WO2017020629A1 - 相变抑制传热板式热交换器 - Google Patents

相变抑制传热板式热交换器 Download PDF

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Publication number
WO2017020629A1
WO2017020629A1 PCT/CN2016/082585 CN2016082585W WO2017020629A1 WO 2017020629 A1 WO2017020629 A1 WO 2017020629A1 CN 2016082585 W CN2016082585 W CN 2016082585W WO 2017020629 A1 WO2017020629 A1 WO 2017020629A1
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WIPO (PCT)
Prior art keywords
plate
heat transfer
phase change
liquid
change suppression
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PCT/CN2016/082585
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English (en)
French (fr)
Inventor
仝爱星
李居强
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浙江嘉熙光电设备制造有限公司
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Application filed by 浙江嘉熙光电设备制造有限公司 filed Critical 浙江嘉熙光电设备制造有限公司
Priority to US15/739,990 priority Critical patent/US10619951B2/en
Publication of WO2017020629A1 publication Critical patent/WO2017020629A1/zh

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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F23/00—Features relating to the use of intermediate heat-exchange materials, e.g. selection of compositions
    • F28F23/02—Arrangements for obtaining or maintaining same in a liquid state
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/03—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits
    • F28D1/0308—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other
    • F28D1/0316—Assemblies of conduits in parallel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
    • F28D15/02—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes
    • F28D15/0233—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies in which the medium condenses and evaporates, e.g. heat pipes the conduits having a particular shape, e.g. non-circular cross-section, annular
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/12—Elements constructed in the shape of a hollow panel, e.g. with channels
    • F28F3/14—Elements constructed in the shape of a hollow panel, e.g. with channels by separating portions of a pair of joined sheets to form channels, e.g. by inflation

