JPS5932791A - Corrugated type heat exchanger - Google Patents

Corrugated type heat exchanger

Info

Publication number
JPS5932791A
JPS5932791A JP13986382A JP13986382A JPS5932791A JP S5932791 A JPS5932791 A JP S5932791A JP 13986382 A JP13986382 A JP 13986382A JP 13986382 A JP13986382 A JP 13986382A JP S5932791 A JPS5932791 A JP S5932791A
Authority
JP
Japan
Prior art keywords
corrugated
corrugated fins
flat tubes
heat exchanger
fins
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
JP13986382A
Other languages
Japanese (ja)
Inventor
Mizuho Yokoyama
瑞穂 横山
Hideo Ide
井出 英雄
Misao Suzuki
操 鈴木
Takeshi Uchida
内田 武士
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 JP13986382A priority Critical patent/JPS5932791A/en
Publication of JPS5932791A publication Critical patent/JPS5932791A/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
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/126Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element consisting of zig-zag shaped fins

Landscapes

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

Abstract

PURPOSE:To obtain the corrugated type heat exchanger with excellent heat- exchange performance by a method wherein corrugation forming grooves with the same pitch as that of corrugated fins are provided on the surface of flat tubes so as to realize uniform pitch intervals of the corrugated fins after being assembled and at the same time to keep the straight line portions of the corrugated fins precisely at right angle to the flat tubes. CONSTITUTION:The respective pitches of the corrugated fins 4 and 5 are surely kept at constant and at the same time the straight line portions of the corrugated fins 4 and 5 are allowed to take the direction at right angle to the flat tubes 3B-3D by matingly joining the trough and crest parts of the corrugation formed on the flat tubes 3B-3D with the crest and trough parts of the corrugated fins 4 and 5. In addition, the genration of turbulent flow in the coolant flowing within the flat tubes due to the corrugation brings the effect to improve the heat- exchange efficiency of the heat exchanger. Furthermore, because of the pitches of the corrugated fins 4 and 5 being kept at constant, the resistance of the air flow passing through corrugated fin portions is reduced and consequently the effect to contrive to save energy as a whole is developed.

Description

【発明の詳細な説明】 本発明は熱交換器に係り、特に、コルゲー ト型熱交換
器に好適な偏平管の形状に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat exchanger, and particularly to a flat tube shape suitable for a corrugated heat exchanger.

第1図及び第2図は従来この柚のコルゲート型熱交換器
の一例を示したものである。波型状に曲折した扁平管1
0間に、波型形状のコルゲートフィン2が多数配列され
ている。この偏平管1とコルゲートフィン2は溶接にて
接合し−Cある。
FIGS. 1 and 2 show an example of a conventional corrugated heat exchanger. Flat tube bent into a wave shape 1
A large number of wavy corrugated fins 2 are arranged between the two. The flat tube 1 and the corrugated fins 2 are joined by welding.

最近、省資源省エネルギ化が各界で叫ばれているが、上
記したコルゲート型熱交換器に於いても、熱交換性能の
効率化及びコンパクト化が大きな課題となっている。特
に、熱交換効率の向上に於い一コバ、コルゲートフィン
2のrlI己夕1jピッチが1に要l焚素となっている
Recently, there has been a call for resource and energy conservation in various fields, and even in the above-mentioned corrugated heat exchanger, increasing the efficiency of heat exchange performance and making it more compact have become major issues. Particularly, in improving the heat exchange efficiency, the pitch of the corrugated fins 2 is an essential element.

第3図(A)乃至(C)は従来のコルゲート型熱交換器
に於ける偏平管1の間に配列されたコルゲートフィン2
の配置状態を示したものである。
FIGS. 3(A) to 3(C) show corrugated fins 2 arranged between flat tubes 1 in a conventional corrugated heat exchanger.
This shows the arrangement of the .

