JPS6093291A - Lamination type heat exchanger - Google Patents

Lamination type heat exchanger

Info

Publication number
JPS6093291A
JPS6093291A JP20106983A JP20106983A JPS6093291A JP S6093291 A JPS6093291 A JP S6093291A JP 20106983 A JP20106983 A JP 20106983A JP 20106983 A JP20106983 A JP 20106983A JP S6093291 A JPS6093291 A JP S6093291A
Authority
JP
Japan
Prior art keywords
heat
gas
heat exchanger
input gas
return gas
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
JP20106983A
Other languages
Japanese (ja)
Inventor
Motonobu Kawarada
河原田 元信
Hiroshi Kano
博司 鹿野
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.)
Fujitsu Ltd
Original Assignee
Fujitsu 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 Fujitsu Ltd filed Critical Fujitsu Ltd
Priority to JP20106983A priority Critical patent/JPS6093291A/en
Publication of JPS6093291A publication Critical patent/JPS6093291A/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
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0062Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements
    • F28D9/0075Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements the plates having openings therein for circulation of the heat-exchange medium from one conduit to another

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 improve heat exchanging efficiency by a method wherein a heat conductive board is provided with flow paths for input gas and return gas. CONSTITUTION:The high pressure input gas pipe 5 and the return gas pipe 6 of nitrogen are connectsd to a heat insulating board 7 while the heat conductive board 10, having the flow path 8 for the return gas and the flow path 9 for the high pressure input gas at the lower part thereof, is prepared. Further, the heat insulating board 13, having a hole 11 for return gas and the hole 12 for the high pressure input gas, is provided below the heat conductive board 10. Furthermore, the heat conductive board 10 and the heat insulating board 7 are provided below the heat insulating board 13 while the heat exchanger is constituted of the combination of 7-10-13-10-7...-13-10-7. Flow paths 8, 9 are provided in the plane of the heat conductive board and whereby a heat exchanging area between the high-temperature side high pressure input gas and the low-temperature side low pressure return gas may be increased and the heat exchanger, having a high heat exchanging efficiency, may be obtained.

Description

【発明の詳細な説明】 発明の技術分野 本発明は積層型熱交換器に係シ、特に熱交換面積を増大
させて熱交換効率を向上せしめた積層型熱交換器に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION Technical Field of the Invention The present invention relates to a laminated heat exchanger, and more particularly to a laminated heat exchanger that has an increased heat exchange area and improved heat exchange efficiency.

技術の背景 温度の異なる二つの流体(気体や液体ンを固体壁を介し
て接触させ両流体間で熱の移動を行わせる熱交換器はそ
の構造上、多管式熱交換器、二重管式熱交換器、積層型
熱交換器等の種々の熱交換器が知られている。
Technology Background Heat exchangers that bring two fluids (gas or liquid) with different temperatures into contact through a solid wall and transfer heat between the two fluids are structurally divided into shell-and-tube heat exchangers and double-tube heat exchangers. Various heat exchangers are known, such as type heat exchangers and laminated type heat exchangers.

上記の熱交換器の中で積層型熱交換器は軽量小型等の利
点によシ小型化をめられる冷凍機等によく使用されてい
る。
Among the above-mentioned heat exchangers, the laminated heat exchanger is often used in refrigerators and the like where miniaturization is required due to its advantages such as light weight and small size.

従来技術と問題点 従来の積層型熱交換器は第1図に示すように例えばポリ
エチレンからなる板厚約0.1覇の熱的絶縁板lと、銅
からなる板厚約0.2 mmの熱的良導板2を交互に積
層したものである。各々の板には入力ガス人と帰還ガス
Bを通す穴3と4が開けられており、入力ガスAと帰還
ガスBは熱的良導板2によって熱交換せしめられる。上
記熱的絶縁板lと熱的良導板の厚さは例えば0.2mm
程度である。
Prior Art and Problems As shown in Figure 1, a conventional laminated heat exchanger consists of a thermally insulating plate made of polyethylene with a thickness of about 0.1 mm, and a plate made of copper with a thickness of about 0.2 mm. Thermal conductive plates 2 are alternately laminated. Each plate is provided with holes 3 and 4 through which the input gas and the return gas B pass, and the input gas A and the return gas B are caused to exchange heat by the thermally conductive plate 2. The thickness of the thermally insulating plate l and the thermally conductive plate is, for example, 0.2 mm.
That's about it.