Definitions

  • FIG. 7 is a structural schematic view showing a liquid pipe in a phase change suppression heat transfer heat exchange plate in a phase change suppression heat transfer plate type heat exchanger according to Embodiment 2 of the present invention.
  • FIGS. 10 to 11 are schematic perspective views showing a phase change suppression heat transfer plate type heat exchanger according to a third embodiment of the present invention.
  • FIGS. 12 to 13 are schematic perspective views showing a phase change suppression heat transfer plate type heat exchanger according to a fourth embodiment of the present invention.
  • the present invention provides a phase change suppression heat transfer plate heat exchanger, which comprises: a liquid communication main pipe 2, a liquid communication main pipe 3, and a plurality of blocks. a phase change suppression heat transfer heat exchange plate 11 arranged in parallel; the surfaces of the plurality of phase change suppression heat transfer heat exchange plates 11 are parallel to each other, and the phase change suppression heat transfer heat exchange plate 11 is a composite plate structure,
  • the phase change suppression heat transfer heat exchange plate 11 is formed with a liquid pipe 110 having a certain structural shape and a closed network pipe 108 having a certain structural shape; the closed network pipe 108 is filled with a phase change suppression working medium 109;
  • the inlet liquid communication manifold 2 and the liquid outlet communication manifold 3 are at least fixed to one side of the phase change suppression heat transfer heat exchange plate 11, and the length direction of the liquid inlet communication manifold 2 and the liquid outlet communication manifold 3
  • the plurality of phase change suppression heat transfer heat exchange plates 11 extend in a direction in which the heat transfer heat exchange plates 11 are arranged in
  • the liquid inlet communication manifold 2 and the liquid outlet communication manifold 3 are respectively located on opposite sides of the phase change suppression heat transfer heat exchange plate 11; the surface of the phase change suppression heat transfer heat exchange plate 11 may be The liquid inlet communication manifold 2 and the liquid outlet communication manifold 3 are perpendicular to each other, and may be inclined at a certain angle with respect to the liquid inlet communication manifold 2 and the liquid outlet communication manifold 3, for example, the phase change suppression transmission
  • the angle of inclination of the heat exchange plate 11 with respect to the liquid inlet communication manifold 2 and the liquid outlet communication manifold 3 is 5° to 90°; preferably, in the embodiment, the phase change suppression heat transfer heat exchange plate
  • the surface of 11 may be perpendicular to the liquid inlet communication manifold 2 and the liquid outlet communication manifold 3.
  • one end of the liquid communication communication manifold 2 and the liquid communication communication manifold 3 is closed, and the other end is for connection with a liquid system (not shown).
  • the liquid conduit 110 and the closed network conduit 108 are both formed by an inflation process, and a surface corresponding to the closed network conduit 108 is formed on the surface of the phase change suppression heat transfer heat exchange plate 11 A raised structure 107 and a second raised structure 105 corresponding to the liquid conduit 110.
  • the first raised structure 107 and the second raised structure 105 are formed on different surfaces of the phase change suppression heat transfer heat exchange plate 11, respectively.
  • the phase change suppression heat transfer heat exchange plate 11 includes an intermediate plate 112, a first plate 111, and a second plate 113; the first plate 111, the intermediate plate 112, and the first The two plates 113 are sequentially stacked, and the first plate 111 and the second plate 113 are respectively located at two sides of the intermediate plate 112, and are combined with the intermediate plate 112 by a rolling process; the closed network a pipe 108 is located between the intermediate plate 112 and the first plate 111, the first protruding structure 107 is located on the first plate 111; the liquid pipe 110 is formed on the intermediate plate 112 and the Between the second plates 113, the second raised structure 105 is located on the second plate 113.
  • the shape of the liquid pipe 110 may be designed according to actual needs, as described in FIG. 2, in the present example, the shape of the liquid pipe 110 is linear, but the embodiment is not limited thereto.
  • the shape of the liquid pipe 110 is linear, wherein the linear pipe structure is the liquid pipe 110, and the two sides of the liquid pipe 110 are non-liquid pipe portions 104;
  • One end of the liquid pipe 110 is a liquid inlet pipe 102, and the other end is a liquid connection pipe 103.
  • the liquid pipe 110 passes through the liquid inlet pipe 102 and the liquid outlet pipe 103 and the liquid inlet communication pipe 2 and the outlet.
  • the liquid communication manifolds 3 are in communication.
  • the material of the phase change suppression heat transfer heat exchange plate 11 (ie, the material of the intermediate plate 8, the first plate 7 and the second plate 9) should be a material having good thermal conductivity; preferably In the present embodiment, the material of the phase change suppression heat transfer heat exchange plate 11 may be copper, a copper alloy, aluminum, an aluminum alloy, titanium, a titanium alloy, or any combination of any one or more.
  • the phase change suppression heat transfer plate type heat exchanger of the present invention through which the liquid flows through the liquid communication main pipe 2 in parallel, flows through the liquid pipes 110 of the plurality of phase change suppression heat transfer heat exchange plates 11, and conducts heat through the pipe wall.
  • the phase change suppression working medium 109 in the adjacent closed network conduit 108 on the phase change suppression heat transfer heat exchange plate 11 further causes the temperature of the entire phase change suppression heat transfer heat exchange plate 11 to be uniform and flows through
  • the phase change suppresses the heat exchange of the air of the heat transfer heat exchange plate 11 to increase the temperature of the corresponding air, and the temperature of the liquid flowing through the phase change heat transfer heat exchange plate 11 is lowered, and the liquid entering the temperature is lowered.
  • the liquid communication manifold 3 is introduced into the liquid system for the next round of heat exchange cycles.
  • the present invention further provides a phase change suppression heat transfer plate heat exchanger, the structure of the phase change suppression heat transfer plate heat exchanger in the embodiment and the phase described in the first embodiment.
  • the structure of the variable suppression heat transfer plate heat exchanger is substantially the same, and the difference is that the liquid pipe 110 is distributed on the surface of the phase change suppression heat transfer heat exchange plate 11; the phase change suppresses heat transfer heat
  • the surface of the exchange plate 11 is different from the angle between the liquid inlet communication manifold 2 and the liquid outlet communication manifold 3; the phase change suppression heat transfer plate heat exchanger has different mounting directions in practical applications.
  • the liquid pipe 110 is preferably located on a longitudinal center line of the phase change suppression heat transfer heat exchange plate 11; and in this embodiment, as shown in FIG. 7, the liquid pipe is 110 close to the phase change to suppress heat transfer and heat transfer Change the side of the board.
  • the preferred mounting direction of the phase change suppression heat transfer plate heat exchanger is that the phase change suppression heat transfer heat exchange plate 11 and the liquid pipe 110 are vertically downward and perpendicular to the horizontal plane.
  • the liquid inlet communication manifold 2 is located below the phase change suppression heat transfer heat exchange plate 11, and the liquid outlet communication manifold 3 is located above the phase change suppression heat transfer heat exchange plate 11, the liquid communication connection
  • the main pipe 2 and the liquid discharge communication pipe 3 are parallel to the horizontal plane; in this embodiment, as shown in FIG. 5 and FIG. 6, the arrow marked with g indicates the direction of gravity, that is, the direction vertically downward.
  • phase change suppression heat transfer plate heat exchanger of the embodiment are the same as those of the phase change suppression heat transfer plate heat exchanger of the first embodiment. For details, refer to the first embodiment. It is no longer exhaustive here.
  • the present invention further provides a phase change suppression heat transfer plate heat exchanger, the structure of the phase change suppression heat transfer plate heat exchanger in the embodiment and the phase described in the first embodiment.
  • the structure of the variable suppression heat transfer plate heat exchanger is substantially the same, and the difference between the two is that the liquid pipe 110 is distributed on the surface of the phase change suppression heat transfer heat exchange plate 11; the phase change suppression heat transfer plate type
  • the heat exchangers are installed in different orientations in practical applications.
  • the liquid pipe 110 is preferably located on a longitudinal center line of the phase change suppression heat transfer heat exchange plate 11; and in this embodiment, as shown in FIG. 7, the liquid pipe is 110 is adjacent to one side of the phase change suppression heat transfer heat exchange plate.
