JPS61231394A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPS61231394A
JPS61231394A JP7238485A JP7238485A JPS61231394A JP S61231394 A JPS61231394 A JP S61231394A JP 7238485 A JP7238485 A JP 7238485A JP 7238485 A JP7238485 A JP 7238485A JP S61231394 A JPS61231394 A JP S61231394A
Authority
JP
Japan
Prior art keywords
pipe member
pressure
heat
heat exchanger
low
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.)
Pending
Application number
JP7238485A
Other languages
Japanese (ja)
Inventor
Hidefumi Saito
英文 斎藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shimadzu Corp
Original Assignee
Shimadzu Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shimadzu Corp filed Critical Shimadzu Corp
Priority to JP7238485A priority Critical patent/JPS61231394A/en
Publication of JPS61231394A publication Critical patent/JPS61231394A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/02Heat-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 helically coiled
    • F28D7/024Heat-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 helically coiled the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration

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)
  • Separation By Low-Temperature Treatments (AREA)
  • Details Of Heat-Exchange And Heat-Transfer (AREA)

Abstract

PURPOSE:To enable a heat exchanger to display its heat-exchanging performance and to be easily manufactured, by a construction wherein a heat exchanger is constituted of a cylindrical casing, a pipe member affixed to the inner periphery of the casing in a substantially wound state, and heat-exchanging plates disposed in the casing with the outer peripheral edges supported in contact with the pipe member. CONSTITUTION:The pipe member 2 is affixed to the inner periphery of the cylindrical casing 1, and a plurality of heat-exchanging plates 3 permeable to fluids are disposed on the inside of the pipe member 2, with the outer peripheral edges 3a thereof supported in contact with the pipe member 2. A high- pressure gas H introduced through an upper high-pressure port 11 flows through a high-pressure passage 17 in the member 2, and is led out through a lower high-pressure port 12. On the other hand, a low-pressure gas L introduced through a lower low-pressure port 13 flows up sequentially through through-holes of the plates 3, and is discharged to the exterior of the casing 1 through the upper low-pressure port 14. The gas L and the gas H exchange heat with each other through the pipe member 2 and the plates 3.

Description

【発明の詳細な説明】 [産業上の利用分野1     〜 本発明は、 He液化装置等に好適に使用できる熱交換
器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field 1] The present invention relates to a heat exchanger that can be suitably used in He liquefaction equipment and the like.

L従来の技術1 クロードサイクルによるHe液化装置等のように、深冷
を利用した機器においては、その装置容積のうち熱交換
器の占める割合が大きい、そのため、熱交換器を小形化
しないと、装置全体をコンパクトにすることができない
という問題があった。しかしながら、熱交換器を単に小
さくするだけでは、熱交換効率が低下′して常温域から
低温域への熱侵入が大きくなるという不都合を招く、そ
のため、この種装置のコンパクト化は容易には実現・し
得なかった。
LPrior art 1 In equipment that uses deep cooling, such as a He liquefaction equipment using a Claude cycle, the heat exchanger occupies a large proportion of the equipment volume.Therefore, unless the heat exchanger is made smaller, There was a problem that the entire device could not be made compact. However, simply making the heat exchanger smaller will lead to the inconvenience of lower heat exchange efficiency and increased heat intrusion from the normal temperature range to the low temperature range, so it is not easy to make this type of equipment more compact.・I couldn't do it.

゛ところで、近年、第4図にネオように、高圧パス用・
の透窓aおよび低圧パス用の透窓すを有した枠体状の断
熱スペーサCと、多数の透孔dを有した熱交換プレート
eとを交互に積層するタイプのいわゆる積層熱交換器が
開発され、これらの問題が解決されつつある。
゛By the way, in recent years, as shown in Figure 4, high-voltage path
A so-called laminated heat exchanger is a type in which a frame-shaped heat insulating spacer C having a transparent window a and a transparent window for a low pressure path and a heat exchange plate e having a large number of through holes d are laminated alternately. are being developed and these problems are being solved.

