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JPH054599B2 - - Google Patents
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JPH054599B2 - - Google Patents

Info

Publication number
JPH054599B2
JPH054599B2 JP254985A JP254985A JPH054599B2 JP H054599 B2 JPH054599 B2 JP H054599B2 JP 254985 A JP254985 A JP 254985A JP 254985 A JP254985 A JP 254985A JP H054599 B2 JPH054599 B2 JP H054599B2
Authority
JP
Japan
Prior art keywords
refrigerant
pipe
port
flat
flange
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
JP254985A
Other languages
Japanese (ja)
Other versions
JPS61161398A (en
Inventor
Toshio Oohara
Yoshuki Yamauchi
Yoshio Myata
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.)
Denso Corp
Original Assignee
NipponDenso 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 NipponDenso Co Ltd filed Critical NipponDenso Co Ltd
Priority to JP254985A priority Critical patent/JPS61161398A/en
Publication of JPS61161398A publication Critical patent/JPS61161398A/en
Publication of JPH054599B2 publication Critical patent/JPH054599B2/ja
Granted 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
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/0246Arrangements for connecting header boxes with flow lines
    • F28F9/0251Massive connectors, e.g. blocks; Plate-like connectors
    • 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
    • F28D1/03Heat-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 plate-like or laminated conduits
    • F28D1/0308Heat-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 plate-like or laminated conduits the conduits being formed by paired plates touching each other
    • F28D1/0325Heat-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 plate-like or laminated conduits the conduits being formed by paired plates touching each other the plates having lateral openings therein for circulation of the heat-exchange medium from one conduit to another
    • 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
    • F28F9/0246Arrangements for connecting header boxes with flow lines

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (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] 本発明は、冷凍装置の蒸発器などとして使用す
るため積層型熱交換器に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a stacked heat exchanger for use as an evaporator in a refrigeration system or the like.

[従来の技術] 伝熱媒体の出入口を備えており、偏平な薄い盤
状をなす多数の偏平管を各出入口がそれぞれ連接
されるようにして積層合体させた構造を持つた、
主として冷凍装置の冷媒蒸発器として使用され
る、当業界でいう所の積層型熱交換器は、第14
図および第15図に示された如き一般的構造を備
えている。
[Prior Art] A heat transfer medium has an inlet/outlet for a heat transfer medium, and has a structure in which a large number of flat tubes in the shape of a flat thin plate are laminated and combined so that each inlet/outlet is connected to each other.
The laminated heat exchanger in the art, which is mainly used as a refrigerant evaporator in refrigeration equipment, is the 14th layer heat exchanger.
It has a general structure as shown in FIG.

第14図は冷媒蒸発器としての熱交換器の正面
図、第15図はその部分拡大断面図、第16図は
冷媒蒸気圧のかかりかたを示し、第17図は熱交
換器内における冷媒の流れ方を説明した部分断面
図であつて、A1,A2……は薄い盤状をなす偏
平管群、B1,B2……は偏平管Aに設けた冷媒
分配管または集合管の挿通用孔の周辺部を膨出さ
せて形成された冷媒の出入用ポート部、aは相隣
るポートの固着面、bは相隣る偏平管Aの下端部
の接合固着個所、dは2分割構造を有する偏平管
Aの衝接合体ラインである。3は偏平管A群に冷
媒を配分させるための分配管、4は配分された冷
媒を再び集合させるための集合管で、この図では
3の背後に位置する。5,6は冷媒の分配管3に
ポート部B群のそれぞれと連通されるような配置
をもつて設けられた冷媒の出口または入口孔であ
る。冷媒の分配(集合)管3,4は、盤状偏平管
A群の各々のポート部Bを貫くようにして設けら
れている挿通用孔efを貫通させる状態のもとに組
付けられる。7と8は冷媒の循環用配管、9は偏
平管A群の間〓部に取付けたコルゲートフインで
ある。
Fig. 14 is a front view of a heat exchanger as a refrigerant evaporator, Fig. 15 is a partially enlarged sectional view thereof, Fig. 16 shows how the refrigerant vapor pressure is applied, and Fig. 17 shows the refrigerant in the heat exchanger. It is a partial cross-sectional view explaining how the refrigerant flows, where A1, A2... are a group of thin plate-shaped flat tubes, and B1, B2... are holes for insertion of a refrigerant distribution pipe or a collecting pipe provided in the flat pipe A. The refrigerant inlet/outlet port is formed by expanding the peripheral part of the refrigerant, a is the fixation surface of the adjacent ports, b is the joining fixation point of the lower end of the adjacent flat tube A, and d is the two-part structure. This is the collision line of the flat tube A having the structure shown in FIG. 3 is a distribution pipe for distributing refrigerant to the flat tube group A, and 4 is a collecting pipe for collecting the distributed refrigerant again, which is located behind 3 in this figure. Reference numerals 5 and 6 denote refrigerant outlet or inlet holes provided in the refrigerant distribution pipe 3 so as to communicate with each of the port portions B group. The refrigerant distribution (collection) pipes 3 and 4 are assembled in such a manner that they pass through the insertion holes ef provided so as to pass through the port portions B of each of the plate-shaped flat tubes A group. 7 and 8 are piping for refrigerant circulation, and 9 is a corrugated fin installed between the flat tubes A group.

