JPS625579Y2 - - Google Patents

Info

Publication number
JPS625579Y2
JPS625579Y2 JP306182U JP306182U JPS625579Y2 JP S625579 Y2 JPS625579 Y2 JP S625579Y2 JP 306182 U JP306182 U JP 306182U JP 306182 U JP306182 U JP 306182U JP S625579 Y2 JPS625579 Y2 JP S625579Y2
Authority
JP
Japan
Prior art keywords
flat tube
protrusion
guide groove
heat exchanger
water guide
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
Application number
JP306182U
Other languages
Japanese (ja)
Other versions
JPS58107476U (en
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 filed Critical
Priority to JP1982003061U priority Critical patent/JPS58107476U/en
Publication of JPS58107476U publication Critical patent/JPS58107476U/en
Application granted granted Critical
Publication of JPS625579Y2 publication Critical patent/JPS625579Y2/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
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/047Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag
    • F28D1/0477Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag
    • F28D1/0478Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag the conduits having a non-circular cross-section
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2225/00Reinforcing means
    • F28F2225/04Reinforcing means for conduits

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

【考案の詳細な説明】 本考案は熱交換器、特に車輌用冷房装置の横置
きタイプの熱交換器に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat exchanger, particularly a horizontal type heat exchanger for a vehicle cooling system.

一般に車輌冷房装置用の熱交換器はケースに収
納されて車輌前席の助手席側ダツシユボードの下
に取り付ける型式が多く用いられており、着座者
の足先きのスペースに余裕を確保できるように前
記熱交換器の設置スペースは横長形状となる場合
が多い。これに使用される熱交換器は折曲蛇行す
る偏平管の平行をなす部分を垂直方向に配置した
縦置きタイプと、水平方向に配置した横置きタイ
プの何れかが採択される。
In general, heat exchangers for vehicle cooling systems are often housed in a case and installed under the dash board on the passenger side of the front seat of the vehicle, so that there is plenty of space for the feet of the occupants. The installation space for the heat exchanger is often horizontally elongated. The heat exchanger used for this purpose is either a vertical type in which parallel portions of bent and meandering flat tubes are arranged vertically, or a horizontal type in which parallel parts are arranged in a horizontal direction.

ところで熱交換器においては冷房用取入空気は
偏平管内部を流れる冷媒と熱交換して冷却され同
時に空気中の水分は凝縮水となり空気流によつて
コルゲートフイン及び偏平管の表面上を吹き流さ
れて下流側辺に至るが、熱交換器ではこの凝縮水
の処理が問題となる。即ち横長形状の設置スペー
スに縦置きタイプを用いると凝縮水の流下排出に
は良いが、偏平管の段数が多くなるに伴い偏平管
の折曲部も増すので、相対的にコルゲートフイン
の挟着される面積が小さくなり、設置スペースの
所定の正面々積に対して熱交換部の正面々積の比
率が減少して冷却効率が悪くなる等の欠点があ
る。これに反して横置きタイプは正面々積に対す
る熱交換部正面々積の比率は大きくなるが、凝縮
水が偏平管の空気流の下流側辺から飛水し、排水
処理が困難である等の欠点がある。
By the way, in a heat exchanger, the intake air for cooling is cooled by exchanging heat with the refrigerant flowing inside the flat tubes, and at the same time, moisture in the air becomes condensed water and is blown onto the surface of the corrugated fins and flat tubes by the air flow. The condensed water then reaches the downstream side, but treatment of this condensed water becomes a problem in the heat exchanger. In other words, using a vertical type in a horizontally long installation space is good for draining condensed water, but as the number of stages of flat tubes increases, the number of bent portions of the flat tubes also increases, making it relatively difficult for corrugated fins to be pinched. There are drawbacks such as a reduction in the surface area of the heat exchanger, and a decrease in the ratio of the front-to-face area of the heat exchanger to a predetermined front-to-face area of the installation space, resulting in poor cooling efficiency. On the other hand, with the horizontal type, the ratio of the front-to-front area of the heat exchanger to the front-to-front area is larger, but condensed water splashes from the downstream side of the airflow of the flat tube, making it difficult to treat wastewater. There are drawbacks.

