JP3903888B2 - Heat exchanger - Google Patents
Heat exchanger Download PDFInfo
- Publication number
- JP3903888B2 JP3903888B2 JP2002263915A JP2002263915A JP3903888B2 JP 3903888 B2 JP3903888 B2 JP 3903888B2 JP 2002263915 A JP2002263915 A JP 2002263915A JP 2002263915 A JP2002263915 A JP 2002263915A JP 3903888 B2 JP3903888 B2 JP 3903888B2
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- JP
- Japan
- Prior art keywords
- cut
- raised
- heat exchanger
- angle
- corner
- 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 - Fee Related
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/12—Tubular 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
- F28F1/126—Tubular 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
- F28F1/128—Fins with openings, e.g. louvered fins
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/047—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag
- F28D1/0477—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag
- F28D1/0478—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag the conduits having a non-circular cross-section
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F17/00—Removing ice or water from heat-exchange apparatus
- F28F17/005—Means for draining condensates from heat exchangers, e.g. from evaporators
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Geometry (AREA)
- Air-Conditioning For Vehicles (AREA)
Description
【0001】
【発明の属する技術分野】
この発明は、冷凍装置のエバポレータなど気体の冷却に使用される熱交換器に関する。
【0002】
【従来の技術】
自動車などの空調装置には、冷房用のエバポレータとして、平行したチューブの間にコルゲートフィンを接合した熱交換器が使用される。コルゲートフィンには、気流との熱交換効率を増大させるため、気流と交差する方向の切り起こし列(ルーバー)が設けられる。切り起しは、フィンに、気流に交差する方向の直線的な切り込みを平行して等間隔に列設し、切り込みの全幅がほぼ一定の傾斜となるようにプレス成形される。
【0003】
近年、熱交換性能の向上の為、コルゲートフィンの山高さ、フィンピッチを小さくする傾向にあるが、そうすると排水性の低下と水飛びの増大を生じる。熱交換器の表面で気流中の水分により生じた結露は、迅速に下方に流下させ排出させることが、熱交換効率の増大および水飛びの防止のために重要である。このため、コルゲートフィンの中間部や折り曲げ部に排水穴を開けたものが提案され(特許文献1参照)、ルーバーの非成形部に排水穴を開けたものが公知である(特許文献2参照)。
【0004】
【特許文献1】
実開昭61−128578号公報(図5、図6)。
【特許文献2】
実開昭62−34675号公報(図1)。
【0005】
【発明が解決しようとする課題】
これらは、いずれもコルゲートフィンに穴開け加工を必要とし、コルゲートフィンの形成工程が複雑になるとともに、穴開け際にスクラップが発生するためスクラップ処理が必要となり、生産性が低下する。また、コルゲートフィンとチューブとの接合面積が低減するため、コルゲートフィンからチューブへの熱移動が妨げられ熱交換効率(冷却性能)が低下するという問題が生じる。
【0006】
この発明の目的は、スクラップ処理が不要で、高い熱交換効率が得られるとともに、排水性を改善でき水飛びを低減させることが可能なルーバー付きフィンを備えた熱交換器の提供にある。
【0007】
【課題を解決するための手段】
この発明は、平行したチューブ間に、気流と交差する方向に切り起こし列を有するフィンを接合した熱交換器において、切り起こし列を構成する切り起こしは、全幅が傾斜しており、隅部の切り起こし角度が、中間部の切り起こし角度より大きく設定されて、隅部では上下方向に透視開口を生じる。このため、凝縮水は切り起こし角度の大きい隅部から円滑に下方に流下し、水飛びが低減できるとともに、フィンからチューブへの熱移動が円滑に行われる。切り起こし角度の大きい隅部は、切り起こしの両側に設けることが望ましい。この発明のフィンは、コルゲートフィンが一般的であるが、プレートフィンに適用することも可能である。
【0008】
また、切り起こしの隅部は、中間部に比較して気流速度が小さく、かつ露結の主な発生源であるチューブの側面に近いため、水飛びの発生が確実に防止できるとともに、迅速な排水に有効である。さらに、隅部の切り起こし角度を大きくした切り起こし列(ルーバー)は、プレス型の成形のみで容易に形成できる。このためコストアップの原因である加工の複雑化やスクラップの発生コストは、生じない。
【0009】
さらに、両隅部の切り起こし角度αを中間部の切り起こし角度βの1.5倍以上、2.5倍以下に設定することが望ましい。従来のエバポレータ用コルゲートフィン式熱交換器では、切り起こし角度αは35度程度が一般的である。この発明では、両隅部の切り起こし角度αは70度±10度の範囲が排水性の観点から好適であり、切り起こし角度αの部分の幅wは切り起こしの全幅Wの20%〜40%の範囲が適当である。
【0010】
【発明の実施の形態】
図1は、自動車の空調装置内に設置され冷凍装置のエバポレータとして使用される熱交換器1を示す。熱交換器1は、蛇行状に曲げられて内部を冷媒が流れる偏平チューブ2と、該偏平チューブ2の直線部分21の両側面22、22にロウ付けされたコルゲートフィン3とからなる。この実施例では、偏平チューブ2は略W字形を呈し、両端に入口管23および出口管24が設けられている。
【0011】
