首页> 外国专利> METHOD cheap separated fractions FORMING substances, in particular isotope, carried out simultaneously with the conversion of heat energy into mechanical

METHOD cheap separated fractions FORMING substances, in particular isotope, carried out simultaneously with the conversion of heat energy into mechanical

机译:方法廉价分离的级分形成物质,特别是同位素,与热能转化为机械同时进行

摘要

1.method u0440u0430u0437u0434u0435u043bu0435u043du0438u00a0 fractions, u0432u0445u043eu0434u00a0u0449u0438u0445 in substance using their different thermal physical characteristics, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 so that the device u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442 several groups of thermal processes on the substance, e.g. two, so that the u0445u043eu0442u00a0 in one of them u0433u043eu043cu043eu0433u0435u043du043du043eu0435 substance u0441u043eu0441u0442u043eu00a0u0449u0435u0435 from several, for example twofractions from the primary u0441u043eu0441u0442u043eu00a0u043du0438u00a0 u043fu0435u0440u0435u0432u043eu0434u00a0u0442 in heterogeneous u0441u043eu0441u0442u043eu00a0u043du0438u0435 fluid and a pair of u0445u043eu0442u00a0 in one group of heat processes, u0440u0430u0437u0434u0435u043bu00a0u044eu0442 substance u0445u043eu0442u00a0 a gr u0443u043fu043fu044b thermal processes into several parts, for example for two, so that the u0434u043eu043bu00a0 mass of fluid in one of the parts u043eu0442u043bu0438u0447u0430u0435u0442u0441u00a0 against a portion of the mass of fluid in the other part or dr. u0440u0443u0433u0438u0445 u0447u0430u0441u0442u00a0u0445 u0445u043eu0442u00a0 in one group of thermal processesu0434u043eu0431u0430u0432u043bu00a0u044eu0442 to u0445u043eu0442u00a0 to one part of the chemical substance, concurring on the sectarian composition to the compound separated from that part of the substance.;2. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the primary u0441u043eu0441u0442u043eu00a0u043du0438u0435u043c substances u0445u043eu0442u00a0 in one group of thermal processes u00a0u0432u043bu00a0u0435u0442u0441u00a0 gas u0441u043eu0441u0442u043eu00a0u043du0438u0435.;3. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that at the beginning of each group of heat processes u043eu0441u0443u0449u0435u0441u0442u0432u043bu0435u043du0438u00a0 substance has the same composition of both groups u0444u0440u0430u043au0446u0438u043eu043du043du044bu043c u0434u043bu00a0 tep u043bu043eu0432u044bu0445 processes.;4. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that at the beginning of each group u043eu0441u0443u0449u0435u0441u0442u0432u043bu0435u043du0438u00a0 thermal processes of substance is the same in both groups u0434u043bu00a0 thermal processes.;5. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that at the beginning of each group of heat processes u043eu0441u0443u0449u0435u0441u0442u0432u043bu0435u043du0438u00a0 thermal physical parameters of materials, such as temperature, pressure, u0431u044au0435u043c, u00a0u0432u043bu00a0u044eu0442u0441u00a0 identical u0434u043bu00a0 both groups of thermal processes.;6. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the u043fu0435u0440u0435u0432u043eu0434u00a0u0442 substance in a heterogeneous u0441u043eu0441u0442u043eu00a0u043du0438u0435 fluid and a pair of u0430u0434u0438u0430u0431u0430u0442u0438u0447u0435u0441u043au0438 u0445u043eu0442u00a0 in one group of thermal processes.;7. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that after the transfer substance in a heterogeneous u0441u043eu0441u0442u043eu00a0u043du0438u0435 vapor and fluid density is greater than or equal to fluid density necessary for u00a0 started u0434u0435u0439u0441u0442u0432u0438u00a0 other devices with any way to be received by the application of this method.;8. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the u0440u0430u0437u0434u0435u043bu00a0u044eu0442 substance on the part of the various physical u0441u043eu0441u0442u043eu00a0u043du0438u00a0u043cu0438.;9. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the u0440u0430u0437u0434u0435u043bu00a0u044eu0442 substance u0445u043eu0442u00a0 in one group of thermal processes in two parts.;10. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the u0440u0430u0437u0434u0435u043bu00a0u044eu0442 substance u0445u043eu0442u00a0 in one group of heat processes without u0438u0437u043cu0435u043du0435u043du0438u00a0 total.;11. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the u0440u0430u0437u0434u0435u043bu00a0u044eu0442 substance into two parts u0445u043eu0442u00a0 in one group of heat processes so that the mass is the mass of one part of the other part.;12. method for p.1, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, after u0440u0430u0437u0434u0435u043bu0435u043du0438u00a0 substances apart or after u0434u043eu0431u0430u0432u043bu0435u043du0438u00a0 substance separated part permits the heat transfer between the separated part of the substances a refrigerator, u0434u043eu0432u043eu0434u00a0u0442 u0445u043eu0442u00a0 density would be one part of the divided substance to the density required u0434u043bu00a0 started u0434u0435u0439u0441u0442u0432u0438u00a0 other device application a method with the substancereceived as a result of the way of any thermodynamic process, for example u0438u0437u043eu0442u0435u0440u043cu0438u0447u0435u0441u043au0438u043c or u0438u0437u043eu0431u0430u0440u043du044bu043c compression u043fu0435u0440u0435u0434u0430u0432u0430u00a0 u0445u043eu043bu043eu0434u0438u043bu044cu043du0438 ku heat given from the u0441u0436u0438u043cu0430u0435u043cu043eu0433u043e substances, prevent heat transfer between the separated part of the substance and the refrigerator.;13. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the u0434u043eu0431u0430u0432u043bu00a0u044eu0442 substance to separate u0447u0430u0441u0442u00a0u043c so that part of the substance of a thermal process of fluid mass excess the portion of the mass of the fluid, the other part of the substance of the thermal process of the substance u0434u043eu0431u0430u0432u043bu00a0u044eu0442 other thermal process of fluid mass greater than before liu of the liquid substance that is another part of heat process.;14. method for p.1, u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0, u0434u043eu0431u0430u0432u043bu00a0u044eu0442 substance to separate u0447u0430u0441u0442u00a0u043c so that part of the substance of a thermal process of fluid mass not exceeding the proportion of the mass s of another part of the substance of the thermal process of the substance u0434u043eu0431u0430u0432u043bu00a0u044eu0442 other thermal process of fluid mass not exceeding the proportion of mas another part of the same si liquid substance heat process.;15. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the u0434u043eu0431u0430u0432u043bu00a0u044eu0442 substance to separate u0447u0430u0441u0442u00a0u043c to communicate these parts to the desired density.;16. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the u0434u043eu0431u0430u0432u043bu00a0u044eu0442 substance to separate u0447u0430u0441u0442u00a0u043c after u0434u043eu0432u0435u0434u0435u043du0438u00a0 these parts to the desired density.;17. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that after the u0434u043eu0431u0430u0432u043bu0435u043du0438u00a0 substances to separate u0447u0430u0441u0442u00a0u043c or after u0434u043eu0432u0435u0434u0435u043du0438u00a0 substance to permit heat transfer u043cu0435u0436u0434 density from the substance and a heater, u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442 heating of the substance by any known u0442u0435u0440u043cu043eu0434u0438u043du0430u043cu0438u0447u0435u0441u043au0438u043cu0438 processes.;18. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that after the u0434u043eu0431u0430u0432u043bu0435u043du0438u00a0 substances to separate u0447u0430u0441u0442u00a0u043c or after u0434u043eu0432u0435u0434u0435u043du0438u00a0 substance to permit heat transfer u043cu0435u0436u0434 density from the substance and a heater, the heating of the substance u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442 u0438u0437u043eu0445u043eu0440u043du043e.;19. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the heating substance u043eu0441u0443u0449u0435u0441u0442u0432u043bu00a0u044eu0442 until a temperature of, for example, to the temperature necessary u0434u043bu00a0 started u0434u0435u0439u0441u0442u0432u0438u00a0 another u0443u0441u0442u0440u043e u0439u0441u0442u0432u0430 with any way to be received by the application of this method.;20. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that after the heating the substance prevents heat transfer between the heater and the u043du0430u0433u0440u0435u0442u044bu043c substance u043du0430u0433u0440u0435u0442u043eu0435 substance in mobile devices on the developed a different or the same way, or in the reservoir.;21. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the primary u0441u043eu0441u0442u043eu00a0u043du0438u0435u043c substances u0445u043eu0442u00a0 in one group of thermal processes u00a0u0432u043bu00a0u0435u0442u0441u00a0 liquid u0441u043eu0441u0442u043eu00a0u043du0438u0435.;22. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that the u043fu0435u0440u0435u0432u043eu0434u00a0u0442 substance in a heterogeneous u0441u043eu0441u0442u043eu00a0u043du0438u0435 liquid and steam through the following actions, namely to permit heat transfer between a heater and a heating substance before moving in a heterogeneous u0441u043eu0441u0442u043eu00a0u043du0438u0435 liquid and steam, prevent heat transfer between the substance and a heater u0445u043eu0442u00a0 in one group of thermal processes.;23. method for u043eu0442u043bu0438u0447u0430u044eu0449u0438u0439u0441u00a0 1, so that after the u0434u043eu0431u0430u0432u043bu0435u043du0438u00a0 substances to separate u0447u0430u0441u0442u00a0u043c u0445u043eu0442u00a0 one group of heat processes use the substance u0434u043bu00a0 surmounted u0431u0440u0430u0437u043eu0432u0430u043du0438u00a0 thermal energy into mechanical by any known method by heating the substance, u0440u0430u0441u0448u0438u0440u0435u043du0438u00a0 substances with respect to mechanical work, u043eu0445u043bu0430u0436 u0434u0435u043du0438u00a0 or condensation substance of heat into the refrigerator.