第1図及び上記説明のような構造をしているためガスの
流れ方向には熱伝導が悪く、流れに垂直な方向には熱伝
導が良くなっている。このような構造を有する熱交換器
では高温側の高圧入力ガスAが熱交換されて低温側の低
圧帰還ガスBとなるだめの熱交換効率は熱交換面積(六
3,4の内壁面積層が非常に小さいためにその向上を妨
げられている。
Since the structure is as shown in FIG. 1 and explained above, heat conduction is poor in the gas flow direction, but heat conduction is good in the direction perpendicular to the gas flow. In a heat exchanger having such a structure, the heat exchange efficiency of the high-pressure input gas A on the high-temperature side being heat exchanged to become the low-pressure return gas B on the low-temperature side is determined by the heat exchange area (inner wall area layer of 63, 4). It is so small that its improvement is hindered.

発明の目的 上記欠点を鑑み本発明は熱交換効率を向上させた改良さ
れた熱交換器を提供することを目的とする。
OBJECTS OF THE INVENTION In view of the above drawbacks, it is an object of the present invention to provide an improved heat exchanger with improved heat exchange efficiency.

発明の構成 本発明の目的は熱的絶縁板と、熱的良導板とを交互に積
層せしめ且つ該熱的絶縁板と熱的良導板に入力ガス用流
通口及び帰還ガス用流通口の2つの流通口をそれぞれ配
役せしめた積層型熱交換器において; 前記熱的良導板に前記入力ガス用及び帰還ガス用流路を
具備したことを特徴とする積層型熱交換器によって達成
される。す彦わち本発明でd]板の面方向にガス流路を
設けて熱交換面積を増大させるのである。
Structure of the Invention The object of the present invention is to alternately laminate thermally insulating plates and thermally conductive plates, and to provide input gas flow ports and return gas flow ports on the thermally insulating plates and the thermally conductive plates. A laminated heat exchanger in which two flow ports are respectively provided; Achieved by a laminated heat exchanger characterized in that the thermally conductive plate is provided with the input gas flow path and the return gas flow path. . In other words, in the present invention, gas flow channels are provided in the plane direction of the plate to increase the heat exchange area.

発明の実施例 以下本発明の実施例を図面に基づいて説明する。第2図
は本発明の1実施例を示す概略斜視図である。
Embodiments of the Invention Below, embodiments of the present invention will be described based on the drawings. FIG. 2 is a schematic perspective view showing one embodiment of the present invention.

第2図において例えば窒素の高圧入力ガスパイプ5と帰
還ガスバイブロは例えばポリエチレンからなる熱的絶縁
板7と接合させ、その下部には帰還ガスの流路8と高圧
入力ガスの流路9を有する例えは銅からなる熱的良導体
の板(熱的良導板)】0が具備されている。A、Bはそ
れぞれ高圧入力ガス及び低圧帰還ガスを示す。該熱的良
導板10の下部には帰還ガス用穴11及び高圧入力ガス
用穴]2を各々有する熱的絶縁板13が設けられている
。本実施例の熱交換器は該熱的絶縁板13の下部に上述
の熱的良導板lO及び熱的絶縁板7が具備され該上記板
を7−10−13−10−7・・・−13−10−7と
組合せて構成したものである。このように熱的良導板の
平面内に流路8,9を設けることによって高温側の高圧
入力ガスと低温ガスの低圧帰還ガスとの間の熱交換面積
が増大し、熱交換効率の太きガ熱交換器が得られる(ガ
ス流の方向を矢印で示す)。
In FIG. 2, a high-pressure input gas pipe 5 of, for example, nitrogen and a return gas vibro are connected to a thermally insulating plate 7 made of, for example, polyethylene, and a flow path 8 for return gas and a flow path 9 for high-pressure input gas are provided at the bottom thereof. is equipped with a plate of good thermal conductivity made of copper (good thermal conductivity plate). A and B indicate high pressure input gas and low pressure return gas, respectively. A thermally insulating plate 13 having a return gas hole 11 and a high-pressure input gas hole 2 is provided at the bottom of the thermally conductive plate 10. The heat exchanger of this embodiment is provided with the above-mentioned thermally conductive plate lO and thermally insulating plate 7 below the thermally insulating plate 13, and the plates 7-10-13-10-7... -13-10-7. By providing the flow paths 8 and 9 within the plane of the thermally conductive plate, the heat exchange area between the high-pressure input gas on the high-temperature side and the low-pressure return gas on the low-temperature side increases, and the heat exchange efficiency increases. A gas heat exchanger is obtained (direction of gas flow is indicated by arrows).

壕だ上記熱的良導体の板厚が薄いため十分な流路断面積
が得られない場合は該板lO′、10″を第3図に示す
ような同一のパターンの流路を有する多層板とすればよ
い。
If a sufficient flow passage cross-sectional area cannot be obtained due to the thinness of the plate of the thermally good conductor described above, the plate 10', 10'' may be replaced with a multilayer plate having passages of the same pattern as shown in Fig. 3. do it.

