JPS6234150Y2 - - Google Patents

Info

Publication number
JPS6234150Y2
JPS6234150Y2 JP1982091465U JP9146582U JPS6234150Y2 JP S6234150 Y2 JPS6234150 Y2 JP S6234150Y2 JP 1982091465 U JP1982091465 U JP 1982091465U JP 9146582 U JP9146582 U JP 9146582U JP S6234150 Y2 JPS6234150 Y2 JP S6234150Y2
Authority
JP
Japan
Prior art keywords
needle
corrugated
fins
fin
heat exchanger
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
JP1982091465U
Other languages
Japanese (ja)
Other versions
JPS58194384U (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 JP9146582U priority Critical patent/JPS58194384U/en
Priority to DE8383730057T priority patent/DE3377666D1/en
Priority to AU15994/83A priority patent/AU1599483A/en
Priority to EP19830730057 priority patent/EP0097612B1/en
Priority to CA000430892A priority patent/CA1230872A/en
Publication of JPS58194384U publication Critical patent/JPS58194384U/en
Priority to KR2019860006841U priority patent/KR870001425Y1/en
Application granted granted Critical
Publication of JPS6234150Y2 publication Critical patent/JPS6234150Y2/ja
Granted legal-status Critical Current

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Description

【考案の詳細な説明】 本考案は針状フインを具えた熱交換器に関し、
フイン側の圧力損失の低減および流速の均一化に
よる伝熱性能の向上を企図したものである。
[Detailed description of the invention] The present invention relates to a heat exchanger equipped with needle-like fins.
This is intended to improve heat transfer performance by reducing pressure loss on the fin side and making the flow velocity uniform.

従来から熱交換器の伝熱性能の向上をはかるた
め伝熱管に種々のフインを接合することが行なわ
れており、その形状等も種々提案されている。例
えば、本願考案者らが提案した針状フインを具え
た熱交換器(実願昭56−111005号、実願昭57−
1714号)にあつてはカーエアコンや住宅用エアコ
ン等の各種空調機の熱交換器として伝熱性能が優
れたものであり、その構造は、第1図〜第3図に
示すように、伝熱管として内部に隔壁1aを有す
る押出偏平管1が用いられ、その偏平面1bが互
いに間隔をおいて対向すると共に平行に配置さ
れ、この偏平面1bで形成される間隔内に帯状金
属薄板でコルゲート成形された針状フイン群2が
偏平管1の長手方向と直交して接合されている。
そして、偏平管1の両端部のユニオン3を介して
熱交換媒体が管内に送給され、管外では、偏平管
1の長手方向と直交する方向、すなわち針状フイ
ン群2のコルゲート成形された直線部に沿う方向
から空気等が流入して熱交換が行なわれる。
Conventionally, various types of fins have been joined to heat exchanger tubes in order to improve the heat transfer performance of heat exchangers, and various shapes of the fins have been proposed. For example, the heat exchanger equipped with needle-like fins proposed by the inventors of the present application (Utility Application No. 111005, 1983, Utility Application No. 111005, 1982)
No. 1714) has excellent heat transfer performance as a heat exchanger for various air conditioners such as car air conditioners and residential air conditioners, and its structure is as shown in Figures 1 to 3. An extruded flat tube 1 having a partition wall 1a inside is used as a heat tube.The flat surfaces 1b of the extruded flat tube 1 are arranged parallel to each other at intervals, and corrugated metal strips are formed within the interval formed by the flat surfaces 1b. A group of shaped needle-like fins 2 are joined perpendicularly to the longitudinal direction of the flat tube 1.
Then, the heat exchange medium is fed into the tube through the unions 3 at both ends of the flat tube 1, and outside the tube, the corrugate molding of the needle-like fin groups 2 is carried out in a direction perpendicular to the longitudinal direction of the flat tube 1. Air and the like flow in from the direction along the straight portion to perform heat exchange.

