JPH07127984A - Parallel flow type heat exchanger and its manufacturing method - Google Patents
Parallel flow type heat exchanger and its manufacturing methodInfo
- Publication number
- JPH07127984A JPH07127984A JP13694192A JP13694192A JPH07127984A JP H07127984 A JPH07127984 A JP H07127984A JP 13694192 A JP13694192 A JP 13694192A JP 13694192 A JP13694192 A JP 13694192A JP H07127984 A JPH07127984 A JP H07127984A
- Authority
- JP
- Japan
- Prior art keywords
- corrugated fins
- fins
- heat exchanger
- tubes
- fin
- 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.)
- Granted
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular 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
- F28F1/126—Tubular 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-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
- F28D1/02—Heat-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
- F28D1/04—Heat-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
- F28D1/053—Heat-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 straight
- F28D1/0535—Heat-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 straight the conduits having a non-circular cross-section
- F28D1/05366—Assemblies of conduits connected to common headers, e.g. core type radiators
- F28D1/05375—Assemblies of conduits connected to common headers, e.g. core type radiators with particular pattern of flow, e.g. change of flow direction
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Geometry (AREA)
- Automatic Assembly (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、複数積層されたチュー
ブの両端にヘッダタンクが設けられたパラレルフロー熱
交換器およびその製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a parallel flow heat exchanger in which header tanks are provided at both ends of a plurality of laminated tubes and a method for manufacturing the same.
【0002】[0002]
【従来の技術】パラレルフロータイプの熱交換器は、複
数のチューブが波状フィンを介して互いに平行に積層さ
れ、これらのチューブの両端にはヘッダタンクが連結さ
れている。ヘッダタンクには出入口パイプが設けられて
いるとともに必要なヘッダタンク内の箇所に仕切板が設
けられ、出入口パイプの間で複数のチューブを一まとま
りのパスとして複数回蛇行しながら熱交換媒体が通流さ
れる。2. Description of the Related Art In a parallel flow type heat exchanger, a plurality of tubes are laminated in parallel with each other via corrugated fins, and header tanks are connected to both ends of these tubes. The header tank is provided with an inlet / outlet pipe, and a partition plate is provided at a required location in the header tank.The heat exchange medium passes through the tubes while meandering a plurality of tubes multiple times as one unit path. Shed
【0003】また、パラレルフロータイプの熱交換器を
製造する場合には、チューブ、フィン、ヘッダタンク、
サイドプレート、および出口パイプ、入口パイプ等の各
部品はそれぞれ別個に製作される。例えば、チューブは
アルミ部材を押出し成形により形成され、所定長さに切
断されて形成される。波状フィンはアルミ合金により薄
板状に形成され、フォーミングギアにより所定の山数で
所定のピッチに成形される。ヘッダタンクはアルミ合金
部材をプレス成形により形成される。Further, when manufacturing a parallel flow type heat exchanger, tubes, fins, header tanks,
The side plate and each component such as the outlet pipe and the inlet pipe are manufactured separately. For example, the tube is formed by extruding an aluminum member and cut into a predetermined length. The wavy fins are formed of aluminum alloy into a thin plate shape, and are formed by a forming gear with a predetermined number of peaks and a predetermined pitch. The header tank is formed by pressing an aluminum alloy member.
【0004】そして、組立時には、例えば治具に所定数
のチューブおよびサイドプレートを幅方向に立てて整列
され、整列されたチューブ間に上方から波状フィンを押
入し、両側のサイドプレートに帯状の治具を装着して本
圧縮し、この状態でサイドプレートおよびチューブの両
端にヘッダタンクを挿入する。次に両端側のサイドプレ
ートを炉内治具によりクランプした状態で、フッ素系フ
ラックスを塗布して乾燥し、炉内で加熱により一体ろう
付けされ、冷却後治具を取外して熱交換器が得られる
(例えば、特開昭62−207572号、特開昭62−
78731号、特開平2−172637号)。At the time of assembly, for example, a predetermined number of tubes and side plates are aligned in a jig in the width direction, and wavy fins are pressed from above between the aligned tubes to form strip-shaped treatments on the side plates on both sides. Attach the tool and perform main compression, and insert the header tanks at both ends of the side plate and tube in this state. Next, while the side plates on both ends are clamped by the in-furnace jig, fluorine-based flux is applied and dried, and they are brazed together by heating in the furnace.After cooling, the jig is removed to obtain a heat exchanger. (For example, JP-A-62-207572 and JP-A-62-172).
78731, JP-A-2-172637).
