JPS589099Y2 - Finch tube for heat exchanger - Google Patents

Finch tube for heat exchanger

Info

Publication number
JPS589099Y2
JPS589099Y2 JP1980158856U JP15885680U JPS589099Y2 JP S589099 Y2 JPS589099 Y2 JP S589099Y2 JP 1980158856 U JP1980158856 U JP 1980158856U JP 15885680 U JP15885680 U JP 15885680U JP S589099 Y2 JPS589099 Y2 JP S589099Y2
Authority
JP
Japan
Prior art keywords
tube
fin
heat exchanger
welding
welded
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
JP1980158856U
Other languages
Japanese (ja)
Other versions
JPS5782682U (en
Inventor
真男 原
Original Assignee
藤川 一市
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 藤川 一市 filed Critical 藤川 一市
Priority to JP1980158856U priority Critical patent/JPS589099Y2/en
Publication of JPS5782682U publication Critical patent/JPS5782682U/ja
Application granted granted Critical
Publication of JPS589099Y2 publication Critical patent/JPS589099Y2/en
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 本考案は、主として熱交換器に用いられるフィンチュー
ブの改良構造に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improved structure of a fin tube mainly used in a heat exchanger.

従来、この種フィンチューブの構造としては、第4図乃
至第6図に示すものが知られている。
Conventionally, as this type of fin tube structure, those shown in FIGS. 4 to 6 are known.

該フィンチューブ10は、熱媒体となる例えば水を通流
させる為のチューブ11と、この長手方向に於て所定間
隔毎に多数列設されたフィン12とから構成されている
The fin tube 10 is composed of a tube 11 through which a heat medium, for example, water, flows, and fins 12 arranged in multiple rows at predetermined intervals in the longitudinal direction.

前記フィン12は、第4図に示す如く、通常、左右に二
分割されて居り、これらの間には所要の間隙が形成され
る。
As shown in FIG. 4, the fins 12 are usually divided into left and right halves, with a required gap formed between them.

斯くの如きフィンチューブ10を作製する場合、従来に
あっては、左右に二分割されたフィン素体13.13に
は第6図に示す如く、各々チューブ11の外径に適合し
た曲率を備える円弧切欠14゜14が切設され、両フィ
ン素体13,13(ri電気抵抗溶接法に依ってチュー
ブ11に溶着される。
When manufacturing such a fin tube 10, conventionally, the fin body 13 and 13, which are divided into left and right halves, are each provided with a curvature that matches the outer diameter of the tube 11, as shown in FIG. A circular arc notch 14° 14 is cut out, and both fin bodies 13, 13 are welded to the tube 11 by RI electric resistance welding.

つ捷り、チューブ11を中心にして左右両側方からフィ
ン素体13,13を移動せしめてチューブ11に圧接し
、両者を溶接していたのである。
The fin bodies 13, 13 were moved from both the left and right sides around the tube 11, and were brought into pressure contact with the tube 11, thereby welding them together.

ところが、この様な方法にて製作されたフィンチューブ
10は、各フィン素体13,13がチューブ11の外周
に溶着しであるにも拘わらず、その熱伝達効率が悪かっ
た。
However, the fin tube 10 manufactured by such a method had poor heat transfer efficiency even though the fin bodies 13, 13 were welded to the outer periphery of the tube 11.

そこで、原因を解明して行くと、フィン素体13.13
とチューブ11との溶接部分が、その当合面全範に亘っ
て均一に溶着されていない事が判明した。
So, when we elucidated the cause, we found that the fin body 13.13
It was found that the welded portion between the tube 11 and the tube 11 was not uniformly welded over the entire contact surface.

つ1す、電気抵抗溶接に依って溶着されてはいるのだが
、部分的に溶着している場合が往々にしてあったのであ
る。
First, although they were welded by electric resistance welding, there were often cases where they were partially welded.