この構造の熱交換器では、配管7から供給され
る冷媒は第17図に矢印で示されたように冷媒分
配管3に流入し、冷媒入口孔5からそれぞれ対応
する位置にあるポート部Bを経て偏平A内を流下
し、下端に達すると管内を縦方向に2区画に分割
する仕切壁を設けた切決部を通過した後、上昇に
転じて再びポート部Bに戻り、冷媒集合管4に設
けられた冷媒出口孔6から集合管4内に流入す
る。冷媒は偏平管A内を通過する間にコルゲート
フイン9を介して外気から気化の潜熱を吸収して
冷凍仕事を果し、再循環のために配管8を経て冷
媒圧縮機に吸入されるように構成されている。
In the heat exchanger with this structure, the refrigerant supplied from the pipe 7 flows into the refrigerant distribution pipe 3 as indicated by the arrows in FIG. After that, it flows down inside the flat A, and when it reaches the lower end, it passes through a cut section with a partition wall that vertically divides the inside of the pipe into two sections, then turns upward and returns to the port section B, where it flows into the refrigerant collecting pipe 4. The refrigerant flows into the collecting pipe 4 from the refrigerant outlet hole 6 provided in the refrigerant. While passing through the flat tube A, the refrigerant absorbs the latent heat of vaporization from the outside air through the corrugated fins 9 to perform refrigeration work, and is sucked into the refrigerant compressor via the pipe 8 for recirculation. It is configured.

[発明が解決しようとる問題点] 上述の如き従来の熱交換機は、第15図にみら
れるように、冷媒の分配管3または集合管4は、
その両端部を除いて偏平群A1,A2…、ポート
部B1,B2…に設けてある挿通用孔eまたはf
に単に插し通されているに過ぎない。従つて冷媒
分配(集合)管3,4とポート部Bに設けたその
挿通用孔eまたはfとの間にはすき間gが存在す
ることになる。
[Problems to be Solved by the Invention] In the conventional heat exchanger as described above, as shown in FIG. 15, the refrigerant distribution pipe 3 or collecting pipe 4 is
Insertion holes e or f provided in the flat groups A1, A2..., port portions B1, B2..., excluding both ends thereof
It is simply being rubbed through. Therefore, a gap g exists between the refrigerant distribution (collection) pipes 3, 4 and their insertion holes e or f provided in the port section B.

前述の如く、冷媒分配管3からポート部B内に
吐出された冷媒は、第16図に矢印イで示された
ように気化に伴なう蒸気圧をポート部Bの内壁面
に対して及ぼすので、ポート部Bは膨張作用力を
受けることになり、その結果として、第1には2
分割構造を有する偏平管Aの接合固着面dを引き
剥がす力Fが、また第2には分配管3の挿通用孔
eの口径を拡張させて口縁部に亀裂を生じさせる
力Gが発生する。そして支間距離が長く中間に補
強手段を施し難いこの種の構造の熱交換器は、偏
平間Aを構成するアルミニウムなどの金属板材の
厚みを増すことによつて耐圧強度の向上を図る他
なかつた。
As mentioned above, the refrigerant discharged from the refrigerant distribution pipe 3 into the port B exerts vapor pressure on the inner wall surface of the port B due to vaporization, as shown by arrow A in FIG. Therefore, the port portion B will receive an expansion force, and as a result, firstly, the second
A force F is generated that peels off the bonded fixed surface d of the flat tube A having a split structure, and a second force G is generated that expands the diameter of the insertion hole e of the distribution pipe 3 and causes a crack at the mouth edge. do. For heat exchangers with this type of structure, where the span distance is long and it is difficult to provide reinforcing means in the middle, the only way to improve the pressure resistance is to increase the thickness of the metal plate material such as aluminum that makes up the flat span A. .

さらにこの種の熱交換器では、冷媒の流路は冷
媒分配管3に設けた冷媒入口5群からそれぞれポ
ート部Bを経て各偏平管A1,A2…内に流入
し、管内の一方の区画内を流下した後、他方の区
画内を上昇して冷媒集合管4に設けられた出口孔
6に吸収されるように構成されているにもかかわ
らず、冷媒の分配(集合)管と偏平管Aの挿通用
孔e,fとの間にはすき間gが存在するために、
このような各偏平管ごとに独立した流路を確保す
ることができず、分配管3の上流側に位置する偏
平管A1のポート内に一旦流入した冷媒が管内に
流下ぜす、第17図矢印ロで示されたように、下
流側の偏平管A2のポート内に短絡的に流入して
しまい、冷媒分配管3による各ポート部B1,B
2…への均等分配機能がそこなわれる不都合が伴
なつた。
Furthermore, in this type of heat exchanger, the refrigerant flow path is such that the refrigerant flows from the 5 groups of refrigerant inlets provided in the refrigerant distribution pipe 3 through the respective port portions B into each of the flat pipes A1, A2, etc. Although the refrigerant distribution (collection) pipe and the flat pipe A Since there is a gap g between the insertion holes e and f,
It is not possible to secure an independent flow path for each such flat tube, and the refrigerant that has once flowed into the port of the flat tube A1 located on the upstream side of the distribution pipe 3 flows down into the tube. As shown by the arrow B, the refrigerant flows into the port of the flat tube A2 on the downstream side in a short-circuit manner, and the refrigerant distribution pipe 3 connects the ports B1 and B.
This resulted in the inconvenience that the function of equal distribution to...2 was impaired.