【0005】[0005]
【発明が解決しようとする課題】しかしながら、上記従
来のパラレルフロータイプの熱交換器においては、図1
0に示すように、チューブ6間に介装される波状フィン
4の向きが同一の向きに挿入して組付けられていたの
で、加熱ろう付時に炉内治具により積層方向に僅かに加
圧して一体ろう付けすると、波状フィンの残留応力によ
り、図11に示すように、熱交換器1の正面形状が図中
の二点鎖線であるべきところが実線のようにゆがんでし
まい、双方の対角線AとBが大幅に異なってしまう不具
合を生ずる場合があった。However, in the above conventional parallel flow type heat exchanger, as shown in FIG.
As shown in 0, since the wavy fins 4 interposed between the tubes 6 were inserted and assembled in the same direction, a slight pressure was applied in the stacking direction by the jig in the furnace during the heating brazing. When integrally brazed, due to the residual stress of the wavy fins, as shown in FIG. 11, the front shape of the heat exchanger 1 is distorted like a solid line where the two-dot chain line in the figure is distorted, and both diagonal lines A In some cases, there was a problem that B and B were significantly different.
【0006】すなわち、波状フィンは一般に冷間圧延さ
れたロール材を一対のフィン成形ギアにより加工され、
フィン成形ギアにより山を中心とした左右の傾斜角を均
一にして成形されるが、フィン成形時の残留応力が特定
な方向に波状フィンに残留し、この残留応力がろう付け
時の構成部材の軟化に伴ってろう付け後に正面形状が変
形する場合があった。その結果、製品として外観が不良
となるばかりでなく、ブラケットとその取付け位置が大
幅にずれて取付け不良となったり、また、むりに取付け
るようとしてろう付け部に亀裂が生じ、気がつかずにそ
のまま取付けた場合は熱交換媒体の漏洩の原因ともなる
おそれがあった。That is, the wavy fin is generally formed by processing a cold-rolled roll material with a pair of fin forming gears.
The fin forming gear makes the left and right tilt angles centered on the mountain uniform, but the residual stress during fin forming remains in the wavy fin in a specific direction, and this residual stress of the component parts during brazing is used. The front shape may be deformed after brazing due to softening. As a result, not only the appearance of the product is bad, but also the bracket and its mounting position are significantly displaced, resulting in improper mounting. In this case, there is a risk that the heat exchange medium may leak.
【0007】そこで、本発明は、ろう付け後の正面形状
の変形を防止し、熱交換器の外観不良、ブラケットの取
付け位置ずれおよびろう付け部の亀裂の発生をなくした
熱交換器およびその製造方法を提供することを目的とし
ている。Therefore, the present invention prevents the deformation of the front shape after brazing, and eliminates the appearance of the heat exchanger, the displacement of the mounting position of the bracket, and the cracking of the brazing portion, and the manufacturing thereof. It is intended to provide a way.
【0008】[0008]
【課題を解決するための手段】第1請求項の熱交換器
は、互いに平行に整列されたチューブとこれら複数のチ
ューブの間に介装された波状フィンとが積層され、配列
された上記チューブの両端にヘッダタンクが連通接続さ
れたパラレルフロー熱交換器にあって、上記波状フィン
が、フィン成形移送方向に沿う通常の波状フィンと、こ
の通常の波状フィンに対し反転した反転の波状フィンと
により、規則的に配設された構成とされている。A heat exchanger according to a first aspect of the present invention is a tube in which tubes arranged in parallel with each other and corrugated fins interposed between these tubes are laminated and arranged. In a parallel flow heat exchanger in which header tanks are communicatively connected to both ends of the wavy fins, the wavy fins are normal wavy fins along the fin forming transfer direction, and wavy fins that are inverted with respect to the normal wavy fins. Therefore, it is arranged regularly.
【0009】第2請求項の熱交換器の製造方法は、所定
長に切断されたチューブと、成形ギヤにより成形され所
定の山数およびピッチに切断された波状フィンと、ヘッ
ダタンク等他の部材を移送し、自動組立機において複数
のチューブを整列させた後互いに隣り合うチューブ間に
上記波状フィンを介装し、チューブの両端に上記ヘッダ
タンクを組付け、炉内治具によりクランプして加熱によ
り一体ろう付けを行なうパラレルフロー熱交換器の製造
方法であって、上記チューブ間に波状のフィンを介装す
る際に、フィン成形移送方向に沿う通常の波状フィン
と、この通常の波状フィンに対し反転した反転の波状フ
ィンとを別個に上記自動組立機に移送し、双方の波状フ
ィンを規則的に配設する構成とされている。According to the second aspect of the method for manufacturing a heat exchanger, a tube cut into a predetermined length, a wavy fin formed by a forming gear and cut into a predetermined number of pitches and a predetermined pitch, and other members such as a header tank. After aligning a plurality of tubes in an automatic assembly machine, the corrugated fins are interposed between the tubes adjacent to each other, the header tanks are attached to both ends of the tubes, and the tubes are clamped and heated by a jig in the furnace. A method for manufacturing a parallel flow heat exchanger that integrally brazes by means of a method, wherein, when a corrugated fin is interposed between the tubes, a normal corrugated fin along a fin forming transfer direction and a normal corrugated fin are provided. On the other hand, the inverted wavy fins that have been inverted are transferred separately to the automatic assembly machine, and both wavy fins are regularly arranged.