[発明が解決しようとする問題点] ところが、前述した積層熱交換器は、前記断熱スペーサ
Cと熱交換プレー)eとの接着または接合が完全でない
と、高圧パスfから低圧パスgへのガス漏れが発生する
。そのため、組^立てをクリーンルームで行なわなけれ
ばならない等の制約があり、製作が容易でないという間
軸がある。
[Problems to be Solved by the Invention] However, in the above-described laminated heat exchanger, if the adhesion or bonding between the heat insulating spacer C and the heat exchange plate (e) is not perfect, gas may flow from the high pressure path f to the low pressure path g. A leak occurs. Therefore, there are restrictions such as assembly having to be performed in a clean room, and manufacturing is not easy.

本発明は、このような問題点を解消することを目的とし
てなされたもので、従来の積層熱交換器と同等の性能を
発揮させることができ、しかも、特殊な設備を要するこ
となく簡単に製作することができる熱交換器を提供しよ
うとするものである。
The present invention was made with the aim of solving these problems, and can exhibit the same performance as conventional laminated heat exchangers, and can be easily manufactured without requiring special equipment. The aim is to provide a heat exchanger that can

L問題点を解決するための手段] 本発明は、このような目的を達成するために。Measures to solve the L problem] The present invention aims to achieve such an objective.

熱交換器を、筒状のケースと、このケースの内周□  
に略巻装状態に添設した熱庄導の良好なパイプ部材と、
このパイプ部材に外周縁を接触支持させて前記ケース内
に配設した流体透過性を有する熱交換板とをA@してな
るものにし、前記パイプ部材の内部を高圧流体が通過す
る高圧流路とするとともに、前記ケースの一端から前記
各熱交換板を通してケースの他端に至る空間を低圧流体
が通過する低圧流路となしたことを特徴とする。
The heat exchanger is connected to a cylindrical case and the inner circumference of this case □
A pipe member with good thermal conductivity attached to the pipe in a substantially wrapped state,
A heat exchange plate having fluid permeability is disposed in the case with the outer peripheral edge thereof being contacted and supported by the pipe member, and a high-pressure flow path through which high-pressure fluid passes through the inside of the pipe member. In addition, the space from one end of the case to the other end of the case through each of the heat exchange plates is a low-pressure flow path through which low-pressure fluid passes.

1作用] このような構成のものであれば、前記パイプ部゛村内に
形成された長い高圧流路中を流れる高圧流体と、このパ
イプ部材に外周縁を接触支持させた何枚もの熱交換板を
透過しつつ流れる低圧流体との間で熱交換が行なわれる
。そのため、多数枚の熱交換プレートを介して熱交換を
行なう従来の積層熱交換器と同じような性悌を発揮させ
ることができる。
1 Effect] With such a configuration, the high-pressure fluid flowing in the long high-pressure flow path formed in the pipe section and the number of heat exchange plates whose outer peripheries are supported in contact with the pipe member Heat exchange occurs between the low-pressure fluid flowing through it. Therefore, it is possible to exhibit the same performance as a conventional laminated heat exchanger that exchanges heat through a large number of heat exchange plates.

しかも、高圧流体は、パイプ部材の内部を通過するため
、接合面での気密性が不要となる。また、高圧流路は急
拡大、急縮小がないため、部材の圧損を招くことなしに
流体を円滑に流すことができる。
Moreover, since the high-pressure fluid passes through the inside of the pipe member, there is no need for airtightness at the joint surfaces. Further, since the high-pressure flow path does not suddenly expand or contract, fluid can flow smoothly without causing pressure loss in the members.

L実施例J 以下1本発明の一実施例を第1図および第2図を参照し
て説明する。
LEmbodiment J An embodiment of the present invention will be described below with reference to FIGS. 1 and 2.

