[go: up one dir, main page]

JP2936775B2 - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JP2936775B2
JP2936775B2 JP7331591A JP7331591A JP2936775B2 JP 2936775 B2 JP2936775 B2 JP 2936775B2 JP 7331591 A JP7331591 A JP 7331591A JP 7331591 A JP7331591 A JP 7331591A JP 2936775 B2 JP2936775 B2 JP 2936775B2
Authority
JP
Japan
Prior art keywords
pipe
tank
partition walls
refrigerant
opening
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
JP7331591A
Other languages
Japanese (ja)
Other versions
JPH04309766A (en
Inventor
山内  芳幸
昌宏 下谷
恵津夫 長谷川
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
Denso Corp
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 Denso Corp filed Critical Denso Corp
Priority to JP7331591A priority Critical patent/JP2936775B2/en
Publication of JPH04309766A publication Critical patent/JPH04309766A/en
Application granted granted Critical
Publication of JP2936775B2 publication Critical patent/JP2936775B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • F28F9/026Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
    • F28F9/027Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes
    • F28F9/0273Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes with multiple holes
    • 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
    • F28D1/0333Heat-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 the plates having integrated connecting members

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】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、冷媒蒸発器、冷媒凝縮
器、ヒータコア、ラジエータまたはオイルクーラ等の熱
交換器に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger such as a refrigerant evaporator, a refrigerant condenser, a heater core, a radiator or an oil cooler.

【0002】[0002]

【従来の技術】従来より、図4および図5に示したよう
に、冷媒を蒸発させるチューブ部101、およびこのチ
ューブ部101の一端部に入口タンク部102を有する
複数の冷媒流路管103を積層してなる積層型熱交換器
100において、複数のチューブ部101毎に均等に冷
媒を分配する供給孔104を形成したパイプ105を入
口タンク部102内に配設したもの(例えば実公昭53
−45875号公報など)が提案されている。
2. Description of the Related Art Conventionally, as shown in FIGS. 4 and 5, a tube portion 101 for evaporating a refrigerant and a plurality of refrigerant flow tubes 103 having an inlet tank portion 102 at one end of the tube portion 101 are provided. In the laminated heat exchanger 100, a pipe 105 having a supply hole 104 for evenly distributing a refrigerant for each of a plurality of tube portions 101 is disposed in an inlet tank portion 102 (for example, Japanese Utility Model Publication No. 53-53).
No. 45875) has been proposed.

【0003】そして、この積層型熱交換器100におい
ては、仕切り壁106に形成された開口部107の内径
とパイプ105の外径との差が0.1mm未満となるよう
に形成して、入口タンク部102の仕切り壁106とパ
イプ105との間に隙間がないようにしている。
In the laminated heat exchanger 100, the difference between the inner diameter of the opening 107 formed in the partition wall 106 and the outer diameter of the pipe 105 is less than 0.1 mm, and the inlet is formed. There is no gap between the partition wall 106 of the tank 102 and the pipe 105.

【0004】この理由は、入口タンク部102の仕切り
壁106とパイプ105との間を隙間なくろう付けによ
りシールしないと、パイプ105によって複数のチュー
ブ部101毎に均等に冷媒を分配する目的を達成するこ
とができないからである。
The reason for this is that if the space between the partition wall 106 of the inlet tank 102 and the pipe 105 is not sealed by brazing without any gap, the object of uniformly distributing the refrigerant to the plurality of tube parts 101 by the pipe 105 is achieved. Because they cannot do it.

【0005】[0005]

【発明が解決しようとする課題】ところが、入口タンク
部102の仕切り壁106とパイプ105との間に隙間
のない寸法では、図4に示したように、複数の冷媒流路
管103を積層した後に、パイプ105を各開口部10
7を貫通するように複数の冷媒流路管103の入口タン
ク部102に挿入する方法。あるいは、図5に示したよ
うに、パイプ105に冷媒流路管103を構成するコア
プレート108を1枚ずつ差し込んでいく方法のどちら
の方法を採用したとしても、パイプ105の外周が仕切
り壁106に引っ掛かってしまい、冷媒流路管103の
入口タンク部102とパイプ105との組み付けが容易
に行えなかった。
However, in a case where there is no gap between the partition wall 106 of the inlet tank 102 and the pipe 105, a plurality of refrigerant flow pipes 103 are stacked as shown in FIG. Later, the pipe 105 is connected to each opening 10.
7 is inserted into the inlet tank section 102 of the plurality of refrigerant flow pipes 103 so as to penetrate the refrigerant pipes 7. Alternatively, as shown in FIG. 5, the outer periphery of the pipe 105 is divided into the partition wall 106 regardless of the method of inserting the core plate 108 constituting the refrigerant flow path tube 103 into the pipe 105 one by one. , And the assembling of the inlet tank portion 102 of the refrigerant flow pipe 103 and the pipe 105 could not be easily performed.

【0006】本発明は、タンクとパイプとの組み付けが
容易で、しかもパイプの外周とタンクの複数の仕切り壁
とを確実にシールする熱交換器の提供を目的とする。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a heat exchanger that can easily assemble a tank and a pipe and that reliably seals the outer periphery of the pipe and a plurality of partition walls of the tank.

【0007】[0007]

【課題を解決するための手段】本発明は、並列して配設
され、内部を流れる熱媒体が熱交換される複数のチュー
ブ部と、これらのチューブ部の端部に接続されていると
ともに、前記複数のチューブ部毎に連通する複数のタン
ク部に区画する複数の仕切り壁を有し、且つこれらの仕
切り壁に開口部を有するタンクと、外周に前記複数のチ
ューブ部毎に均等に熱媒体を分配する供給孔を有し、前
記複数の仕切り壁の各開口部を貫通して前記タンク内に
挿入されたパイプとを備え、前記パイプは、前記複数の
仕切り壁の各開口部より設定寸法だけ細い径で、且つ内
圧と外圧との差圧により径が前記設定寸法以上増加する
管状部材により形成されている技術手段を採用した。
SUMMARY OF THE INVENTION According to the present invention, a plurality of tubes are arranged in parallel, and a heat medium flowing therethrough is exchanged with heat. The tubes are connected to ends of the tubes. A tank having a plurality of partition walls partitioned into a plurality of tank portions communicating with each of the plurality of tube portions, and a tank having openings in these partition walls; And a pipe inserted into the tank through each opening of the plurality of partition walls, and the pipe has a dimension set from each opening of the plurality of partition walls. The technical means is formed by a tubular member having a diameter which is only small and whose diameter is increased by the differential pressure between the internal pressure and the external pressure.

【0008】[0008]

【作用】パイプの径が複数の仕切り壁の各開口部より設
定寸法だけ細いので、タンクを複数のタンク部に区画す
る複数の仕切り壁の各開口部を貫通するようにタンク内
にパイプを挿入する際に、パイプの外周が複数の仕切り
壁に引っ掛かることなくタンク内に挿入される。
[Function] Since the diameter of the pipe is smaller than each opening of the plurality of partition walls by the set dimension, the pipe is inserted into the tank so as to penetrate each opening of the plurality of partition walls that divides the tank into a plurality of tank sections. At this time, the outer periphery of the pipe is inserted into the tank without being caught by the plurality of partition walls.

【0009】タンクにパイプを組み付けた後にパイプ内
に熱媒体等を流入させると、その熱媒体等がパイプの外
周に形成された供給孔を通過するときの圧力損失分だけ
パイプの内圧と外圧とに差圧が生ずる。この差圧によっ
てパイプの径が前述の設定寸法以上増加して、パイプの
外周と複数の仕切り壁とが密着する。このため、パイプ
の供給孔からあるタンク部内に流入した熱媒体は、パイ
プの外周と複数の仕切り壁との間から隣設する他のタン
ク部内に流入することはなくなる。したがって、パイプ
内に流入した熱媒体は、複数のチューブ部毎に均等に分
配されることとなる。
When a heat medium or the like is caused to flow into the pipe after the pipe is assembled in the tank, the internal and external pressures of the pipe are reduced by the pressure loss when the heat medium and the like pass through the supply holes formed on the outer periphery of the pipe. , A differential pressure occurs. Due to this pressure difference, the diameter of the pipe increases by more than the set dimension, and the outer periphery of the pipe and the plurality of partition walls come into close contact with each other. Therefore, the heat medium flowing into a certain tank portion from the supply hole of the pipe does not flow into another adjacent tank portion from between the outer periphery of the pipe and the plurality of partition walls. Therefore, the heat medium flowing into the pipe is evenly distributed for each of the plurality of tube portions.

【0010】[0010]

【実施例】本発明の熱交換器を図1ないし図3に示す一
実施例に基づき説明する。図1ないし図3は積層型冷媒
蒸発器を示した図である。積層型冷媒蒸発器1は、内部
に流入した気液混合冷媒と外部を通過する空気とを熱交
換させることによって、気液混合冷媒を冷媒ガスとする
ものである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A heat exchanger according to the present invention will be described with reference to one embodiment shown in FIGS. 1 to 3 are views showing a laminated refrigerant evaporator. The laminated refrigerant evaporator 1 uses the gas-liquid mixed refrigerant as a refrigerant gas by exchanging heat between the gas-liquid mixed refrigerant flowing into the inside and air passing outside.

【0011】この積層型冷媒蒸発器1は、一対の成型プ
レート2を接合して形成される冷媒流路管3、および隣
接された2つの冷媒流路管3間に配設されたコルゲート
フィン4を積層型冷媒蒸発器1の幅方向に複数積層して
炉中にて一体ろう付けされて組み立てられる。
The laminated refrigerant evaporator 1 has a refrigerant flow pipe 3 formed by joining a pair of molded plates 2 and a corrugated fin 4 disposed between two adjacent refrigerant flow pipes 3. Are laminated in the width direction of the laminated refrigerant evaporator 1 and brazed in a furnace to be assembled.

【0012】成型プレート2は、薄い板状のアルミニウ
ム合金の両面にろう材を被着させたクラッド板をプレス
加工することにより浅い皿状に形成されている。
The molding plate 2 is formed in a shallow dish shape by pressing a clad plate in which a brazing material is adhered to both surfaces of a thin plate-shaped aluminum alloy.

【0013】冷媒流路管3には、一端部に本発明のタン
ク部としてのカップ状の入口タンク部5およびカップ状
の出口タンク部(図示せず)が形成されている。また、
入口タンク部5と出口タンク部との間には、入口タンク
部5と出口タンク部とを略U字状に連通し、内部を流れ
る冷媒を空気と熱交換させる偏平な皿状のチューブ部6
が形成されている。
At one end of the refrigerant flow pipe 3, a cup-shaped inlet tank 5 and a cup-shaped outlet tank (not shown) are formed as the tank of the present invention. Also,
Between the inlet tank 5 and the outlet tank, the inlet tank 5 and the outlet tank communicate with each other in a substantially U-shape, and a flat dish-shaped tube 6 for exchanging heat between the refrigerant flowing therein and air.
Are formed.

【0014】なお、複数の入口タンク部5により本発明
のタンクとしての入口タンク7が形成されている。ま
た、複数の入口タンク部5は、それぞれ1つのチューブ
部6毎に連通し、隣設する入口タンク部5とを区画する
複数の仕切り壁8を有する。これらの仕切り壁8には、
円筒状のパイプ9が差し込まれる開口部10が形成され
ている。さらに、最も上流側に位置する入口タンク部5
とパイプ9との間は、硬質の環状部材11内に保持され
たパッキン材12によってシールされている。
The plurality of inlet tanks 5 form an inlet tank 7 as the tank of the present invention. Further, the plurality of inlet tanks 5 have a plurality of partition walls 8 that communicate with each one of the tube portions 6 and partition adjacent inlet tanks 5. On these partition walls 8,
An opening 10 into which a cylindrical pipe 9 is inserted is formed. Furthermore, the inlet tank 5 located at the most upstream side
The seal between the pipe and the pipe 9 is sealed by a packing material 12 held in a hard annular member 11.

【0015】パイプ9の外周には、それぞれ1つのチュ
ーブ部6に冷媒を分配するための供給孔13が形成され
ている。パイプ9は、気液混合冷媒が供給孔13を通過
する時の内部の圧力と外部の圧力との差圧により弾性変
形や塑性変形によって外径が増加し易い材質(例えば合
成ゴム、樹脂、アルミニウム等の金属)および肉厚(例
えばナイロン樹脂(商品名)の場合は肉厚1.5mm、ア
ルミニウムの場合は肉厚0.015mm)の管状部材であ
る。
A supply hole 13 for distributing the refrigerant to one tube portion 6 is formed on the outer periphery of the pipe 9. The pipe 9 is made of a material (for example, synthetic rubber, resin, aluminum, etc.) whose outer diameter is liable to increase due to elastic deformation or plastic deformation due to the differential pressure between the internal pressure and the external pressure when the gas-liquid mixed refrigerant passes through the supply hole 13. And the like (for example, 1.5 mm in the case of nylon resin (trade name) and 0.015 mm in the case of aluminum).

【0016】そして、本実施例では、図1に示したよう
に、仕切り壁8の開口部10の開口径をφD1 、パイプ
9の外径をφD2 としたとき、0.1mm≦D1 −D2
(設定寸法)≦2.0mmを満足するように仕切り壁8の
開口部10およびパイプ9を形成している。なお、D1
−D2 <0.1mmの場合は、仕切り壁8の開口部10に
パイプ9を差し込み難いため除くことにした。また、D
1 −D2 >2.0mmの場合は、パイプ9の強度が弱くな
るため除くことにした。
In this embodiment, as shown in FIG. 1, when the opening diameter of the opening 10 of the partition wall 8 is φD 1 and the outer diameter of the pipe 9 is φD 2, 0.1 mm ≦ D 1 −D 2
The opening 10 of the partition wall 8 and the pipe 9 are formed so as to satisfy (set dimensions) ≦ 2.0 mm. Note that D1
When -D2 <0.1 mm, the pipe 9 was difficult to be inserted into the opening 10 of the partition wall 8 and was therefore removed. Also, D
In the case of 1-D2> 2.0 mm, the strength of the pipe 9 was reduced, so that it was removed.

【0017】さらに、供給孔13の開口径をφdとした
とき、0.1mm≦d≦3.0mmを満足するように供給孔
13を形成している。なお、d<0.1mmの場合は、気
液混合冷媒がパイプ9内から吐出し難いため除くことに
した。d>3.0mmの場合は、気液混合冷媒がパイプ9
内から吐出する時の内部の圧力と外部の圧力との差圧が
あまり増加しないため除くことにした。
Further, when the opening diameter of the supply hole 13 is φd, the supply hole 13 is formed so as to satisfy 0.1 mm ≦ d ≦ 3.0 mm. In the case of d <0.1 mm, the gas-liquid mixed refrigerant is difficult to discharge from inside the pipe 9 and is therefore excluded. When d> 3.0 mm, the gas-liquid mixed refrigerant
Since the pressure difference between the internal pressure and the external pressure when discharging from the inside does not increase so much, it was decided to remove it.

【0018】本実施例の積層型冷媒蒸発器1の作用を図
1ないし図3に基づき説明する。この積層型冷媒蒸発器
1は、図1に示したように、仕切り壁8の開口部10の
開口径(φD1 )、パイプ9の外径(φD2 )を、0.
1mm≦D1 −D2 (設定寸法)≦2.0mmを満足するよ
うに形成している。
The operation of the laminated refrigerant evaporator 1 according to the present embodiment will be described with reference to FIGS. As shown in FIG. 1, the laminated refrigerant evaporator 1 has an opening diameter (φD 1) of the opening 10 of the partition wall 8 and an outer diameter (φD 2) of the pipe 9.
It is formed so as to satisfy 1 mm ≦ D 1 −D 2 (set dimension) ≦ 2.0 mm.

【0019】すなわち、仕切り壁8の開口部10の開口
径とパイプ9の外径との差である設定寸法が0.1mm以
上であるため、複数の冷媒流路管3を積層して一体ろう
付けした後に、パイプ9を複数の仕切り壁8の各開口部
10を貫通するように入口タンク7内に嵌め込む際に、
パイプ9の外周が仕切り壁8に引っ掛かることなく、ス
ムーズに挿入することができる。よって、入口タンク7
へのパイプ9の組み付け作業が著しく簡易なものとな
る。
That is, since the set dimension, which is the difference between the opening diameter of the opening 10 of the partition wall 8 and the outer diameter of the pipe 9, is at least 0.1 mm, a plurality of refrigerant flow pipes 3 are laminated and integrated. After fitting, when fitting the pipe 9 into the inlet tank 7 so as to penetrate each opening 10 of the plurality of partition walls 8,
The pipe 9 can be inserted smoothly without being caught on the partition wall 8 by the outer periphery. Therefore, the inlet tank 7
The operation of assembling the pipe 9 into the pipe becomes extremely simple.

【0020】製造された積層型冷媒蒸発器1を冷凍サイ
クルに組み込んで冷房運転を行うと、パイプ9内には気
液混合冷媒が流入する。パイプ9内に流入した気液混合
冷媒は、複数の供給孔13からこれらの供給孔13に応
じたそれぞれの入口タンク部5内に流入し、さらにそれ
ぞれのチューブ部6に流入する。
When the cooling operation is performed by incorporating the manufactured laminated refrigerant evaporator 1 into a refrigeration cycle, a gas-liquid mixed refrigerant flows into the pipe 9. The gas-liquid mixed refrigerant flowing into the pipe 9 flows from the plurality of supply holes 13 into the respective inlet tank portions 5 corresponding to the supply holes 13, and further flows into the respective tube portions 6.

【0021】このとき、図2に示したように、供給孔1
3の開口径(φd)は0.1mm≦d≦3.0mmを満足す
るように形成されている。このため、パイプ9の供給孔
13から気液混合冷媒がと吐出する際に、パイプ9の供
給孔13を気液混合冷媒が通過する時の圧力損失分だけ
パイプ9の内部の圧力と外部の圧力とに差圧が発生す
る。この内外圧差によってパイプ9の外径が設定寸法以
上に弾性膨張することにより、複数の仕切り壁8とパイ
プ9の外周面とが密着して確実にシールされるので、気
液混合冷媒が入口タンク7の仕切り壁8とパイプ9との
間から漏れて隣設する入口タンク部5内に流れ込むこと
はない。
At this time, as shown in FIG.
The opening diameter (φd) of No. 3 is formed so as to satisfy 0.1 mm ≦ d ≦ 3.0 mm. For this reason, when the gas-liquid mixed refrigerant is discharged from the supply hole 13 of the pipe 9, the internal pressure of the pipe 9 and the external pressure are reduced by the pressure loss when the gas-liquid mixed refrigerant passes through the supply hole 13 of the pipe 9. A differential pressure is generated with the pressure. Since the outer diameter of the pipe 9 elastically expands beyond a set size due to the difference between the inner and outer pressures, the plurality of partition walls 8 and the outer peripheral surface of the pipe 9 are tightly sealed and securely sealed. 7 does not leak from between the partition wall 8 and the pipe 9 and flow into the adjacent inlet tank 5.

【0022】したがって、パイプ9内に流入した気液混
合冷媒は、複数のチューブ部6毎に均一に分配されるた
め、複数のチューブ部6毎に均一な熱交換を行うことが
できる。このため、それぞれのチューブ部6における熱
交換効率の低下を抑えることができる。
Therefore, the gas-liquid mixed refrigerant that has flowed into the pipe 9 is evenly distributed to each of the plurality of tube portions 6, so that uniform heat exchange can be performed for each of the plurality of tube portions 6. For this reason, it is possible to suppress a decrease in heat exchange efficiency in each of the tube portions 6.

【0023】ここで、パイプ9の供給孔13を気液混合
冷媒が通過する時の膨張度合を調べるために実験を行っ
た。この実験に用いた寸法を後述する。パイプ9の外径
(φD2 )を15mmとし、設定寸法を0.5mmとした場
合、複数の仕切り壁8の各開口部10の内径(φD1 )
は15.5mmとなる。また、パイプ9の材質はナイロン
樹脂(商品名)〔E=2.0kg/mm2 〕で、肉厚が1.
5mmのものを使用した。
Here, an experiment was conducted to examine the degree of expansion when the gas-liquid mixed refrigerant passes through the supply hole 13 of the pipe 9. The dimensions used in this experiment will be described later. When the outer diameter (φD2) of the pipe 9 is 15 mm and the set dimension is 0.5 mm, the inner diameter (φD1) of each opening 10 of the plurality of partition walls 8 is set.
Is 15.5 mm. The material of the pipe 9 is nylon resin (trade name) [E = 2.0 kg / mm 2 ] and the wall thickness is 1.
The thing of 5 mm was used.

【0024】そして、チューブ部6の本数が20本のと
きパイプ9の供給孔13の数を20個とし、開口径(φ
d)を0.3mmとすると、冷房運転中にパイプ9の供給
孔13を気液混合冷媒が通過する時には、パイプ9の内
部の圧力と外部の圧力とに2kg/cm2 以上の差圧が発生
する。
When the number of the tube portions 6 is 20, the number of the supply holes 13 of the pipe 9 is set to 20, and the opening diameter (φ
Assuming that d) is 0.3 mm, when the gas-liquid mixed refrigerant passes through the supply hole 13 of the pipe 9 during the cooling operation, a differential pressure of 2 kg / cm 2 or more between the internal pressure and the external pressure of the pipe 9 is generated. Occur.

【0025】したがって、パイプ9の直径の歪は、下記
の式で表せる。 (ΔD2 /D2 )=ε=(σ0 /E)={(P・D2 )/2t}/E なお、Pは差圧、tはパイプ9の肉厚、Eはパイプ9の
ヤング率である。
Therefore, the distortion of the diameter of the pipe 9 can be expressed by the following equation. (ΔD2 / D2) = ε = (σ0 / E) = {(P · D2) / 2t} / E where P is the differential pressure, t is the wall thickness of the pipe 9, and E is the Young's modulus of the pipe 9.

【0026】すなわち、パイプ9の膨張度合は、下記の
式で表せる。 ΔD2 =D2 ×{(P・D2 )/2t}/E この上式に数値を代入すると、0.75mmとなり、パイ
プ9が0.75mm径方向に膨張することが分かる。
That is, the degree of expansion of the pipe 9 can be expressed by the following equation. .DELTA.D2 = D2.times. {(P.D2) / 2t} / E By substituting a numerical value into the above equation, it becomes 0.75 mm, and it can be seen that the pipe 9 expands in the radial direction of 0.75 mm.

【0027】このため、0.5mmの設定寸法、つまり、
複数の仕切り壁8の各開口部10とパイプ9の外周との
隙間は確実にシールすることができる。このようにし
て、他の材質および肉厚のパイプ9を採用したときも、
設定寸法を考慮に入れてそのパイプ9の膨張度合を設計
することによって、同様に複数の仕切り壁8の各開口部
10とパイプ9の外周とをシールできる。
Therefore, the set dimension of 0.5 mm, that is,
The gaps between the openings 10 of the plurality of partition walls 8 and the outer periphery of the pipe 9 can be reliably sealed. In this way, when a pipe 9 of another material and thickness is adopted,
By designing the degree of expansion of the pipe 9 in consideration of the set dimensions, each opening 10 of the plurality of partition walls 8 and the outer periphery of the pipe 9 can be similarly sealed.

【0028】(変形例)本実施例では、本発明を積層型
冷媒蒸発器に用いたが、本発明を積層型熱交換器以外の
冷媒蒸発器に用いても良い。また、本発明を冷媒凝縮
器、ヒータコア、ラジエータまたはオイルクーラ等に用
いても良い。
(Modification) In the present embodiment, the present invention is applied to a laminated refrigerant evaporator. However, the present invention may be applied to a refrigerant evaporator other than a laminated heat exchanger. Further, the present invention may be used for a refrigerant condenser, a heater core, a radiator, an oil cooler, or the like.

【0029】本実施例では、円筒形状のパイプを用いた
が、楕円形状、多穴断面形状のパイプを用いても良い。
また、運転時にパイプに発生する内外圧力差により弾性
膨張だけでなく、製作時の加圧によりパイプを塑性変形
させて複数の仕切り壁の各開口部とパイプの外周とをシ
ールしても良い。
In this embodiment, a cylindrical pipe is used. However, an elliptical pipe or a multi-hole cross-sectional pipe may be used.
Further, not only elastic expansion due to a pressure difference between the inside and outside generated in the pipe during operation but also plastic deformation of the pipe by pressurization at the time of manufacturing may seal each opening of the plurality of partition walls and the outer periphery of the pipe.

【0030】[0030]

【発明の効果】本発明は、タンク内に挿入される複数の
仕切り壁の各開口部より設定寸法だけ細い径の管状部材
によりパイプを形成することによって、タンクへのパイ
プの組み付け時に、パイプの外周が複数の仕切り壁に引
っ掛かることなくタンク内に挿入されるので、タンクへ
のパイプの組み付けをスムーズに行うことができる。
According to the present invention, a pipe is formed by a tubular member having a diameter smaller than a set dimension from each opening of a plurality of partition walls inserted into the tank, so that the pipe is attached to the tank when the pipe is assembled. Since the outer periphery is inserted into the tank without being caught by the plurality of partition walls, the pipe can be smoothly assembled to the tank.

【0031】しかも、内圧と外圧との差圧により径が設
定寸法以上増加する管状部材によりパイプを形成するこ
とによって、パイプをタンクに組み付けた後に、パイプ
内に熱媒体等を流入させるとパイプが径方向外方に膨張
するので、パイプの外周とタンクの複数の仕切り壁とを
確実にシールすることができる。
Further, by forming the pipe with a tubular member whose diameter increases by a predetermined dimension or more due to the differential pressure between the internal pressure and the external pressure, after the pipe is assembled into the tank and the heat medium or the like flows into the pipe, the pipe is formed. Since it expands radially outward, the outer periphery of the pipe and the plurality of partition walls of the tank can be reliably sealed.

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

【図1】本発明の積層型冷媒蒸発器の冷房運転前の状態
を示した断面図である。
FIG. 1 is a cross-sectional view showing a state before a cooling operation of a laminated refrigerant evaporator of the present invention.

【図2】本発明の積層型冷媒蒸発器の冷房運転中の状態
を示した断面図である。
FIG. 2 is a cross-sectional view showing a state in which a cooling operation of the laminated refrigerant evaporator of the present invention is performed.

【図3】本発明の積層型冷媒蒸発器を示した正面図であ
る。
FIG. 3 is a front view showing a laminated refrigerant evaporator of the present invention.

【図4】従来の積層型冷媒蒸発器の組み付け方法を示し
た断面図である。
FIG. 4 is a cross-sectional view illustrating a method of assembling a conventional laminated refrigerant evaporator.

【図5】従来の積層型冷媒蒸発器の組み付け方法を示し
た断面図である。
FIG. 5 is a sectional view showing a method of assembling a conventional laminated refrigerant evaporator.

【符号の説明】[Explanation of symbols]

1 積層型冷媒蒸発器(熱交換器) 5 入口タンク部(タンク部) 6 チューブ部 7 入口タンク(タンク) 8 仕切り壁 9 パイプ 10 開口部 13 供給孔 Reference Signs List 1 laminated refrigerant evaporator (heat exchanger) 5 inlet tank (tank) 6 tube 7 inlet tank (tank) 8 partition wall 9 pipe 10 opening 13 supply hole

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F28F 9/02 301 ──────────────────────────────────────────────────続 き Continuation of front page (58) Field surveyed (Int.Cl. 6 , DB name) F28F 9/02 301

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 並列して配設され、内部を流れる熱媒体
が熱交換される複数のチューブ部と、これらのチューブ
部の端部に接続されているとともに、前記複数のチュー
ブ部毎に連通する複数のタンク部に区画する複数の仕切
り壁を有し、且つこれらの仕切り壁に開口部を有するタ
ンクと、外周に前記複数のチューブ部毎に均等に熱媒体
を分配する供給孔を有し、前記複数の仕切り壁の各開口
部を貫通して前記タンク内に挿入されたパイプとを備
え、前記パイプは、前記複数の仕切り壁の各開口部より
設定寸法だけ細い径で、且つ内圧と外圧との差圧により
径が前記設定寸法以上増加する管状部材により形成され
ていることを特徴とする熱交換器。
1. A plurality of tube portions which are arranged in parallel and exchange heat with a heat medium flowing therethrough, are connected to ends of these tube portions, and communicate with each of the plurality of tube portions. A plurality of partition walls partitioned into a plurality of tank portions, and a tank having openings in these partition walls, and a supply hole on the outer periphery for uniformly distributing the heat medium for each of the plurality of tube portions. A pipe inserted through the opening of each of the plurality of partition walls into the tank, wherein the pipe has a diameter smaller than each of the openings of the plurality of partition walls by a set dimension, and an internal pressure. A heat exchanger characterized by being formed of a tubular member whose diameter increases by more than the set dimension due to a pressure difference from an external pressure.
JP7331591A 1991-04-05 1991-04-05 Heat exchanger Expired - Lifetime JP2936775B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7331591A JP2936775B2 (en) 1991-04-05 1991-04-05 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7331591A JP2936775B2 (en) 1991-04-05 1991-04-05 Heat exchanger

Publications (2)

Publication Number Publication Date
JPH04309766A JPH04309766A (en) 1992-11-02
JP2936775B2 true JP2936775B2 (en) 1999-08-23

Family

ID=13514620

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7331591A Expired - Lifetime JP2936775B2 (en) 1991-04-05 1991-04-05 Heat exchanger

Country Status (1)

Country Link
JP (1) JP2936775B2 (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3332428B2 (en) * 1992-11-30 2002-10-07 昭和電工株式会社 Stacked condenser and method of manufacturing the same
DE19719252C2 (en) * 1997-05-07 2002-10-31 Valeo Klimatech Gmbh & Co Kg Double-flow and single-row brazed flat tube evaporator for a motor vehicle air conditioning system
FR2769974B1 (en) * 1997-10-20 2000-01-07 Valeo Climatisation EVAPORATOR WITH IMPROVED HEAT EXCHANGE CAPACITY
US7017656B2 (en) * 2001-05-24 2006-03-28 Honeywell International, Inc. Heat exchanger with manifold tubes for stiffening and load bearing
DE102011003649A1 (en) 2011-02-04 2012-08-09 Behr Gmbh & Co. Kg Heat exchanger
US9568225B2 (en) 2013-11-01 2017-02-14 Mahle International Gmbh Evaporator having a hybrid expansion device for improved aliquoting of refrigerant
US10197312B2 (en) 2014-08-26 2019-02-05 Mahle International Gmbh Heat exchanger with reduced length distributor tube
US10126065B2 (en) 2015-06-17 2018-11-13 Mahle International Gmbh Heat exchanger assembly having a refrigerant distribution control using selective tube port closures
FR3059398A1 (en) * 2016-11-30 2018-06-01 Valeo Systemes Thermiques DEVICE FOR DISPENSING A REFRIGERANT FLUID INSIDE A COLLECTOR BOX OF A HEAT EXCHANGER FOR AN AIR CONDITIONING INSTALLATION OF A VEHICLE

Also Published As

Publication number Publication date
JPH04309766A (en) 1992-11-02

Similar Documents

Publication Publication Date Title
US4821797A (en) Fluid cooler
JP4129119B2 (en) Heat exchanger assembly using grommet and integral casting tank
US4546822A (en) Heat exchanger with adhesive seals
CN110017704B (en) Integrated heat exchanger
US20050061489A1 (en) Integrated multi-function return tube for combo heat exchangers
JP3760571B2 (en) Heat exchanger
JP2936775B2 (en) Heat exchanger
WO1999030100A1 (en) Heat exchanger
US20080000627A1 (en) Heat exchanger
JPH05272889A (en) Heat exchanger
JP2009138909A (en) Pipe joint device
JP2984326B2 (en) Heat exchanger
US6543530B2 (en) Heat exchanger having an improved pipe connecting structure
KR20130065174A (en) Heat exchanger for vehicle
US6209629B1 (en) Beaded plate for a heat exchanger and method of making same
JP4682494B2 (en) Heat exchanger
KR20210158512A (en) Heat exchanger
JP3405879B2 (en) Plate type refrigerant flow divider
JPH05215482A (en) Heat exchanger
JP4664114B2 (en) Multi-plate heat exchanger
KR100433959B1 (en) Plastic Oil Cooler
US20190353426A1 (en) Side member and heat exchanger having the same
US20080230214A1 (en) Heat exchanger and method of manufacturing the same
JP3409350B2 (en) Stacked heat exchanger
CN216409858U (en) Shell and tube heat exchanger with cavity

Legal Events

Date Code Title Description
FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080611

Year of fee payment: 9

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110611

Year of fee payment: 12

EXPY Cancellation because of completion of term