JPH0599581A - Heat exchanger and manufacture thereof - Google Patents

Heat exchanger and manufacture thereof

Info

Publication number
JPH0599581A
JPH0599581A JP22232891A JP22232891A JPH0599581A JP H0599581 A JPH0599581 A JP H0599581A JP 22232891 A JP22232891 A JP 22232891A JP 22232891 A JP22232891 A JP 22232891A JP H0599581 A JPH0599581 A JP H0599581A
Authority
JP
Japan
Prior art keywords
heat exchange
plate
heat exchanger
exchange tubes
exchange 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.)
Withdrawn
Application number
JP22232891A
Other languages
Japanese (ja)
Inventor
Yasuhiko Tanaka
庸彦 田中
Etsuro Kubota
悦郎 久保田
Akinori Ogasawara
明徳 小笠原
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.)
Nippon Light Metal Co Ltd
Original Assignee
Nippon Light Metal 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 Nippon Light Metal Co Ltd filed Critical Nippon Light Metal Co Ltd
Priority to JP22232891A priority Critical patent/JPH0599581A/en
Publication of JPH0599581A publication Critical patent/JPH0599581A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular 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
    • F28F1/24Tubular 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
    • F28F1/32Tubular 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
    • 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
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/047Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag
    • F28D1/0477Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag
    • F28D1/0478Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag the conduits having a non-circular cross-section
    • 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
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/053Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight
    • F28D1/0535Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being straight the conduits having a non-circular cross-section
    • F28D1/05366Assemblies of conduits connected to common headers, e.g. core type radiators
    • F28D1/05383Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To improve heat exchanging performance of a heat exchanger having platelike fins and heat exchanging tubes. CONSTITUTION:A plurality of platelike fins 3 to be arranged at suitable intervals and heat exchanging tubes 2 arranged in a plurality of stages are mounted in a contact crossing state. Flat parts 4 are formed at positions of the tubes 2 in contact with the fins 3. Each fin 3 has a bent contact piece 9 in close contact with the part 4 of the tube 2, and the fin is formed of a bent wavy plate between the tubes 2.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は熱交換器及びその製造
方法に関するもので、更に詳細には、例えば自動車用空
調機器あるいは家屋用空調機器等に使用される熱交換器
で、適宜間隔をおいて配列される複数の板状フィンと複
数段の熱交換管を接触交差した熱交換器及びその製造方
法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger and a method for manufacturing the same, and more specifically, it is a heat exchanger used in, for example, an air conditioner for automobiles or an air conditioner for houses, which is appropriately spaced. The present invention relates to a heat exchanger in which a plurality of plate-shaped fins arranged in a row and a plurality of stages of heat exchange tubes are in contact with each other and a manufacturing method thereof.

【0002】[0002]

【従来の技術】従来のこの種の熱交換器として、図12
に示すように、一定間隔をおいて平行に配列された複数
の平板状フィンaと、これら平板状フィンaを貫通する
断面円形の熱交換管bとからなる熱交換器が知られてい
る。この熱交換器は、円形熱交換管bを平板状フィンa
に穿設した透孔(図示せず)に挿入した後、円形熱交換
管bの内径より僅かに大きい径を有する円筒棒を円形熱
交換管b内に挿入して拡管して、平板状フィンaと円形
熱交換管bとを密着させることにより、製造される。
2. Description of the Related Art As a conventional heat exchanger of this type, FIG.
As shown in FIG. 2, a heat exchanger is known which includes a plurality of flat plate-shaped fins a arranged in parallel at regular intervals, and a heat exchange tube b having a circular cross section that penetrates these flat plate-shaped fins a. In this heat exchanger, a circular heat exchange tube b is connected to a flat plate fin a.
After being inserted into a through hole (not shown) formed in the circular heat exchange tube b, a cylindrical rod having a diameter slightly larger than the inner diameter of the circular heat exchange tube b is inserted into the circular heat exchange tube b to expand the flat plate fin. It is manufactured by bringing a into close contact with the circular heat exchange tube b.

