JP2010065892A - Heat exchanger - Google Patents

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Publication number
JP2010065892A
JP2010065892A JP2008231405A JP2008231405A JP2010065892A JP 2010065892 A JP2010065892 A JP 2010065892A JP 2008231405 A JP2008231405 A JP 2008231405A JP 2008231405 A JP2008231405 A JP 2008231405A JP 2010065892 A JP2010065892 A JP 2010065892A
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Prior art keywords
heat exchanger
water guide
flat
water
flat tube
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Japanese (ja)
Inventor
Hirokazu Fujino
宏和 藤野
Genei Kin
鉉永 金
Haruo Nakada
春男 中田
Toshimitsu Kamata
俊光 鎌田
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Daikin Industries Ltd
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Daikin Industries Ltd
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Priority to JP2008231405A priority Critical patent/JP2010065892A/en
Publication of JP2010065892A publication Critical patent/JP2010065892A/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F17/00Removing ice or water from heat-exchange apparatus
    • F28F17/005Means for draining condensates from heat exchangers, e.g. from evaporators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular 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
    • F28F1/126Tubular 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
    • F28F1/128Fins with openings, e.g. louvered fins

Abstract

<P>PROBLEM TO BE SOLVED: To provide a heat exchanger having improved water drainage performance with respect to condensation water. <P>SOLUTION: In the heat exchanger 10, flat tubes 11 are arranged at a plurality of stages with plane parts 11a facing vertically. Corrugated fins 12 are arranged in ventilation spaces sandwiched between the flat tubes 11 vertically adjacent to each other. Water introduction parts 13 are arranged outside the ventilation spaces and extended to the vertical direction while connected to the flat tubes 11. In the water introduction parts 13 vertically adjacent to each other, the lower part of the water introduction part 13 positioned on the upper side is brought into contact with the upper part of the water introduction part 13 positioned on the lower side. Due to this structure, condensation water is easily made to flow downwardly via the water introduction parts 13, so as to improve water drainage. <P>COPYRIGHT: (C)2010,JPO&amp;INPIT

Description

本発明は、扁平管とフィンとを備えた熱交換器に関する。   The present invention relates to a heat exchanger provided with flat tubes and fins.

従来、扁平管の平面部を水平にし、平面部と平面部との間にフィンを配置した熱交換器が広く普及している。このような熱交換器では、フィンが扁平管によって分断されているので、結露水が滞留して通風抵抗となる。この結露水の滞留を解消するために、フィンの端部から突出部を空気流の下流側へ突出させ、その突出部に切り欠きを設けた熱交換器が提供されている(特許文献1参照)。特許文献1に開示されている熱交換器によれば、発生した結露水は、空気流に押されて下流側に集まり、切り欠きを通って下方へ落下する。   Conventionally, a heat exchanger in which a flat portion of a flat tube is horizontal and fins are disposed between the flat portion and the flat portion has been widely used. In such a heat exchanger, since the fins are divided by the flat tube, the condensed water stays and becomes ventilation resistance. In order to eliminate the retention of the condensed water, a heat exchanger is provided in which a protrusion is protruded from the end of the fin to the downstream side of the air flow, and a notch is provided in the protrusion (see Patent Document 1). ). According to the heat exchanger disclosed in Patent Document 1, the generated condensed water is pushed by the air flow, gathers on the downstream side, and falls downward through the notch.

しかしながら、上記のような熱交換器では、結露水が切り欠きから落下するのは、結露水が自重で落下できる程度の大きさまで成長したときであって、周期的に結露水が熱交換器に滞留することがあり、結露水に対する水はけ性は低い。また、熱交換器の小型化がさらに進む状況下において、熱交換器の小型化は結露水に対する熱交換器の水はけ性を低下させる可能性が高いので、さらなる水はけ性の向上が求められている。
実公昭63−6632号公報
However, in the heat exchanger as described above, the condensed water falls from the notch when the condensed water has grown to a size that can be dropped by its own weight, and the condensed water periodically enters the heat exchanger. It may stay, and the drainage of condensed water is low. In addition, in a situation where further downsizing of the heat exchanger is progressing, the downsizing of the heat exchanger is likely to reduce the drainability of the heat exchanger with respect to the dew condensation water, so further improvement in drainage is required. .
Japanese Utility Model Publication No. 63-6632

本発明の課題は、結露水に対する水はけ性を向上させた熱交換器を提供することにある。   The subject of this invention is providing the heat exchanger which improved the drainage property with respect to dew condensation water.

第1発明に係る熱交換器は、扁平管とフィンと導水部とを備えている。扁平管は、平面部を上下方向に向けた状態で複数段配列されている。フィンは、上下に隣接する扁平管に挟まれた通風空間に配置されている。導水部は、通風空間から外れた外側空間に配置され、扁平管と繋がった状態で上方向及び/又は下方向に延びている。上下に隣接する導水部では、上側に位置する導水部の下部が、下側に位置する導水部の上部と接触している。   The heat exchanger according to the first aspect of the present invention includes a flat tube, fins, and a water conduit. The flat tubes are arranged in a plurality of stages in a state where the plane portion is directed in the vertical direction. The fins are arranged in a ventilation space sandwiched between flat tubes adjacent vertically. The water guide portion is disposed in an outer space that is out of the ventilation space, and extends upward and / or downward in a state of being connected to the flat tube. In the water guide section adjacent vertically, the lower part of the water guide section located on the upper side is in contact with the upper part of the water guide section located on the lower side.

この熱交換器では、上下に隣接する導水部同士が接触しているので、フィン表面の結露水が導水部を介して下方へ流れ易く、水はけがよい。   In this heat exchanger, since the water guide portions adjacent in the vertical direction are in contact with each other, the condensed water on the fin surface easily flows downward through the water guide portion, and drainage is good.

第2発明に係る熱交換器は、第1発明に係る熱交換器であって、導水部が扁平管と一体である。この熱交換器では、部品点数および作業工数が低減されるので、製造コストの増大が抑制される。   A heat exchanger according to a second aspect of the present invention is the heat exchanger according to the first aspect of the present invention, wherein the water conduit is integral with the flat tube. In this heat exchanger, since the number of parts and the number of work steps are reduced, an increase in manufacturing cost is suppressed.

第3発明に係る熱交換器は、第2発明に係る熱交換器であって、扁平管には、当初外側空間に向って延びる突出部が形成されている。導水部は、突出部が上下方向に捩じられることによって形成されている。この熱交換器では、加工が単純であり生産性が向上する。   A heat exchanger according to a third aspect of the present invention is the heat exchanger according to the second aspect of the present invention, wherein the flat tube is initially formed with a protruding portion extending toward the outer space. The water guide portion is formed by twisting the protruding portion in the vertical direction. In this heat exchanger, processing is simple and productivity is improved.

第4発明に係る熱交換器は、第1発明に係る熱交換器であって、導水部が扁平管に接触する板状部材であり扁平管及びフィンから独立している。この熱交換器では、導水部が板状であるので、幅、長さ及び傾斜角度の調節が容易である。   A heat exchanger according to a fourth aspect of the present invention is the heat exchanger according to the first aspect of the present invention, wherein the water guide portion is a plate-like member that contacts the flat tube and is independent of the flat tube and the fin. In this heat exchanger, since the water guide is plate-shaped, the width, length, and inclination angle can be easily adjusted.

第5発明に係る熱交換器は、第4発明に係る熱交換器であって、導水部が扁平管の平面部とフィンとに挟まれている。この熱交換器では、扁平管、フィン及び導水部の接合を同時に行なうことができるので、製造コストの増大が抑制される。   A heat exchanger according to a fifth aspect of the present invention is the heat exchanger according to the fourth aspect of the present invention, wherein the water conduit is sandwiched between the flat portion of the flat tube and the fins. In this heat exchanger, since the flat tube, the fin, and the water guide portion can be joined at the same time, an increase in manufacturing cost is suppressed.

第1発明に係る熱交換器では、上下に隣接する導水部同士が接触しているので、フィン表面の結露水が導水部を介して下方へ流れ易く、水はけがよい。   In the heat exchanger according to the first aspect of the invention, since the water guide portions adjacent in the vertical direction are in contact with each other, the dew condensation water on the fin surface easily flows downward through the water guide portion, and the drainage is good.

第2発明に係る熱交換器では、部品点数および作業工数が低減されるので、製造コストの増大が抑制される。   In the heat exchanger according to the second invention, the number of parts and the number of work steps are reduced, so that an increase in manufacturing cost is suppressed.

第3発明に係る熱交換器では、加工が単純であり生産性が向上する。   In the heat exchanger according to the third invention, the processing is simple and the productivity is improved.

第4発明に係る熱交換器では、導水部が板状であるので、幅、長さ及び傾斜角度の調節が容易である。   In the heat exchanger according to the fourth aspect of the present invention, since the water guide portion is plate-shaped, it is easy to adjust the width, length, and inclination angle.

第5発明に係る熱交換器では、扁平管、フィン及び導水部の接合を同時に行なうことができるので、製造コストの増大が抑制される。   In the heat exchanger according to the fifth aspect of the present invention, the flat tube, the fins, and the water guide portion can be joined at the same time, so that an increase in manufacturing cost is suppressed.

以下図面を参照しながら、本発明の実施形態について説明する。なお、以下の実施形態は、本発明の具体例であって、本発明の技術的範囲を限定するものではない。   Embodiments of the present invention will be described below with reference to the drawings. The following embodiments are specific examples of the present invention and do not limit the technical scope of the present invention.

<熱交換器10の構成>
図1は、本発明の一実施形態に係る熱交換器の斜視図であり、図2は、扁平管の長手方向と垂直な平面における熱交換器の断面図である。図1、図2において、熱交換器10は、扁平管11、波形フィン12、導水部13及びヘッダ15を備えている。
<Configuration of heat exchanger 10>
FIG. 1 is a perspective view of a heat exchanger according to an embodiment of the present invention, and FIG. 2 is a cross-sectional view of the heat exchanger in a plane perpendicular to the longitudinal direction of the flat tube. 1 and 2, the heat exchanger 10 includes a flat tube 11, a corrugated fin 12, a water guide portion 13, and a header 15.

(扁平管11)
扁平管11は、アルミニウムまたはアルミニウム合金から成形されており、伝熱面となる平面部11aと、冷媒が流れる複数の冷媒流路11bを有している(図2参照)。図2に示すように、扁平管11は、平面部11aを上下に向けた状態で複数段配列されている。
(Flat tube 11)
The flat tube 11 is formed from aluminum or an aluminum alloy, and includes a flat portion 11a serving as a heat transfer surface and a plurality of refrigerant flow paths 11b through which a refrigerant flows (see FIG. 2). As shown in FIG. 2, the flat tubes 11 are arranged in a plurality of stages with the flat surface portion 11a facing up and down.

(波形フィン12)
波形フィン12は、波形に折り曲げられたアルミニウム製またはアルミニウム合金製のフィンである。図2に示すように、波形フィン12は、上下に隣接する扁平管11に挟まれた通風空間に配置され、谷部及び山部が扁平管11の平面部11aと接触している。なお、谷部と山部と平面部11aとはロウ付け溶接されている。
(Waveform fin 12)
The corrugated fin 12 is a fin made of aluminum or aluminum alloy bent into a corrugated shape. As shown in FIG. 2, the corrugated fins 12 are arranged in a ventilation space sandwiched between upper and lower flat tubes 11, and a valley portion and a mountain portion are in contact with a flat portion 11 a of the flat tube 11. In addition, the trough part, the peak part, and the plane part 11a are brazed and welded.

伝熱面12aは、通風空間を通過する空気流Aと熱交換する部分であり、効率よく熱交換を行うためのルーバー12cを有している。ルーバー12cは、伝熱面12aの一方の面から他方の面へ貫通する開口を形成している。説明の便宜上、図2正面視において、伝熱面12aの正面を「第1面」、背面を「第2面」と呼ぶ。伝熱面12aの中央から上流側に位置するルーバー12c群は、空気流が第2面からから第1面へ流れるように傾いており、伝熱面12aの中央から下流側に位置するルーバー12c群は、空気流が第1面からから第2面へ流れるように傾いている。   The heat transfer surface 12a is a part that exchanges heat with the airflow A that passes through the ventilation space, and has a louver 12c for efficiently exchanging heat. Louver 12c forms an opening penetrating from one surface of heat transfer surface 12a to the other surface. For convenience of explanation, in the front view of FIG. 2, the front surface of the heat transfer surface 12 a is referred to as “first surface” and the back surface is referred to as “second surface”. The louver 12c group located upstream from the center of the heat transfer surface 12a is inclined so that the air flow flows from the second surface to the first surface, and the louver 12c located downstream from the center of the heat transfer surface 12a. The group is tilted so that the airflow flows from the first surface to the second surface.

(導水部13)
導水部13は、上下に隣接する扁平管11に挟まれた通風空間の外側に位置し、導水部13の長手方向は上下方向に延び、導水部13の幅方向は空気流Aと平行に延びている。上下方向に隣接する導水部13では、上側に位置する導水部13の下部が、下側に位置する導水部13の上部と近接し、又は接触している。
(Water guide 13)
The water guide portion 13 is located outside the ventilation space sandwiched between the vertically adjacent flat tubes 11, the longitudinal direction of the water guide portion 13 extends in the vertical direction, and the width direction of the water guide portion 13 extends in parallel with the air flow A. ing. In the water guide part 13 adjacent to the up-down direction, the lower part of the water guide part 13 located on the upper side is close to or in contact with the upper part of the water guide part 13 located on the lower side.

導水部13は、扁平管11の上側の平面部11aと接触しており、本実施形態では、扁平管11の上側の平面部11aと一体成形されている。以下図面を用いて、扁平管11と導水部13の製造方法について説明する。   The water guide portion 13 is in contact with the upper flat portion 11a of the flat tube 11, and is integrally formed with the upper flat portion 11a of the flat tube 11 in this embodiment. Hereinafter, the manufacturing method of the flat tube 11 and the water guide part 13 is demonstrated using drawing.

図3は製造途中の扁平管の断面図である。図3において、工程P1では、複数の凹溝状の冷媒流路11bが形成された扁平容器11vと、平面部11aと導水部13とを有する平板11pとが張り合わされる。工程P2では、扁平容器11vと平板11pとがロウ付け溶接によって結合される。   FIG. 3 is a cross-sectional view of a flat tube being manufactured. In FIG. 3, in step P <b> 1, the flat container 11 v in which a plurality of concave groove-like refrigerant channels 11 b are formed and the flat plate 11 p having the flat portion 11 a and the water guide portion 13 are bonded together. In the process P2, the flat container 11v and the flat plate 11p are joined by brazing welding.

工程P3では、導水部13が上下方向を向くように、平面部11aとの連結部11jを中心に捩じられる。ここで、導水部13が捩じられる前の平板11pの平面状態について説明する。図4は、製造途中の扁平管の平板の平面図である。図4において、平板11pでは、平面部11aと導水部13とは、連結部11jによって繋がっているだけであり、連結部11j以外は切り込み線11sによって分断されている。また、隣接する導水部13同士も切り込み線11sで分断されている。このように、導水部13は、連結部11jを中心に容易に捩じられる。本実施形態では、導水部13は、連結部11jを中心にほぼ90°捩じられるので、導水部13は鉛直方向とほぼ平行である。   In the process P3, the water guide 13 is twisted around the connecting portion 11j with the flat surface portion 11a so as to face in the vertical direction. Here, the planar state of the flat plate 11p before the water guide portion 13 is twisted will be described. FIG. 4 is a plan view of a flat plate of a flat tube being manufactured. In FIG. 4, in the flat plate 11p, the plane part 11a and the water guide part 13 are only connected by the connection part 11j, and other than the connection part 11j is divided by the cut line 11s. Adjacent water guide portions 13 are also separated by a cut line 11s. Thus, the water guide part 13 is easily twisted around the connection part 11j. In this embodiment, since the water guide part 13 is twisted about 90 degrees centering on the connection part 11j, the water guide part 13 is substantially parallel to the perpendicular direction.

(ヘッダ15)
図1において、ヘッダ15は、上下方向に複数段配列された扁平管11の両端に連結されている。説明の便宜上、図1の正面視右側のヘッダを「第1ヘッダ151」と呼び、左側のヘッダを「第2ヘッダ152」と呼ぶ。第1ヘッダ151及び第2ヘッダ152は、扁平管11を支持する機能と、冷媒を扁平管11の冷媒流路11bに導く機能と、冷媒流路11bから出てきた冷媒を集合させる機能とを有している。
(Header 15)
In FIG. 1, the header 15 is connected to both ends of flat tubes 11 arranged in a plurality of stages in the vertical direction. For convenience of explanation, the header on the right side in FIG. 1 is called “first header 151”, and the header on the left side is called “second header 152”. The first header 151 and the second header 152 have a function of supporting the flat tube 11, a function of guiding the refrigerant to the refrigerant flow path 11b of the flat pipe 11, and a function of collecting the refrigerant that has come out of the refrigerant flow path 11b. Have.

(冷媒の流れ)
図1において、第1ヘッダ151の入口151aから流入した冷媒は、最上段の扁平管11の各冷媒流路11bへほぼ均等に分配され第2ヘッダ152に向って流れる。第2ヘッダ152に達した冷媒は、2段目の扁平管11の各冷媒流路11bへ均等に分配され第1ヘッダ151へ向って流れる。以降、奇数段目の扁平管11内の冷媒は、第2ヘッダ152へ向って流れ、偶数段目の扁平管11内の冷媒は、第1ヘッダ151に向って流れる。そして、最下段で且つ偶数段目の扁平管11内の冷媒は、第1ヘッダ151に向って流れ、第1ヘッダ151で集合し出口151bから流出する。
(Refrigerant flow)
In FIG. 1, the refrigerant flowing from the inlet 151 a of the first header 151 is distributed almost evenly to the respective refrigerant flow paths 11 b of the uppermost flat tube 11 and flows toward the second header 152. The refrigerant reaching the second header 152 is evenly distributed to the respective refrigerant flow paths 11b of the second-stage flat tube 11 and flows toward the first header 151. Thereafter, the refrigerant in the odd-numbered flat tubes 11 flows toward the second header 152, and the refrigerant in the even-numbered flat tubes 11 flows toward the first header 151. And the refrigerant | coolant in the flat tube 11 of the lowest level and the even-numbered level flows toward the 1st header 151, gathers at the 1st header 151, and flows out from the exit 151b.

熱交換器10が蒸発器として機能するとき、冷媒流路11bを流れる冷媒は、波形フィン12を介して通風空間を流れる空気流から吸熱する。熱交換器10が凝縮器として機能するときは、冷媒流路11bを流れる冷媒は、波形フィン12を介して通風空間を流れる空気流へ放熱する。   When the heat exchanger 10 functions as an evaporator, the refrigerant flowing through the refrigerant flow path 11b absorbs heat from the air flow flowing through the ventilation space via the corrugated fins 12. When the heat exchanger 10 functions as a condenser, the refrigerant flowing through the refrigerant flow path 11b radiates heat to the air flow flowing through the ventilation space via the corrugated fins 12.

(結露水の流れ)
一般に、扁平管11が平面部11aを上下に向けて配列されているとき、熱交換器表面の水はけが悪く、蒸発器として利用した場合、滞留した結露水が空気流Aの抵抗となり熱交換性能が低下することがある。しかし、本実施形態の熱交換器10では、図1、図2に示すように、導水部13があるので、結露水は導水部13を介して下方へ流れる。以下、結露水の流れについて図面を用いて説明する。
(Flow of condensed water)
In general, when the flat tubes 11 are arranged with the flat portion 11a facing up and down, the water on the surface of the heat exchanger is poorly drained, and when used as an evaporator, the accumulated condensed water becomes the resistance of the air flow A and heat exchange performance. May decrease. However, in the heat exchanger 10 of this embodiment, as shown in FIG. 1 and FIG. 2, since there is a water guide portion 13, the condensed water flows downward through the water guide portion 13. Hereinafter, the flow of condensed water will be described with reference to the drawings.

図2において、波形フィン12の伝熱面12aで発生した結露水Wは、重力によって伝熱面12aを降下しながら、空気流Aに押されて下流側へ移動する。波形フィン12の谷部へ降下した結露水も空気流Aに押されて下流側へ移動する。また、波形フィン12の谷部と扁平管11の平面部11aとの隙間に侵入した結露水は、その隙間による毛細管現象と空気流Aの風圧とによって下流側へ移動する。そして、波形フィン12の下流側端部に達した結露水は、空気流Aに押されて通風空間の外側に位置する導水部13へ移動し、導水部13に沿ってさらに下方の導水部13へ移動する。   In FIG. 2, the dew condensation water W generated on the heat transfer surface 12a of the corrugated fin 12 is pushed by the air flow A and moves downstream while descending the heat transfer surface 12a by gravity. Condensed water descending to the valleys of the corrugated fins 12 is also pushed by the air flow A and moves downstream. In addition, the dew condensation water that has entered the gap between the valley of the corrugated fin 12 and the flat portion 11a of the flat tube 11 moves downstream due to the capillary phenomenon caused by the gap and the wind pressure of the airflow A. The condensed water that has reached the downstream end of the corrugated fin 12 is pushed by the air flow A and moves to the water guide section 13 located outside the ventilation space, and further along the water guide section 13, the water guide section 13 further below. Move to.

<特徴>
熱交換器10では、扁平管11は、平面部11aを上下方向に向けた状態で複数段配列されている。波形フィン12は、上下に隣接する扁平管11に挟まれた通風空間に配置されている。導水部13は、通風空間の外側に配置され、扁平管11と繋がった状態で鉛直方向に延びている。上下に隣接する導水部13では、上側に位置する導水部13の下部が、下側に位置する導水部13の上部と接触しているので、結露水が導水部13を介して下方へ流れ易く、水はけがよい。導水部13は扁平管11と一体であるので、部品点数および作業工数が低減され、製造コストの増大が抑制されている。また、導水部13は、扁平管11の上側の平面部11aのうち、通風空間の外側に突出した部分が上下方向に捩じられることによって形成さるので、加工が単純であり生産性が高い。
<Features>
In the heat exchanger 10, the flat tubes 11 are arranged in a plurality of stages with the flat surface portion 11a facing in the vertical direction. The corrugated fins 12 are arranged in a ventilation space sandwiched between flat tubes 11 adjacent in the vertical direction. The water guide portion 13 is disposed outside the ventilation space and extends in the vertical direction in a state of being connected to the flat tube 11. In the water guide part 13 adjacent to the upper and lower sides, the lower part of the water guide part 13 located on the upper side is in contact with the upper part of the water guide part 13 located on the lower side. Well drained. Since the water guide part 13 is integral with the flat tube 11, the number of parts and work man-hours are reduced, and the increase in manufacturing cost is suppressed. Moreover, since the water conveyance part 13 is formed when the part which protruded outside the ventilation space among the plane parts 11a above the flat tube 11 is twisted up and down, processing is simple and productivity is high.

<変形例>
上記実施形態では、導水部13と扁平管11の一部とが一体成形されているが、それに限定されるものではない。以下、図面を参照しながら導水部の変形例について説明する。図5は、変形例に係る熱交換器の斜視図であり、図6は、図5の扁平管の長手方向と垂直な平面における熱交換器の部分断面図である。なお、上記実施形態と同じ部材には、同じ符号を付与して説明を省略する。
<Modification>
In the said embodiment, although the water guide part 13 and a part of flat tube 11 are integrally molded, it is not limited to it. Hereinafter, modified examples of the water guide section will be described with reference to the drawings. FIG. 5 is a perspective view of a heat exchanger according to a modification, and FIG. 6 is a partial cross-sectional view of the heat exchanger in a plane perpendicular to the longitudinal direction of the flat tube of FIG. In addition, the same code | symbol is provided to the same member as the said embodiment, and description is abbreviate | omitted.

(扁平管111)
扁平管111は、アルミニウムまたはアルミニウム合金から成形されており、伝熱面となる平面部111aと、冷媒が流れる複数の冷媒流路111bを有している(図6参照)。扁平管111の平面部111a及び冷媒流路111bは、押し出し加工または引き抜き加工によって一体成形されている。図6に示すように、扁平管111は、平面部111aを上下に向けた状態で複数段配列されている。
(Flat tube 111)
The flat tube 111 is formed from aluminum or an aluminum alloy, and includes a flat portion 111a serving as a heat transfer surface and a plurality of refrigerant channels 111b through which a refrigerant flows (see FIG. 6). The flat portion 111a and the refrigerant flow path 111b of the flat tube 111 are integrally formed by extrusion processing or drawing processing. As shown in FIG. 6, the flat tubes 111 are arranged in a plurality of stages with the flat portion 111 a facing up and down.

(導水部113)
図5、図6において、導水部113は、上下に隣接する扁平管111に挟まれた通風空間の外側に位置し、導水部113の長手方向は鉛直下方に延び、導水部113の幅方向は空気流と平行に延びている。上下方向に隣接する導水部113では、上側に位置する導水部113の下部が、下側に位置する導水部113の上部と近接し、又は接触している。
(Water guide part 113)
5 and 6, the water guide portion 113 is located outside the ventilation space sandwiched between the vertically adjacent flat tubes 111, the longitudinal direction of the water guide portion 113 extends vertically downward, and the width direction of the water guide portion 113 is It extends parallel to the air flow. In the water guide part 113 adjacent to the up-down direction, the lower part of the water guide part 113 located on the upper side is close to or in contact with the upper part of the water guide part 113 located on the lower side.

導水部113は、扁平管111の上側の平面部111aと接触しており、本実施形態では、導水部113の一部が、扁平管111の上側の平面部111aと波形フィン12の谷部との間に挟まれている。以下図面を用いて、導水部113の製造方法について説明する。   The water guide portion 113 is in contact with the upper flat portion 111a of the flat tube 111, and in this embodiment, a part of the water guide portion 113 includes the upper flat portion 111a of the flat tube 111 and the valley portion of the corrugated fin 12. It is sandwiched between. Hereinafter, the manufacturing method of the water conveyance part 113 is demonstrated using drawing.

図7は変形例に係る熱交換器の導水部の素材の平面図である。図7において、導水部113の素材は、導水部113と、扁平管111の平面部111aと波形フィン12の谷部との間に挟まれる保持部114とを有している。導水部113と保持部114とは、連結部114jによって繋がっているだけであり、連結部114j以外は切り込み線114sによって分断されている。また、隣接する導水部113同士も切り込み線114sで分断されている。   FIG. 7 is a plan view of the material of the water guide section of the heat exchanger according to the modification. In FIG. 7, the material of the water guide portion 113 includes the water guide portion 113 and a holding portion 114 sandwiched between the flat portion 111 a of the flat tube 111 and the valley portion of the corrugated fin 12. The water guide part 113 and the holding | maintenance part 114 are only connected by the connection part 114j, and other than the connection part 114j is parted by the cut line 114s. Further, adjacent water guide portions 113 are also separated by a cut line 114s.

図8は、変形例に係る熱交換器の導水部が形成される途中の断面図である。図8において、工程P11では、導水部113と保持部114とに分断されている素材をセットする。導水部113と保持部114とは、連結部114jだけでつながっている。工程P12では、導水部113が鉛直下方を向くように連結部114jを中心にほぼ90°下方へ曲げられる。工程P13では、導水部113の幅方向が保持部114の長手方向と交差するように連結部114jを中心に捩じられる。本実施形態では、導水部13は、連結部114jを中心にほぼ90°捩じられるので、保持部114が扁平管111と波形フィン12に挟まれたとき、導水部113は空気流の方向と平行になる。   FIG. 8 is a cross-sectional view in the middle of formation of the water conduit of the heat exchanger according to the modification. In FIG. 8, in the process P11, the divided material is set to the water guide part 113 and the holding part 114. The water guide part 113 and the holding | maintenance part 114 are connected only by the connection part 114j. In the process P12, the water guide portion 113 is bent downward by approximately 90 ° around the connecting portion 114j so as to face vertically downward. In the process P13, the connecting portion 114j is twisted so that the width direction of the water guide portion 113 intersects the longitudinal direction of the holding portion 114. In the present embodiment, since the water guide portion 13 is twisted by approximately 90 ° around the connecting portion 114j, when the holding portion 114 is sandwiched between the flat tube 111 and the corrugated fins 12, the water guide portion 113 is in the direction of the air flow. Become parallel.

<変形例の特徴>
熱交換器10では、上側に位置する導水部113の下部が、下側に位置する導水部113の上部と接触しているので、結露水が導水部113を介して下方へ流れ易く、水はけがよい。また、導水部113が扁平管111の平面部111aと波形フィン12とに挟まれており、扁平管111、波形フィン12及び導水部113の接合を同時に行なうことができるので、製造コストの増大が抑制される。
<Features of modification>
In the heat exchanger 10, since the lower part of the water guide part 113 located on the upper side is in contact with the upper part of the water guide part 113 located on the lower side, the dew condensation water easily flows downward through the water guide part 113, and the water is damaged. Good. Moreover, since the water guide part 113 is pinched | interposed into the flat part 111a and the corrugated fin 12 of the flat tube 111, since the flat tube 111, the corrugated fin 12, and the water guide part 113 can be performed simultaneously, an increase in manufacturing cost increases. It is suppressed.

以上のように、本発明に係る熱交換器は、扁平管が水平となるように配置された場合でも結露水に対して水はけがよいので、空調機の熱交換器及び自動車のラジエターに有用である。   As described above, the heat exchanger according to the present invention is useful for a heat exchanger of an air conditioner and a radiator of an automobile because water can be drained from the condensed water even when the flat tube is arranged to be horizontal. is there.

本発明の一実施形態に係る熱交換器の斜視図。The perspective view of the heat exchanger which concerns on one Embodiment of this invention. 図1の扁平管の長手方向と垂直な平面における熱交換器の部分断面図。The fragmentary sectional view of the heat exchanger in the plane perpendicular | vertical to the longitudinal direction of the flat tube of FIG. 製造途中の扁平管の断面図。Sectional drawing of the flat tube in the middle of manufacture. 製造途中の扁平管の平板の平面図。The top view of the flat plate of the flat tube in the middle of manufacture. 変形例に係る熱交換器の斜視図。The perspective view of the heat exchanger which concerns on a modification. 図5の扁平管の長手方向と垂直な平面における熱交換器の部分断面図。The fragmentary sectional view of the heat exchanger in the plane perpendicular | vertical to the longitudinal direction of the flat tube of FIG. 変形例に係る熱交換器の導水部の素材の平面図。The top view of the raw material of the water guide part of the heat exchanger which concerns on a modification. 変形例に係る熱交換器の導水部が形成される途中の断面図。Sectional drawing in the middle of the water conveyance part of the heat exchanger which concerns on a modification being formed.

符号の説明Explanation of symbols

10 熱交換器
11,111 扁平管
11a,111a 平面部
12 波形フィン
13,113 導水部
DESCRIPTION OF SYMBOLS 10 Heat exchanger 11,111 Flat tube 11a, 111a Plane part 12 Corrugated fin 13,113 Water conveyance part

Claims (5)

平面部(11a,111a)を上下方向に向けた状態で複数段配列される扁平管(11,111)と、
上下に隣接する前記扁平管(11,111)に挟まれた通風空間に配置されるフィン(12)と、
前記通風空間から外れた外側空間に配置され、前記扁平管(11,111)と繋がった状態で上方向及び/又は下方向に延びる導水部(13,113)と、
を備え、
上下に隣接する前記導水部(13)では、上側に位置する前記導水部(13,113)の下部が、下側に位置する前記導水部(13,113)の上部と接触している、
熱交換器(10)。
Flat tubes (11, 111) arranged in a plurality of stages with the flat portions (11a, 111a) oriented in the vertical direction;
A fin (12) disposed in a ventilation space sandwiched between the flat tubes (11, 111) adjacent vertically;
A water guide section (13, 113) disposed in an outer space outside the ventilation space and extending upward and / or downward while being connected to the flat tube (11, 111);
With
In the water guide part (13) adjacent vertically, the lower part of the water guide part (13, 113) located on the upper side is in contact with the upper part of the water guide part (13, 113) located on the lower side,
Heat exchanger (10).
前記導水部(13)は、前記扁平管(11)と一体である、
請求項1に記載の熱交換器(10)。
The water conduit (13) is integral with the flat tube (11).
The heat exchanger (10) according to claim 1.
前記扁平管(11)には、当初前記外側空間に向って延びる突出部が形成されており、
前記導水部(13)は、前記突出部が上下方向に捩じられることによって形成されている、
請求項2に記載の熱交換器(10)。
The flat tube (11) is initially formed with a protrusion extending toward the outer space,
The water guide portion (13) is formed by twisting the protruding portion in the vertical direction.
The heat exchanger (10) according to claim 2.
前記導水部(113)は、前記扁平管(111)に接触する板状部材であり、前記扁平管(111)及び前記フィン(12)から独立している、
請求項1に記載の熱交換器(10)。
The water guiding portion (113) is a plate-like member that contacts the flat tube (111), and is independent of the flat tube (111) and the fin (12).
The heat exchanger (10) according to claim 1.
前記導水部(113)は、前記扁平管(111)の前記平面部(111a)と前記フィン(12)とに挟まれている、
請求項4に記載の熱交換器(10)。
The water guide portion (113) is sandwiched between the flat portion (111a) and the fin (12) of the flat tube (111).
The heat exchanger (10) according to claim 4.
JP2008231405A 2008-09-09 2008-09-09 Heat exchanger Pending JP2010065892A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (1)

Publication Number Publication Date
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Family

ID=42191624

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013257109A (en) * 2012-06-14 2013-12-26 Fujitsu General Ltd Heat exchanger
CN104296424A (en) * 2014-09-29 2015-01-21 杭州三花微通道换热器有限公司 Heat exchanger
CN106802029A (en) * 2015-11-25 2017-06-06 杭州三花微通道换热器有限公司 Heat exchanger core body and the heat exchanger with it
CN108253834A (en) * 2016-12-28 2018-07-06 丹佛斯微通道换热器(嘉兴)有限公司 Flat tube for heat exchanger and the heat exchanger with the flat tube

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013257109A (en) * 2012-06-14 2013-12-26 Fujitsu General Ltd Heat exchanger
CN104296424A (en) * 2014-09-29 2015-01-21 杭州三花微通道换热器有限公司 Heat exchanger
CN106802029A (en) * 2015-11-25 2017-06-06 杭州三花微通道换热器有限公司 Heat exchanger core body and the heat exchanger with it
CN108253834A (en) * 2016-12-28 2018-07-06 丹佛斯微通道换热器(嘉兴)有限公司 Flat tube for heat exchanger and the heat exchanger with the flat tube

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