第3図(A)に示す如く、本来コルゲートフィン2は偏
平管1に対して直線部が直角方向になるように配列され
なければならないのに拘らず、第2図(J3)に示す如
く山部及び谷部が滑らかなアール部で加工されたコルゲ
ートフィン2や、第3図(C)に示す如く山部及び谷部
の曲げアーノ棗・の小さなコルゲートフィン2の如く、
偏平管1に対し7直線部分が直角に位置せず、ブ頃いた
状態に1つ−C配設されてし−まりのが大部分であった
。これは、熱交換器組立時、両側からの締付は力が不平
衡なことと、コルゲートフィン2の形状不良や剛性の程
度などの多くの因子により傾いた状態に配設されてしま
うと考えられている。このように偏平管1にコルゲート
フィン2が傾いて配設された場合、偏平管10間隔が変
化すると共に、偏平管1とコルゲートフィン2の接合面
積が不均一となり、特に第3図(C)で7バした様な場
合は、コルケートフィン2の接合面積が大幅に減少する
ことにより、熱交換性能が低下する欠点があった。更に
、コルゲートフィン2に対応して配置されるルーバの間
隔が不均一となり、コルゲートフィン2を通過する抵抗
が大となりこれも熱交換性能を低下させていた。
As shown in Fig. 3 (A), although the corrugated fins 2 should originally be arranged so that the straight portions are perpendicular to the flat tube 1, they are arranged in a ridge as shown in Fig. 2 (J3). Such as the corrugated fin 2 whose rounded portions and troughs are smooth, and the small corrugated fin 2 whose crests and troughs are curved as shown in Fig. 3 (C).
In most cases, the seven straight sections were not located at right angles to the flat tube 1, but were arranged in a crooked manner. This is because when assembling the heat exchanger, tightening from both sides causes unbalanced forces, and the corrugated fins 2 are placed in an inclined position due to many factors such as poor shape and rigidity. It is being When the corrugated fins 2 are disposed on the flat tube 1 at an angle as described above, the interval between the flat tubes 10 changes and the joint area between the flat tube 1 and the corrugated fins 2 becomes uneven, especially as shown in FIG. 3(C). In such a case, the bonding area of the corrugated fins 2 is significantly reduced, resulting in a reduction in heat exchange performance. Furthermore, the spacing between the louvers arranged corresponding to the corrugated fins 2 becomes uneven, and the resistance of passing through the corrugated fins 2 becomes large, which also reduces the heat exchange performance.

本発明の目的は、上記の欠点を解消し、熱交換性能に優
Itたコルケート型熱交換器を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to eliminate the above-mentioned drawbacks and provide a corrugated heat exchanger with excellent heat exchange performance.

本発明は、コルゲート型熱交換器の偏平管の表面にコル
ゲートフィンのピッチと同じ凹凸溝を設け、コルゲー 
トフインの山側と谷側VC+izする前記偏平管の凹凸
が交互に位A”するようにして、組立後ノコルゲートフ
ィンのピッチ間隔を均一にすると共に、更に組立後の向
かい介″)偏平管の凹凸を凹に対して凸を、凸Vこ対し
て凹を正確に配+M’することにより、偏平管に対し、
コルケートツインの直線部分を正確に直角方向に保9こ
とにより、−に記目的を達成する。
The present invention provides corrugated grooves on the surface of the flat tubes of a corrugated heat exchanger with the same pitch as the corrugated fins.
The unevenness of the flat tube on the peak side and the valley side of the fins is made to be alternately A", so that the pitch interval of the corrugated fins is made uniform after assembly, and the unevenness of the flat tube is By accurately arranging the convex to the concave and the concave to the convex V, +M' to the flat tube,
By keeping the straight portions of the corrugated twin accurately at right angles, the purpose stated in - is achieved.

以下本発明の一実施例を図面Vこ3i1−って説iJJ
する。
An embodiment of the present invention will be described below with reference to the drawing V3i1-iJJ.
do.

第4図(A)乃至(C)は本発明のコルケ−ト型熱交換
器の一実施例の要部金示した説明図である。相対する偏
平管3A、、31)には各凹凸を向い合わせた状、つに
して耐直、シ、第3図(B)で小才ようにコルゲートフ
ィン4の山部と谷部を偏イ管3 J3と偏平管3Cの四
部と凸部に 合しで接合することによって配設している
。第3図(C)は偏平管3C,3Bに施す凹凸の形状を
角状とした例について示しである。この例では曲折部が
直角方向に折れ曲がっているコルゲートフィン5の山部
と谷部を偏平管3C,3Dの凸7S15と四部に 合し
て接合することにより配設している。
FIGS. 4(A) to 4(C) are explanatory diagrams showing essential parts of an embodiment of the corrugated heat exchanger of the present invention. The opposing flat tubes 3A, 31) are made with their concave and convex portions facing each other. It is arranged by joining the four parts and the convex part of pipe 3 J3 and flat pipe 3C together. FIG. 3(C) shows an example in which the irregularities formed on the flat tubes 3C and 3B are angular in shape. In this example, the crests and troughs of the corrugated fin 5, whose bent portions are bent at right angles, are arranged by aligning and joining the convex portions 7S15 of the flat tubes 3C and 3D.

