JP2014074581A - Heat exchanger - Google Patents

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JP2014074581A
JP2014074581A JP2013200948A JP2013200948A JP2014074581A JP 2014074581 A JP2014074581 A JP 2014074581A JP 2013200948 A JP2013200948 A JP 2013200948A JP 2013200948 A JP2013200948 A JP 2013200948A JP 2014074581 A JP2014074581 A JP 2014074581A
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tube
flow
thermal energy
fluid
heat exchanger
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JP6401439B2 (en
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Tai-Her Yang
泰和 楊
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    • 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
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0066—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids
    • F28D7/0083—Multi-circuit heat-exchangers, e.g. integrating different heat exchange sections in the same unit or heat-exchangers for more than two fluids with units having particular arrangement relative to a supplementary heat exchange medium, e.g. with interleaved units or with adjacent units arranged in common flow of supplementary heat exchange medium
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00—Tubular elements; Assemblies of tubular elements
    • F28F1/003—Multiple wall conduits, e.g. for leak detection
    • 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
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • F28D7/106—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically consisting of two coaxial conduits or modules of two coaxial conduits
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00—Tubular elements; Assemblies of tubular elements
    • F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely

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

Abstract

PROBLEM TO BE SOLVED: To provide a heat exchange body in a first flow channel and to provide a heat exchanger for exchanging heat energy between the heat exchange body in the first flow channel and an external heat exchange body.SOLUTION: A first flow guide pipe body (101) is composed of a thermal conductor and includes at least one first flow channel (102) in its inside, both ends of the at least one first flow channel (102) are connected to two first joining rooms (103), and first fluid gateways (104) are respectively formed in the two first joining rooms (103). A second flow guide pipe body (201) is composed of a thermal conductor, formed so as to cover the outside of the first flow channel (102) of the first flow guide pipe body (101) and includes at least one second flow channel (202) having an annular cross section formed so as to cover the first flow channel (102), both ends of the at least one second flow channel (202) are connected to two second joining rooms (203), and second fluid gateways (204) are respectively formed in the two second joining rooms (203).

Description

本発明は、熱交換器に関し、詳しくは、多層管及び管路の重ね合わせにより三つの熱エネルギー体の間で熱交換を行う熱交換器に関する。   The present invention relates to a heat exchanger, and more particularly, to a heat exchanger that performs heat exchange between three thermal energy bodies by overlapping a multilayer pipe and a pipe line.

従来の熱交換器は、管路内を流れる流体と、管路外を流れる流体もしくは管路外と接触する固体または流体との間で熱交換を行い、二種類の熱交換体の間で熱交換を行う。   Conventional heat exchangers exchange heat between a fluid flowing in a pipe and a fluid flowing outside the pipe or a solid or fluid in contact with the outside of the pipe, and heat is exchanged between two types of heat exchangers. Exchange.

特開２００３−３０１４３４号公報JP 2003-301434 A

本発明は、二重の管構造を有し、直径が比較的小さい管体の内部に形成されている第１流路、および、直径が比較的小さい管体の外壁と直径が比較的大きい管体の内壁との間に形成されている第２流路を有し、固体、液体、又は、気体である熱交換体の中に位置することにより、第１流路内の熱交換体と第１流路内の熱交換体と外部の熱交換体との間で熱エネルギの交換を行う熱交換器を提供することを目的とする。   The present invention relates to a first flow path having a double tube structure and formed inside a tube having a relatively small diameter, and an outer wall of the tube having a relatively small diameter and a tube having a relatively large diameter. A second flow path formed between the inner wall of the body and the second flow path located in the heat exchange body that is solid, liquid, or gas; An object of the present invention is to provide a heat exchanger that exchanges heat energy between a heat exchanger in one flow path and an external heat exchanger.