本考案は上述の点に鑑み横置きタイプの熱交換
器を改良したものであり、、冷媒流路を区画した
偏平管を折曲蛇行し、平行をなす部分間にコルゲ
ートフインを挟着し、前記偏平管の両端に冷媒の
流入、流出ヘツダを接続して構成し、該平行をな
す部分を水平方向に配置した熱交換器において、
前記偏平管は空気流の下流側辺に沿い所定長さの
突条を一体形成すると共に、該突条の表裏面の所
定位置に所定深さの線条を形成して該線条部より
突条を上方に折曲して水平方向の導水溝を形成
し、且つ該導水溝の端部において突条を適宜巾切
欠いて排水部を形成し、凝縮水がコルゲートフイ
ン及び偏平管の表面上を吹き流されて導水溝に流
れ込み排水部から排水され、凝縮水が偏平管の空
気流の下流側辺から飛水するのを防止できる熱交
換器を提供するものである。
The present invention is an improvement on the horizontal type heat exchanger in view of the above-mentioned points.The flat tube that defines the refrigerant flow path is bent and meandered, and corrugated fins are sandwiched between the parallel parts. A heat exchanger configured by connecting refrigerant inflow and outflow headers to both ends of the flat tube, and in which the parallel portions are arranged horizontally,
The flat tube has a protrusion of a predetermined length integrally formed along the downstream side of the air flow, and a filament of a predetermined depth is formed at a predetermined position on the front and back surfaces of the protrusion so that the protrusion protrudes from the filament. The strip is bent upward to form a horizontal water guide groove, and at the end of the water guide groove, the protruding strip is notched to an appropriate width to form a drainage section, so that condensed water flows over the surfaces of the corrugated fin and flat tube. To provide a heat exchanger that is blown away, flows into a water guide groove, is drained from a drainage part, and can prevent condensed water from flying out from the downstream side of the airflow of a flat tube.

以下本考案に係る一実施例を添付図面に基いて
詳述する。
An embodiment of the present invention will be described in detail below with reference to the accompanying drawings.

第1図で示すように熱交換器は帯状の偏平管1
を折曲蛇行し、偏平管1の両端に流入ヘツダ2及
び流出ヘツダ3を接続し、偏平管1の相隣接する
平行部1a間にコルゲートフイン4を挟着し、最
外端のコルゲートフイン4に端板5を固定し、ま
た偏平管1の折曲部1bには枠体6を装着して構
成される。冷房用取入空気は図面裏面方向から取
入れられ、コルゲートフイン4を通過する時に偏
平管1の内部を流過する冷媒の蒸発熱により冷却
され、図面表面方向に排出される。第2図に示す
ように、偏平管1は内部に複数の冷媒流路7が形
成された断面多孔管構造体で、アルミニウム等熱
伝導性が良好な材料を用いて押出成形等で形成さ
れ、一側辺沿いに該偏平管1と一体に形成された
突条8が形成されており、この突条8の表裏面の
対応する所定位置に所定深さの線条9,10が突
条8に沿つて刻設されている。線条9,10を突
条8の表裏面に設けたのは線条9,10を折曲部
として突条8を表裏何れの方向にも折曲げを容易
にするためである。第3図に示すように、偏平管
1は突条8を備えた側辺を空気流の下流側に位置
するように前記熱交換器内に配設する。偏平管1
のコルゲートフイン4を挟着した平行部1aの
夫々において、突条8の先端部8aを線条9,1
0を折曲部として折曲し、折曲した突条8の先端
部8′aを一側壁とし偏平管1の側辺部を他側壁
とする断面形状略コ字状の導水溝11を偏平管1
側辺沿いに形成する。そして上記突条8は導水溝
11の水平端部において適宜巾切欠かれて排水部
12を形成し、偏平管1の折曲部1bにおける突
条8の残余の部分は折曲せずそのまま残してお
く。
As shown in Figure 1, the heat exchanger consists of a band-shaped flat tube 1
The inflow header 2 and the outflow header 3 are connected to both ends of the flat tube 1, and the corrugated fins 4 are sandwiched between the adjacent parallel parts 1a of the flat tube 1. An end plate 5 is fixed to the flat tube 1, and a frame 6 is attached to the bent portion 1b of the flat tube 1. The intake air for cooling is taken in from the back side of the drawing, is cooled by the heat of evaporation of the refrigerant flowing inside the flat tube 1 when passing through the corrugated fins 4, and is discharged towards the front side of the drawing. As shown in FIG. 2, the flat tube 1 is a cross-sectional porous tube structure in which a plurality of refrigerant channels 7 are formed inside, and is formed by extrusion molding or the like using a material with good thermal conductivity such as aluminum. A protrusion 8 integrally formed with the flat tube 1 is formed along one side, and filaments 9 and 10 of a predetermined depth are provided at corresponding predetermined positions on the front and back surfaces of the protrusion 8. It is engraved along the The reason why the filaments 9 and 10 are provided on the front and back surfaces of the protrusion 8 is to make it easy to bend the protrusion 8 in either direction by using the filaments 9 and 10 as bending parts. As shown in FIG. 3, the flat tube 1 is disposed within the heat exchanger so that the side surface provided with the protrusion 8 is located on the downstream side of the air flow. Flat tube 1
In each of the parallel parts 1a sandwiching the corrugated fins 4, the tips 8a of the protrusions 8 are connected to the filaments 9, 1.
0 as a bending part, and flatten a water guide groove 11 having a substantially U-shaped cross section with the tip 8'a of the bent protrusion 8 as one side wall and the side part of the flat tube 1 as the other side wall. tube 1
Form along the sides. The protrusion 8 is notched to an appropriate width at the horizontal end of the water guide groove 11 to form a drainage portion 12, and the remaining portion of the protrusion 8 at the bent portion 1b of the flat tube 1 is left unbent. put.

