JPH0739914B2 - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPH0739914B2
JPH0739914B2 JP62143433A JP14343387A JPH0739914B2 JP H0739914 B2 JPH0739914 B2 JP H0739914B2 JP 62143433 A JP62143433 A JP 62143433A JP 14343387 A JP14343387 A JP 14343387A JP H0739914 B2 JPH0739914 B2 JP H0739914B2
Authority
JP
Japan
Prior art keywords
tube
pipe
flat
heat exchanger
widened
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 - Lifetime
Application number
JP62143433A
Other languages
Japanese (ja)
Other versions
JPS6317391A (en
Inventor
バウアー ディーター
ヘッセ ボルフガング
エーリッヒマン ベルナー
シュラーデ ヘルベルト
Original Assignee
ズ−ドドイツチエ キユ−レルフアブリク ユリウス エフエル.ベ−ル ゲゼルシヤフト ミツト ベシユレンクテル ハフツング ウント コンパニ− コマンデイトゲゼルシヤフト
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 ズ−ドドイツチエ キユ−レルフアブリク ユリウス エフエル.ベ−ル ゲゼルシヤフト ミツト ベシユレンクテル ハフツング ウント コンパニ− コマンデイトゲゼルシヤフト filed Critical ズ−ドドイツチエ キユ−レルフアブリク ユリウス エフエル.ベ−ル ゲゼルシヤフト ミツト ベシユレンクテル ハフツング ウント コンパニ− コマンデイトゲゼルシヤフト
Publication of JPS6317391A publication Critical patent/JPS6317391A/en
Publication of JPH0739914B2 publication Critical patent/JPH0739914B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • F28D1/05358Assemblies of conduits connected side by side or with individual headers, e.g. section type radiators
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21CMANUFACTURE OF METAL SHEETS, WIRE, RODS, TUBES OR PROFILES, OTHERWISE THAN BY ROLLING; AUXILIARY OPERATIONS USED IN CONNECTION WITH METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL
    • B21C37/00Manufacture of metal sheets, bars, wire, tubes or like semi-manufactured products, not otherwise provided for; Manufacture of tubes of special shape
    • B21C37/06Manufacture of metal sheets, bars, wire, tubes or like semi-manufactured products, not otherwise provided for; Manufacture of tubes of special shape of tubes or metal hoses; Combined procedures for making tubes, e.g. for making multi-wall tubes
    • B21C37/15Making tubes of special shape; Making tube fittings
    • B21C37/22Making finned or ribbed tubes by fixing strip or like material to tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21DWORKING OR PROCESSING OF SHEET METAL OR METAL TUBES, RODS OR PROFILES WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21D53/00Making other particular articles
    • B21D53/02Making other particular articles heat exchangers or parts thereof, e.g. radiators, condensers fins, headers
    • B21D53/08Making other particular articles heat exchangers or parts thereof, e.g. radiators, condensers fins, headers of both metal tubes and sheet metal
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00Evaporators; Condensers
    • F25B39/02Evaporators
    • 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
    • F28F1/02Tubular elements of cross-section which is non-circular
    • F28F1/025Tubular elements of cross-section which is non-circular with variable shape, e.g. with modified tube ends, with different geometrical features
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • F28F13/12Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media by creating turbulence, e.g. by stirring, by increasing the force of circulation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/0219Arrangements for sealing end plates into casing or header box; Header box sub-elements
    • F28F9/0221Header boxes or end plates formed by stacked 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
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0068Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
    • F28D2021/0071Evaporators

Landscapes

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

Abstract

1. Heat exchanger, particularly a cooling medium evaporator, consisting of a plurality of flat pipes parallel with one another, but arranged with a space between them and joined together, between which pipes a plurality of fins have been fitted to increase the heat exchange surface, said pipes being provided at both their end regions with a widened part of the pipe wall, being laid by means of this part directly on a corresponding part of the adjacent pipe and connected therewith, particularly by soldering, there being provided in each widened part, transversally to the longitudinal axis of the flat pipes, connection openings with the adjacent flat pipe or to the adjacent group of pipes, characterized in that the widened part (2a, 2b) of each flat pipe (2) extends over the entire width of the pipe, but, towards the narrow longitudinal sides (2') runs in the form of a pointed arch into the arc-shaped parts (8) of the flat pipe, and in that, in the region (20, 21) of each flat pipe (2, 20) lying between the widened parts (2a, 2b, 20a, 20b) of the pipe wall (4) turbulence inserts (7, 70) are provided which fill up the entire pipe width (B).

