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    • 2. 发明申请
    • Heat exchanger
    • 热交换器
    • US20050284617A1
    • 2005-12-29
    • US11218455
    • 2005-09-02
    • Masahiro KobayashiHideaki MukaidaHiroshi MukaiyamaNorio SawadaMasafumi UedaShigeya IshigakiKoji Sato
    • Masahiro KobayashiHideaki MukaidaHiroshi MukaiyamaNorio SawadaMasafumi UedaShigeya IshigakiKoji Sato
    • F24F20060101F28D1/04F28D1/047F28F1/32
    • F28D1/0477F28F1/325
    • A heat exchanger is provided in which high heat transfer efficiency has been attained by optimizing the slit array and setting an optimum range for the width of a slit and the spacing between slits. Slits 51 and 52 formed in front of the heat transfer coil 4 and slits 55 and 56 formed behind the heat transfer coil are arranged so as to provide a mutually different length among adjoining partitioned slits in the vertical direction, as well as a mutually different length between directly opposite partitioned slits in the horizontal direction. As a result, the position at which the slit is partitioned is staggered. The two slits 53 and 54 formed side by side between heat transfer coil 4 and heat transfer coil 4 are of the same length. For a 7 mm diameter heat transfer coil, the slit width relative to the diameter of the heat transfer coil ranges from 1.2/7 (approximately 0.17) to 2.0/7 (approximately 0.29), and the slit spacing relative to the diameter of the heat transfer coil ranges from 1.3/7 (approximately 0.18) to 3.5/7 (approximately 0.5).
    • 提供了一种热交换器,其中通过优化狭缝阵列并设置狭缝宽度和狭缝之间的间距的最佳范围已经实现了高传热效率。 在传热线圈4的前方形成的狭缝51,52和在传热线圈后面形成的狭缝55,56布置成在相邻的分隔开的狭缝之间在垂直方向上提供相互不同的长度,以及相互不同的长度 在水平方向上直接相对的分隔狭缝之间。 结果,狭缝被分隔的位置交错。 在传热线圈4和传热线圈4之间并排形成的两个狭缝53和54具有相同的长度。 对于7mm直径的传热线圈,相对于传热线圈的直径的狭缝宽度范围为1.2 / 7(约0.17)至2.0 / 7(约0.29),并且相对于热的直径的狭缝间隔 传输线圈范围为1.3 / 7(约0.18)至3.5 / 7(约0.5)。
    • 6. 发明申请
    • HEAT EXCHANGER AND MANUFACTURING METHOD OF THE SAME
    • 热交换器及其制造方法
    • US20100025025A1
    • 2010-02-04
    • US12442282
    • 2007-09-26
    • Kazuyoshi TomochikaNorio SawadaHiroshi MukaiyamaKotaro Matsu
    • Kazuyoshi TomochikaNorio SawadaHiroshi MukaiyamaKotaro Matsu
    • F28F3/00B23P15/26
    • F28D9/005F25B39/00F28F3/027Y10T29/49378
    • There is disclosed a heat exchanger capable of suppressing the increase of a pressure drop while improving a non-uniform rate distribution of a fluid. A heat exchanger T of the present invention is constituted of flat plates 1, 2 each having an inflow port 15 of the fluid on one end thereof and an outflow port 16 of the fluid on the other end, and offset type fins 5 provided in the flat plates 1, 2, and includes a fin orthogonal region H where the plate fins 5 cross the flow direction of the fluid from the inflow port 15 to the outflow port 16 at right angles and a fin parallel region V where the plate fins 5 are disposed in parallel with the flow direction of the fluid from the inflow port 15 to the outflow port 16, the fin orthogonal regions H are provided on the sides of the inflow port 15 and the outflow port 16, and the fin parallel region V is provided between the respective fin orthogonal regions H.
    • 公开了能够抑制压降增加的热交换器,同时提高流体的不均匀分布。 本发明的热交换器T由平板1,2构成,平板1,2的一端具有流体的流入口15和另一端的流体的流出口16, 平板1,2,并且包括鳍片正交区域H,其中板状散热片5以直角从流入端口15到流出端口16流过流体的流动方向,并且翅片平行区域V 与从流入口15到流出口16的流体的流动方向平行配置,翅片正交区域H设置在流入口15和流出口16的侧面,并且翅片平行区域V设置 在相应的翅片正交区域H之间。
    • 9. 发明申请
    • Cooling and heating system
    • 制冷供暖系统
    • US20060218948A1
    • 2006-10-05
    • US11392772
    • 2006-03-30
    • Masahisa OtakeIchiro KamimuraHiroshi MukaiyamaKoji Sato
    • Masahisa OtakeIchiro KamimuraHiroshi MukaiyamaKoji Sato
    • F25B13/00
    • F25B13/00F25B9/008F25B2309/061F25B2313/0231F25B2313/02791F25B2313/0314F25B2313/0315F25B2339/047F25B2500/19F25B2600/0253F25B2600/17F25B2700/1931F25B2700/21152F25B2700/2117Y02B30/741
    • There is disclosed a cooling and heating system in which a refrigerant is used in a supercritical state and in which cooling and heating capacity can be controlled so as to maximize a coefficient of performance. A cooling and heating system 130 includes: an outdoor unit 101 indicating a compressor 102 and an outdoor heat exchanger 103a; a plurality of indoor units 105 including indoor heat exchangers 106; a high pressure tube 111; a low pressure tube 112; and an intermediate tube 113. The system includes: a refrigerant pressure detection unit PC01 for measuring a pressure of the refrigerant discharged from the compressor 102; a first refrigerant temperature detection unit TC03 which measures an outlet temperature of the refrigerant in a case where the outdoor heat exchanger 103 functions as a gas cooler and which measures an inlet temperature of the refrigerant in a case where the outdoor heat exchanger 103 functions as an evaporator; and a second refrigerant temperature detection unit TCO8 which measures an outlet temperature of the refrigerant in a case where the indoor heat exchanger 106 functions as a gas cooler and which measures an inlet temperature of the refrigerant in a case where the indoor heat exchanger 106 functions as an evaporator.
    • 公开了一种冷却和加热系统,其中在超临界状态下使用制冷剂,并且其中可以控制冷却和加热能力以使性能系数最大化。 冷却和加热系统130包括:表示压缩机102和室外热交换器103a的室外机101; 包括室内热交换器106的多个室内机105; 高压管111; 低压管112; 和中间管113。 该系统包括:用于测量从压缩机102排出的制冷剂的压力的制冷剂压力检测单元P01C01 < 在室外热交换器103用作气体冷却器的情况下,测量制冷剂的出口温度并测量制冷剂的入口温度的第一制冷剂温度检测单元T03C03在以下情况下 室外热交换器103用作蒸发器; 以及在室内热交换器106作为气体冷却器的情况下测量制冷剂的出口温度的第二制冷剂温度检测单元T8C8,并且在一个情况下测量制冷剂的入口温度 其中室内热交换器106用作蒸发器。