JPS61272593A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPS61272593A JPS61272593A JP11363485A JP11363485A JPS61272593A JP S61272593 A JPS61272593 A JP S61272593A JP 11363485 A JP11363485 A JP 11363485A JP 11363485 A JP11363485 A JP 11363485A JP S61272593 A JPS61272593 A JP S61272593A
- Authority
- JP
- Japan
- Prior art keywords
- fins
- slits
- fin
- divided
- heat medium
- 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
Links
Classifications
-
- 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
- F28F1/32—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 the means having portions engaging further tubular elements
- F28F1/325—Fins with openings
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、空気調和機や冷凍庫、冷蔵庫等に用いられる
フィンチューブ型熱交換器に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a fin-tube heat exchanger used in air conditioners, freezers, refrigerators, and the like.
従来の技術
近年、熱交換器の性能向上は目ざましいものがあり、千
鳥配管熱交換器や完全独立フィン熱交換器はすでに実用
化されている。2. Description of the Related Art In recent years, the performance of heat exchangers has improved dramatically, and staggered pipe heat exchangers and completely independent fin heat exchangers have already been put into practical use.
以下第3図、第4図を参照しながら、上述した従来の熱
交換器について説明を行なう。The conventional heat exchanger mentioned above will be explained below with reference to FIGS. 3 and 4.
図において、1は多数並行に配列された小片のフィンで
、気流入方向で各列に分断されている。In the figure, reference numeral 1 denotes a large number of small fins arranged in parallel, which are divided into rows in the air inflow direction.
2はフィン1を貫通する熱媒体管で、千鳥状に配管され
ている。Reference numeral 2 denotes heat medium pipes that pass through the fins 1 and are arranged in a staggered manner.
以上のように構成された熱交換器について、以下その動
作について説明する。The operation of the heat exchanger configured as above will be described below.
フィン1のフィン間を流れる気流Aと熱媒体管2の管内
を流れる熱媒体の間で熱交換が行なわれる。その際、フ
ィン1は気流A方向で各列毎に分断されているため、フ
ィン表面に生じる境界層の発達を分断し、かつ境界層前
縁効果により、気流Aとフィン1の間で大きい熱伝達を
得ている。更に熱媒体管2が千鳥状に配管されているこ
とによって気流Aの乱れを大きくし、気流Aとフィン1
及び熱媒体管2の間で大きい熱伝達を得ている。Heat exchange occurs between the airflow A flowing between the fins of the fins 1 and the heat medium flowing inside the heat medium pipe 2. At this time, since the fins 1 are divided into each row in the direction of the airflow A, the development of the boundary layer generated on the fin surface is divided, and due to the leading edge effect of the boundary layer, a large amount of heat is generated between the airflow A and the fins 1. Getting the transmission. Furthermore, since the heat medium pipes 2 are arranged in a staggered manner, the turbulence of the airflow A is increased, and the airflow A and the fins 1 are
A large heat transfer is obtained between the heat medium pipe 2 and the heat medium pipe 2.
発明が解決しようとする問題点
しかしながら上記のような構成では、フィン1の表面に
生じる境界層が極iに薄くなることはなく、かつ千鳥状
に配管された熱媒体管2によって乱された気流Aがフィ
ン1により逆に整流されてしまい、十分に大きい熱伝達
を得ることができないという問題点を有していた。Problems to be Solved by the Invention However, with the above configuration, the boundary layer formed on the surface of the fins 1 does not become extremely thin, and the airflow disturbed by the heat medium pipes 2 arranged in a staggered manner There was a problem in that A was reversely rectified by the fins 1, making it impossible to obtain sufficiently large heat transfer.
又、一般的にスリット3をフィン10表面に設けること
により熱伝達を向上させることができるが、比較的フィ
ンピッチaの大きいものにおいては、スリット3の高さ
bもフィンピッチaの増大に伴って大きくしなければな
らないのに反して、フィン板厚Cがコストとの兼ね合い
で従来のo、15−前後であるためにフィン加工の面か
らスリット3の高さbはフィンピッチaに対して十分に
高くすることはできず、スリット3による熱伝達の向上
は小さなものであるという問題点も有していた。Generally, heat transfer can be improved by providing the slits 3 on the surface of the fins 10, but in those with a relatively large fin pitch a, the height b of the slits 3 also increases as the fin pitch a increases. On the other hand, the fin plate thickness C is around 0,15-15mm compared to the conventional one due to cost considerations, so the height b of the slit 3 is smaller than the fin pitch a from the viewpoint of fin processing. It was not possible to make the height sufficiently high, and there was also the problem that the improvement in heat transfer by the slits 3 was small.
