JP2019007729A - Heat exchanger - Google Patents
Heat exchanger Download PDFInfo
- Publication number
- JP2019007729A JP2019007729A JP2018166800A JP2018166800A JP2019007729A JP 2019007729 A JP2019007729 A JP 2019007729A JP 2018166800 A JP2018166800 A JP 2018166800A JP 2018166800 A JP2018166800 A JP 2018166800A JP 2019007729 A JP2019007729 A JP 2019007729A
- Authority
- JP
- Japan
- Prior art keywords
- tube
- thermal energy
- heat exchanger
- flow
- energy body
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- 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
Landscapes
- 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
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.
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2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 for exchanging heat energy between a heat exchanger in two flow paths 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、平行に配列されるn(nは2以上の整数)本の内側管状部材、内側管状部材を並列に接続するとともに第3熱エネルギ体と接触する内側管接続部材、および、両端に設けられる第1流体出入口を有し、内部に少なくとも一つの第1流路(102)が形成され、流体である第1熱エネルギ体(105)の流通に用いられる。第2導流管体(201)は、熱伝導体により構成され、内側管状部材の外径より内径が大きく内側管状部材の外側に設けられるn本の外側管状部材、外側管状部材を並列に接続するとともに第3熱エネルギ体と接触する外側管接続部材、および、両端に設けられる第2流体出入口を有し、環状断面を有する少なくとも一つの第2流路(202)が形成され、流体である第2熱エネルギ体(205)の流通に用いられる。 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 constituted by a heat conductor, and connects n (n is an integer of 2 or more) inner tubular members and inner tubular members arranged in parallel and in parallel with the third heat. The first thermal energy body (105), which has an inner pipe connecting member that comes into contact with the energy body, and a first fluid inlet / outlet provided at both ends, has at least one first flow path (102) formed therein, and is a fluid. ). The second diversion tube body (201) is formed of a heat conductor, and has an inner diameter larger than the outer diameter of the inner tubular member and connects n outer tubular members and outer tubular members provided outside the inner tubular member in parallel. And at least one second flow path (202) having an annular cross section is formed and is a fluid having an outer pipe connecting member that contacts the third thermal energy body and a second fluid inlet / outlet provided at both ends. Used for distribution of the second thermal energy body (205).
第2導流管体(201)の外層は、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。第3エネルギ体(305)は、液体又は固体である。 The outer layer of the second diversion tube (201) is in contact with the third thermal energy body (305) composed of a liquid phase or solid phase thermal energy body to form a three-layer annular structure. Thus, the heat energy is exchanged among the three of 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. The third energy body (305) is a liquid or a solid.
(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 2nd flow conduit body (201) in it is contacting the 3rd thermal energy body (305) comprised by the thermal energy body of gas, a liquid, or a 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。図8等に示す通り、第1合流室(103)は第1導流管体を構成する2つの内側管状部材を接続するものであり、第2合流室(203)は第2導流管体を構成する2つの外側管状部材を接続するものであって、第1合流室(103)が「内側管接続部材」に対応し、第2合流室(203)が「外側管接続部材」に対応する。 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. As shown in FIG. 8 and the like, the first merging chamber (103) connects two inner tubular members constituting the first convection tube, and the second merging chamber (203) is the second convection tube. The first joining chamber (103) corresponds to the “inner pipe connecting member”, and the second joining chamber (203) corresponds to the “outer pipe connecting member”. To do.
(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 (11)
前記第1導流管体(101)は、熱伝導体により構成され、平行に配列されるn(nは2以上の整数)本の内側管状部材、前記内側管状部材を並列に接続するとともに第3熱エネルギ体(305)と接触する内側管接続部材、および、両端に設けられる第1流体出入口を有し、内部に少なくとも一つの第1流路(102)が形成され、流体である第1熱エネルギ体(105)の流通に用いられ、
前記第2導流管体(201)は、熱伝導体により構成され、前記内側管状部材の外径より内径が大きく前記内側管状部材の外側に設けられるn本の外側管状部材、前記外側管状部材を並列に接続するとともに前記第3熱エネルギ体(305)と接触する外側管接続部材、および、両端に設けられる第2流体出入口を有し、環状断面を有する少なくとも一つの第2流路(202)が形成され、流体である第2熱エネルギ体(205)の流通に用いられ、
前記第2導流管体(201)の外層は、液相、又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い、
前記第3エネルギ体(305)は、液体又は固体である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 current guide tube (101) is formed of a heat conductor, and connects n (n is an integer of 2 or more) inner tubular members arranged in parallel, and connects the inner tubular members in parallel. The inner pipe connecting member that contacts the three thermal energy bodies (305) and the first fluid inlet / outlet provided at both ends, and at least one first flow path (102) is formed inside, and is the first fluid Used to distribute thermal energy bodies (105),
The second flow guide tube (201) is formed of a heat conductor, and has an inner diameter larger than an outer diameter of the inner tubular member, n outer tubular members provided outside the inner tubular member, and the outer tubular member. Are connected in parallel and contacted with the third thermal energy body (305), and at least one second flow path (202) having an annular cross section, and a second fluid inlet / outlet provided at both ends. ) Is formed and used for the circulation 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 liquid phase or solid phase thermal energy body, and has a three-layer annular structure. By forming, 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 heat exchanger according to claim 3, wherein the third energy body (305) is liquid or solid.