  • the preferred mounting direction of the phase change suppression heat transfer plate heat exchanger is that the phase change suppression heat transfer heat exchange plate 11 and the liquid pipe 110 are vertically downward and perpendicular to the horizontal plane.
  • the liquid inlet communication manifold 2 is located below the phase change suppression heat transfer heat exchange plate 11, and the liquid outlet communication manifold 3 is located above the phase change suppression heat transfer heat exchange plate 11, the liquid communication connection
  • the manifold 2 and the outlet communicating manifold 3 are both parallel to the horizontal plane; in this embodiment, as shown in FIGS. 10 and 11, the arrow marked with g indicates the direction of gravity, that is, the direction vertically downward.
  • phase change suppression heat transfer heat exchange plates 11 are vertically vertically downward from the horizontal plane; the liquid inlet communication manifold 2 and the liquid outlet communication manifold 3 are located on both sides of the phase change suppression heat transfer heat exchange plate 11 And both are parallel to the horizontal plane; the liquid conduit 110 is parallel to the horizontal plane.
  • phase change suppression heat transfer plate heat exchanger of the embodiment are the same as those of the phase change suppression heat transfer plate heat exchanger of the first embodiment. For details, refer to the first embodiment. It is no longer exhaustive here.
  • the present invention further provides a phase change suppression heat transfer plate heat exchanger, the structure of the phase change suppression heat transfer plate heat exchanger in the embodiment and the phase described in the first embodiment.
  • the structure of the variable suppression heat transfer plate heat exchanger is substantially the same, the difference between the two is that the shape of the liquid pipe 110 is different; the liquid pipe 110 is distributed on the surface of the phase change suppression heat transfer heat exchange plate 11
  • the distribution position of the liquid inlet communication manifold 2 and the liquid outlet communication manifold 3 is different; the phase change suppression heat transfer plate heat exchanger has different installation directions in practical applications.
  • the shape of the liquid pipe 110 is preferably linear, and in the embodiment, as shown in FIG. 12 and FIG. 14, the shape of the liquid pipe 110 is U-shaped.
  • the liquid pipe 110 is preferably located on a longitudinal center line of the phase change suppression heat transfer heat exchange plate 11; in this embodiment, as shown in FIG. 12 and FIG.
  • the liquid conduit 110 is adjacent to one side of the phase change suppression heat transfer heat exchange plate.
  • the liquid inlet communication manifold 2 and the liquid outlet communication manifold 3 are preferably respectively located on opposite sides of the phase change suppression heat transfer heat exchange plate 11;
  • the liquid communication main pipe 2 and the liquid discharge communication main pipe 3 are located on the same side of the phase change suppression heat transfer heat exchange plate 11.
  • the preferred mounting direction of the phase change suppression heat transfer plate heat exchanger is that the phase change suppression heat transfer heat exchange plate 11 and the liquid pipe 110 are vertically downward and perpendicular to the horizontal plane.
  • the liquid inlet communication manifold 2 is located below the phase change suppression heat transfer heat exchange plate 11, and the liquid outlet communication manifold 3 is located above the phase change suppression heat transfer heat exchange plate 11, the liquid communication connection
  • the main pipe 2 and the liquid discharge communication pipe 3 are parallel to the horizontal plane; in this embodiment, as shown in FIG. 12 and FIG. 13, the arrow marked with g indicates the direction of gravity, that is, the direction vertically downward.
  • the phase change suppression heat transfer heat exchange plate 11 is vertically vertically downward from the horizontal plane; the liquid inlet communication manifold 2 and the liquid outlet communication manifold 3 are located on one side of the phase change suppression heat transfer heat exchange plate 11 And both are parallel to the horizontal plane; the liquid conduit 110 is parallel to the horizontal plane.
  • phase change suppression heat transfer plate heat exchanger when used for heat dissipation, that is, the temperature of the liquid in the liquid pipe 110 is high, heat of the liquid in the liquid pipe 110 needs to be dissipated into the air.
  • the phase change suppressing heat transfer heat exchange plate 11 When the liquid is cooled, the phase change suppressing heat transfer heat exchange plate 11 is as shown in FIGS. 12 to 13, and the liquid pipe 110 is adjacent to the phase change suppression heat transfer heat exchange plate 11; and when the phase change is performed
  • the heat transfer plate heat exchanger is used for heating, that is, when the temperature of the liquid in the liquid pipe 110 is low, when the liquid needs to be heated by the heat exchanger, the liquid pipe 110 should be close to the phase change suppression pass.
  • the structure in Figs. 12 and 13 is rotated by 180° on the premise that the direction of gravity is kept constant.
  • phase change suppression heat transfer plate heat exchanger of the embodiment are the same as those of the phase change suppression heat transfer plate heat exchanger of the first embodiment. For details, refer to the first embodiment. It is no longer exhaustive here.
  • the present invention further provides a phase change suppression heat transfer plate heat exchanger, the structure of the phase change suppression heat transfer plate heat exchanger in the embodiment and the phase described in the first embodiment.
  • the structure of the variable suppression heat transfer plate type heat exchanger is substantially the same, and the difference is that the phase change suppresses the heat transfer heat exchange plate 11 having a different structure; the first convex corresponding to the closed network pipe 108
  • the structure 107 and the second protrusion structure 105 corresponding to the liquid pipe 110 are different in position on the phase change suppression heat transfer heat exchange plate 11.
  • the phase change suppression heat transfer heat exchange plate 11 includes an intermediate plate 112, a first plate 111, and a second plate 113; the first plate 111, the intermediate plate 112, and the first The two plates 113 are sequentially stacked, and the first plate 111 and the second plate 113 are respectively located on both sides of the intermediate plate 112, and are combined with the intermediate plate 112 by a rolling process;
  • the phase change suppression heat transfer heat exchange plate 11 includes a first plate member 111 and a second plate member 113; the first plate member 111 and the second plate member 113 are compounded by a rolling process.
  • the first protruding structure 107 and the second protruding structure 105 are respectively formed on different surfaces of the phase change suppression heat transfer heat exchange plate 11 and the closed network is a pipe 108 is located between the intermediate plate 112 and the first plate 111, and the first protruding structure 107 is located on the first plate 111, the liquid pipe 110 is formed between the intermediate plate 112 and the second plate 113, and the second protrusion structure 105 is located on the second plate 113.
  • first protruding structure 107 and the second protruding structure 105 are located on the first plate 111 or the second plate 113 at the same time, which means that the phase change suppresses heat transfer heat.
  • the switching plate 11 is in a single-sided expanded state, and the first protruding structure 107 and the second protruding structure 105 are located on the first plate 111 and the second plate 113 at the same time.
  • the heat exchange plate 11 is in a double-sided expanded state.
  • the first protruding structure 107 and the second protruding structure 105 are simultaneously located on the first plate 111 and the second plate 113.
  • the installation direction of the phase change suppression heat transfer plate heat exchanger can be set according to actual needs, which is not limited herein.
  • phase change suppression heat transfer plate heat exchanger of the embodiment are the same as those of the phase change suppression heat transfer plate heat exchanger of the first embodiment. For details, refer to the first embodiment. It is no longer exhaustive here.
  • the present invention provides a phase change suppression heat transfer plate heat exchanger in which a closed network pipe and a liquid pipe are combined in a phase change suppression heat transfer heat exchange plate of a phase change suppression heat transfer plate heat exchanger.
  • the phase change suppression working medium is filled in the closed network pipe to constitute a phase change suppression heat transfer device, and the temperature change of the phase change suppression heat transfer heat exchange plate is improved; the heat transfer rate of the heat transfer device is suppressed by the phase change
  • the characteristics of uniform temperature are improved, the temperature difference with air and the effective heat transfer area are improved, the heat dissipation capacity and heat exchange efficiency of the phase change suppression heat transfer heat exchange plate are greatly improved; and the phase change suppression heat transfer plate heat exchanger has The characteristics of uniform temperature and high heat transfer greatly shorten the length of the liquid pipeline, reduce the flow resistance and energy consumption, and the amount of fluid used, and improve the efficiency and energy efficiency ratio of the heat exchanger.

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  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

一种相变抑制传热板式热交换器，包括：进液连通总管（2）、出液连通总管（3）及多块平行排布的相变抑制传热热交换板（11）；相变抑制传热热交换板（11）内形成有具有一定结构形状的液体管道（110）及具有一定结构形状的封闭网络状管道（108）；封闭网络状管道（108）内填充有相变抑制工作介质（109）；进液连通总管（2）及出液连通总管（3）至少固定于相变抑制传热热交换板（11）的一边，其长度方向沿多块相变抑制传热热交换板（11）平行排布的方向延伸，且均与液体管道（110）的内部相连通。热交换器利用相变抑制传热器件的导热速率快、均温性好的特点，提高与空气的温差和有效传热面积，进而提高了散热能力和热交换效率；缩短流体管路的长度，减小流动阻力和能耗，以及流体的使用量，提高热交换器的效率和能效比。

Description

相变抑制传热板式热交换器 技术领域
本发明涉及一种热交换器，特别是涉及一种相变抑制传热板式热交换器。
背景技术
气液热交换器广泛应用于汽车散热器、空调的蒸发器和冷凝器，高铁动车牵引系统变流器的液冷系统、风电变流器冷却系统、数据中心等领域。随着技术的飞速发展，对热交换器的要求也越来越高，既要换热效率高、体积小、重量轻、又要噪声小，易维护，成本低。
目前通用的气液热交换器主要采用铜管外胀接铝散热片换热器，即液体管路为盘绕的铜管，铜管外胀接铝制散热片组，液体在管内流动，将热量通过管壁传导给散热片，由风扇驱动空气流过散热片，带走热量，降低管内液体的温度，从而实现将液体的热量散发到冷却空气中，达到系统冷却的目的。由于液体管路为串联，且管路长，流动阻力大，管外翅片与液体管路之间存在接触热阻，且采用的散热片导热系数在200W/m.k,，翅片效率较低，翅片尺寸较小，因此必须增加液体管路的长度，翅片的数量，才能满足散热需求，这也使得热交换器重量和体积增大，同时增加了液体循环的动力消耗，系统成本高、体积大、重量重。
发明内容
鉴于以上所述现有技术的缺点，本发明的目的在于提供一种相变抑制传热板式热交换器，用于解决现有技术铜管外胀接铝散热片换热器存在的液体管路长，流动阻力大，散热片效率低等问题，以大幅提高气液热交换器的翅片效率和散热能力，减小液体管路长度和流动阻力，以满足大功率热交换系统的散热需求。
为实现上述目的及其他相关目的，本发明提供一种相变抑制传热板式热交换器，所述相变抑制传热板式热交换器包括：进液连通总管、出液连通总管及多块平行排布的相变抑制传热热交换板；
所述相变抑制传热热交换板为复合板式结构，所述相变抑制传热热交换板内形成有具有一定结构形状的液体管道及具有一定结构形状的封闭网络状管道；所述封闭网络状管道内填充有相变抑制工作介质；
所述进液连通总管及所述出液连通总管至少固定于所述相变抑制传热热交换板的一边，所述进液连通总管及所述出液连通总管的长度方向沿所述多块相变抑制传热热交换板平行排布的方向延伸，且所述进液连通总管及所述出液连通总管的内部均与所述液体管道的内部相连通。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述液体管道及所述封闭网络状管道均通过吹胀工艺形成，并在所述相变抑制传热热交换板表面形成与所述封闭网络状管道相对应的第一凸起结构及与所述液体管道相对应的第二凸起结构。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述第一凸起结构及所述第二凸起结构分别形成于所述相变抑制传热热交换板的不同表面上。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述相变抑制传热热交换板包括中间板材、第一板材及第二板材；所述第一板材、所述中间板材及所述第二板材依次叠置，所述第一板材及所述第二板材分别位于所述中间板材的两侧，并与所述中间板材通过辊压工艺复合在一起；
所述封闭网络状管道位于所述中间板材及所述第一板材之间，所述第一凸起结构位于所述第一板材上；
所述液体管道形成于所述中间板材及所述第二板材之间，所述第二凸起结构位于所述第二板材上。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述进液连通总管及所述出液连通总管分别位于所述相变抑制传热热交换板相对的两边；所述液体管道的形状为直线形。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述液体管道位于所述相变抑制传热热交换板的纵向中心线上。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述液体管道靠近所述相变抑制传热热交换板的一边。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述进液连通总管及所述出液连通总管位于所述相变抑制传热热交换板的同一边；所述液体管道的形状为U型。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述第一凸起结构及所述第二凸起结构形成于所述相变抑制传热热交换板的同一表面上。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述相变抑制传热热交换板的两表面上均形成有所述第一凸起结构及所述第二凸起结构。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述相变抑制传热热交换板包括第一板材及第二板材；所述第一板材及所述第二板材通过辊压工艺复合在一起；
所述封闭网络状管道及所述液体管道位于所述第一板材及所述第二板材之间；所述第一凸起结构及所述第二凸起结构同时位于所述第一板材上、所述第二板材上、或所述第一板材及所述第二板材上。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述进液连通总管及所述出液连通总管分别位于所述相变抑制传热热交换板的两端；所述液体管道的形状为直线形，且所述液体管道靠近所述相变抑制传热热交换板的一边。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述进液连通总管及所述出液连通总管的一端封闭，另一端与液体系统相连接。
作为本发明的相变抑制传热板式热交换器的一种优选方案，所述相变抑制传热热交换板的表面与所述进液连通总管及所述出液连通总管相垂直或相对于所述进液连通总管及所述出液连通总管倾斜一定的角度。
本发明的相变抑制传热板式热交换器，具有以下有益效果：在相变抑制传热板式热交换器的相变抑制传热热交换板内将封闭网络状管道及液体管道组合在一起，在封闭网络状管道内充入相变抑制工作介质，构成相变抑制传热器件，提高了相变抑制传热热交换板的均温性；利用相变抑制传热器件的导热速率快、均温性好的特点，提高了与空气进行热交换的温差和有效传热面积，大大提高了相变抑制传热热交换板的散热能力和热交换效率；使得相变抑制传热板式热交换器具有均温和高效换热的特性，大大缩短液体管道的长度，减小流动阻力和能耗，以及流体的使用量，提高热交换器的效率和能效比。
附图说明
图1显示为本发明实施例一中提供的相变抑制传热板式热交换器的立体结构示意图。
图2显示为本发明实施例一中提供的相变抑制传热板式热交换器中相变抑制传热热交换板中液体管道的结构示意图。
图3显示为本发明实施例一中提供的相变抑制传热板式热交换器中相变抑制传热热交换板中封闭网络状管道的结构示意图。
图4显示为本发明实施例一中提供的相变抑制传热板式热交换器中相变抑制传热热交换板的局部截面结构示意图。
图5显示为本发明实施例二中提供的相变抑制传热板式热交换器的立体结构示意图。
图6显示为本发明实施例二中提供的相变抑制传热板式热交换器的侧视结构示意图。
图7显示为本发明实施例二中提供的相变抑制传热板式热交换器中相变抑制传热热交换板中液体管道的结构示意图。
图8显示为本发明实施例二中提供的相变抑制传热板式热交换器中相变抑制传热热交换板中封闭网络状管道的结构示意图。
图9显示为本发明实施例二中提供的相变抑制传热板式热交换器中相变抑制传热热交换板的局部截面结构示意图。
图10至图11显示为本发明实施例三中提供的相变抑制传热板式热交换器的立体结构示意图。
图12至图13显示为本发明实施例四中提供的相变抑制传热板式热交换器的立体结构示意图。
图14显示为本发明实施例四中提供的相变抑制传热板式热交换器中相变抑制传热热交换板中液体管道的结构示意图。
图15显示为本发明实施例四中提供的相变抑制传热板式热交换器中相变抑制传热热交换板中封闭网络状管道的结构示意图。
图16显示为本发明实施例五中提供的相变抑制传热板式热交换器中相变抑制传热热交换板中液体管道及封闭网络状管道的结构示意图。
