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    Refrigerant cycle system with ejector pump
    31.
    发明授权
    Refrigerant cycle system with ejector pump 失效
    带喷射泵的制冷循环系统

    公开(公告)号：US06675609B2

    公开(公告)日：2004-01-13

    申请号：US10350779

    申请日：2003-01-23

    Applicant: Hirotsugu Takeuchi ,  Yasushi Yamanaka ,  Atsushi Inaba

    Inventor： Hirotsugu Takeuchi ,  Yasushi Yamanaka ,  Atsushi Inaba

    IPC: F25B106

    CPC classification number: F25B27/02 ,  B60H2001/3298 ,  F25B1/08 ,  F25B1/10 ,  F25B6/04 ,  F25B9/008 ,  F25B2309/061 ,  F25B2341/0012 ,  F25B2341/0015 ,  F25B2400/075 ,  F25B2400/23 ,  Y02A30/274

    Abstract: In a refrigerant cycle system with an ejector pump, refrigerant to be introduced into a nozzle of the ejector pump is heated in a heat exchanger using waste heat from a vehicle engine as a heating source, and any one of a first mode, a second mode and a third mode can be selectively set based on a thermal load of an evaporator. In the first mode, refrigerant circulates from the evaporator toward a radiator only by the ejector pump. In the second mode, refrigerant circulate from the evaporator toward the radiator only by a compressor. Further, in the third mode, refrigerant circulates from the evaporator toward the radiator by using both the ejector pump and the compressor. Accordingly, the waste heat can be effectively recovered while a flow resistance of the refrigerant can be restricted.

    Abstract translation: 在具有喷射泵的制冷剂循环系统中，要引入喷射泵的喷嘴的制冷剂在热交换器中使用来自车辆发动机的余热作为加热源加热，并且第一模式，第二模式 并且可以基于蒸发器的热负荷来选择性地设定第三模式。 在第一模式中，制冷剂仅通过喷射泵从蒸发器向散热器循环。 在第二模式中，制冷剂仅通过压缩机从蒸发器向散热器循环。 此外，在第三模式中，制冷剂通过使用喷射泵和压缩机两者从蒸发器向散热器循环。 因此，可以有效地回收废热，同时可以限制制冷剂的流动阻力。

    Cryogenic refrigerating system
    32.
    发明申请
    Cryogenic refrigerating system 有权
    低温制冷系统

    公开(公告)号：US20020162353A1

    公开(公告)日：2002-11-07

    申请号：US10111384

    申请日：2002-05-02

    Inventor： Hee-Jun Park

    IPC: F25B007/00 ,  F25B001/06 ,  F25B043/00 ,  F25B041/00

    CPC classification number: F25B5/04 ,  F25B9/006 ,  F25B41/00 ,  F25B2341/0011 ,  F25B2341/0015

    Abstract: The present invention provides a cryogenic refrigerating system for achieving ultra low temperature by sequentially obtaining low temperature through repetition of expansion and evaporation of a mixed-refrigerant in multiple stages. The refrigerating system includes a heat exchanger and a compressor between a final evaporator and a compressor. The heat exchanger causes evaporated refrigerant vapor in a suction tube for the compressor to be heated and to be drawn into the compressor, and causes the refrigerant condensed by a condenser to be supercooled. The refrigerating system includes a plurality of expansion/suction apparatuses connected with one another between the gas/liquid separator and the final evaporator.

    Abstract translation: 本发明提供一种低温制冷系统，用于通过重复多级混合制冷剂的膨胀和蒸发而顺序获得低温来实现超低温。 制冷系统包括热交换器和最终蒸发器与压缩机之间的压缩机。 热交换器使得用于压缩机的吸入管中的蒸发的制冷剂蒸汽被加热并被吸入压缩机，并且使由冷凝器冷凝的制冷剂过冷。 制冷系统包括在气液分离器和最终蒸发器之间彼此连接的多个膨胀/抽吸装置。

    Method and apparatus for exchanging heat with a condensable fluid
    33.
    发明授权
    Method and apparatus for exchanging heat with a condensable fluid 失效
    用于与可冷凝流体进行热交换的方法和装置

    公开(公告)号：US4261177A

    公开(公告)日：1981-04-14

    申请号：US13531

    申请日：1979-02-21

    Applicant: Jacques Sterlini

    Inventor： Jacques Sterlini

    IPC: F04D29/58 ,  F24J3/00 ,  F25B1/10 ,  F24F3/16

    CPC classification number: F24J3/00 ,  F04D29/58 ,  F25B1/10 ,  F25B2341/0012 ,  F25B2341/0015 ,  F25B2400/23

    Abstract: A process and apparatus for exchanging heat with condensable fluid are disclosed. In the process, a two-phase fluid is passed through the tubes of a heat exchanger under conditions of temperature and pressure such that the quality of the two-phase flow lies in the range of 0.03 to 0.97. The two-phase fluid is in a state of thermodynamic saturation at both the entry and exit of the heat exchanger. The change in quality of the two-phase mixture passing through the heat exchanger is distributed over the entire heat exchanger. The apparatus according to the invention includes a plurality of connected modular stages, each stage including a heat exchanger, a vapor-liquid separator, a compressor, an ejector and the suitable conduits to establish fluid communication between adjacent stages.

    Abstract translation: 公开了一种与可冷凝流体进行热交换的方法和装置。 在此过程中，两相流体在温度和压力条件下通过热交换器的管，使得两相流的质量在0.03至0.97的范围内。 两相流体在热交换器的入口和出口都处于热力学饱和状态。 通过热交换器的两相混合物的质量变化分布在整个热交换器上。 根据本发明的装置包括多个连接的模块化阶段，每个阶段包括热交换器，气 - 液分离器，压缩机，喷射器和用于在相邻级之间建立流体连通的合适导管。

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