この針状フイン群2は帯状金属薄板(板幅h)
の幅方向両端部2aをわずかに残して多数の矩形
の打抜部2bを形成して梯子状にし、これを長手
方向に沿つて蛇行幅wとして蛇行させてコルゲー
ト成形したものであり、その幅方向両端をあらか
じめ偏平面1bに塗布したろう材や接着剤でろう
付けしたり接着して接合してある。こうして接合
された針状フイン2cを多数有する針状フイン群
2の配列は空気4の流れ方向と平行なフインピツ
チがPL、空気4の流れ方向と直角なフインピツ
チがPTとなつている。
This needle-like fin group 2 is a strip-shaped metal thin plate (plate width h)
A large number of rectangular punched parts 2b are formed leaving only a small part of both ends 2a in the width direction to form a ladder shape, and this is corrugated by meandering along the longitudinal direction with a meandering width w. Both ends in the direction are joined by brazing or gluing using a brazing material or adhesive applied to the flat surface 1b in advance. In the arrangement of the needle-like fin group 2 having a large number of needle-like fins 2c joined in this manner, the fin pitch parallel to the flow direction of the air 4 is P L and the fin pitch perpendicular to the flow direction of the air 4 is P T .

ところが、かような針状フイン2cを具えた熱
交換器では、針状フイン群2への空気4の流入は
コルゲート成形の彎曲部、すなわち頂部および底
部から行なわれると共に空気の流出も同様に彎曲
部で行なわれることから空気4の流入、流出に大
きな障害となり、空気4のコルゲート成形の彎曲
部での流速ベクトル4aは小さく、直線部での流
速ベクトル4bは大きくなる。このため、熱交換
器の入力側と出口側との圧力損失が大きくなると
共に流速の不均一による熱伝達率の低下を招き伝
熱性能が低下する欠点がある。
However, in a heat exchanger equipped with such needle-like fins 2c, the air 4 flows into the needle-like fin group 2 from the curved parts of the corrugated molding, that is, from the top and bottom, and the air also flows out from the curved parts. This creates a major obstacle to the inflow and outflow of the air 4, and the flow velocity vector 4a of the air 4 at the curved part of the corrugated molding is small, and the flow velocity vector 4b of the air 4 at the straight part becomes large. For this reason, the pressure loss between the input side and the outlet side of the heat exchanger increases, and the heat transfer coefficient decreases due to non-uniform flow velocity, resulting in a decrease in heat transfer performance.

本考案はかかる従来の欠点を解消し、圧力損失
が小さく伝熱性能の高い熱交換器の提供を目的と
する。かかる目的を達成する本考案の構成は、内
部に熱交換媒体を通過させる偏平管の偏平面が互
いに間隔をおいて平行対向配置され、相対向した
偏平面間に針状フインがフイン帯の幅方向に配置
された針状コルゲートフイン帯を針状フインの長
さ方向が該偏平面に直交するとともにコルゲート
波高方向がほぼ空気の流れ方向となるように配
設・接合してなる熱交換器において、前記コルゲ
ートフインを、帯状金属板の幅方向両端部を残し
コルゲート成形の彎曲部に対応する部分を打抜く
と共にコルゲート成形の直線部に対応する部分に
多数のスリツトを打ち抜いた梯子状の針状フイン
群としたことを特徴とする。
The present invention aims to eliminate such conventional drawbacks and provide a heat exchanger with low pressure loss and high heat transfer performance. The structure of the present invention that achieves this object is such that the flat surfaces of the flat tube through which the heat exchange medium is passed are arranged parallel to each other at intervals, and the needle-like fins are arranged between the opposite flat surfaces so that the width of the fin band is equal to the width of the fin band. In a heat exchanger in which needle-like corrugated fin bands arranged in the direction are arranged and joined so that the length direction of the needle-like fins is perpendicular to the oblique plane and the corrugated wave height direction is approximately in the air flow direction. , the corrugated fin is formed into a ladder-like needle-like shape by punching out the corrugated fin at the part corresponding to the curved part of the corrugated molding, leaving both ends in the width direction of the band-shaped metal plate, and punching out a large number of slits in the part corresponding to the straight part of the corrugated molding. It is characterized by being a fin group.

以下、本考案の一実施例を図面に基づき詳細に
説明する。
Hereinafter, one embodiment of the present invention will be described in detail based on the drawings.