本発明による熱交換器は、第１導流管体（１０１）、および、第２導流管体（２０１）を備える。第１導流管体（１０１）は、熱伝導体により構成され、内部に少なくとも一つの第１流路（１０２）を有し、少なくとも一つの前記第１流路（１０２）の両端が二つの第１合流室（１０３）に接続されており、二つの第１合流室（１０３）にそれぞれ第１流体出入口（１０４）が形成されており、二つの第１流体出入口（１０４）が流体である第１熱エネルギ体（１０５）の流入または流出に用いられる。第２導流管体（２０１）は、熱伝導体により構成され、第１導流管体（１０１）の第１流路（１０２）の外部を覆うよう形成されており、第１流路（１０２）を覆うように形成されている環状断面を有する第２流路（２０２）を少なくとも一つ有し、少なくとも一つの第２流路（２０２）の両端が二つの第２合流室（２０３）に接続されており、二つの第２合流室（２０３）にそれぞれ第２流体出入口（２０４）が形成されており、第２流体出入口（２０４）が流体である第２熱エネルギ体（２０５）の流入または流出に用いられる。第１導流管体（１０１）の第１流路（１０２）の外部に第１流路（１０２）の外径より大きい管体内径を有する第２流路（２０２）を有する第２導流管体（２０１）を嵌め込むことで、二層構造の管体を構成する。   The heat exchanger according to the present invention includes a first diversion tube (101) and a second diversion tube (201). The first flow guiding body (101) is formed of a heat conductor, has at least one first flow path (102) inside, and at least one of the first flow paths (102) has two ends. Connected to the first merge chamber (103), the first fluid inlet / outlet (104) is formed in each of the two first merge chambers (103), and the two first fluid inlet / outlets (104) are fluids. Used for inflow or outflow of the first thermal energy body (105). The second diversion tube (201) is made of a heat conductor and is formed so as to cover the outside of the first flow path (102) of the first diversion tube (101). 102) has at least one second flow path (202) having an annular cross section formed so as to cover, and at least one second flow path (202) has two second joining chambers (203). The second fluid inlet / outlet (204) is formed in each of the two second merge chambers (203), and the second fluid inlet / outlet (204) is a fluid of the second thermal energy body (205). Used for inflow or outflow. A second current flow having a second flow path (202) having a tube inner diameter larger than the outer diameter of the first flow path (102) outside the first flow path (102) of the first flow guiding body (101). By fitting the tubular body (201), a tubular body having a two-layer structure is formed.

第２導流管体（２０１）の外層は、気相、液相、又は固相の熱エネルギ体により構成される第３熱エネルギ体（３０５）と接触しており、三層の環状の構造を形成することで、第２熱エネルギ体（２０５）と第１熱エネルギ体（１０５）と第３熱エネルギ体（３０５）との三者の間で熱エネルギの交換を行う。第２流路（２０２）の外部と接触する熱エネルギ体は、地層、地表土壌、海、川、湖、池、流動流体、大気、流動気体により構成される自然熱エネルギ体である。   The outer layer of the second flow guiding body (201) is in contact with the third thermal energy body (305) composed of a thermal energy body in a gas phase, a liquid phase, or a solid phase, and has a three-layer annular structure. Thus, the heat energy is exchanged between the second thermal energy body (205), the first thermal energy body (105), and the third thermal energy body (305). The thermal energy body that comes into contact with the outside of the second flow path (202) is a natural thermal energy body composed of a stratum, surface soil, sea, river, lake, pond, fluid fluid, air, and fluid gas.

本発明の第一実施形態による熱交換器を示す模式図である。It is a mimetic diagram showing the heat exchanger by a first embodiment of the present invention. 本発明の第一実施形態による熱交換器の側面を示す模式図である。It is a mimetic diagram showing the side of the heat exchanger by a first embodiment of the present invention. 本発明の第二実施形態による熱交換器を示す模式図を示す。The schematic diagram which shows the heat exchanger by 2nd embodiment of this invention is shown. 本発明の第二実施形態による熱交換器の側面を示す模式図である。It is a schematic diagram which shows the side surface of the heat exchanger by 2nd embodiment of this invention. 本発明の第三実施形態による熱交換器を示す模式図である。It is a schematic diagram which shows the heat exchanger by 3rd embodiment of this invention. 本発明の第三実施形態による熱交換器の側面を示す模式図である。It is a schematic diagram which shows the side surface of the heat exchanger by 3rd embodiment of this invention. 本発明の第四実施形態による熱交換器を示す模式図である。It is a schematic diagram which shows the heat exchanger by 4th embodiment of this invention. 本発明の第四実施形態による熱交換器の側面を示す模式図である。It is a schematic diagram which shows the side surface of the heat exchanger by 4th embodiment of this invention. 本発明の第五実施形態による熱交換器を示す模式図である。It is a schematic diagram which shows the heat exchanger by 5th embodiment of this invention. 本発明の第五実施形態による熱交換器の側面を示す模式図である。It is a schematic diagram which shows the side surface of the heat exchanger by 5th embodiment of this invention. 本発明の第六実施形態による熱交換器を示す模式図である。It is a schematic diagram which shows the heat exchanger by 6th embodiment of this invention. 本発明の第六実施形態による熱交換器の側面を示す模式図である。It is a schematic diagram which shows the side surface of the heat exchanger by 6th embodiment of this invention. 本発明の第七実施形態による熱交換器を示す模式図である。It is a schematic diagram which shows the heat exchanger by 7th embodiment of this invention. 本発明の第七実施形態による熱交換器の側面を示す模式図である。It is a schematic diagram which shows the side surface of the heat exchanger by 7th embodiment of this invention.