この様な状態では、比較的大きな面積を有するフィン素
体13,13でいくら良好に受熱してもチューブ内の熱
媒体1での熱伝達経路に於ては寸断されてしまうので、
熱交換効率が悪くなる訳である。
In such a state, no matter how well the fin bodies 13, 13 having relatively large areas receive heat, the heat transfer path in the heat medium 1 inside the tube is interrupted.
This results in poor heat exchange efficiency.

従来にあっては、この様なフィンチューブでも差支えな
かったのであるが、現今に於てば、エネルギーの有効利
用が叫ばれる様になり、熱交換器の全体構造からフィン
チューブ等の如く細部に到る壕で悉さに検討され、改善
する事を要求されて来たのである。
In the past, there was no problem with finned tubes like this, but nowadays, there is a growing demand for effective use of energy, and there are changes from the overall structure of heat exchangers to the details such as finned tubes. Every trench has been thoroughly examined and improvements have been requested.

本考案は、叙上の問題点に鑑み、これを解消する為に創
案されたもので、その主たる目的は、)インとチューブ
との溶着が完全に行なわれて、所定の熱交換効率を間断
なく発揮し得る熱交換器用フィンチューブを提供するに
ある。
This invention was devised in order to solve the above-mentioned problems, and its main purpose is to completely weld the inner part and the tube, and maintain a predetermined heat exchange efficiency. To provide a finned tube for a heat exchanger that can be used without any problems.

本考案の他の目的は、従来から使用している自動抵抗溶
接機等の設備をその1−!活用してフィンとチューブと
の完全溶着が可能となり、特別な器具・機器並びに装置
を必要としないで製造できる熱交換器用フィンチューブ
を提供するにある。
Another purpose of this invention is to improve equipment such as automatic resistance welding machines that have been used conventionally. To provide a fin tube for a heat exchanger that can be manufactured without the need for special equipment, equipment, or equipment, and which enables complete welding of fins and tubes.

本考案の更に他の目的は、フィンを構成するフィン素体
の円弧状切欠、つ1リチユ一ブ外周に当合する端面を、
連続した凹凸形状にすると共に、円弧状切欠の終端角部
をチューブ外周に当合せぬ様切欠いて切除形状とし、該
切除部を除く円弧状切欠、つ1り連続凹凸部の全範がチ
ューブ外周に均一に溶着され、且つ切除部が存する事に
依り同部分の過剰溶着並びに溶接歪等を防止する様にし
た熱交換器用フィンチューブを提供するにある。
Still another object of the present invention is to form a circular notch in the fin body constituting the fin, and an end surface that abuts against the outer circumference of the fin.
In addition to creating a continuous uneven shape, the end corner of the circular notch is cut out so that it does not touch the outer periphery of the tube, and the entire range of the circular notch and the continuous uneven part excluding the cut out part is the outer circumference of the tube. To provide a fin tube for a heat exchanger which is uniformly welded to the fin tube and which is prevented from excessive welding and welding distortion due to the presence of the cut portion.

以下、本考案の一実施例を示す図面、とりわけ第1図乃
至第3図に基づきその詳細を説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, details of an embodiment of the present invention will be explained based on the drawings, especially FIGS. 1 to 3.

本考案に係る熱交換器用フィンチューブ1は、第1図乃
至第2図に示す如く、水等の熱媒体を通流させる円筒状
のチューブ2と、排ガス・蒸気等の主として高温気体の
熱を受熱するフィン3とから成って居り、該フィン3は
チューブ2の長手軸方向に所定間隔毎に多数配設されて
いる。
As shown in FIGS. 1 and 2, a finned tube 1 for a heat exchanger according to the present invention includes a cylindrical tube 2 through which a heat medium such as water flows, and a cylindrical tube 2 through which heat of mainly high-temperature gases such as exhaust gas and steam flows. A large number of fins 3 are arranged at predetermined intervals in the longitudinal direction of the tube 2.