本考案の熱交換器の伝熱管は従来同様内部の長
手方向に沿つて隔壁1a(図では断面の短軸方向
に形成されるが長軸方向でも良い)が設けられた
押出偏平管1が用いられ、その偏平面1bが互い
に間隔をおいて対向すると共に平行に配置される
よう一本の偏平管1を第1図のように蛇行させた
り、あるいはヘツダを介して多数の偏平管1を取
付けることで製作されたものであり、この偏平面
1bで形成される間隔内に帯状金属薄板でコルゲ
ート成形された圧力損失が小さく伝熱性能の高い
針状フイン群20が偏平管1の長手方向と直交さ
せたり、あるいは傾斜させて、ろう付けや接着剤
で接合されて熱交換器とされる。
The heat exchanger tube of the present invention uses an extruded flat tube 1 having a partition wall 1a (formed in the short axis direction of the cross section in the figure, but it may be formed in the long axis direction) along the longitudinal direction of the inside, as in the conventional case. A single flat tube 1 is meandered as shown in Fig. 1 so that the flat surfaces 1b thereof face each other at intervals and are arranged in parallel, or a large number of flat tubes 1 are attached via headers. A group of needle-like fins 20, which are corrugated from a band-shaped thin metal plate and have low pressure loss and high heat transfer performance, are arranged in the interval formed by the flat surface 1b in the longitudinal direction of the flat tube 1. They are made into a heat exchanger by being made perpendicular or at an angle and joined by brazing or adhesive.

この針状フイン群20は、従来の針状フイン群
2(第3図a,b参照)について詳しく考察した
ところ圧力損失の増大及び熱伝達率の低下原因が
コルゲート成形の彎曲部R、すなわち頂部と底部
とに位置する針状フイン2cによつて空気4の流
入および流出が阻害されることにあることが判明
したことに基づいて作られたものであり、フイン
素材となる帯状金属薄板の幅方向両端部20aを
わずかに残し、コルゲート成形の彎曲部Rに対応
する部分を大きく打ち抜いて打抜部20bを形成
する一方、コルゲート成形の直線部Lに対応する
部分には幅方向両端部20aをわずかに残し、幅
方向に多数の矩形のスリツト20cを形成して梯
子状の針状フイン20dを打ち残し、これを長手
方向に沿つて蛇行させてコルゲート成形したもの
である。そして、伝熱管としての偏平管1の偏平
面1b間への接合は、あらかじめ偏平面1bに塗
布したろう材や接着剤でコルゲート成形後の針状
フイン群20の幅方向両端をろう付や接着して行
なわれるが、この接合の際、コルゲート成形の直
線部Lが偏平管1の幅方向と平行となるよう配置
したり、あるいは角度θだけ傾斜させて配置す
る。
A detailed study of the conventional needle fin group 2 (see Figures 3a and b) shows that the cause of the increase in pressure loss and the decrease in heat transfer coefficient is the curved part R of corrugate molding, that is, the top of this needle fin group 20. It was made based on the fact that it was found that the inflow and outflow of the air 4 was obstructed by the needle-like fins 2c located at the bottom and the width of the strip metal thin plate that was the fin material. A punched portion 20b is formed by largely punching out a portion corresponding to the curved portion R of the corrugated molding, leaving only a small portion of both end portions 20a in the width direction. A large number of rectangular slits 20c are formed in the width direction, and ladder-like needle-like fins 20d are left, and these are corrugated by meandering along the longitudinal direction. The flat tube 1 as a heat transfer tube is joined between the flat surfaces 1b by brazing or gluing both widthwise ends of the needle fin group 20 after corrugated molding using a brazing material or adhesive applied to the flat surfaces 1b in advance. However, during this joining, the straight part L of the corrugated molding is arranged so as to be parallel to the width direction of the flat tube 1, or it is arranged so as to be inclined by an angle θ.

このような針状フイン群20を具えた熱交換器
では、コルゲート成形された彎曲部Rには針状フ
イン20dが設けてないため空気4の流入・流出
が阻害されずスムーズとなると共に均一となり彎
曲部Rでの空気4の流速ベクトル4aと直線部L
での空気4の流速ベクトル4bとが等しくなる結
果、空気の圧力損失が低減され熱伝達率の向上と
なる。したがつて、同一伝熱性能の熱交換器とし
ては小型化が達成できる。
In the heat exchanger equipped with such a needle-like fin group 20, since the needle-like fins 20d are not provided in the corrugated curved portion R, the inflow and outflow of the air 4 is not obstructed and becomes smooth and uniform. Flow velocity vector 4a of air 4 in curved part R and straight part L
As a result, the pressure loss of the air is reduced and the heat transfer coefficient is improved. Therefore, a smaller heat exchanger with the same heat transfer performance can be achieved.