（第一実施形態）
本発明の実施形態による熱交換器は、多重の管構造を有し、外層の管路が内層の管路を覆うことにより、外層の管路内の流体と内層の管路内の流体とが熱交換可能である。また、熱交換器は、固体又は流体である熱エネルギ体の中に位置し、外層の管路内の流体と熱エネルギ体とが熱交換を行い、三種類の熱交換体の間で熱交換を行う。
主な構成を以下のように説明する。
図１は、本発明の第一実施形態による熱交換器の模式図である。
図２は、図１に示す実施形態の側面を示す模式図である。 (First embodiment)
The heat exchanger according to the embodiment of the present invention has a multiple pipe structure, and the outer layer pipe line covers the inner layer pipe line, so that the fluid in the outer layer pipe line and the fluid in the inner layer pipe line are connected. Heat exchange is possible. In addition, the heat exchanger is located in a solid or fluid thermal energy body, and the fluid in the outer pipe line and the thermal energy body exchange heat to exchange heat between the three types of heat exchangers. I do.
The main configuration will be described as follows.
FIG. 1 is a schematic diagram of a heat exchanger according to a first embodiment of the present invention.
FIG. 2 is a schematic diagram showing a side surface of the embodiment shown in FIG.

図１と図２に示すように、熱交換器は、複数の流路を有する第１導流管体（１０１）を備える。第１導流管体（１０１）は熱伝導体により構成される。第１導流管体（１０１）の管穴により第１流路（１０２）を構成する。第１流路（１０２）の両端は別々に第１合流室（１０３）を経てから、更に第１流体出入口（１０４）を経て、流体である第１熱エネルギ体（１０５）が流れ込んだり、流れ出したりする。第１導流管体（１０１）の外部に第１流路（１０２）の外径より大きい複数の流路を有する第２導流管体（２０１）が形成されている。第２導流管体（２０１）が第１導流管体（１０１）の外部に嵌め込まれていることで二層構造を有する管体を構成する。第２導流管体（２０１）は熱伝導体により構成される。また第２導流管体（２０１）の内径と第１流路（１０２）の外径との管径差により環状断面を有する第２流路（２０２）を構成する。第２流路（２０２）の両端は別々に第２合流室（２０３）を経てから、更に第２流体出入口（２０４）を経て、流体である第２熱エネルギ体（２０５）が流れ込んだり、流れ出したりする。その中の第２導流管体（２０１）の外層は、気体、液体、又は固体の熱エネルギ体により構成される第３熱エネルギ体（３０５）と接触している。これにより、更に三層環状であるトライピースの熱エネルギ体熱交換器を構成することにより、第２熱エネルギ体（２０５）と第１熱エネルギ体（１０５）と第３熱エネルギ体（３０５）との三者の間熱エネルギの交換を行う。
第１導流管体（１０１）、第２導流管体（２０１）は、複数の流路により構成されることができる。
第１導流管体（１０１）、第２導流管体（２０１）は、円形、四角形、橢円形又は他の幾何形状の管体により構成されることができる。
第１導流管体（１０１）、第２導流管体（２０１）は、同じ形又は異なる形の管体により構成されることができる。 As shown in FIGS. 1 and 2, the heat exchanger includes a first diversion tube (101) having a plurality of flow paths. The first flow guiding body (101) is composed of a heat conductor. A first flow path (102) is constituted by a tube hole of the first flow guiding tube (101). Both ends of the first flow path (102) separately pass through the first merge chamber (103), and further through the first fluid inlet / outlet (104), the first thermal energy body (105) as a fluid flows in and out. Or A second diversion tube (201) having a plurality of channels larger than the outer diameter of the first channel (102) is formed outside the first diversion tube (101). A pipe body having a two-layer structure is configured by fitting the second diversion tube body (201) outside the first diversion tube body (101). The second flow guiding tube (201) is composed of a heat conductor. Moreover, the 2nd flow path (202) which has an annular cross section is comprised by the pipe diameter difference of the internal diameter of a 2nd flow conduit (201), and the outer diameter of a 1st flow path (102). The two ends of the second flow path (202) separately pass through the second merge chamber (203), and further through the second fluid inlet / outlet (204), the second thermal energy body (205) as a fluid flows in and out. Or The outer layer of the second flow guiding body (201) therein is in contact with the third thermal energy body (305) constituted by a thermal energy body of gas, liquid, or solid. Thus, by forming a heat energy body heat exchanger of a tri-piece having a three-layered annular shape, the second thermal energy body (205), the first thermal energy body (105), and the third thermal energy body (305). The heat energy is exchanged between the three parties.
The first diversion tube (101) and the second diversion tube (201) can be constituted by a plurality of flow paths.
The first diversion tube (101) and the second diversion tube (201) may be formed of circular, quadrangular, oval or other geometric shapes.
The first flow guiding body (101) and the second flow guiding tube (201) can be configured by the same shape or different shapes.

第１熱エネルギ体（１０５）、第２熱エネルギ体（２０５）は、同じ又は異なる流体により構成され、気体、液体、気体から液体に変換可能な流体、又は、液体から気体に変換可能な流体により構成される。   The first thermal energy body (105) and the second thermal energy body (205) are composed of the same or different fluids, and are gas, liquid, fluid that can be converted from gas to liquid, or fluid that can be converted from liquid to gas. Consists of.

第１導流管体（１０１）の中で流動する第１熱エネルギ体（１０５）及び第２導流管体（２０１）の中で流動する第２熱エネルギ体（２０５）の流れは、同じ又は逆である。   The flow of the first thermal energy body (105) flowing in the first conduction pipe body (101) and the second thermal energy body (205) flowing in the second conduction pipe body (201) are the same. Or vice versa.

（第二実施形態）
本実形態では、熱交換器の第３熱エネルギ体（３０５）が気体又は液体の流体により構成されるとき、流体ポンプ（４００）を加設することで、第３熱エネルギ体（３０５）をポンピングすることにより、熱交換効果を向上する。
図３は、第３熱エネルギ体が流体であり、流体ポンピング装置を設置する実施形態を示す模式図である。
図４は、図３の実施形態の側面を示す模式図である。
図３と図４は、流体ポンプ（４００）を加設することで、第３熱エネルギ体（３０５）をポンピングすることにより、熱交換効果を向上することを示す。 (Second embodiment)
In this embodiment, when the third heat energy body (305) of the heat exchanger is composed of a gas or liquid fluid, the third heat energy body (305) is added by adding a fluid pump (400). The heat exchange effect is improved by pumping.
FIG. 3 is a schematic diagram showing an embodiment in which the third thermal energy body is a fluid and a fluid pumping device is installed.
FIG. 4 is a schematic diagram showing a side view of the embodiment of FIG.
3 and 4 show that the heat exchange effect is improved by pumping the third thermal energy body (305) by adding the fluid pump (400).

（第三実施形態）
図５は、導熱フィン（１０００）を加設する第三実施形態による熱交換器を示す模式図である。
図６は図５に示す実施形態の側面を示す模式図である。 (Third embodiment)
FIG. 5 is a schematic view showing a heat exchanger according to the third embodiment in which a heat conducting fin (1000) is added.
FIG. 6 is a schematic view showing a side surface of the embodiment shown in FIG.

図５と図６は、第２導流管体（２０１）の間に、導熱フィン（１０００）を設置することにより、第２導流管体（２０１）と第３熱エネルギ体（３０５）との間で熱エネルギを伝送することを示す。   5 and FIG. 6, the heat conduction fin (1000) is installed between the second heat conduction tube (201), so that the second heat conduction tube (201), the third heat energy body (305), and Shows the transfer of thermal energy between the two.

（第四実施形態）
本実施形態の熱交換器の第１導流管体（１０１）及び第２導流管体（２０１）は、第１導流管体（１０１）同士及び第２導流管体（２０１）同士が直列に接続されている。 (Fourth embodiment)
In the heat exchanger according to the present embodiment, the first and second current-carrying pipes (101) and (201) are the first current-flow pipe bodies (101) and the second current-flow pipe bodies (201). Are connected in series.

図７は、第１導流管体（１０１）の複数の第１導流管体（１０１）が直列に接続されており、第１導流管体（１０１）外部を覆う第２導流管体（２０１）の第２導流管体（２０１）が直列に接続されている模式図を示す。
図８は図７の実施形態の側面を示す模式図である。 FIG. 7 shows a second current guide tube in which a plurality of first current flow tubes (101) of the first current flow tube (101) are connected in series, and covers the outside of the first current flow tube (101). The schematic diagram by which the 2nd diversion tube body (201) of a body (201) is connected in series is shown.
FIG. 8 is a schematic view showing a side surface of the embodiment of FIG.