このように本実施例では、偏平管3B、3Cの凹凸部に
コルゲートフィン4の山と谷を 合接合し、また、偏平
管3C,3Dの凹凸部にコルゲートフィン5の山と谷を
 合して接合することによす、コルゲートフィン4及び
コルゲートフィン5のピンチを一定確実に保つことが出
来、又コルゲートフィン4,5の直線部を偏平’1J3
B〜3Dに対し−Cik角方向に正確に保つことが出来
る。特に、第4図(C)で示す例では、偏平管3C,3
1)の表面の凹凸により、コルゲートフィンの偏平管に
対する接触面積が増大すると共に、溶接のフラックスの
溜19部となるため、接合溶接条件が良好になる。
In this way, in this embodiment, the peaks and valleys of the corrugated fins 4 are joined to the uneven parts of the flat tubes 3B and 3C, and the peaks and valleys of the corrugated fin 5 are joined to the uneven parts of the flat pipes 3C and 3D. By joining the corrugated fins 4 and 5, the pinch of the corrugated fins 4 and 5 can be maintained constant, and the straight parts of the corrugated fins 4 and 5 can be flattened.
It is possible to accurately maintain the -Cik angle direction with respect to B to 3D. In particular, in the example shown in FIG. 4(C), the flat tubes 3C, 3
The surface irregularities described in 1) increase the contact area of the corrugated fin with the flat tube and serve as a reservoir for welding flux, resulting in better joining welding conditions.

第6図は、第4図(A)及び(13)で示した如く、偏
平管3Bに凹凸を形成する方法例を示したものである。
FIG. 6 shows an example of a method for forming irregularities on the flat tube 3B as shown in FIGS. 4(A) and (13).

これは、コルケートフィン4のピッチと同じピッチの凹
凸を有するロール6A、6J3の狭隙部に偏平管3Bを
送って、圧延転写力11工することにより、均一の凹凸
部を有する偏平管3Bを高速に製造することが出来る。
This is achieved by feeding the flat tube 3B into the narrow gap between the rolls 6A and 6J3, which have unevenness with the same pitch as the pitch of the corrugated fins 4, and by applying a rolling transfer force of 11 times, the flat tube 3B having a uniform unevenness is created. can be manufactured at high speed.

第6図は第4図(C)で示した様な凹凸を偏平管に形成
する方法を示したものである。コルゲートフィン5のピ
ッチと同じ凹凸ピッチを有する金属板7A、7Bにより
偏平管3Dを挾み圧下することVCよって、偏平管3D
の表面に角状の凹凸を形成する。この方法は、特に凹凸
形状の各角部の半径の小さな形状のものを形成する場合
に正確に圧延出来るという特徴がある。
FIG. 6 shows a method of forming irregularities as shown in FIG. 4(C) on a flat tube. By sandwiching and compressing the flat tube 3D between metal plates 7A and 7B having the same unevenness pitch as the pitch of the corrugated fins 5, the flat tube 3D
forming angular irregularities on the surface. This method is characterized in that it can be rolled accurately, especially when forming an uneven shape with each corner having a small radius.

第7図(A)及び(B)は凹凸r施]〜た偏平管3B、
3D内を流れる熱交換用冷媒の状態を4くしたものであ
る。この様な凹凸のある偏平管3 B 。
FIGS. 7(A) and (B) show a flat tube 3B with unevenness.
The state of the heat exchange refrigerant flowing in 3D is multiplied by 4. Flat tube 3B with such unevenness.

3Dによれば、偏平管内面近傍金流扛る冷媒の一部に乱
流が発生し、熱交換性能金回」ニさせることが出来る。
According to 3D, turbulent flow occurs in a part of the refrigerant flowing around the inner surface of the flat tube, and the heat exchange performance can be improved.

なお、この乱流による熱交換性能の同上は、コルケート
フィンのピッチ全狭める場合の数倍となる。
Note that the heat exchange performance due to this turbulent flow is several times that of the case where the pitch of the corrugated fins is completely narrowed.