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は熱交換器、特に冷媒気化器に係り、さらに詳し
くは互いに或る間隔で配置され、互いに接続されている
多数の平行な扁平管からなり、この扁平間の間に熱交換
面積を増大させる多数のフインが挿入されており、扁平
管の両端部領域に管壁の拡幅部分が設けられており、こ
の拡幅部分が隣接の管の相当する部分は直接接してお
り、かつこの部分と、特に半田付けによって結合されて
おり、各拡幅部分内に管の長手軸に対して横方向に延び
隣接の1本の扁平管あるいは隣接の扁平管群へ連通する
開口部が設けられている熱交換器、特に冷媒気化器に関
するものである。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger, particularly a refrigerant vaporizer, and more particularly to a large number of parallel flat tubes arranged at a certain distance from each other and connected to each other. It consists of a number of fins that increase the heat exchange area between the flats, and the widened portions of the pipe wall are provided in both end regions of the flat pipe. The corresponding part is in direct contact and is connected to this part, in particular by soldering, in each widening part extending laterally to the longitudinal axis of the pipe and adjacent to one flat tube or to an adjacent flat tube. The present invention relates to a heat exchanger provided with an opening communicating with a tube group, particularly a refrigerant vaporizer.

〔従来の技術〕[Conventional technology]

この種の熱交換器は、本出願人の以前の出願、特願昭60
−290899号(特開昭61−175481号)によってすでに提案
されている。この種の熱交換器は、ディスク状の熱交換
体を有する熱交換器に比較して扁平管をその全長にわた
って半田付けあるいは接着する必要はなく、端部と連通
口のみを半田付けないし接着するだけでよいので、製造
の著しい簡略化が達成されるという利点を有する。提案
された構造では、扁平管の拡幅された端部分のみが直接
接しているので、別体の接線管スリーブを設けなくても
済む。
This type of heat exchanger is disclosed in the applicant's previous application, Japanese Patent Application No.
It has already been proposed by JP-A-290899 (JP-A-61-175481). In this type of heat exchanger, it is not necessary to solder or bond the flat tube over its entire length as compared with a heat exchanger having a disk-shaped heat exchanger, and only the end and the communication port are soldered or bonded. This has the advantage that a significant simplification of the production is achieved, since In the proposed construction, only the widened end of the flat tube is in direct contact, so that no separate tangential tube sleeve is required.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

しかしこの種の構造の熱交換器では、パイプ端部の拡幅
部分がパイプ幅全体にわたって延びていないということ
が或る点において欠点となる。というのはこの種の拡幅
を形成する場合に材料の延び過ぎによって、特に扁平管
の長手方向端部の屈曲された壁の領域に亀裂が生じるか
らである。それによって、乱流パッドの形のオイルクー
ラーの例で知られているように、公知の構造では扁平管
の内部にパッドを挿入することはできない。提案された
熱交換体の場合に設けられている全幅にわたらない拡幅
部分では、管幅の一部のみを満たす乱流パッドの挿入し
かできい。このような場合だと熱交換手段は乱流パッド
の外側を通って流れるので、熱伝導を改良する乱流パッ
ドの効果は達成されないことになる。
However, in the heat exchanger of this kind of structure, a disadvantage is that the widened portion at the end of the pipe does not extend over the entire width of the pipe. The reason for this is that overextending of the material when forming this kind of widening causes cracks, in particular in the region of the curved wall at the longitudinal end of the flat tube. Thereby, it is not possible to insert the pad inside the flat tube with the known construction, as is known in the example of oil coolers in the form of turbulent pads. In the widened part provided in the case of the proposed heat exchange element which does not extend over the entire width, it is only possible to insert a turbulent flow pad that fills only part of the tube width. In such a case, the heat exchange means will flow through the outside of the turbulence pad, so that the effect of the turbulence pad to improve heat transfer will not be achieved.

本発明は以上のような欠点を除去するためになされたも
ので、乱流パッドが管の全幅を満たしていない管に比較
してより大きい熱交換能力を可能にする熱交換器を提供
することを目的としている。
The present invention has been made to eliminate the above drawbacks, and provides a heat exchanger that enables a larger heat exchange capacity as compared with a tube in which the turbulent flow pad does not fill the entire width of the tube. It is an object.

〔問題点を解決するための手段及び作用〕[Means and Actions for Solving Problems]

上記の目的を達成するために本発明によれば、熱交換器
の管の拡幅部分の間に管の全幅を満たす乱流パッドを設
ける構成が採用されている。それによって乱流パッドが
管の全幅を満たしていない管に比較してより大きい熱交
換能力が可能となる。
In order to achieve the above object, according to the present invention, a configuration is adopted in which a turbulent flow pad that fills the entire width of the tube is provided between the widened portions of the tube of the heat exchanger. This allows for greater heat exchange capacity compared to tubes where the turbulence pad does not fill the full width of the tube.

このことは、各扁平管の拡幅部分が幅狭の長手方向側へ
向かって尖頭状に延びて扁平管の長手方向端縁の屈曲部
となっているので、拡幅部分が管の全幅にわたって設け
られることが可能になることによって、達成することが
できる。拡幅部分が端部領域へ向かって尖頭状に延びて
いることによって、端部領域における管材料の伸びは平
行な管壁の中央部におけるよりも少ない。したがって亀
裂を生じず危険を伴う伸び過ぎは起こらない。このよう
に達成することによって簡単な方法で、扁平管の幅を有
する乱流パッドを開放した管へ軸方向に挿入し、公知の
ように固定することが可能となる。一般に溶接継目が設
けられる幅狭の端部領域に変形が生じないことも有利で
ある。
This means that the widened portion of each flat tube extends sharply toward the narrow longitudinal direction side and forms the bent portion of the longitudinal edge of the flat tube, so that the widened portion is provided over the entire width of the tube. By being able to be done, it can be achieved. Because of the pointed extension of the widened portion toward the end regions, the tubing material stretches less in the end regions than in the central portions of the parallel tube walls. Therefore, there is no crack and no dangerous overstretching. This accomplishes in a simple manner a turbulence pad having the width of a flat tube can be axially inserted into an open tube and fixed in a known manner. It is also advantageous that no deformation occurs in the narrow end regions, which are generally provided with weld seams.

しかしまた他の方法では、拡幅された部分を扁平管の幅
の一部にわたってのみ設けることも可能であるが、この
場合には扁平管の全幅にわたって乱流パッドを挿入する
ために所定の手段を設けなければならない。このこと
は、乱流パッドをまずジグザグの波形にして長円管の中
央領域へ挿入し、この管の乱流パッドが取り付けられて
いる領域を平行に圧縮して、乱流パッドが波形から平ら
に延びた形に押圧されるまで変形することによって達成
される。したがってこの方法では扁平管は乱流パッドの
挿入後に初めて形成される。この方法は非常に有利であ
ることが証明されている。この方法によれば、このよう
にして挿入された乱流パッドは最初は長円形の管の中央
部分がプレート状に変形されることにより扁平管内に固
定されるという利点が得られる。
However, in another method, it is also possible to provide the widened portion only over a part of the width of the flat tube, but in this case, a predetermined means for inserting the turbulent flow pad over the entire width of the flat tube is provided. Must be provided. This means that the turbulence pad is first zig-zag corrugated and inserted into the central region of the oval tube and the region of the tube where the turbulence pad is attached is compressed in parallel, causing the turbulence pad to flatten from the corrugation. It is achieved by deforming until pressed into an elongated shape. Therefore, in this method, the flat tube is formed only after the turbulent flow pad is inserted. This method has proven to be very advantageous. This method has the advantage that the turbulent flow pad inserted in this way is fixed in the flat tube by initially deforming the central part of the oval tube into a plate shape.

〔実施例〕〔Example〕

以下、図面に示す2つの実施例を用いて本発明の特徴と
利点を説明する。
The features and advantages of the present invention will be described below with reference to two embodiments shown in the drawings.

