JPS6344696Y2 - - Google Patents

Info

Publication number
JPS6344696Y2
JPS6344696Y2 JP11598083U JP11598083U JPS6344696Y2 JP S6344696 Y2 JPS6344696 Y2 JP S6344696Y2 JP 11598083 U JP11598083 U JP 11598083U JP 11598083 U JP11598083 U JP 11598083U JP S6344696 Y2 JPS6344696 Y2 JP S6344696Y2
Authority
JP
Japan
Prior art keywords
cut
fins
airflow
raised
raised piece
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.)
Expired
Application number
JP11598083U
Other languages
Japanese (ja)
Other versions
JPS6027282U (en
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 filed Critical
Priority to JP11598083U priority Critical patent/JPS6027282U/en
Publication of JPS6027282U publication Critical patent/JPS6027282U/en
Application granted granted Critical
Publication of JPS6344696Y2 publication Critical patent/JPS6344696Y2/ja
Granted legal-status Critical Current

Links

Description

【考案の詳細な説明】 産業上の利用分野 本考案は、空気調和機や冷凍庫・冷蔵庫等に使
用するフインチユーブ型の熱交換器に関する。
[Detailed Description of the Invention] Industrial Application Field The present invention relates to a Finch-Ube heat exchanger used in air conditioners, freezers, refrigerators, etc.

従来例の構成とその問題点 従来の熱交換器は第1図に示すように平行に配
設されるプレート状フイン1とこれらフイン1に
貫通される冷媒管2とより構成されており、フイ
ン1にはルーバー状の切起し片3が気流に対向し
て施されている。この切起し片3によつてフイン
1が所々分断されて境界層前縁効果により、熱伝
達率の向上が計れているが、通風気流に対しては
大きな乱れを起こすことがなく、そのため熱伝達
率の向上も小さなものであるという問題点があつ
た。
Structure of the conventional example and its problems As shown in Fig. 1, the conventional heat exchanger is composed of plate-shaped fins 1 arranged in parallel and refrigerant pipes 2 penetrating through these fins 1. 1 has a louver-shaped cut and raised piece 3 facing the airflow. The fins 1 are divided in places by the cut and raised pieces 3, and the heat transfer coefficient is improved due to the leading edge effect of the boundary layer. There was a problem that the improvement in transmission rate was also small.

考案の目的 本考案はフインチユーブ型の熱交換器の、フイ
ンの熱伝達率の向上、即ち能力の向上を計ること
を目的とする。
Purpose of the invention The purpose of the invention is to improve the heat transfer coefficient of the fins of a finch tube heat exchanger, that is, to improve the capacity.

考案の構成 この目的を達成するために本考案は、プレート
フインに気流と直交する方向に長い切起し片を形
成し、この切起し片が冷媒管配列の間にあり、か
つ一面が気流と対向する様に折曲或は湾曲するこ
とにより、フインの切起し後の長穴によつてフイ
ンを分断して境界層前縁効果を得、熱伝達率の向
上を計ると共に、切起し片の一面を気流と対向す
ることによつて気流を乱し乱流促進効果を得、熱
伝達率の向上を計るものである。このように一種
の切起し片に依つて、境界層前縁効果と乱流促進
効果とが同時に得られ、熱伝達率の向上即ち能力
の向上が計れるようにしたものである。
Structure of the invention In order to achieve this object, the present invention forms a long cut and raised piece in the direction perpendicular to the air flow on the plate fin, and this cut and raised piece is located between the refrigerant pipe arrays, and one side of the cut and raised piece is arranged in a direction perpendicular to the air flow. By bending or curving the fins so as to face the fins, the long holes after the fins are cut and raised divide the fins to obtain a boundary layer leading edge effect, improving the heat transfer coefficient. By arranging one side of the strip to face the airflow, the airflow is disturbed and the turbulence promoting effect is obtained, thereby improving the heat transfer coefficient. In this way, by using a kind of cut and raised piece, the leading edge effect of the boundary layer and the effect of promoting turbulence can be obtained at the same time, and the heat transfer coefficient can be improved, that is, the performance can be improved.

実施例の説明 以下本考案の一実施例を添付図面に従い説明す
る。
DESCRIPTION OF EMBODIMENTS An embodiment of the present invention will be described below with reference to the accompanying drawings.

第3〜6図において、10はプレート状フイン
で、このフイン10が多数並行に配列され、これ
らに対して冷媒管11が直交するよう貫通せしめ
て熱交換器12を構成している。フイン10には
冷媒管11より気流上流側に位置し気流と直交す
る方向に多数の長い切起し片13を形成し、かつ
この切起し片13の一面が冷媒管11配列の間に
あり気流と対向する様に切起し片13は湾曲され
ている。また、14はフイン10に多数の切起し
片13を切起こしたことによつて形成される多数
の長穴である。この長穴14の長さ、つまり切起
し片13の長さは略冷媒管11同志のピツチより
若干大きく、このため切起し片13の先端は隣接
するフイン10の長穴14の中まで入り込んでい
る。
In FIGS. 3 to 6, reference numeral 10 denotes a plate-shaped fin, and a large number of these fins 10 are arranged in parallel, and a refrigerant pipe 11 is passed orthogonally through these fins to form a heat exchanger 12. The fins 10 have a large number of long cut and raised pieces 13 located upstream of the refrigerant pipes 11 in a direction perpendicular to the airflow, and one surface of these cut and raised pieces 13 is located between the refrigerant pipes 11 array. The cut and raised piece 13 is curved so as to face the airflow. Further, reference numeral 14 denotes a large number of elongated holes formed by cutting and raising a large number of cut and raised pieces 13 on the fin 10. The length of this elongated hole 14, that is, the length of the cut and raised piece 13, is slightly larger than the pitch between the refrigerant pipes 11, so that the tip of the cut and raised piece 13 extends into the elongated hole 14 of the adjacent fin 10. I'm getting into it.