图17显示为本发明实施例五中提供的相变抑制传热板式热交换器中相变抑制传热热交换板的局部截面结构示意图。
元件标号说明
11  相变抑制传热热交换板
2   进液连通总管
3   出液连通总管
102 进液体接管
103 出液体接管
104 非液体管道部分
105 第二凸起结构
106 非网格状管道部分
107 第一凸起结构
108 网格状管道
109 相变抑制工作介质
110 液体管道
111 第一板材
112 中间板材
113 第二板材
α   出液连通总管与水平面垂直时相变抑制传热热交换板与水平面的夹角
具体实施方式
以下通过特定的具体实例说明本发明的实施方式，本领域技术人员可由本说明书所揭露的内容轻易地了解本发明的其他优点与功效。本发明还可以通过另外不同的具体实施方式加以实施或应用，本说明书中的各项细节也可以基于不同观点与应用，在没有背离本发明的精神下进行各种修饰或改变。
请参阅图1至图17需要说明的是，本实施例中所提供的图示仅以示意方式说明本发明的基本构想，虽图示中仅显示与本发明中有关的组件而非按照实际实施时的组件数目、形状及尺寸绘制，其实际实施时各组件的型态、数量及比例可为一种随意的改变，且其组件布局型态也可能更为复杂。
实施例一
请参阅图1至图4，本发明提供一种相变抑制传热板式热交换器，所述相变抑制传热板式热交换器包括：进液连通总管2、出液连通总管3及多块平行排布的相变抑制传热热交换板11；所述多块相变抑制传热热交换板11的表面相互平行，所述相变抑制传热热交换板11为复合板式结构，所述相变抑制传热热交换板11内形成有具有一定结构形状的液体管道110及具有一定结构形状的封闭网络状管道108；所述封闭网络状管道108内填充有相变抑制工作介质109；所述进液连通总管2及所述出液连通总管3至少固定于所述相变抑制传热热交换板11的一边，所述进液连通总管2及所述出液连通总管3的长度方向沿所述多块相变抑制传热热交换板11平行排布的方向延伸，且所述进液连通总管2及所述出液连通总管3的内部均与所述液体管道110的内部相连通。
作为示例，所述进液连通总管2及所述出液连通总管3分别位于所述相变抑制传热热交换板11相对的两边；所述相变抑制传热热交换板11的表面可以与所述进液连通总管2及所述出液连通总管3相垂直，也可以相对于所述进液连通总管2及所述出液连通总管3倾斜一定的角度，譬如，所述相变抑制传热热交换板11相对于所述进液连通总管2及所述出液连通总管3倾斜的角度为5°～90°；优选地，本实施例中，所述相变抑制传热热交换板11的表面可以与所述进液连通总管2及所述出液连通总管3相垂直。
作为示例，所述进液连通总管2及所述出液连通总管3的一端封闭，另一端用于与液体系统(未示出)相连接。
作为示例，所述相变抑制工作介质109为流体，优选地，所述相变抑制工作介质109可以为气体或液体或气体与液体的混合物，更为优选地，本实施例中，所述相变抑制工作介质109为液体与气体的混合物。
作为示例，所述液体管道110及所述封闭网络状管道108均通过吹胀工艺形成，并在所述相变抑制传热热交换板11表面形成与所述封闭网络状管道108相对应的第一凸起结构107及与所述液体管道110相对应的第二凸起结构105。
作为示例，所述第一凸起结构107及所述第二凸起结构105分别形成于所述相变抑制传热热交换板11的不同表面上。
作为示例，请参阅图4，所述相变抑制传热热交换板11包括中间板材112、第一板材111及第二板材113；所述第一板材111、所述中间板材112及所述第二板材113依次叠置，所述第一板材111及所述第二板材113分别位于所述中间板材112的两侧，并与所述中间板材112通过辊压工艺复合在一起；所述封闭网络状管道108位于所述中间板材112及所述第一板材111之间，所述第一凸起结构107位于所述第一板材111上；所述液体管道110形成于所述中间板材112及所述第二板材113之间，所述第二凸起结构105位于所述第二板材113上。在相变抑制传热板式热交换器的所述相变抑制传热热交换板11内将所述液体管道110及封闭网络状管道108组合在一起，利用所述相变抑制传热热交换板11的导热速率快、均温性好的特点，提高了所述相变抑制传热热交换板11与空气的热交换温差和有效换热面积，大大提高了所述相变抑制传热热交换板11的散热能力和热交换效率；使得所述相变抑制传热板式热交换器具有均温和高效换热的特性，大大缩短所述液体管道110的长度，减小流动阻力和能耗，以及流体的使用量，提高热交换器的效率和能效比。
作为示例，所述液体管道110的形状可以根据实际需要设计，如图2所述，本示例中以所述液体管道110的形状为直线形作为示例，但本实施例中并不仅限于此。如图2所示，所述液体管道110的形状为直线形，其中，直线状的细管结构即为所述液体管道110，所述液体管道110两侧即为非液体管道部分104；所述液体管道110的一端为进液体接管102，另一端为出液体接管103，所述液体管道110通过所述进液体接管102及所述出液体接管103与所述进液连通总管2及所述出液连通总管3相连通。
作为示例，所述液体管道110位于所述相变抑制传热热交换板11的纵向中心线上。
作为示例，所述封闭网络状管道108的形状可以为六边形蜂窝状、圆形蜂窝状、四边形蜂窝状、首尾串联的多个U形，、菱形、三角形、圆环形或其中任一种以上的任意组合。
图3以所述封闭网络状管道108的形状为六边形蜂窝状为示例，如图3所示，所述相变 抑制传热热交换板11的边缘部分及六边形部分为非网格状管道部分106，环绕各六边形周围并相互连通的结构即为所述封闭网络状管道108。
作为示例，所述相变抑制传热热交换板11的材料(即所述中间板材8、所述第一板材7及所述第二板材9的材料)应为导热性良好的材料；优选地，本实施例中，所述相变抑制传热热交换板11的材料均可以为铜、铜合金、铝、铝合金、钛、钛合金、或任一种以上的任意组合。
请继续参阅图1，在实际应用中所述相变抑制传热板式热交换器的安装方向可以如图1所示，图1中，标有g的箭头表示重力的方向，即竖直向下的方向。此时，所述相变抑制传热热交换板11及所述液体管道110均竖直向下与水平面垂直；所述进液连通总管2位于所述相变抑制传热热交换板11的下方，所述出液连通总管3位于所述相变抑制传热热交换板11的上方，所述进液连通总管2及所述出液连通总管3均与水平面相平行。
需要说明的是，图1仅给出所述相变抑制传热板式热交换器的一种优选安装方向的示例，本实施例中，所述相变抑制传热板式热交换器的安装方向并不以图1中所示的安装方式为限，在其他示例中，所述相变抑制传热板式热交换器的安装方向可以为在图1中所示的安装方向的基础上向左或向右翻转90°、180°或270°，也可以为在图1中所示的安装方向的基础上向前或向后翻转90°、180°或270°。
本发明的相变抑制传热板式热交换器，工作时液体通过所述进液连通总管2、并行流过多个相变抑制传热热交换板11的液体管道110，通过管壁将热量传导至相变抑制传热热交换板11上邻近的封闭网络状管道108中的相变抑制工作介质109，进而使整个所述相变抑制传热热交换板11上温度均匀，并于流过所述相变抑制传热热交换板11的空气进行热交换，从而使相应的空气温度升高，流过所述相变抑传热热交换板11的液体温度降低，温度降低后的液体进入所述出液连通总管3，进入液体系统中，进行下一轮的热交换循环。
实施例二
请参阅图5至图9，本发明还提供一种相变抑制传热板式热交换器，本实施例中所述相变抑制传热板式热交换器的结构与实施例一中所述的相变抑制传热板式热交换器的结构大致相同，二者的区别在于：所述液体管道110在所述相变抑制传热热交换板11表面上分布位置不同；所述相变抑制传热热交换板11的表面与所述进液连通总管2及所述出液连通总管3的夹角不同；所述相变抑制传热板式热交换器在实际应用中的安装方向不同。
具体的，在实施例一中，所述液体管道110优选地位于所述相变抑制传热热交换板11的纵向中心线上；而本实施例中，如图7所示，所述液体管道110靠近所述相变抑制传热热交 换板的一边。
具体的，在实施例一中，所述相变抑制传热热交换板11的表面优选地与所述进液连通总管2及所述出液连通总管3相垂直，即所述相变抑制传热热交换板11的表面与所述进液连通总管2及所述出液连通总管3的优选夹角为90°；而本实施例中，如图6所示，所述相变抑制传热热交换板11的表面与所述进液连通总管2及所述出液连通总管3的夹角小于90°，即所述相变抑制传热热交换板11的表面相对于所述进液连通总管2及所述出液连通总管3倾斜一定的角度。
具体的，在实施例一中，所述相变抑制传热板式热交换器的优选安装方向为所述相变抑制传热热交换板11及所述液体管道110均竖直向下与水平面垂直；所述进液连通总管2位于所述相变抑制传热热交换板11的下方，所述出液连通总管3位于所述相变抑制传热热交换板11的上方，所述进液连通总管2及所述出液连通总管3均与水平面相平行；而本实施例中，如图5及图6所示，标有g的箭头表示重力的方向，即竖直向下的方向，所述相变抑制传热板式热交换器的优选装方向为所述进液连通总管2及所述出液连通总管3均与水平面垂直，所述相变抑制传热热交换板11与水平面形成一定的夹角α，所述液体管道110与水平面平行，优选地，相变抑制传热热交换板11的表面与水平面的夹角α为3°～85°。