【0010】[0010]
【作用】したがって、チューブ間には、フィン成形移送
方向に沿う通常の波状フィンと、この通常の波状フィン
に対し反転した反転の波状フィンとが規則的に、例え
ば、交互に配設されるので、波状フィンの成形加工時に
波状フィン自体に残留する応力が互いに相殺される向き
に配設されることになり、加熱による一体ろう付け時に
おける熱交換器の正面形状の変形を阻止する。その結
果、ブラケットとその取付け部の位置ずれを生ずること
がなくなり、無理に取付けることに伴うろう付け部の亀
裂やこの亀裂部からの熱交換媒体の漏洩をも防止でき
る。Therefore, between the tubes, the normal wavy fins along the fin forming transfer direction and the inverted wavy fins that are the reverse of the normal wavy fins are regularly and alternately arranged. The stresses remaining in the wavy fins during the forming process of the wavy fins are arranged so as to cancel each other out, and deformation of the front shape of the heat exchanger during integral brazing due to heating is prevented. As a result, the bracket and the mounting portion thereof are not displaced from each other, and it is possible to prevent cracks in the brazing portion and leakage of the heat exchange medium from the crack portion due to the excessive mounting.
【0011】[0011]
【実施例】以下に、本発明の一実施例を図面に基づいて
説明する。図1は本実施例の熱交換器(コンデンサ)1
を示しており、2は入側のヘッダタンク、3は出側のヘ
ッダタンクを示している。An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a heat exchanger (condenser) 1 of this embodiment.
2 shows an inlet side header tank and 3 shows an outlet side header tank.
【0012】双方のヘッダタンク2と3との間には波状
フィン4,5と交互にして互いに平行に積層された偏平
チューブ6が介装され、各偏平チューブ6の両端が双方
のヘッダタンク2,3に連通接続されている。各ヘッダ
タンク2,3の上下端はそれぞれ盲キャップ7により閉
塞され、積層された偏平チューブ6の上端側および下端
側には断面U字状のサイドプレート8が配設されてい
る。一方のヘッダタンク2には熱交換媒体の入口継手9
が取付けられ、他方のヘッダタンク3には出口継手10
が取付けられている。Between the two header tanks 2 and 3, there are interposed flat tubes 6 alternately stacked with the corrugated fins 4 and 5 in parallel with each other, and both ends of each flat tube 6 are located in both header tanks 2. , 3 are connected for communication. The upper and lower ends of the header tanks 2 and 3 are closed by blind caps 7, and side plates 8 having a U-shaped cross section are arranged on the upper end side and the lower end side of the laminated flat tubes 6. One header tank 2 has a heat exchange medium inlet joint 9
Is attached to the other header tank 3 and the outlet joint 10
Is installed.
【0013】また、入口継手9と出口継手10との間
で、熱交換媒体が一まとまりの複数の偏平チューブ6を
通じて複数回通流方向を反転して通流されるように、双
方のヘッダタンク2,3内には仕切板11が設けられて
いる。本実施例では、熱交換媒体が4回反転する5パス
となるように仕切板11が設けられている。Further, between the inlet joint 9 and the outlet joint 10, the header tanks 2 of both sides are arranged so that the heat exchange medium flows through the plurality of flat tubes 6 which are gathered together by reversing the flowing direction a plurality of times. A partition plate 11 is provided in each of the three. In this embodiment, the partition plate 11 is provided so that the heat exchange medium has five passes in which it is inverted four times.
【0014】更に、本実施例の熱交換器1では、サイド
プレート8と偏平チューブ6の間や偏平チューブ6間に
設けられる波状フィン4,5が互いに残留応力を相殺す
る向きに配設されている。すなわち、図2に示すよう
に、偏平チューブ6を介して互いに隣り合う波状フィン
4,5の向きを、波状フィン4,5の山と山、谷と谷と
が正面から見て上下方向に重なり合うよう、線xに対し
対称的に配設されている。また、このような波状フィン
4,5の組付けは、図3に示すように、本実施例では、
後述するフィン成形ギア17から送り出された所定長に
切断して形成されたそのままの向きの通常の波状フィン
4と、同様に成形された波状フィン4を横方向に180
度回転した向きの反転の波状フィン5とを交互に規則的
に配設した構成となっている。Further, in the heat exchanger 1 of the present embodiment, the corrugated fins 4 and 5 provided between the side plate 8 and the flat tubes 6 and between the flat tubes 6 are arranged so as to cancel the residual stress with each other. There is. That is, as shown in FIG. 2, the direction of the wavy fins 4 and 5 adjacent to each other via the flat tube 6 is such that the peaks and crests and the troughs and valleys of the wavy fins 4 and 5 overlap in the vertical direction when viewed from the front. Thus, they are arranged symmetrically with respect to the line x. Further, as shown in FIG. 3, the assembling of the wavy fins 4 and 5 is performed in the present embodiment.
