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1.发明申请METHOD FOR LOW POWER NON-COKING LIQUID HYDROCARBON FUEL VAPORIZATION AND SUPERCRITICAL PHASE CHANGE 审中-公开低功率非焦化液化石油气蒸发和超临界相变方法公开(公告)号：US20140272732A1
公开(公告)日：2014-09-18
申请号：US13803206
申请日：2013-03-14
Inventor： David A. Clark
CPC classification number: F23D11/445 , F22B1/18
Abstract: Methods for vaporizing hydrocarbon fuel and delivering the hydrocarbon fuel in either a vaporized phase or a supercritical phase to, for example, a combustion chamber are provided herein. A method of vaporizing a hydrocarbon fuel, wherein the hydrocarbon fuel is in a liquid phase at a first temperature and a first pressure, and wherein the first temperature of the liquid phase hydrocarbon fuel is less than its intrinsic oxidation or endothermic reaction temperature, the method may include lowering a pressure of the liquid phase hydrocarbon fuel from the first pressure to a second pressure; and heating the liquid phase hydrocarbon fuel from the first temperature to a second temperature, wherein the hydrocarbon fuel at the second temperature and the second pressure is in a substantially completely vaporized phase substantially without thermally oxidizing the hydrocarbon fuel, and wherein the hydrocarbon fuel in the substantially completely vaporized phase does not form carbonaceous contaminants.
Abstract translation: 本文提供了将烃燃料蒸发并将气化相或超临界相中的烃燃料输送到例如燃烧室的方法。 一种汽化碳氢燃料的方法，其中烃燃料在第一温度和第一压力下处于液相，并且其中液相烃燃料的第一温度低于其本身的氧化或吸热反应温度，该方法 可以包括将液相烃燃料的压力从第一压力降低到第二压力; 以及将所述液相烃燃料从所述第一温度加热到第二温度，其中在所述第二温度和所述第二压力下的所述烃燃料基本上完全蒸发，基本上不对所述烃燃料进行热氧化，并且其中所述烃燃料在 基本完全蒸发的相不会形成碳质污染物。
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2.发明授权公开(公告)号：US10119703B2
公开(公告)日：2018-11-06
申请号：US13803206
申请日：2013-03-14
Inventor： David A. Clark
Abstract: Methods for vaporizing hydrocarbon fuel and delivering the hydrocarbon fuel in either a vaporized phase or a supercritical phase to, for example, a combustion chamber are provided herein. A method of vaporizing a hydrocarbon fuel, wherein the hydrocarbon fuel is in a liquid phase at a first temperature and a first pressure, and wherein the first temperature of the liquid phase hydrocarbon fuel is less than its intrinsic oxidation or endothermic reaction temperature, the method may include lowering a pressure of the liquid phase hydrocarbon fuel from the first pressure to a second pressure; and heating the liquid phase hydrocarbon fuel from the first temperature to a second temperature, wherein the hydrocarbon fuel at the second temperature and the second pressure is in a substantially completely vaporized phase substantially without thermally oxidizing the hydrocarbon fuel, and wherein the hydrocarbon fuel in the substantially completely vaporized phase does not form carbonaceous contaminants.
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