本発明は、偏平管Aのポート部Bの耐圧強度を
充分に高められて偏平管材料の肉厚が薄くて足り
ると共に、冷媒分配管3による冷媒分配機能を充
分に確保することのできる熱交換器を提供するこ
とを目的とする。
The present invention provides a heat exchanger that can sufficiently increase the pressure resistance of the port portion B of the flat tube A, so that the wall thickness of the flat tube material can be thin, and can sufficiently ensure the refrigerant distribution function by the refrigerant distribution pipe 3. The purpose is to provide equipment.

[問題点を解決するための手段] 上記の目的を達成するために本発明の熱交換器
は、偏平方向に2分割可能であり、該偏平面に伝
熱媒体の分配管または集合管の挿通用孔を設ける
と共に、該孔の周辺部を膨出させて伝熱媒体の出
入用ポート部を形成させてなる盤状偏平管群を積
層合体し、前記挿通用孔群に挿通させる如くに前
記分配管または重合管を組付けた構造を有する積
層型熱交換器において、前記挿通用孔の周縁にフ
ランジ状部が設けられており、且つ該フランジ状
部が前記分配管または集合管に固着された構成を
採用した。
[Means for Solving the Problems] In order to achieve the above object, the heat exchanger of the present invention can be divided into two in the flat direction, and a distribution pipe or a collecting pipe for the heat transfer medium is inserted into the flat plane. A group of disk-shaped flat tubes each having a communication hole and bulging out the peripheral portion of the hole to form a port for the entry and exit of a heat transfer medium are laminated together, and the tubes are inserted into the group of insertion holes. In a laminated heat exchanger having a structure in which distribution pipes or overlapping pipes are assembled, a flange-like part is provided at the periphery of the insertion hole, and the flange-like part is fixed to the distribution pipe or collecting pipe. A new configuration was adopted.

[作用] 上記の如き構造を備えた本発明の熱交換器は、
伝熱媒体の分配(集合)管の挿通用孔の周縁にフ
ランジ状部を設けることによつて、またこのフラ
ンジ状部の長さだけ伝熱媒体の出入ポート部の厚
さ、従つてポート部の容積が縮少されることによ
つて、伝熱媒体が呈する圧力に対するポート部の
耐圧強度を高めさせる。
[Function] The heat exchanger of the present invention having the above structure has the following features:
By providing a flange-like part on the periphery of the insertion hole of the heat transfer medium distribution (collection) pipe, the thickness of the heat transfer medium inlet/outlet port part, and therefore the port part, can be reduced by the length of this flange-like part. By reducing the volume of the port, the pressure resistance strength of the port portion against the pressure exerted by the heat transfer medium is increased.

そしてフランジ状部を伝熱媒体の分配(集合)
管の外周面に固着させることによつて耐圧強度が
さらに大幅に向上させると共に、偏平管群の相互
間を伝熱媒体が短絡的に流れて分配管の機能が減
殺されることを防止する。
Then, the flange-shaped part is used to distribute (collect) the heat transfer medium.
By fixing it to the outer peripheral surface of the tube, the pressure resistance is further improved significantly, and the function of the distribution pipe is prevented from being impaired due to the heat transfer medium flowing between the flat tube groups in a short-circuit manner.

[実施例] 以下に本発明の熱交換器を付図に基づいて具体
的に説明する。
[Example] The heat exchanger of the present invention will be specifically described below based on the accompanying drawings.

第1図ないし第6図は自動車用空気調和装置の
エバポレータとして本発明による熱交換器の構造
説明図であつて、エバポレータは、アルミニウム
板などからなる2枚のコアプレート1と2を、例
えていえば極めて偏平な“最中の皮”状に対向し
て貼り合せ、上端部に冷媒の出入用ポート部Bを
設けた偏平管A群を積層合体させてなる本体と、
積層合体されているポート部Bを插し貫くように
した組込まれており、各ポート部Bに冷媒を分配
し、各偏平管A内を一巡した冷媒を回収し、集合
させるための冷媒分配管3と冷媒集合管4、およ
びこれら両管に接続された冷媒供給配管7および
排出配管8並びに相隣る偏平管Aの管〓部に嵌め
込ませた伝熱面積増大用のコルゲートフイン9を
主要構成要素として成り立つている。15は補強
用の側壁板である。
Figures 1 to 6 are structural explanatory diagrams of a heat exchanger according to the present invention as an evaporator for an automobile air conditioner. For example, a main body formed by laminating and combining a group of flat tubes A, which are laminated together in an extremely flat "middle skin" shape and have a refrigerant inlet/outlet port part B at the upper end;
A refrigerant distribution pipe is built in so as to pass through the laminated and combined port parts B, and distributes the refrigerant to each port part B, and collects and collects the refrigerant that has made a round in each flat tube A. The main components are a refrigerant collecting pipe 4, a refrigerant supply pipe 7 and a discharge pipe 8 connected to these pipes, and a corrugated fin 9 fitted into the bottom part of the adjacent flat pipe A to increase the heat transfer area. It is made up of elements. 15 is a side wall plate for reinforcement.

偏平管Aは第3図および第4図に示されたよう
に、例えば厚さが0.4mm〜0.8mmの材質A3003のア
ルミニウム板の両表面に板厚比で約10%のろう材
A4004を溶融メツキ法などによつてあらかじめク
ラツドさせてあるコアプレート1と2とを、それ
ぞれ極く偏平な“最中の皮”状にプレス成形した
ものをろう付け法によつて貼り合せることによつ
て形作られている。両コアプレート1と2にはそ
の上端部に外側向きの膨出部1aと2aが設けら
れ、両膨出部1a,2aの内側空間が偏平管A内
への冷媒出入用ポート部Bとして機能する。また
両タンクプレート1と2にはそれぞれ偏平管A内
空間を2つの区画室に分割するための上下方向の
仕切壁1b,2bが設けられ、仕切壁1b,2b
の下端部が欠如していることによつて両区画室h
とiの連通路jが形成されている。そして区画室
hの上部に位置する分配管3には冷媒供給スリツ
ト3aが、また区画室iの上部に位置する集合管
4には冷媒排出スリツト4aが設けてあるので、
スリツト3aから流入した冷媒は区画室hを流下
し、その下端部に到つて連通路jを通過した後、
上昇に転じてスリツト4aに達する冷媒流路が形
成されることになる。コアプレート1と2にはそ
れぞれ冷媒の流路の細分化用と、偏平管Aの補強
のための多数の打出しリブ1cおよび2cが設け
られており、2枚のコアプレート1と2が貼り合
された時、両プレートのリブ1cと2cおよび仕
切壁1bと2bとは当接されてろう付け接合され
る。なお、傾斜向に配向されているリブ1cと2
cは、その斜向方向を反対向きにすることによつ
て両リブはX字型に交叉した状態のもとに衝接さ
れるので偏平管Aの構造強度が高められる。1
d,2dはコアプレート1および2の下端縁部を
直角に折り曲げて形成されたヒレ状部であつて、
相隣る偏平管Aの下端縁部の連結合体用部材とし
て機能する。lは相隣る偏平管Aのヒレ状部の当
接面、dはコアプレート1および2のそれぞれの
周縁部を繞る両者のろう付け合体用接合面であ
る。
As shown in Figures 3 and 4, the flat tube A is made of an aluminum plate made of A3003 with a thickness of 0.4 mm to 0.8 mm, and has a brazing material of about 10% of the plate thickness on both surfaces.
Core plates 1 and 2, which have been previously clad with A4004 using a melt plating method, are each press-molded into an extremely flat “skin in the middle” and then bonded together using a brazing method. It is shaped in a twisted manner. Both core plates 1 and 2 are provided with outward bulging portions 1a and 2a at their upper ends, and the inner spaces of both bulging portions 1a and 2a function as a port portion B for the refrigerant to enter and exit the flat tube A. do. Further, both tank plates 1 and 2 are respectively provided with vertical partition walls 1b and 2b for dividing the interior space of the flat tube A into two compartments.
Due to the lack of the lower end of both compartments h
A communication path j between and i is formed. The distribution pipe 3 located above the compartment h is provided with a refrigerant supply slit 3a, and the collecting pipe 4 located above the compartment i is provided with a refrigerant discharge slit 4a.
The refrigerant flowing from the slit 3a flows down the compartment h, reaches its lower end, passes through the communication path j, and then
A refrigerant flow path is formed which turns upward and reaches the slit 4a. The core plates 1 and 2 are provided with a large number of ribs 1c and 2c, respectively, for dividing the refrigerant flow path and reinforcing the flat tube A. When assembled, the ribs 1c and 2c and the partition walls 1b and 2b of both plates are brought into contact and brazed together. Note that the ribs 1c and 2 are oriented in an inclined direction.
In c, by making the diagonal directions opposite to each other, both ribs abut against each other in an X-shaped crossing state, thereby increasing the structural strength of the flat tube A. 1
d and 2d are fin-like parts formed by bending the lower edges of the core plates 1 and 2 at right angles,
It functions as a connecting body member for the lower end edges of adjacent flat tubes A. 1 is a contact surface of the fin-like portions of adjacent flat tubes A, and d is a joint surface for brazing and joining the core plates 1 and 2, which covers the respective peripheral edges of the core plates 1 and 2.

偏平管Aの冷媒出入口ポート部Bの両側面には
それぞれ冷媒分配管3と冷媒集合管4の挿通用孔
10および11が穿たれており、それぞれの孔の
周縁にはポート部Bの側面に対して直角をなして
外向きに伸びるフランジ状部12,13が形成さ
れている。
Holes 10 and 11 for insertion of the refrigerant distribution pipe 3 and the refrigerant collecting pipe 4 are bored on both sides of the refrigerant inlet/outlet port part B of the flat tube A, respectively, and holes 10 and 11 for insertion of the refrigerant distribution pipe 3 and the refrigerant collecting pipe 4 are bored on the sides of the port part B at the periphery of each hole. Flange-like portions 12, 13 are formed which extend outwardly at right angles thereto.

冷媒分配管3および冷媒集合管4は、偏平管A
1,A2…のポート部B1,B2…の積層合体層
を、第1図および第2図に示された如く、貫通し
た状態のもとにポート部B群にそれぞれ設けられ
ているフランジ状部12および13に嵌合され、
ろう付け接合法によつて固着されている。冷媒分
配管3と集合管4には、各々独立した冷媒通路を
内蔵する各偏平管Aに冷媒を供給するためのスリ
ツト3aと冷媒排出用のスリツト4aとがそれぞ
れポート部B1,B2…内に向けて開口するよう
に一定間隔をもつて第5図に示されたように設け
られている。
The refrigerant distribution pipe 3 and the refrigerant collecting pipe 4 are flat pipes A
As shown in FIGS. 1 and 2, the flange-shaped portions are respectively provided in the port portions B group, penetrating the laminated combined layers of port portions B1, B2, etc. of port portions B1, B2, and so on. 12 and 13,
It is fixed by brazing. In the refrigerant distribution pipe 3 and the collecting pipe 4, a slit 3a for supplying refrigerant to each flat pipe A having a built-in independent refrigerant passage, and a slit 4a for discharging refrigerant are provided in port portions B1, B2, respectively. As shown in FIG. 5, they are provided at regular intervals so as to open toward the opposite direction.

エバポレータへの冷媒の供給配管7または排出
配管8の取付手段を例示した第6図において、2
0は冷媒供給配管7または排出配管8の取付用の
金属製継手部材であつて、角筒状の本体部分21
に両開口端の栓体22と23をろう付けして作ら
れている。この継手部材20には冷媒配管7また
は8の嵌合用孔24と、冷媒分配管3または冷媒
集合管4の管端部を嵌合させるための孔25が設
けられている。7aは管端部の外径を嵌合用孔2
4の口径に合致させるための絞り加工部である。
継手部材20と冷媒配管7または8および冷媒分
配管3または冷媒集合管4とはろう付け接合によ
つて気密に合体される。
In FIG. 6 illustrating the means for attaching the refrigerant supply pipe 7 or discharge pipe 8 to the evaporator, 2
0 is a metal joint member for attaching the refrigerant supply pipe 7 or the discharge pipe 8, and is a rectangular cylindrical main body portion 21
It is made by brazing plugs 22 and 23 at both open ends. This joint member 20 is provided with a hole 24 for fitting the refrigerant pipe 7 or 8 and a hole 25 for fitting the pipe end of the refrigerant distribution pipe 3 or the refrigerant collecting pipe 4. 7a is the fitting hole 2 for the outer diameter of the tube end.
This is a drawing part to match the diameter of No. 4.
The joint member 20 and the refrigerant pipe 7 or 8 and the refrigerant distribution pipe 3 or the refrigerant collecting pipe 4 are airtightly joined together by brazing.

上記のような構造を備えたエバポレータの組立
方法は、従来のそれと異る所はなく、あらかじめ
ろう材がクラツドされているコアプレート1と2
および冷媒分配管3集合管4並びにろう材がクラ
ツドされていないコルゲートフイン9を第1図お
よび第2図に示された状態に仮組立し、治具によ
つて固定させたうえ、ろう付け炉に通入させるこ
とによつて組立が完了する。
The method of assembling an evaporator with the above structure is no different from that of conventional methods, and consists of core plates 1 and 2, which are clad with brazing filler metal in advance.
The refrigerant distribution pipe 3, the collector pipe 4, and the corrugated fin 9 in which the brazing material is not clad are temporarily assembled in the state shown in Figs. 1 and 2, fixed with a jig, and then Assembly is completed by passing it through.

第7図はエバポレータの外観斜視図であり、第
8図はエバポレータの内部での冷媒の流路を模式
的に説明した図であり、27と28は配管用ジヨ
イントである。kは各偏平管A内における冷媒の
流れ方を示した流線である。
FIG. 7 is an external perspective view of the evaporator, and FIG. 8 is a diagram schematically explaining a refrigerant flow path inside the evaporator, and 27 and 28 are piping joints. k is a streamline showing how the refrigerant flows within each flat tube A.

つぎに本発明による熱交換器の作動上の特徴
を、その部分的縦断面図として第9図および従来
の構造の熱交換器の部分的縦断面図としての第1
6図を参照しながら説明する。冷媒供給配管7か
ら冷媒分配管3内に送り込まれた液相冷媒は分配
管3に一定間隔をもつて設けれてている冷媒供給
用スリツト3aから各偏平管Aの冷媒出入用ポー
ト部Bに吐出され、外気熱を吸収することによつ
て気化膨脹が始まるので、ポート部Bの内壁面に
対して図の矢印で示されたように蒸気圧が及ぼさ
れ、既述の如く、2分割構成を有する偏平第Aの
ろう付け接合面dを引き剥がそうとする力Fと、
ポート部Bの両側面の冷媒分配管および集合管の
挿通用孔10および11の口径を拡張させて口縁
部に亀裂を生じさせるような作用力Gが発生す
る。しかし従来の構造の熱交換器の部分断面図と
しての第16図と対比すれば明らかなように、ポ
ート部Bはその両側面にフランジ状部12と13
を設けた分だけポート部Bの厚み(偏平方向の
巾)が狭められるので、ポートの内容積が相当程
度縮少されることによつてポート部Bが内圧によ
つて変形される度合が著しく少なくなり、従つて
接合面dに及ぼされる剥離作用力が大幅に低減さ
れる。この実施例ではポート部Bのフランジ状部
を含めた厚みを13.6mm、フランジ状部12および
13の長さをそれぞれ3.0mmに設定した。そして
フランジ状部12と13は冷媒分配管3に密に嵌
合させてろう付け固着されているので、ポート部
Bが内圧によつて膨脹し、変形させられる度合は
さらに格段に減少することになる、 ポート部Bと冷媒分配管3または集合管4とが
ろう付けによつて固着合体されたことによつて、
従来のエバポレータに存在した、相隣る偏平管A
の各ポート部Bを空間的に短絡させる間隙gが消
滅するので、この間隙gのために冷媒分配管3の
分配機能が低下するという従来の構造のエバポレ
ータの別の難点も同時に解消される。
Next, the operational characteristics of the heat exchanger according to the present invention will be described in FIG. 9, which is a partial longitudinal sectional view, and FIG.
This will be explained with reference to FIG. The liquid phase refrigerant sent into the refrigerant distribution pipe 3 from the refrigerant supply pipe 7 is passed through refrigerant supply slits 3a provided at regular intervals in the distribution pipe 3 to the refrigerant inlet/outlet port B of each flat tube A. As the gas is discharged and vaporization and expansion begins by absorbing outside air heat, vapor pressure is exerted on the inner wall surface of port B as shown by the arrow in the figure, and as mentioned above, the two-part structure is formed. A force F trying to peel off the brazed joint surface d of the flat No. A having
An acting force G is generated that expands the diameters of the insertion holes 10 and 11 of the refrigerant distribution pipe and collecting pipe on both sides of the port portion B, and causes cracks to occur at the mouth edges. However, as is clear from FIG. 16, which is a partial sectional view of a heat exchanger with a conventional structure, the port portion B has flange-like portions 12 and 13 on both sides thereof.
Since the thickness (width in the flat direction) of the port portion B is reduced by the amount that is provided, the internal volume of the port is reduced to a considerable extent, and the degree to which the port portion B is deformed by internal pressure is significantly reduced. Therefore, the peeling force exerted on the bonding surface d is significantly reduced. In this example, the thickness of the port portion B including the flange portion was set to 13.6 mm, and the lengths of the flange portions 12 and 13 were each set to 3.0 mm. Since the flange-shaped parts 12 and 13 are tightly fitted to the refrigerant distribution pipe 3 and fixed by brazing, the degree to which the port part B is expanded and deformed by internal pressure is further significantly reduced. Because the port part B and the refrigerant distribution pipe 3 or the collecting pipe 4 are firmly joined together by brazing,
Adjacent flat tubes A that existed in conventional evaporators
Since the gap g that spatially short-circuits the respective port portions B is eliminated, another drawback of the conventional structure of the evaporator, that is, the distribution function of the refrigerant distribution pipe 3 is degraded due to the gap g, is also solved.

第10図ないし第12図に偏平管Aのポート部
Bの両側面に設けるフランジ状部の別の形状事例
をそれぞれ示した。第10図のフランジ状部30
および31にはその先端面に外周側向きの折り返
し部30aおよび31aが設けられているので、
フランジ状部がポート部Bの内圧によつてその口
径を拡張させられるのに耐える抵抗力を増大させ
ることができるし、エバポレータの構造強度の向
上にも寄与する。
10 to 12 show examples of other shapes of the flange-like portions provided on both sides of the port portion B of the flat tube A. Flange-shaped portion 30 in FIG.
and 31 are provided with folded parts 30a and 31a facing toward the outer circumferential side on their tip surfaces, so that
It is possible to increase the resistance force with which the flange-shaped portion is able to withstand expansion of its diameter due to the internal pressure of the port portion B, and also contributes to improving the structural strength of the evaporator.

第11図に示されたフランジ状部32および3
3は相隣る偏平管Aの各ポート部に設けられたフ
ランジ状部が互いに重なり合つた状態のもとにろ
う付けされるように構成されているので、前記の
実施例と同様な効果が得られる。
Flanges 32 and 3 shown in FIG.
3 is constructed so that the flange-shaped parts provided at each port part of adjacent flat tubes A are brazed to each other while overlapping each other, so that the same effect as in the previous embodiment can be obtained. can get.

第12図の実施例のフランジ状部34および3
5は、第11図に示されたフランジ状部32に設
けたフランジ状部の重ね合せ用膨出部が省略され
ている。
Flanges 34 and 3 of the embodiment of FIG.
5, the bulge portion for overlapping the flange portions provided on the flange portion 32 shown in FIG. 11 is omitted.

また第13図に示された実施例では、偏平管A
のポート部Bの内容積を極端に小さくして耐圧強
度を高めるために、両フランジ状部36および3
7のポートの各一半部の接合固着面dとが直線で
結ばれるようなポート部形状が与えられている。
Further, in the embodiment shown in FIG. 13, the flat tube A
In order to extremely reduce the internal volume of the port portion B and increase the pressure resistance, both flange-like portions 36 and 3
The port portion is shaped such that the joining and fixing surfaces d of each half of the ports No. 7 are connected with a straight line.

なお、本実施例では第8図に示すごとく冷媒の
流れは冷却分配管3から冷媒集合管4へ各偏平管
A内の冷媒通路に沿つてU字形状に一度に流れる
ものであるが、少なくとも冷媒分配管3、さらに
は必要に応じて冷媒集合管4部に冷媒の流通を阻
止する仕切り板を設けることにより、一度に冷媒
が流れ込む冷媒通路数を減らし、各冷媒通路での
冷媒の分配量をより均一にし冷媒分配管3から冷
媒集合管4へさらに冷媒分配管3へ戻し再び冷媒
集合管4へというように繰り返し冷媒を流しても
良いことは、明らかである。
In this embodiment, as shown in FIG. 8, the refrigerant flows all at once in a U-shape from the cooling distribution pipe 3 to the refrigerant collecting pipe 4 along the refrigerant passages in each flat tube A. By providing a partition plate to block the flow of refrigerant in the refrigerant distribution pipe 3 and, if necessary, in the refrigerant collecting pipe 4, the number of refrigerant passages through which refrigerant flows at once can be reduced, and the amount of refrigerant distributed in each refrigerant passage can be reduced. It is clear that the refrigerant may be made to flow more uniformly from the refrigerant distribution pipe 3 to the refrigerant collecting pipe 4, then back to the refrigerant distribution pipe 3, and then again to the refrigerant collecting pipe 4, and so on.

[発明の効果] 本発明による熱交換器は次のような効果を奏す
る。
[Effects of the Invention] The heat exchanger according to the present invention has the following effects.

(イ) 各偏平管のポート部の両側面の冷媒分配(集
合)管の挿通用孔の口縁部にフランジ状部を設
けたことによつて、ポート部の厚さが減少した
部だけポート内容積が縮少され、冷媒蒸気圧に
対するポート部の耐圧強度を著しく向上させら
れる。そして相隣る偏平管の間隙巾は不変であ
るので、コルゲートフインの表面積も不変に保
たれる。
(b) By providing a flange-like part on the edge of the insertion hole of the refrigerant distribution (collecting) pipe on both sides of the port part of each flat tube, only the part where the thickness of the port part is reduced becomes a port. The internal volume is reduced, and the pressure resistance of the port against refrigerant vapor pressure is significantly improved. Since the width of the gap between adjacent flat tubes remains unchanged, the surface area of the corrugated fin also remains unchanged.

(ロ) 前記(イ)の効果によつて偏平管を構成するコア
プレートの肉厚を節減することができ、材料費
と重量の低減が図られる。
(b) Due to the effect of (a) above, the wall thickness of the core plate constituting the flat tube can be reduced, leading to reductions in material costs and weight.

(ハ) ポート部のフランジ状部を冷媒分配(集合)
管に気密的にろう付けして両者を固着させたの
で、ポート部の構造強度(耐変形性)はさらに
飛躍的に向上させられる。
(c) Refrigerant distribution (collection) using the flange-shaped part of the port
Since the tube is airtightly brazed and the two are fixed together, the structural strength (deformation resistance) of the port section can be further dramatically improved.

(ニ) 前記(ハ)の処置を講じたことによつて、従来の
熱交換器にみられた如き、ポート部の両側面の
冷媒分配(集合)管の挿通用孔と挿通配管との
間にすき間が存在しなくなるので、相隣るポー
ト部間の短絡的冷媒流は生せず、冷媒を各ポー
ト部に均等に分配でき、熱交換性能が向上され
る。
(d) By taking the measures in (c) above, the gap between the insertion holes of the refrigerant distribution (collecting) pipes on both sides of the port section and the insertion piping, as seen in conventional heat exchangers. Since there is no gap between the ports, there is no short-circuit refrigerant flow between adjacent port sections, and the refrigerant can be evenly distributed to each port section, improving heat exchange performance.

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

第1図ないし第13図は本発明による熱交換器
の実施例図であつて、第1図は正面図、第2図は
第1図の部分拡大縦断面図、第3図および第4図
は偏平管を構成する2枚のタンクプレートの内の
一方の側断面図と平面図、第5図は冷媒分配(集
合)管の側面図と横断面図、第6図は熱交換器へ
の冷媒配管の取付方法を説明した斜視図、第7図
は熱交換器の外観斜視図、第8図は熱交換器の内
部での冷媒の流路を示した模式的説明図、第9図
はポート部に冷媒の蒸気圧が及ぼされる状況を説
明した図、第10図ないし第12図はポート部に
形成されるフランジ状部の別の形状をそれぞれ例
示したポート部近傍の縦断面図、第13図はポー
ト部の形状の別の事例を示したポート部近傍の縦
断面図、第14図ないし第17図は従来の熱交換
器としてのエバポレータに関する図面であつて、
第14図は正面図、第15図は第14図の部分拡
大縦断面図、第16図はポート部に冷媒蒸気圧が
及ぼされる状況の説明図、第17図は冷媒分配管
から各偏平管のポート部に冷媒が流入する状況を
示した説明図である。 図中、A……偏平管、B……ポート部、1,2
……コアプレート、3……冷媒分配管、4……冷
媒集合管、3a,4a……冷媒出入口スリツト、
12,13……フランジ状部、d……偏平管の貼
り合せ接合面。
1 to 13 are views showing an embodiment of the heat exchanger according to the present invention, in which FIG. 1 is a front view, FIG. 2 is a partially enlarged vertical sectional view of FIG. 1, and FIGS. 3 and 4. 5 is a side sectional view and a plan view of one of the two tank plates that make up the flat tube, FIG. 5 is a side view and cross sectional view of the refrigerant distribution (collection) pipe, and FIG. FIG. 7 is an external perspective view of the heat exchanger, FIG. 8 is a schematic diagram showing the refrigerant flow path inside the heat exchanger, and FIG. 9 is a perspective view explaining how to install the refrigerant piping. 10 to 12 are longitudinal cross-sectional views of the vicinity of the port section illustrating different shapes of the flange-shaped portion formed in the port section, and FIG. FIG. 13 is a longitudinal sectional view near the port section showing another example of the shape of the port section, and FIGS. 14 to 17 are drawings regarding an evaporator as a conventional heat exchanger,
Fig. 14 is a front view, Fig. 15 is a partial enlarged vertical sectional view of Fig. 14, Fig. 16 is an explanatory diagram of the situation in which refrigerant vapor pressure is applied to the port, and Fig. 17 is from the refrigerant distribution pipe to each flat pipe. FIG. 2 is an explanatory diagram showing a situation in which refrigerant flows into a port portion of the vehicle. In the diagram, A...Flat tube, B...Port section, 1, 2
... core plate, 3 ... refrigerant distribution pipe, 4 ... refrigerant collecting pipe, 3a, 4a ... refrigerant inlet/outlet slit,
12, 13...flange-shaped portion, d...bonding joint surface of flat tube.

Claims (1)

【特許請求の範囲】 1 偏平方向に2分割可能であり、該偏平面に伝
熱媒体の分配管または集合管の挿通用孔を設ける
と共に、該孔の周辺部を膨出させて伝熱媒体の出
入用ポート部を形成させてなる盤状偏平管群を積
層合体し、前記挿通用孔群に挿通させる如くに前
記分配管または重合管を組付けた構造を有する積
層型熱交換器において、 前記挿通用孔の周縁にフランジ状部が設けられ
ており、且つ該フランジ状部が前記分配管または
集合管に固着されていることを特徴とする熱交換
器。
[Scope of Claims] 1. It can be divided into two parts in the flat direction, and a hole for the insertion of a distribution pipe or a collecting pipe for the heat transfer medium is provided in the flat plane, and the periphery of the hole is bulged to allow the heat transfer medium to pass through. In a laminated heat exchanger having a structure in which a group of plate-shaped flat tubes each forming an inlet/outlet port portion are laminated and combined, and the distribution tube or superimposed tube is assembled so as to be inserted into the insertion hole group, A heat exchanger characterized in that a flange-like part is provided at the periphery of the insertion hole, and the flange-like part is fixed to the distribution pipe or the collecting pipe.
JP254985A 1985-01-10 1985-01-10 Heat exchanger Granted JPS61161398A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP254985A JPS61161398A (en) 1985-01-10 1985-01-10 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP254985A JPS61161398A (en) 1985-01-10 1985-01-10 Heat exchanger

Publications (2)

Publication Number Publication Date
JPS61161398A JPS61161398A (en) 1986-07-22
JPH054599B2 true JPH054599B2 (en) 1993-01-20

Family

ID=11532459

Family Applications (1)

Application Number Title Priority Date Filing Date
JP254985A Granted JPS61161398A (en) 1985-01-10 1985-01-10 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS61161398A (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01178466U (en) * 1988-06-02 1989-12-20
DE3917173C2 (en) * 1989-05-30 1994-08-25 Showa Aluminium Co Ltd Process for the production of a heat exchanger collector
AU663964B2 (en) * 1992-08-31 1995-10-26 Mitsubishi Jukogyo Kabushiki Kaisha Stacked heat exchanger
US5431217A (en) * 1993-11-09 1995-07-11 General Motors Corporation Heat exchanger evaporator
JPH07190650A (en) * 1993-12-28 1995-07-28 Rinnai Corp Heat exchanger
US6338383B1 (en) 1999-12-22 2002-01-15 Visteon Global Technologies, Inc. Heat exchanger and method of making same
JP2002130988A (en) * 2000-10-20 2002-05-09 Mitsubishi Heavy Ind Ltd Laminated heat-exchanger
CN110966885A (en) * 2018-09-29 2020-04-07 浙江盾安热工科技有限公司 Flat tubes and heat exchangers
JP6971954B2 (en) * 2018-12-05 2021-11-24 株式会社ユタカ技研 Heat exchanger

Also Published As

Publication number Publication date
JPS61161398A (en) 1986-07-22

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