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    • 1. 发明申请
    • Heat exchanger and method of manufacturing the same
    • 换热器及其制造方法
    • US20080230214A1
    • 2008-09-25
    • US12075560
    • 2008-03-12
    • Wei ChenHiroyasu ShimanukiKen MutoEtsuo Hasegawa
    • Wei ChenHiroyasu ShimanukiKen MutoEtsuo Hasegawa
    • F28F9/02B21D53/02
    • B21D53/02F28F9/0246F28F2275/125Y10T29/4935
    • A heat exchanger includes a connector for connecting a header tank to an exterior pipe. The connector includes a first member configured to define a communication path through which a tank open portion of the header tank communicates with an interior of the exterior pipe, and a second member to which the first member is fixed. The first member and the second member are fixed to each other after being separately formed by pressing, and the second member has a fastening portion through which the connector is fastened to the exterior pipe. Furthermore, the first member includes a first connection portion that is fitted into the tank open portion at one open side of the communication path, and a second connection portion fitted to an open portion of the exterior pipe at other open side of the communication path.
    • 热交换器包括用于将集管箱连接到外部管道的连接器。 连接器包括构造成限定连通路径的第一构件,集管箱的罐开口部分通过该连通路径与外部管道的内部连通,第二构件固定到第一构件。 第一构件和第二构件在通过按压分开形成之后彼此固定,并且第二构件具有紧固部分,连接器通过该紧固部分紧固到外部管道。 此外,第一构件包括:第一连接部,其在连通路径的一个开放侧装配到罐开口部;以及第二连接部,其在连通路径的另一开口侧嵌合到外管的开口部。
    • 7. 发明授权
    • Heat exchanger
    • 热交换器
    • US06923019B2
    • 2005-08-02
    • US10685794
    • 2003-10-15
    • Masaaki KawakuboEtsuo HasegawaKen Muto
    • Masaaki KawakuboEtsuo HasegawaKen Muto
    • F25B1/00F25B39/04F28D1/053F28F1/02F28F9/02
    • F28F1/022F28D1/05391F28D2021/0073
    • In a high-pressure side heat exchanger for a vapor compression refrigerant cycle, a refrigerant passage is formed such that a flow area (S), a length (L), and an equivalent diameter (d) satisfy the conditional expression 0.04×e−1.8d≦S/L≦2.1×e−1.8d. The flow area (S) is obtained by dividing the product of a total cross-sectional area of the passages in one tube and the number of tubes by the path number. The length (L) is a flow distance of the refrigerant from the refrigerant inlet to the refrigerant outlet. That is, the length (L) is obtained by the product of the length of the tube and the path number. The diameter (d) is obtained by dividing the product of four and the cross-sectional area of the passage by a circumference of the passage.
    • 在蒸汽压缩制冷剂循环的高压侧热交换器中,形成制冷剂通路,使得流动面积(S),长度(L)和当量直径(d)满足条件表达式0.04xe -1.8d <= S / L <= 2.1×E -1.8d 。 流量面积(S)通过将一个管中的通道的总截面积与管数的乘积除以路径数获得。 长度(L)是制冷剂从制冷剂入口到制冷剂出口的流动距离。 也就是说,长度(L)通过管的长度和路径数的乘积获得。 直径(d)通过将通道的四倍和通道的横截面积除以通道的圆周来获得。