本発明は上記問題点に鑑み、極端に大きい熱伝達が得ら
れる熱交換器を提供するものである。In view of the above-mentioned problems, the present invention provides a heat exchanger that can obtain extremely large heat transfer.
問題点を解決するだめの手段
上記問題点を解決するために本発明の熱交換器は、気流
入口端にひねり片を多数分断して設け、かつひねシ片の
気流後流部の表面に多数のスリットを設けたフィンと、
前記フィンを貫通する熱媒体管とを備えたものである。Means for Solving the Problems In order to solve the above-mentioned problems, the heat exchanger of the present invention has a plurality of divided twisted pieces at the air inlet end, and a large number of twisted pieces on the surface of the air flow downstream part of the twisted pieces. A fin with a slit,
and a heat medium pipe passing through the fins.
作 用
本発明は上記した構成によって、フィン間を流れる気流
がひねυ片によって大きく乱され、かつフィン表面に生
じる境界層がスリットにより分断されて境界層厚さが薄
く維持されることとなる。Operation According to the above-described configuration of the present invention, the airflow flowing between the fins is greatly disturbed by the twist piece, and the boundary layer formed on the fin surface is divided by the slit, so that the thickness of the boundary layer is maintained thin.
しかも境界層を形成する気流が入口端でひねり片によっ
て乱されているため、フィンピッチが大きくてもフィン
表面に生じる境界層は薄いものとなり、スリットの高さ
がフィンピッチに対して比較的低くても十分境界層を分
断することができ、境界層厚さが薄く維持されることと
なる。Moreover, since the airflow that forms the boundary layer is disturbed by the twisted piece at the inlet end, the boundary layer formed on the fin surface is thin even if the fin pitch is large, and the height of the slit is relatively low compared to the fin pitch. The boundary layer can be sufficiently divided even when the boundary layer is thinned, and the thickness of the boundary layer can be maintained thin.
実施例
以下本発明の一実施例の熱交換器について、図面を参照
しながら説明する。EXAMPLE Hereinafter, a heat exchanger according to an example of the present invention will be described with reference to the drawings.
第1図は本発明の一実施例における熱交換器を示すもの
である。第1図において、4は多数並行に配列されたフ
ィンで、気流B方向で各列に分断されている。6はフィ
ン4の気流入口端に設けたひねシ片で、多数分断されて
設けられている。6はフィン4の表面に設けられたスリ
ットで、多数施しである。2は熱媒体管で従来の構成と
同じものである。FIG. 1 shows a heat exchanger in one embodiment of the present invention. In FIG. 1, numeral 4 denotes a large number of fins arranged in parallel, which are divided into rows in the direction of airflow B. Reference numeral 6 denotes a twist piece provided at the air inlet end of the fin 4, which is divided into many pieces. Numeral 6 denotes slits provided on the surface of the fin 4, which are provided in large numbers. Reference numeral 2 denotes a heat medium tube, which has the same structure as the conventional one.
以上のように構成された熱交換器について、以下その動
作について説明する。The operation of the heat exchanger configured as above will be described below.
フィン4のフィン間を流れる気流Bと熱媒体管2の管内
を流れる熱媒体の間で熱交換が行なわれる。その際、フ
ィン4が気流B方向で各列に分断されているため、フィ
ン表面に生じる境界層の発達を分断すると共に、千鳥状
に配管されている熱媒体管2と、フィン4の気流入口端
に設けられたひねり片6によって気流Bが犬きく乱され
ることによっても熱伝達が促進されている。更には、ス
リット6が気流Bに対してひねり片6のすぐ後流側に位
置するため、フィンピッチdが犬きくてもスリットθ付
近に生じる境界層は極めて薄いものとなり、スリット6
の高さeがフィンピッチdに対して比較的低くてもスリ
ット6は境界層内に含まれることなく境界層を分断して
境界層厚さを薄く維持することができる。Heat exchange occurs between the airflow B flowing between the fins of the fins 4 and the heat medium flowing inside the heat medium tube 2. At this time, since the fins 4 are divided into rows in the direction of the airflow B, the development of a boundary layer that occurs on the fin surface is divided, and the heat transfer pipes 2 and the air inlet of the fins 4, which are arranged in a staggered manner, are separated. Heat transfer is also promoted by the airflow B being disturbed by the twist piece 6 provided at the end. Furthermore, since the slit 6 is located immediately downstream of the twist piece 6 with respect to the airflow B, even if the fin pitch d is large, the boundary layer generated near the slit θ is extremely thin, and the slit 6
Even if the height e is relatively low with respect to the fin pitch d, the slit 6 is not included in the boundary layer and can divide the boundary layer to maintain a thin boundary layer thickness.
