JP2006317046A - Heat exchanger tube - Google Patents

Heat exchanger tube Download PDF

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JP2006317046A
JP2006317046A JP2005138769A JP2005138769A JP2006317046A JP 2006317046 A JP2006317046 A JP 2006317046A JP 2005138769 A JP2005138769 A JP 2005138769A JP 2005138769 A JP2005138769 A JP 2005138769A JP 2006317046 A JP2006317046 A JP 2006317046A
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tube
ridges
heat transfer
fins
axis direction
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Wakayuki Ishida
稚之 石田
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Abstract

<P>PROBLEM TO BE SOLVED: To improve heat exchanger effectiveness of a heat exchanger tube by improving a heat exchange area with a fluid inside and outside the tube. <P>SOLUTION: A tube wall is formed with circumferentially long projected strip parts 2 and recessed groove parts 3 alternately in a tube axis direction, and a fin 4 is joined to the outer peripheral surface of either one of each projected strip part 2 and each recessed groove part 3. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、熱交換率に優れた伝熱管に関するものである。   The present invention relates to a heat transfer tube having an excellent heat exchange rate.

この種の伝熱管としては、特許文献1に示すように、二重管式の液化天然ガス気化器に用いられるものであって、管の内外周面に螺旋状に伸びるフィンを設けるものが知られている。
一方、特許文献2には、管内周面に内溝と凸部とを形成したものが開示されている。
特開平8−183971号公報 特開平10−115495号公報
As this type of heat transfer tube, as shown in Patent Document 1, a tube used in a double tube type liquefied natural gas vaporizer, in which fins extending spirally are provided on the inner and outer peripheral surfaces of the tube, is known. It has been.
On the other hand, Patent Document 2 discloses one in which inner grooves and convex portions are formed on the inner peripheral surface of the pipe.
JP-A-8-183971 Japanese Patent Laid-Open No. 10-115495

特許文献1及び2の伝熱管では、伝熱管内部にフィンあるいは凸部等の熱交換面積を向上させるための加工が施されており、フィンを設けるか凸部等を形成するかのいずれかのみを行っており、熱交換率を十分に大きくできない。
本発明は、このような問題点を解決し得る伝熱管を提供することを目的とする。
本発明は、管軸方向交互に凸条部と凹条部とを形成すると共に、外周面にフィンを接合して、管内外の流体との熱交換面積を向上させて、熱交換率を向上させることができる伝熱管を提供すること目的とする。
In the heat transfer tubes of Patent Documents 1 and 2, the heat transfer tube is processed to improve the heat exchange area such as fins or protrusions, and only the fins are provided or the protrusions are formed. The heat exchange rate cannot be increased sufficiently.
An object of this invention is to provide the heat exchanger tube which can solve such a problem.
The present invention forms convex ridges and concave ridges alternately in the tube axis direction, and joins fins to the outer peripheral surface to improve the heat exchange area with the fluid inside and outside the tube, thereby improving the heat exchange rate. It is an object of the present invention to provide a heat transfer tube that can be made to flow.

前記目的を達成するため、本発明は次の手段を講じた。即ち、
管壁に周方向に長い凸条部2と凹条部3とを管軸方向交互に形成しており、この凸条部2または凹条部3のいずれか一方の外周面にフィン4が接合されている。
これによって、管内外の流体との熱交換面積を向上させて、熱交換率を向上させることができる。
前記管壁に周方向に長いフィン4を管軸方向に間隔をあけて形成しており、このフィン4間の管壁に周方向に長い凸条部2または凹条部3が設けられている。
In order to achieve the above object, the present invention takes the following measures. That is,
On the tube wall, long ridges 2 and concave ridges 3 that are long in the circumferential direction are formed alternately in the tube axis direction, and fins 4 are joined to the outer peripheral surface of either the ridges 2 or the ridges 3. Has been.
Thereby, the heat exchange area with the fluid inside and outside the pipe can be improved, and the heat exchange rate can be improved.
Fins 4 that are long in the circumferential direction are formed in the pipe wall at intervals in the pipe axis direction, and a long protruding strip 2 or a concave strip 3 is provided in the pipe wall between the fins 4 in the circumferential direction. .