コルゲートフィン3は、金属条を蛇行状に曲げて形成され、半円筒状の湾曲部4と平板部5とからなる。平板部5には、切り起こし6が列設され切り起こし列(ルーバー)60となっている。湾曲部4は、先端が側面22に当接してロウ付けされている。左右両側のコルゲートフィン3A、3Bの外側の湾曲部4の先端は、偏平チューブ2の外側面に固着されたサイドプレート11の内面にロウ付けされている(図2参照)。この湾曲部4の先端には、コルゲートフィン3と偏平チューブ2との接触面積を低減させるような欠落部は存在しないため、コルゲートフィン3から偏平チューブ2への熱伝導は円滑に行われ、高い冷却性能が得られる。
【0012】
切り起こし6は、図3に示す如く、コルゲートフィン3の板幅方向に平行して直線状に多数の切れ目Aを入れ、切れ目Aの両側が上下逆の方向の切り起こし6となるように塑性変形させる。プレス成形により、ルーバー60を構成する切り起こし6が一度に形成でき、コルゲートフィン3に穴開け加工を行う場合のようにスクラップは発生しない。ルーバー60を構成する切り起こし6は、ほぼ中央部で、切り起こし方向が逆転している。
【0013】
この実施例では、切り起こし6は、両隅部61、61が切り起こし角度α=60度に設定され、中間部62は切り起こし角度β=30度に設定されている。全幅Wに対する切り起こし角度α=60度の部分(両隅部61、61)の幅wの割合は20%となっている。これにより、両隅部61、61では、図3の(イ)に示す平面図の如く上下方向に透視開口63が生じ、図4に矢印Yで示す如く、水滴は迅速に下方に流下し、コルゲートフィン3に付着した滞留時間が短縮される。
【0014】
エバポレータでは、熱交換器1内で冷媒が気化するため、偏平チューブ2およびコルゲートフィン3の表面で結露が生じ易い。結露した水滴は、側面22を伝って流下し、側面22と至近距離にある両隅部61、61を通じて迅速に下方に落下する。側面22の付近は、直線部分21、21の中間部に比較し、空調空気の流速が遅い。このため、水滴が空調空気流に飛ばされ、下流に設置されているヒータコアやエアミックスドアに付着したり、各種の吹出口から車室に浸入する、いわゆる水飛びの発生も確実に防止できる。
【0015】
〔変形例〕
切り起こし角度αの大きい両隅部61、61は、この実施例の如く、切り起こし6の両側に設けることが望ましいが、左右両側のコルゲートフィン3A、3Bなどでは片側だけに設けてもよい。
【図面の簡単な説明】
【図1】この発明の熱交換器の正面図である。
【図2】図1の要部を拡大した斜視図である。
【図3】切り起こし列の平面図および正面断面図である。
【図4】切り起こし列の側面断面図である。
【符号の説明】
1 熱交換器
2 偏平チューブ
3 コルゲートフィン
4 湾曲部
5 平板部
6 切り起こし
60 切り起こし列(ルーバー)
61 隅部
62 中間部
63 透視開口 [0001]
BACKGROUND OF THE INVENTION
The present invention relates to a heat exchanger used for cooling a gas such as an evaporator of a refrigeration apparatus.
[0002]
[Prior art]
In an air conditioner such as an automobile, a heat exchanger in which corrugated fins are joined between parallel tubes is used as an evaporator for cooling. In order to increase the efficiency of heat exchange with the airflow, the corrugated fin is provided with a cut and raised row (louver) in a direction intersecting with the airflow. In the cutting and raising, linear cuts in the direction intersecting the air flow are arranged in parallel at equal intervals on the fins, and press-molded so that the entire width of the cuts has a substantially constant inclination.
[0003]
In recent years, in order to improve the heat exchange performance, there is a tendency to reduce the peak height and fin pitch of the corrugated fins, but this causes a decrease in drainage and an increase in water splash. Condensation caused by moisture in the airflow on the surface of the heat exchanger is important to increase the heat exchange efficiency and prevent water splashing by quickly flowing down and discharging. For this reason, the thing which opened the drainage hole in the intermediate part and the bending part of a corrugated fin is proposed (refer patent document 1), and the thing which opened the drainage hole in the non-molding part of a louver is known (refer patent document 2). .
[0004]
[Patent Document 1]
Japanese Utility Model Publication No. 61-128578 (FIGS. 5 and 6).
[Patent Document 2]
Japanese Utility Model Publication No. 62-34675 (FIG. 1).
[0005]
[Problems to be solved by the invention]
Both of these require drilling in the corrugated fins, complicating the corrugated fin formation process, and generating scrap when drilling, which necessitates scrap processing and reduces productivity. Moreover, since the junction area of a corrugated fin and a tube reduces, the heat transfer from a corrugated fin to a tube is prevented and the problem that heat exchange efficiency (cooling performance) falls arises.
