JPS61243291A - Finned heat exchanger - Google Patents

Finned heat exchanger

Info

Publication number
JPS61243291A
JPS61243291A JP8383285A JP8383285A JPS61243291A JP S61243291 A JPS61243291 A JP S61243291A JP 8383285 A JP8383285 A JP 8383285A JP 8383285 A JP8383285 A JP 8383285A JP S61243291 A JPS61243291 A JP S61243291A
Authority
JP
Japan
Prior art keywords
fin
heat transfer
flat plate
heat exchanger
fins
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
JP8383285A
Other languages
Japanese (ja)
Inventor
Shigeo Aoyama
繁男 青山
Masaaki Adachi
安立 正明
Hiroyoshi Tanaka
博由 田中
Yoshiyuki Tsuda
善行 津田
Tomoaki Ando
智朗 安藤
Fumitoshi Nishiwaki
文俊 西脇
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Refrigeration Co
Matsushita Electric Industrial Co 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 Matsushita Refrigeration Co, Matsushita Electric Industrial Co Ltd filed Critical Matsushita Refrigeration Co
Priority to JP8383285A priority Critical patent/JPS61243291A/en
Publication of JPS61243291A publication Critical patent/JPS61243291A/en
Pending legal-status Critical Current

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To contrive the cost down and the improvement of heat transfer performance of the heat exchanger by a method wherein belt-type protuberances, formed continuously on the front and rear surfaces of a fin so as to be opposed to the airflow in the heat exchanger, are provided on the flat fin between heat transfer tubes. CONSTITUTION:The finned heat exchanger is formed by a method wherein the heat transfer tubes 8 are inserted vertically into the fin collars 7 of the flat plate fin 6 and the fin collars 7 and the heat transfer tubes 8 are integrated by expanding the heat transfer tubes 8 from the inside thereof. Upon expanding the tubes, the belt-type protuberances 10 are formed continuously on the front and rear surfaces of the flat plate fin 6 between the heat transfer tubes in parallel to the longitudinal direction of the fin 6 where by the flat plate fin 6, weakened in the strength thereof by providing slit type cut-ups 11, can be reinforced sufficiently and smooth expanding work of the tube may be effected. The airflow, passing between the slit type cut-ups 11 provided on the front and rear surfaces of the flat plate fin 6, collides against the belt type protuberances 10 and the flow thereof is disturbed, whereby the formation of temperature boundary layer is interferred. Accordingly, a temperature gradient on the surface of the fin is increased and heat exchange between the fins and the airflow is promoted, whereby the heat transfer coefficient may be improved.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、冷凍、あるいは空調用装置に用いるフィン付
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 finned heat exchanger used in refrigeration or air conditioning equipment.

従来の技術 従来、この種の熱交換器は第4図に示すようへ一定間隔
で平行に並べられた平板フィン群1と、このフィン群1
に直角に挿入された伝熱管群2から構成され、空気はフ
ィン群1間を矢印方向3に流動して管内流体と熱交換を
行なう構成であったこのような熱交換器大は、近年、小
型化、高性能化が要求されており、その1つとして空気
側の熱抵抗を減少させるために、例えば、第5図に示す
ようなフィン表面に適当な工夫が施されてきた。
BACKGROUND OF THE INVENTION Conventionally, this type of heat exchanger has a flat plate fin group 1 arranged in parallel at regular intervals as shown in FIG.
In recent years, such large heat exchangers have been constructed with a heat exchanger tube group 2 inserted at right angles to the fin group 1, and air flows between the fin groups 1 in the direction of the arrow 3 to exchange heat with the fluid inside the tubes. There is a demand for smaller size and higher performance, and in order to reduce the thermal resistance on the air side, appropriate improvements have been made to the fin surface, as shown in FIG. 5, for example.

この場合、フィン表面上に二側辺部を開口してスリット
状切り起し4,5を設けることによシ伝熱性能の向上を
図っている。
In this case, the heat transfer performance is improved by providing slit-like cutouts 4 and 5 with two side edges opened on the fin surface.

発明が解決しようとする問題点 しかし、このような構成ではスリット状切り起し4,6
をフィンの長手方向に平行に切り起しているため、強度
的に弱くなる傾向にあり、従って強度を増すためにはフ
ィン板厚を厚くしなければならず、これは、フィン付熱
交換器の重量増加を招いたり、コストアップ等の要因に
なるという問題があった。
Problems to be Solved by the Invention However, in such a configuration, the slit-like cutouts 4, 6
Because the fins are cut parallel to the longitudinal direction of the fins, they tend to be weak in strength. Therefore, in order to increase the strength, the fin plate thickness must be increased, and this is because the fin heat exchanger This has caused problems such as an increase in weight and an increase in cost.

そこで、本発明は、フィンの強度を向上させて、フィン
薄肉化、即ち、コストダウンを図ると共顛フィン付熱交
換器における空気側熱抵抗を減少せしめて伝熱性能の向
上を図るものである。
Therefore, the present invention aims to improve the heat transfer performance by improving the strength of the fins and reducing the thickness of the fins, in other words, reducing the cost. be.

問題点を解決するための手段 上記問題点を解決する本発明の技術的な手段法気流と対
向する突起部を表裏に連続して設けた帯状突起を伝熱管
間の平板フィン上に設けたものである。
Means for Solving the Problems Technical means of the present invention for solving the above-mentioned problems A band-shaped protrusion, in which protrusions facing the airflow are continuously provided on the front and back sides, is provided on the flat plate fin between the heat exchanger tubes. It is.

作    用 この技術的手段による作用は次のようになる。For production The effect of this technical means is as follows.

すなわち、上記のような帯状突起を設けているため、フ
ィンの強度、特にフィンの長手方向の強度が得られ、フ
ィンの薄肉化が可能になシ、フィン付熱交換器としての
コストダウンが図れる。
In other words, since the above-mentioned band-shaped protrusions are provided, the strength of the fins, especially in the longitudinal direction of the fins, can be obtained, the fins can be made thinner, and the cost of the heat exchanger with fins can be reduced. .

また、帯状突起付近を流動する気流は、帯状突起によっ
て流れが乱され、それによって、温度境界層の形成を妨
げるため、フィンと気流間の熱交換が促進され、熱伝達
率が向上する。しかも、帯状突起は連続して表裏に設け
られているため、フィンの表裏において熱伝達率が向上
する。
Further, the flow of the airflow flowing near the band-like protrusions is disturbed by the band-like protrusions, thereby preventing the formation of a temperature boundary layer, thereby promoting heat exchange between the fins and the airflow, and improving the heat transfer coefficient. Moreover, since the strip-shaped protrusions are continuously provided on the front and back sides, the heat transfer coefficient is improved on the front and back sides of the fin.

実施例 以下、本発明の一実施例を添付図面に基づいて説明する
EXAMPLE Hereinafter, an example of the present invention will be described based on the accompanying drawings.

第1図a、bに示すように、6は一定間隔で並べられ、
その間を気流が流動する平板フィン、7は平板フィンe
上にバーリング加工されたフィンカラー、8は平板フィ
ン6に直角に挿入され、その内部を冷媒が流動する伝熱
管で、この伝熱管8は平板フィン6上に千鳥状に配列さ
れている。そして、気流方向9と直角な方向に配設され
た伝熱管8間の平板フィンθ上に、気流方向9に対して
その長手方向が直角に、帯状突起1oを設けている。こ
の帯状突起10は、気流と対向する二側辺部を平板フィ
ンの平面部と連続し、突起部を表裏に連続して設けたも
のである。また、帯状突起1oの前後の平板フィンe上
には、気流と対向する二側辺部を開口したスリット状切
シ起し11が帯状突起1oの長手方向に平行に設置され
ている。
As shown in Figure 1 a and b, 6 are arranged at regular intervals,
Flat fins through which air flows, 7 is a flat fin e
Fin collars 8 with burring on the top are heat transfer tubes that are inserted perpendicularly into the flat fins 6 and through which the refrigerant flows, and the heat transfer tubes 8 are arranged in a staggered manner on the flat fins 6. A band-shaped protrusion 1o is provided on the flat plate fins θ between the heat exchanger tubes 8 disposed in a direction perpendicular to the airflow direction 9, the longitudinal direction of which is perpendicular to the airflow direction 9. The band-shaped protrusion 10 has two side portions facing the airflow that are continuous with the plane portion of the flat fin, and protrusions are provided continuously on the front and back sides. Moreover, on the flat plate fins e before and after the strip-like projection 1o, slit-shaped cut-and-raised ribs 11 with openings on two sides facing the airflow are installed parallel to the longitudinal direction of the strip-like projection 1o.