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に記載の熱交換器。 When the third thermal energy body (305) is composed of a liquid,
The heat exchanger according to claim 1, further comprising a fluid pump (400), wherein the heat exchange effect is improved by pumping the third thermal energy body (305).
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, wherein the flow guide plate (222) and the flow guide plate (111) have the same spiral winding method.
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, wherein the flow guide plate (222) and the flow guide plate (111) have different spiral winding methods.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/628,116 | 2012-09-27 | ||
US13/628,116 US20140083666A1 (en) | 2012-09-27 | 2012-09-27 | Tri-Piece Thermal Energy Body Heat Exchanger Having Multi-Layer Pipeline and Transferring Heat to Exterior Through Outer Periphery of Pipeline |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2013200948A Division JP6401439B2 (en) | 2012-09-27 | 2013-09-27 | Heat exchanger |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2019007729A true JP2019007729A (en) | 2019-01-17 |
JP6746647B2 JP6746647B2 (en) | 2020-08-26 |
Family
ID=49328337
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2013200948A Active JP6401439B2 (en) | 2012-09-27 | 2013-09-27 | Heat exchanger |
JP2018166800A Active JP6746647B2 (en) | 2012-09-27 | 2018-09-06 | Heat exchanger |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2013200948A Active JP6401439B2 (en) | 2012-09-27 | 2013-09-27 | Heat exchanger |
Country Status (8)
Country | Link |
---|---|
US (1) | US20140083666A1 (en) |
EP (1) | EP2713131B1 (en) |
JP (2) | JP6401439B2 (en) |
CN (3) | CN203501858U (en) |
AU (2) | AU2013234402B2 (en) |
CA (1) | CA2828311C (en) |
SG (1) | SG2013073028A (en) |
TW (3) | TWM476252U (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20140083666A1 (en) * | 2012-09-27 | 2014-03-27 | Tai-Her Yang | Tri-Piece Thermal Energy Body Heat Exchanger Having Multi-Layer Pipeline and Transferring Heat to Exterior Through Outer Periphery of Pipeline |
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 |
CN106197088A (en) * | 2016-08-19 | 2016-12-07 | 张家港市德胜染整有限责任公司 | A kind of waste-heat recovery device of dyeing waste-water |
CN112292202A (en) * | 2018-06-12 | 2021-01-29 | 株式会社Ihi | Reaction device |
CN109210967B (en) * | 2018-09-17 | 2020-01-14 | 中国核动力研究设计院 | Multi-stage sleeve heat exchanger for reactor fuel testing loop |
CZ308768B6 (en) * | 2020-03-17 | 2021-05-05 | Vysoká Škola Báňská - Technická Univerzita Ostrava | Recuperative screw heat exchanger, especially for bulk materials |
CN113464216B (en) * | 2021-07-28 | 2023-07-28 | 湖南湘化机汽轮机有限公司 | Steam turbine for waste heat recovery of steam boiler |
Family Cites Families (34)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1798330A (en) * | 1925-09-18 | 1931-03-31 | Leek Albert Edward | Heat-exchange apparatus |
US1738914A (en) * | 1926-08-04 | 1929-12-10 | George T Mott | Apparatus for heat exchanging |
US1701341A (en) * | 1928-02-24 | 1929-02-05 | Frick Co | Cooling coil |
US2658728A (en) * | 1948-06-25 | 1953-11-10 | Lummus Co | Method of detecting leakage between heat transfer fluids |
US2858677A (en) * | 1955-04-11 | 1958-11-04 | Marley Co | Water cooling apparatus |
JPS5756071Y2 (en) * | 1977-04-16 | 1982-12-03 | ||
US4210199A (en) * | 1978-06-14 | 1980-07-01 | Doucette Industries, Inc. | Heat exchange system |
JPS58136985A (en) * | 1982-02-08 | 1983-08-15 | Mitsubishi Electric Corp | Heat exchanger |
FR2552216B1 (en) * | 1983-09-21 | 1988-08-12 | Onera (Off Nat Aerospatiale) | IMPROVEMENTS TO HEAT EXCHANGER TUBES AND TO EXCHANGERS MADE WITH SUCH TUBES |