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

第1図a,b、第2図、第3図a,bは従来の
針状フインを具えた熱交換器にかかり、第1図a
は正面図、第1図bは横断面図、第2図は部分斜
視図、第3図aは管部分の横断面図、第3図bは
一部分の横断面図、第4図a,bおよび第5図は
本考案の熱交換器の一実施例にかかり、第4図
a,bはそれぞれ一部分の横断面図、第5図はフ
イン部分の拡大斜視図である。 図面中、1は偏平管、1aは隔壁、1bは偏平
面、4は空気、4a,4bは流速ベクトル、20
は針状フイン群、20aは幅方向両端部、20b
は打抜部、20cはスリツト、20dは針状フイ
ン、L,Rはコルゲート成形の直線部および彎曲
部、である。
Figure 1 a, b, Figure 2, Figure 3 a, b apply to a conventional heat exchanger equipped with needle-like fins;
is a front view, FIG. 1 b is a cross-sectional view, FIG. 2 is a partial perspective view, FIG. 3 a is a cross-sectional view of the pipe section, FIG. 3 b is a partial cross-sectional view, and FIGS. 4 a, b 5 shows an embodiment of the heat exchanger of the present invention, FIGS. 4a and 4b are partial cross-sectional views, and FIG. 5 is an enlarged perspective view of the fin portion. In the drawing, 1 is a flat tube, 1a is a partition wall, 1b is a flat surface, 4 is air, 4a and 4b are flow velocity vectors, and 20
20a is a needle-like fin group, 20a is both ends in the width direction, 20b
20c is a punched portion, 20c is a slit, 20d is a needle-like fin, and L and R are a straight portion and a curved portion of corrugated molding.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 内部に熱交換媒体を通過させる偏平管の偏平面
が互いに間隔をおいて平行対向配置され、相対向
した偏平面間に針状フインがフイン帯の幅方向に
配置された針状コルゲートフイン帯を針状フイン
の長さ方向が該偏平面に直交するとともにコルゲ
ート波高方向がほぼ空気の流れ方向となるように
配設・接合してなる熱交換器において、前記コル
ゲートフインを、帯状金属板の幅方向両端部を残
しコルゲート成形の彎曲部に対応する部分を打抜
くと共にコルゲート成形の直線部に対応する部分
に多数のスリツトを打ち抜いた梯子状の針状フイ
ン群としたことを特徴とする熱交換器。
An acicular corrugated fin band in which the flat surfaces of flat tubes through which a heat exchange medium is passed are arranged parallel to each other at intervals, and needle fins are arranged in the width direction of the fin band between the opposing flat surfaces. In a heat exchanger in which needle-shaped fins are arranged and joined so that the length direction thereof is perpendicular to the flat plane and the corrugated wave height direction is substantially in the air flow direction, the corrugated fins are arranged and A heat exchanger characterized by forming a ladder-like needle-like fin group by punching out a part corresponding to a curved part of corrugate molding, leaving both ends in the direction, and punching out a large number of slits in a part corresponding to a straight part of corrugate molding. vessel.
JP9146582U 1982-06-21 1982-06-21 Heat exchanger Granted JPS58194384U (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP9146582U JPS58194384U (en) 1982-06-21 1982-06-21 Heat exchanger
DE8383730057T DE3377666D1 (en) 1982-06-21 1983-06-21 Heat exchanger
AU15994/83A AU1599483A (en) 1982-06-21 1983-06-21 Heat exchanger with fins
EP19830730057 EP0097612B1 (en) 1982-06-21 1983-06-21 Heat exchanger
CA000430892A CA1230872A (en) 1982-06-21 1983-06-21 Heat exchanger
KR2019860006841U KR870001425Y1 (en) 1982-06-21 1986-05-07 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9146582U JPS58194384U (en) 1982-06-21 1982-06-21 Heat exchanger

Publications (2)

Publication Number Publication Date
JPS58194384U JPS58194384U (en) 1983-12-24
JPS6234150Y2 true JPS6234150Y2 (en) 1987-08-31

Family

ID=30099839

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9146582U Granted JPS58194384U (en) 1982-06-21 1982-06-21 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS58194384U (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5224300U (en) * 1975-08-12 1977-02-21
JPS5642093A (en) * 1979-09-12 1981-04-20 Hitachi Ltd Heat exchanger

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54155669U (en) * 1978-04-21 1979-10-29

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5224300U (en) * 1975-08-12 1977-02-21
JPS5642093A (en) * 1979-09-12 1981-04-20 Hitachi Ltd Heat exchanger

Also Published As

Publication number Publication date
JPS58194384U (en) 1983-12-24

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