第1実施例 第1図から第3図に示す熱交換器1は、互いに平行に整
合された軸線5を有し互いに直接隣接して並べられてい
る多数の扁平管2から構成されている。扁平管2はそれ
ぞれ端部に形成されている拡幅された拡幅部分2a,2bで
互いに接しており、かつ扁平管の間に熱交換フィン3が
設けられており、この熱交換フィンは第1図の図面平面
方向において扁平管2を流れる熱交換媒体、特に空気の
熱をよりよく奪うのに用いられる。
First Embodiment A heat exchanger 1 shown in FIGS. 1 to 3 is composed of a large number of flat tubes 2 having axes 5 aligned parallel to each other and arranged directly adjacent to each other. The flat tubes 2 are in contact with each other at the widened widened portions 2a, 2b formed at their ends, and the heat exchange fins 3 are provided between the flat tubes. Is used to better remove the heat of the heat exchange medium, especially the air, flowing through the flat tube 2 in the plane of the drawing.

扁平管2の拡幅部分2aないし2bは、本実施例では端面側
に挿入されたトラップ10によって閉鎖されている。この
トラップは第3図の下方の2本の扁平管では設けられて
いない。図から明らかなように、扁平管2の中央部分2c
は拡幅部分2aよりも著しく狭く、かつ平行な壁を有する
扁平管の長手方向端縁には屈曲部8が設けられており、
この屈曲部はそれぞれ平行な壁4へ移行している。さら
に図から明らかなように拡幅部分2aないし類似の部分2b
の平行な壁部分4′には開口部6,6′が形成されてい
る。この平行な壁部分4′は移行領域9を介して下方へ
移行して壁4となっており、この移行領域は壁4上でも
壁4′上でもほぼ垂直に設けられている。この移行領域
9は管の長手方向両端、すなわちそれぞれ屈曲部8へ向
かって小さくなっており、これはまず平行な壁4′が屈
曲部8へ向かって尖った屈曲部を形成するように延びて
いるからである。したがって拡幅部分2a,2bを拡幅する
際の材料の延びは、屈曲部8の領域へ向かって徐々に小
さくなっており、屈曲部の領域ではゼロになる。尖頭形
に拡幅することによって、屈曲部の領域にき裂が生じる
危険を完全に防止することができ、前記拡幅は適当な工
具を用いて行うことができる。第3図に示すように管は
互いに良好に接して設けられており、かつ扁平管2の全
体の幅Bを有する乱流装置7を扁平管に軸方向に挿入し
て固定することができるという利点を有する。
The widened portions 2a and 2b of the flat tube 2 are closed by a trap 10 inserted on the end face side in this embodiment. This trap is not provided in the lower two flat tubes in FIG. As is clear from the figure, the central portion 2c of the flat tube 2
Is a narrow tube which is significantly narrower than the widened portion 2a and has a bent portion 8 at the longitudinal edge of the flat tube having parallel walls.
The bends respectively transition to parallel walls 4. Further, as is clear from the figure, the widened portion 2a or similar portion 2b
Openings 6, 6'are formed in the parallel wall portions 4'of. This parallel wall portion 4'moves downwards via a transition region 9 into a wall 4, which is provided substantially vertically on the wall 4 as well as on the wall 4 '. This transition area 9 is reduced towards the longitudinal ends of the tube, ie towards the bend 8, respectively, which means that first the parallel walls 4 ′ extend towards the bend 8 so as to form a sharp bend. Because there is. Therefore, the extension of the material when widening the widened portions 2a and 2b gradually decreases toward the region of the bent portion 8 and becomes zero in the region of the bent portion. By widening in a pointed manner, the risk of cracking in the region of the bend can be completely prevented and the widening can be carried out with a suitable tool. As shown in FIG. 3, the tubes are provided in good contact with each other, and the turbulent flow device 7 having the entire width B of the flat tube 2 can be axially inserted and fixed in the flat tube. Have advantages.