【0003】また、別の熱交換器として、図13に示す
ように、上記円形熱交換管bに変えて断面偏平状の熱交
換管cを有する熱交換器が知られている。このように断
面偏平状の熱交換管cを用いることにより、円形熱交換
管aを有する熱交換器では温度調節される流体である空
気側の圧力損失を低下させるのを防止することができ
る。
As another heat exchanger, as shown in FIG. 13, a heat exchanger having a heat exchange tube c having a flat cross section in place of the circular heat exchange tube b is known. By using the heat exchange tube c having a flat cross section in this way, it is possible to prevent the pressure loss on the air side, which is the fluid whose temperature is adjusted, from decreasing in the heat exchanger having the circular heat exchange tube a.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、前者す
なわち、円形熱交換管bを有する熱交換器においては、
熱交換管が円形断面であるため、空気側抵抗が大きく、
熱交換器としての性能を確保するための風量を得るため
には大きなファンが必要であった。そのため、熱交換器
及びファンで生じる騒音の問題があった。また、熱交換
管間の間隔を大きくすることにより、空気側の抵抗を小
さくすることは可能であるが、必要な熱交換性能を得る
ためには熱交換器が大きくなるという問題があった。
However, in the former case, that is, in the heat exchanger having the circular heat exchange tubes b,
Since the heat exchange tube has a circular cross section, the air side resistance is large,
A large fan was required to obtain the air volume to secure the performance as a heat exchanger. Therefore, there is a problem of noise generated in the heat exchanger and the fan. Further, it is possible to reduce the resistance on the air side by increasing the distance between the heat exchange tubes, but there is a problem that the heat exchanger becomes large in order to obtain the required heat exchange performance.

【0005】また、後者すなわち熱交換管を偏平状に形
成したものにおいては、円形熱交換管bに比べて空気側
抵抗の損失を少なくすることはできるが、偏平の熱交換
管は製品として耐圧性能を確保するために、内部に柱を
有する断面形状とする必要がある。したがって、断面円
形の熱交換管のような簡便な拡管手段がなかったため、
偏平状熱交換管cと平板状フィンaとの間の密着性が悪
くなり、そのため、熱抵抗が高くなると共に、熱交換効
率が低くなり、必要な熱交換性能を得るためには熱交換
器を大きくせざるを得なかった。
In the latter case, in which the heat exchange tube is formed in a flat shape, the loss of resistance on the air side can be reduced as compared with the circular heat exchange tube b, but the flat heat exchange tube is a pressure resistant product. In order to secure the performance, it is necessary to have a cross-sectional shape having columns inside. Therefore, since there was no simple expansion means such as a heat exchange tube with a circular cross section,
The adhesion between the flat heat exchange tube c and the flat fin a becomes poor, and therefore the heat resistance becomes high and the heat exchange efficiency becomes low. In order to obtain the necessary heat exchange performance, the heat exchanger is required. I had no choice but to increase.

【0006】この発明は上記事情に鑑みなされたもの
で、熱交換管とフィンとの密着性を良好にすると共に、
熱交換性能を良好にした小型でかつ簡単に製造できる熱
交換器及びその製造方法を提供することを目的とするも
のである。
The present invention has been made in view of the above circumstances, and improves the adhesion between the heat exchange tubes and the fins.
It is an object of the present invention to provide a small-sized heat exchanger which has excellent heat exchange performance and can be easily manufactured, and a manufacturing method thereof.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
に、この発明の第1の熱交換器は、適宜間隔をおいて配
列される複数の板状フィンと、上記板状フィンと接触交
差すると共に互いに複数段状に配列される熱交換管とを
具備し、上記熱交換管における上記板状フィンと接触す
る部位を平坦状に形成し、上記板状フィンは、上記熱交
換管の平坦部と密着する折曲接触片を有すると共に、熱
交換管間において屈曲する波形板にて形成してなるもの
である。
In order to achieve the above object, a first heat exchanger of the present invention comprises a plurality of plate-shaped fins arranged at appropriate intervals and a contact intersection of the plate-shaped fins. And heat exchanging tubes arranged in a plurality of stages with each other, the portion of the heat exchanging tube that comes into contact with the plate fins is formed flat, and the plate fins are flat in the heat exchanging tubes. It has a bent contact piece that comes into close contact with the portion and is formed by a corrugated plate that bends between the heat exchange tubes.