前記フィン3は、薄板で構成され、本実施例に於ては左
右に二分割されており、これらの間には所定の間隙が形
成される。
The fin 3 is made of a thin plate, and in this embodiment is divided into left and right halves, with a predetermined gap formed between them.

左右のフィン素体4,4のチューブ側端部には、チュー
ブ2の外径りに呼応した円弧状切欠5,5が切設されて
いる。
Arc-shaped notches 5, 5 corresponding to the outer diameter of the tube 2 are cut in the tube-side ends of the left and right fin bodies 4, 4.

本考案にあっては、この円弧状切欠5を、連続凹凸部6
と、その両端側にある切除部7,7とで構成している。
In the present invention, this arcuate notch 5 is replaced by a continuous uneven portion 6.
and cutout portions 7, 7 on both ends thereof.

前記切除部7,7ば、円弧状切欠5の終端角部にあって
、角を落して造形され、比較的小範囲に止めである。
The cutout portions 7, 7 are located at the terminal corners of the arcuate notch 5, are shaped with rounded corners, and are stopped within a relatively small area.

連続凹凸部6は、前記切除部7,7以外の全てに亘って
比較的広範囲に形成され、本実施例の場合、鋸歯状(ギ
ザギザ)にしてその歯先並びに歯底に丸みを付けである
The continuous concavo-convex portion 6 is formed over a relatively wide area except for the cut-out portions 7, 7, and in this embodiment, it is serrated and has rounded tips and bottoms. .

勿論、鋸歯状に限定される事はなく、くし状や歯車の歯
型状等にする事も可能である。
Of course, the shape is not limited to a sawtooth shape, and it is also possible to have a comb shape, a gear tooth shape, etc.

第3図に示す如く連続凹凸部6を造形する場合、例えば
歯先と歯底の中程(歯膜)を通る直径(ピッチ円直径)
D′を、チューブ2の外径りと同等にすると、電気抵抗
溶接の際、歯先部分が溶融して歯底に向い最終段階に於
ては、チューブ2の外周とはその全範に亘って均一に溶
着される。
When modeling a continuous uneven portion 6 as shown in FIG. 3, for example, the diameter (pitch circle diameter) passing between the tooth tip and the tooth bottom (dental membrane)
If D' is made equal to the outer diameter of the tube 2, during electric resistance welding, the tip of the tooth will melt and face the bottom of the tooth, and in the final stage, the outer circumference of the tube 2 will extend over its entire range. Welded uniformly.

勿論、連続凹凸部6の曲率は上述の様に限定される事は
なく、回部の溶は込み状態や最終溶着仕上がり状態を加
味した上で適宜設定し得る。
Of course, the curvature of the continuous concavo-convex portion 6 is not limited as described above, and can be appropriately set in consideration of the welding state of the rounded portion and the final welding finish state.

要は、溶接当初に於てはチューブ2との接触面積が少な
くて漸次大きくなる様にすると共に、この事がチューブ
2とフィン素体4の接合面全範に於て等間隔に均等に行
なわれるべく連続凹凸部6の形状・ピッチ・高さ・曲率
等の諸条件を設定すれば良い訳である。
The point is that the contact area with the tube 2 is small at the beginning of welding and gradually increases, and this is done evenly at equal intervals over the entire joint surface between the tube 2 and the fin body 4. It is sufficient to set various conditions such as the shape, pitch, height, curvature, etc. of the continuous uneven portion 6 as much as possible.

加えて本考案にあっては、円弧状切欠5の終端角部を切
除して切除部7を造形している。
In addition, in the present invention, the terminal corner of the arcuate notch 5 is cut out to form the cutout part 7.

従来にあっては、第4図並びに第6図に示す如く、チュ
ーブとの接合面積を増大し熱交換効果を高める意味から
これがない。
Conventionally, as shown in FIGS. 4 and 6, this has not been done in order to increase the joint area with the tube and enhance the heat exchange effect.

然し従来の如く構成して置くと、同部分が他の部分より
過剰ぎみに溶着し、この為部分的な溶接歪が発生して問
題であった。
However, when constructed as in the past, the same part was welded more tightly than other parts, which caused a problem in that local welding distortion occurred.

そこで本考案にあっては、第1図並びに第3図に示す如
くこの角部を始めからカットして置いてチューブ2に当
合・溶着されない様にしたのである。
Therefore, in the present invention, as shown in FIGS. 1 and 3, this corner is cut off from the beginning to prevent it from coming into contact with the tube 2 and being welded.

この様にすると、熱伝達率は若干低下するが、前述した
過剰溶着や部分的な溶接歪を完全に除去できるのである
In this way, although the heat transfer coefficient is slightly lowered, the above-mentioned excessive welding and local welding distortion can be completely eliminated.

該切除部7は本実施例の如く直線状に限らず、弧状等で
も良い。
The cutout portion 7 is not limited to a straight line as in this embodiment, but may be arcuate or the like.

虜、本実施例では、フィン3を左右に二分割した構造の
ものについて述べたが、例えば左右上下に四分割したフ
ィン3に本考案を適用する事もできる。
In this embodiment, a structure in which the fin 3 is divided into two parts horizontally is described, but the present invention can also be applied to, for example, a fin 3 which is divided into four parts horizontally and vertically.

分割の仕方は二以上であれば任意である。而して各フィ
ン素体4ば、板材をプレス加工に依り打抜いて連続凹凸
部6並びに切除部7を備えた円弧状切欠5を造形するの
で極めて容易に且つ精度良く多量生産ができる。
The method of division is arbitrary as long as there are two or more. Since each fin body 4 is formed by punching out a plate material by press working to form an arcuate notch 5 having continuous uneven portions 6 and cut-out portions 7, mass production is possible with great ease and accuracy.

チューブ2並びにフィン3の材質は、コ般鋼やステンレ
ス・耐蝕鋼等の特殊鋼その他の抵抗溶接できる全てのも
のが適用可能で、用途に応じて適宜採用できる。
The material of the tube 2 and the fin 3 may be general steel, special steel such as stainless steel or corrosion-resistant steel, or any other material that can be resistance welded, and can be appropriately adopted depending on the purpose.

以上既述した如く、本考案に依ればフィンとチューブと
の溶着が完全に行なわれて所定の熱交換効率を間断なく
発揮し得る。
As described above, according to the present invention, the fins and tubes are completely welded together, and a predetermined heat exchange efficiency can be achieved without interruption.

既存の設備をその捷1使用して製造でき、新たな設備投
資をする必要がなく、直ちに実施可能である。
It can be manufactured using existing equipment, and there is no need to invest in new equipment, and it can be implemented immediately.

フィン素体の円弧状切欠を連続した凹凸状にすると共に
切除部を有する形状にしたので、溶接初期から終了捷で
の過程に於て漸次チューブとの接触面積が増大し、この
事は等間隔箇所毎に行なわれて完全に溶融して溶着され
る。
Since the arc-shaped notch in the fin body is made into a continuous uneven shape and has a cutout, the contact area with the tube gradually increases from the initial welding stage to the final welding process. This is done in each location to ensure complete melting and welding.

従って溶着後は連続凹凸部の全範が間断なく接着される
為熱伝達率が良好となり、ひいては熱交換効率を著しく
高め得る事ができる等諸種の効果を奏するものである。
Therefore, after welding, the entire range of the continuous uneven portions is bonded without interruption, resulting in a good heat transfer coefficient, which brings about various effects such as significantly increasing the heat exchange efficiency.