本発明に係る熱交換器は、第1図に示すように1円筒状
のケースlの内周にパイプ部材2を添設するとともに、
このパイプ部材2の内側に流体透過性を有した複数板の
熱交換板3を、その外周縁3aを前記パイプ部材2に接
触支持させて配設している。パイプ部材2は、熱伝導の
良好な材料により作られた耐圧管であり、第2図に示す
ような巻装状態に成形して前記ケースlの内周に気□密
に添接させである。詳述すれば、このパイプ部材2は、
図中上下方向に所定の間隔をあけて平行に並ぶ複数段の
水平巻回m4と、上段の水平巻回部4を1段の水平巻回
部4に順次連通させる複数′の段部5とからなるもので
、具体的には、1本の耐圧管を円周方向所定個所が段状
をなすように変形させつつ螺旋状に巻回成形したもので
ある。熱交換板3は、多数の透孔6を有した円板状のも
ので、熱伝導の良好な材料により作られている。そして
、この熱交換板3を前記パイプ部材2の水平巻回部4の
内周に嵌合させ、その嵌合部7をロー付により接合して
いる。しかして、この実施例では、各水平巻回部4に3
板づつ熱交換板3を取着している。なお、前記各熱交換
板3の外周部−個所には、前記段部5間に形成される隙
間8に挿入される突f19がそれぞれ設けである。
As shown in FIG. 1, the heat exchanger according to the present invention includes a pipe member 2 attached to the inner circumference of a cylindrical case l, and
A plurality of heat exchange plates 3 having fluid permeability are disposed inside the pipe member 2 so that their outer peripheral edges 3a are in contact with and supported by the pipe member 2. The pipe member 2 is a pressure-resistant pipe made of a material with good thermal conductivity, and is formed into a wrapped state as shown in FIG. 2 and attached to the inner circumference of the case l in an air-tight manner. . To be more specific, this pipe member 2 is
In the figure, a plurality of horizontal windings m4 arranged in parallel at a predetermined interval in the vertical direction, and a plurality of stages 5 that sequentially connect the upper horizontal winding part 4 to the one-stage horizontal winding part 4. Specifically, it is formed by winding a single pressure tube into a spiral shape while deforming it so that predetermined portions in the circumferential direction form steps. The heat exchange plate 3 is disk-shaped with a large number of through holes 6, and is made of a material with good thermal conductivity. This heat exchange plate 3 is fitted onto the inner periphery of the horizontally wound portion 4 of the pipe member 2, and the fitting portion 7 is joined by brazing. Therefore, in this embodiment, each horizontal winding section 4 has three windings.
Heat exchange plates 3 are attached one by one. Incidentally, each of the heat exchange plates 3 is provided with a protrusion f19 inserted into the gap 8 formed between the step portions 5 at the outer peripheral portion thereof.

また、前記ケースlの上端および下端に高圧ポート11
.12および低圧ポー)13.14を有した端蓋15.
16を気密に装着している。すなわち、この熱交換器は
、前記パイプ部材2の内部を高圧流路17とするととも
に、前記ケースlの一端から前記各熱交換板3を通して
ケースlの他端に至る空間を低圧流路18となしている
。しかして、前・記各高圧ポート11.12は、前記高
圧流路17に連通し、前記低圧ポート13.14は前記
低圧流路18に連通しでいる。
Also, high pressure ports 11 are provided at the upper and lower ends of the case l.
.. 12 and low pressure port) 13.14.
16 is attached airtight. That is, in this heat exchanger, the inside of the pipe member 2 is a high-pressure passage 17, and the space from one end of the case l through each heat exchange plate 3 to the other end of the case l is a low-pressure passage 18. I am doing it. Thus, each of the high pressure ports 11.12 communicates with the high pressure passage 17, and the low pressure port 13.14 communicates with the low pressure passage 18.

なお、この熱交換器を製作する場合には′、螺旋状に成
形したパイプ部・材2の内側に熱交換板3をロー付し、
しかる後に、前記パイプ部材2の外側にケースlをかぶ
せるようにするのが望ましい。
In addition, when manufacturing this heat exchanger, the heat exchange plate 3 is brazed on the inside of the pipe part/material 2 formed into a spiral shape,
After that, it is desirable to cover the outside of the pipe member 2 with the case l.