【0008】また、この発明の第2の熱交換器の製造方
法は、上記第1の発明の熱交換器の製造方法において、
互いに平行に配列される熱交換管に、板状フィンの折曲
接触片を遊嵌させて複数の板状フィンを互いに平行に傾
斜状に配列した後、上記板状フィンを上記熱交換管が近
接する方向に押圧して上記折曲接触片を熱交換管の平坦
部に密着することを特徴とするものである。
A second heat exchanger manufacturing method according to the present invention is the same as the heat exchanger manufacturing method according to the first invention.
After the bent contact pieces of the plate-shaped fins are loosely fitted to the heat exchange tubes arranged in parallel with each other to arrange the plurality of plate-shaped fins in an inclined shape parallel to each other, the plate-shaped fins are connected to each other by the heat-exchange tubes. It is characterized in that the bent contact piece is brought into close contact with the flat portion of the heat exchange tube by pressing in the direction of approaching.

【0009】この発明において、上記熱交換管は複数段
状に配列されるものであれば、複数の熱交換管を互いに
平行に配列したもの、あるいは蛇行状に屈曲されるもの
のいずれであっても差し支えない。また、熱交換管は板
状フィンと接触する部位に平坦部を有するものであれ
ば、その形状は任意のものでよく、例えば内部に複数の
区画通路を有する偏平パイプを使用することができる。
この偏平パイプは例えばアルミニウム合金製押出形材に
て形成することができる。
In the present invention, as long as the heat exchange tubes are arranged in a plurality of stages, the heat exchange tubes may be arranged in parallel with each other or bent in a meandering shape. It doesn't matter. Further, the heat exchange tube may have any shape as long as it has a flat portion at a portion in contact with the plate fin, and for example, a flat pipe having a plurality of partition passages therein can be used.
This flat pipe can be formed of, for example, an extruded aluminum alloy profile.

【0010】上記板状フィンは、上記熱交換管の平坦部
と接触する折曲接触片を有すると共に、熱交換管間にお
いて屈曲する波形板にて形成されていれば、折曲接触片
の折曲方向は任意でよく、また、熱交換管間の屈曲部は
1以上であれば複数の屈曲部を有するものであってもよ
い。
The plate fin has a bent contact piece that comes into contact with the flat portion of the heat exchange tube, and if it is formed by a corrugated plate that bends between the heat exchange tubes, the bent contact piece is folded. The bending direction may be arbitrary, and the bending portion between the heat exchange tubes may have a plurality of bending portions as long as the bending portion is one or more.

【0011】[0011]

【作用】上記のように構成することにより、板状フィン
の折曲接触片と熱交換管の平坦部とが密着するので、熱
抵抗を小さくでき、熱交換効率を高めることができる。
したがって、同一の熱交換性能において熱交換器を小型
化することができる。
With the above construction, the bent contact piece of the plate-shaped fin and the flat portion of the heat exchange tube are in close contact with each other, so that the heat resistance can be reduced and the heat exchange efficiency can be improved.
Therefore, the heat exchanger can be downsized with the same heat exchange performance.

【0012】また、熱交換管間において板状フィンが屈
曲する波形状とすることにより、板状フィンの強度を高
めることができると共に、温調用流体との接触面積の増
大による熱交換効率の向上が図れる。
Further, by making the plate-shaped fin bend between the heat exchange tubes, the strength of the plate-shaped fin can be increased, and the heat exchange efficiency is improved by increasing the contact area with the temperature control fluid. Can be achieved.

【0013】[0013]

【実施例】以下にこの発明の実施例について詳細に説明
する。
Embodiments of the present invention will be described in detail below.

【0014】◎第一実施例 図1はこの発明の熱交換器の第一実施例の斜視図、図2
はその要部拡大断面斜視図が示されている。
First Embodiment FIG. 1 is a perspective view of a first embodiment of the heat exchanger of the present invention, FIG.
The main part is shown in an enlarged sectional perspective view.