A normal wavy fin 4 which is formed by cutting it to a predetermined length and is sent out from a fin forming gear 17, which will be described later, and a wavy fin 4 which is similarly formed are laterally moved 180 degrees.
It has a configuration in which wavy fins 5 each having an inverted direction of rotation are alternately arranged regularly.
【0015】次に上記構成の熱交換器1を自動化により
製造する場合について説明する。Next, a case where the heat exchanger 1 having the above structure is manufactured by automation will be described.
【0016】上記偏平チューブ6は、アルミ材を押出し
成形により内部流路を有する偏平状に形成され、ロール
に巻かれている。そして、所定長の偏平チューブ6を得
るには、図4に示すように、偏平チューブ材13をロー
ル12から引出してカッタ14により所定長に切断し、
このようにして形成された所定長の偏平チューブ6が移
送される。The flat tube 6 is formed into a flat shape having an internal flow path by extruding an aluminum material and wound around a roll. Then, in order to obtain the flat tube 6 of a predetermined length, as shown in FIG. 4, the flat tube material 13 is pulled out from the roll 12 and cut into a predetermined length by a cutter 14,
The flat tube 6 having a predetermined length thus formed is transferred.
【0017】また、上記サイドプレート8も所定長に切
断され、プレス加工により横断面U字状に成形されて移
送される。Further, the side plate 8 is also cut into a predetermined length, is pressed into a U-shaped cross section, and is transferred.
【0018】上記波状フィン4,5は、図5に示すよう
に、ロール15に巻かれた素材16を引出してフォーミ
ング工程の一対の成形ギア17により所定形状の波状に
成形される。成形された素材16は、所定の波数やピッ
チを揃えてカッティグ工程の刃18により切断され、所
定波数で所定ピッチの波状フィン4が得られる。このよ
うにして得られた波状フィン4は移送され、反転部19
において、成形時のまま搬送される通常の波状フィン4
と、これを横向きに180度横転させた反転の波状フィ
ン5とに分けて移送される。したがって、通常の波状フ
ィン4と反転の波状フィン5とは互いに天地が逆の向き
となる。As shown in FIG. 5, the corrugated fins 4 and 5 are formed into a corrugated shape having a predetermined shape by pulling out the material 16 wound on a roll 15 and using a pair of molding gears 17 in the forming process. The formed material 16 is cut with a blade 18 in a cutting process with a predetermined wave number and a uniform pitch, and the wavy fins 4 having a predetermined pitch and a predetermined wave number are obtained. The wavy fins 4 thus obtained are transferred to the reversing unit 19
In the normal wavy fin 4 which is conveyed at the time of molding
And the inverted wavy fins 5 which are laterally turned 180 degrees and transferred. Therefore, the normal wavy fins 4 and the inverted wavy fins 5 are turned upside down.
【0019】また、ヘッダタンク2,3、盲キャップ
7、入口継手9、出口継手10、仕切板11もそれぞれ
成形されて移送される。尚、ヘッダタンク2,3として
は、本実施例では、図6に示すように、径方向に二分割
されるタンクプレート21とエンドプレート22とから
なるヘッダタンク2,3を用いている。尚、図6中、2
3はチューブ挿入孔を示す。The header tanks 2 and 3, the blind cap 7, the inlet joint 9, the outlet joint 10, and the partition plate 11 are also molded and transferred. As the header tanks 2 and 3, in the present embodiment, as shown in FIG. 6, the header tanks 2 and 3 including a tank plate 21 and an end plate 22 which are divided into two in the radial direction are used. Incidentally, in FIG. 6, 2
Reference numeral 3 indicates a tube insertion hole.
【0020】そして、各部材は熱交換器1の自動組立機
に送給される。組立機においては、まず、複数の偏平チ
ューブ6と両側のサイドプレート8とが幅方向を上下に
して整列され、これらの間に上記波状フィン4,5が順
次挿入される。この場合、上述した通常の波状フィン4
と反転した波状フィン5とが規則的に、例えば交互に配
設される。その後、整列した偏平チューブ6の両端にヘ
ッダタンク2,3のタンクプレート21の挿入孔23が
挿入され、タンクプレート21にヘッダタンク2,3の
エンドプレート22が装着され、ヘッダタンク2,3に
盲キャップ7が装着され、炉内治具によりクランプされ
る。Then, each member is fed to the automatic assembly machine of the heat exchanger 1. In the assembling machine, first, the plurality of flat tubes 6 and the side plates 8 on both sides are aligned with the width direction vertically, and the wavy fins 4 and 5 are sequentially inserted between them. In this case, the normal wavy fin 4 described above
And the inverted wavy fins 5 are regularly arranged, for example, alternately. After that, the insertion holes 23 of the tank plates 21 of the header tanks 2 and 3 are inserted into both ends of the aligned flat tubes 6, the end plates 22 of the header tanks 2 and 3 are attached to the tank plate 21, and the header tanks 2 and 3 are attached. The blind cap 7 is attached and clamped by the jig in the furnace.
【0021】炉内治具によりクランプされた組付け後の
熱交換器1は、フッ素系フラックスを塗布し、乾燥させ
た後、所定時間加熱され冷却して炉内治具を取外して得
られる。その後、出入口パイプ9,10をヘッダタンク
2,3にトーチろう付け等により取付けられる。The assembled heat exchanger 1 clamped by the in-furnace jig is obtained by removing the in-furnace jig by applying a fluorine-based flux, drying it, and then heating and cooling for a predetermined time. After that, the inlet and outlet pipes 9 and 10 are attached to the header tanks 2 and 3 by torch brazing or the like.
【0022】このように、本実施例では、整列された偏
平チューブ間に通常の波状フィンと反転した波状フィン
とを交互に配設したことにより、波状に成形するフォー
ミングの際に、波状フィン自体に残留する応力が互いに
相殺する向きに配設されるので、加熱によりろう付けさ
れる際に、従来のような波状フィンの残留応力が一方向
に作用して熱交換器の正面形状がゆがんでしまうことが
なくなり、製品の外観性を確保することができる。その
結果、熱交換器のブラケットとその取付け部との位置ず
れも生ずることがなくなり、無理に取付ける必要もない
のでろう付け部の亀裂を生ずることがなく、亀裂からの
熱交換媒体の漏洩がなくなる。As described above, in this embodiment, the normal wavy fins and the inverted wavy fins are alternately arranged between the aligned flat tubes, so that the wavy fins themselves can be formed during the wavy forming. Since the residual stresses in the heat exchanger are arranged so as to cancel each other out, when the brazing is performed by heating, the residual stress of the wavy fin acts in one direction and the front shape of the heat exchanger is distorted. Therefore, the appearance of the product can be secured. As a result, the bracket of the heat exchanger and the mounting portion will not be displaced, and since it is not necessary to forcibly mount it, cracks will not occur in the brazing portion, and leakage of the heat exchange medium from the cracks will be eliminated. .
【0023】尚、本実施例では、図3に示すように、反
転の波状フィン5を通常の波状フィン4に対し180度
横転させたが、これに限られない。例えば、図7に示す
ように、通常の波状フィン4の移送方向端mを基軸にし
て、天地と前後端を反転させるようにしてもよい。ま
た、図8に示すように、天地をそのままの状態で線nを
中心にして前後端a,bを入れ換えるようにしてもよ
い。In the present embodiment, as shown in FIG. 3, the inverted wavy fins 5 are laterally rotated 180 degrees with respect to the normal wavy fins 4, but the invention is not limited to this. For example, as shown in FIG. 7, the vertical direction and the front and rear ends may be inverted with the transfer direction end m of the normal wavy fin 4 as the base axis. Further, as shown in FIG. 8, the front and rear ends a and b may be interchanged with the top and bottom as it is with the line n as the center.
【0024】更に、本実施例では、通常の波状フィン4
と反転した波状フィン5とを互いに隣接して交互に配設
したが、これに限られない。例えば、図9に示すよう
に、互いに同数の通常波状フィン4と反転波状フィン5
とをそれぞれ複数組毎にセットして線xに対し対称的に
配設してもよく、種々組合せた配設形態にしてもよい。Further, in this embodiment, the normal wavy fin 4 is used.
And the inverted wavy fins 5 are alternately arranged adjacent to each other, the present invention is not limited to this. For example, as shown in FIG. 9, the same number of normal wavy fins 4 and inverted wavy fins 5 are provided.
And may be set in a plurality of sets, and they may be arranged symmetrically with respect to the line x, or may be arranged in various combinations.
