JPS5986892A - Heat exchanger with ultra-cold temperature device - Google Patents

Heat exchanger with ultra-cold temperature device

Info

Publication number
JPS5986892A
JPS5986892A JP19599582A JP19599582A JPS5986892A JP S5986892 A JPS5986892 A JP S5986892A JP 19599582 A JP19599582 A JP 19599582A JP 19599582 A JP19599582 A JP 19599582A JP S5986892 A JPS5986892 A JP S5986892A
Authority
JP
Japan
Prior art keywords
heat exchanger
low
plates
pressure
tube
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
JP19599582A
Other languages
Japanese (ja)
Inventor
Yoshinori Shiraku
善則 白楽
Hisanao Ogata
久直 尾形
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP19599582A priority Critical patent/JPS5986892A/en
Publication of JPS5986892A publication Critical patent/JPS5986892A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • F28D7/08Heat-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 otherwise bent, e.g. in a serpentine or zig-zag

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

PURPOSE:To obtain a heat exchanger in small size with high efficiency and with low pressure loss, by remarkably increasing the efficiency of fins of a porous plate 8, by constituting a heat exchanger in such a manner that a plurality of porous plates, on which tubes through which hot fluid in high pressure flows, being bend and thermally adhered to the plates, are laminated, and the laminated plates are inserted into a tube through which cold fluid in low pressure flows. CONSTITUTION:A slender tube 9 to flow hot fluid in high pressure is put on a porous plate 8 in the shape of a letter S and is thermally adhered to the plate 8. A heat exchanger is constituted in such a manner that a plurality of porous plates constituted as mentioned above are laminated, connecting slender tubes 9 of each plate to each other, and the laminated plates are inserted into a flow tube 10 in low pressure. The high temperature fluid in high pressure is fed into the tube from an inlet 11, exchanging heat with the cold fluid in low pressure by the intermediary of porous plates 8, and is discharged from an outlet 2.

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は、極低温装置の熱交換器に係シ、特に高圧の低
温液体と低圧の低温ガスとの熱交換に好適な熱交換器に
関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a heat exchanger for a cryogenic device, and particularly to a heat exchanger suitable for heat exchange between a high-pressure low-temperature liquid and a low-pressure low-temperature gas.

〔従来技術〕[Prior art]

従来のこの種の高圧の低温液体と低圧の低温ガスとの熱
交換に用いられる熱交換器について第1゜2図を用いて
説明する。第2(at、(b)に示すような多孔板lと
スペーサーリング2を交互に複数個積層して、低圧の低
温ガス3の流路を形成する。この流路の周囲に、高圧の
低温液体4を流す細管5を巻き付けて、熱的に接合する
。これを管6に接続し、断熱真壁層7に配置する。この
ように、従来の熱交換器は、多孔板1の円周部分に細管
6を巻き付けるので、多孔板1の外径が大きくなった場
合、多孔板のフィン効率が著しく低下し、熱交換効率が
低下するという欠点があった。また、細管6は、スペー
サー付積層多孔板の周囲にらせん状に巻回されるので、
多孔板の側面の伝熱面積が全て使用できないので、この
部分で伝導による熱抵抗が大きくなり、熱交換効率が低
下するという欠点があった。
A conventional heat exchanger of this type used for heat exchange between a high-pressure low-temperature liquid and a low-pressure low-temperature gas will be described with reference to FIGS. 1-2. A plurality of perforated plates 1 and spacer rings 2 as shown in second (at, (b)) are alternately stacked to form a flow path for low-pressure low-temperature gas 3.A high-pressure low-temperature gas The thin tube 5 through which the liquid 4 flows is wrapped around and thermally bonded.This is connected to the tube 6 and placed on the heat insulating wall layer 7.In this way, the conventional heat exchanger Since the thin tube 6 is wound around the perforated plate 1, if the outer diameter of the perforated plate 1 becomes large, the fin efficiency of the perforated plate will be significantly reduced, resulting in a decrease in heat exchange efficiency. Because it is wound in a spiral around the perforated plate,
Since the entire heat transfer area on the side surface of the perforated plate cannot be used, there is a drawback that heat resistance due to conduction increases in this area and heat exchange efficiency decreases.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、低温ガス流体と低温液体との熱交換を
高効率、低圧力損失で行うことができかつ小型の熱交換
器を提供することにある。
An object of the present invention is to provide a compact heat exchanger capable of exchanging heat between a low-temperature gas fluid and a low-temperature liquid with high efficiency and low pressure loss.

〔発明の概要〕[Summary of the invention]

本発明の特徴は、多孔板面上に、高圧の低温流体が流れ
る管をくつ曲させて、熱的にはシ付けたものを複数個積
層し、これを低圧の低温流体の流路管の中に挿入して構
成し、多孔板のフィン効率を著しく向上させ、高効率、
低圧力損失で小型の熱交換器を得ようとするものである
A feature of the present invention is that a plurality of tubes through which high-pressure low-temperature fluid flows are bent and thermally bonded, and a plurality of tubes are stacked on the perforated plate surface. By inserting the fin into the perforated plate, the fin efficiency of the perforated plate is significantly improved, resulting in high efficiency,
The aim is to obtain a compact heat exchanger with low pressure loss.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明の一実施例を第3図、第4図により説明す
る。第3図に示すように、多孔板8の面上に、高圧の高
温流体を流す細管1−1S字状に配置し、熱的に接続す
る。このように、形成した多孔板全細管9を連結しなが
ら、複数個積層し、低圧の流路管10の中に挿入し、構
成する。高圧の高温流体は、入口11から入り、多孔板
8を介して、低圧の低温流体と熱交換しながら、出口1
2に出る。細管9を多孔板面上で、S字状などのように
くつ曲させて、はシ付けることによって、多孔板のフィ
ン効率は大きくなり、熱交換効率が著しく向上する。
An embodiment of the present invention will be described below with reference to FIGS. 3 and 4. As shown in FIG. 3, thin tubes 1-1 through which high-pressure, high-temperature fluid flows are arranged in an S-shape on the surface of the perforated plate 8 and are thermally connected. A plurality of the perforated plate thin tubes 9 formed in this way are stacked while being connected, and are inserted into a low-pressure flow path tube 10 to form a structure. The high-pressure, high-temperature fluid enters from the inlet 11 and exchanges heat with the low-pressure, low-temperature fluid through the perforated plate 8.
Go to 2. By bending the thin tubes 9 in an S-shape or the like on the surface of the perforated plate and attaching them, the fin efficiency of the perforated plate is increased, and the heat exchange efficiency is significantly improved.