【0015】この発明の熱交換器は、互いに間隔をおい
て対峙する一対のヘッダーパイプ1,1と、これらヘッ
ダーパイプ1,1に接続する複数段状に配列される偏平
状の熱交換管2,2…と、これら偏平状熱交換管2,2
…と接触交差すべく直交状に配列されると共に一定の間
隔をおいて互いに平行な複数の板状フィン3,3…とで
構成されている。
The heat exchanger of the present invention comprises a pair of header pipes 1 and 1 facing each other with a space therebetween, and flat heat exchange pipes 2 connected to the header pipes 1 and 1 and arranged in a plurality of stages. , 2 ... and these flat heat exchange tubes 2, 2
.. and a plurality of plate-like fins 3, 3 ... Which are arranged orthogonally so as to intersect with each other and are parallel to each other at a constant interval.

【0016】この場合、熱交換管2は、表裏面に平坦部
4を有する熱交換管本体5の内部に複数の区画壁6,6
…によって区画される複数の熱媒体通路7,7…を有す
るアルミニウム合金(A1050)製の押出形材にて形
成されている。
In this case, the heat exchange tube 2 has a plurality of partition walls 6, 6 inside a heat exchange tube body 5 having flat portions 4 on the front and back surfaces.
It is formed of an extruded profile made of an aluminum alloy (A1050) having a plurality of heat medium passages 7, 7 ...

【0017】板状フィン3は、熱交換管2を貫挿する偏
平楕円形の透孔8の縁部において熱交換管2の平坦部4
に密着する折曲接触片9を有すると共に、熱交換管2,
2間において屈曲する波形板にて形成されている(図3
参照)。なおこの場合、板状フィン3の屈曲部は1つで
あるが、図4に示すように、熱交換管2,2間において
更に“く”字状に屈曲することもでき、このように
“く”字状の屈曲部10を設けることにより、板状フィ
ン3の強度を更に強固にすることができる。また、板状
フィン3を熱交換管2,2間においてのみ屈曲させる構
造であってもよい(図5参照)。
The plate-shaped fin 3 has a flat portion 4 of the heat exchange tube 2 at an edge portion of a flat elliptical through hole 8 through which the heat exchange tube 2 is inserted.
Has a bent contact piece 9 that closely adheres to the heat exchange tube 2,
It is formed by a corrugated plate that bends between two (Fig. 3
reference). In this case, the plate-shaped fin 3 has only one bent portion, but as shown in FIG. 4, it can be further bent into a "dogleg" shape between the heat exchange tubes 2 and 2. By providing the V-shaped bent portion 10, the strength of the plate fin 3 can be further strengthened. Alternatively, the plate fin 3 may be bent only between the heat exchange tubes 2 and 2 (see FIG. 5).

【0018】◎第二実施例 図6はこの発明の熱交換器の第二実施例の斜視図、図7
は図6のVII−VII線に沿う拡大断面図が示されてい
る。
Second Embodiment FIG. 6 is a perspective view of a second embodiment of the heat exchanger according to the present invention, and FIG.
Is an enlarged sectional view taken along the line VII-VII in FIG.

【0019】第二実施例における熱交換器は板状フィン
の一側に設けた切欠溝内に熱交換管を挿入させるように
した場合である。すなわち、上記第一実施例では板状フ
ィン3に設けた偏平楕円形状の透孔8に熱交換管2を貫
通させた状態で板状フィン3と熱交換管2とを直交状に
接触交差させているが、この第二実施例においては波板
状フィン3に設けた偏平楕円形状の切欠溝11の開口部
を介して熱交換管2を挿入すると共に、切欠溝11の縁
部に折曲された接触片9を熱交換管2の平坦部4に密着
して、板状フィン3と熱交換管2とを直交状に接触交差
させるようにした場合である。
The heat exchanger in the second embodiment is a case in which the heat exchange tube is inserted into a notch groove provided on one side of the plate-shaped fin. That is, in the first embodiment described above, the plate fins 3 and the heat exchange tubes 2 are made to contact each other in an orthogonal manner in a state where the heat exchange tubes 2 penetrate through the flat elliptical through holes 8 provided in the plate fins 3. However, in the second embodiment, the heat exchange tube 2 is inserted through the opening of the flat elliptical cutout groove 11 provided in the corrugated fin 3, and the edge of the cutout groove 11 is bent. This is a case where the contact piece 9 thus formed is brought into close contact with the flat portion 4 of the heat exchange tube 2 so that the plate-shaped fins 3 and the heat exchange tube 2 come into contact with each other in an orthogonal manner.

