JP2891523B2 - Heat exchanger manufacturing method - Google Patents
Heat exchanger manufacturing methodInfo
- Publication number
- JP2891523B2 JP2891523B2 JP2222709A JP22270990A JP2891523B2 JP 2891523 B2 JP2891523 B2 JP 2891523B2 JP 2222709 A JP2222709 A JP 2222709A JP 22270990 A JP22270990 A JP 22270990A JP 2891523 B2 JP2891523 B2 JP 2891523B2
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- wall
- thickness
- flat tube
- width direction
- 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 - Fee Related
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-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
- F28D1/02—Heat-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
- F28D1/04—Heat-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
- F28D1/047—Heat-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
- F28D1/0471—Heat-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 having a non-circular cross-section
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-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
- F28D1/02—Heat-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
- F28D1/04—Heat-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
- F28D1/053—Heat-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
- F28D1/0535—Heat-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
- F28D1/05366—Assemblies of conduits connected to common headers, e.g. core type radiators
- F28D1/05383—Assemblies of conduits connected to common headers, e.g. core type radiators with multiple rows of conduits or with multi-channel conduits
-
- 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
- F28F1/02—Tubular elements of cross-section which is non-circular
- F28F1/022—Tubular elements of cross-section which is non-circular with multiple channels
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-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
- F28D1/02—Heat-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
- F28D2001/0253—Particular components
- F28D2001/026—Cores
- F28D2001/0266—Particular core assemblies, e.g. having different orientations or having different geometric features
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Geometry (AREA)
- Bending Of Plates, Rods, And Pipes (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 この発明は、ルームエアコン等に用いられるアルミニ
ウム等の金属製熱交換器の製造方法、更に詳しくは、熱
交換器コアが偏平チューブの幅方向に曲成された非平面
タイプの熱交換器の製造方法に関する。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of manufacturing a heat exchanger made of metal such as aluminum used for a room air conditioner or the like, and more particularly, to a method in which a heat exchanger core is bent in a width direction of a flat tube. The present invention relates to a method for manufacturing a formed non-planar heat exchanger.
従来の技術 近時、ルームエアコン用の熱交換器として、高熱交換
性能及び低圧力損失をメリットとする、いわゆるマルチ
フロータイプと称される熱交換器が好んで用いられる傾
向にある。2. Description of the Related Art In recent years, as a heat exchanger for a room air conditioner, a so-called multi-flow type heat exchanger, which has advantages of high heat exchange performance and low pressure loss, has been favorably used.
この熱交換器は、第2図に示されるように、左右に一
対の中空筒状のアルミニウム製ヘッダー(1)(2)間
に多数本の同アルミニウム製偏平チューブ(3)を渡
し、該偏平チューブ(3)間に同アルミニウム製コルゲ
ートフィン(4)を配置したものとなされている。冷媒
は、入口管(5)から一方のヘッダー(1)に流入した
のち、同時に各偏平チューブ(3)内に分流され、チュ
ーブ(3)間の隙間を流通する空気と熱交換を行い、そ
して他方のヘッダー(2)内で合流し、出口管(6)か
ら流出される。また、ヘッダー(1)(2)内を仕切っ
て冷媒を複数回蛇行させるようにすることもある。In this heat exchanger, as shown in FIG. 2, a plurality of aluminum flat tubes (3) are passed between a pair of hollow cylindrical aluminum headers (1) and (2) on the left and right sides. The aluminum corrugated fins (4) are arranged between the tubes (3). The refrigerant flows into one of the headers (1) from the inlet pipe (5), and at the same time, is diverted into the flat tubes (3) to exchange heat with the air flowing through the gap between the tubes (3). It merges in the other header (2) and flows out of the outlet pipe (6). In some cases, the inside of the headers (1) and (2) is partitioned to make the refrigerant meander a plurality of times.
そして、このマルチフロータイプの熱交換器におい
て、狭い設置スペースを有効利用して熱交換性能を高い
ものすることなどを目的として、同第2図に示されるよ
うに、熱交換器コア(7)が偏平チューブ(3)の長さ
方向中間位置において該偏平チューブ(3)の幅方向に
L字状に屈曲成形されたL字型熱交換器に構成されるこ
とがある。In this multi-flow type heat exchanger, as shown in FIG. 2, for the purpose of effectively utilizing a narrow installation space to enhance heat exchange performance, a heat exchanger core (7) is used. May be configured as an L-shaped heat exchanger bent and formed in an L-shape in the width direction of the flat tube (3) at an intermediate position in the length direction of the flat tube (3).
かかるL字型熱交換器の製造は、例えば、第3図に示
されるように、ヘッダー(1)(2)の側面に形成され
たチューブ挿入孔(8)に直線状の偏平チューブ素材
(9)の端部を挿入配置していわゆるスケルトンを作製
したのち、このスケルトンのチューブ(9)間にコルゲ
ートフィン(4)を配置し、そして全体を一括ろう付け
することにより接合一体化して平面的な熱交換器基体を
製作する。しかるのち、この熱交換器基体のコア部を、
偏平チューブ素材(9)の長さ方向中間所定位置におい
て該偏平チューブ素材(9)の幅方向にL字状に屈曲成
形せしめることによって行われる。For example, as shown in FIG. 3, the production of such an L-shaped heat exchanger is performed by inserting a straight flat tube material (9) into a tube insertion hole (8) formed in the side surface of the header (1) (2). ), A corrugated fin (4) is arranged between the tubes (9) of the skeleton, and the whole is joined together by brazing to form a flat skeleton. Make a heat exchanger substrate. Thereafter, the core of the heat exchanger base is
This is performed by bending the flat tube material (9) into an L-shape in the width direction of the flat tube material (9) at a predetermined position in the longitudinal direction.
また、他の製造方法として、予め曲げ加工を施した偏
平チューブを用いてL字状スケルトンを製作し、チュー
ブ間にコルゲートフィンを配置した後、全体を一括ろう
付けすることもある。As another manufacturing method, an L-shaped skeleton may be manufactured using a flat tube that has been subjected to a bending process in advance, and after corrugated fins are arranged between the tubes, the whole may be collectively brazed.
発明が解決しようとする課題 しかしながら、この種の非平面型マルチフロー熱交換
器の製造では、いずれにしても、偏平チューブ素材
(9)に、第4図に示されるように、その幅方向に曲げ
加工を施したものとなければならず、そのため、この曲
げ加工によって、偏平チューブ素材(9)の幅方向の内
側において圧縮曲げ応力による縮みを生じると共に、幅
方向の外側において引張り曲げ応力による伸びを生じ、
その結果、特に熱交換器における偏平チューブ(3)の
幅方向の外側において、冷媒に対する耐圧強度が十分で
なくなったり、また割れ等が発生するおそれがあった。However, in the manufacture of this type of non-planar type multi-flow heat exchanger, in any case, the flat tube material (9) is, as shown in FIG. The flattened tube material (9) must be subjected to a bending process, so that the flattening tube material (9) shrinks due to compressive bending stress on the inside in the width direction and elongates on the outside in the width direction due to tensile bending stress. Yields
As a result, there is a possibility that the pressure resistance to the refrigerant may not be sufficient, or cracks may occur, especially on the outer side in the width direction of the flat tube (3) in the heat exchanger.
これに対処するため、断面係数を大きくすべくチュー
ブ幅を短くすることもあるが、チューブ幅を短くするこ
とは、チューブ間に配置されるフィンの幅をも短くする
ことになって熱交換性能の劣化を招く結果となって好ま
しいことではない。In order to cope with this, the tube width may be shortened to increase the section modulus.However, shortening the tube width also shortens the width of the fins arranged between the tubes, resulting in heat exchange performance. This is not preferable because it results in deterioration of the device.
この発明は、上記のような従来の問題点を解決し、熱
交換器コアが曲成された非平面タイプのマルチフロー熱
交換器を、従来よりも幅広の偏平チューブを使用して、
該偏平チューブの曲げ加工部の幅方向外側における耐圧
強度の低下、割れ等の欠陥を招くことなく、製造するこ
とのできる方法を提供することを目的とする。The present invention solves the conventional problems as described above, and uses a non-planar type multi-flow heat exchanger in which a heat exchanger core is bent, using a flat tube wider than before,
It is an object of the present invention to provide a method that can be manufactured without causing a defect such as a decrease in pressure resistance and a crack or the like on a widthwise outside of a bent portion of the flat tube.
課題を解決するための手段 上記目的において、この発明は、複数本の偏平チュー
ブとフィンとが交互配置にされて形成された熱交換器コ
アの各チューブの両端が一対の中空ヘッダーの側面に連
通接続され、かつ前記熱交換器コアが偏平チューブの幅
方向のいずれか一方の向きに曲成された熱交換器の製造
方法であって、前記偏平チューブとして、内部を幅方向
に仕切る少なくとも1以上の仕切壁を有し、幅方向にお
ける一端外壁の肉厚を他端外壁の肉厚よりも大に設定す
るとともに、前記仕切壁の肉厚を、前記一端外壁の肉厚
と前記他端外壁の肉厚との中間に設定した押出型材製の
偏平なチューブ素材を用い、該偏平チューブ素材に厚肉
側を外側とした幅方向の曲げ加工を施して熱交換器コア
の曲がりを形成することを特徴とする熱交換器の製造方
法を要旨とする。Means for Solving the Problems In the above object, the present invention provides a heat exchanger core formed by alternately arranging a plurality of flat tubes and fins, wherein both ends of each tube communicate with side surfaces of a pair of hollow headers. A method for manufacturing a heat exchanger wherein the heat exchanger core is connected and the heat exchanger core is bent in one direction in the width direction of the flat tube, wherein at least one or more partitions the interior in the width direction as the flat tube. The thickness of one end outer wall in the width direction is set to be larger than the thickness of the other end outer wall, and the thickness of the partition wall is the thickness of the one end outer wall and the thickness of the other end outer wall. Using a flat tube material made of an extruded mold material set in the middle of the wall thickness, performing a bending process in the width direction with the thick side on the outside to form a bend of the heat exchanger core. Features of heat exchanger A summary of the manufacturing method.
作用 上記方法では、偏平チューブとして、内部に少なくと
も1以上の仕切壁を有し、幅方向における一端外壁の肉
厚を他端外壁の肉厚よりも大に設定するとともに、仕切
壁の肉厚を、前記一端外壁の肉厚と前記他端外壁の肉厚
との中間に設定した押出型材製の偏平なチューブ素材を
用いるものである。このようにチューブ素材の両端外壁
及び仕切壁の各肉厚を、曲げ加工による応力に応じて、
各壁ごとに適当に設定することにより、幅方向全域にお
いて、曲げ加工による応力の悪影響を有効に回避でき
る。このため、曲げ加工によって偏平チューブの曲げの
外側の側端部外壁や仕切壁等の壁部に割れ等の欠陥が生
じる可能性がないかあるいは低くなることはもとより、
曲げ加工後における当該壁部等の耐圧強度の低下もない
かあるいは低く抑えられる。In the above method, the flat tube has at least one or more partition walls inside, and the thickness of one end outer wall in the width direction is set to be larger than the thickness of the other end wall, and the thickness of the partition wall is reduced. A flat tube material made of an extruded die set at an intermediate point between the thickness of the outer wall at one end and the thickness of the outer wall at the other end is used. In this way, the thickness of each outer wall and the partition wall of both ends of the tube material is adjusted according to the stress caused by the bending process.
By properly setting each wall, the adverse effect of stress due to bending can be effectively avoided in the entire region in the width direction. For this reason, the possibility that defects such as cracks occur in the wall portions such as the outer side end outer wall and the partition wall outside the bending of the flat tube due to the bending process is reduced or reduced,
After the bending, the pressure resistance of the wall and the like is not reduced or suppressed.
実施例 以下、この発明の実施例を説明する。Examples Hereinafter, examples of the present invention will be described.
製造する熱交換器は、前述した第4図に示されるよう
なアルミニウム製L型マルチフロー熱交換器である。な
お、本発明方法は、図示のようなL型熱交換器の製造に
限定されるものではなく、要は熱交換器コア(7)が偏
平チューブ(3)の幅方向のいずれか一方の向きに曲げ
られた型式の非平面型熱交換器を広く対象とするもので
あり、従ってコ字型、円弧型等の熱交換器もその対象と
して含む。The heat exchanger to be manufactured is an aluminum L-type multi-flow heat exchanger as shown in FIG. 4 described above. It should be noted that the method of the present invention is not limited to the production of the L-shaped heat exchanger as shown in the figure, but the point is that the heat exchanger core (7) is oriented in one of the width directions of the flat tube (3). The present invention is intended to cover a wide range of non-planar type heat exchangers, and accordingly includes U-shaped, arc-shaped, etc. heat exchangers.
そして、この熱交換器の製造も、基本的には、前述し
た第3図に示されるようにヘッダー(1)(2)と直線
状偏平チューブ素材(9)とを組み合わせてスケールト
ンを製作し、チューブ素材(9)間にコルゲートフィン
(4)を配置する工程と、全体を一括ろう付けにより接
合一体化して平面的な熱交換器基体を製作する工程と、
この熱交換器基体を偏平チューブ素材(9)の長さ方向
中間所定位置において該偏平チューブ(9)の幅方向に
L字状に屈曲成形せしめる工程とを順次遂行することに
よって行う。なお、場合によっては、前述のように、予
め曲げ加工を施した偏平チューブを用いてL字型スケル
トンを製作し、チューブ間にコルゲートフィンを配置し
た後、全体を一括ろう付けする方法等が採用されてもよ
い。In the manufacture of this heat exchanger, basically, as shown in FIG. 3, the scale ton is manufactured by combining the headers (1) and (2) with the linear flat tube material (9). Disposing a corrugated fin (4) between tube materials (9); and joining and integrating the whole by batch brazing to produce a planar heat exchanger substrate.
A step of bending the heat exchanger base into an L-shape in the width direction of the flat tube (9) at a predetermined position in the lengthwise middle of the flat tube material (9). In some cases, as described above, a method of manufacturing an L-shaped skeleton by using a flat tube that has been subjected to a bending process in advance, arranging corrugated fins between the tubes, and brazing the whole as a whole is employed. May be done.
そして、この熱交換器の製造には、偏平チューブ素材
(9)として、第1図に示されるような横断面構成のも
のを使用する。In the manufacture of the heat exchanger, a flat tube material (9) having a cross section as shown in FIG. 1 is used.
即ち、同図の偏平チューブ素材(9)は、内部が三つ
の仕切壁(10)(11)(12)によって幅方向に四室に仕
切られた多穴タイプのものである。That is, the flat tube material (9) in the figure is of a multi-hole type in which the interior is partitioned into four chambers in the width direction by three partition walls (10), (11) and (12).
そして、この偏平チューブ素材(9)の壁厚は次のよ
うに設定する。The wall thickness of the flat tube material (9) is set as follows.
即ち、幅方向一端部の外壁(13)の肉厚aはチューブ
内を流通する冷媒の圧力に耐えうる適当厚さに設定する
と共に、幅方向他端部の外壁(14)の肉厚eは、前記端
部外壁(13)の肉厚aよりも大に設定する。肉厚eの具
体的な大きさは、このチューブ素材(9)に施される曲
げ、チューブ幅B等をどの程度のものに設定するかに依
存してケースバイケースで設定する。That is, the thickness a of the outer wall (13) at one end in the width direction is set to an appropriate thickness that can withstand the pressure of the refrigerant flowing in the tube, and the thickness e of the outer wall (14) at the other end in the width direction is The thickness is set to be larger than the thickness a of the end outer wall (13). The specific size of the wall thickness e is set on a case-by-case basis depending on the bending, tube width B, and the like to be applied to the tube material (9).
なお、チューブ幅Bとしては、熱交換器の性能上、6
〜20mm、好適には6〜16mm、更に好適には10〜14mmに設
定される。下限値を下回って小さいとチューブ間に介在
されるフィンの幅も小さくなって熱交換性能の劣化を招
くことになり、また上限値を越えて大きいとフィンの幅
が大きくなり過ぎて流通空気の抵抗が増大し圧力損失の
増大を招く等の不都合を生じる。The tube width B is 6 in terms of the performance of the heat exchanger.
-20 mm, preferably 6-16 mm, and more preferably 10-14 mm. If it is smaller than the lower limit, the width of the fins interposed between the tubes becomes smaller and the heat exchange performance is degraded. Inconveniences such as an increase in resistance and an increase in pressure loss occur.
また、各仕切壁(10)(11)(12)の肉厚b、c、d
は、同図のように、前記薄肉な端部外壁(13)の肉厚a
と、厚肉な端部外壁(14)の肉厚eとの中間の肉厚値に
設定する必要があり、また薄肉な端部外壁(13)側の仕
切壁(10)側から漸次厚肉となるように設定するのが好
ましい。なお、仕切壁(10)(11)(12)の肉厚は、仕
切壁がチューブ素材(9)の幅方向における曲げの際の
中立軸のどちら側にどの程度離れて位置しているか等を
考慮して設定すべきであり、従って、例えば中立軸の外
側に位置しない仕切壁(10)(11)の厚さb、cについ
ては、肉薄な端部外壁(13)の肉厚aと略同じ厚さと
し、中立軸の外側に位置する仕切壁(12)の厚さについ
ては若干厚肉に設定するというようにしてもよい。ま
た、場合によっては、仕切壁(10)(11)(12)を全て
同じ厚さに設定する場合もありうる。The thickness b, c, d of each partition wall (10) (11) (12)
The thickness a of the thin end outer wall (13) is shown in FIG.
And the thickness e of the thick end outer wall (14) must be set to an intermediate value, and the thickness of the thin end outer wall (13) is gradually increased from the partition wall (10) side. It is preferable to set so that The wall thickness of the partition walls (10), (11) and (12) is determined by how far the partition wall is located on the neutral axis when the tube material (9) is bent in the width direction and how far away the partition wall is. Therefore, for example, the thicknesses b and c of the partition walls (10) and (11) that are not located outside the neutral axis are substantially equal to the thickness a of the thin end outer wall (13). The thickness of the partition wall (12) located outside the neutral axis may be set to be slightly thicker. In some cases, the partition walls (10), (11), and (12) may all be set to the same thickness.
なお、偏平チューブ素材(9)の上下の外壁(15)の
厚さfについては、第1図では、幅方向一定に設定して
いるが、厚肉な端部外壁(14)に向けて漸次厚肉となる
ように設定するようにしてもよい。The thickness f of the upper and lower outer walls (15) of the flat tube material (9) is set to be constant in the width direction in FIG. 1, but gradually toward the thick end outer wall (14). You may make it set so that it may become thick.
このような断面偏肉構成の偏平チューブ素材(9)の
製造は、該断面形状の押出成形孔を有する押出用ダイ
ス、例えばポートホールダイスを用い、押出成形によっ
て生産性よく容易に行うことができる。The production of the flat tube material (9) having such a cross-sectionally uneven wall thickness can be easily performed with good productivity by extrusion using an extrusion die having an extrusion molding hole having the cross-sectional shape, for example, a porthole die. .
そして、この直線状偏平チューブ素材(9)を用い、
これと、ヘッダー(1)(2)、コルゲートフィン
(4)等とを組み合わせて前述のように全体を一体接合
して平面状の熱交換器基体を製作し、そして、この熱交
換器基体を、偏平チューブ素材(9)の幅方向にL字状
に屈曲加工せしめることにより、曲げ加工に付し、それ
によってL字状に曲成された熱交換器コアを有するマル
チフロー熱交換器に製造する。And, using this straight flat tube material (9),
This is combined with the headers (1) and (2), the corrugated fins (4), etc., and the whole is integrally joined as described above to produce a flat heat exchanger base. The flat tube material (9) is bent in an L-shape in the width direction to be bent, thereby producing a multi-flow heat exchanger having an L-shaped heat exchanger core. I do.
この曲げ工程において、偏平チューブ素材(9)の外
側の曲がり部に割れ等の欠陥が発生せず、また得られた
熱交換器のチューブ(3)の当該外側の曲がり部も十分
な耐圧強度を有するものになる。また、仕切壁(10)
(11)(12)の肉厚も上記のように設定したから、曲げ
の際にそれらに破れ等の欠陥を生じることもない。In this bending step, no defect such as a crack is generated in the outer bent portion of the flat tube material (9), and the outer bent portion of the obtained heat exchanger tube (3) also has a sufficient pressure resistance. Will have. In addition, partition wall (10)
(11) Since the thicknesses of (12) and (12) are set as described above, they do not cause defects such as tearing during bending.
発明の効果 上述の次第で、この発明は、熱交換器コアが屈曲状な
いし湾曲状に曲げられた非平面型マルチフロー熱交換器
の製造において、偏平チューブとして、内部に少なくと
も1以上の仕切壁を有し、軸方向における一端外壁の肉
厚を他端外壁の肉厚よりも大に設定するとともに、仕切
壁の肉厚を、前記一端外壁の肉厚と前記他端外壁の肉厚
との中間に設定した押出型材製の偏平なチューブ素材を
用いるものであるため、両端外壁及び仕切壁の各壁部に
おいて、曲げ加工による応力の悪影響を有効に回避で
き、曲げ加工によって偏平チューブの曲げの外側の側端
部外壁や仕切壁等の壁部に割れ等の欠陥が生じる可能性
がないかあるいは低くなることはもとより、曲げ加工後
における当該壁部等の耐圧強度の低下もないかあるいは
低く抑えられる。従って、従来よりも幅広の偏平チュー
ブを使用することができ、熱交換性能の高い当該型式の
熱交換器を製造することができる。しかも、チューブ素
材に対する曲げ加工をスピーディに行えるというメリッ
トもあり、ひいては熱交換器の生産性向上に寄与するこ
とができる。Effect of the Invention As described above, the present invention relates to a method for manufacturing a non-planar multi-flow heat exchanger in which a heat exchanger core is bent or curved, and as a flat tube, at least one or more partition walls inside. The thickness of one end outer wall in the axial direction is set to be larger than the thickness of the other end outer wall, and the thickness of the partition wall is the thickness of the one end outer wall and the thickness of the other end outer wall. Since the flat tube material made of the extruded die material set in the middle is used, the adverse effects of the stress due to bending can be effectively avoided at the outer walls at both ends and the partition wall, and the bending of the flat tube can be prevented by bending. In addition to the possibility that defects such as cracks are generated or reduced in the wall portion such as the outer side end outer wall and the partition wall, the pressure resistance strength of the wall portion and the like after bending is not reduced or reduced. Restrained It is. Therefore, a flat tube wider than before can be used, and a heat exchanger of this type having high heat exchange performance can be manufactured. In addition, there is an advantage that the bending of the tube material can be performed speedily, which can contribute to an improvement in the productivity of the heat exchanger.
加えて、かかる偏平チューブ素材は押出型材製だか
ら、上記のような偏肉構成の偏平チューブの製作も容易
に行うことができる。In addition, since the flat tube material is made of an extruded material, it is possible to easily manufacture a flat tube having the above-described flat wall structure.
第1図ないし第3図はこの発明の一実施例を示すもの
で、第1図は本発明方法に使用される偏平チューブ素材
の一例を示す断面斜視図、第2図は熱交換器の斜視図、
第3図はチューブ、ヘッダー、フィンを分離状態に示す
斜視図である。 第4図は、従来の熱交換器に使用されていた偏平チュー
ブ素材の断面斜視図である。 (1)(2)…ヘッダー、(3)…偏平チューブ、
(4)…フィン、(7)…熱交換器コア、(9)…偏平
チューブ素材、(10)(11)(12)…仕切壁、(13)
(14)…端部外壁。1 to 3 show an embodiment of the present invention. FIG. 1 is a sectional perspective view showing an example of a flat tube material used in the method of the present invention, and FIG. 2 is a perspective view of a heat exchanger. Figure,
FIG. 3 is a perspective view showing a tube, a header, and a fin in a separated state. FIG. 4 is a sectional perspective view of a flat tube material used in a conventional heat exchanger. (1) (2) ... header, (3) ... flat tube,
(4) fin, (7) heat exchanger core, (9) flat tube material, (10) (11) (12) partition wall, (13)
(14) ... End outer wall.
フロントページの続き (58)調査した分野(Int.Cl.6,DB名) B21D 53/08 F28F 1/02 Continuation of the front page (58) Field surveyed (Int.Cl. 6 , DB name) B21D 53/08 F28F 1/02
Claims (1)
置にされて形成された熱交換器コアの各チューブの両端
が一対の中空ヘッダーの側面に連通接続され、かつ前記
熱交換器コアが偏平チューブの幅方向のいずれか一方の
向きに曲成された熱交換器の製造方法であって、 前記偏平チューブとして、内部を幅方向に仕切る少なく
とも1以上の仕切壁を有し、幅方向における一端外壁の
肉厚を他端外壁の肉厚よりも大に設定するとともに、前
記仕切壁の肉厚を、前記一端外壁の肉厚と前記他端外壁
の肉厚との中間に設定した押出型材製の偏平なチューブ
素材を用い、 該偏平チューブ素材に厚肉側を外側とした幅方向の曲げ
加工を施して熱交換器コアの曲がりを形成することを特
徴とする熱交換器の製造方法。An end of each tube of a heat exchanger core formed by alternately arranging a plurality of flat tubes and fins is connected at both ends to side surfaces of a pair of hollow headers, and the heat exchanger core is A method for manufacturing a heat exchanger bent in one direction in a width direction of a flat tube, wherein the flat tube has at least one or more partition walls that partition the inside in the width direction, An extruded mold member in which the thickness of one end outer wall is set to be larger than the thickness of the other end outer wall, and the thickness of the partition wall is set to an intermediate value between the thickness of the one end outer wall and the thickness of the other end outer wall. A method for manufacturing a heat exchanger, comprising: using a flat tube material made of aluminum; and bending the flat tube material in the width direction with the thick side outside.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2222709A JP2891523B2 (en) | 1990-08-24 | 1990-08-24 | Heat exchanger manufacturing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2222709A JP2891523B2 (en) | 1990-08-24 | 1990-08-24 | Heat exchanger manufacturing method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04105734A JPH04105734A (en) | 1992-04-07 |
JP2891523B2 true JP2891523B2 (en) | 1999-05-17 |
Family
ID=16786680
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2222709A Expired - Fee Related JP2891523B2 (en) | 1990-08-24 | 1990-08-24 | Heat exchanger manufacturing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2891523B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10317141B2 (en) | 2014-11-25 | 2019-06-11 | Hydro Extruded Solutions As | Multi port extrusion tubing design |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2558542Y2 (en) * | 1991-05-30 | 1997-12-24 | 本田技研工業株式会社 | Outdoor heat exchanger for vehicles |
KR100744486B1 (en) * | 2001-06-12 | 2007-08-01 | 한라공조주식회사 | Heat exchanger |
JP4751662B2 (en) * | 2004-08-10 | 2011-08-17 | 昭和電工株式会社 | Plate for manufacturing flat tube, method for manufacturing flat tube, and method for manufacturing heat exchanger |
JP2007093144A (en) * | 2005-09-29 | 2007-04-12 | Denso Corp | Heat exchanging tube and heat exchanger |
JP6136124B2 (en) * | 2012-06-14 | 2017-05-31 | 株式会社富士通ゼネラル | Heat exchanger manufacturing method and heat exchanger |
JP2014095524A (en) * | 2012-11-12 | 2014-05-22 | Hitachi Appliances Inc | Air conditioner |
CN104797900B (en) * | 2012-11-13 | 2016-11-09 | 三菱电机株式会社 | Pancake heat-transfer pipe, the manufacture method with the cross-fin tube type heat exchanger of this pancake heat-transfer pipe and the cross-fin tube type heat exchanger utilizing the method to manufacture |
CN219347479U (en) * | 2022-11-30 | 2023-07-14 | 浙江盾安热工科技有限公司 | Flat heat exchange tube and heat exchanger |
-
1990
- 1990-08-24 JP JP2222709A patent/JP2891523B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10317141B2 (en) | 2014-11-25 | 2019-06-11 | Hydro Extruded Solutions As | Multi port extrusion tubing design |
Also Published As
Publication number | Publication date |
---|---|
JPH04105734A (en) | 1992-04-07 |
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