JPS5849895A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPS5849895A
JPS5849895A JP14624881A JP14624881A JPS5849895A JP S5849895 A JPS5849895 A JP S5849895A JP 14624881 A JP14624881 A JP 14624881A JP 14624881 A JP14624881 A JP 14624881A JP S5849895 A JPS5849895 A JP S5849895A
Authority
JP
Japan
Prior art keywords
flat tube
heat exchanger
strength members
tube
arrangement
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.)
Pending
Application number
JP14624881A
Other languages
Japanese (ja)
Inventor
Takeo Tanaka
武雄 田中
Masaaki Ito
正昭 伊藤
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.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP14624881A priority Critical patent/JPS5849895A/en
Publication of JPS5849895A publication Critical patent/JPS5849895A/en
Pending 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
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/40Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only inside the tubular element
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To improve the heat transmitting performance inside the tube of the heat exchanger by a method wherein the arrangement of strength members, which form coolant passages within the flat tube. CONSTITUTION:Subject heat exchanger is formed: Firstly, an intermediate member 13 is produced by forming strength members 11, which are laid out in such an arrangement as to promote heat transmission, and a positioner 12, which coagulates at an intermediate temperature of about 150 deg.C and serves to keep the fixed intervals between the members 11, into one integral body. Secondly, the intermediate member 13 is inserted into the flat tube 10, which has no partition walls at all. Thirdly, pressure is applied from the outside of the flat tube 10 so as to temporarily fix the strength members 11 and the flat tube 10. Fourthly, the positioner 12 is removed by washing with water or the like. Fifthly, after that, the strength members 11 and the flat tube 10 are put in a high temperature furnace in order to be jointed together with one another to complete the heat exchanger. Owing to the structure as described above, the coolant in the flat tube 10 freely flows normal to the direction of main flow and as well as the free selection of arrangement of the strength members becomes possible, resulting in enabling to realize a heat pipe with high performance.

Description

【発明の詳細な説明】 本発明は強度部材によって内部に複数の冷媒流路を並列
に形成した偏平管を蛇行状にし互いに平行する部分にコ
ルゲートフィンを接合してなる熱交換器に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat exchanger comprising a flat tube in which a plurality of refrigerant flow paths are formed in parallel using a strength member in a meandering shape and corrugated fins are joined to mutually parallel portions.

従来、この種の熱交換器は第illに示すように蛇行状
に折曲形成された偏平管1と偏平$1の並行する部分に
接合されたコルゲートフィン2と冷媒入口管3か接続さ
れ九人ロヘッダ4と、冷媒出口管5が!IHされた出口
へラダ6から構成されている。偏平管1は第2図に示す
ように管内が耐圧を青感して設けられた多数の強度部材
7によって内部に複数の冷媒流路8が並夕1jに形成さ
れている。
Conventionally, this type of heat exchanger has a flat tube 1 bent into a meandering shape, corrugated fins 2 joined to parallel parts of the flat tube 1, and a refrigerant inlet pipe 3 connected to each other, as shown in FIG. The header 4 and the refrigerant outlet pipe 5! It consists of a rudder 6 to the IH exit. As shown in FIG. 2, the flat tube 1 has a plurality of refrigerant flow paths 8 arranged in parallel lines 1j inside the tube by a large number of strength members 7 provided so that the inside of the tube can withstand pressure.

このような蛇行状の偏平管は、普通押し出し加工によシ
形成して偏平管を蛇行状に折シ曲げて形成する検閲加工
や平板を積層し、高温炉中にて接合する熱間加工によp
製造される。
Such serpentine flat tubes are usually formed by extrusion processing and censored processing in which the flat tube is bent into a serpentine shape, or hot processing in which flat plates are laminated and joined in a high-temperature furnace. Yop
Manufactured.

偏平管を、熱間加工で製造すると、部品点数が多く、溶
接個所が多いので接合面の信頼性を確保する丸め精密金
gを必要とし、設備費が高価となる。これらの問題点は
冷間加工の場合殆んど解決される。しかし、冷間加工の
場合、耐圧を考慮して区切られた冷媒流路となる多数の
空間は各々独立し良ものとならざるを先ず、各々の空間
を流れる流体は互いに隣接する空間に流れることはない
When a flat tube is manufactured by hot processing, there are many parts and many welding points, so rounding precision gold g is required to ensure the reliability of the joint surface, and the equipment cost is high. Most of these problems are solved by cold working. However, in the case of cold working, the large number of spaces that serve as refrigerant flow paths separated in consideration of pressure resistance must be independent and good, and firstly, the fluid flowing through each space must flow into adjacent spaces. There isn't.