上記構成において凝縮水はコルゲートフイン4
及び偏平管1の表面上を空気流に吹き流されて導
水溝11に流れ込む。この導水溝11は空気流の
陰になつているので導水溝11に流入した凝縮水
は飛散されることなく導水溝11の端部の排水部
12に導びかれ速やかに排水される。ここで熱交
換器を水平に対してθの角度をもつて正面視横方
向に傾斜配置すれば前記凝縮水は更に迅速に排水
されることになる。
In the above configuration, the condensed water is transferred to the corrugated fin 4.
The water is blown away by the air flow on the surface of the flat tube 1 and flows into the water guide groove 11. Since the water guide groove 11 is in the shadow of the air flow, the condensed water flowing into the water guide groove 11 is guided to the drainage part 12 at the end of the water guide groove 11 without being scattered, and is quickly drained. If the heat exchanger is arranged at an angle of θ with respect to the horizontal in a lateral direction when viewed from the front, the condensed water can be drained more quickly.

尚導水溝11端部の排水部12は図示のように
導水溝11の両端部に設けても、また左右何れか
一方の端部のみに設けても良い。特に熱交換器を
傾斜配置する場合には導水溝11の下流側端部の
みに排水部12を設ければ十分である。
The drainage portions 12 at the ends of the water guide groove 11 may be provided at both ends of the water guide groove 11 as shown in the figure, or may be provided only at either the left or right end. Particularly when the heat exchanger is arranged at an angle, it is sufficient to provide the drainage section 12 only at the downstream end of the water guide groove 11.

以上説明したように本考案によれば、偏平管の
空気流の下流側辺に該偏平管と一体に形成した突
条を上方に折曲し、偏平管の平行部の前記側辺沿
いに水平方向の導水溝を形成し、且つ該導水溝の
両端部に排水部を形成したので、凝縮水はコルゲ
ートフイン及び偏平管の表面上を空気流に吹き流
されて導水溝に流れ込み該導水溝の端部の排水部
から排水され、偏平管の前記側辺からの飛水を防
止することができる。従つて横長形状の設置スペ
ースに縦置きタイプに替え該スペースの形状に合
致した横置きタイプを用いることにより設置スペ
ースの所定の正面々積に対する熱交換部の比率が
増大し、冷却効率を向上することができる。また
前記突条の両面に線条を形成し該線条を折曲部と
して突条の線条から先端部を折曲して導水溝を形
成するので、折曲蛇行状に形成され交互に表裏が
反復する偏平管の夫々の平行部において突条の何
れの面が上面になつていても平行部の突条の先端
部をすべて上方に折曲して前記導水溝を形成する
ことができ、熱交換器の組立性が向上するという
利点がある。
As explained above, according to the present invention, a protrusion integrally formed with the flat tube is bent upward on the downstream side of the air flow of the flat tube, and the protrusion is bent upward along the side of the parallel portion of the flat tube. Since a water guide groove is formed in the direction of the water guide groove and drainage portions are formed at both ends of the water guide groove, the condensed water is blown away by the air flow on the surface of the corrugated fin and the flat tube and flows into the water guide groove. Water is drained from the drainage portion at the end, and water can be prevented from splashing from the sides of the flat tube. Therefore, by using a horizontal type that matches the shape of the space instead of a vertical type in a horizontally long installation space, the ratio of the heat exchange section to the predetermined front-to-front area of the installation space increases, improving cooling efficiency. be able to. In addition, striations are formed on both sides of the protrusion, and the striations are used as bent portions to form water guide grooves by bending the tips of the striations of the protrusion. In each of the parallel parts of the flat tube where repeating is repeated, no matter which surface of the protrusions is the upper surface, the water guide groove can be formed by bending all the tips of the protrusions in the parallel parts upward, This has the advantage of improving the ease of assembling the heat exchanger.