机译:1.方法 u0440 u0430 u0437 u0434 u0435 u043b u0435 u043d u0438 u00a0馏分的实质是 u0432 u0445 u043e u0434 u0434 u00a0 u0449 u0438 u04438 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0,以便设备 u043e u0441 u0443 u0449 u0435 u0441 u0441 u0442 u0432 u043b u00a0 u0442对该物质进行几组热处理,例如两个,因此 u0445 u043e u0442 u00a0其中之一 u0433 u043e u043c u043c u043e u0433 u0435 u043d u043d u043d u043e u0435实体 u0441 u043e u043e u0441 u0442 u043e u00 u0449 u0435 u0435来自主要 u0441 u043e u0441 u0442 u043e u00a0 u043d u0438 u00a0 u043f u0435 u0440 u0435 u0432 u043e u0434 u0040一组加热过程中的异种 u0441 u043e u0441 u0442 u043e u00a0 u043d u0438 u0435中的u0442和一组u0445 u043e u0442 u00a0 u0435 u043b u00a0 u044e u0442物质 u0445 u043e u0442 u00a0 a gr u0443 u043f u043f u044b热加工分为几个部分,例如两个部分,因此 u0434 u043e u043b u00a0零件之一中的流体质量与另一零件中的流体质量的一部分或dr的一部分成正比。 u0440 u0443 u0433 u0438 u0445 u0447 u0430 u0441 u0442 u00a0 u0445 u0445 u043e u0442 u00a0在一组热处理中 u0434 u043e u0431 u0431 u0430 u0432 u043b u00a0到化学物质的一部分,并在宗派组成上同意从该化学物质的那部分分离出的化合物。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,这样主 u0441 u043e u0441 u0442 u0432 u043e u00a0 u043d u0438 u0435一组热处理中的 u043c物质 u0445 u043e u0442 u00a0 u00a0 u0432 u043b u00a0 u0435 u0442 u0441 u00a0气体 u0441 u043e u0441 u0441 u0442 u043e u00a0 u043d u043d u0435。; 3。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,以便在每组加热过程开始时 u043e u0441 u0443 u0449 u0435 u0441 u0442 u0432 u043b u0435 u043d u0438 u00a0物质的两组组成相同 u0444 u0440 u0430 u043a u0446 u0438 u043e u043d u043d u043d u044b u043c u0434 u043b u00a0 tep u043b u043e u0432 u044b u0445进程;; 4。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此在每个组的开头 u043e u0441 u0443 u0449 u0435 u0441 u0442 u0432 u043b u0435 u043d u0438 u00a0两组物质的热过程相同。5.。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,以便在每组加热过程开始时 u043e u0441 u0443 u0449 u0435 u0441 u0442 u0432 u043b u0435 u043d u0438 u00a0材料的热物理参数,例如温度,压力, u0431 u044a u0435 u043c, u00a0 u0432 u043b u043a u00a0 u044e u0442 u0441两组热处理均相同; 6 .. u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此 u043f u0435 u0440 u0435 u0432 u0432 u043e u0434 u00a0 u0442物质在异构 u0441 u043e u0441 u0442 u043e u00a0 u043d u0438 u0435流体和一对 u0430 u0434 u0438 u0430 u0431 u0430 u0442 u0442 u0438 u0447 u0435 u0441 u043a u0438 u0445 u043e u0442 u00a0在一组热处理中; 7。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,以便在转移物质之后将其异质 u0441 u043e u0441 u0441 u0442 u043e u00a0 u043d u0438 u0435蒸气和流体密度大于或等于启动 u0434 u0435 u0439 u0441 u0442 u0432 u0438 u00a0其他设备所必需的流体密度这种方法; 8。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此 u0440 u0430 u0437 u0434 u0435 u0435 u043b u00a0 u044e u0442物质在各种物理 u0441 u043e u0441 u0442 u043e u00a0 u043d u0438 u00a0 u043c u0438。; 9。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此 u0440 u0430 u0437 u0434 u0435 u0435 u043b u00a0 u044e u0442物质一组热处理过程分为两个部分:10。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此 u0440 u0430 u0437 u0434 u0435 u0435 u043b u00a0 u044e u0442物质一组不包含 u0438 u0437 u043c u0435 u043d u0435 u043d u0438 u00a0的加热过程中的一组加热过程。11。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,以便将 u0440 u0430 u0437 u0434 u0435 u043b u00a0 u044e u0442物质分成两个部分 u0445 u043e u0442 u00a0进行一组加热处理,从而使质量等于一个部分的质量另一部分; 12。第1页的方法, u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0之后,在 u0440 u0430 u0437 u0434 u0434 u0435 u043b u0435 u043d u0438 u00a0物质分开或位于 u0434 u043e u0431 u0430 u0432 u043b u0435 u043d u0438d u0438 u00a0物质分离部分允许物质的分离部分在冰箱之间进行热传递, u043e u0434 u00a0 u0442 u0445 u043e u0442 u00a0密度将是所分配密度的一部分,即所需密度 u0434 u043b u00a0开始 u0434 u0435 u0439 u0441 u0441 u0442 u0432 u0438 u00a0其他设备应用通过任何热力学过程的方式接收到的物质的方法,例如 u0438 u0437 u043e u0442 u0435 u0440 u043c u0438 u0447 u0435 u0441 u0431 u043a u0438 u043c或 u0438 u0437 u043e u0431 u0430 u0440 u043d u044b u043c压缩 u043f u0435 u0440 u0435 u0434 u0430 u0432 u0430 u00a0 u0445 u043e u043b u043e u0434 u043b u044c u043d u0438从 u044提供的热量1 u0436 u0438 u043c u0430 u0435 u043c u043e u0433 u043e物质,防止物质的分离部分与冰箱之间传热; 13。