第2図から明らかなように、拡幅部分2aの平行な壁4′
はほぼ境界線11の間の領域に延びており、かつこの境界
線からより材料の少ない尖った屈曲部によって形成され
ている外方へ向かって、そしてまた好ましくは斜め上方
の外方へ向かって延びる端壁部分12が設けられており、
境界線11の間の領域には低く延びる領域が設けられてい
る。このように形成することによって、中央領域におい
ても、すなわち壁4′の領域においても材料の延びを許
容範囲内に保つことができるように配慮されている。
As is clear from FIG. 2, the parallel walls 4'of the widened portion 2a.
Extend approximately in the region between the borderlines 11 and from this borderline outwards, which is formed by sharper bends of less material, and also preferably obliquely upwards outwards. An extending end wall portion 12 is provided,
An area extending low is provided in the area between the boundary lines 11. Due to this formation, care is taken that the material elongation can be kept within an acceptable range, even in the central region, ie in the region of the wall 4 '.

第2実施例 第4図から第7図に示すものは冷媒気化用の扁平管の他
の実施例であって、この扁平管にも乱流パッド70が設け
られているが、この扁平管の構成は異なっている。本実
施例では扁平管の端部領域は拡幅されておらず、第4図
の上部に示すように元になる材料として長円形の断面を
有する管20′が選択されており、この管の壁40の互いの
間隔はbで示されている。この長円管20′の長さはB′
である。このように形成された長円パイプ20′内に乱流
パッド70′が波形あるいはジグザグに挿入される。この
乱流パッドの長さは全体で、後述のように管が変形した
後にこの変形部分の長さに相当する長さに設定されてい
る。したがって長さBを有するこの乱流パッド70′は第
4図の上部に示すように、管20内で符号21で示す領域を
占めるように(第5図と第6図参照)管20内へ軸方向に
挿入され、次にこの乱流パッドが変形される。この変形
が行われた後にこの中央部分21はローラあるいはプレス
機によって圧縮され、しかも管20′のこの領域が厚さd
と幅Bを有するように圧縮される。したがってこのよう
に形成された扁平管20の拡幅端部領域は全体の幅Bを持
たない。しかし領域21では乱流パッド70は全長にわたっ
て幅Bを有し、変形工程によって第4図に示す拡張位置
を占め、かつ軸方向においてもこの位置に固定されてい
る。この変形工程で変わらず領域21より拡幅されている
部分20aと20bに、第1図から第3図に示す実施例の開口
部6と同様の開口部を設けることができる。しかし本実
施例では拡幅部分にそれぞれ2つの開口部60ないし60′
が形成されており、これらの開口部は扁平管を隣接させ
たときに個々の扁平管20間を連通させる。本実施例では
さらに、開口部60に外方へ突出するスリーブ61が設けら
れるよう配慮がなされており、このスリーブはたとえば
適当な打ち出しによって形成される。するとこの実施例
には、扁平管気化器あるいは扁平管熱交換器を形成する
のに1種類の扁平管20しか必要とせず、この扁平管を互
いに半田付けすればよいという利点がある。ここでスリ
ーブ61は、開口部60′内に嵌入する寸法に設定される。
他の実施例の場合と同様、この管の開放端はトラップ10
を挿入することによって閉鎖される。
Second Embodiment FIG. 4 to FIG. 7 show another embodiment of the flat tube for vaporizing the refrigerant, which is also provided with the turbulent flow pad 70. The composition is different. In this embodiment, the end region of the flat tube is not widened, and the tube 20 'having an oval cross section is selected as the original material as shown in the upper part of FIG. 4, and the wall of this tube is selected. The spacing of the 40 from each other is indicated by b. The length of this oval tube 20 'is B'
Is. The turbulent flow pad 70 'is corrugated or zigzag inserted into the oval pipe 20' thus formed. The length of the turbulent flow pad is generally set to a length corresponding to the length of the deformed portion after the pipe is deformed as described later. Therefore, this turbulence pad 70 'having a length B is introduced into the tube 20 so as to occupy the area designated by the numeral 21 in the tube 20, as shown in the upper part of FIG. 4 (see FIGS. 5 and 6). Inserted axially, this turbulence pad is then deformed. After this deformation has taken place, this central part 21 is compressed by rollers or presses, and this area of the tube 20 'has a thickness d.
And have a width B. Therefore, the widened end region of the flat tube 20 thus formed does not have the entire width B. However, in the region 21, the turbulent pad 70 has a width B over its entire length, occupies the expanded position shown in FIG. 4 by the deformation process and is also fixed in this position in the axial direction. Openings similar to the openings 6 of the embodiment shown in FIGS. 1 to 3 can be provided in the portions 20a and 20b that are wider than the region 21 without changing in this deformation process. However, in this embodiment, two openings 60 to 60 'are formed in the widened portion.
Are formed, and these openings allow communication between the individual flat tubes 20 when the flat tubes are adjacent to each other. In the present embodiment, it is further considered that the opening 60 is provided with a sleeve 61 projecting outward, and this sleeve is formed by, for example, a suitable stamping. This embodiment then has the advantage that only one type of flat tube 20 is required to form a flat tube vaporizer or flat tube heat exchanger, and the flat tubes can be soldered together. Here, the sleeve 61 is set to a size that fits into the opening 60 '.
As in the other embodiments, the open end of this tube is trap 10
Closed by inserting.