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

第1図は本考案に係る一実施例を示す正面全体
概要図、第2図は偏平管の概略断面図、第3図は
導水溝の説明図である。 1……偏平管、1a……平行部、1b……折曲
部、4……コルゲートフイン、8……突条、9,
10……線条、11……導水溝、12……排水
部。
FIG. 1 is an overall schematic front view showing an embodiment of the present invention, FIG. 2 is a schematic sectional view of a flat tube, and FIG. 3 is an explanatory view of a water guide groove. DESCRIPTION OF SYMBOLS 1... Flat tube, 1a... Parallel part, 1b... Bent part, 4... Corrugated fin, 8... Projection, 9,
10... Line, 11... Water guide groove, 12... Drainage section.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 冷媒流路を区画した偏平管を折曲蛇行し、平行
をなす部分間にコルゲートフインを挟着し、前記
偏平管の両端に冷媒の流入、流出ヘツダを接続し
て構成し、該平行をなす部分を水平方向に配置し
た熱交換器において、前記偏平管は空気流の下流
側辺に沿い所定長さの突条を一体形成すると共に
該突条の表裏面の所定位置に所定深さの線条を形
成して該線条部より前記突条を上方に折曲して水
平方向の導水溝を形成し、且つ該導水溝の端部に
おいて前記突条を適宜巾切欠いて排水部を形成し
たことを特徴とする熱交換器。
A flat tube that defines a refrigerant flow path is bent and meandered, corrugated fins are sandwiched between the parallel parts, and refrigerant inflow and outflow headers are connected to both ends of the flat tube, so that the parallel paths are formed. In a heat exchanger in which parts are arranged horizontally, the flat tube integrally forms a protrusion of a predetermined length along the downstream side of the air flow, and a line of a predetermined depth is formed at a predetermined position on the front and back surfaces of the protrusion. A horizontal water guide groove was formed by forming a strip, and the protrusion was bent upward from the linear portion, and a drainage portion was formed by notching the protrusion to an appropriate width at the end of the water guide groove. A heat exchanger characterized by:
JP1982003061U 1982-01-13 1982-01-13 Heat exchanger Granted JPS58107476U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1982003061U JPS58107476U (en) 1982-01-13 1982-01-13 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1982003061U JPS58107476U (en) 1982-01-13 1982-01-13 Heat exchanger

Publications (2)

Publication Number Publication Date
JPS58107476U JPS58107476U (en) 1983-07-21
JPS625579Y2 true JPS625579Y2 (en) 1987-02-07

Family

ID=30016010

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1982003061U Granted JPS58107476U (en) 1982-01-13 1982-01-13 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS58107476U (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012093010A (en) * 2010-10-25 2012-05-17 Sharp Corp Heat exchanger and air conditioner mounted with the same
JP5009409B2 (en) * 2010-10-25 2012-08-22 シャープ株式会社 Heat exchanger and air conditioner equipped with the same
CN103180684B (en) * 2010-10-25 2015-12-16 夏普株式会社 Heat exchanger and the air conditioner being provided with heat exchanger

Also Published As

Publication number Publication date
JPS58107476U (en) 1983-07-21

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