【0020】なお、図7において、符号12は板状フィ
ン3に設けられた空気側熱伝達率向上兼補強用切起し部
である。なお、第二実施例において、その他の部分は上
記第一実施例と同じであるので、同一部分には同一符号
を付してその説明は省略する。
In FIG. 7, reference numeral 12 is a cut-and-raised portion provided on the plate-shaped fin 3 for improving the air-side heat transfer coefficient and for reinforcing. Since the other parts of the second embodiment are the same as those of the first embodiment, the same parts are designated by the same reference numerals and the description thereof will be omitted.

【0021】◎第三実施例 図8はこの発明の熱交換器の第三実施例の斜視図が示さ
れている。
Third Embodiment FIG. 8 shows a perspective view of a third embodiment of the heat exchanger of the present invention.

【0022】第三実施例における熱交換器は蛇行状の熱
交換管に板状フィンを接触交差させるようにした場合で
ある。すなわち、蛇行状に屈曲された断面が偏平楕円形
状の熱交換管2の複数段部を、波板状フィン3の一側に
設けられた偏平楕円形状の切欠溝11の開口部から挿入
して、蛇行状熱交換管2と板状フィン3とを接触交差さ
せるようにした場合である。
The heat exchanger according to the third embodiment is a case where plate-like fins are made to contact and intersect with a meandering heat exchange tube. That is, a plurality of stepped portions of the heat exchange tube 2 bent in a meandering shape and having a flat elliptical cross section are inserted from the openings of the flat elliptical cutout grooves 11 provided on one side of the corrugated fin 3. This is a case where the meandering heat exchange tube 2 and the plate-like fin 3 are in contact with each other and intersect with each other.

【0023】なお、第三実施例において、その他の部分
は上記第一実施例及び第二実施例と同じであるので、同
一部分には同一符号を付してその説明は省略する。
Since the other parts of the third embodiment are the same as those of the first and second embodiments, the same parts are designated by the same reference numerals and the description thereof will be omitted.

【0024】次に、この発明の熱交換器の製造方法につ
いて図9ないし図11を参照して説明する。
Next, a method of manufacturing the heat exchanger of the present invention will be described with reference to FIGS. 9 to 11.

【0025】上記第一実施例で説明した熱交換器を製造
する場合について説明すると、まず、複数の熱交換管
2,2…を一定間隔をおいて平行に配列し、これら熱交
換管2,2…を板状フィン3の透孔8内を貫通するよう
に板状フィン3の透孔8を順次熱交換管2,2…に遊嵌
する(図9参照)。この際、透孔8の縁部に折曲された
折曲接触片9のテーパ部9aの拡開側から熱交換管2を
挿入する方が好ましい。また、ここでは平行に配列され
た熱交換管2,2…に対して板状フィン3を挿入させる
ようにしているが、逆に平行に配列された板状フィン
3,3…の透孔8に熱交換管2を貫通させるようにして
もよい。
The case of manufacturing the heat exchanger described in the first embodiment will be described. First, a plurality of heat exchange tubes 2, 2 ... Are arranged in parallel at regular intervals, and the heat exchange tubes 2, 2. The through holes 8 of the plate fin 3 are sequentially loosely fitted into the heat exchange tubes 2, 2 so as to penetrate the inside of the through hole 8 of the plate fin 3 (see FIG. 9). At this time, it is preferable to insert the heat exchange tube 2 from the opening side of the tapered portion 9a of the bent contact piece 9 bent at the edge of the through hole 8. Further, here, the plate-like fins 3 are inserted into the heat exchange tubes 2, 2 ... Arranged in parallel, but the through holes 8 of the plate-like fins 3, 3 ... Arranged in parallel are opposite. Alternatively, the heat exchange tube 2 may be passed through.

