow passage to a level sufficient to change at least a portion thereof from a liquid state to a vapor state and deliver a stream of substantially vaporized fuel from the outlet end of the at least one capillary flow passage, a combustion chamber for combusting the stream of substantially vaporized fuel and air, the combustion chamber in communication with the outlet end of the at least one capillary flow passage and a conversion device operable to convert heat released by combustion in the combustion chamber into mechanical or electrical power. The conversion device can be a device capable of producing up to about 5,000 watts of mechanical or electrical power.

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What is claimed is: 1. An apparatus for producing power from a source of liquid fuel, comprising: (a) at least one capillary flow passage, said at least one capillary flow passage having an inlet end and an outlet end and having substantially uniform electrical resistance along its length, said inl

What is claimed is: 1. An apparatus for producing power from a source of liquid fuel, comprising: (a) at least one capillary flow passage, said at least one capillary flow passage having an inlet end and an outlet end and having substantially uniform electrical resistance along its length, said inlet end in fluid communication with the source of liquid fuel; (b) an electrical heat source arranged along said at least one capillary flow passage, said electrical heat source operable to heat the liquid fuel in said at least one capillary flow passage uniformly along the length of said capillary flow passage while said liquid fuel is within said capillary flow passage to a level sufficient to change said liquid fuel from a liquid state to a vapor state and deliver a stream of vaporized fuel from said outlet end of said at least one capillary flow passage; (c) a combustion chamber for combusting the stream of vaporized fuel and air, said combustion chamber in communication with said outlet end of said at least one capillary flow passage; and (d) a conversion device operable to convert heat released by combustion in said combustion chamber into mechanical and/or electrical power of up to 5000 watts, said conversion device comprising a device selected from the group consisting of a Stirling engine, a Stirling engine with electrical alternator and a Stirling engine with electrical generator. 2. The apparatus of claim 1, wherein said heat source comprises a resistance-heating element. 3. The apparatus of claim 1, further comprising a fluid control valve which controls the flow of liquid fuel from the liquid fuel source. 4. The apparatus of claim 3, wherein said at least one capillary flow passage comprises at least one capillary tube. 5. The apparatus of claim 4, wherein said heat source comprises a section of said capillary tube heated by passing an electrical current therethrough. 6. The apparatus of claim 5, further comprising means for cleaning deposits formed during operation of the apparatus. 7. The apparatus of claim 3, further comprising means for cleaning deposits formed during operation of the apparatus. 8. The apparatus of claim 7, wherein said means for cleaning deposits includes said fluid control valve, said heat source and an oxidizer control valve for placing said at least one capillary flow passage in fluid communication with an oxidizer, said heat source also being operable to heat the oxidizer in said at least one capillary flow passage to a level sufficient to oxidize deposits formed during the heating of the liquid fuel, wherein said oxidizer control valve for placing said at least one capillary flow passage in fluid communication with an oxidizer is operable to alternate between the introduction of liquid fuel and the introduction of oxidizer into said capillary flow passage and enables in-situ cleaning of said capillary flow passage when the oxidizer is introduced into said at least one capillary flow passage. 9. The apparatus of claim 8, wherein said at least one capillary flow passage comprises a plurality of capillary flow passages, each of said capillary flow passages being in fluid communication with a supply of fuel and a supply of oxidizing gas. 10. The apparatus of claim 8, wherein the oxidizer comprises air, exhaust gas, steam and mixtures thereof. 11. The apparatus of claim 7, wherein said means for cleaning deposits comprises means for abrading deposits formed during operation of the apparatus. 12. The apparatus of claim 11, wherein said means for abrading deposits comprises an axially movable rod positioned so as to be in axial alignment with said at least one capillary flow passage. 13. The apparatus of claim 12, wherein said means for abrading deposits comprises cleaning brushes disposed along said axially movable rod. 14. The apparatus of claim 7, wherein said means for cleaning deposits includes said fluid control valve and a solvent control valve for placing said at least one capillary flow passage In fluid communication with a solvent, said solvent control valve disposed at one end of said at least one capillary flow passage, and wherein said solvent control valve for placing said at least one capillary flow passage in fluid communication with a solvent is operable to alternate between the introduction of liquid fuel and the introduction of solvent into said capillary flow passage and enables in-situ cleaning of said capillary flow passage when the solvent is introduced into said at least one capillary flow passage. 15. The apparatus of claim 7, wherein said means for cleaning deposits includes said fluid control valve, said fluid control valve operable for placing said at least one capillary flow passage in fluid communication with a solvent, enabling in-situ cleaning of said capillary flow passage when the solvent is introduced into said at least one capillary flow passage. 16. The apparatus of claim 15, wherein the solvent comprises liquid fuel from the liquid fuel source and wherein the heat source is phased-out during cleaning of said capillary flow passage. 17. The apparatus of claim 1, wherein said combustion chamber includes an igniter operable to ignite the vaporized fuel. 18. The apparatus of claim 1, wherein said heat source is effective to vaporize the liquid fuel to a level effective to reduce the ignition energy requirements of the igniter. 