図７と図８に示すように、第１導流管体（１０１）は熱伝導体により構成され、複数の第１流路（１０２）が第１合流室（１０３）を経て、直列に接続されている。直列接続されている第１流路（１０２）の両端は別々に第１流体出入口（１０４）に接続されている。第１流体出入口（１０４）には、流体である第１熱エネルギ体（１０５）が流れ込んだり、流れ出したりする。管体内径が第１導流管体（１０１）の外径により大きい第２導流管体（２０１）が第１導流管体（１０１）の外部に嵌め込まれることにより、二層構造管体を構成する。第２導流管体（２０１）は熱伝導体により構成され、第２導流管体（２０１）の比較的大きい内径と第１導流管体（１０１）の外径との管径差により形成されている環状断面の第２流路（２０２）を有する。複数の第２流路（２０２）は、第２合流室（２０３）を介して直列に接続されている。直列に接続された第２流路（２０２）の両端は別々に第２流体出入口（２０４）に接続されている。これにより、流体である第２熱エネルギ体（２０５）が流れ込んだり、流れ出したりする。第２導流管体（２０１）の外層は、気体や液体の流体、又は固体の熱エネルギ体により構成される第３熱エネルギ体（３０５）と接触している。これにより三層環状である三種の熱エネルギ体を有する熱交換器が構成され、第２熱エネルギ体（２０５）と第１熱エネルギ体（１０５）と第３熱エネルギ体（３０５）との三者の間で熱エネルギの交換を行う。   As shown in FIG. 7 and FIG. 8, the first diversion tube (101) is constituted by a heat conductor, and a plurality of first flow paths (102) are connected in series via the first merge chamber (103). Has been. Both ends of the first flow path (102) connected in series are separately connected to the first fluid inlet / outlet (104). The first thermal energy body (105), which is a fluid, flows into or out of the first fluid inlet / outlet (104). A second flow guiding tube (201) whose inner diameter is larger than the outer diameter of the first flow guiding tube (101) is fitted to the outside of the first flow guiding tube (101), whereby a two-layer structure tube Configure. The second diversion tube (201) is composed of a heat conductor, and is due to a difference in tube diameter between the relatively large inner diameter of the second diversion tube (201) and the outer diameter of the first diversion tube (101). It has the 2nd flow path (202) of the cyclic | annular cross section currently formed. The plurality of second flow paths (202) are connected in series via the second merge chamber (203). Both ends of the second flow path (202) connected in series are separately connected to the second fluid inlet / outlet (204). Thereby, the 2nd thermal energy body (205) which is a fluid flows in and flows out. The outer layer of the second flow guiding body (201) is in contact with a third thermal energy body (305) configured by a gas or liquid fluid, or a solid thermal energy body. As a result, a heat exchanger having three types of thermal energy bodies having a three-layer annular shape is formed, and the third thermal energy body (205), the first thermal energy body (105), and the third thermal energy body (305). The heat energy is exchanged between the persons.

（第五実施形態）
図９は、図５、図６の第１導流管体（１０１）の第１流路（１０２）が直列に接続されており、第１導流管体（１０１）の外部を覆う第２導流管体（２０１）の第２流路（２０２）が直列に接続されている実施形態を示す模式図である。 図１０は図９の実施形態の側面を示す模式図である。 (Fifth embodiment)
In FIG. 9, the first flow path (102) of the first flow guide tube (101) of FIGS. 5 and 6 is connected in series, and the second flow path covers the outside of the first flow guide tube (101). It is a schematic diagram which shows embodiment which the 2nd flow path (202) of a flow guide tube (201) is connected in series. FIG. 10 is a schematic view showing a side surface of the embodiment of FIG.

図９と図１０にしめすように、第１導流管体（１０１）の複数の第１流路（１０２）同士、及び、第１導流管体（１０１）の外部を覆う第２導流管体（２０１）の複数の第２流路（２０２）同士は直列に接続されている。   As shown in FIG. 9 and FIG. 10, the second current covering the plurality of first flow paths (102) of the first current guiding tube (101) and the outside of the first current guiding tube (101). The plurality of second flow paths (202) of the pipe body (201) are connected in series.

（第六実施形態）
本実施形態では、第１導流管体（１０１）外部と第２導流管体（２０１）の内部との間に形成されている螺旋状の導流板（２２２）、及び、第１導流管体（１０１）の内部に形成されている螺旋状の導流板（１１１）をさらに備え、伝熱効果を高める。 (Sixth embodiment)
In the present embodiment, the spiral current guide plate (222) formed between the outside of the first current guide tube (101) and the inside of the second current guide tube (201), and the first guide A spiral flow guide plate (111) formed inside the flow tube body (101) is further provided to enhance the heat transfer effect.

図１１に示すように、第１導流管体（１０１）外部と第２導流管体（２０１）内部との間に形成されている螺旋状の導流板（２２２）、及び、第１導流管体（１０１）の内部に形成されている螺旋状の導流板（１１１）は、同じ螺旋の巻き方を有する。
図１２は図１１の実施形態の側面を示す模式図である。 As shown in FIG. 11, the spiral current guide plate (222) formed between the outside of the first current guide tube (101) and the inside of the second current guide tube (201), and the first The spiral flow guide plate (111) formed inside the flow guide tube (101) has the same spiral winding method.
FIG. 12 is a schematic view showing a side surface of the embodiment of FIG.

図１１と図１２に示すように、本実施形態の熱交換器は、第１導流管体（１０１）の外部と第２導流管体（２０１）の内部との間に形成されている螺旋状の導流板（２２２）、及び、第１導流管体（１０１）の内部に形成されている螺旋状の導流板（１１１）とは同じ螺旋の巻き方を有する。   As shown in FIGS. 11 and 12, the heat exchanger of the present embodiment is formed between the outside of the first diversion tube (101) and the inside of the second diversion tube (201). The spiral flow guide plate (222) and the spiral flow guide plate (111) formed inside the first flow guide tube (101) have the same spiral winding method.