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此 u0434 u043e u0431 u0430 u0432 u0432 u043b u00a0 u044e u0442物质分隔 u0447 u0430 u0441 u0442 u00a0 u043c,以使一部分流体质量的热过程超出部分流体的质量,另一部分物质的热过程的质量其他热过程的流体质量大于热过程的另一部分液态物质之前的热量; 14。其他热过程的流体质量。第1页的方法, u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0, u0434 u043e u0431 u0430 u0432 u0432 u043b u00a0 u044e u0442物质分隔 u0447 u0430 u0441 u0442 u00a0 u043c,以使一部分热物质的流体质量不超过另一部分热物质的质量s的比例15,其他热过程中流体质量的比例不超过其他同种液体物质热过程的比例。15。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此 u0434 u043e u0431 u0430 u0432 u0432 u043b u00a0 u044e u0442物质分隔 u0447 u0430 u0441 u0442 u00a0 u043c,以将这些部分传递到所需的密度。16。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此 u0434 u043e u0431 u0430 u0432 u0432 u043b u00a0 u044e u0442物质将 u0434 u043e u0432 u0432 u0435 u0434 u0435 u043d u043d u00438 u00a0之后的 u0447 u0430 u0441 u0442 u00a0 u043c分隔为所需的密度。; 17。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此在 u0434 u043e u0431 u0430 u0432 u0432 u043b u0435 u043d u0438 u00a0物质分隔 u0447 u0430 u0441 u0442 u00a0 u043c或之后 u0434 u043e u0432 u0435 u0434 u0435 u043d u043d u0438 u00a0物质允许传热 u043c u0435 u0436 u0434物质和加热器的密度, u043e u0441 u0443 u0449 u0435 u0441 u0442 u0432 u043b u00a0 u044e u0442通过任何已知的 u0442 u0435 u0440 u04340 u043c u043e u0434 u0438 u043d u0430 u043c u0438 u0447 u0435 u0441 u043a u0438 u043c u0438进程。; 18。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此在 u0434 u043e u0431 u0430 u0432 u0432 u043b u0435 u043d u0438 u00a0物质分隔 u0447 u0430 u0441 u0442 u00a0 u043c或之后 u0434 u043e u0432 u0435 u0434 u0435 u043d u043d u0438 u00a0物质允许传热 u043c u0435 u0436 u0434物质和加热器的密度,物质的加热 u043e u0441 u0443 u0449 u0435 u0441 u0442 u0432 u043b u00a0 u044e u0442 u0438 u0437 u0433 u043e u043e u0445 u043e u0440 u043d u043e。; 19。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,以便加热物质 u043e u0441 u0443 u0449 u0435 u0441 u0442 u0432 u043b u00a0 u044e u0442,直到达到例如所需的温度为止 u0434 u043b u00a0开始 u0434 u0435 u0439 u0441 u0442 u0432 u0438 u00a0其他 u0443 u0441 u0442 u0440 u043e u0439 u0441 u0442 u0432 u0430,并且该方法的应用可以通过任何方式接收它; 20。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此该物质在加热后可以防止加热器和 u043d u0430 u0433 u0440 u0435 u0442 u044b u043c物质 u043d u0430 u0433 u0440 u0435 u0442 u0432 u043e u0435在开发出来的移动设备上以不同或相同的方式,或者在水库中; 21。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,这样主 u0441 u043e u0441 u0442 u0432 u043e u00a0 u043d u0438 u0435一组热处理中的 u043c物质 u0445 u043e u0442 u00a0 u00a0 u0432 u043b u00a0 u0435 u0442 u0441 u00a0液体 u0441 u043e u0441 u0441 u0442 u043e u00a0 u043d u043d u0435。; 22。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此 u043f u0435 u0440 u0435 u0432 u0432 u043e u0434 u00a0 u0442物质异质 u0441 u043e u0441 u0442 u043e u00a0 u043d u0438 u0435中的液体和蒸汽通过以下动作进行操作,即在异质 u0441 u043e中移动之前允许加热器和加热物质之间进行热传递23,在一组热处理中,防止液体与蒸汽之间的热传递,防止物质与加热器之间的热传递。 u043e u0442 u043b u0438 u0447 u0430 u044e u0449 u0438 u0439 u0441 u00a0 1的方法,因此在 u0434 u043e u0431 u0430 u0432 u0432 u043b u0435 u043d u0438 u00a0物质分离出来 u0447 u0430 u0441 u0442 u00a0 u043c u0445 u043e u0442 u00a0一组加热过程使用的物质 u0434 u043b u00a0覆盖了 u0431 u0440 u0430 u0437 u043e u0432 u0430 u043d u0438 u00a0通过任何已知的方法通过加热物质将其热能转化为机械能,这些物质是关于机械工作的, u043e u0445 u043b u0430 u0436 u0434 u0435 u043d u0438 u00a0或冷凝的热量进入冰箱。

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