【0026】上記のようにして熱交換管2,2…と、板
状フィン3,3…とを直交状に接触交差させた後、図1
1に示すように、熱交換管2,2…の間隔が互いに近接
する方向に屈曲角度約75度から屈曲角度約65度にな
るように圧縮荷重Pを加えると、折曲接触片9が熱交換
管2の平坦部4に密着する。具体的には、熱交換管2の
管の厚さCを2mm、板状フィン3の屈曲角度Aを75
度、熱交換管2,2間の距離を10.7mm、透孔8の幅
Dを2.1mmとして圧縮荷重Pを加えたところ、以下の
ようになった。
After the heat exchange tubes 2, 2 ... And the plate-like fins 3, 3 ...
As shown in FIG. 1, when a compressive load P is applied in such a direction that the intervals of the heat exchange tubes 2, 2 ... It comes into close contact with the flat portion 4 of the exchange tube 2. Specifically, the thickness C of the heat exchange tube 2 is 2 mm, and the bending angle A of the plate fin 3 is 75 mm.
When the distance between the heat exchange tubes 2 and 2 was 10.7 mm and the width D of the through hole 8 was 2.1 mm and a compressive load P was applied, the result was as follows.

【0027】すなわち、屈曲角度Bが65度、熱交換管
2,2間の距離が10.0mm、そして、透孔8の幅が
1.97mmとなるため熱交換管2と板状フィン3とは強
固に密着する。
That is, the bending angle B is 65 degrees, the distance between the heat exchange tubes 2 and 2 is 10.0 mm, and the width of the through hole 8 is 1.97 mm, so that the heat exchange tube 2 and the plate-like fins 3 are Adheres tightly.

【0028】上記のようにして熱交換管2,2…と板状
フィン3,3…とを接触交差状に密着させた後、外面に
ろう材がクラッドされたアルミニウム合金製ヘッダーパ
イプ1,1に、熱交換管2の端部を挿入し、そして、熱
交換管2とヘッダーパイプ1をろう付けして熱交換器の
組立て作業は完了する。この際、ろう付け方法は任意の
方法でよく、例えばトーチろう付け、高周波ろう付け、
炉中ろう付け等の手段で行うことができる。
After the heat exchange tubes 2, 2 and the plate-like fins 3, 3 are brought into close contact with each other in a contact-crossing manner as described above, an aluminum alloy header pipe 1, 1 having a brazing material clad on the outer surface thereof. Then, the end portion of the heat exchange tube 2 is inserted, and the heat exchange tube 2 and the header pipe 1 are brazed to complete the assembly work of the heat exchanger. At this time, any brazing method may be used, such as torch brazing, high frequency brazing,
It can be performed by means such as brazing in a furnace.

【0029】一方、上記第二実施例及び第三実施例の熱
交換器を製造する場合には、以下の手順で製造する。こ
こでは第三実施例の熱交換器の製造方法について説明す
る。
On the other hand, when manufacturing the heat exchangers of the second and third embodiments, the following procedure is used. Here, a method of manufacturing the heat exchanger of the third embodiment will be described.

【0030】まず、蛇行状に屈曲された熱交換管2を偏
平楕円形状の切欠溝11内に挿入しながら板状フィン3
を一定間隔に平行に配列する。次に、熱交換管2の間隔
が近接する方向に屈曲角度約75度から屈曲角度約65
度になるように圧縮荷重Pを加えて折曲接触片9を熱交
換管2の平坦部4に密着する。具体的には、熱交換管2
の管の厚さCを5mm、板状フィン3の屈曲角度Aを80
度、熱交換管2の間隔を16.8mm、切欠溝11の幅D
を5.2mmとして圧縮荷重Pを加えたところ、屈曲角度
Bが70度、熱交換管2の間隔が16.0mm、切欠溝1
1の幅Dが4.96mmとなって折曲接触片9が熱交換管
2の平坦部4に強固に密着する。そして、上述と同様に
熱交換管2の端部をヘッダーパイプ1に挿入した後、ろ
う付けして熱交換器の組立て作業は完了する。
First, the plate-shaped fin 3 is inserted while inserting the heat exchange tube 2 bent in a meandering shape into the flat elliptical notch groove 11.
Are arranged in parallel at regular intervals. Next, the bending angle of about 75 degrees to the bending angle of about 65 in the direction in which the intervals of the heat exchange tubes 2 approach
The bending contact piece 9 is brought into close contact with the flat portion 4 of the heat exchange tube 2 by applying a compressive load P so as to be constant. Specifically, the heat exchange tube 2
The thickness C of the tube is 5 mm, and the bending angle A of the plate fin 3 is 80
Degree, the distance between the heat exchange tubes 2 is 16.8 mm, and the width D of the notch groove 11 is
When a compressive load P was applied with 5.2 mm, the bending angle B was 70 degrees, the distance between the heat exchange tubes 2 was 16.0 mm, and the notch groove 1
The width D of 1 becomes 4.96 mm, and the bent contact piece 9 firmly adheres to the flat portion 4 of the heat exchange tube 2. Then, similarly to the above, after inserting the end portion of the heat exchange pipe 2 into the header pipe 1, brazing is performed to complete the assembly work of the heat exchanger.

