JPH0583838B2 - - Google Patents

Info

Publication number
JPH0583838B2
JPH0583838B2 JP60135782A JP13578285A JPH0583838B2 JP H0583838 B2 JPH0583838 B2 JP H0583838B2 JP 60135782 A JP60135782 A JP 60135782A JP 13578285 A JP13578285 A JP 13578285A JP H0583838 B2 JPH0583838 B2 JP H0583838B2
Authority
JP
Japan
Prior art keywords
fluid
fluid passage
flow path
fluid flow
flat plate
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
JP60135782A
Other languages
Japanese (ja)
Other versions
JPS61295492A (en
Inventor
Kazumi Tokizaki
Ryoichi Hoshino
Hirotaka Tanaka
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.)
Altemira Co Ltd
Original Assignee
Showa Aluminum 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 Showa Aluminum Corp filed Critical Showa Aluminum Corp
Priority to JP13578285A priority Critical patent/JPS61295492A/en
Publication of JPS61295492A publication Critical patent/JPS61295492A/en
Publication of JPH0583838B2 publication Critical patent/JPH0583838B2/ja
Granted 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
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0043Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another

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 この発明は、例えば大型オイルクーラ等に使用
せられる積層型熱交換器に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a stacked heat exchanger used, for example, in large oil coolers.

この明細書において、アルミニウムとは、純ア
ルミニウムおよびアルミニウム合金を含んで意味
するものとする。
In this specification, aluminum is meant to include pure aluminum and aluminum alloys.

従来の技術 近年、大型オイルクーラとしてアルミニウム製
積層型熱交換器が多く使用されている。この熱交
換器は、オイルの通過する第1流体流路と、これ
に対して直交方向に空気が流通する第2流体流路
とが平板により隔てられて上下に交互に配置され
ているものであるが、従来の熱交換器は、第1流
体流路を構成するチユーブと、チユーブ同志の間
の第2流体流路内に収められるフインとが、真空
ろう付け法によつて一体に接合され、その他の流
体導入用ヘツダおよび排出用ヘツダ並びに流体導
入管および排出管等が例えばアルゴン溶接によつ
て接合されることにより製造されていた。
BACKGROUND OF THE INVENTION In recent years, aluminum laminated heat exchangers have been widely used as large oil coolers. In this heat exchanger, a first fluid flow path through which oil passes and a second fluid flow path through which air flows perpendicularly to the first fluid flow path are separated by a flat plate and are arranged vertically alternately. However, in conventional heat exchangers, the tubes forming the first fluid flow path and the fins housed in the second fluid flow path between the tubes are integrally joined by vacuum brazing. , other fluid introduction headers, discharge headers, fluid introduction pipes, discharge pipes, etc. have been manufactured by joining, for example, by argon welding.

発明が解決しようとする課題 しかしながら、このような従来の熱交換器で
は、溶接箇所が非常に多く、従つてその製造が非
常に面倒で、手間がかかり、溶接に熟練を要する
とともに、製造コストが高くついた。また溶接箇
所が多いため、溶接不良による液漏れが生じ易
く、さらにヘツダ等の溶接時に発生するいわゆる
スパツター(アルミニウム片)が器内に入り込
み、これによつて熱交換器の性能が害されるとい
う問題があつた。
Problems to be Solved by the Invention However, in such conventional heat exchangers, there are a large number of welding points, and therefore manufacturing thereof is extremely troublesome and time-consuming, requires skill in welding, and manufacturing costs are high. It was expensive. In addition, since there are many welding points, liquid leakage is likely to occur due to poor welding, and there is also the problem that so-called spatter (aluminum pieces) generated when welding headers etc. enter the heat exchanger, impairing the performance of the heat exchanger. It was hot.

この発明の目的は、上記の従来技術の問題を解
決し、複数の流体が第1および第2流体流路内を
平面よりみて直交流となつて流されかつ各流路内
においてフインによつてその流れの方向を規制さ
れて、熱交換効率が非常にすぐれており、またヘ
ツダ部を第1および第2流体流路の左右両側に一
体に組み込むように形成することにより、溶接部
分が非常に少なく、従つてその製造を容易かつ安
価になし得るとともに、液漏れを生じることが非
常に少なく、また器内にスパツター等の異物が入
り込むようなことが全くないうえに、耐圧性にす
ぐれており、しかも第1流体流路の流通方向を自
在にかつ簡単に設定することができて、熱交換性
能の向上を図り得る、熱交換器を提供しようとす
るにある。
It is an object of the present invention to solve the above-mentioned problems of the prior art, and to allow a plurality of fluids to flow in a cross flow in first and second fluid channels when viewed from a plane, and to have fins in each channel. The direction of the flow is regulated, resulting in extremely high heat exchange efficiency, and by forming the header portions so as to be integrated into both the left and right sides of the first and second fluid flow paths, the welded portions are extremely Therefore, it can be manufactured easily and inexpensively, and there is very little chance of liquid leakage, and there is no chance of foreign matter such as spatter getting into the container, and it has excellent pressure resistance. Moreover, it is an object of the present invention to provide a heat exchanger in which the flow direction of the first fluid flow path can be freely and easily set, and the heat exchange performance can be improved.