このような構成のものであれば、例えば、上側の高圧ポ
ート11から導入した高圧ガスHは、パイプ部材2内の
高圧流路17を流通し、下側の高圧ポー)12から導出
される。一方、下側の低圧ポート13から導入した低圧
ガスLは、複数の熱交換&3の透孔6を順次に通過して
上昇し、上側の低圧ポート14からケースl外へ排出さ
れる。
With such a configuration, for example, the high pressure gas H introduced from the upper high pressure port 11 flows through the high pressure passage 17 in the pipe member 2 and is led out from the lower high pressure port 12. On the other hand, the low-pressure gas L introduced from the lower low-pressure port 13 sequentially passes through the through holes 6 of the heat exchange &3, rises, and is discharged from the upper low-pressure port 14 to the outside of the case l.

そのため、この低圧ガスLと前記高圧ガスHとが前記パ
イプ部材2および熱交換板3を介して熱交換を行なうこ
とになる。しかして、このものは。
Therefore, this low pressure gas L and the high pressure gas H exchange heat via the pipe member 2 and the heat exchange plate 3. However, this one...

高圧ガスHを長い高圧流路17に導くとともに、低圧ガ
スLを何枚のも熱交換板3を順次に透過させつつ流通さ
せるようにし二いるので、多数枚の熱交換プレートを介
して熱交、換を行なわせる従来の積層熱交換器と同じよ
うな性能を発揮させることができる。
The high-pressure gas H is guided into the long high-pressure flow path 17, and the low-pressure gas L is passed through a number of heat exchange plates 3 in sequence and circulated. It is possible to exhibit the same performance as a conventional laminated heat exchanger that performs .

しかも、高圧ガスHは、パイプ部材2の内部を通過する
ようになっており、接合部分において高圧流路17と低
圧流路18とを区画する必要がないため、接合面におけ
る気密性が要求されない。
Moreover, since the high-pressure gas H passes through the inside of the pipe member 2, there is no need to partition the high-pressure flow path 17 and the low-pressure flow path 18 at the joint, so airtightness at the joint surface is not required. .

そのため、クリーンルームで組立てを行なう等の配慮が
全く不要となり、製作の容易化を図ることができる。
Therefore, consideration such as assembling in a clean room is completely unnecessary, and manufacturing can be facilitated.

また、高圧流路17は、急拡大および急縮小することが
ないので、圧力損失を小さく抑えることができる。その
為、この熱交換器を組み込んだ機器全体のシステム効率
の向上に寄与し得るものとなる。
Moreover, since the high-pressure channel 17 does not suddenly expand or contract, pressure loss can be kept small. Therefore, it can contribute to improving the system efficiency of the entire device incorporating this heat exchanger.

なお、パイプ部材の形態は前記実施例のものに限られな
いのは勿論であり、例えば、円形でなく多角形になるよ
うにして螺旋状に成形したものや、第3図に示すような
ものにしてもよい、第3図に示すパイプ部材22は、展
開した場合に蛇行した形になるような形態をなしている
Note that the shape of the pipe member is of course not limited to that of the above embodiments; for example, it may be formed into a polygonal shape instead of a circle, or a shape as shown in FIG. 3. The pipe member 22 shown in FIG. 3 has a meandering configuration when unfolded.

また、パイプ部材間の隙間には、断熱材を介設してもよ
い、さらに、パイプ部材自体の断面形状を円形以外の形
1例えば、四角形等にしてもよい。
Further, a heat insulating material may be interposed in the gap between the pipe members, and the cross-sectional shape of the pipe member itself may be made into a shape other than a circle, for example, a square.

また、ケースも、単なる筒状のものに限らず、例えば、
その内周に前記パイプ部材の形状に合わせたくぼみを設
ける等5種々変形が可能である。
In addition, the case is not limited to a simple cylindrical case, for example,
Various modifications are possible, such as providing a recess on the inner periphery to match the shape of the pipe member.