（第七実施形態）
図１３は、第１導流管体（１０１）の外部と第２導流管体（２０１）の内部との間に形成されている螺旋状の導流板（２２２）、及び、第１導流管体（１０１）の内部に形成されている螺旋状の導流板（１１１）が、異なる螺旋の巻き方を有する実施形態を示す模式図である。
図１４は図１３の実施形態の断面を示す模式図である。 (Seventh embodiment)
FIG. 13 shows a spiral current guide plate (222) formed between the outside of the first current guide tube (101) and the inside of the second current guide tube (201), and the first guide It is a schematic diagram which shows embodiment which the spiral flow guide plate (111) formed in the inside of a flow tube body (101) has a different spiral winding method.
FIG. 14 is a schematic view showing a cross section of the embodiment of FIG.

図１３と図１４に示すように、本実施形態では、第１導流管体（１０１）の外部と第２導流管体（２０１）の内部との間に形成されている螺旋状の導流板（２２２）、及び、第１導流管体（１０１）の内部に形成されている螺旋状の導流板（１１１）は、異なる螺旋の巻き方を有する。   As shown in FIGS. 13 and 14, in the present embodiment, the spiral guide formed between the outside of the first conduit tube (101) and the interior of the second conduit tube (201). The flow plate (222) and the spiral flow guide plate (111) formed inside the first flow guide tube (101) have different spiral winding methods.

１０１：第１導流管体、
１０２：第１流路、
１０３：第１合流室、
１０４：第１流体出入口、
１０５：第１熱エネルギ体、
１１１、２２２：螺旋状の導流板、
２０１：第２導流管体、
２０２：第２流路、
２０３：第２合流室、
２０４：第２流体出入口、
２０５：第２熱エネルギ体、
３０５：第３熱エネルギ体、
４００：流体ポンプ、
１０００：導熱フィン。 101: the first flow guiding tube,
102: 1st flow path,
103: 1st merge room,
104: first fluid inlet / outlet;
105: first thermal energy body,
111, 222: Spiral flow guide plate,
201: second diversion tube,
202: second flow path,
203: 2nd merge room,
204: Second fluid inlet / outlet;
205: second thermal energy body,
305: third thermal energy body,
400: fluid pump,
1000: Heat conducting fin.

Claims (14)

第１導流管体（１０１）、および、第２導流管体（２０１）を備え、
前記第１導流管体（１０１）は、熱伝導体により構成され、内部に少なくとも一つの第１流路（１０２）を有し、少なくとも一つの前記第１流路（１０２）の両端が二つの第１合流室（１０３）に接続されており、二つの前記第１合流室（１０３）にそれぞれ第１流体出入口（１０４）が形成されており、二つの前記第１流体出入口（１０４）が流体である第１熱エネルギ体（１０５）の流入または流出に用いられ、
前記第２導流管体（２０１）は、熱伝導体により構成され、前記第１導流管体（１０１）の前記第１流路（１０２）の外部を覆うよう形成されており、前記第１流路（１０２）を覆うように形成されている環状断面を有する第２流路（２０２）を少なくとも一つ有し、少なくとも一つの前記第２流路（２０２）の両端が二つの第２合流室（２０３）に接続されており、二つの前記第２合流室（２０３）にそれぞれ第２流体出入口（２０４）が形成されており、前記第２流体出入口（２０４）が流体である第２熱エネルギ体（２０５）の流入または流出に用いられ、
前記第１導流管体（１０１）の前記第１流路（１０２）の外部に前記第１流路（１０２）の外径より大きい管体内径を有する前記第２流路（２０２）を有する前記第２導流管体（２０１）を嵌め込むことで、二層構造の管体を構成し、
前記第２導流管体（２０１）の外層は、気相、液相、又は固相の熱エネルギ体により構成される第３熱エネルギ体（３０５）と接触しており、三層の環状の構造を形成することで、前記第２熱エネルギ体（２０５）と前記第１熱エネルギ体（１０５）と前記第３熱エネルギ体（３０５）との三者の間で熱エネルギの交換を行うことを特徴とする熱交換器。 A first diversion tube (101) and a second diversion tube (201),
The first flow conduit body (101) is made of a heat conductor, has at least one first flow path (102) inside, and at least one end of the first flow path (102) has two ends. The first fluid inlet / outlet (104) is formed in each of the two first junction chambers (103), and the two first fluid inlets / outlets (104) are connected to the first junction chamber (103). Used for inflow or outflow of the first thermal energy body (105) which is a fluid;
The second diversion tube (201) is made of a heat conductor and is formed to cover the outside of the first flow path (102) of the first diversion tube (101). There is at least one second flow path (202) having an annular cross section formed to cover one flow path (102), and at least one second flow path (202) has two second ends. The second fluid inlet / outlet (204) is formed in each of the two second junction chambers (203), and the second fluid inlet / outlet (204) is a second fluid. Used for inflow or outflow of thermal energy body (205),
The second flow path (202) having a tube inner diameter larger than the outer diameter of the first flow path (102) outside the first flow path (102) of the first flow guiding body (101). By fitting the second flow guide tube (201), a two-layer structure tube is formed,
The outer layer of the second flow guiding body (201) is in contact with a third thermal energy body (305) composed of a thermal energy body in a gas phase, a liquid phase, or a solid phase, and has a three-layer annular shape. By forming a structure, heat energy is exchanged between the second thermal energy body (205), the first thermal energy body (105), and the third thermal energy body (305). A heat exchanger characterized by 前記第１導流管体（１０１）は熱伝導体により構成され、
少なくとも一つの前記第１流路（１０２）は、前記第１合流室（１０３）を経由して、直列に接続されており、直列に接続されている前記第１流路（１０２）の両端に前記第１流体出入口（１０４）が形成されており、
前記第１流体出入口（１０４）は、流体である前記第１熱エネルギ体（１０５）の流入または流出に用いられ、
前記第１導流管体（１０１）の前記第１流路（１０２）の外部に前記第１流路（１０２）の外径より大きい管体内径を有する前記第２流路（２０２）を有する前記第２導流管体（２０１）を嵌め込むことで、二層構造管体を構成し、
前記第２導流管体（２０１）は、熱伝導体により構成され、
少なくとも一つの前記第２流路（２０２）は、前記第２流路（２０２）の内径と前記第１流路（１０２）の外径との管径差により環状断面を有し、前記第２合流室（２０３）を経由して直列に接続されており、直列に接続されている少なくとも一つの前記第２流路（２０２）の両端に前記第２流体出入口（２０４）が形成されており、
前記第２流体出入口（２０４）は、流体である前記第２熱エネルギ体（２０５）の流入または流出に用いられ、
前記第２導流管体（２０１）の外層は、気相または液相の流体、もしくは固相の熱エネルギ体により構成される前記第３熱エネルギ体（３０５）と接触しており、三層の環状構造を構成することにより、前記第２熱エネルギ体（２０５）と前記第１熱エネルギ体（１０５）と前記第３熱エネルギ体（３０５）との三者の間で熱エネルギの交換を行うことを特徴とする請求項１に記載の熱交換器。 The first flow guiding body (101) is constituted by a heat conductor,
At least one of the first flow paths (102) is connected in series via the first merge chamber (103), and is connected to both ends of the first flow paths (102) connected in series. The first fluid inlet / outlet (104) is formed;
The first fluid inlet / outlet (104) is used for inflow or outflow of the first thermal energy body (105), which is a fluid,
The second flow path (202) having a tube inner diameter larger than the outer diameter of the first flow path (102) outside the first flow path (102) of the first flow guiding body (101). By fitting the second flow guiding tube (201), a two-layer structure tube is formed,
The second flow guiding tube (201) is constituted by a heat conductor,
At least one of the second flow paths (202) has an annular cross section due to a pipe diameter difference between an inner diameter of the second flow path (202) and an outer diameter of the first flow path (102). The second fluid inlet / outlet (204) is formed at both ends of at least one of the second flow paths (202) connected in series via the junction chamber (203),
The second fluid inlet / outlet (204) is used for inflow or outflow of the second thermal energy body (205), which is a fluid,
