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    • 3. 发明授权
    • Vapor-compression refrigerant cycle with ejector
    • 带喷射器的蒸气压缩制冷剂循环
    • US06862897B2
    • 2005-03-08
    • US10779571
    • 2004-02-13
    • Kazuhisa MakidaHirotsugu TakeuchiHiroshi Oshitani
    • Kazuhisa MakidaHirotsugu TakeuchiHiroshi Oshitani
    • F25B1/00F25B9/00F25B41/00F25B1/06
    • F25B9/006B60H2001/3298F25B41/00F25B2341/0012F25B2400/12F25B2400/23
    • In a vapor-compression refrigerant cycle having an ejector, a mixture refrigerant of a first refrigerant and a second refrigerant is used. When the mixture refrigerant is decompressed and expanded in a nozzle of the ejector, the first refrigerant has an adiabatic heat drop that is larger than that of the second refrigerant. Further, the second refrigerant has an evaporation latent heat that is larger than that of the first refrigerant. In a gas-liquid separator, a gas-phase amount of the first refrigerant is made larger than that of the second refrigerant, and a liquid-phase amount of the second refrigerant is made larger than that of the first refrigerant. For example, the first refrigerant is propane, and the second refrigerant is butane. Accordingly, expansion energy recovered in the nozzle can be effectively converted to pressure energy in a pressure increasing portion of the ejector while cooling capacity of an evaporator can be improved.
    • 在具有喷射器的蒸汽压缩制冷剂循环中,使用第一制冷剂和第二制冷剂的混合制冷剂。 当混合制冷剂在喷射器的喷嘴中减压膨胀时,第一制冷剂具有比第二制冷剂大的绝热散热。 此外,第二制冷剂具有大于第一制冷剂的蒸发潜热。 在气液分离器中,使第一制冷剂的气相量大于第二制冷剂的气相量,使第二制冷剂的液相量比第一制冷剂的液相量大。 例如,第一制冷剂是丙烷,第二制冷剂是丁烷。 因此,可以在喷射器的增压部分中有效地将在喷嘴中回收的膨胀能量转化为压力能量,同时可以提高蒸发器的冷却能力。
    • 6. 发明申请
    • Refrigerant cycle device
    • 制冷循环装置
    • US20080098757A1
    • 2008-05-01
    • US11977479
    • 2007-10-25
    • Hirotsugu TakeuchiMakoto IkegamiHaruyuki Nishijima
    • Hirotsugu TakeuchiMakoto IkegamiHaruyuki Nishijima
    • F25B41/06F25B15/00F25B49/02F25B39/02
    • F25B41/00B60H2001/3298F25B5/02F25B40/00F25B2341/0011F25B2700/21175
    • In a refrigerant cycle device having an ejector, a branch portion for branching a flow of refrigerant flowing out of the ejector into at least a first refrigerant stream and a second refrigerant stream is located. A first evaporator for evaporating the refrigerant of the first refrigerant stream is located to allow the refrigerant to flow to a suction side of the compressor, and a second evaporator for evaporating the refrigerant of the second refrigerant stream is located to allow the refrigerant to flow to an upstream side of a refrigerant suction port of the ejector. In addition, the branch portion is located to maintain a dynamic pressure of the refrigerant flowing out of the ejector, and the second evaporator is connected to the branch portion in a range where the dynamic pressure can be applied to an inside of the second evaporator.
    • 在具有喷射器的制冷剂循环装置中,设置有用于将从喷射器流出的制冷剂流分流成至少第一制冷剂流和第二制冷剂流的分支部。 定位用于蒸发第一制冷剂流的制冷剂的第一蒸发器以允许制冷剂流到压缩机的吸入侧,并且用于蒸发第二制冷剂流的制冷剂的第二蒸发器被定位成允许制冷剂流到 喷射器的制冷剂吸入口的上游侧。 此外,分支部分被定位成保持流出喷射器的制冷剂的动态压力,并且第二蒸发器在可以将动态压力施加到第二蒸发器的内部的范围内连接到分支部分。