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

第1図〜第3図は本発明の1実施例を説明するもので第
1図は本発明に基づき直接隣接する扁平管から形成され
た冷媒気化器の概略縦断面図、 第2図は第1図の冷媒気化器の一部の矢印II方向におけ
る側面図、 第3図は第1図の冷媒気化器の矢印II方向における上面
図、管の上方の端部の一部のみが開放状態で示されてお
り、 第4図〜第7図は本発明の他の実施例を説明するもの
で、 第4図は扁平管の製造工程の概略説明図で、ここでは乱
流装置は中央部分の変形前に挿入されており、 第5図は第4図に示す方法によって形成された扁平管の
一部断面で示す側面図、 第6図は第5図の扁平管のVI−VI線に沿った部分断面
図、 第7図は第5図の管の矢印VII方向における上面図であ
る。 2,20……扁平管、 2a,2b,20a,20b……拡幅部分、 7,70……乱流パッド、 8……屈曲部。
1 to 3 illustrate one embodiment of the present invention. FIG. 1 is a schematic vertical sectional view of a refrigerant vaporizer formed from flat tubes directly adjacent to each other according to the present invention, and FIG. 1 is a side view of a part of the refrigerant vaporizer of FIG. 1 in the direction of arrow II, FIG. 3 is a top view of the refrigerant vaporizer of FIG. 1 in the direction of arrow II, and only a part of the upper end of the pipe is open. 4 to 7 are diagrams for explaining another embodiment of the present invention, and FIG. 4 is a schematic explanatory diagram of the manufacturing process of the flat tube, in which the turbulent flow device is at the central portion. It has been inserted before the deformation, FIG. 5 is a side view showing a partial cross section of the flat tube formed by the method shown in FIG. 4, and FIG. 6 is taken along line VI-VI of the flat tube of FIG. FIG. 7 is a partial sectional view, and FIG. 7 is a top view of the pipe of FIG. 5 in the direction of arrow VII. 2,20 …… Flat tube, 2a, 2b, 20a, 20b …… Widened part, 7,70 turbulence pad, 8 …… Bent part.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 ボルフガング ヘッセ ドイツ連邦共和国,7827 レーフィンゲ ン,マルティーンシュトラーセ 11 (72)発明者 ベルナー エーリッヒマン ドイツ連邦共和国,7143 バイヒンゲン /エンツ,アインシュタインシュトラーセ 21 (72)発明者 ヘルベルト シュラーデ ドイツ連邦共和国,7016 ゲルリンゲン, ヨハン−ツィマァマン−シュトラーセ 22 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Wolfgang Hesse Germany, 7827 Leifingen, Martinstrasse 11 (72) Inventor Berner Erichmann Germany, 7143 Bayingen / Enz, Einsteinstrasse 21 (72) Invention Herbert Schlader Germany, 7016 Gerlingen, Johann-Zimmermann-Strasse 22