The outer layer of the second flow guiding body (201) is in contact with the third thermal energy body (305) composed of a gas phase or liquid phase fluid, or a solid phase thermal energy body, and has three layers. Therefore, the heat energy can be exchanged between the second thermal energy body (205), the first thermal energy body (105), and the third thermal energy body (305). The heat exchanger according to claim 1, wherein the heat exchanger is performed. 前記第１導流管体（１０１）および第２導流管体（２０１）は、円形、四角形、または、橢円形の管体により構成されていることを特徴とする請求項１または２に記載の熱交換器。   The said 1st current conducting tube (101) and the 2nd current conducting tube (201) are comprised by the circular, square, or a round-circular tube, The 1st or 2 characterized by the above-mentioned. Heat exchanger. 前記第１導流管体（１０１）および第２導流管体（２０１）は、同じ形状又は異なる形状の管体により構成されていることを特徴とする請求項１または２に記載の熱交換器。   The heat exchange according to claim 1 or 2, wherein the first and second flow guiding tubes (101) and (201) are formed of tubes having the same shape or different shapes. vessel. 前記第１熱エネルギ体（１０５）と第２熱エネルギ体（２０５）とは、同じ又は異なる流体により構成されていることを特徴とする請求項１または２に記載の熱交換器。   The heat exchanger according to claim 1 or 2, wherein the first thermal energy body (105) and the second thermal energy body (205) are made of the same or different fluids. 前記流体は、気体、液体、もしくは、気体から液体に変換可能又は液体から気体に変換可能である流体により構成されることを特徴とする請求項１または２に記載の熱交換器。   The heat exchanger according to claim 1 or 2, wherein the fluid is constituted by gas, liquid, or a fluid that can be converted from gas to liquid or liquid to gas. 前記第３熱エネルギ体（３０５）は、流体又は固体により構成されることを特徴とする請求項１または２に記載の熱交換器。   The heat exchanger according to claim 1 or 2, wherein the third thermal energy body (305) is composed of a fluid or a solid. 前記第３熱エネルギ体（３０５）が流体により構成される場合、
流体ポンプ（４００）をさらに備え、第３熱エネルギ体（３０５）をポンピングすることにより、熱交換効果を向上することを特徴とする請求項１または２に記載の熱交換器。 When the third thermal energy body (305) is composed of a fluid,
The heat exchanger according to claim 1 or 2, further comprising a fluid pump (400), wherein the heat exchange effect is improved by pumping the third thermal energy body (305). 前記第１導流管体（１０１）の中で流動する前記第１熱エネルギ体（１０５）の流れ、及び、前記第２導流管体（２０１）の中で流動する前記第２熱エネルギ体（２０５）の流れは、同じ又は逆であることを特徴とする請求項１または２に記載の熱交換器。   The flow of the first thermal energy body (105) flowing in the first diversion tube (101) and the second thermal energy body flowing in the second diversion tube (201) The heat exchanger according to claim 1 or 2, wherein the flow of (205) is the same or reverse. 二層又はそれ以上の熱伝導体によって構成され、少なくとも一つの導流管体が形成されており、少なくとも一つの前記導流管体の中に同種又は異種の流体が流れており、隣り合う導流管体を流れる流体の方向が同じ又は逆であることを特徴とする請求項１又は２に記載の熱交換器。   It is composed of two or more layers of heat conductors, and at least one diverter tube is formed, and the same or different fluid flows in at least one of the diverter tubes, and adjacent conductors The heat exchanger according to claim 1 or 2, wherein the direction of the fluid flowing through the flow tube body is the same or opposite. 前記第２導流管体（２０１）に形成されている導熱フィン（１０００）をさらに備えることを特徴とする請求項１または２に記載の熱交換器。   The heat exchanger according to claim 1 or 2, further comprising a heat-conducting fin (1000) formed in the second flow-conducting tube (201). 前記第１導流管体（１０１）の外壁と前記第２導流管体（２０１）の内壁との間に形成されている螺旋状の導流板（２２２）、及び、前記第１導流管体（１０１）の内壁に形成されている螺旋状の導流板（１１１）のうち少なくとも一つをさらに備えることを特徴とする請求項１または２に記載の熱交換器。   A spiral current guide plate (222) formed between an outer wall of the first current guide tube (101) and an inner wall of the second current guide tube (201); and the first current guide The heat exchanger according to claim 1 or 2, further comprising at least one of a spiral flow guide plate (111) formed on an inner wall of the tube body (101). 前記第１導流管体（１０１）の外壁と前記第２導流管体（２０１）の内壁との間に形成されている螺旋状の導流板（２２２）、及び、前記第１導流管体（１０１）の内壁に形成されている螺旋状の導流板（１１１）をさらに備え、
前記導流板（２２２）と前記導流板（１１１）とは同じ螺旋の巻き方を有することを特徴とする請求項１または２に記載の熱交換器。 A spiral current guide plate (222) formed between an outer wall of the first current guide tube (101) and an inner wall of the second current guide tube (201); and the first current guide A spiral flow guide plate (111) formed on the inner wall of the tube (101);
The heat exchanger according to claim 1 or 2, wherein the flow guide plate (222) and the flow guide plate (111) have the same spiral winding method. 前記第１導流管体（１０１）の外壁と前記第２導流管体（２０１）の内壁との間に形成されている螺旋状の導流板（２２２）、及び、前記第１導流管体（１０１）の内壁に形成されている螺旋状の導流板（１１１）をさらに備え、
前記導流板（２２２）と前記導流板（１１１）とは異なる螺旋の巻き方を有することを特徴とする請求項１または２に記載の熱交換器。 A spiral current guide plate (222) formed between an outer wall of the first current guide tube (101) and an inner wall of the second current guide tube (201); and the first current guide A spiral flow guide plate (111) formed on the inner wall of the tube (101);
The heat exchanger according to claim 1 or 2, wherein the flow guide plate (222) and the flow guide plate (111) have different spiral winding methods.
JP2013200948A 2012-09-27 2013-09-27 Heat exchanger Active JP6401439B2 (en)

Applications Claiming Priority (2)

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CN105972869B (en) * 2016-06-14 2019-02-12 杨胜东 A kind of big channel evaporative condenser dual-purpose heat exchanger and its system
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