上記構成において、切起し片13によつて形成
される多数の長穴14によつて気流に対しフイン
10は多数分断されるため、境界層前縁効果によ
り熱伝達率の向上が計れる。また、切起し片13
の一面が気流に対向し、かつ、冷媒管11配列の
間に位置しているため、気流を大きく乱し、乱流
促進効果が得られ熱伝達率の向上が計れる。しか
も、切起し片13自身も伝達面積として寄与する
ため、伝熱面積が減少するという必配も全く無い
ものである。
In the above configuration, since the fins 10 are divided into many parts from the airflow by the many elongated holes 14 formed by the cut and raised pieces 13, the heat transfer coefficient can be improved due to the leading edge effect of the boundary layer. In addition, the cut and raised piece 13
Since one side faces the airflow and is located between the arrays of refrigerant pipes 11, the airflow is greatly disturbed, a turbulence promotion effect is obtained, and the heat transfer coefficient can be improved. Furthermore, since the cut and raised pieces 13 themselves also contribute to the heat transfer area, there is no necessity for the heat transfer area to decrease at all.

従つて、切起し片13による乱流促進効果と切
起しによつてできる長穴14による境界層前縁効
果によつて、熱伝達率が著しく向上し、かつ、伝
熱面積が減少するようなことも全くないため、能
力の大巾な向上が計れるという効果が得られる。
Therefore, due to the turbulent flow promotion effect of the cut and raised pieces 13 and the leading edge effect of the boundary layer due to the elongated holes 14 formed by the cut and raised pieces, the heat transfer coefficient is significantly improved and the heat transfer area is reduced. Since there is no such thing at all, the effect of being able to measure a large improvement in ability can be obtained.

考案に効果 以上の説明からも明らかなように本考案は、プ
レートフインに気流と交直する方向に所定長さの
切起し片を形成し、この切起し片が冷媒管配列の
間にありかつ一面が気流と対向する様に折曲或は
湾曲することにより、切起し片による乱流促進効
果と、切起し片によつてできる長穴による境界層
前縁効果によつて、熱伝達率が著しく向上し、か
つ伝熱面積が減少するようなことが全く無いた
め、能力の大巾は向上が計れるという効果が得ら
れるものである。
Effect on the invention As is clear from the above explanation, the present invention has a cut and raised piece of a predetermined length formed on the plate fin in a direction perpendicular to the airflow, and this cut and raised piece is placed between the refrigerant pipe arrays. In addition, by bending or curving one side so as to face the airflow, heat is reduced by the effect of promoting turbulent flow due to the cut and raised pieces and the leading edge effect of the boundary layer due to the elongated hole formed by the cut and raised pieces. Since the transfer rate is significantly improved and the heat transfer area is not reduced at all, the effect is that the capability can be greatly improved.

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

第1図は従来の熱交換器の斜視図、第2図は第
1図の要部斜視図、第3図は本考案の熱交換器の
一実施例を示す斜視図、第4図は同熱交換器の要
部斜視図、第5図は第3図の正面図、第6図は第
4図の側面図である。 10……プレートフイン、11……冷媒管、1
3……切起し片、14……長穴。
Fig. 1 is a perspective view of a conventional heat exchanger, Fig. 2 is a perspective view of the main part of Fig. 1, Fig. 3 is a perspective view showing an embodiment of the heat exchanger of the present invention, and Fig. 4 is the same. 5 is a front view of FIG. 3, and FIG. 6 is a side view of FIG. 4. 10...Plate fin, 11...Refrigerant pipe, 1
3... cut and raised piece, 14... long hole.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 多数並行に配列されるプレートフインと、この
フインを貫通する冷媒管より成り、前記プレート
フインに気流と直交する方向に所定長さの切起し
片を形成し、この切起し片を前記冷媒管の配列の
間にあり、かつ一面が気流と対向する様に折曲あ
るいは湾曲した熱交換器。
Consisting of a large number of plate fins arranged in parallel and a refrigerant pipe passing through the fins, a cut and raised piece of a predetermined length is formed on the plate fin in a direction perpendicular to the air flow, and this cut and raised piece is used to direct the refrigerant to the plate fin. A heat exchanger that is located between an array of tubes and is bent or curved so that one side faces the airflow.
JP11598083U 1983-07-25 1983-07-25 Heat exchanger Granted JPS6027282U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11598083U JPS6027282U (en) 1983-07-25 1983-07-25 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11598083U JPS6027282U (en) 1983-07-25 1983-07-25 Heat exchanger

Publications (2)

Publication Number Publication Date
JPS6027282U JPS6027282U (en) 1985-02-23
JPS6344696Y2 true JPS6344696Y2 (en) 1988-11-21

Family

ID=30267541

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11598083U Granted JPS6027282U (en) 1983-07-25 1983-07-25 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS6027282U (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5337402B2 (en) * 2008-05-14 2013-11-06 パナソニック株式会社 Finned tube heat exchanger
US11781812B2 (en) 2016-08-31 2023-10-10 Brazeway, Inc. Fin enhancements for low Reynolds number airflow
US10578374B2 (en) * 2016-08-31 2020-03-03 Brazeway, Inc. Fin enhancements for low Reynolds number airflow

Also Published As

Publication number Publication date
JPS6027282U (en) 1985-02-23

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