次に、こげ実施例の構成における作用を説明する。Next, the operation of the structure of the burnt embodiment will be explained.

フィン付熱交換器は、平板フィン6のフィンカラー7に
直角に伝熱管8を挿入し、その伝熱管8を内部から拡管
することによシ、フィンカラー7と伝熱管8を一体化さ
せて形成される。この拡管の際に、伝熱管8間の平板フ
ィンe上に、平板フィン6の長手方向に平行に帯状突起
10を平板フィン6の表裏に連続して設けているので、
スリット状切り起し11を設けたことによって強度的に
弱くなる平板フィンeを十分補強することができ、スム
ーズな拡管作業が可能になる。従って、帯状突起10を
設けて強度が増した分、フィン材料の薄肉化が可能とな
り、コストダウンを図れる。
The heat exchanger with fins integrates the fin collar 7 and the heat exchanger tube 8 by inserting the heat exchanger tube 8 perpendicularly into the fin collar 7 of the flat plate fin 6 and expanding the heat exchanger tube 8 from inside. It is formed. During this tube expansion, strip-like protrusions 10 are continuously provided on the front and back sides of the flat plate fins 6 in parallel to the longitudinal direction of the flat plate fins 6 on the flat plate fins e between the heat transfer tubes 8.
By providing the slit-shaped cut-and-raised portions 11, the flat plate fins e, which become weak in strength, can be sufficiently reinforced, and smooth pipe expansion work becomes possible. Therefore, since the strength is increased by providing the band-like projections 10, the fin material can be made thinner, and costs can be reduced.

また、平板フィン6の表裏に設けたスリット状切り起し
11の間を通過する気流は、帯状突起1oにぶつかって
流れが乱され、それによって、温度境界層の形成を妨げ
る。従って、フィン表面上における温度勾配が大きくな
るだめ、フィンと気流間の熱交換が促進され、熱伝達率
が向上する。
Furthermore, the airflow passing between the slit-like cutouts 11 provided on the front and back sides of the flat plate fin 6 collides with the band-like protrusion 1o and is disturbed, thereby preventing the formation of a temperature boundary layer. Therefore, as the temperature gradient on the fin surface becomes larger, heat exchange between the fin and the airflow is promoted, and the heat transfer coefficient is improved.

しかも、帯状突起1oは平板フィン6の表裏に設けられ
ているため、平板フィン6の表裏において熱伝達率が向
上する。
Moreover, since the band-like projections 1o are provided on the front and back sides of the flat plate fins 6, the heat transfer coefficient is improved on the front and back sides of the flat plate fins 6.

次に本発明の他の実施例について説明する。Next, other embodiments of the present invention will be described.

第2図vは他の実施例を示しており、この実施例では、
帯状突起10’の長手方向が気流方向9に対して傾斜角
を有するように、帯状突起10’を設けられている。ま
た、帯状突起10′の前後の平板フィン6上には、帯状
突起10′の長手方向に平行にスリット状切り起し11
′が設けられている。
FIG. 2v shows another embodiment, in which:
The strip-shaped protrusion 10' is provided such that the longitudinal direction of the strip-shaped protrusion 10' has an inclination angle with respect to the airflow direction 9. Further, on the flat plate fins 6 before and behind the band-like projection 10', slit-shaped cut-outs 11 are formed parallel to the longitudinal direction of the band-like projection 10'.
' is provided.