【0025】表1は、各種熱交換器におけるろう付け後
の変形を実測したものの集計表で、上記通常の波状フィ
ン4および反転した波状フィン5の配設比率を異ならし
め、更にフィンの数を違えたときの、ろう付け後の変形
を実測し表にしたものである。通常および反転のフィン
配設比率は「1:1」「1:2」「1:3」「1:4」
の4種類、フィンの数は15から50迄の5個間隔で、
図11に示すAとBの差異を、2mm未満が○印、2〜4
mmが△印、4mmを超えるものが×印として記載されてい
る。尚、フィンの配設は、通常および反転を交互にした
もの、通常および反転を2個づつ、3個づつ、4個づつ
を各々1組としてこれらの各組を各別に交互に配置した
もの、上半分を通常とし下半分を反転としたものの各種
で行ない、これらの数値(AとBの差異)の単純平均値
を採用した。Table 1 is a tabulation table of actually measured deformation after brazing in various heat exchangers, in which the arrangement ratios of the normal wavy fins 4 and the inverted wavy fins 5 are made different, and the number of fins is further changed. This is a table in which the deformations after brazing when measured incorrectly are measured. Normal and inverted fin arrangement ratios are "1: 1""1:2""1:3""1:4"
, The number of fins is from 15 to 50 with 5 intervals,
The difference between A and B shown in FIG.
A mark with mm of Δ and a mark of more than 4 mm is described as X. The arrangement of the fins is such that the normal and the reverse are alternately arranged, the normal and the reverse are two, three, and four, and each of these sets is alternately arranged. The upper half was set to be normal and the lower half was made to be inverted, and various measurements were performed, and a simple average value of these numerical values (difference between A and B) was adopted.
【0026】これによると、フィンの配設比率が「1:
1」の場合はフィンの個数に関係なく良好な結果が得ら
れ、またフィンの配設比率が「1:2」の場合がこれに
つぎ、フィン配設比率が異なるにしたがい、更にその場
合フィンの個数が多くなるにしたがい、変形が大きくな
る結果が得られた。According to this, the fin arrangement ratio is "1:".
In the case of "1", good results are obtained regardless of the number of fins, and when the fin arrangement ratio is "1: 2", the fin arrangement ratio is different. It was found that the deformation increased with the increase in the number of.
【0027】[0027]
【表1】 [Table 1]
【0028】[0028]
【発明の効果】以上説明したように、本発明によれば、
積層される複数のチューブ間に、フィン成形移送方向に
沿う通常の波状フィンと、この通常の波状フィンに対し
反転した反転の波状フィンとを規則的に配設したので、
波状フィンの成形加工時に波状フィン自体に残留した残
留応力が互いに相殺されることになり、加熱による一体
ろう付け時に残留応力が一方向に作用して熱交換器の正
面形状が変形する事態を阻止することができる。その結
果、ブラケットとその取付け部との位置ずれも生ずるこ
とがなくなり、取付け作業が容易化されるとともに、従
来無理に取付けることに伴うろう付け部の亀裂やこの亀
裂からの熱交換媒体の漏洩を防止することができる。As described above, according to the present invention,
Since a regular wavy fin along the fin forming transfer direction and an inverted wavy fin that is inverted with respect to this normal wavy fin are regularly arranged between a plurality of laminated tubes,
Residual stresses remaining in the wavy fins during the forming process of the wavy fins cancel each other out, preventing the residual stress from acting in one direction during integral brazing due to heating and deforming the front shape of the heat exchanger. can do. As a result, there will be no positional deviation between the bracket and its mounting part, and the mounting work will be facilitated. Also, cracks in the brazing part and leakage of the heat exchange medium from this crack will occur as a result of forcibly mounting the bracket. Can be prevented.
【図1】本発明の実施例に係り、熱交換器の正面図であ
る。FIG. 1 is a front view of a heat exchanger according to an embodiment of the present invention.
【図2】波状フィンの配設状態を示す拡大正面図であ
る。FIG. 2 is an enlarged front view showing a disposition state of wavy fins.
【図3】波状フィンの反転を示す説明図である。FIG. 3 is an explanatory diagram showing the reversal of the wavy fins.
【図4】チューブの成形を説明する説明図である。FIG. 4 is an explanatory diagram illustrating the molding of a tube.
【図5】波状フィンの成形を説明する説明図である。FIG. 5 is an explanatory view illustrating the forming of a wavy fin.
【図6】ヘッダタンクを示す、図1中のVI−VI矢視
断面図である。FIG. 6 is a cross-sectional view taken along the line VI-VI in FIG. 1, showing a header tank.
【図7】本発明の他の実施例に係り、波状フィンの反転
方法を説明する説明図である。FIG. 7 is an explanatory diagram illustrating a method of reversing a wavy fin according to another embodiment of the present invention.
【図8】本発明の他の実施例に係り、波状フィンの反転
方法を説明する説明図である。FIG. 8 is an explanatory diagram illustrating a method of reversing a wavy fin according to another embodiment of the present invention.
【図9】本発明の波状フィンの配設方向の他の実施例を
示す拡大正面図である。FIG. 9 is an enlarged front view showing another embodiment of the arrangement direction of the wavy fins of the present invention.
【図10】従来例に係り、波状フィンの配設状況を説明
する要部の正面図である。FIG. 10 is a front view of a main portion for explaining a disposition state of wavy fins according to a conventional example.
【図11】熱交換器の概略正面図である。FIG. 11 is a schematic front view of a heat exchanger.
1 熱交換器 2,3 ヘッダタンク 4 通常の波状フィン 5 反転した波状フィン 6 チューブ 1 heat exchanger 2, 3 header tank 4 normal wavy fins 5 inverted wavy fins 6 tube
─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成4年6月2日[Submission date] June 2, 1992
【手続補正1】[Procedure Amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0019[Correction target item name] 0019
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0019】また、ヘッダタンク2,3、盲キャップ
7、入口継手9、出口継手10、仕切板11もそれぞれ
成形されて移送される。尚、ヘッダタンク2,3として
は、本実施例では、図6に示すように、径方向に二分割
されるエンドプレート21とタンクプレート22とから
なるヘッダタンク2,3を用いている。尚、図6中、2
3はチューブ挿入孔を示す。The header tanks 2 and 3, the blind cap 7, the inlet joint 9, the outlet joint 10, and the partition plate 11 are also molded and transferred. As the header tanks 2 and 3, in the present embodiment, as shown in FIG. 6, the header tanks 2 and 3 including the end plate 21 and the tank plate 22 which are divided into two in the radial direction are used. Incidentally, in FIG. 6, 2
Reference numeral 3 indicates a tube insertion hole.
【手続補正2】[Procedure Amendment 2]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0020[Correction target item name] 0020
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0020】そして、各部材は熱交換器1の自動組立機
に送給される、組立機においては、まず、複数の偏平チ
ューブ6と両側のサイドプレート8とが幅方向を上下に
して整列され、これらの間に上記波状フィン4,5が順
次挿入される。この場合、上述した通常の波状フィン4
と反転した波状フィン5とが規則的に、例えば交互に配
設される。その後、整列した偏平チューブ6の両端にヘ
ッダタンク2,3のエンドプレート21の挿入孔23が
挿入され、エンドプレート21にヘッダタンク2,3の
タンクプレート22が装着され、ヘッダタンク2,3に
盲キャップ7が装着され、炉内治具によりクランプされ
る。Then, each member is fed to the automatic assembling machine of the heat exchanger 1. In the assembling machine, first, the plurality of flat tubes 6 and the side plates 8 on both sides are aligned vertically in the width direction. The corrugated fins 4 and 5 are sequentially inserted between them. In this case, the normal wavy fin 4 described above
And the inverted wavy fins 5 are regularly arranged, for example, alternately. After that, the insertion holes 23 of the end plates 21 of the header tanks 2 and 3 are inserted into both ends of the aligned flat tubes 6, the tank plates 22 of the header tanks 2 and 3 are attached to the end plates 21, and the header tanks 2 and 3 are attached. The blind cap 7 is attached and clamped by the jig in the furnace.
【手続補正3】[Procedure 3]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0022[Name of item to be corrected] 0022
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0022】このように、本実施例では、整列された偏
平チューブ間に通常の波状フィンと反転した波状フィン
とを交互に配設したことにより、波状に成形するフォー
ミングの際に、波状フィン自体に残留する応力が互いに
相殺する向きに配設されるので、加熱によりろう付けさ
れる際に、従来のような波状フィンの残留応力が一方向
に作用して熱交換器の正面形状がゆがんでしまうことが
なくなり、製品の外観性を確保することができる。その
結果、熱交換器のブラケットとその取付け部との位置ず
れも生ずることがなくなり、無理に取付ける必要もない
のでろう付け部の亀裂を生ずることがなく、亀裂からの
熱交換媒体の漏洩がなくなる。また、波状フィンのフォ
ーミング成形に起因して、正面側から見たとき波状フィ
ンの前側高さと後側高さとの不一致を生じることがある
が、この場合、波状フィンをそのまま重ねる従来の配設
態様を行なうと、複数の波状フィンによって前後高さの
差が累積的に加算され、熱交換器は前側或いは後側へ傾
いてしまうことになる。その点本実施例によれば、偏平
チューブ間に通常の波状フィンと反転した波状フィンと
が交互に配設されるので、波状フィンの前後の高さの差
は相殺されて、かような不具合を回避することができ
る。As described above, in this embodiment, the normal wavy fins and the inverted wavy fins are alternately arranged between the aligned flat tubes, so that the wavy fins themselves are formed at the time of forming for forming the wavy shape. Since the residual stresses in the heat exchanger are arranged so as to cancel each other out, when the brazing is performed by heating, the residual stress of the wavy fin acts in one direction and the front shape of the heat exchanger is distorted. Therefore, the appearance of the product can be secured. As a result, the bracket of the heat exchanger and the mounting portion will not be displaced, and since it is not necessary to forcibly mount it, cracks will not occur in the brazing portion, and leakage of the heat exchange medium from the cracks will be eliminated. . Further, due to the forming forming of the wavy fins, the front height and the rear height of the wavy fins may not match when viewed from the front side. In this case, the conventional arrangement mode in which the wavy fins are stacked as they are When this is done, the difference in height between the front and rear is cumulatively added by the plurality of wavy fins, and the heat exchanger is inclined to the front side or the rear side. In that respect, according to the present embodiment, since the normal wavy fins and the inverted wavy fins are alternately arranged between the flat tubes, the height difference between the front and the back of the wavy fins is offset, which causes such a problem. Can be avoided.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 梅原 孝文 群馬県邑楽郡邑楽町篠塚2873−1 東洋冷 熱工業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Takafumi Umehara 2873-1, Shinozuka, Ura-cho, Euraku-gun, Gunma Toyo Cold Energy Co., Ltd.
Claims (2)
ら複数のチューブの間に介装された波状フィンとが積層
され、配列された前記チューブの両端にヘッダタンクが
連通接続されたパラレルフロー熱交換器において、前記
波状フィンが、フィン成形移送方向に沿う通常の波状フ
ィンと、この通常の波状フィンに対し反転した反転の波
状フィンとにより、規則的に配設されていることを特徴
とするパラレルフロー熱交換器。1. A parallel flow heat exchange system in which tubes arranged in parallel with each other and corrugated fins interposed between the tubes are stacked, and header tanks are connected in communication with both ends of the arranged tubes. In the container, the corrugated fins are regularly arranged by a normal corrugated fin along the fin forming transfer direction and an inverted corrugated fin that is the reverse of the normal corrugated fin. Flow heat exchanger.
ヤにより成形され所定の山数およびピッチに切断された
波状フィンと、ヘッダタンク等他の部材を移送し、自動
組立機において複数のチューブを整列させた後互いに隣
り合うチューブ間に前記波状フィンを介装し、チューブ
の両端に前記ヘッダタンクを組付け、炉内治具によりク
ランプして加熱により一体ろう付けを行なうパラレルフ
ロー熱交換器の製造方法において、前記チューブ間に波
状のフィンを介装する際に、フィン成形移送方向に沿う
通常の波状フィンと、この通常の波状フィンに対し反転
した反転の波状フィンとを別個に前記自動組立機に移送
し、双方の波状フィンを規則的に配設することを特徴と
するパラレルフロー熱交換器の製造方法。2. A tube cut into a predetermined length, a corrugated fin formed by a molding gear and cut into a predetermined number of ridges and a pitch, and other members such as a header tank are transferred to a plurality of tubes in an automatic assembly machine. Parallel flow heat exchanger in which the corrugated fins are interposed between adjacent tubes, the header tanks are attached to both ends of the tubes, and clamped by a jig in the furnace for integral brazing by heating. In the manufacturing method of (1), when the corrugated fins are interposed between the tubes, the normal corrugated fins along the fin forming transfer direction and the reversed corrugated fins inverted with respect to the normal corrugated fins are separately and automatically A method for manufacturing a parallel flow heat exchanger, which comprises transferring to an assembling machine and regularly disposing both wavy fins.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP04136941A JP3131499B2 (en) | 1992-05-28 | 1992-05-28 | Parallel flow heat exchanger and method of manufacturing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP04136941A JP3131499B2 (en) | 1992-05-28 | 1992-05-28 | Parallel flow heat exchanger and method of manufacturing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07127984A true JPH07127984A (en) | 1995-05-19 |
JP3131499B2 JP3131499B2 (en) | 2001-01-31 |
Family
ID=15187117
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---|---|---|---|
JP04136941A Expired - Fee Related JP3131499B2 (en) | 1992-05-28 | 1992-05-28 | Parallel flow heat exchanger and method of manufacturing the same |
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JP (1) | JP3131499B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101527191B1 (en) * | 2015-02-17 | 2015-06-09 | 그린테크주식회사 | Manufacturing method of heat exchanger |
-
1992
- 1992-05-28 JP JP04136941A patent/JP3131499B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101527191B1 (en) * | 2015-02-17 | 2015-06-09 | 그린테크주식회사 | Manufacturing method of heat exchanger |
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JP3131499B2 (en) | 2001-01-31 |
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