これによって、管内外の流体との熱交換面積を向上させて、熱交換率を向上させることができる。
管壁に周方向に長い凸条部2と凹条部3とを管軸方向交互に形成しており、この凸条部2の前後の管壁を二つ折りして周方向に折り込み部5を形成し、この折り込み部5の先端にフィン4を接合している。
これによって、管内外の流体との熱交換面積を向上させて、熱交換率を向上させることができる。しかも、折り込み部5は管軸方向に密に形成できるので、熱交換面積を拡大して熱交換率をさらに向上させることができる。
Thereby, the heat exchange area with the fluid inside and outside the pipe can be improved, and the heat exchange rate can be improved.
In the tube wall, long ridges 2 and concave ridges 3 that are long in the circumferential direction are formed alternately in the tube axis direction, and the tube wall before and after the ridges 2 is folded in two to fold the folds 5 in the circumferential direction. The fin 4 is joined to the tip of the folded portion 5.
Thereby, the heat exchange area with the fluid inside and outside the pipe can be improved, and the heat exchange rate can be improved. In addition, since the folded portions 5 can be formed densely in the tube axis direction, the heat exchange area can be expanded to further improve the heat exchange rate.

前記凸条部2はリング状または螺旋状である。
これによって、フィン4の接合が容易になる。
The ridge portion 2 has a ring shape or a spiral shape.
This facilitates the bonding of the fins 4.

本発明により、管内外の流体との熱交換面積を向上させて、熱交換率を向上させることができる。   According to the present invention, the heat exchange area with the fluid inside and outside the pipe can be improved, and the heat exchange rate can be improved.

以下、本発明の実施の形態を図面に基づき説明する。
第1実施形態の伝熱管1は、管内外の流体の熱を交換する金属製の伝熱管として、ボイラー等の熱交換器に用いられる。
図1において示すように、管壁に管軸方向螺旋状に隆起して1条の凸条部2と凹条部3とを形成し、前記凹条部3の外周面に沿ってフィン4を接合して構成されている。
前記凸条部2は、管軸方向の端部に設けられるストレート管状の管端部6に隣接して、管壁が径外方向に太鼓状に突隆している部分であって、管軸方向に前記凹条部3の長さ分(螺旋ピッチ)だけ間隔をあけて形成されている。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
The heat transfer tube 1 of the first embodiment is used in a heat exchanger such as a boiler as a metal heat transfer tube that exchanges heat of fluid inside and outside the tube.
As shown in FIG. 1, the tube wall protrudes spirally in the tube axis direction to form a single ridge portion 2 and a concave ridge portion 3, and fins 4 are formed along the outer peripheral surface of the concave ridge portion 3. It is constructed by joining.
The ridge portion 2 is a portion in which the tube wall protrudes in a drum shape in the radially outward direction adjacent to a straight tubular tube end portion 6 provided at an end portion in the tube axis direction. It is formed in the direction with an interval corresponding to the length of the concave strip 3 (spiral pitch).

前記凹条部3は、管軸方向に隣接する前記凸条部2の間に形成され、前記管端部6と略同径となっている。
前記フィン4は、凹条部3の谷底の外周面に帯板の基端側を接合し、螺旋状に周回しながら、蝋付け、溶接等の伝熱を阻害しにくい接合方法で接合されている。
前記伝熱管1の内周面の内溝7は、管内周面の伝熱面積を拡大させて熱交換率を向上させている。前記内溝7は、管軸方向に対する傾斜角が異なる2種類の溝から構成され、2種類の内溝7の境界には内溝境界線8が設けられ、前記内溝境界線8近傍においてそれぞれの内溝7に沿って移動してきた管内の流体同士が衝突して乱流を生じさせ、熱交換率を向上させられるようになっている。
The concave strip portion 3 is formed between the convex strip portions 2 adjacent in the tube axis direction and has substantially the same diameter as the tube end portion 6.
The fin 4 is joined to the outer peripheral surface of the valley bottom of the concave strip portion 3 by a joining method that hardly hinders heat transfer such as brazing and welding while spirally turning around the base plate side. Yes.
The inner groove 7 on the inner peripheral surface of the heat transfer tube 1 increases the heat transfer area of the inner peripheral surface of the tube and improves the heat exchange rate. The inner groove 7 is composed of two types of grooves having different inclination angles with respect to the tube axis direction, and an inner groove boundary line 8 is provided at the boundary between the two types of inner grooves 7, respectively, in the vicinity of the inner groove boundary line 8. The fluids in the pipes that have moved along the inner groove 7 collide with each other to generate turbulent flow, thereby improving the heat exchange rate.