発明の詳細 な説明したように、本発明によれば、高温側のガス流路
と低温側のガス流路における熱交換面積が大きくなるた
めに熱交換器の熱交換効率を向上させることが出来、そ
の結果同一の熱交換効率を得るだけならば熱交換器を軽
量小型化することが出来る。
As described in detail, according to the present invention, the heat exchange area of the high temperature side gas flow path and the low temperature side gas flow path is increased, so that the heat exchange efficiency of the heat exchanger can be improved. As a result, the heat exchanger can be made lighter and smaller if only the same heat exchange efficiency is obtained.

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

第1図は従来技術を説明するための概略斜視図であシ、
第2図は本発明に係る1実施例を説明するための棚1略
斜視図でオ)、第3図は本発明に係る他の実施例を説明
するだめの要部概略断面図である。 1.7.10”・・・熱的絶縁板、 2.10,10’・・・熱的良導板、 3.4・・・穴、5・・・高圧入力ガスパイプ、6・・
・帰還ガスパイプ、8・・・帰還ガス流路、9・・・高
圧入力ガス流路、11・・・帰還ガス用穴、12・・・
高圧入力ガス用穴。 特許出願人 富士通株式会社 特許出願代理人 弁理士 青 木 朗 弁理士 西 舘 和 之 弁理士内田幸男 弁理士 山 口 昭 之 第3回
FIG. 1 is a schematic perspective view for explaining the prior art;
FIG. 2 is a schematic perspective view of the shelf 1 for explaining one embodiment of the present invention, and FIG. 3 is a schematic cross-sectional view of a main part of the shelf 1 for explaining another embodiment of the present invention. 1.7.10''...Thermal insulating plate, 2.10,10'...Thermal conductive plate, 3.4...Hole, 5...High pressure input gas pipe, 6...
・Return gas pipe, 8...Return gas flow path, 9...High pressure input gas flow path, 11...Return gas hole, 12...
Hole for high pressure input gas. Patent applicant Fujitsu Limited Patent application agent Akira Aoki Patent attorney Kazuyuki Nishidate Patent attorney Yukio Uchida Patent attorney Akira Yamaguchi 3rd session

Claims (1)

【特許請求の範囲】[Claims] 1、熱的絶縁板と、熱的良導板とを交互に積層せしめ且
つ該熱的絶縁板と熱的良導板に入力ガス用流通口及び帰
還ガス用流通口の2つの流通口をそれぞれ配設せしめた
積層型熱交換器において、前記熱的良導板に前記入力ガ
ス用及び帰還ガス用流路を具備したことを特徴とする積
層型熱交換器。
1. Thermal insulating plates and thermally conductive plates are laminated alternately, and the thermally insulating plates and the thermally conductive plate are provided with two flow ports, an input gas flow port and a return gas flow port, respectively. 1. A laminated heat exchanger, characterized in that the thermally conductive plate is provided with the input gas flow path and the return gas flow path.
JP20106983A 1983-10-28 1983-10-28 Lamination type heat exchanger Pending JPS6093291A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20106983A JPS6093291A (en) 1983-10-28 1983-10-28 Lamination type heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20106983A JPS6093291A (en) 1983-10-28 1983-10-28 Lamination type heat exchanger

Publications (1)

Publication Number Publication Date
JPS6093291A true JPS6093291A (en) 1985-05-25

Family

ID=16434869

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20106983A Pending JPS6093291A (en) 1983-10-28 1983-10-28 Lamination type heat exchanger

Country Status (1)

Country Link
JP (1) JPS6093291A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5429183A (en) * 1992-06-17 1995-07-04 Mitsubishi Denki Kabushiki Kaisha Plate-type heat exchanger and method of producing the same
US5531269A (en) * 1992-06-12 1996-07-02 Dahlgren; Arthur Plate heat exchanger for liquids with different flows
JPH09113176A (en) * 1995-09-07 1997-05-02 Modine Mfg Co Heat exchanger with adaptor
US6082445A (en) * 1995-02-22 2000-07-04 Basf Corporation Plate-type heat exchangers
CN106931821A (en) * 2017-04-06 2017-07-07 中国科学院工程热物理研究所 A kind of heat exchanger plates and gas liquid heat exchanger

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5531269A (en) * 1992-06-12 1996-07-02 Dahlgren; Arthur Plate heat exchanger for liquids with different flows
US5429183A (en) * 1992-06-17 1995-07-04 Mitsubishi Denki Kabushiki Kaisha Plate-type heat exchanger and method of producing the same
US6082445A (en) * 1995-02-22 2000-07-04 Basf Corporation Plate-type heat exchangers
JPH09113176A (en) * 1995-09-07 1997-05-02 Modine Mfg Co Heat exchanger with adaptor
CN106931821A (en) * 2017-04-06 2017-07-07 中国科学院工程热物理研究所 A kind of heat exchanger plates and gas liquid heat exchanger

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