そのため、蒸発器を例にとれば、ヘッダでの流量分配が
極度に愚−場合、冷媒流量の少ない空間では出口ヘッダ
に達する途中で完全に蒸発してしまい隣接する空間から
液冷媒が補給されないため、この部分では殆んど熱交熱
せず、伝熱性能が低下してしまう。
For this reason, taking an evaporator as an example, if the flow distribution at the header is extremely poor, in a space where the refrigerant flow rate is low, it will completely evaporate on the way to the outlet header, and liquid refrigerant will not be replenished from the adjacent space. , there is almost no heat exchange in this part, resulting in a decrease in heat transfer performance.

ま九、この種熱交換器の伝熱性能全向上させるためKは
、コルゲートフィン2の形状と共に偏平管1内の形状も
工夫する必要がある。しかし上述の押出し加工では、管
内の形状は加工が困難であるため、自由に選択すること
は出来ない、すなわち冷間加工では、管内の伝熱を促進
できる形状を低プストで製作することが−しい。
(9) In order to completely improve the heat transfer performance of this type of heat exchanger, it is necessary to devise the shape of the corrugated fins 2 as well as the shape of the inside of the flat tube 1. However, in the above-mentioned extrusion process, the shape of the inside of the tube cannot be freely selected because it is difficult to process.In other words, in cold working, it is difficult to create a shape that can promote heat transfer inside the tube at a low cost. Yes.

本発明は上記の点に鋼み、偏平管の管内冷媒通路を形成
する補強部材の形状を工夫し管内伝熱性能を向上させた
熱交換器を得ることを目的としたものである。
The present invention addresses the above points and aims to provide a heat exchanger with improved intra-tube heat transfer performance by devising the shape of the reinforcing member forming the intra-pipe refrigerant passage of the flat tube.

本発明は、隔壁を持たない偏平管の管内に伝熱を促進で
きる形状に形成した強度部材と、この強度部材の間隔を
一定に保持する九めの中子(150cm*の中温で凝固
する)とが一体化した中間部材を挿入した後、偏平管の
外部から加圧し、強度部材と偏平管を仮着けし、水洗等
により中子を除去し、その故、さらに高温炉にて強度部
材と偏平管を接合して形成することを特徴とする。
The present invention consists of a strength member formed in a shape that can promote heat transfer inside a flat tube without partition walls, and a ninth core (150cm* solidified at medium temperature) that maintains a constant distance between the strength members. After inserting the intermediate member that is integrated with the flat tube, pressure is applied from the outside of the flat tube, the strength member and the flat tube are temporarily attached, the core is removed by washing with water, etc. It is characterized by being formed by joining flat tubes.

以下本発明の熱交換器における偏平管の製造方法を1s
3図〜第7図によシ説明する。
The method for manufacturing flat tubes in the heat exchanger of the present invention will be described below for 1 s.
This will be explained with reference to FIGS. 3 to 7.

まず、第3図に示すように、隔壁のない偏平管1Gを形
成し、また第4図、第5図に示すように偏平管10内に
一定間隔で挿入される強度部材111に形成する。強度
部材11は複数用いられて、等間隔で挿入される。また
強度部材11は等間隔で仕切られ九隣接する空間を流体
が流れることが出来るように、第4図の例ではルーパー
状に、また、第5図の例ではくし状にあらかじめプレス
加工により成形する。また成形後強度部材110端面f
ill、llbにはロー材を塗る。次に隣接する強度部
材10の間隔を一定にすること、および偏平管内に挿入
する際変形するのを防止する目的で第6図に示すように
食塩等の比較的低い温度で溶融し、常温において凝固す
る中子12を用い、強度部材11および中子12からな
る中間部材131作る。なお中子12の材質として、水
溶性のものであることを必須とする。また中子里2の厚
さは、強度部材11の高さの約172〜3/41!度と
なるように調節する。
First, as shown in FIG. 3, a flat tube 1G without partition walls is formed, and as shown in FIGS. 4 and 5, strength members 111 are formed to be inserted into the flat tube 10 at regular intervals. A plurality of strength members 11 are used and inserted at equal intervals. The strength members 11 are partitioned at equal intervals and formed in advance by press working into a looper shape in the example shown in FIG. 4, and a comb shape in the example shown in FIG. do. In addition, the end face f of the strength member 110 after molding
Apply wax to ill and llb. Next, in order to make the interval between adjacent strength members 10 constant and to prevent deformation when inserted into a flat tube, as shown in FIG. Using the solidifying core 12, an intermediate member 131 consisting of the strength member 11 and the core 12 is made. Note that the material of the core 12 must be water-soluble. Moreover, the thickness of Nakakosato 2 is approximately 172 to 3/41 of the height of the strength member 11! Adjust to the desired degree.