【0031】[0031]

【発明の効果】以上に説明したように、この発明は上記
のように構成されているので、以下のような効果が得ら
れる。
As described above, since the present invention is constructed as described above, the following effects can be obtained.

【0032】1)請求項1記載の熱交換器によれば、板
状フィンの折曲接触片を熱交換管の平坦部に密着すると
共に、板状フィンを熱交換管間において屈曲する波形板
にて形成するので、熱抵抗を小さくできると共に、熱交
換効率を高めることができ、同一の熱交換性能を有する
熱交換器において小型化することができる。また、板状
フィンの強度を高めることができると共に、堅牢な構造
とすることができる。更には、温調用流体の抵抗を小さ
くすることができるので、騒音の防止が図れる。
1) According to the heat exchanger of the first aspect, the corrugated plate in which the bent contact piece of the plate-shaped fin is brought into close contact with the flat portion of the heat-exchange tube and the plate-shaped fin is bent between the heat-exchange tubes. Since it is formed by, the heat resistance can be reduced, the heat exchange efficiency can be improved, and the heat exchanger having the same heat exchange performance can be downsized. In addition, the strength of the plate-shaped fins can be increased and a robust structure can be obtained. Furthermore, since the resistance of the temperature control fluid can be reduced, noise can be prevented.

【0033】2)請求項2記載の熱交換器の製造方法に
よれば、互いに平行に配列される熱交換管に、板状フィ
ンの折曲接触片を遊嵌させて複数の板状フィンを互いに
平行に傾斜状に配列した後、板状フィンを熱交換管が近
接する方向に押圧して折曲接触片を熱交換管の平坦部に
密着するので、簡単な作業によって熱交換性能の高い熱
交換器を製造することができる。
2) According to the method of manufacturing a heat exchanger of claim 2, the bent contact pieces of the plate-shaped fins are loosely fitted to the heat exchange tubes arranged in parallel with each other to form a plurality of plate-shaped fins. After arranging the fins parallel to each other in an inclined shape, the plate-shaped fins are pressed in the direction in which the heat exchange tubes approach each other, and the bent contact pieces are brought into close contact with the flat portion of the heat exchange tubes. A heat exchanger can be manufactured.

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

【図1】この発明の熱交換器の第一実施例を示す斜視図
である。
FIG. 1 is a perspective view showing a first embodiment of a heat exchanger of the present invention.

【図2】図1の要部を拡大して示す断面斜視図である。2 is a cross-sectional perspective view showing an enlarged main part of FIG. 1. FIG.

【図3】図2の III−III 線に沿う断面図である。FIG. 3 is a sectional view taken along line III-III in FIG.

【図4】この発明における板状フィンの別の形態を示す
断面図である。
FIG. 4 is a cross-sectional view showing another form of the plate-shaped fin according to the present invention.

【図5】この発明における板状フィンの更に別の形態を
示す断面図である。
FIG. 5 is a cross-sectional view showing still another form of the plate-shaped fin according to the present invention.

【図6】この発明の熱交換器の第二実施例を示す斜視図
である。
FIG. 6 is a perspective view showing a second embodiment of the heat exchanger of the present invention.

【図7】図6のVII−VII線に沿う断面図である。7 is a sectional view taken along the line VII-VII in FIG.

【図8】この発明の熱交換器の第三実施例を示す斜視図
である。
FIG. 8 is a perspective view showing a third embodiment of the heat exchanger of the present invention.

【図9】この発明における熱交換管と板状フィンとの取
付状態を示す説明図である。
FIG. 9 is an explanatory view showing a mounting state of a heat exchange tube and a plate-like fin in the present invention.