前記伝熱管1の加工方法は、金属板の一面に内溝7をロールで圧延形成し、この金属板の両端部を内溝7が内周にくるように接合して金属管を成形する。次いで、前記金属管をバルジ加工(ハイドロフォーミング加工)によって管内から管壁を拡管して螺旋状の凸条部2を形成する。次に、凸条部2間の凹条部3に沿って帯板を接合してフィン4を形成する。なお、伝熱管1はストレート管に帯板を螺旋状に接合してフィン4を形成してから、フィン4の間を隆起して凸条部2を形成しても良い。また、フィン4は凸条部2の頂部に沿って形成しても良い。   In the method of processing the heat transfer tube 1, the inner groove 7 is rolled and formed on one surface of a metal plate, and both ends of the metal plate are joined so that the inner groove 7 comes to the inner periphery, thereby forming the metal tube. Next, the metal tube is expanded from the inside of the tube by bulging (hydroforming) to form the spiral ridge 2. Next, the strips are joined along the concave stripes 3 between the convex stripes 2 to form the fins 4. In the heat transfer tube 1, the strips may be spirally joined to the straight tube to form the fins 4, and then the protrusions 2 may be formed by protruding between the fins 4. Further, the fin 4 may be formed along the top of the ridge 2.

図2において、第2実施形態の伝熱管1は、径外側に突隆したリング状の凸条部2と凹条部3とが管軸方向に交互に複数形成されている。また、フィン4はリングで形成され、リング状の凸条部2の頂部に嵌合して接合されており、谷底に設けるよりも大きく突出している。
第2実施形態の伝熱管1の加工方法は、ストレート管を管軸方向に一定間隔をおいて隆起させて、凸条部2を形成し、全凸条部2にリングを嵌合して接合してフィン4を形成する。
In FIG. 2, the heat transfer tube 1 of the second embodiment has a plurality of ring-shaped protruding ridges 2 and protruding ridges 3 protruding alternately in the tube axis direction. Moreover, the fin 4 is formed with a ring, is fitted and joined to the top of the ring-shaped convex strip 2, and protrudes larger than that provided at the bottom of the valley.
The processing method of the heat transfer tube 1 of the second embodiment is that a straight tube is raised at a constant interval in the tube axis direction to form a convex portion 2, and a ring is fitted to all the convex portions 2 and joined. Thus, the fin 4 is formed.

図3において、第3実施形態の伝熱管1は、管軸方向に交互に凸条部2と凹条部3とを形成した伝熱管1(波状管)を、凸条部2の管軸方向の前後の管壁を縮管すると共に、径外側に突出させて二つ折りして折り込み部5を管軸方向に間隔をあけて形成しており、この折り込み部5の先端側にリングの内周を基端側を接合してフィン4を形成している。波状管に直接接合するより凸条部2及びフィン4を大径にできかつフィン4の間隔を密にできる。
第3実施形態の伝熱管1の加工方法は、図4において示すように、金属製の素材パイプの周方向に凹部形成型8を押し当てて凹条部9が管軸方向に間隔をあけて設けられた波状管10を形成する。凹条部9は素材パイプの周方向にリング状に設けると次工程の縮管工程で素材パイプを固定しやすいので、好適には素材パイプまたは凹部形成型8を周方向に回転させながら加工する。
In FIG. 3, the heat transfer tube 1 according to the third embodiment includes a heat transfer tube 1 (corrugated tube) in which convex ridges 2 and concave ridges 3 are alternately formed in the tube axis direction. The tube walls before and after the tube are contracted, and are folded in two by projecting outward in the diameter, and the fold portion 5 is formed with a gap in the tube axis direction. The fins 4 are formed by joining the base ends. The ridges 2 and the fins 4 can be made larger in diameter than the direct bonding to the corrugated tube, and the intervals between the fins 4 can be made closer.
As shown in FIG. 4, the processing method of the heat transfer tube 1 according to the third embodiment is such that the recess forming die 8 is pressed against the circumferential direction of the metal material pipe so that the recesses 9 are spaced apart in the tube axis direction. The provided corrugated tube 10 is formed. If the concave portion 9 is provided in a ring shape in the circumferential direction of the material pipe, it is easy to fix the material pipe in the subsequent contraction process, and therefore, preferably, the material pipe or the recess forming die 8 is processed while rotating in the circumferential direction. .

次に、管軸方向に所定間隔をもって形成した凹条部9に挟持型11を差し込み、管軸方向に移動して凹条部9間の管壁を圧縮し、凸条部2が形成すると同時に折り込み部5を形成する。この折り込み部5の先端側にリングを継ぎ足すように接合することで、フィン4を形成する。
本発明は前記実施形態における各部材の形状およびそれぞれの前後・左右・上下の位置関係は、図1〜4に示すように構成することが最良である。しかし、前記実施形態に限定されるものではなく、部材、構成を種々変形したり、組み合わせを変更したりすることもできる。
Next, the sandwiching die 11 is inserted into the concave strips 9 formed at a predetermined interval in the tube axis direction, moved in the tube axial direction to compress the tube wall between the concave strips 9, and the convex strips 2 are formed at the same time. The folding part 5 is formed. The fin 4 is formed by joining so that a ring may be added to the front end side of the folding part 5.
In the present invention, the shape of each member and the positional relationship between the front, rear, left, and right in the embodiment are best configured as shown in FIGS. However, it is not limited to the said embodiment, A member, a structure can be variously deformed, and a combination can also be changed.

前記第2、3実施形態では、フィン4を凹条部3に接合することもできるが、凸条部2の頂部にフィン4を接合した方が溶接作業が容易になる。
管壁は凸条部2と凹条部3とを滑らかに連続して設け、正面視波状なるようにしたりすることもできる。さらに、管壁外周面に内溝を設けて熱交換率を更に向上させることもできる。
In the second and third embodiments, the fins 4 can be joined to the concave strips 3, but welding work is easier when the fins 4 are joined to the tops of the convex strips 2.
The tube wall can also be provided with a smooth and continuous ridge portion 2 and a concave ridge portion 3 so as to have a front view wave shape. Furthermore, an inner groove can be provided on the outer peripheral surface of the tube wall to further improve the heat exchange rate.

本発明の第1実施形態の伝熱管の一部断面側面図である。It is a partial cross section side view of the heat exchanger tube of 1st Embodiment of this invention. 第2実施形態の伝熱管の一部断面側面図である。It is a partial cross section side view of the heat exchanger tube of 2nd Embodiment. 第3実施形態の伝熱管の一部断面側面図である。It is a partial cross section side view of the heat exchanger tube of 3rd Embodiment. 第3実施形態の伝熱管の加工方法の説明図である。It is explanatory drawing of the processing method of the heat exchanger tube of 3rd Embodiment.

符号の説明Explanation of symbols

1 伝熱管
2 凸条部
3 凹条部
4 フィン
5 折り込み部
6 管端部
7 内溝
8 内溝境界線
9 凹条部
10 波状管
11 挟持型
12 内部型
DESCRIPTION OF SYMBOLS 1 Heat-transfer tube 2 Convex part 3 Concave part 4 Fin 5 Folding part 6 Pipe end part 7 Inner groove 8 Inner groove boundary line 9 Concave part 10 Corrugated pipe 11 Clamping type 12 Internal type

Claims (4)

管壁に周方向に長い凸条部(2)と凹条部(3)とを管軸方向交互に形成しており、この凸条部(2)または凹条部(3)のいずれか一方の外周面にフィン(4)が接合されていることを特徴とする伝熱管。   On the tube wall, long ridges (2) and ridges (3) that are long in the circumferential direction are formed alternately in the tube axis direction, and either one of the ridges (2) or the ridges (3). A heat transfer tube characterized in that fins (4) are joined to the outer peripheral surface of the heat transfer tube. 管壁に周方向に長いフィン(4)を管軸方向に間隔をあけて形成しており、このフィン(4)間の管壁に周方向に長い凸条部(2)または凹条部(3)が設けられていることを特徴とする伝熱管。   Fins (4) that are long in the circumferential direction are formed in the tube wall at intervals in the tube axis direction, and convex ribs (2) or concave strips (2) that are long in the circumferential direction are formed on the tube wall between the fins (4). A heat transfer tube characterized in that 3) is provided. 管壁に周方向に長い凸条部(2)と凹条部(3)とを管軸方向交互に形成しており、この凸条部(2)の前後の管壁を二つ折りして周方向に折り込み部(5)を形成し、この折り込み部(5)の先端にフィン(4)を接合していることを特徴とする伝熱管。   The tube wall is formed with ridges (2) and ridges (3) that are long in the circumferential direction alternately in the tube axis direction, and the tube wall before and after the ridges (2) is folded in two A heat transfer tube, wherein a folded portion (5) is formed in a direction, and a fin (4) is joined to a tip of the folded portion (5). 前記凸条部(2)はリング状または螺旋状であることを特徴とする請求項1〜3のいずれかに記載の伝熱管。   The heat transfer tube according to any one of claims 1 to 3, wherein the protruding portion (2) has a ring shape or a spiral shape.
JP2005138769A 2005-05-11 2005-05-11 Heat exchanger tube Pending JP2006317046A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101975522A (en) * 2010-11-09 2011-02-16 上海化工研究院 High-efficient heat exchanger
WO2011103410A2 (en) * 2010-02-19 2011-08-25 3Ip, Llc Heat fins and related systems and methods
US8469082B2 (en) 2008-12-06 2013-06-25 3Ip, Llc Heat transfer between tracer and pipe
CN108801033A (en) * 2018-08-17 2018-11-13 上海欧贡制冷科技有限公司 A kind of efficient heat-exchanging pipe of condensation
JP7387990B2 (en) 2019-03-07 2023-11-29 富士電機株式会社 fin tube heat exchanger

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5363074A (en) * 1976-11-17 1978-06-06 Okamura Shiro Momentary rain detector
JPS6396492A (en) * 1986-10-07 1988-04-27 Furukawa Electric Co Ltd:The Finned tubular body and manufacture thereof
JPH089304Y2 (en) * 1990-09-14 1996-03-21 株式会社日本設計 Wall panel installation structure
JP2003148890A (en) * 2001-08-31 2003-05-21 Tosetz Co Ltd Heat exchanger tube and its manufacturing method

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5363074A (en) * 1976-11-17 1978-06-06 Okamura Shiro Momentary rain detector
JPS6396492A (en) * 1986-10-07 1988-04-27 Furukawa Electric Co Ltd:The Finned tubular body and manufacture thereof
JPH089304Y2 (en) * 1990-09-14 1996-03-21 株式会社日本設計 Wall panel installation structure
JP2003148890A (en) * 2001-08-31 2003-05-21 Tosetz Co Ltd Heat exchanger tube and its manufacturing method

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8469082B2 (en) 2008-12-06 2013-06-25 3Ip, Llc Heat transfer between tracer and pipe
US8662156B2 (en) 2008-12-06 2014-03-04 Qmax Industries, Llc Heat transfer between tracer and pipe
US9841239B2 (en) 2008-12-06 2017-12-12 Qmax Industries, Llc Heat transfer between tracer and pipe
US10520257B2 (en) 2008-12-06 2019-12-31 Controls Southeast, Inc. Heat transfer between tracer and pipe
WO2011103410A2 (en) * 2010-02-19 2011-08-25 3Ip, Llc Heat fins and related systems and methods
WO2011103410A3 (en) * 2010-02-19 2011-12-01 3Ip, Llc Heat fins and related systems and methods
CN101975522A (en) * 2010-11-09 2011-02-16 上海化工研究院 High-efficient heat exchanger
CN108801033A (en) * 2018-08-17 2018-11-13 上海欧贡制冷科技有限公司 A kind of efficient heat-exchanging pipe of condensation
JP7387990B2 (en) 2019-03-07 2023-11-29 富士電機株式会社 fin tube heat exchanger

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