ざらに、熱交換板も前記実施例のものに限られるもので
はなく1例えば、熱の伝導をよくするために、中央が薄
くなった凹レンズ状のものにしたり、透孔を設ける代わ
りに熱交換板全体を多孔質金属で製作する等の変形例が
考えられ6゜また、前記実施例では、パイプ部材と熱交
換板とをロー付により接合させる場合について説明した
が1本発明は必ずしもこのようなものに限られないのは
勿論であり、例えば、前記パイプ部材と前記熱交換板と
を溶接や拡散接合あるいは接着等により接続したり、完
全に一体化したものも本発明に含まれる。
Generally speaking, the heat exchange plate is not limited to the one in the above embodiment.1 For example, in order to improve heat conduction, it may be made into a concave lens shape with a thinner center, or a heat exchange plate may be used instead of providing a through hole. Modifications such as manufacturing the entire plate from porous metal may be considered6.Also, in the above embodiment, a case was explained in which the pipe member and the heat exchange plate were joined by brazing, but the present invention does not necessarily apply to such a case. Of course, the present invention is not limited to this, and for example, the present invention also includes a structure in which the pipe member and the heat exchange plate are connected by welding, diffusion bonding, adhesive, etc., or are completely integrated.

[発明の効果J 本発明は、以上のような構成であるから、従来のJiA
層熱交熱交換器等の性能を発揮させることができ、しか
も、#i合部における気密性が要求されないため特殊な
設備を要することなく簡単に製作することができる優れ
た熱交換器を提供できるものである。
[Effect of the Invention J] Since the present invention has the above configuration, the conventional JiA
Provides an excellent heat exchanger that can exhibit the performance of a layered heat exchanger, etc., and can be easily manufactured without requiring special equipment because airtightness is not required at the #i joint. It is possible.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本発明の一実施例を示し、N41図は一部有略し
た断面図、第2図は分解した斜視図である。第3IAは
、本発明の他の実施例を説明するための説明図、第4図
は従来例を示す斜視図である。 1目eケース 2.22−◆−パイプ部材 3・鳴・熱交換板 3a吻・・外周縁 6・・・透孔 1711・・高圧流路 18・−・低圧流路 H・・・高圧流体(高圧ガス) L−倭φ低圧流体(低圧ガス)
The drawings show one embodiment of the present invention, and FIG. N41 is a partially omitted sectional view, and FIG. 2 is an exploded perspective view. 3IA is an explanatory view for explaining another embodiment of the present invention, and FIG. 4 is a perspective view showing a conventional example. 1st e case 2.22-◆-pipe member 3, sound, heat exchange plate 3a proboscis...outer periphery 6...through hole 1711...high-pressure flow path 18--low-pressure flow path H...high-pressure fluid (High pressure gas) L-Wa φ Low pressure fluid (Low pressure gas)

Claims (1)

【特許請求の範囲】[Claims] 筒状のケースと、このケースの内周に略巻装状態に添設
した熱伝導の良好なパイプ部材と、このパイプ部材に外
周縁を接触支持させて前記ケース内に配設した流体透過
性を有する熱交換板とを具備し、前記パイプ部材の内部
を高圧流体が通過する高圧流路とするとともに、前記ケ
ースの一端から前記各熱交換板を通してケースの他端に
至る空間を低圧流体が通過する低圧流路となしたことを
特徴とする熱交換器。
A cylindrical case, a pipe member with good heat conduction attached to the inner periphery of the case in a substantially wrapped state, and a fluid permeable pipe member disposed inside the case with the outer periphery of the pipe member contacting and supported. and a heat exchange plate having a heat exchange plate, the inside of the pipe member being a high pressure passage through which high pressure fluid passes, and a space from one end of the case to the other end of the case through each of the heat exchange plates being a space for low pressure fluid to pass through. A heat exchanger characterized by having a low-pressure passage through which the heat exchanger passes.
JP7238485A 1985-04-04 1985-04-04 Heat exchanger Pending JPS61231394A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7238485A JPS61231394A (en) 1985-04-04 1985-04-04 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7238485A JPS61231394A (en) 1985-04-04 1985-04-04 Heat exchanger

Publications (1)

Publication Number Publication Date
JPS61231394A true JPS61231394A (en) 1986-10-15

Family

ID=13487732

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7238485A Pending JPS61231394A (en) 1985-04-04 1985-04-04 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS61231394A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018070009A1 (en) * 2016-10-13 2018-04-19 三菱電機株式会社 Heat pump apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018070009A1 (en) * 2016-10-13 2018-04-19 三菱電機株式会社 Heat pump apparatus

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