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】互いに或る間隔で配置され、互いに接続さ
れている多数の平行な扁平管からなり、この扁平管の間
に熱交換面積を増大させる多数のフィンが挿入されてお
り、扁平管の両端部領域に管壁の拡幅部分が設けられて
おり、この拡幅部分が隣接の管の相当する部分に直接接
しており、かつこの部分と、特に半田付けによって結合
されており、各拡幅部分内に管の長手軸に対して横方向
に延び隣接の1本の扁平管あるいは隣接の扁平管群へ連
通する開口部が設けられてい熱交換器において、各扁平
管(2,2)の拡幅部分(2a,2b,20a,20b)の間に位置する
領域(2c,21)に管の全幅(B)を満たす乱流パッド
(7,70)が設けられていることを特徴とする熱交換器。
1. A flat tube comprising a plurality of parallel flat tubes arranged at a certain distance from each other and connected to each other, and a large number of fins for increasing a heat exchange area being inserted between the flat tubes. A widened portion of the pipe wall is provided in both end regions of the pipe, and the widened portion is in direct contact with a corresponding portion of an adjacent pipe, and is joined to this portion, in particular, by soldering. Inside the heat exchanger, there is an opening that extends laterally with respect to the longitudinal axis of the tube and communicates with one adjacent flat tube or a group of adjacent flat tubes. Heat exchange characterized in that a turbulent flow pad (7,70) is provided in the area (2c, 21) located between the portions (2a, 2b, 20a, 20b) to fill the entire width (B) of the tube. vessel.
【請求項2】各扁平管(2)の拡幅部分(2a,2b)は管
の全幅にわたって延びているが、しかし幅狭の長手側
(2′)へ向かって尖頭状に屈曲し、扁平管(2)の屈
曲部(8)となっていることを特徴とする特許請求の範
囲第1項に記載の熱交換器。
2. The widened portion (2a, 2b) of each flat tube (2) extends over the entire width of the tube, but bends sharply toward the narrower longitudinal side (2 ') and is flattened. The heat exchanger according to claim 1, wherein the heat exchanger is a bent portion (8) of the pipe (2).
【請求項3】拡幅部分(2a,2b)の屈曲部(8)となる
領域がや球形に形成されていることを特徴とする特許請
求の範囲第2項に記載の熱交換器。
3. The heat exchanger according to claim 2, wherein a region to be the bent portion (8) of the widened portion (2a, 2b) is formed in a slightly spherical shape.
【請求項4】拡幅部分(2a,2b)の壁から平行な管壁
(4′)へ移行する部分がこの平行な管壁に対してほぼ
垂直に延びていることを特徴とする特許請求の範囲第2
項あるいは第3項に記載の熱交換器。
4. A widened portion (2a, 2b) wall transitioning from a wall to a parallel tube wall (4 ') extends substantially perpendicular to the parallel tube wall. Range second
The heat exchanger according to item 3 or 4.
【請求項5】扁平管(20)の拡幅部分(20a)が扁平管
(20)の幅(B)の一部にわたって延びていることを特
徴とする特許請求の範囲第1項に記載の熱交換器。
5. The heat according to claim 1, wherein the widened portion (20a) of the flat tube (20) extends over a part of the width (B) of the flat tube (20). Exchanger.
【請求項6】拡幅部分(20a)が長円管(20′)の断面
に相当し、この長円管の管壁(40)の拡幅部分(20a,20
b)間の領域がより小さい幅(b)に圧縮されているこ
とを特徴とする特許請求の範囲第5項に記載の熱交換
器。
6. The widened portion (20a) corresponds to the cross section of the elliptic tube (20 '), and the widened portion (20a, 20a) of the tube wall (40) of the elliptic tube (20a).
Heat exchanger according to claim 5, characterized in that the region between b) is compressed to a smaller width (b).
【請求項7】端部(2a,2b)の拡幅された扁平管(2)
に、乱流パッド(7)が軸方向に挿入されたことを特徴
とする特許請求の範囲第1項に記載の熱交換器。
7. A flat tube (2) having widened ends (2a, 2b).
A heat exchanger according to claim 1, characterized in that a turbulent flow pad (7) is axially inserted in it.
【請求項8】波形(70′)の乱流パッド(70)が長円管
(20′)の中央領域(21)へ挿入されたこと、及びこの
管(20′)の乱流パッド(70′)が取り付けられている
領域(21)が平行に圧縮されて、乱流パッドが波形から
平らに延びた形に押圧されるまで変形が行われたことを
特徴とする特許請求の範囲第1項に記載の熱交換器。
8. A turbulent pad (70) of corrugated (70 ') is inserted into the central region (21) of an oval tube (20') and the turbulent pad (70 ') of this tube (20'). Claim 1 characterized in that the region (21) to which the ') is attached is compressed in parallel and deformed until the turbulent pad is pressed into a flattened form from the corrugations. The heat exchanger according to item.
JP62143433A 1986-07-09 1987-06-10 Heat exchanger Expired - Lifetime JPH0739914B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19863622953 DE3622953A1 (en) 1986-07-09 1986-07-09 HEAT EXCHANGER, ESPECIALLY REFRIGERANT EVAPORATOR
DE3622953.9 1986-07-09