以上のように本実施例によれば、ひねシ片5をフィン4
の気流入口端に多数分断して設け、かつスリット6をフ
ィン4の表面に設けることにより、境界層を形成する気
流Bが入口端でひねり片6によって乱され、フィンピッ
チdが大きくてもフィン4表面に生じる境界層は薄いも
のとなり、スリット6の高さeがフィンピッチdに対し
て比較的低くてもスリット6は境界層内に含まれること
なく境界層を分断し、境界層厚さを薄く維持して極めて
大きい熱伝達を得ることができる。As described above, according to this embodiment, the twist piece 5 is connected to the fin 4.
By providing a large number of slits 6 at the air inlet end of the fin 4 and providing the slits 6 on the surface of the fin 4, the airflow B forming a boundary layer is disturbed by the twisted piece 6 at the inlet end, and even if the fin pitch d is large, the fin 4 The boundary layer formed on the surface becomes thin, and even if the height e of the slit 6 is relatively low with respect to the fin pitch d, the slit 6 is not included in the boundary layer but divides the boundary layer, and the boundary layer thickness can be kept thin for extremely high heat transfer.
発明の効果
以上のように本発明は、ひねシ片をフィンの気流入口端
に多数分断して設け、かつスリットをフィン表面に多数
設けることにより、スリットの効果をより増大させ、フ
ィン表面に生じる境界層を薄く維持して極めて大きい熱
伝達を得ることができる。Effects of the Invention As described above, the present invention further increases the effect of the slits by providing a large number of twisted pieces at the air inlet end of the fin and providing a large number of slits on the fin surface. The boundary layer can be kept thin to obtain extremely high heat transfer.
第1図は本発明の一実施例における熱交換器の斜視図、
第2図は第1図のフィンを示す要部斜視図、第3図は従
来の熱交換器の斜視図、第4図は従来の熱交換器のスリ
ット形状を示す要部斜視図である。
2・・・・・・熱媒体管、4・・・・・・フィン、5・
・・・・・ひねり片、6・・・・・・スリット。
代理人の氏名 弁理士 中 尾 敏 男 ほか1名2・
・・熱様+t−脅
4・・・フィンFIG. 1 is a perspective view of a heat exchanger in an embodiment of the present invention;
2 is a perspective view of a main part showing the fin of FIG. 1, FIG. 3 is a perspective view of a conventional heat exchanger, and FIG. 4 is a perspective view of a main part showing the slit shape of a conventional heat exchanger. 2... heat medium pipe, 4... fin, 5...
...Twist piece, 6...Slit. Name of agent: Patent attorney Toshio Nakao and 1 other person2.
...Netsu-sama + t-threat 4...Finn
Claims (1)
熱媒体管とより成り、前記フィンの気流入口端にひねり
片を多数分断して設け、かつ前記ひねり片の気流後流部
のフィン表面に多数のスリットを設けた熱交換器。It consists of a large number of fins arranged in parallel and a heat medium pipe passing through the fins, and a plurality of twisted pieces are divided and provided at the air inlet end of the fins, and on the fin surface of the airflow trailing part of the twisted pieces. A heat exchanger with many slits.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11363485A JPS61272593A (en) | 1985-05-27 | 1985-05-27 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11363485A JPS61272593A (en) | 1985-05-27 | 1985-05-27 | Heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61272593A true JPS61272593A (en) | 1986-12-02 |
Family
ID=14617204
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11363485A Pending JPS61272593A (en) | 1985-05-27 | 1985-05-27 | Heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61272593A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4997036A (en) * | 1987-11-03 | 1991-03-05 | Gea Luftkuhlergesellschaft Happel Gmbh & Co. | Heat exchanger tube |
US5421403A (en) * | 1992-01-27 | 1995-06-06 | Mitsubishi Denki Kabushiki Kaisha | Air conditioner |
US5738168A (en) * | 1995-12-08 | 1998-04-14 | Ford Motor Company | Fin tube heat exchanger |
-
1985
- 1985-05-27 JP JP11363485A patent/JPS61272593A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4997036A (en) * | 1987-11-03 | 1991-03-05 | Gea Luftkuhlergesellschaft Happel Gmbh & Co. | Heat exchanger tube |
US5421403A (en) * | 1992-01-27 | 1995-06-06 | Mitsubishi Denki Kabushiki Kaisha | Air conditioner |
US5738168A (en) * | 1995-12-08 | 1998-04-14 | Ford Motor Company | Fin tube heat exchanger |
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