以上に示す方法で製作した中間部材13を第7図に示す
ように偏平管10に挿入する。この状態において偏平管
10の上面101.下面10bから加圧して偏平管10
と強度部材11を仮り着けする。次に偏平管10内と中
間部材13の間にできる空間に水t−流し、中子12を
溶かすことによシ、徐4に中子12を除去する。十分に
中子12が除去できた後、管内の水懺シを行なう。
The intermediate member 13 manufactured by the method described above is inserted into the flat tube 10 as shown in FIG. In this state, the upper surface 101 of the flat tube 10. Pressure is applied from the lower surface 10b to flatten the tube 10.
and temporarily attach the strength member 11. Next, water is poured into the space created between the inside of the flat tube 10 and the intermediate member 13 to dissolve the core 12, and the core 12 is gradually removed. After the core 12 has been sufficiently removed, the inside of the pipe is drained with water.

次に高温炉にて、前述した強度部材11の上面111%
下面flbのロー材を溶かすことによシ偏平管!0と強
度部材11を固定する。これにより、偏平管は管内に互
いに隣接する流路を遅過する強度部材が形成される。
Next, in a high temperature furnace, 111% of the upper surface of the above-mentioned strength member 11 is heated.
By melting the brazing material on the lower surface flb, you can create a flat tube! 0 and the strength member 11 are fixed. As a result, the flat tube forms a strength member within the tube that slows down the flow paths adjacent to each other.

以上説明し九ように、本発明によれば偏平管内の冷媒の
流れは、流れと直角方向に自由に流れるようになplか
り強度部材の形状を自由に選択できるので、高性能な伝
熱管とすることが可能となる。
As explained above, according to the present invention, the flow of refrigerant in the flat tube is made to flow freely in the direction perpendicular to the flow, and the shape of the strength member can be freely selected, resulting in a high-performance heat exchanger tube. It becomes possible to do so.

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

第1図は従来のフルゲートフィン熱交換器の一例を説明
する囚、第2図は第1図における偏平管の断面図、第3
図〜2@7図は本発明の熱交換器における偏平管の製造
方法を説明する図である、。 lO・・・偏平管、11・・・強度部材、12・・・中
子、13・・・中間部材。 第1図 方Z図 ■ 3  図 YJ4図
Figure 1 is a diagram explaining an example of a conventional full-gate fin heat exchanger, Figure 2 is a cross-sectional view of the flat tube in Figure 1, and Figure 3 is a cross-sectional view of the flat tube in Figure 1.
Figures 2 to 7 are diagrams illustrating the method for manufacturing flat tubes in the heat exchanger of the present invention. lO: Flat tube, 11: Strength member, 12: Core, 13: Intermediate member. Figure 1 Figure Z ■ 3 Figure YJ4 Figure

Claims (1)

【特許請求の範囲】[Claims] 1、強度部材によって内部K(l[数の冷媒要路を並列
に形成した偏平管を蛇行状にし、互いに平行する部分に
コルゲートフィンt−接合してなる熱交換器において、
前記偏平管は、管内に隣接する冷媒流路を連通する形状
O1]11部材と水溶性中子とからなる中間部材を配設
後管内壁と強度部材を仮着けし、中子を除去した後、管
内壁と強度部材を溶接して構成したことt−特徴とする
熱交換器。
1. In a heat exchanger made of flat tubes with internal K(l) parallel refrigerant channels formed in a meandering shape and corrugated fins T-joined to mutually parallel parts,
The flat tube has a shape in which adjacent refrigerant flow paths are connected to each other after arranging an intermediate member consisting of an O1]11 member and a water-soluble core, temporarily attaching a strength member to the inner wall of the tube, and removing the core. , A heat exchanger characterized in that it is constructed by welding an inner wall of a pipe and a strength member.
JP14624881A 1981-09-18 1981-09-18 Heat exchanger Pending JPS5849895A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14624881A JPS5849895A (en) 1981-09-18 1981-09-18 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14624881A JPS5849895A (en) 1981-09-18 1981-09-18 Heat exchanger

Publications (1)

Publication Number Publication Date
JPS5849895A true JPS5849895A (en) 1983-03-24

Family

ID=15403436

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14624881A Pending JPS5849895A (en) 1981-09-18 1981-09-18 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS5849895A (en)

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