この場合、帯状突起10’によるフィン材料の補強効果
は、第1の実施例と殆んど変わらないか、むしろ、フィ
ンの巾方向(長手方向に直角な方向)の強度が増加する
In this case, the reinforcing effect of the fin material by the strip projections 10' is almost the same as in the first embodiment, or rather the strength in the width direction (direction perpendicular to the longitudinal direction) of the fin is increased.

また、帯状突起10′の長手方向が気流方向9に対して
傾斜角を有しているため、帯状突起10′を乗り越える
流れ12と帯状突起10′に沿う流れ13との干渉によ
って、帯状突起10’の斜め後方に渦が発生する。これ
に、第1の実施例で述べた温度境界層の形成を妨げる効
果が加わって、フィンと気流間の熱交換が促進され、熱
伝達率が向上する。
Furthermore, since the longitudinal direction of the strip protrusion 10' has an inclination angle with respect to the air flow direction 9, the flow 12 overcoming the strip protrusion 10' and the flow 13 along the strip protrusion 10' interfere with each other, causing the strip protrusion 10 to A vortex is generated diagonally behind '. In addition to this, the effect of preventing the formation of the temperature boundary layer described in the first embodiment is added to promote heat exchange between the fins and the airflow, improving the heat transfer coefficient.

なお、上記第1.第2の実施例では、帯状突起10 、
10’の前後にスリット状切り起し11゜11′を設け
ているが、これの代わりにルーパを設けても同様の効果
が得られる。
In addition, the above 1. In the second embodiment, the band-shaped protrusion 10,
Although slit-shaped cut-and-raised portions 11° 11' are provided before and after 10', the same effect can be obtained by providing a looper instead.

次に本発明の第3の実施例について説明する。Next, a third embodiment of the present invention will be described.

第3図は第3の実施例を示しており、この実施例では帯
状突起10’の気流に対向する壁に開口部14を設けて
いる。そのため、フィン材の強度面では、第1及び第2
の実施例よシ劣るが、伝熱性能面では気流が開口部14
を通じて流入出することによって得られる、いわゆる混
合効果と、開口部14の端部における境界層前線効果と
が加わって、フィンの表面熱伝達率が一層向上する。
FIG. 3 shows a third embodiment, in which an opening 14 is provided in the wall of the band-like projection 10' facing the airflow. Therefore, in terms of strength of the fin material, the first and second
Although it is inferior to the embodiment shown in FIG.
The so-called mixing effect obtained by flowing in and out through the openings 14, together with the boundary layer front effect at the ends of the openings 14, further improves the surface heat transfer coefficient of the fins.

発明の効果 本発明は、一定間隔で平行に並べられ、その間を気流が
流動する平板フィンと、この平板フィンに直角に挿入さ
れ、内部を流体が流動する伝熱管とから構成され、気流
と対向する突起部を表裏に連続して設けた帯状突起を前
記伝熱管間の平板フィン上に設けることによって、フィ
ン材の強度を向上させることができ、そのため、フィン
の薄肉化、ひいては、フィン付熱交換器としてのコスト
ダウンが図れる。また、帯状突起によって、その付近の
気流が乱され、温度境界層の形成が妨げられるため、フ
ィンと気流間の熱交換が促進され、伝熱性能が向上する
Effects of the Invention The present invention consists of flat plate fins that are arranged in parallel at regular intervals, through which air flows, and heat transfer tubes that are inserted at right angles to the flat fins, through which fluid flows, and which face the air flow. The strength of the fin material can be improved by providing a band-like projection on the flat plate fin between the heat transfer tubes, which has continuous protrusions on the front and back sides. The cost of the exchanger can be reduced. In addition, the band-like protrusions disturb the airflow in the vicinity and prevent the formation of a temperature boundary layer, thereby promoting heat exchange between the fins and the airflow and improving heat transfer performance.

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

第1図は本発明の第1の実施例によるフィン付熱交換器
の要部平面図及び要部断面図、第2図は本発明の第2の
実施例によるフィン付熱交換器の要部平面図及び要部断
面図、第3図は本発明の第3の実施例によるフィン付熱
交換器の要部斜視図、第4図は従来のフィン付熱交換器
の斜視図、第6図は同フィン付熱交換器の要部平面図及
び要部断面図である。 6・・・・・・平板フィン、8・・・・・・伝熱管、9
・・・・・・気流方向、10 、10’  、 10’
・・・・・・帯状突起、11゜11′・・・・・・スリ
うト状切シ起し、14・・・・・・開口部。 6−−−平、まフィン 蘂五図     8−伝#S菅 第 4 図 fs5図 ^           Cト ベ      6
FIG. 1 is a plan view and a sectional view of a main part of a finned heat exchanger according to a first embodiment of the present invention, and FIG. 2 is a main part of a finned heat exchanger according to a second embodiment of the present invention. 3 is a perspective view of a main part of a finned heat exchanger according to a third embodiment of the present invention; FIG. 4 is a perspective view of a conventional finned heat exchanger; FIG. 6 is a plan view and a sectional view of a main part; 2 is a plan view and a sectional view of a main part of the finned heat exchanger. 6... Flat plate fin, 8... Heat exchanger tube, 9
...Airflow direction, 10, 10', 10'
... Band-like projection, 11°11' ... Slit-like cut and rise, 14 ... Opening. 6----Tai, muffin 5th figure 8-den #S Kan No. 4 figure fs5 figure ^ C top 6

Claims (3)

【特許請求の範囲】[Claims] (1)一定間隔で平行に並べられ、その間を気流が流動
する平板フィンと、この平板フィンに直角に挿入され内
部を流体が流動する伝熱管とから構成され、気体と対向
する突起部を表裏に連続して設けた帯状突起を前記伝熱
管間の平板フィン上に設けたフィン付熱交換器。
(1) Consists of flat plate fins that are arranged in parallel at regular intervals, through which air flows, and heat transfer tubes that are inserted at right angles to the flat plate fins and through which fluid flows. A heat exchanger with fins, in which a continuous band-shaped protrusion is provided on a flat plate fin between the heat transfer tubes.
(2)帯状突起の長手方向が気流方向に対して傾斜角を
有する特許請求の範囲第1項記載のフィン付熱交換器。
(2) The finned heat exchanger according to claim 1, wherein the longitudinal direction of the band-like protrusions has an inclination angle with respect to the airflow direction.
(3)帯状突起の一部に開口部を設けた特許請求の範囲
第1項記載のフィン付熱交換器。
(3) The finned heat exchanger according to claim 1, wherein an opening is provided in a part of the band-shaped projection.
JP8383285A 1985-04-19 1985-04-19 Finned heat exchanger Pending JPS61243291A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8383285A JPS61243291A (en) 1985-04-19 1985-04-19 Finned heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8383285A JPS61243291A (en) 1985-04-19 1985-04-19 Finned heat exchanger

Publications (1)

Publication Number Publication Date
JPS61243291A true JPS61243291A (en) 1986-10-29

Family

ID=13813667

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8383285A Pending JPS61243291A (en) 1985-04-19 1985-04-19 Finned heat exchanger

Country Status (1)

Country Link
JP (1) JPS61243291A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5509469A (en) * 1994-04-19 1996-04-23 Inter-City Products Corporation (Usa) Interrupted fin for heat exchanger
US5752567A (en) * 1996-12-04 1998-05-19 York International Corporation Heat exchanger fin structure

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5509469A (en) * 1994-04-19 1996-04-23 Inter-City Products Corporation (Usa) Interrupted fin for heat exchanger
US5752567A (en) * 1996-12-04 1998-05-19 York International Corporation Heat exchanger fin structure

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