【図10】熱交換管と板状フィンとの密着前の状態を示
す説明図である。
FIG. 10 is an explanatory diagram showing a state before the heat exchange tube and the plate fin are brought into close contact with each other.

【図11】熱交換管と板状フィンとの密着状態を示す説
明図である。
FIG. 11 is an explanatory diagram showing a contact state between a heat exchange tube and a plate fin.

【図12】従来の熱交換器を示す斜視図である。FIG. 12 is a perspective view showing a conventional heat exchanger.

【図13】従来の別の熱交換器を示す斜視図である。FIG. 13 is a perspective view showing another conventional heat exchanger.

【符号の説明】[Explanation of symbols]

2 熱交換管 3 板状フィン 4 平坦部 8 透孔 9 折曲接触片 11 切欠溝 2 heat exchange tube 3 plate-like fin 4 flat part 8 through hole 9 bent contact piece 11 notch groove

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成4年10月14日[Submission date] October 14, 1992

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】発明の名称[Name of item to be amended] Title of invention

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【発明の名称】 熱交換器及びその製造方法Title: Heat exchanger and method for manufacturing the same

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 適宜間隔をおいて配列される複数の板状
フィンと、上記板状フィンと接触交差すると共に互いに
複数段状に配列される熱交換管とを具備し、 上記熱交換管における上記板状フィンと接触する部位を
平坦状に形成し、 上記板状フィンは、上記熱交換管の平坦部と密着する折
曲接触片を有すると共に、熱交換管間において屈曲する
波形板にて形成してなることを特徴とする熱交換器。
1. A heat exchange tube comprising: a plurality of plate-shaped fins arranged at appropriate intervals; and heat exchange tubes arranged in a plurality of stages and contacting and intersecting with the plate-shaped fins. The portion that comes into contact with the plate-shaped fins is formed into a flat shape, and the plate-shaped fins have bent contact pieces that come into close contact with the flat portions of the heat exchange tubes, and are formed by corrugated plates that bend between the heat exchange tubes. A heat exchanger characterized by being formed.
【請求項2】 請求項1記載の熱交換器の製造方法にお
いて、 互いに平行に配列される熱交換管に、板状フィンの折曲
接触片を遊嵌させて複数の板状フィンを互いに平行に傾
斜状に配列した後、上記板状フィンを上記熱交換管が近
接する方向に押圧して上記折曲接触片を熱交換管の平坦
部に密着することを特徴とする熱交換器の製造方法。
2. The method of manufacturing a heat exchanger according to claim 1, wherein the bent contact pieces of the plate-shaped fins are loosely fitted to the heat exchange tubes arranged in parallel with each other so that the plurality of plate-shaped fins are parallel to each other. After arranging the plate-shaped fins in a slanting manner, the plate-shaped fins are pressed in the direction in which the heat exchange tubes approach each other, and the bent contact pieces are brought into close contact with the flat portion of the heat exchange tubes. Method.
JP22232891A 1991-08-08 1991-08-08 Heat exchanger and manufacture thereof Withdrawn JPH0599581A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22232891A JPH0599581A (en) 1991-08-08 1991-08-08 Heat exchanger and manufacture thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22232891A JPH0599581A (en) 1991-08-08 1991-08-08 Heat exchanger and manufacture thereof

Publications (1)

Publication Number Publication Date
JPH0599581A true JPH0599581A (en) 1993-04-20

Family

ID=16780632

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22232891A Withdrawn JPH0599581A (en) 1991-08-08 1991-08-08 Heat exchanger and manufacture thereof

Country Status (1)

Country Link
JP (1) JPH0599581A (en)

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JP2005342602A (en) * 2004-06-02 2005-12-15 Nichias Corp Corrugated plate laminated body filter
US8322408B2 (en) 2004-06-30 2012-12-04 Daikin Industries, Ltd. Heat exchanger and air conditioner
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JP2008121934A (en) * 2006-11-09 2008-05-29 Nichirin Co Ltd Plate fin tube heat exchanger and its manufacturing method
GB2445575A (en) * 2007-01-12 2008-07-16 Kuan-Yin Chou Radiating structure
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US11313630B2 (en) 2016-07-01 2022-04-26 Mitsubishi Electric Corporation Heat exchanger and refrigeration cycle apparatus having heat exchanger
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