Publications (2)

Publication Number Publication Date
JPS6317391A JPS6317391A (en) 1988-01-25
JPH0739914B2 true JPH0739914B2 (en) 1995-05-01

Family

ID=6304670

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62143433A Expired - Lifetime JPH0739914B2 (en) 1986-07-09 1987-06-10 Heat exchanger

Country Status (5)

Country Link
EP (1) EP0253167B1 (en)
JP (1) JPH0739914B2 (en)
AT (1) ATE43707T1 (en)
DE (2) DE3622953A1 (en)
ES (1) ES2008864B3 (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3900744A1 (en) * 1989-01-12 1990-07-26 Sueddeutsche Kuehler Behr HEAT EXCHANGER
JPH0346757U (en) * 1989-08-29 1991-04-30
FR2715216B1 (en) * 1994-01-20 1996-02-16 Valeo Thermique Moteur Sa Heat exchanger tube, process for its conformation and heat exchanger comprising such tubes.
FR2715217B1 (en) * 1994-01-20 1996-03-01 Valeo Thermique Moteur Sa Heat exchanger tube, in particular for a motor vehicle, process for its conformation and heat exchanger comprising such tubes.
DE19543986A1 (en) * 1995-11-25 1997-05-28 Behr Gmbh & Co Heat exchanger and a method of manufacturing a heat exchanger
IT1291636B1 (en) * 1997-04-22 1999-01-19 Whirlpool Co MODULAR HEAT EXCHANGER PARTICULARLY FOR WASHING DRYERS AND SIMILAR MACHINES
DE19722097A1 (en) * 1997-05-27 1998-12-03 Behr Gmbh & Co Heat exchanger and heat exchanger arrangement for a motor vehicle
DE19723878B4 (en) * 1997-06-06 2007-10-25 Behr Gmbh & Co. Kg Heat exchanger
DE10138247A1 (en) * 2001-08-03 2003-02-13 Behr Gmbh & Co Heat exchanger arrangement used in motor vehicles comprises a heat exchanger having adjacent pipe ends designed and joined together to form a collector
CN106839854A (en) * 2017-01-26 2017-06-13 上海宝丰机械制造有限公司 Heat exchanger tube and the evaporative condenser including it

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2345331A (en) * 1942-04-18 1944-03-28 Morris Motors Ltd Heat interchange apparatus
DE2747275A1 (en) * 1977-10-21 1979-04-26 Volkswagenwerk Ag HEAT EXCHANGERS, IN PARTICULAR LIGHT METAL HEAT EXCHANGERS
US4269265A (en) * 1979-11-29 1981-05-26 Modine Manufacturing Company Tubular heat exchanger with turbulator
DE8126746U1 (en) * 1981-09-14 1982-02-25 Süddeutsche Kühlerfabrik Julius Fr. Behr GmbH & Co KG, 7000 Stuttgart FLAT TUBE HEAT EXCHANGER WITH TURBULEN INSERT
DE3502619A1 (en) * 1985-01-26 1986-07-31 Süddeutsche Kühlerfabrik Julius Fr. Behr GmbH & Co KG, 7000 Stuttgart HEAT EXCHANGER, ESPECIALLY REFRIGERANT EVAPORATOR

Also Published As

Publication number Publication date
JPS6317391A (en) 1988-01-25
ATE43707T1 (en) 1989-06-15
EP0253167B1 (en) 1989-05-31
EP0253167A1 (en) 1988-01-20
DE3760214D1 (en) 1989-07-06
ES2008864B3 (en) 1989-08-16
DE3622953A1 (en) 1988-01-21

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