本発明によれば、多孔板1枚当シの熱交換効率が著しく
向上するので、必要な多孔板の枚数を低減でき、結局、
圧力損失の小さい熱交換器を得ることができるという効
果がある。
According to the present invention, the heat exchange efficiency per perforated plate is significantly improved, so the number of required perforated plates can be reduced, and as a result,
This has the effect that a heat exchanger with low pressure loss can be obtained.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、多孔板の伝熱面積に対するフィン効率
を大きくすることができるので、多孔板1枚当シの熱交
換量が増加し、必要な熱交換量に対する多孔板の枚数を
著しく低減できることになシ、結局全体の圧力損失金小
さくすることができる効果かめる。
According to the present invention, the fin efficiency relative to the heat transfer area of the perforated plate can be increased, so the amount of heat exchange per per perforated plate increases, and the number of perforated plates relative to the required amount of heat exchange is significantly reduced. In the end, the overall pressure loss can be reduced.

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

第1図は、従来の積層型熱交換器の一例の断面図、第2
図は、従来の積層型熱交換器の構成妥素を示す斜視図で
ある。第3図は、本発明の極低温装置の熱交換器の構成
要素の多孔板の正面図、第4図は、本発明の極低温装置
の熱交換器の斜視断面図である。 1・・・多孔板、2・・・スペーサーリング、3・・・
低圧流体、4・・・高圧流体、5・・・細管、8・・・
多孔板、9・・・細管、10・・・低圧流体流路管、1
1・・・細管。 第1図 舅 Z  図 (L)         (b) 不3図
Figure 1 is a cross-sectional view of an example of a conventional stacked heat exchanger;
The figure is a perspective view showing the structure of a conventional laminated heat exchanger. FIG. 3 is a front view of a perforated plate that is a component of the heat exchanger of the cryogenic apparatus of the present invention, and FIG. 4 is a perspective sectional view of the heat exchanger of the cryogenic apparatus of the present invention. 1... Perforated plate, 2... Spacer ring, 3...
Low pressure fluid, 4... High pressure fluid, 5... Thin tube, 8...
Perforated plate, 9... Thin tube, 10... Low pressure fluid flow path pipe, 1
1...tubule. Figure 1 Father-in-law Z Figure (L) (b) Figure 3

Claims (1)

【特許請求の範囲】[Claims] 高圧の低温流体と低圧の低温流体とを熱交換する極低温
装置の熱交換器において、面上に高圧の低温流体が流れ
る管がくつ曲させてはり付けられ、熱的に接合された熱
伝導性の多孔板あるいはワイヤメツシュを複数個積層し
、これを低圧の低温流体の流路管に挿入して、構成した
ことを特徴とする極低温装置の熱交換器。
In a heat exchanger for a cryogenic device that exchanges heat between a high-pressure, low-temperature fluid and a low-pressure, low-temperature fluid, the tubes through which the high-pressure, low-temperature fluid flows are bent and glued onto the surface, and the heat conduction is thermally connected. 1. A heat exchanger for a cryogenic device, characterized in that it is constructed by laminating a plurality of perforated plates or wire meshes and inserting them into a flow path tube for a low-pressure, low-temperature fluid.
JP19599582A 1982-11-10 1982-11-10 Heat exchanger with ultra-cold temperature device Pending JPS5986892A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19599582A JPS5986892A (en) 1982-11-10 1982-11-10 Heat exchanger with ultra-cold temperature device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19599582A JPS5986892A (en) 1982-11-10 1982-11-10 Heat exchanger with ultra-cold temperature device

Publications (1)

Publication Number Publication Date
JPS5986892A true JPS5986892A (en) 1984-05-19

Family

ID=16350466

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19599582A Pending JPS5986892A (en) 1982-11-10 1982-11-10 Heat exchanger with ultra-cold temperature device

Country Status (1)

Country Link
JP (1) JPS5986892A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0162828A2 (en) * 1984-05-24 1985-11-27 Armaturjonsson AB Heat exchanger
FR2693791A1 (en) * 1992-07-16 1994-01-21 Commissariat Energie Atomique Compact heat exchanger with a high heat exchange coefficient between a liquid phase and a flowing gaseous phase.

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5454358A (en) * 1977-10-07 1979-04-28 Stainless Equipment Co Heat exchanger and method of producing same

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5454358A (en) * 1977-10-07 1979-04-28 Stainless Equipment Co Heat exchanger and method of producing same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0162828A2 (en) * 1984-05-24 1985-11-27 Armaturjonsson AB Heat exchanger
FR2693791A1 (en) * 1992-07-16 1994-01-21 Commissariat Energie Atomique Compact heat exchanger with a high heat exchange coefficient between a liquid phase and a flowing gaseous phase.
WO1994002793A1 (en) * 1992-07-16 1994-02-03 Commissariat A L'energie Atomique Compact heat exchanger having a high heat exchange coefficient between a liquid phase and a flowing gaseous phase

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