本実施例によれば、偏平管3A〜31〕に凹凸金形成し
、この凹凸部にコルゲートフィン4,5の山部と谷部を
 合接合することにより、コルゲートフイン4,5の各
ピッチ全一定確実に保持し得る効果があると共に、コル
ゲートフィン4,5の直線部を偏平管3B〜3DK対し
て直角方向となる。Lうにする効果があり、壕だ、偏平
な!内部を流れる冷媒に乱流が発生する事により、熱交
換効率を著しく向上させる効果かめる。壕だ、前述した
如く、コルゲートフィン4,5のピッチが一定となり、
コルゲートフィン4,5に対応し−C配置されるルーバ
の間隔も均一となるため、コルゲートフィン部を通過す
る空気流の抵抗を減少させ、送風効率を向上させること
ができるため、全体として熱交換器の省エネルギ化を図
る効果がある。
According to this embodiment, by forming uneven metal on the flat tubes 3A to 31 and joining the peaks and troughs of the corrugated fins 4 and 5 to the uneven parts, each pitch of the corrugated fins 4 and 5 is completely fixed. This has the effect of being able to be held constant and reliably, and the straight portions of the corrugated fins 4 and 5 are perpendicular to the flat tubes 3B to 3DK. It has the effect of making it look rough and flat! By creating turbulence in the refrigerant flowing inside, the heat exchange efficiency can be significantly improved. As mentioned above, the pitch of corrugated fins 4 and 5 is constant,
Since the spacing between the louvers arranged corresponding to the corrugated fins 4 and 5 is also uniform, the resistance of the air flow passing through the corrugated fins can be reduced and the air blowing efficiency can be improved, so that the overall heat exchange is improved. This has the effect of saving energy in the device.

以上目己述した如く本発明によれば熱交換性能に優れた
コルゲート型熱交換器を提供することができる。
As described above, according to the present invention, a corrugated heat exchanger with excellent heat exchange performance can be provided.

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

Claims (1)

【特許請求の範囲】[Claims] 1、冷媒を送流する偏平管を、曲折させて直線部が平行
に配列されるように形成し、これら偏平管の直線部に、
コルゲートフィンの直線部が前記偏平管の直線部と直角
方向になるようにコルゲートフィンを結合して配列し、
コルゲートフィン間に被冷却風を送風して熱交換を行な
うコルゲート型熱交換器において、互いに向き合う前記
偏平管の直線部にコルゲートフィンピッチと同じピッチ
の凹凸を形成し、この凹部と凸部にコルゲートフィンの
山部と谷部を 合溶涜し、偏平管とコルゲートフィンと
を結合することを特徴とするコルケート型熱交換器。
1. The flat tubes that flow the refrigerant are bent so that the straight parts are arranged in parallel, and the straight parts of these flat tubes are
The corrugated fins are combined and arranged so that the straight part of the corrugated fin is perpendicular to the straight part of the flat tube,
In a corrugated heat exchanger that performs heat exchange by blowing cooled air between corrugated fins, the straight portions of the flat tubes facing each other are formed with unevenness having the same pitch as the corrugated fin pitch, and the corrugated portions are formed in the concave and convex portions. A corrugated heat exchanger characterized by combining flat tubes and corrugated fins by merging the peaks and valleys of the fins.
JP13986382A 1982-08-13 1982-08-13 Corrugated type heat exchanger Pending JPS5932791A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13986382A JPS5932791A (en) 1982-08-13 1982-08-13 Corrugated type heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13986382A JPS5932791A (en) 1982-08-13 1982-08-13 Corrugated type heat exchanger

Publications (1)

Publication Number Publication Date
JPS5932791A true JPS5932791A (en) 1984-02-22

Family

ID=15255293

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13986382A Pending JPS5932791A (en) 1982-08-13 1982-08-13 Corrugated type heat exchanger

Country Status (1)

Country Link
JP (1) JPS5932791A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100955332B1 (en) * 2002-07-18 2010-04-30 한라공조주식회사 Plate of lamination-type heat exchanger, its manufacturing process
JP2013257096A (en) * 2012-06-13 2013-12-26 Sanden Corp Heat exchanger
EP2724106B1 (en) * 2011-06-24 2019-08-07 AIC Spólka Akcyjna Heat exchanger tube set

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100955332B1 (en) * 2002-07-18 2010-04-30 한라공조주식회사 Plate of lamination-type heat exchanger, its manufacturing process
EP2724106B1 (en) * 2011-06-24 2019-08-07 AIC Spólka Akcyjna Heat exchanger tube set
JP2013257096A (en) * 2012-06-13 2013-12-26 Sanden Corp Heat exchanger

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