課題を解決するための手段 この発明は、上記の目的を達成するために、平
板により隔てられた第1流体流路と第2流体流路
とを交互に備えた熱交換器において、第1流体流
路が、上下両側に配置されかつ両端部もしくは所
要の一端部に流体通過孔を有する平板と、両平板
同志の間に介在されかつ平板と略同形同大の外周
を有する第1流体流路形成用環状体とによつて形
成され、第1流体流路内に、平たいプレート部
と、これの上下両面に直交状に設けられた多数の
並列状凸部とよりなる押出形材製のインナー・フ
インが環状体の左右両端部分の内側を除いて収め
られ、第2流体流路が、上下両側に配置されかつ
両端部もしくは所要の一端部に流体通過孔を有す
る平板と、両平板同志の間において左右両側に配
置された一対のスペーサとによつて形成されて、
前後に開口し、この第2流体流路に正面よりみて
波形のコルゲート・フインが配置されており、左
右両スペーサの少なくとも1つに、上下両平板の
流体通過孔に連通する流体通過孔があけられ、平
板の左右両端部の流体通過孔と、第1流体流路形
成用環状体のインナー・フインの無い左右両端部
分と、スペーサの流体通過孔とによつて左右両側
のヘツダ部が形成されている熱交換器を要旨とし
ている。
Means for Solving the Problems In order to achieve the above object, the present invention provides a heat exchanger that alternately includes a first fluid flow path and a second fluid flow path separated by a flat plate. A flat plate in which a flow path is arranged on both the upper and lower sides and has a fluid passage hole at both ends or a required end; and a first fluid flow that is interposed between both the flat plates and has an outer periphery that is approximately the same shape and size as the flat plate. An extruded section formed by a channel-forming annular body and comprising a flat plate section and a large number of parallel convex sections provided perpendicularly on both upper and lower surfaces of the flat plate section within the first fluid flow path. The inner fin is housed in the annular body except for the inside of both left and right end portions, and the second fluid flow path is arranged on both the upper and lower sides and includes a flat plate having a fluid passage hole at both ends or a required end, formed by a pair of spacers arranged on both left and right sides between the
A corrugated fin is arranged in the second fluid flow path, which is open in the front and rear, and has a corrugated shape when viewed from the front, and at least one of the left and right spacers has a fluid passage hole that communicates with the fluid passage hole in the upper and lower flat plates. The left and right header portions are formed by the fluid passage holes at both left and right ends of the flat plate, the left and right end portions of the first fluid flow path forming annular body without inner fins, and the fluid passage holes of the spacer. The main focus is on heat exchangers that are

作 用 上記熱交換器によれば、第1流体流路内に、平
たいプレート部と、これの上下両面に直交状に設
けられた多数の並列状凸部とよりなる押出形材製
のインナー・フインが収められていて、平板の左
右両端部の流体通過孔と、第1流体流路形成用環
状体のインナー・フインの無い左右両端部分と、
スペーサの流体通過孔とによつて左右両側のヘツ
ダ部が形成されている。従つて、オイル等の第1
流体は、左右両側のうち一方のヘツダ部より導入
され、第1流体流路内を押出形材製のインナー・
フインの平たいプレート部および多数の並列状凸
部によつて第1流体の流通方向が規制されて、イ
ンナー・フインに接触しながら並行流となつて移
行し、他方のヘツダ部より流出され、これに対
し、第2流体流路は前後に開口していて、フアン
による強制送風によつてあるいは車両等の走行に
よる自然通風によつて空気よりなる第2流体が、
正面よりみて波形のコルゲート・フインによつて
その流通方向を規制されて、コルゲート・フイン
に接触しながら通過せしめられ、これにより、第
1流体と第2流体が平面よりみて直交流となつて
かつ平板と押出形材製インナー・フインとコルゲ
ート・フインとを介して相互に熱交換せられ、熱
交換効率がすぐれているものである。
Function: According to the above heat exchanger, an inner plate made of an extruded shape, which includes a flat plate portion and a large number of parallel convex portions provided perpendicularly on both upper and lower surfaces of the flat plate portion, is provided in the first fluid flow path. Fluid passage holes at both left and right ends of the flat plate in which the fins are housed, and left and right end portions of the first fluid flow path forming annular body without inner fins;
Header portions on both left and right sides are formed by the fluid passage holes of the spacer. Therefore, the first oil etc.
The fluid is introduced from one of the left and right headers, and flows through the first fluid flow path through an inner tube made of extruded material.
The flow direction of the first fluid is regulated by the flat plate portion of the fin and the numerous parallel convex portions, and the first fluid flows in parallel while contacting the inner fin, flows out from the other header portion, and flows out from the other header portion. On the other hand, the second fluid flow path is open in the front and rear, and the second fluid made of air is caused by forced air flow from a fan or natural ventilation from a running vehicle, etc.
When viewed from the front, the flow direction of the fluid is regulated by the corrugated fins, and the fluid is allowed to pass through while contacting the corrugated fins, so that the first fluid and the second fluid form a cross flow when viewed from the plane. Heat is exchanged between the flat plate, inner fins made of extruded material, and corrugated fins, and the heat exchange efficiency is excellent.

実施例 この発明の実施例を、以下図面に基づいて説明
する。
Embodiments Examples of the present invention will be described below based on the drawings.

なお、この明細書において、前後、左右および
上下は第6図を基準とし、前とは第6図図面紙葉
の表側、後とは同裏側をいい、また左とは同図左
側、右とは同右側をいい、上とは同図上側、下と
は同下側をいうものとする。
In this specification, front, back, left, right, and top and bottom are based on FIG. 6, and "front" refers to the front side of the paper sheet in FIG. 6, "back" refers to the back side, and "left" refers to the left side, right and refers to the right side of the figure, "top" refers to the upper side of the figure, and "bottom" refers to the lower side of the figure.

この発明の第1実施例を示す第1図〜第7図に
おいて、この発明による熱交換器1はアルミニウ
ム製であつて、例えば大型オイルクーラとして使
用せられる。この熱交換器1は、アルミニウム・
ブレージング・シートよりなる平板3により隔て
られた第1流体流路Aと第2流体流路Bとを上下
方向に交互に有している。第1流体流路Aにはオ
イルが流通し、また第2流体流路Bには空気が流
通する。両流路A,Bはこれらの流体が直交状に
流れるように配置されている。熱交換器1の左右
両側には、ヘツダ部2,2が一体に組み込まるよ
うに形成されている。
1 to 7 showing a first embodiment of the present invention, a heat exchanger 1 according to the present invention is made of aluminum and is used, for example, as a large oil cooler. This heat exchanger 1 is made of aluminum.
It has a first fluid flow path A and a second fluid flow path B separated by a flat plate 3 made of a brazing sheet, which alternate in the vertical direction. Oil flows through the first fluid flow path A, and air flows through the second fluid flow path B. Both channels A and B are arranged so that these fluids flow orthogonally. Header portions 2, 2 are formed on both left and right sides of the heat exchanger 1 so as to be integrally incorporated therein.

すなわち、第3図と第5図に示すように、熱交
換器1の第1流体流路Aは、上下両側に配置され
かつ左右両端部に流体通過孔4,4を有する平板
3,3と、両平板3,3同志の間に介在されかつ
平板3,3と略同形同大の外周を有する第1流体
流路形成用環状体5と、環状体5の内側に左右両
端部を除いて配置されたアルミニウム押出形材製
のインナー・フイン6とによつて形成されてい
る。
That is, as shown in FIGS. 3 and 5, the first fluid flow path A of the heat exchanger 1 includes flat plates 3, 3 arranged on both the upper and lower sides and having fluid passage holes 4, 4 at both left and right ends. , a first fluid flow path forming annular body 5 interposed between both flat plates 3, 3 and having an outer periphery of approximately the same shape and size as the flat plates 3, 3; The inner fins 6 are made of extruded aluminum and are arranged as follows.

第2流体流路Bは、上下両側に配置されかつ左
右両端部に流体通過孔4,4を有する平板3,3
と、両平板3,3同志の間において左右両側に配
置された一対のスペーサ7,7と、両スペーサ
7,7同志の中間に配置されたコルゲート・フイ
ン8とによつて形成されて、前後に開口してい
る。また、左右両スペーサ7,7に、上下両平板
3,3の流体通過孔4,4に連通する流体通過孔
9,9があけられている。
The second fluid flow path B includes flat plates 3, 3 which are arranged on both the upper and lower sides and have fluid passage holes 4, 4 at both left and right ends.
It is formed by a pair of spacers 7, 7 arranged on both left and right sides between both flat plates 3, 3, and a corrugated fin 8 arranged between both spacers 7, 7. It is open to Further, fluid passage holes 9, 9 are formed in both the left and right spacers 7, 7, which communicate with the fluid passage holes 4, 4 of both the upper and lower flat plates 3, 3.

従つて左右両側のヘツダ部2,2は、平板3の
左右両端部の流体通過孔4,4と、第1流体流路
形成用環状体5のインナー・フイン6の無い左右
両端部分と、スペーサ7,7の流体通過孔9,9
とによつて形成されている。
Therefore, the left and right header portions 2, 2 are connected to the fluid passage holes 4, 4 at both the left and right ends of the flat plate 3, the left and right end portions of the first fluid flow path forming annular body 5 without the inner fin 6, and the spacer. 7, 7 fluid passage holes 9, 9
It is formed by.

ここで、第1流体流路A内に収められたインナ
ー・フイン6は、アルミニウム押出形材製であつ
て、平たいプレート部6aと、これの上下両面に
直交状に設けられた多数の並列状凸部6bとによ
つて構成されている。また第2流体流路B内には
上下一対の正面よりみて波形のいわゆるマルチエ
ントリー・コルゲート・フイン8,8が配置さ
れ、これらのフイン8,8は両者の間に介在され
たアルミニウム・ブレージング・シートよりなる
中間プレート10により接合される。
Here, the inner fin 6 housed in the first fluid flow path A is made of extruded aluminum, and includes a flat plate portion 6a and a large number of parallel fins provided perpendicularly on both upper and lower surfaces of the flat plate portion 6a. It is constituted by a convex portion 6b. Also, in the second fluid flow path B, a pair of upper and lower corrugated corrugated fins 8, 8 are disposed, and these fins 8, 8 have an aluminum brazing structure interposed between them. They are joined by an intermediate plate 10 made of a sheet.

熱交換器1の第1および第2流体流路A,B
は、熱交換器1の上下両端部分を除き、上記のよ
うな構成を有している。この実施例では、熱交換
器1の上面左右両端部に流体導入管11と流体排
出管12が接続され、同下面は塞がれているた
め、上下両端部分はつぎのような構成を有してい
る。
First and second fluid flow paths A, B of heat exchanger 1
has the above-mentioned configuration except for the upper and lower end portions of the heat exchanger 1. In this embodiment, the fluid introduction pipe 11 and the fluid discharge pipe 12 are connected to both left and right ends of the upper surface of the heat exchanger 1, and the lower surface thereof is closed, so that the upper and lower ends have the following configuration. There is.

まず上端部分には、第2図に示すように、左右
両端に流体通過孔14,14を有する比較的厚肉
のアルミニウム板よりなる表面板13と、これよ
り下側に配置されかつ両端に流体通過孔4,4を
有するアルミニウム・ブレージング・シートより
なる平板3,3と、それぞれ流体通過孔9,9を
有する左右一対のスペーサ7,7と、両スペーサ
7,7の中間に配せられた1枚のコルゲート・フ
イン8とによつて第2流体流路Bが形成されてい
る。
First, as shown in FIG. 2, at the upper end part, there is a surface plate 13 made of a relatively thick aluminum plate having fluid passage holes 14, 14 at both left and right ends, and a surface plate 13 made of a relatively thick aluminum plate that has fluid passage holes 14, 14 at both left and right ends. Flat plates 3, 3 made of aluminum brazing sheets having passage holes 4, 4, a pair of left and right spacers 7, 7 each having fluid passage holes 9, 9, and placed between the two spacers 7, 7. A second fluid flow path B is formed by one corrugated fin 8.

つぎに、熱交換器1の下端部分には、第4図に
示すように、流体通過孔の全くない比較的厚肉の
表面板13と、これの上側に配置されかつ両端に
流体通過孔を有していないアルミニウム・ブレー
ジング・シートよりなる平板3,3と、同じく流
体通過孔を有していない左右一対のスペーサ7,
7と、両スペーサ7,7の中間に配せられた1枚
のコルゲート・フイン8とによつて第2流体流路
Bが形成されているものである。熱交換器1の前
後両面には、すべての第2流体流路Bの外周を囲
むように一対の短いダクト15,15が取り付け
られている。
Next, as shown in FIG. 4, the lower end portion of the heat exchanger 1 includes a relatively thick surface plate 13 having no fluid passage holes, and a relatively thick surface plate 13 arranged above this and having fluid passage holes at both ends. A pair of left and right spacers 7, which also do not have fluid passage holes, are made of aluminum brazing sheets.
7 and one corrugated fin 8 disposed between both spacers 7, 7, a second fluid flow path B is formed. A pair of short ducts 15, 15 are attached to both the front and rear surfaces of the heat exchanger 1 so as to surround the outer periphery of all the second fluid flow paths B.

上記熱交換器1は、アルミニウム・ブレージン
グ・シートよりなる平板3,3と、第1流体流路
形成用環状体5と、インナー・フイン6と、スペ
ーサ7,7と、コルゲート・フイン8,8および
中間プレート10と、上下両表面板13,13と
を重合状態に配置し、例えば真空ろう付け法によ
り一体に接合することにより製造し得るものであ
る。なお、この実施例では、平板3としてアルミ
ニウム・ブレージング・シートが使用されている
が、これに限らず、平板3としてアルミニウム板
を使用するとともに、この平板3、第1流体流路
形成用環状体5およびスペーサ7等の熱交換器構
成部材の所要の上面と下面にそれぞれろう材層を
ハケ塗り等の塗布によつて形成し、このろう材層
により熱交換器1全体を接合することも可能であ
る。
The heat exchanger 1 includes flat plates 3, 3 made of aluminum brazing sheets, an annular body 5 for forming a first fluid flow path, inner fins 6, spacers 7, 7, and corrugated fins 8, 8. It can be manufactured by arranging the intermediate plate 10 and both the upper and lower surface plates 13 in a superposed state and joining them together by, for example, vacuum brazing. In this embodiment, an aluminum brazing sheet is used as the flat plate 3, but the invention is not limited to this. An aluminum plate can be used as the flat plate 3, and this flat plate 3 and the annular body for forming the first fluid flow path It is also possible to form a brazing material layer on the required upper and lower surfaces of heat exchanger component members such as 5 and spacer 7 by brush coating or the like, and to join the entire heat exchanger 1 with this brazing material layer. It is.

上記熱交換器1においては、例えば左側の流体
導入管11よりオイルが導入される。オイルは左
側ヘツダ部2よりすべての第1流体流路A内を、
押出形材製のインナー・フイン6の平たいプレー
ト部6aおよび多数の並列状凸部6bによつてオ
イルの流通方向が規制されて、インナー・フイン
6に接触しながら並行流となつて移行し、他方の
右側ヘツダ部2より流出して、同ヘツダ部2より
流体排出管12へと排出される。これに対し、第
2流体流路Bは、前後に開口していて、フアンに
よる強制送風によつてあるいは車両等の走行によ
る自然通風によつて空気が、正面よりみて波形の
コルゲート・フイン8によつてその流通方向を規
制されて、コルゲート・フイン8に接触しながら
通過せしめられ、これにより、オイルと空気とが
平面よりみて直交流となつてかつ平板3と押出形
材製インナー・フイン6とコルゲート・フイン8
とを介して相互に熱交換せしめられる。
In the heat exchanger 1, oil is introduced, for example, from the left fluid introduction pipe 11. The oil flows through all the first fluid flow paths A from the left header section 2.
The direction of oil flow is regulated by the flat plate portion 6a and the numerous parallel convex portions 6b of the inner fin 6 made of extruded material, and the oil flows in parallel while contacting the inner fin 6. It flows out from the other right header section 2 and is discharged from the same header section 2 to the fluid discharge pipe 12. On the other hand, the second fluid flow path B is open in the front and rear, and air is forced into corrugated fins 8 that are corrugated when viewed from the front by forced airflow from a fan or by natural ventilation from running vehicles. Therefore, the flow direction of the oil is regulated, and the oil and air are allowed to pass while contacting the corrugated fins 8, so that the oil and air flow in a cross flow when viewed from the plane, and between the flat plate 3 and the extruded inner fins 6. and Colgate Huynh 8
Heat is exchanged between the two.

このような熱交換器1は、オイル・クーラとし
て例えばエンジンオイルの冷却に、あるいは産業
機械の冷却に、また各種油圧システムのオイルの
冷却に使用せられるものである。
Such a heat exchanger 1 is used as an oil cooler, for example, to cool engine oil, industrial machinery, or oil in various hydraulic systems.

第8図は、この発明の第2実施例を示すもので
ある。ここで、上記第1実施例の場合と異なる点
は、第1流体流路Aが2個単位で流れの方向が変
つて、流体が蛇行状に移行するようになされてい
る。従つて流れの方向が変わる部分では、平板3
の端部は塞がつていて流体通過孔があけられてお
らず、またスペーサも同様に流体通過孔の無いも
のが用いられている。
FIG. 8 shows a second embodiment of the invention. Here, the difference from the first embodiment is that the direction of flow changes in units of two first fluid channels A, so that the fluid moves in a meandering manner. Therefore, in the part where the flow direction changes, the flat plate 3
The end of the spacer is closed and has no fluid passage hole, and the spacer also has no fluid passage hole.

この第2実施例のその他の点は上記第1実施例
の場合と同様であり、図面において同一のものに
は同一の符号を付した。
The other points of this second embodiment are the same as those of the first embodiment, and the same parts are given the same reference numerals in the drawings.

なお、上記各実施例においては、第1流体流路
Aが水平に配置されたいわゆる横型のオイルクー
ラが示されているが、この発明は第1流体流路A
が垂直に配置された縦型のオイルクーラにも同様
に適用されるものである。またこの発明による熱
交換器は、オイルクーラだけでなく、気体および
流体について複数種類の熱交換を行なう各種の熱
交換器にも適用可能である。
Note that in each of the above embodiments, a so-called horizontal oil cooler in which the first fluid flow path A is arranged horizontally is shown, but the present invention is applicable to the first fluid flow path A.
The same applies to vertical oil coolers in which the oil cooler is vertically arranged. Furthermore, the heat exchanger according to the present invention is applicable not only to oil coolers but also to various heat exchangers that perform multiple types of heat exchange with gas and fluid.

発明の効果 この発明は、上述のように、平板により隔てら
れた第1流体流路と第2流体流路とを交互に備え
た熱交換器において、第1流体流路が、上下両側
に配置されかつ両端部もしくは所要の一端部に流
体通過孔を有する平板と、両平板同志の間に介在
されかつ平板と略同形同大の外周を有する第1流
体流路形成用環状体とによつて形成され、第1流
体流路内に、平たいプレート部と、これの上下両
面に直交状に設けられた多数の並列状凸部とより
なる押出形材製のインナー・フインが環状体の左
右両端部分の内側を除いて収められ、第2流体流
路が、上下両側に配置されかつ両端部もしくは所
要の一端部に流体通過孔を有する平板と、両平板
同志の間において左右両側に配置された一対のス
ペーサとによつて形成されて、前後に開口し、こ
の第2流体流路に正面よりみて波形のコルゲー
ト・フインが配置されており、左右両スペーサの
少なくとも1つに、上下両平板の流体通過孔に連
通する流体通過孔があけられ、平板の左右両端部
の流体通過孔と、第1流体流路形成用環状体のイ
ンナー・フインの無い左右両端部分と、スペーサ
の流体通過孔とによつて左右両側のヘツダ部が形
成されているもので、この発明の熱交換器によれ
ば、オイル等の第1流体は、左右両側のうち一方
のヘツダ部より導入されて、第1流体流路内を押
出形材製のインナー・フインの平たいプレート部
および多数の並列状凸部によつて第1流体の流通
方向が規制されて、インナー・フインに接触しな
がら並行流となつて移行し、他方のヘツダ部より
流出される。これに対し、第2流体流路は前後に
開口していて、内部に正面よりみて波形のコルゲ
ート・フインが配置されており、フアンによる強
制送風によつてあるいは車両等の走行による自然
通風によつて空気よりなる第2流体が、正面より
みて波形のコルゲート・フインによつてその流通
方向を規制されて、コルゲート・フインに接触し
ながら通過せしめられるものである。
Effects of the Invention As described above, the present invention provides a heat exchanger that alternately includes a first fluid flow path and a second fluid flow path separated by a flat plate, in which the first fluid flow path is arranged on both the upper and lower sides. a flat plate having a fluid passage hole at both ends or one required end; and a first fluid flow path forming annular body interposed between the flat plates and having an outer circumference of approximately the same shape and size as the flat plate. Inner fins made of extruded material, each consisting of a flat plate part and a large number of parallel convex parts provided orthogonally on both the upper and lower surfaces of the flat plate part, are formed in the first fluid flow path on the left and right sides of the annular body. A second fluid passage is arranged on both the upper and lower sides and has a fluid passage hole at both ends or a required end, and a second fluid flow path is arranged on both the left and right sides between the flat plates. When viewed from the front, corrugated fins are arranged in this second fluid flow path, and at least one of the left and right spacers has upper and lower flat plates. Fluid passage holes are opened that communicate with the fluid passage holes of the flat plate, the fluid passage holes at both left and right ends of the flat plate, the left and right ends of the first fluid passage forming annular body without inner fins, and the fluid passage holes of the spacer. According to the heat exchanger of the present invention, a first fluid such as oil is introduced from one of the left and right header parts, and the first fluid is introduced from one of the left and right header parts. The flow direction of the first fluid is regulated in the fluid flow path by the flat plate portion of the inner fin made of an extruded shape material and a large number of parallel convex portions, and the first fluid flows in parallel while contacting the inner fin. It migrates and flows out from the other header. On the other hand, the second fluid flow path is open in the front and rear, and corrugated fins are arranged inside when viewed from the front, and are operated by forced air from a fan or by natural ventilation from running vehicles, etc. The second fluid made of air is regulated in its flow direction by the corrugated fins when viewed from the front, and is allowed to pass through while contacting the corrugated fins.

従つて、この発明の熱交換器によれば、第1流
体と第2流体が平面よりみて直交流となつてかつ
平板と押出形材製インナー・フインとコルゲー
ト・フインとを介して相互に熱交換せられ、熱交
換効率がすぐれているという効果を奏する。
Therefore, according to the heat exchanger of the present invention, the first fluid and the second fluid flow in cross flow when viewed from the plane, and they mutually transfer heat through the flat plate, the inner fin made of extruded material, and the corrugated fin. The effect is that the heat exchange efficiency is excellent.

また、この発明の熱交換器は、ヘツダ部が第1
および第2流体流路の左右両側に組み込まれるよ
うに一体に設けられているから、溶接部分が非常
に少なく、かつ生産工程数が少なくてすみ、従つ
てその製造を容易かつ安価になし得るとともに、
液漏れを生じることが非常に少ない。また器内に
スパツター等の異物が入り込むようなことが全く
ないうえに、積層タイプであるため耐圧性にすぐ
れている。しかも所要の一端部の流体通過孔が塞
がれた平板と、流体通過孔のないスペーサとを適
宜配置することにより、第1流体流路の流通方向
を自在にかつ簡単に設定することができて、熱交
換性能の向上を図り得るという利点がある。
Further, in the heat exchanger of the present invention, the header portion is the first
Since it is integrally provided so as to be incorporated on both the left and right sides of the second fluid flow path, there are very few welded parts and the number of production steps is reduced, and therefore, it can be manufactured easily and inexpensively. ,
There is very little chance of liquid leakage. In addition, there is no possibility of foreign matter such as spatter getting into the container, and since it is a laminated type, it has excellent pressure resistance. Furthermore, by appropriately arranging a flat plate with a fluid passage hole at one end that is closed and a spacer without a fluid passage hole, the flow direction of the first fluid flow path can be freely and easily set. This has the advantage of improving heat exchange performance.

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

図面はこの発明の2つの実施例を示すもので、
第1図は第1実施例の熱交換器の部分省略斜視
図、第2図は第1図の熱交換器の上端部分の流路
構成を示す分解斜視図、第3図は中間部分の流路
構成を示す分解斜視図、第4図は同下端部分の流
路構成を示す分解斜視図、第5図は第1図の要部
拡大斜視図、第6図は流体導入・排出管およびダ
クトを取り付けた熱交換器の正面図、第7図は同
左側面図である。第8図は第2実施例の熱交換器
の断面図である。 1……熱交換器、2……ヘツダ部、A……第1
流体流路、B……第2流体流路、3……平板、
4,9,14……流体通過孔、5……第1流体流
路形成用環状体、6……インナー・フイン、6a
……平たいプレート部、6b……並列状凸部、7
……スペーサ、8……コルゲート・フイン、13
……表面板。
The drawings show two embodiments of the invention,
Fig. 1 is a partially omitted perspective view of the heat exchanger of the first embodiment, Fig. 2 is an exploded perspective view showing the flow path configuration of the upper end portion of the heat exchanger of Fig. FIG. 4 is an exploded perspective view showing the flow path configuration at the lower end of the same, FIG. 5 is an enlarged perspective view of the main part of FIG. 1, and FIG. 6 is a fluid introduction/discharge pipe and duct. FIG. 7 is a front view of the heat exchanger with the heat exchanger attached, and FIG. 7 is a left side view of the same. FIG. 8 is a sectional view of the heat exchanger of the second embodiment. 1...Heat exchanger, 2...Header part, A...1st
Fluid channel, B...second fluid channel, 3...flat plate,
4, 9, 14...Fluid passage hole, 5...Annular body for forming a first fluid flow path, 6...Inner fin, 6a
...Flat plate part, 6b... Parallel convex part, 7
...Spacer, 8...Corrugate fin, 13
...Surface board.

Claims (1)

【特許請求の範囲】[Claims] 1 平板3により隔てられた第1流体流路Aと第
2流体流路Bとを交互に備えた熱交換器におい
て、第1流体流路Aが、上下両側に配置されかつ
両端部もしくは所要の一端部に流体通過孔4を有
する平板3,3と、両平板3,3同志の間に介在
されかつ平板3,3と略同形同大の外周を有する
第1流体流路形成用環状体5とによつて形成さ
れ、第1流体流路A内に、平たいプレート部6a
と、これらの上下両面に直交状に設けられた多数
の並列状凸部6bとよりなる押出形材製のインナ
ー・フイン6が環状体5の左右両端部分の内側を
除いて収められ、第2流体流路Bが、上下両側に
配置されかつ両端部もしくは所要の一端部に流体
通過孔4を有する平板3,3と、両平板3,3同
志の間において左右両側に配置された一対のスペ
ーサ7,7とによつて形成されて、前後に開口
し、この第2流体流路Bに正面よりみて波形のコ
ルゲート・フイン8が配置されており、左右両ス
ペーサ7,7の少なくとも1つに、上下両平板
3,3の流体通過孔4,4に連通する流体通過孔
9があけられ、平板3の左右両端部の流体通過孔
4,4と、第1流体流路形成用環状体5のインナ
ー・フイン6の無い左右両端部分と、スペーサ
7,7の流体通過孔9,9とによつて左右両側の
ヘツダ部2,2が形成されている熱交換器。
1 In a heat exchanger that alternately includes a first fluid passage A and a second fluid passage B separated by a flat plate 3, the first fluid passage A is arranged on both the upper and lower sides, and the first fluid passage A is arranged at both ends or at the required portion. Flat plates 3, 3 having a fluid passage hole 4 at one end, and a first fluid flow path forming annular body interposed between both flat plates 3, 3 and having an outer periphery of approximately the same shape and size as the flat plates 3, 3. 5 and a flat plate portion 6a in the first fluid flow path A.
and a large number of parallel convex portions 6b provided perpendicularly on both the upper and lower surfaces of the annular body 5. An inner fin 6 made of an extruded material is housed in the annular body 5 except for the inside of both left and right end portions. Flat plates 3, 3 in which fluid flow paths B are arranged on both upper and lower sides and have fluid passage holes 4 at both ends or a required end, and a pair of spacers arranged on both left and right sides between both flat plates 3, 3. A corrugated fin 8 is disposed in this second fluid flow path B and has a corrugated shape when viewed from the front. , a fluid passage hole 9 communicating with the fluid passage holes 4, 4 of both the upper and lower flat plates 3, 3 is opened, and the fluid passage holes 4, 4 at both left and right ends of the flat plate 3, and the first annular body 5 for forming a fluid flow path. A heat exchanger in which left and right header portions 2, 2 are formed by left and right end portions without inner fins 6 and fluid passage holes 9, 9 of spacers 7, 7.
JP13578285A 1985-06-20 1985-06-20 Heat exchanger Granted JPS61295492A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13578285A JPS61295492A (en) 1985-06-20 1985-06-20 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13578285A JPS61295492A (en) 1985-06-20 1985-06-20 Heat exchanger

Publications (2)

Publication Number Publication Date
JPS61295492A JPS61295492A (en) 1986-12-26
JPH0583838B2 true JPH0583838B2 (en) 1993-11-29

Family

ID=15159723

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13578285A Granted JPS61295492A (en) 1985-06-20 1985-06-20 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS61295492A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5111671A (en) * 1991-02-07 1992-05-12 General Motors Corporation Evaporator with expanding and contracting passes for improving uniformity of air temperature distribution
FR2788116B1 (en) * 1998-12-30 2001-05-18 Valeo Climatisation HEATING, VENTILATION AND / OR AIR CONDITIONING DEVICE COMPRISING A THERMAL LOOP EQUIPPED WITH AN EVAPORATOR
FR2788117B1 (en) * 1998-12-30 2001-03-02 Valeo Climatisation HEATING, VENTILATION AND / OR AIR CONDITIONING DEVICE COMPRISING A THERMAL LOOP EQUIPPED WITH AN EVAPORATOR
FR2788118B1 (en) * 1998-12-30 2003-04-18 Valeo Climatisation HEATING, VENTILATION AND / OR AIR CONDITIONING DEVICE COMPRISING A THERMAL BURNER EQUIPPED WITH AN EVAPORATOR
US11486648B2 (en) 2017-01-30 2022-11-01 Kyocera Corporation Heat exchanger

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58165474U (en) * 1982-04-27 1983-11-04 東洋ラジエーター株式会社 Multi-plate heat exchanger

Also Published As

Publication number Publication date
JPS61295492A (en) 1986-12-26

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