DE3411675A1 (en) * | 1984-03-27 | 1985-10-10 | Josef Hubert 5203 Much Schick | DEVICE FOR EXCHANGING HEAT AND FUEL BETWEEN TWO OR MORE FLOWABLE MEDIA |
JPS6159188A (en) * | 1984-08-30 | 1986-03-26 | Toyo Radiator Kk | Charge air cooler |
JPS63154967U (en) * | 1987-03-30 | 1988-10-12 | ||
JPH03279789A (en) * | 1990-03-28 | 1991-12-10 | Yanmar Diesel Engine Co Ltd | Double piped heat exchanger |
CN2094021U (en) * | 1991-05-25 | 1992-01-22 | 程效民 | Tube in tube tubular heat-exchanger |
JPH09113168A (en) * | 1995-10-13 | 1997-05-02 | Tokyo Gas Co Ltd | Double tube type vaporizer |
JP2001280864A (en) * | 2000-03-30 | 2001-10-10 | Hitachi Ltd | Heat exchanger and manufacturing method therefor |
CN2449174Y (en) * | 2000-10-25 | 2001-09-19 | 于奎明 | Large volume sleeve pipe type heat-exchanger |
JP2003050092A (en) * | 2001-08-06 | 2003-02-21 | Ee R C:Kk | Heat exchanger |
TW495013U (en) * | 2001-12-04 | 2002-07-11 | Taiwan Reduce Pollutant Techno | Heat exchanger |
CN2588308Y (en) * | 2002-11-26 | 2003-11-26 | 郝德欣 | Cold and hot water exchanger for central heating |
JP2005127684A (en) * | 2003-10-27 | 2005-05-19 | Atago Seisakusho:Kk | Double tube type heat exchanger |
JP4033402B2 (en) * | 2004-04-27 | 2008-01-16 | 本田技研工業株式会社 | Heat exchanger |
CN1719179A (en) * | 2005-07-11 | 2006-01-11 | 刘庆久 | Pipe heat exchanger |
CN200947001Y (en) * | 2006-04-30 | 2007-09-12 | 华南理工大学 | Sleeve-type heat exchanger |
WO2008078194A2 (en) * | 2006-06-20 | 2008-07-03 | Adir Segal, Ltd. | Thermal load management system |
CN101105373A (en) * | 2007-08-01 | 2008-01-16 | 中原工学院 | Fin-sleeve type three mediums composite heat-exchanger |
DE102007054703B4 (en) * | 2007-11-14 | 2012-04-19 | GEA Luftkühler GmbH | heat exchangers |
JP2009162395A (en) * | 2007-12-28 | 2009-07-23 | Showa Denko Kk | Double-wall-tube heat exchanger |
CN101226033A (en) * | 2008-02-18 | 2008-07-23 | 中原工学院 | Shell-sleeve type three-medium composite heat exchanger |
CN201407930Y (en) * | 2009-06-01 | 2010-02-17 | 刘洪亮 | Highly-effective sewage heat exchanger |
CN201715902U (en) * | 2009-10-16 | 2011-01-19 | 杨泰和 | Heat absorbing or releasing device with flow paths staggered and evenly distributed according to temperature difference |
JP5743051B2 (en) * | 2010-09-15 | 2015-07-01 | 三浦工業株式会社 | Heat exchanger and boiler water supply system |
CN201945215U (en) * | 2010-12-27 | 2011-08-24 | 青岛磐石容器制造有限公司 | Fixed tube plate type double-tube heat exchanger |
US20140083666A1 (en) * | 2012-09-27 | 2014-03-27 | Tai-Her Yang | Tri-Piece Thermal Energy Body Heat Exchanger Having Multi-Layer Pipeline and Transferring Heat to Exterior Through Outer Periphery of Pipeline |
-
2012
- 2012-09-27 US US13/628,116 patent/US20140083666A1/en not_active Abandoned
-
2013
- 2013-09-26 CA CA2828311A patent/CA2828311C/en active Active
- 2013-09-27 CN CN201320600892.XU patent/CN203501858U/en not_active Expired - Lifetime
- 2013-09-27 SG SG2013073028A patent/SG2013073028A/en unknown
- 2013-09-27 AU AU2013234402A patent/AU2013234402B2/en active Active
- 2013-09-27 EP EP13186548.7A patent/EP2713131B1/en active Active
- 2013-09-27 CN CN201310448066.2A patent/CN103697725A/en active Pending
- 2013-09-27 JP JP2013200948A patent/JP6401439B2/en active Active
- 2013-09-27 TW TW102218081U patent/TWM476252U/en not_active IP Right Cessation
- 2013-09-27 TW TW102134914A patent/TWI586932B/en active
- 2013-09-27 TW TW106115210A patent/TWI619922B/en active
- 2013-09-27 CN CN201910500868.0A patent/CN110274494A/en active Pending
-
2017
- 2017-11-28 AU AU2017268511A patent/AU2017268511A1/en not_active Abandoned
-
2018
- 2018-09-06 JP JP2018166800A patent/JP6746647B2/en active Active
Also Published As
Publication number | Publication date |
---|---|
AU2013234402A2 (en) | 2017-03-02 |
AU2013234402B2 (en) | 2017-09-21 |
TW201416638A (en) | 2014-05-01 |
JP6746647B2 (en) | 2020-08-26 |
TWI586932B (en) | 2017-06-11 |
AU2013234402A1 (en) | 2014-04-10 |
CN110274494A (en) | 2019-09-24 |
CN103697725A (en) | 2014-04-02 |
TW201730495A (en) | 2017-09-01 |
CA2828311C (en) | 2020-07-28 |
CA2828311A1 (en) | 2014-03-27 |
US20140083666A1 (en) | 2014-03-27 |
TWI619922B (en) | 2018-04-01 |
SG2013073028A (en) | 2014-04-28 |
EP2713131B1 (en) | 2016-06-08 |
EP2713131A1 (en) | 2014-04-02 |
AU2017268511A1 (en) | 2017-12-14 |
JP2014074581A (en) | 2014-04-24 |
TWM476252U (en) | 2014-04-11 |
JP6401439B2 (en) | 2018-10-10 |
CN203501858U (en) | 2014-03-26 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2019007729A (en) | Heat exchanger | |
US10119769B2 (en) | Tri-piece thermal energy body heat exchanger having multi-layer pipeline and transferring heat to exterior through outer periphery of pipeline | |
TWI609165B (en) | Pipe member equipped with heat insulation core pipeline and u-shaped annularly-distributed pipeline | |
TWI522594B (en) | Thermal conductive cylinder installed with u-type core piping and loop piping | |
CN108562179B (en) | Spiral jet flow sleeve heat exchanger and working method thereof | |
TWI606226B (en) | Pipe member equipped with heat insulation core pipeline, auxiliary heat conduction structure and u-shaped annularly-distributed pipeline | |
CN204007233U (en) | The U-shaped pipe heat exchanger of a kind of continuous helical deflecting plate | |
JP3188901U (en) | Heat exchanger | |
JP2009103360A (en) | Plate laminated heat exchanger | |
CN203489738U (en) | Stainless steel spiral winding type tubular cooler | |
CA3010569A1 (en) | Heat exchanger | |
JP2005147567A (en) | Double pipe type heat exchanger | |
CN104964584A (en) | Double-pipe heat exchanger | |
CN211290562U (en) | Water route heating structure device | |
CN212658122U (en) | Heat exchanger | |
KR20110138319A (en) | Double layer pipe | |
JP2005147566A (en) | Double pipe type heat exchanger | |
CN103206883B (en) | Finned helix tube | |
JP2011185467A (en) | Heat transfer tube and heat exchanger | |
TWI618908B (en) | Thermal conductive cylinder installed with u-type core piping and loop piping | |
JP6254364B2 (en) | Heat exchanger for heat pump water heater | |
JP2016109322A (en) | Water-refrigerant heat exchanger | |
TH130325B (en) | Double pipes for heat exchanger | |
CN104344751A (en) | Tubular heat exchanger with locating pin | |
TH79442B (en) | Tubular heat exchangers and their manufacturing methods |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20180910 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20190710 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20190716 |
|
A601 | Written request for extension of time |
Free format text: JAPANESE INTERMEDIATE CODE: A601 Effective date: 20191016 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20191216 |
|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20200204 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20200602 |
|
A911 | Transfer to examiner for re-examination before appeal (zenchi) |
Free format text: JAPANESE INTERMEDIATE CODE: A911 Effective date: 20200609 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20200714 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20200805 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 6746647 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |