JPH0670557B2 - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPH0670557B2 JPH0670557B2 JP2314939A JP31493990A JPH0670557B2 JP H0670557 B2 JPH0670557 B2 JP H0670557B2 JP 2314939 A JP2314939 A JP 2314939A JP 31493990 A JP31493990 A JP 31493990A JP H0670557 B2 JPH0670557 B2 JP H0670557B2
- Authority
- JP
- Japan
- Prior art keywords
- flow path
- hollow
- portions
- fluid
- cross
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- 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、例えばインタークーラ(給気用中間冷却
器)等に使用される熱交換器に関するものである。Description: TECHNICAL FIELD The present invention relates to a heat exchanger used in, for example, an intercooler (intercooler for air supply).
従来の技術 この種の熱交換器として、本出願人は、先に、熱交換第
1流体が流される少なくとも1つの第1流路と、第1流
体と熱交換されるべき熱交換第2流体が流される少なく
とも1つの第2流路とを備えている熱交換器を提案した
(実開昭63-197986号公報参照)。2. Description of the Related Art As a heat exchanger of this type, the present applicant has previously proposed that at least one first flow path through which a heat exchange first fluid flows and a heat exchange second fluid to be heat-exchanged with the first fluid. A heat exchanger provided with at least one second flow path through which water is flowed has been proposed (see Japanese Utility Model Laid-Open No. 63-197986).
この先提案の熱交換器において、第1流路は、相互に所
定間隔をあけて対向する平板と、これらの平板同志の間
に介在された第1流体流路形成体とによって形成され、
第2流路は、相互に所定間隔をあけて対向する平板と、
これらの平板同志の間に介在されかつ平板の左右もしく
は前後側縁部に対応するように配置された一対の間隔保
持用側壁部および両側壁部同志の中間に位置せしめられ
たフィン部材とによって形成されていた。In the previously proposed heat exchanger, the first flow path is formed by flat plates facing each other at a predetermined interval and a first fluid flow path forming body interposed between the flat plates.
The second flow path is a flat plate facing each other with a predetermined gap,
Formed by a pair of side-walls for spacing and a fin member located in the middle of both side walls arranged between the flat plates and corresponding to the left and right or front and rear side edges of the flat plates. It had been.
そして、従来は、第1流体流路形成体が、平板の左右両
側縁部に対応するように配置された一対の間隔保持用側
壁部と、これら両側壁部同志を連結するとともに内部に
側壁部と平行な多数の中空部を有しかつ上下両面のうち
少なくとも片面が断面波形とされた中空連結壁部とより
なるアルミニウム押出型材によってつくられ、中空連結
壁部の波頭部の頂面が平板に接合されていた。Then, conventionally, the first fluid flow path forming member connects the pair of space holding side wall portions arranged so as to correspond to the left and right side edge portions of the flat plate and the both side wall portions to each other, and the side wall portion is provided inside. Made of an extruded aluminum material having a hollow connecting wall part having a plurality of hollow parts parallel to each other and at least one of the upper and lower surfaces having a corrugated cross section, and the top surface of the wave head of the hollow connecting wall part is a flat plate. Was joined to.
発明が解決しようとする課題 しかしながら、この先提案の熱交換器では、アルミニウ
ム中空押出型材によってつくられた第1流体流路形成体
内側の横断面略菱形の中空部の断面積に比べて、同流路
形成体の上下両外側の波形凹状部、およびこの凹状部に
対向する平板部分によって囲まれた横断面略三角形の中
空部の断面積の方がかなり小さく、このため、両中空部
内を流れる流体の流量および流速等がかなり異なって、
流れが不均一となり、かつ圧力損失が大きく、とくにイ
ンタークーラに適用した場合、流路内を高温高圧の空気
が高速で流れるため、圧力損失が大きく、熱交換性能が
劣るという問題があった。DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention However, in the previously proposed heat exchanger, compared with the cross-sectional area of the hollow portion having the substantially rhombic cross section inside the first fluid flow path forming body made of the aluminum hollow extrusion mold material, The cross-sectional area of the corrugated concave portions on the upper and lower outer sides of the path forming body and the hollow portion having a substantially triangular cross section surrounded by the flat plate portions facing the concave portions is considerably smaller, and therefore the fluid flowing in both hollow portions is smaller. The flow rate and flow velocity of
When the flow is non-uniform and the pressure loss is large, especially when applied to an intercooler, high-temperature and high-pressure air flows at a high speed in the flow path, resulting in a large pressure loss and poor heat exchange performance.
この発明の目的は、上記の問題を解決し、上下両平板
と、これらの間に介在された第1流体流路形成体とによ
って形成される第1流路内のすべての中空部の断面積が
略等しく、従って、中空部内を流れる流体の流量および
流速等が等しくなって、流体の流れが均一となるととも
に、圧力損失が非常に少なく、例えばインタークーラに
適用した場合に、流路内を高温高圧の空気が高速で流れ
ても、圧力損失が非常に少なく、熱交換性能が向上す
る、熱交換器を提供しようとするにある。An object of the present invention is to solve the above problems and to provide a cross-sectional area of all hollow parts in a first flow path formed by upper and lower flat plates and a first fluid flow path forming body interposed therebetween. Are almost equal, and therefore the flow rate and flow velocity of the fluid flowing in the hollow portion are equal, the fluid flow is uniform, and the pressure loss is very small. For example, when applied to an intercooler, It is an object of the present invention to provide a heat exchanger in which the pressure loss is very small and the heat exchange performance is improved even when high temperature and high pressure air flows at high speed.
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、熱交換第1
流体が流される少なくとも1つの第1流路と、第1流体
と熱交換されるべき熱交換第2流体が流される少なくと
も1つの第2流路とを備えており、第1流路が相互に所
定間隔をあけて対向する平板と、これらの平板同志の間
に介在された第1流体流路形成体とによって形成され、
第2流路が、相互に所定間隔をあけて対向する平板と、
これらの平板同志の間に介在されかつ平板の左右もしく
は前後側縁部に対応するように配置された一対の間隔保
持用側壁部および両側壁部同志の中間に位置せしめられ
たフィン部材とによって形成されている熱交換器におい
て、上記第1流体流路形成体が、平板の左右両側縁部に
対応するように配置された一対の間隔保持用側壁部と、
これら両側壁部同志を連結するとともに内部に側壁部と
平行な多数の中空部を有しかつ上下両外面がそれぞれ断
面波形となされていてその波頭部に上方もしくは下方に
のびている所要高さの凸部を備えた中空連結壁部とより
なるアルミニウム押出型材によってつくられ、中空連結
壁部内側の中空部の断面積と、中空連結壁部の上下両外
面の波形凹状部、これの両側の凸部、および凹状部に対
向する平板部分によって囲まれた中空部の断面積とが略
等しいものとなされている、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 exchange first
At least one first flow path through which a fluid flows and at least one second flow path through which a heat exchange second fluid that is to be heat-exchanged with the first fluid flow are provided, and the first flow paths are mutually Formed by flat plates facing each other at a predetermined interval and a first fluid flow path forming body interposed between the flat plates,
A second flow path and a flat plate facing each other at a predetermined interval;
Formed by a pair of side-walls for spacing and a fin member located in the middle of both side walls arranged between the flat plates and corresponding to the left and right or front and rear side edges of the flat plates. In the heat exchanger described above, the first fluid flow path forming member includes a pair of side wall portions for holding a gap, which are arranged so as to correspond to the left and right side edges of the flat plate,
These side wall parts are connected to each other, and a large number of hollow parts parallel to the side wall parts are provided inside, and the upper and lower outer surfaces are each corrugated in cross section, and the corrugated head extends upward or downward at a required height. Made of extruded aluminum material consisting of a hollow connecting wall with convex portions, the cross-sectional area of the hollow inside the hollow connecting wall, the corrugated concaves on the upper and lower outer surfaces of the hollow connecting wall, and the protrusions on both sides of this. The gist of the heat exchanger is that the cross section area of the hollow portion surrounded by the flat portion facing the concave portion and the concave portion is substantially equal.
作用 上記熱交換器によれば、第1流体流路形成体を構成する
アルミニウム中空押出型材が本来的に備えている中空連
結壁部内側の中空部の断面積と、中空連結壁部の上下両
外側の波形凹状部、これの両側の凸部、および凹状部に
対向する平板部分によって囲まれた中空部の断面積とが
略等しいものとなされているから、第1流路内のすべて
の中空部の断面積が略等しいものとなる。このため、中
空部内を流れる流体の流量および流速等が等しくなり、
流体の流れが均一となる。Action According to the heat exchanger, the cross-sectional area of the hollow portion inside the hollow connecting wall portion originally provided in the aluminum hollow extrusion molding material forming the first fluid flow path forming member, and the upper and lower portions of the hollow connecting wall portion Since the cross-sectional area of the outer corrugated concave portion, the convex portions on both sides of the corrugated concave portion, and the hollow portion surrounded by the flat plate portions facing the concave portion are substantially equal to each other, all the hollows in the first flow path. The cross-sectional areas of the parts are substantially equal. Therefore, the flow rate and the flow velocity of the fluid flowing in the hollow part become equal,
The flow of fluid becomes uniform.
また第1流路内のすべての中空部の断面積が略等しいた
め、圧力損失が非常に少なく、例えば熱交換器をインタ
ークーラに適用した場合に、流路内を高温高圧の空気が
高速で流れても、圧力損失が非常に少なく、熱交換性能
が向上するものである。In addition, since the cross-sectional areas of all hollow parts in the first flow path are substantially equal, the pressure loss is very small. For example, when a heat exchanger is applied to an intercooler, high-temperature and high-pressure air flows in the flow path at high speed. Even if it flows, the pressure loss is very small and the heat exchange performance is improved.
なお、第1流体流路形成体の中空連結壁部の断面波形上
下両外面において、波頭部に設ける凸部の形状を、例え
ば横断面鳩尾状、すなわち波頭部の幅よりも凸部の平坦
な頂面の幅の方が広い形状として、この凸部の幅広の頂
面を平板に接合するものとすると、接合面積が非常に広
くなり、熱交換器の耐圧強度が大幅にアップするので、
好ましい。In addition, the shape of the convex portion provided on the corrugated head on both the outer surfaces of the corrugated section of the hollow connection wall portion of the first fluid flow path forming member is, for example, a dovetail cross section, that is, If the flat top surface has a wider width and the wide top surface of this convex portion is joined to a flat plate, the joint area will be very large and the pressure resistance of the heat exchanger will be greatly increased. ,
preferable.
そしてこの場合、従来の熱交換器の耐圧強度と同じもの
を得るには、アルミニウム製の平板、並びにアルミニウ
ム中空押出型材製の第1流体流路形成体の肉厚を、それ
ぞれ減らすことができて、熱交換器の重量の低減を図り
得るという利点がある。In this case, in order to obtain the same compressive strength as that of the conventional heat exchanger, it is possible to reduce the wall thickness of the flat plate made of aluminum and the thickness of the first fluid flow path forming body made of the aluminum hollow extrusion mold material. The advantage is that the weight of the heat exchanger can be reduced.
実施例 つぎに、この発明の実施例を図面に基づいて説明する。Embodiment Next, an embodiment of the present invention will be described based on the drawings.
なお実施例は、この発明の熱交換器を空冷式インターク
ーラ(給気用中間冷却器)に適用した場合を示すもので
ある。The embodiment shows a case where the heat exchanger according to the present invention is applied to an air-cooling type intercooler (air supply intercooler).
この明細書において、前後および左右は第2図を基準と
し、前とは第2図図面紙葉の表側、後とは同裏側をい
ゝ、また左とは同図左側、右とは同右側をいうものとす
る。In this specification, the front and rear and the left and right are based on FIG. 2, the front means the front side of the drawing sheet in FIG. 2, the rear means the back side, the left means the left side of the figure, and the right side is the right side. Shall be said.
図面において、この発明によるインタークーラ(1)
は、熱交換第1流体として給気が流される多数の第1流
路(A)と、第1流体と熱交換されるべき熱交換第2流
体として冷却用空気が流される多数の第2流路(B)と
を交互に備えている。In the drawings, an intercooler according to the present invention (1)
Is a large number of first flow paths (A) through which supply air flows as a heat exchange first fluid, and a large number of second flows through which cooling air is flown as a heat exchange second fluid that should be heat exchanged with the first fluid. The roads (B) are alternately provided.
給気が流される多数の第1流路(A)は、前後両側の給
気導入用タンク(12)と同排出用タンク(13)に連通せ
しめられ、両タンク(12)と(13)のそれぞれ上部に給
気導入パイプ(14)と同排出パイプ(15)が接続されて
いる。The large number of first flow paths (A) through which the supply air flows is made to communicate with the supply air introduction tank (12) and the discharge air tank (13) on both the front and rear sides of the both tanks (12) and (13). A supply air introduction pipe (14) and a discharge pipe (15) are connected to the upper part of each.
ここで、第1流路(A)は、相互に所定間隔をあけて対
向するアルミニウムブレージングシートよりなる平板
(2)(2)と、これらの平板(2)(2)同志の間に
介在された第1流体流路形成体(3)とによって形成さ
れている。Here, the first flow path (A) is interposed between the flat plates (2) and (2) made of aluminum brazing sheets facing each other with a predetermined gap, and the flat plates (2) and (2). And the first fluid flow path forming body (3).
一方、第2流路(B)は、相互に所定間隔をあけて対向
する平板(2)(2)と、これらの平板(2)(2)同
志の間に介在されかつ平板(2)(2)の前後側縁部に
対応するように配置された一対のアルミニウム押出形材
製の間隔保持用側壁部(10)(10)と、両側壁部(10)
(10)同志の中間に位置せしめられたルーバ付きコルゲ
ート・フィン(11)とによって形成されている。On the other hand, the second flow path (B) is interposed between the flat plates (2) and (2) facing each other at a predetermined interval and the flat plates (2) and (2) (2) (). A pair of side wall parts (10) (10) made of aluminum extruded shape and arranged so as to correspond to the front and rear side edges, and both side wall parts (10).
(10) It is formed by corrugated fins (11) with louvers located in the middle of the comrades.
第1流体流路形成体(3)は、平板(2)の左右両側縁
部に対応するように配置された一対の間隔保持用側壁部
(5)(5)と、これら両側壁部(5)(5)同志を連
結するとともに内部に側壁部(5)(5)と平行な多数
の横断面略菱形の中空部(6)を有しかつ上下両外面が
それぞれ断面波形となされていてその波頭部(4a)に上
方もしくは下方にのびている所要高さの横断面鳩尾状の
凸部(7)(7)を備えた中空連結壁部(4)とよりな
るアルミニウム押出型材によってつくられ、中空連結壁
部(4)の上下両側の横断面鳩尾状凸部(7)(7)の
平坦な頂面(7a)(7a)がそれぞれ平板(2)に接合さ
れている。The first fluid flow path forming member (3) includes a pair of side wall portions (5) (5) for holding a gap, which are arranged so as to correspond to the left and right side edges of the flat plate (2), and the side wall portions (5). ) (5) A plurality of hollow portions (6) having a substantially rhombic cross section parallel to the side wall portions (5) and (5) are formed inside, and the upper and lower outer surfaces are each corrugated in cross section. Made of an aluminum extruded material consisting of a hollow connecting wall portion (4) provided with a convex section (7) (7) having a cross-section dovetail shape of a required height extending upward or downward on the wave head (4a), The flat top surfaces (7a) (7a) of the dovetail-shaped convex portions (7) (7) on the upper and lower sides of the hollow connecting wall portion (4) are respectively joined to the flat plate (2).
そして、中空連結壁部(4)内側の横断面略菱形の中空
部(6)の断面積(S1)と、中空連結壁部(4)の上下
両外面の波形凹状部(8)、これの両側の凸部(7)
(7)、および凹状部(8)に対向する平板部分(2a)
によって囲まれた横断面略五角形の中空部(9)の断面
積(S2)とが略等しいものとなされている。The cross-sectional area (S1) of the hollow portion (6) having a substantially rhombic cross section inside the hollow connecting wall portion (4) and the corrugated concave portions (8) on both the upper and lower outer surfaces of the hollow connecting wall portion (4), Convex parts on both sides (7)
(7) and the flat plate portion (2a) facing the concave portion (8)
The cross-sectional area (S2) of the hollow portion (9) having a substantially pentagonal cross section surrounded by is substantially equal.
ここで具体的には、中空連結壁部(4)内側の横断面略
菱形の中空部(6)の相当径は、例えば約2.5mmであ
り、これに対し、中空連結壁部(4)の上下両外側の横
断面略五角形の中空部(9)の相当径は、約2.3mmであ
って、両中空部(6)(9)の断面積(S1)(S2)は、
略等しいものとなされている。Specifically, the equivalent diameter of the hollow portion (6) having a substantially rhombic cross section inside the hollow connecting wall portion (4) is, for example, about 2.5 mm, whereas the hollow connecting wall portion (4) has an equivalent diameter. The equivalent diameter of the hollow portion (9) having a substantially pentagonal cross section on both the upper and lower outer sides is about 2.3 mm, and the cross-sectional areas (S1) (S2) of both hollow portions (6) (9) are
It is supposed to be almost equal.
なお、上記従来のインタークーラでは、アルミニウム中
空押出型材製の第1流体流路形成体の内側の横断面略菱
形の中空部の相当径は、例えば約2.5mmであり、これに
対し、中空連結壁部の上下両外側の横断面略三角形の中
空部の相当径は、約1.5mmであって、両中空部の断面積
は相互にかなり異なっていた。In the above conventional intercooler, the equivalent diameter of the hollow portion having a substantially rhombic cross section inside the first fluid flow path forming member made of an aluminum hollow extruded material is, for example, about 2.5 mm. The equivalent diameter of the hollow part having a substantially triangular cross-section on both the upper and lower outer sides of the wall part was about 1.5 mm, and the cross-sectional areas of both hollow parts were quite different from each other.
このため従来は、両中空部内を流れる流体の流量および
流速等がかなり異なって、流れが不均一となり、かつ圧
力損失が大きかった。For this reason, conventionally, the flow rates and flow velocities of the fluids flowing in both hollow portions are considerably different, resulting in non-uniform flow and large pressure loss.
また、上記実施例においては、第1流体流路形成体
(3)の中空連結壁部(4)の断面波形上下両外面にお
いて、波頭部(4a)に設ける凸部(7)の形状を、横断
面鳩尾状、すなわち波頭部(4a)の幅よりも凸部(7)
の平坦な頂面(7a)の幅の方が広い形状として、この凸
部(7)の幅広の頂面(7a)を平板(2)に接合してい
るから、第1流体流路形成体(3)と平板(2)との接
合面積が非常に広いものとなっており、インタークーラ
(1)の耐圧強度が大幅にアップしている。In addition, in the above-mentioned embodiment, the shape of the convex portion (7) provided on the corrugated portion (4a) is formed on both upper and lower outer surfaces of the corrugated section of the hollow connecting wall portion (4) of the first fluid flow path forming body (3). , Cross-section dovetail, that is, the convex portion (7) is wider than the width of the crest (4a)
Since the flat top surface (7a) of the is made wider, and the wide top surface (7a) of the convex portion (7) is joined to the flat plate (2), the first fluid flow path forming body is formed. The joint area between (3) and the flat plate (2) is very large, and the pressure resistance of the intercooler (1) is significantly increased.
従って、例えば従来の中空連結壁部の上下両外側の幅の
狭い波頭部をそのまま平板に接合したインタークーラの
耐圧強度と同程度のものを得るには、平板(2)および
第1流体流路形成体(3)の肉厚を、それぞれ減らすこ
とができるものである。Therefore, for example, in order to obtain the same compressive strength as that of the intercooler in which the narrow wave tops on both the upper and lower sides of the conventional hollow connecting wall are directly joined to the flat plate, the flat plate (2) and the first fluid flow can be obtained. The wall thickness of the channel forming body (3) can be reduced respectively.
例えば第1流体流路形成体(3)の中空連結壁部(4)
の上下両外面の波頭部(4a)の幅を0.4mm、これに対し
て、横断面鳩尾状の凸部(7)の平坦な頂面(7a)の幅
を0.7mmとすると、インタークーラ(1)の重量は約20
%低減することが可能であった。For example, the hollow connecting wall portion (4) of the first fluid flow path forming body (3)
If the width of the wave crests (4a) on both the upper and lower outer surfaces of is 0.4mm, while the width of the flat top surface (7a) of the convex section (7) with a transverse cross section is 0.7mm, the intercooler Weight of (1) is about 20
% Could be reduced.
この発明によるインタークーラ(1)において、平板
(2)は少なくとも3枚使用する。従ってインタークー
ラ(1)の最も小さいものは、理論的には第1流路
(A)と第2流路(B)とを1個ずつ有している。実際
には、インタークーラを例にとれば、インタークーラ
(1)は第1流路(A)を1〜20個、並びに第2流路
(B)を1〜20個有していて、第1流路(A)と第2流
路(B)とが交互に配置されている。このような流路
(A)(B)の数は単なる例示であり、インタークーラ
(1)の大きさ、および熱交換性能によって両流路
(A)(B)の数が設定される。また第2流路(B)の
フィン部材(11)は、コルゲート・フィンに限らず、そ
の他の形状のフィンにより構成されていても勿論よい。In the intercooler (1) according to the present invention, at least three flat plates (2) are used. Therefore, the smallest intercooler (1) theoretically has one first flow path (A) and one second flow path (B). In fact, taking the intercooler as an example, the intercooler (1) has 1 to 20 first flow paths (A) and 1 to 20 second flow paths (B). The 1st channel (A) and the 2nd channel (B) are arranged by turns. The number of such channels (A) and (B) is merely an example, and the number of both channels (A) and (B) is set depending on the size of the intercooler (1) and the heat exchange performance. Further, the fin member (11) of the second flow path (B) is not limited to the corrugated fin, and may be formed of fins having other shapes.
上記各実施例のインタークーラ(1)は、流体流路
(A)(B)が水平に配置されたいわゆる横型インター
クーラとして使用されているが、インタークーラ(1)
は両流路(A)(B)が垂直に配置された縦型インター
クーラとして使用されてもよい。The intercooler (1) of each of the above-mentioned embodiments is used as a so-called horizontal type intercooler in which the fluid passages (A) and (B) are horizontally arranged.
May be used as a vertical intercooler in which both flow paths (A) and (B) are vertically arranged.
また、図示のインタークーラ(1)においては、第1流
路(A)と第2流路(B)とが直交状に配置されている
が、両流路(A)(B)は互いに平行に配置される場合
もある。そしてこの場合においては両流路(A)(B)
内の2種の流体は互いに平行流となるようにあるいは互
いに対向流となるように移行せしめられる。Further, in the illustrated intercooler (1), the first flow path (A) and the second flow path (B) are arranged orthogonally, but both flow paths (A) and (B) are parallel to each other. It may be placed in. And in this case, both flow paths (A) and (B)
The two kinds of fluid inside are transferred so as to be parallel to each other or to be opposite to each other.
また実施例は、この発明は熱交換器(1)をインターク
ーラに適用した場合を示しているが、この発明の熱交換
器は、インタークーラだけでなく、気体および流体につ
いて2種類の流体の熱交換を行なう各種の熱交換器にも
同様に適用可能である。In addition, although the present invention shows a case where the present invention applies the heat exchanger (1) to an intercooler, the heat exchanger of the present invention is not limited to the intercooler, and it can be used for two types of fluids, gas and fluid. It can be similarly applied to various heat exchangers that perform heat exchange.
発明の効果 この発明は、上述のように、熱交換第1流体が流される
少なくとも1つの第1流路と、第1流体と熱交換される
べき熱交換第2流体が流される少なくとも1つの第2流
路とを備えており、第1流路が相互に所定間隔をあけて
対向する平板と、これらの平板同志の間に介在された第
1流体流路形成体とによって形成され、第2流路が、相
互に所定間隔をあけて対向する平板と、これらの平板同
志の間に介在されかつ平板の左右もしくは前後側縁部に
対応するように配置された一対の間隔保持用側壁部およ
び両側壁部同志の中間に位置せしめられたフィン部材と
によって形成されている熱交換器において、上記第1流
体流路形成体が、平板の左右両側縁部に対応するように
配置された一対の間隔保持用側壁部と、これら両側壁部
同志を連結するとともに内部に側壁部と平行な多数の中
空部を有しかつ上下両外面がそれぞれ断面波形となされ
ていてその波頭部に上方もしくは下方にのびている所要
高さの凸部を備えた中空連結壁部とよりなるアルミニウ
ム押出型材によってつくられ、中空連結壁部内側の中空
部の断面積と、中空連結壁部の上下両外面の波形凹状
部、これの両側の凸部、および凹状部に対向する平板部
分によって囲まれた中空部の断面積とが略等しいものと
なされているから、第1流路内のすべての中空部の断面
積が略等しいものとなる。このため、中空部内を流れる
流体の流量および流速等が等しくなり、流体の流れが均
一となるとともに、圧力損失が非常に少なく、例えばこ
の発明による熱交換器をインタークーラに適用した場合
に、流路内を高温高圧の空気が高速で流れても、圧力損
失が非常に少なく、熱交換性能が向上するという効果を
奏する。Advantageous Effects of Invention The present invention, as described above, includes at least one first flow path through which the heat exchange first fluid flows, and at least one first flow path through which the heat exchange second fluid to be heat-exchanged with the first fluid flows. Two flow paths, the first flow path is formed by flat plates facing each other with a predetermined gap, and a first fluid flow path forming body interposed between the flat plates, Flat plates whose flow paths are opposed to each other at a predetermined interval, and a pair of side wall parts for holding the space interposed between the flat plates and arranged so as to correspond to the left and right or front and rear side edges of the flat plate, In a heat exchanger formed by a fin member positioned in the middle of both side wall parts, a pair of first fluid flow path forming members arranged so as to correspond to both left and right edges of the flat plate. The space side wall part and these side wall parts A hollow that is connected and has a large number of hollow portions parallel to the side wall portion, the upper and lower outer surfaces are each corrugated in cross section, and the wave head has a convex portion of a required height extending upward or downward. Made of aluminum extruded material consisting of the connecting wall part, and the cross-sectional area of the hollow part inside the hollow connecting wall part, the corrugated concave parts on the upper and lower outer surfaces of the hollow connecting wall part, the convex parts on both sides of this, and the concave part. Since the cross-sectional areas of the hollow portions surrounded by the flat plate portions facing each other are substantially the same, the cross-sectional areas of all the hollow portions in the first flow path are substantially the same. Therefore, the flow rate and the flow velocity of the fluid flowing in the hollow portion become equal, the fluid flow becomes uniform, and the pressure loss is very small. For example, when the heat exchanger according to the present invention is applied to an intercooler, Even if high-temperature and high-pressure air flows at high speed in the passage, the pressure loss is very small and the heat exchange performance is improved.
図面はこの発明をインタークーラに適用した実施例を示
すもので、第1図はインタークーラの要部分解斜視図、
第2図は同要部正面図、第3図は同概略側面図である。 (A)…第1流体流路、(B)…第2流体流路、(1)
…インタークーラ(熱交換器)、(2)…平板、(2a)
…平板部分、(3)…第1流体流路形成体、(4)…中
空連結壁、(4a)…波頭部、(5)…間隔保持用側壁
部、(6)…中空部、(7)…凸部、(8)…波形凹状
部、(9)…中空部、(10)…間隔保持用側壁部、(1
1)…フィン部材、(S1)(S2)…断面積。The drawings show an embodiment in which the present invention is applied to an intercooler, and FIG. 1 is an exploded perspective view of a main part of the intercooler,
FIG. 2 is a front view of the relevant part, and FIG. 3 is a schematic side view of the same. (A) ... 1st fluid channel, (B) ... 2nd fluid channel, (1)
… Intercooler (heat exchanger), (2)… flat plate, (2a)
... flat plate part, (3) ... first fluid flow path forming body, (4) ... hollow connection wall, (4a) ... corrugated head, (5) ... spacing side wall part, (6) ... hollow part, ( 7) ... convex part, (8) ... corrugated concave part, (9) ... hollow part, (10) ... side wall part for spacing, (1)
1) ... Fin member, (S1) (S2) ... Cross-sectional area.
Claims (1)
の第1流路(A)と、第1流体と熱交換されるべき熱交
換第2流体が流される少なくとも1つの第2流路(B)
とを備えており、第1流路(A)が相互に所定間隔をあ
けて対向する平板(2)(2)と、これらの平板(2)
(2)同志の間に介在された第1流体流路形成体(3)
とによって形成され、第2流路(B)が、相互に所定間
隔をあけて対向する平板(2)(2)と、これらの平板
(2)(2)同志の間に介在されかつ平板(2)(2)
の左右もしくは前後側縁部に対応するように配置された
一対の間隔保持用側壁部(10)(10)および両側壁部
(10)(10)同志の中間に位置せしめられたフィン部材
(11)とによって形成されている熱交換器において、 上記第1流体流路形成体(3)が、平板(2)の左右両
側縁部に対応するように配置された一対の間隔保持用側
壁部(5)(5)と、これら両側壁部(5)(5)同志
を連結するとともに内部に側壁部(5)(5)と平行な
多数の中空部(6)を有しかつ上下両外面がそれぞ断面
波形となされていてその波頭部(4a)に上方もしくは下
方にのびている所要高さの凸部(7)(7)を備えた中
空連結壁部(4)とよりなるアルミニウム押出型材によ
ってつくられ、中空連結壁部(4)内側の中空部(6)
の断面積(S1)と、中空連結壁部(4)の上下両外面の
波形凹状部(8)、これの両側の凸部(7)(7)、お
よび凹状部(8)に対向する平板部分(2a)によって囲
まれた中空部(9)の断面積(S2)とが略等しいものと
なされている、熱交換器。1. At least one first flow path (A) through which a heat exchange first fluid flows, and at least one second flow path (through which a heat exchange second fluid to be heat-exchanged with the first fluid flows). B)
And flat plates (2) and (2) having first flow paths (A) facing each other at a predetermined interval, and these flat plates (2).
(2) First fluid flow path forming body (3) interposed between the two
The second flow path (B) is formed by and the flat plates (2) and (2) that face each other with a predetermined gap therebetween, and these flat plates (2) and (2) are interposed between the flat plates (2) and (2). 2) (2)
A fin member (11) located in the middle of a pair of side wall portions (10) (10) for maintaining a space and both side wall portions (10) (10) arranged so as to correspond to the left and right or front and rear side edges of ), The first fluid flow path forming body (3) has a pair of side wall portions for spacing ((3) arranged so as to correspond to both left and right edges of the flat plate (2). 5) and (5) and both side wall portions (5) and (5) are connected to each other, and a plurality of hollow portions (6) parallel to the side wall portions (5) and (5) are provided inside, and both upper and lower outer surfaces are An extruded aluminum material having a hollow connecting wall portion (4) each having a corrugated cross-section and a convex portion (7) (7) of a required height extending upward or downward on the wave head (4a). Hollow part (6) made inside by hollow connecting wall part (4)
Cross-sectional area (S1) of the hollow connecting wall (4) and the corrugated concave portions (8) on the upper and lower outer surfaces of the hollow connecting wall portion (4), the convex portions (7) (7) on both sides of the corrugated concave portion (8), and the flat plate facing the concave portion (8). A heat exchanger in which the cross-sectional area (S2) of the hollow portion (9) surrounded by the portion (2a) is substantially equal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2314939A JPH0670557B2 (en) | 1990-11-19 | 1990-11-19 | Heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2314939A JPH0670557B2 (en) | 1990-11-19 | 1990-11-19 | Heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04186098A JPH04186098A (en) | 1992-07-02 |
| JPH0670557B2 true JPH0670557B2 (en) | 1994-09-07 |
Family
ID=18059475
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2314939A Expired - Fee Related JPH0670557B2 (en) | 1990-11-19 | 1990-11-19 | Heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0670557B2 (en) |
-
1990
- 1990-11-19 JP JP2314939A patent/JPH0670557B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04186098A (en) | 1992-07-02 |
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| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |