JP4221260B2 - Heat exchanger and manufacturing method thereof - Google Patents

Heat exchanger and manufacturing method thereof Download PDF

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JP4221260B2
JP4221260B2 JP2003305894A JP2003305894A JP4221260B2 JP 4221260 B2 JP4221260 B2 JP 4221260B2 JP 2003305894 A JP2003305894 A JP 2003305894A JP 2003305894 A JP2003305894 A JP 2003305894A JP 4221260 B2 JP4221260 B2 JP 4221260B2
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tube
pipe
heat exchanger
flat
flow path
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JP2005076926A (en
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俊行 堀内
卓也 岩本
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T.RAD CO., L T D.
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Description

本発明は、 本発明は熱交換器及びその製造方法に関し、特に、プレート式の熱交換器及びその製造方法に関する。   The present invention relates to a heat exchanger and a manufacturing method thereof, and more particularly to a plate heat exchanger and a manufacturing method thereof.

従来、熱交換器の一つのタイプとして、冷却流体及び被冷却流体をそれぞれ層状に流通させ、熱交換を行わせるプレート式の熱交換器がある。   Conventionally, as one type of heat exchanger, there is a plate-type heat exchanger in which a cooling fluid and a fluid to be cooled are circulated in layers to perform heat exchange.

この種の熱交換器1は、例えば、図5に示されているように、交互に積層される波形フィン2及びプレート3と、波形フィン2の端部に接続される第1ヘッダー4と、流体の流れ方向を変えるために波形フィン2の端部に設けられたディストリビュータ5と、ディストリビュータ5に接続される第2ヘッダー6とから概略構成されている。   This type of heat exchanger 1 includes, for example, as shown in FIG. 5, corrugated fins 2 and plates 3 that are alternately stacked, and a first header 4 that is connected to an end of the corrugated fin 2. In order to change the flow direction of the fluid, a distributor 5 provided at the end of the corrugated fin 2 and a second header 6 connected to the distributor 5 are schematically configured.

そして、この熱交換器1の製作は、波形フィン2の端部をサイドバー7で挟持し、サイドバー7とプレート3の接触部を一体でロー付けした後、第1及び第2ヘッダー4,6を溶接接合することにより行っていた(例えば、特許文献1参照)。   The heat exchanger 1 is manufactured by sandwiching the end portions of the corrugated fins 2 with the side bars 7 and brazing the contact portions of the side bars 7 and the plate 3 together. 6 was welded (for example, refer to Patent Document 1).

また、別の熱交換器10は、図6に示されているように、扁平な外管11に扁平な内管12を内設して形成された2重管13と、外管11と内管12との間に形成された流路14に挿入されたインナーフィン15と、外管11の両端部長面16側に接続された流路14への出入口管17とから概略構成されている。   Further, as shown in FIG. 6, another heat exchanger 10 includes a double pipe 13 formed by providing a flat inner pipe 12 in a flat outer pipe 11, an outer pipe 11 and an inner pipe 11. The inner fin 15 inserted into the flow path 14 formed between the pipes 12 and the inlet / outlet pipe 17 to the flow path 14 connected to the long face 16 side of the both ends of the outer pipe 11 are roughly configured.

そして、この熱交換器10の製作は、各2枚のプレートをそれぞれロウ付けすることにより別々に外管11と内管12を扁平に形成させ、外管11に内管12を内設した後、外管11及び内管12の両端部にエンドキャップ(図示せず)を冠着し、外管11の両端部長面16側に出入口管17を接合することにより行っていた(例えば、特許文献2参照)。   The heat exchanger 10 is manufactured after the two outer plates 11 and the inner tube 12 are separately flattened by brazing each of the two plates, and the inner tube 12 is installed inside the outer tube 11. End caps (not shown) are attached to both ends of the outer tube 11 and the inner tube 12, and the inlet / outlet tube 17 is joined to the long surface 16 side of both ends of the outer tube 11 (for example, Patent Documents). 2).

実開昭55−167084号公報Japanese Utility Model Publication No. 55-167084 実開昭58−52462号公報Japanese Utility Model Publication No. 58-52462

ところが、上記した各熱交換器1,10の場合、部品点数、接合箇所、及び製作工数が多く、また、ロウ付け作業を必要とするため、製作に手間が掛かり、製作コストの低減化が図り難く、流体の漏洩も発生し易いといった問題があった。   However, in the case of each of the heat exchangers 1 and 10 described above, the number of parts, the number of joints, and the number of manufacturing steps are large, and the brazing operation is required. Therefore, the manufacturing takes time and the manufacturing cost is reduced. There is a problem that fluid leakage is likely to occur.

また、前者の熱交換器1の場合には、波形フィン2とプレート3を積層し、一体でロー付けする構造となっており、一層単位で検圧をすることができないため、漏洩等の不良箇所を検出することが難しく、製品の信頼性の向上が図り難いといった問題があった。   In the case of the former heat exchanger 1, the corrugated fins 2 and the plate 3 are laminated and integrally brazed, and the pressure cannot be detected in units of one unit. There is a problem that it is difficult to detect the location and it is difficult to improve the reliability of the product.

さらに、後者の熱交換器10の場合、流路14への出入口管17が外管11の長面16側に接続されているため、出入口管17接続箇所の反対側部分18に流体が十分に廻らず、流路14内の流量分布が不均一となり、熱交換能力が不足するおそれがあった。   Furthermore, in the case of the latter heat exchanger 10, the inlet / outlet pipe 17 to the flow path 14 is connected to the long surface 16 side of the outer pipe 11, so that there is sufficient fluid in the portion 18 on the opposite side of the connecting / exiting pipe 17 connection location. There was a risk that the flow distribution in the flow path 14 would not be uniform and the heat exchange capacity would be insufficient.

本発明は、上記した課題を解決すべくなされたものであり、部品点数、接合箇所、及び製作工数を削減でき、製品の信頼性及び熱交換性能の向上を図ることのできる熱交換器及びその製造方法を提供するものである。   The present invention has been made to solve the above-described problems, and can reduce the number of parts, joint locations, and manufacturing man-hours, and can improve the reliability and heat exchange performance of the product and its heat exchanger. A manufacturing method is provided.

本発明に係る熱交換器は、扁平な外管に扁平な内管を内設した2重管から成る伝熱プレートを備え、前記外管と前記内管との間に形成された流路を流通する流体の出入口がそれぞれ前記外管の短面側に設けられ、前記扁平な2重管は、円筒形状の2重管を同時に押圧し、前記外管と前記内管の各端部同士を接合し、前記流路の両端部を閉塞することにより形成されていることを特徴とする。
A heat exchanger according to the present invention includes a heat transfer plate composed of a double tube in which a flat inner tube is provided in a flat outer tube, and a flow path formed between the outer tube and the inner tube. A fluid inlet / outlet port is provided on the short side of the outer pipe, and the flat double pipe presses the cylindrical double pipe at the same time, and connects the ends of the outer pipe and the inner pipe to each other. It is formed by joining and closing both ends of the flow path .

また、本発明に係る熱交換器の製造方法は、1枚のプレートから1個の円筒体を形成する工程と、該円筒体を押圧し、扁平な筒体を形成する工程と、該扁平な筒体の両端部を閉塞する工程と、前記扁平な筒体の内部を流通する流体の出入口を前記扁平な筒体の短面側に形成する工程とを備えていることを特徴とする。   Moreover, the manufacturing method of the heat exchanger according to the present invention includes a step of forming one cylindrical body from one plate, a step of pressing the cylindrical body to form a flat cylindrical body, The method includes a step of closing both end portions of the cylindrical body, and a step of forming an inlet / outlet of a fluid flowing through the inside of the flat cylindrical body on a short surface side of the flat cylindrical body.

さらに、本発明に係る熱交換器の製造方法は、2枚のプレートから円筒状の2重管を形成する工程と、該円筒状の2重管を同時に押圧し、扁平な2重管を形成する工程と、該扁平な2重管の外管と内管の各端部同士を接合し、前記外管と前記内管との間に形成された流路の両端部を閉塞する工程と、短面側の流路がタンクとして機能可能なように前記流路の出入口を前記外管の短面側に形成する工程とを備えていることを特徴とする。
Furthermore, the method for manufacturing a heat exchanger according to the present invention includes a step of forming a cylindrical double tube from two plates, and simultaneously pressing the cylindrical double tube to form a flat double tube. Joining the ends of the outer tube and the inner tube of the flat double tube, and closing both ends of the flow path formed between the outer tube and the inner tube; And a step of forming an inlet / outlet of the channel on the short surface side of the outer tube so that the channel on the short side can function as a tank .

本発明に係る熱交換器によれば、流路内の流量分布を均一に保つことができるため、熱交換性能を向上させることができる。   According to the heat exchanger according to the present invention, since the flow rate distribution in the flow path can be kept uniform, the heat exchange performance can be improved.

また、本発明に係る熱交換器の製造方法によれば、部品点数、接合箇所、及び製作工数を削減でき、製作コストの低減化が可能となる。さらに、漏洩の発生を抑制でき、検圧を確実に行うことができるため、製品の信頼性を向上させることができる等種々の優れた効果を得ることができる。   Moreover, according to the manufacturing method of the heat exchanger which concerns on this invention, a number of parts, a joining location, and manufacturing man-hours can be reduced, and reduction of manufacturing cost is attained. Furthermore, since the occurrence of leakage can be suppressed and the pressure can be reliably detected, various excellent effects such as improvement of product reliability can be obtained.

以下、図面を参照しつつ、本発明の実施の形態について説明する。以下の説明では、本発明を排熱回収型熱交換器に適用した場合について説明する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. In the following description, the case where the present invention is applied to an exhaust heat recovery type heat exchanger will be described.

図1及び図2はその排熱回収型熱交換器21を示しており、排熱回収型熱交換器21には、平板状の伝熱プレート22が積層されている。伝熱プレート22は、扁平な外管23に扁平な内管24を内設した2重管25から成り、外管23と内管24の間に扁平な筒状の空気流路26(図3(b)参照)が形成されている。それぞれの伝熱プレート22の間及び伝熱プレート22の内管24内には、排ガス流路27が形成され、排ガス流路27には伝熱効率を高めるためそれぞれ波形フィン28が挿入されている。伝熱プレート22の外管23の短面29側には対角を成す位置に、絞り加工により形成されたノズル30が取付けられ、ノズル30にはヘッダープレート31を介してそれぞれ空気入口ヘッダー32、空気出口ヘッダー33が取付けられている。また、伝熱プレート22の両端部には、それぞれ排ガス入口ヘッダー34、排ガス出口ヘッダー35が取付けられている。   FIGS. 1 and 2 show the exhaust heat recovery type heat exchanger 21, and a flat heat transfer plate 22 is laminated on the exhaust heat recovery type heat exchanger 21. The heat transfer plate 22 includes a double tube 25 in which a flat inner tube 24 is provided in a flat outer tube 23, and a flat cylindrical air flow path 26 (see FIG. 3) between the outer tube 23 and the inner tube 24. (B) is formed. Exhaust gas flow paths 27 are formed between the heat transfer plates 22 and in the inner pipe 24 of the heat transfer plates 22, and corrugated fins 28 are inserted into the exhaust gas flow paths 27 in order to increase heat transfer efficiency. Nozzles 30 formed by drawing are attached to diagonal positions on the short surface 29 side of the outer tube 23 of the heat transfer plate 22, and the nozzles 30 are respectively provided with air inlet headers 32, An air outlet header 33 is attached. Further, an exhaust gas inlet header 34 and an exhaust gas outlet header 35 are attached to both ends of the heat transfer plate 22, respectively.

このような構成において、高温の排ガスは、排ガス入口ヘッダー34を介して排ガス流路27内を流通し、空気入口ヘッダー32を介して空気流路26内を流通する空気と熱交換を行う。この結果、空気は、高温の排ガスから熱を回収し、空気出口ヘッダー33を介して所定の場所に供給され、低温となった排ガスは、排ガス出口ヘッダー35を介して外部に排出される。この場合、ノズル30が外管23の短面29側に取付けられており、短面29側の空気流路26がタンクとして機能するため、空気流路26内を均一に空気が分布し、熱交換性能の向上を図ることができる。   In such a configuration, the high-temperature exhaust gas flows through the exhaust gas flow path 27 via the exhaust gas inlet header 34 and exchanges heat with the air flowing through the air flow path 26 via the air inlet header 32. As a result, the air recovers heat from the high-temperature exhaust gas and is supplied to a predetermined location via the air outlet header 33, and the exhaust gas that has become low temperature is discharged to the outside via the exhaust gas outlet header 35. In this case, since the nozzle 30 is attached to the short surface 29 side of the outer tube 23 and the air flow path 26 on the short surface 29 functions as a tank, air is uniformly distributed in the air flow path 26, The exchange performance can be improved.

次に、図1及び図3を参照しつつ、排熱回収型熱交換器21の製造方法について説明する。   Next, a method for manufacturing the exhaust heat recovery type heat exchanger 21 will be described with reference to FIGS. 1 and 3.

図3(a)に示すように、各1枚のプレートをそれぞれ円筒状に曲成し、その各周縁部36,37をそれぞれ溶接接合し、円筒状の外管23及び内管24を形成させた後、外管23に内管24を内設させ、円筒状の2重管25を形成させる。その2重管25を押圧し、図3(b)に示すように、扁平な筒状に加工し、外管23の短面29側の対角を成す位置にノズル30を溶接接合すると共に、外管23と内管24の両端部を溶接接合し、空気流路26の両端部を閉塞させる。その後、このようにして形成した伝熱プレート22を波形フィン28と交互に積層し、内管24に波形フィン28を挿入し、ノズル30にヘッダープレート31を介して空気入口ヘッダー32、空気出口ヘッダー33を取付けると共に、伝熱プレート22の両端部に排ガス入口ヘッダー34、排ガス出口ヘッダー35を取付ける。   As shown in FIG. 3 (a), each plate is bent into a cylindrical shape, and its peripheral portions 36 and 37 are welded to form cylindrical outer tube 23 and inner tube 24, respectively. After that, the inner tube 24 is provided in the outer tube 23 to form a cylindrical double tube 25. As shown in FIG. 3 (b), the double pipe 25 is pressed, processed into a flat cylindrical shape, and the nozzle 30 is welded and joined to the diagonal position on the short surface 29 side of the outer pipe 23, Both ends of the outer tube 23 and the inner tube 24 are welded and joined, and both ends of the air flow path 26 are closed. Thereafter, the heat transfer plates 22 thus formed are alternately laminated with the corrugated fins 28, the corrugated fins 28 are inserted into the inner tube 24, and the air inlet header 32 and the air outlet header are inserted into the nozzle 30 via the header plate 31. 33 and the exhaust gas inlet header 34 and the exhaust gas outlet header 35 are attached to both ends of the heat transfer plate 22.

このように、外管23及び内管24をそれぞれ1枚のプレートから同時に形成することができるため、部品点数及び接合箇所を削減することができ、また、ロウ付けを行わずに、溶接接合だけで製作することもできる。そのため、製作工数を削減でき、製作コストの低減化が可能となり、また、流体の漏洩の発生を抑制することもできる。さらに、伝熱プレート22単位で検圧することができるので、不良箇所を事前に確実に発見することができ、製品の信頼性を向上させることができる。さらにまた、伝熱プレート22の積層数の変更にも容易に対応でき、伝熱プレート22のサイズも容易に変更できるため、製品の設計変更にも柔軟に対応することができる。   As described above, since the outer tube 23 and the inner tube 24 can be simultaneously formed from one plate, the number of parts and the joint location can be reduced, and only the welding joint is performed without brazing. Can also be produced. Therefore, the number of manufacturing steps can be reduced, the manufacturing cost can be reduced, and the occurrence of fluid leakage can be suppressed. Furthermore, since the pressure can be detected in units of the heat transfer plate 22, a defective portion can be surely found in advance, and the reliability of the product can be improved. Furthermore, since the number of stacked heat transfer plates 22 can be easily changed and the size of the heat transfer plate 22 can be easily changed, it is possible to flexibly cope with a change in product design.

なお、上記実施の形態では、伝熱プレート22が2重管25から成る場合について説明したが、本発明は、図4(a)及び(b)に示すように、単管38の場合にも実施可能である。また、ノズル30の取付位置は、短面29側であれば、対角を成す位置に限定されるものではなく、例えば、図4(b)に示すように、互いに同一側に設けられていてもよい。   In the above embodiment, the case where the heat transfer plate 22 is composed of the double tube 25 has been described. However, the present invention can be applied to the case of the single tube 38 as shown in FIGS. 4 (a) and 4 (b). It can be implemented. Further, the mounting position of the nozzle 30 is not limited to the diagonal position as long as it is on the short surface 29 side, and is provided on the same side as shown in FIG. 4B, for example. Also good.

さらに、外管23及び内管24は、波形に成形したウェーブプレートを用いて製作してもよい。この場合、排ガス流路27に波形フィン28を挿入しなくても熱交換性能を十分高めることができるので、部品点数をさらに削減することができ、上記した効果をより一層高めることができる。   Furthermore, you may manufacture the outer tube | pipe 23 and the inner tube | pipe 24 using the wave plate shape | molded in the waveform. In this case, since the heat exchange performance can be sufficiently enhanced without inserting the corrugated fins 28 into the exhaust gas flow path 27, the number of parts can be further reduced, and the above-described effects can be further enhanced.

さらにまた、上記実施の形態では、排熱回収型熱交換器21について説明したが、これは単なる例示であり、本発明は、オイルクーラやインタークーラ等、他の熱交換器にも適用可能であり、熱交換される流体は、液体同士、或いは、液体と気体であってもよい。   Furthermore, in the above-described embodiment, the exhaust heat recovery type heat exchanger 21 has been described. However, this is merely an example, and the present invention can be applied to other heat exchangers such as an oil cooler and an intercooler. The fluid to be heat exchanged may be liquids or liquids and gases.

本発明の実施の形態に係る熱交換器を示す分解斜視図である。It is a disassembled perspective view which shows the heat exchanger which concerns on embodiment of this invention. 本発明の実施の形態における伝熱プレートを示す正面図である。It is a front view which shows the heat-transfer plate in embodiment of this invention. (a)及び(b)は共に、本発明の実施の形態に係る熱交換器の製作手順を示す斜視図である。(A) And (b) is a perspective view which shows the manufacture procedure of the heat exchanger which concerns on embodiment of this invention together. (a)及び(b)は共に、本発明の実施の形態に係る他の熱交換器の製作手順を示す斜視図である。(A) And (b) is a perspective view which shows the manufacture procedure of the other heat exchanger which concerns on embodiment of this invention. 従来例を示す斜視図である。It is a perspective view which shows a prior art example. 他の従来例を示す正面図である。It is a front view which shows another prior art example.

符号の説明Explanation of symbols

21 排熱回収型熱交換器
22 伝熱プレート
23 外管
24 内管
25 2重管
26 空気流路
29 短面
21 Heat recovery type heat exchanger 22 Heat transfer plate 23 Outer pipe 24 Inner pipe 25 Double pipe 26 Air flow path 29 Short face

Claims (2)

扁平な外管に扁平な内管を内設した扁平な2重管から成る伝熱プレートを備え、前記外管と前記内管との間に形成された流路を流通する流体の出入口がそれぞれ前記外管の短面側に設けられ、前記扁平な2重管は、円筒形状の2重管を同時に押圧し、前記外管と前記内管の各端部同士を接合し、前記流路の両端部を閉塞することにより形成されていることを特徴とする熱交換器。 A heat transfer plate comprising a flat double tube in which a flat inner tube is provided in a flat outer tube, and an inlet / outlet for fluid flowing through a flow path formed between the outer tube and the inner tube, respectively Provided on the short surface side of the outer pipe, the flat double pipe presses the cylindrical double pipe at the same time, joins the ends of the outer pipe and the inner pipe, and A heat exchanger characterized by being formed by closing both ends . 2枚のプレートから円筒状の2重管を形成する工程と、
該円筒状の2重管を同時に押圧し、扁平な2重管を形成する工程と、
該扁平な2重管の外管と内管の各端部同士を接合し、前記外管と前記内管との間に形成された流路の両端部を閉塞する工程と、
短面側の流路がタンクとして機能するように前記流路の出入口を前記外管の短面側に形成する工程と、
を備えていることを特徴とする熱交換器の製造方法。
Forming a cylindrical double tube from two plates;
Simultaneously pressing the cylindrical double pipe to form a flat double pipe;
Joining each end of the outer tube and the inner tube of the flat double tube, and closing both ends of a flow path formed between the outer tube and the inner tube;
Forming the inlet / outlet of the flow path on the short face side of the outer pipe so that the short face side flow path functions as a tank;
A method for producing a heat exchanger, comprising:
JP2003305894A 2003-08-29 2003-08-29 Heat exchanger and manufacturing method thereof Expired - Fee Related JP4221260B2 (en)

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KR100943783B1 (en) 2008-06-17 2010-02-23 (주)귀뚜라미 Boiler heat exchanger of double block and boiler heat exchanger including the same
KR101011972B1 (en) 2010-10-05 2011-01-31 정희철 Fin block-unit for heat exchanger and method of manufacturing the same
CN107940737B (en) * 2017-09-25 2021-02-05 汤海明 Dry-type no fin vortex heat exchange device
CN109520354B (en) * 2018-12-17 2021-11-30 青岛钛钽铌锆连续化反应器有限公司 Reaction/mixing/heat exchange tube and reactor

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