19. The apparatus of claim 1, further comprising a fuel source, said fuel source capable of delivering pressurized liquid fuel to said at least one capillary flow passage at a pressure of 100 psig or less. 20. The apparatus of claim 1, wherein said heat source enables the stream of vaporized fuel that mixes with a gas upon exiting said outlet end of said at least one capillary flow passage to form an aerosol having a particle size distribution, a fraction of which is 25 μm or less. 21. The apparatus of claim 1, further comprising a heat exchanger which includes an exhaust duct through which a portion of the exhaust gases exhausted from said combustion chamber are circulated and an air passage through which air is circulated, said heat exchanger preheating the air in said air passage by transferring heat from the exhaust gases in said exhaust duct to the air. 22. The apparatus of claim , further comprising an air blower, said air blower supplying air under pressure to said combustion chamber to enable the pressurized air to mix with the vaporized fuel in a desired air-to-fuel ratio effective to combust the air-fuel mixture. 23. The apparatus of claim I, wherein at least a portion of said at least one capillary flow passage is arranged to be heated by the combusted fuel such that the fuel in said at least one capillary flow passage is vaporized. 24. The apparatus of claim 1, wherein the fuel source includes a fuel pump and a regulation valve, said regulation valve supplying the liquid fuel to the capillary flow passage at a desired flow rate. 25. A method of generating power, comprising: (a) supplying liquid fuel to at least one capillary flow passage, said at least one capillary flow passage having substantially uniform electrical resistance along its length; (b) causing a stream of vaporized fuel to pass through an outlet of the at least one capillary flow passage by electrically heating the liquid fuel uniformly along the length of said capillary flow passage while said liquid fuel Is within the at least one capillary flow passage; (c) combusting the vaporized fuel in a combustion chamber; end (d) converting heat produced by combustion of the vaporized fuel In the combustion chamber into mechanical and/or electrical power of up to 5000 watts, said conversion device comprising a device selected from the group consisting of a Stirling engine, a Stirling engine with electrical alternator and a Stirling engine with electrical generator. 26. The method of claim 25, wherein the at least one capillary flow passage includes at least one capillary tube and the heat source comprises a resistance heating element or section of the capillary tube heated by passing an electrical current therethrough, the method further including flowing the liquid fuel through the capillary tube and vaporizing the liquid fuel by heating the tube. 27. The method of claim 25, wherein the combustion chamber includes an igniter arranged to ignite the vaporized fuel, the method including igniting the vaporized fuel with the Igniter. 28. The method of claim 27, wherein the heat source is effective to vaporize the liquid fuel to a level effective to reduce the ignition energy requirements of the igniter. 29. The method of claim 25, wherein the fuel supply delivers pressurized liquid fuel to the at least one capillary flow passage, the method including delivering pressurized hydrocarbon fuel, oxygenated fuel or mixtures thereof, at a pressure of 100 psig or less to the at least one capillary flow passage. 30. The method of claim 25, wherein the stream of vaporized fuel mixes with air and forms a precombustion aerosol in the combustion chamber prior to start up of combustion, the method including forming the precombustion aerosol having a particle size distribution, a fraction of which is 25 μm or less prior to igniting the vaporized fuel to initiate combustion. 31. The method of claim 25, further comprising preheating air in a heat exchanger which includes an exhaust duct through which exhaust gases removed from the combustion chamber are circulated and an air passage through which air is circulated, the heat exchanger preheating the air in the air passage by transferring heat from the exhaust gases in the exhaust duct to the air. 32. The method of claim 25, further comprising supplying air under pressure to the combustion chamber such that the pressurized air mixes with the vaporized fuel in a desired air-to-fuel ratio suitable for combustion of the air-fuel mixture. 33. The method of claim 25, further comprising preheating the liquid fuel with a heat exchanger which includes an exhaust duct through which exhaust gases removed from the combustion chamber are circulated and a fuel passage through which the liquid fuel is circulated, the heat exchanger preheating the liquid fuel in the fuel passage by transferring heat from the exhaust gases in the exhaust duct to the liquid fuel. 34. The method of claim 25, wherein the liquid fuel Is heated by an electrical resistance heater and liquid fuel in a portion of the capillary flow passage is heated with heat produced by the combusted fuel. 35. The method of claim 34, wherein the electrical resistance heater is only used for an initial start-up period and the heat from the combusted fuel is used to vaporize the liquid fuel thereafter. 36. The method of claim 25, further comprising cleaning periodically the at least one capillary flow passage. 37. The method of claim 36, wherein said periodic cleaning comprises (i) halting liquid fuel flow to the at least one capillary flow passage, (ii) supplying an oxidizer to the at least one capillary flow passage and (iii) heating the at least one capillary flow passage whereby deposits formed in the at least one capillary flow passage are oxidized. 38. The method of claim 37, further comprising selectively supplying fuel and oxidizer to the at least one capillary flow passage, wherein the supply selection is achieved by a valve mechanism operated by a controller. 39. The method of claim 38, wherein the oxidizer is selected from pressurized air, exhaust gas, steam and mixtures thereof. 40. The method of claim 36, wherein said capillary cleaning step includes abrading deposits formed during said heating of the liquid fuel. 41. The method of claim 40, wherein said deposit abrading utilizes cleaning brushes disposed on an interior surface of the at least one capillary flow passage. 42. The method of claim 36, wherein said periodic cleaning comprises (i) halting said heating of the at least one capillary flow passage, and (ii) supplying a solvent to the at least one capillary flow passage, whereby deposits formed in the at least one capillary flow passage are removed. 43. The method of claim 36, wherein said periodic cleaning comprises (i) phasing-out said heating of the at least one capillary flow passage, and (ii) supplying a solvent to the at least one capillary flow passage, whereby deposits formed in the at least one capillary flow passage are removed. 44. The method of claim 43, wherein the solvent includes liquid fuel from the liquid fuel source.