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

第1図は、本考案に係るフィンチューブを示す縦断モ面
図。 第2図は、一部を縦断して示した同じものの側面図。 第3図は、円弧状切欠の形状を拡大して示す要部拡大正
面図。 第4図は、従来のフィンチューブの構造を示す縦断面面
図。 第5図は、一部を縦断して示す第4図の側面図。 第6図は、フィンとチューブとの分解状態を示す縦断面
面図である。 1・・・・・・熱交換器用フィンチューブ、2・・・・
・・チューブ、3・・・・・・フィン、4・・・・・・
フィン素体、5・・・・・・円弧状切欠、6・・・・・
・連続凹凸部、7・・・・・・切除部。
FIG. 1 is a vertical cross-sectional view showing a fin tube according to the present invention. FIG. 2 is a side view of the same part shown in longitudinal section. FIG. 3 is an enlarged front view of the main part showing the shape of the arcuate notch. FIG. 4 is a longitudinal sectional view showing the structure of a conventional fin tube. FIG. 5 is a side view of FIG. 4, partially shown in longitudinal section. FIG. 6 is a longitudinal sectional view showing the disassembled state of the fin and tube. 1... Fin tube for heat exchanger, 2...
...Tube, 3...Fin, 4...
Fin body, 5... Arc-shaped notch, 6...
・Continuous uneven portion, 7...Removed portion.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 円筒状のチューブ2と、これの長手方向の外周に適当間
隔毎に適数配設されたフィン3とを備え、該フィン3は
少なくとも左右に分割されて各フィン素体4のチューブ
当合端部には円弧状切欠5を形成し、これとチューブ2
とを圧接せしめて電気抵抗溶接法に依って溶着されるフ
ィンチューブに於て、前記フィン素体4に形成する円弧
状切欠5を、比較的広範囲の一つの連続凹凸部6と、そ
の両側に存し円弧状切欠5の終端角部を切除した比較的
狭範囲の二つの切除部Iとで構成した事を特徴とする熱
交換器用フィンチューブ。
It comprises a cylindrical tube 2 and an appropriate number of fins 3 arranged at appropriate intervals on the outer periphery of the tube in the longitudinal direction, and the fins 3 are divided at least left and right so that each fin body 4 has a tube abutting end. An arcuate cutout 5 is formed in the tube 2.
In the fin tube that is welded by electrical resistance welding by press-welding the fin body 4, the arc-shaped notch 5 formed in the fin body 4 is formed on one continuous concavo-convex portion 6 over a relatively wide range, and on both sides of the circular notch 5. A finned tube for a heat exchanger, characterized in that the finned tube for a heat exchanger is constituted by two relatively narrow cutout portions I obtained by cutting off the terminal corners of an arcuate cutout 5.
JP1980158856U 1980-11-05 1980-11-05 Finch tube for heat exchanger Expired JPS589099Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1980158856U JPS589099Y2 (en) 1980-11-05 1980-11-05 Finch tube for heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1980158856U JPS589099Y2 (en) 1980-11-05 1980-11-05 Finch tube for heat exchanger

Publications (2)

Publication Number Publication Date
JPS5782682U JPS5782682U (en) 1982-05-21
JPS589099Y2 true JPS589099Y2 (en) 1983-02-18

Family

ID=29517902

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1980158856U Expired JPS589099Y2 (en) 1980-11-05 1980-11-05 Finch tube for heat exchanger

Country Status (1)

Country Link
JP (1) JPS589099Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5987985A (en) * 1982-10-07 1984-05-21 シエ−フア−・ヴエルケ・ゲゼルシヤフト・ミツト・ベシユレンクテル・ハフツング Method of combining first member with thin wall and thin wall of second member

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3189087A (en) * 1958-03-06 1965-06-15 Green & Son Ltd Tubular heat exchangers
JPS5219258U (en) * 1975-07-28 1977-02-10

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5213006Y2 (en) * 1973-04-18 1977-03-23

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3189087A (en) * 1958-03-06 1965-06-15 Green & Son Ltd Tubular heat exchangers
JPS5219258U (en) * 1975-07-28 1977-02-10

Also Published As

Publication number Publication date
JPS5782682U (en) 1982-05-21

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