需要说明的是，当所述相变抑制传热板式热交换器用于散热时，即所述液体管道110内的液体温度较高，需要将所述液体管道110内液体的热量散热到空气中以冷却液体时，所述相变抑制传热热交换板11如图6所示相较于水平面向上倾斜；而当所述相变抑制传热板式热交换器用于加热时，即所述液体管道110内的液体温度较低，需要通过所述热交换器加热所述液体时，所述相变抑制传热热交换板11相较于水平面向下倾斜。
本实施例中所述相变抑制传热板式热交换器的其他结构及特点与实施例一中所述相变抑制传热板式热交换器的其他结构及特点相同，具体请参阅实施例一，这里不再累述。
实施例三
请参阅图10至图11，本发明还提供一种相变抑制传热板式热交换器，本实施例中所述相变抑制传热板式热交换器的结构与实施例一中所述的相变抑制传热板式热交换器的结构大致相同，二者的区别在于：所述液体管道110在所述相变抑制传热热交换板11表面上分布位置不同；所述相变抑制传热板式热交换器在实际应用中的安装方向不同。
具体的，在实施例一中，所述液体管道110优选地位于所述相变抑制传热热交换板11的纵向中心线上；而本实施例中，如图7所示，所述液体管道110靠近所述相变抑制传热热交换板的一边。
具体的，在实施例一中，所述相变抑制传热板式热交换器的优选安装方向为所述相变抑制传热热交换板11及所述液体管道110均竖直向下与水平面垂直；所述进液连通总管2位于所述相变抑制传热热交换板11的下方，所述出液连通总管3位于所述相变抑制传热热交换板11的上方，所述进液连通总管2及所述出液连通总管3均与水平面相平行；而本实施例中，如图10及图11所示，标有g的箭头表示重力的方向，即竖直向下的方向，所述相变抑制传热热交换板11均竖直向下与水平面垂直；所述进液连通总管2及所述出液连通总管3位于所述相变抑制传热热交换板11的两侧，且均与水平面平行；所述液体管道110与水平面平行。
需要说明的是，当所述相变抑制传热板式热交换器用于散热时，即所述液体管道110内的液体温度较高，需要将所述液体管道110内液体的热量散热到空气中以冷却液体时，所述相变抑制传热热交换板11如图10至图11所示，所述液体管道110靠近所述相变抑制传热热交换板11的下方；而当所述相变抑制传热板式热交换器用于加热时，即所述液体管道110内的液体温度较低，需要通过所述热交换器加热所述液体时，所述液体管道110应靠近所述相变抑制传热热交换板11的上方，即相当于保持重力方向不变的前提下，将图10及图11中的结构旋转180°倒置。
本实施例中所述相变抑制传热板式热交换器的其他结构及特点与实施例一中所述相变抑制传热板式热交换器的其他结构及特点相同，具体请参阅实施例一，这里不再累述。
实施例四
请参阅图12至图15，本发明还提供一种相变抑制传热板式热交换器，本实施例中所述相变抑制传热板式热交换器的结构与实施例一中所述的相变抑制传热板式热交换器的结构大致相同，二者的区别在于：所述液体管道110的形状不同；所述液体管道110在所述相变抑制传热热交换板11表面上分布位置不同；所述进液连通总管2及所述出液连通总管3的分布位置不同；所述相变抑制传热板式热交换器在实际应用中的安装方向不同。
具体的，在实施例一中，所述液体管道110的形状优选为直线形，而本实施例中，如图12及图14所示，所述液体管道110的形状为U型。
具体的，在实施例一中，所述液体管道110优选地位于所述相变抑制传热热交换板11的纵向中心线上；而本实施例中，如图12及图14所示，所述液体管道110靠近所述相变抑制传热热交换板的一边。
具体的，在实施例一中，所述进液连通总管2及所述出液连通总管3优选地分别位于所述相变抑制传热热交换板11相对的两边；而本实施例中，所述进液连通总管2及所述出液连通总管3位于所述相变抑制传热热交换板11的同一边。
具体的，在实施例一中，所述相变抑制传热板式热交换器的优选安装方向为所述相变抑制传热热交换板11及所述液体管道110均竖直向下与水平面垂直；所述进液连通总管2位于所述相变抑制传热热交换板11的下方，所述出液连通总管3位于所述相变抑制传热热交换板11的上方，所述进液连通总管2及所述出液连通总管3均与水平面相平行；而本实施例中，如图12及图13所示，标有g的箭头表示重力的方向，即竖直向下的方向，所述相变抑制传热热交换板11均竖直向下与水平面垂直；所述进液连通总管2及所述出液连通总管3位于所述相变抑制传热热交换板11的一侧，且均与水平面平行；所述液体管道110与水平面平行。
需要说明的是，当所述相变抑制传热板式热交换器用于散热时，即所述液体管道110内的液体温度较高，需要将所述液体管道110内液体的热量散热到空气中以冷却液体时，所述相变抑制传热热交换板11如图12至图13所示，所述液体管道110靠近所述相变抑制传热热交换板11的下方；而当所述相变抑制传热板式热交换器用于加热时，即所述液体管道110内的液体温度较低，需要通过所述热交换器加热所述液体时，所述液体管道110应靠近所述相变抑制传热热交换板11的上方，即相当于保持重力方向不变的前提下，将图12及图13中的结构旋转180°倒置。
本实施例中所述相变抑制传热板式热交换器的其他结构及特点与实施例一中所述相变抑制传热板式热交换器的其他结构及特点相同，具体请参阅实施例一，这里不再累述。
实施例五
请参阅图16至图17，本发明还提供一种相变抑制传热板式热交换器，本实施例中所述相变抑制传热板式热交换器的结构与实施例一中所述的相变抑制传热板式热交换器的结构大致相同，二者的区别在于：所述相变抑制传热热交换板11的结构不同；与所述封闭网络状管道108相对应的所述第一凸起结构107及与所述液体管道110相对应的所述第二凸起结构105在所述相变抑制传热热交换板11上位置不同。
具体的，实施例一中，所述相变抑制传热热交换板11包括中间板材112、第一板材111及第二板材113；所述第一板材111、所述中间板材112及所述第二板材113依次叠置，所述第一板材111及所述第二板材113分别位于所述中间板材112的两侧，并与所述中间板材112通过辊压工艺复合在一起；而本实施例中，所述相变抑制传热热交换板11包括第一板材111及第二板材113；所述第一板材111及所述第二板材113通过辊压工艺复合在一起。
具体的，实施例一中，所述第一凸起结构107及所述第二凸起结构105分别形成于所述相变抑制传热热交换板11的不同表面上，且所述封闭网络状管道108位于所述中间板材112及所述第一板材111之间，所述第一凸起结构107位于所述第一板材111上，所述液体管道 110形成于所述中间板材112及所述第二板材113之间，所述第二凸起结构105位于所述第二板材113上；而本实施例中，所述第一凸起结构107及所述第二凸起结构105形成于所述相变抑制传热热交换板11的同一表面上，且所述封闭网络状管道108及所述液体管道110位于所述第一板材111及所述第二板材113之间；所述第一凸起结构107及所述第二凸起结构105同时位于所述第一板材上111、所述第二板材113上、或所述第一板材111及所述第二板材113上。
需要说明的是，所述第一凸起结构107及所述第二凸起结构105同时位于所述第一板材上111或同时所述第二板材113上是指所述相变抑制传热热交换板11呈单面胀态，所述第一凸起结构107及所述第二凸起结构105同时位于所述第一板材111及所述第二板材113上是指所述相变抑制传热热交换板11呈双面胀态。优选地，本实施例中，所述第一凸起结构107及所述第二凸起结构105同时位于所述第一板材111及所述第二板材113上。
需要进一步说明的是，本实施例中，在实际应用中，所述相变抑制传热板式热交换器的安装方向可以根据实际需要进行设定，此处不做限定。
本实施例中所述相变抑制传热板式热交换器的其他结构及特点与实施例一中所述相变抑制传热板式热交换器的其他结构及特点相同，具体请参阅实施例一，这里不再累述。
综上所述，本发明提供一种相变抑制传热板式热交换器，在相变抑制传热板式热交换器的相变抑制传热热交换板内将封闭网络状管道及液体管道组合在一起，在封闭网络状管道内充入相变抑制工作介质，构成相变抑制传热器件，提高了相变抑制传热热交换板的均温性；利用相变抑制传热器件的导热速率快、均温性好的特点，提高了与空气的温差和有效传热面积，大大提高了相变抑制传热热交换板的散热能力和热交换效率；使得相变抑制传热板式热交换器具有均温和高效换热的特性，大大缩短液体管道的长度，减小流动阻力和能耗，以及流体的使用量，提高热交换器的效率和能效比。
上述实施例仅例示性说明本发明的原理及其功效，而非用于限制本发明。任何熟悉此技术的人士皆可在不违背本发明的精神及范畴下，对上述实施例进行修饰或改变。因此，举凡所属技术领域中具有通常知识者在未脱离本发明所揭示的精神与技术思想下所完成的一切等效修饰或改变，仍应由本发明的权利要求所涵盖。

Claims (14)

  1. 一种相变抑制传热板式热交换器，其特征在于，所述相变抑制传热板式热交换器包括：进液连通总管、出液连通总管及多块平行排布的相变抑制传热热交换板；
    所述相变抑制传热热交换板为复合板式结构，所述相变抑制传热热交换板内形成有具有一定结构形状的液体管道及具有一定结构形状的封闭网络状管道；所述封闭网络状管道内填充有相变抑制工作介质；
    所述进液连通总管及所述出液连通总管至少固定于所述相变抑制传热热交换板的一边，所述进液连通总管及所述出液连通总管的长度方向沿所述多块相变抑制传热热交换板平行排布的方向延伸，且所述进液连通总管及所述出液连通总管的内部均与所述液体管道的内部相连通。
  2. 根据权利要求1所述的相变抑制传热板式热交换器，其特征在于：所述液体管道及所述封闭网络状管道均通过吹胀工艺形成，并在所述相变抑制传热热交换板表面形成与所述封闭网络状管道相对应的第一凸起结构及与所述液体管道相对应的第二凸起结构。
  3. 根据权利要求2所述的相变抑制传热板式热交换器，其特征在于：所述第一凸起结构及所述第二凸起结构分别形成于所述相变抑制传热热交换板的不同表面上。
  4. 根据权利要求3所述的相变抑制传热板式热交换器，其特征在于，所述相变抑制传热热交换板包括中间板材、第一板材及第二板材；所述第一板材、所述中间板材及所述第二板材依次叠置，所述第一板材及所述第二板材分别位于所述中间板材的两侧，并与所述中间板材通过辊压工艺复合在一起；
    所述封闭网络状管道位于所述中间板材及所述第一板材之间，所述第一凸起结构位于所述第一板材上；
    所述液体管道形成于所述中间板材及所述第二板材之间，所述第二凸起结构位于所述第二板材上。
  5. 根据权利要求3所述的相变抑制传热板式热交换器，其特征在于：所述进液连通总管及所述出液连通总管分别位于所述相变抑制传热热交换板相对的两边；所述液体管道的形状为直线形。
  6. 根据权利要求5所述的相变抑制传热板式热交换器，其特征在于：所述液体管道位于所述相变抑制传热热交换板的纵向中心线上。
  7. 根据权利要求5所述的相变抑制传热板式热交换器，其特征在于：所述液体管道靠近所述相变抑制传热热交换板的一边。
  8. 根据权利要求3所述的相变抑制传热板式热交换器，其特征在于：所述进液连通总管及所述出液连通总管位于所述相变抑制传热热交换板的同一边；所述液体管道的形状为U型。
  9. 根据权利要求2所述的相变抑制传热板式热交换器，其特征在于：所述第一凸起结构及所述第二凸起结构形成于所述相变抑制传热热交换板的同一表面上。
  10. 根据权利要求9所述的相变抑制传热板式热交换器，其特征在于：所述相变抑制传热热交换板的两表面上均形成有所述第一凸起结构及所述第二凸起结构。
  11. 根据权利要求9所述的相变抑制传热板式热交换器，其特征在于，所述相变抑制传热热交换板包括第一板材及第二板材；所述第一板材及所述第二板材通过辊压工艺复合在一起；
    所述封闭网络状管道及所述液体管道位于所述第一板材及所述第二板材之间；所述第一凸起结构及所述第二凸起结构同时位于所述第一板材上、所述第二板材上、或所述第一板材及所述第二板材上。
  12. 根据权利要求9所述的相变抑制传热板式热交换器，其特征在于：所述进液连通总管及所述出液连通总管分别位于所述相变抑制传热热交换板的两端；所述液体管道的形状为直线形，且所述液体管道靠近所述相变抑制传热热交换板的一边。
  13. 根据权利要求1所述的相变抑制传热板式热交换器，其特征在于：所述进液连通总管及所述出液连通总管的一端封闭，另一端与液体系统相连接。
  14. 根据权利要求1至13任一项中所述的相变抑制传热板式热交换器，其特征在于：所述相变抑制传热热交换板的表面与所述进液连通总管及所述出液连通总管相垂直或相对于所述进液连通总管及所述出液连通总管倾斜一定的角度。
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CN105004206B (zh) 2015-08-06 2018-10-16 浙江嘉熙科技有限公司 相变抑制传热板式热交换器
CN105486128A (zh) * 2015-12-31 2016-04-13 浙江嘉熙科技有限公司 一体化单面平相变抑制传热板式热交换器及其制造方法
CN105466262A (zh) * 2015-12-31 2016-04-06 浙江嘉熙科技有限公司 一体化相变抑制传热换热板结构及其制造方法
CN105486132A (zh) * 2015-12-31 2016-04-13 浙江嘉熙科技有限公司 双面平相变抑制传热板结构及其制造方法
CN106052206A (zh) * 2016-05-25 2016-10-26 合肥华凌股份有限公司 换热器、制冷设备和换热器的制造方法
CN107782184A (zh) * 2016-08-31 2018-03-09 浙江嘉熙科技有限公司 相变抑制传热板及其制造方法
CN108075083A (zh) * 2018-01-12 2018-05-25 无锡巨日电子科技有限公司 可加热和散热的动力电池组件
CN111366018B (zh) * 2018-12-25 2024-04-12 青岛海尔特种电冰柜有限公司 半导体制冷用散热组件及半导体制冷设备
CN109561640A (zh) * 2019-01-14 2019-04-02 常州常发制冷科技有限公司 多层复合翅片式均温板及加工方法
CN110145950A (zh) * 2019-06-14 2019-08-20 深圳市三和川精密科技有限公司 一种热交换器
CN112964085B (zh) * 2021-02-02 2022-05-03 杭州祥博传热科技股份有限公司 一种自适应相变冷板
CN113446880A (zh) * 2021-06-22 2021-09-28 深圳市飞荣达科技股份有限公司 平板式热管换热器

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5520244A (en) * 1992-12-16 1996-05-28 Sdl, Inc. Micropost waste heat removal system
CN202102836U (zh) * 2011-06-08 2012-01-04 上海东润换热设备制造有限公司 一种变压器板翅式换热器
CN103822515A (zh) * 2014-03-10 2014-05-28 吴鸿平 插管式流体换热器及其制造方法
CN105004206A (zh) * 2015-08-06 2015-10-28 浙江嘉熙光电设备制造有限公司 相变抑制传热板式热交换器
CN204944261U (zh) * 2015-08-06 2016-01-06 浙江嘉熙光电设备制造有限公司 相变抑制传热板式热交换器

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1598441A (zh) * 2004-07-27 2005-03-23 周晖 铝—铝直接结合式铜铝复合集热板芯
JP5444782B2 (ja) * 2008-09-12 2014-03-19 株式会社デンソー 蓄冷熱交換器
CN102042775A (zh) * 2009-10-16 2011-05-04 海鸥能源(马)有限公司 无相变传热装置及其制作方法
JP5862507B2 (ja) * 2012-08-07 2016-02-16 株式会社デンソー 蓄冷熱交換器
CN203224157U (zh) * 2013-02-27 2013-10-02 浙江嘉熙光电设备制造有限公司 一体化薄板型高效传热—散热器件
CN104308366A (zh) * 2014-10-21 2015-01-28 兰州陇星沃尔凯采暖设备制造集团有限公司 非相变抑制传热基板槽道口的封闭工艺
CN204187722U (zh) * 2014-10-21 2015-03-04 兰州陇星沃尔凯采暖设备制造集团有限公司 基于新传热技术的采暖散热器

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5520244A (en) * 1992-12-16 1996-05-28 Sdl, Inc. Micropost waste heat removal system
CN202102836U (zh) * 2011-06-08 2012-01-04 上海东润换热设备制造有限公司 一种变压器板翅式换热器
CN103822515A (zh) * 2014-03-10 2014-05-28 吴鸿平 插管式流体换热器及其制造方法
CN105004206A (zh) * 2015-08-06 2015-10-28 浙江嘉熙光电设备制造有限公司 相变抑制传热板式热交换器
CN204944261U (zh) * 2015-08-06 2016-01-06 浙江嘉熙光电设备制造有限公司 相变抑制传热板式热交换器

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