[0006]
An object of the present invention is to provide a heat exchanger provided with fins with louvers that do not require scrap processing, can obtain high heat exchange efficiency, can improve drainage, and can reduce water splash.
[0007]
[Means for Solving the Problems]
The present invention relates to a heat exchanger in which fins having cut-and-raised rows are joined between parallel tubes in a direction intersecting the air flow, and the cut-and-raised rows constituting the cut-and-raised rows are inclined at the entire width , The cut-and-raised angle is set to be larger than the cut-and-raised angle of the intermediate portion, and a fluoroscopic opening is created in the vertical direction at the corner . For this reason, the condensed water flows smoothly downward from the corner with a large angle of cut and rise, so that water splash can be reduced and heat transfer from the fin to the tube is performed smoothly. It is desirable to provide corners with a large cut and raised angle on both sides of the cut and raised. The fin of the present invention is generally a corrugated fin, but can also be applied to a plate fin.
[0008]
In addition, the corner of the cut and raised portion has a lower airflow speed than the middle part and is close to the side of the tube, which is the main source of condensation, so that the occurrence of water splash can be reliably prevented and the It is effective for drainage. Furthermore, a cut-and-raised row (louver) having a larger corner-raised angle can be easily formed only by press molding. For this reason, the complexity of processing and the cost of scrap generation, which are causes of cost increase, do not occur.
[0009]
Furthermore, it is desirable to set the cut-and-raised angle α at both corners to be 1.5 to 2.5 times the cut-and-raised angle β of the intermediate portion. In a conventional corrugated fin heat exchanger for an evaporator, the cut-and-raised angle α is generally about 35 degrees. In the present invention, the cut-and-raised angle α at both corners is preferably in the range of 70 ° ± 10 ° from the viewpoint of drainage, and the width w of the portion of the cut-and-raised angle α is 20% to 40% of the total width W of the cut and raised. A range of% is suitable.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
FIG. 1 shows a
[0011]
The
[0012]
As shown in FIG. 3, the cut and raised 6 is plastic so that a large number of cuts A are linearly formed parallel to the plate width direction of the
[0013]
In this embodiment, the cut-and-raised
[0014]
In the evaporator, since the refrigerant is vaporized in the
[0015]
[Modification]
The
[Brief description of the drawings]
FIG. 1 is a front view of a heat exchanger according to the present invention.
FIG. 2 is an enlarged perspective view of a main part of FIG.
FIG. 3 is a plan view and a front cross-sectional view of a cut and raised row.
FIG. 4 is a side sectional view of a cut and raised row.
[Explanation of symbols]
DESCRIPTION OF
61
63 Perspective opening
Claims (1)
前記切り起こし列を構成する切り起こしは、全幅が傾斜しており、隅部の切り起こし角度が、中間部の切り起こし角度より大きく設定されて、前記隅部では上下方向に透視開口を生じることを特徴とする熱交換器。In a heat exchanger in which fins having rows cut and raised in a direction intersecting the airflow are joined between parallel tubes,
The cut-and-raised row constituting the cut-and-raised row is inclined in its entire width, and the cut-and-raised angle of the corner is set to be larger than the cut-and-raised angle of the intermediate portion, and a transparent opening is formed in the vertical direction in the corner. A heat exchanger characterized by
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002263915A JP3903888B2 (en) | 2002-09-10 | 2002-09-10 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2002263915A JP3903888B2 (en) | 2002-09-10 | 2002-09-10 | Heat exchanger |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2004101074A JP2004101074A (en) | 2004-04-02 |
JP3903888B2 true JP3903888B2 (en) | 2007-04-11 |
Family
ID=32263494
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP2002263915A Expired - Fee Related JP3903888B2 (en) | 2002-09-10 | 2002-09-10 | Heat exchanger |
Country Status (1)
Country | Link |
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JP (1) | JP3903888B2 (en) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100690891B1 (en) | 2005-05-26 | 2007-03-09 | 엘지전자 주식회사 | Heat exchanger for a drier and condensing type drier utilizing the same |
JP2007232246A (en) * | 2006-02-28 | 2007-09-13 | Denso Corp | Heat exchanger |
FR2906018B1 (en) * | 2006-09-19 | 2015-06-26 | Valeo Systemes Thermiques | HEAT EXCHANGER WITH FINS FOR MOTOR VEHICLE. |
US8627881B2 (en) * | 2008-08-15 | 2014-01-14 | Carrier Corporation | Heat exchanger fin including louvers |
CN102032831A (en) * | 2009-09-28 | 2011-04-27 | 无锡市鑫盛换热器制造有限公司 | Radiating fin |
JP5012972B2 (en) * | 2010-07-30 | 2012-08-29 | ダイキン工業株式会社 | Heat exchanger bending method and heat exchanger |
JP5834324B2 (en) * | 2011-08-03 | 2015-12-16 | 国立大学法人 東京大学 | Corrugated fin heat exchanger |
DE102011117967A1 (en) * | 2011-10-06 | 2013-04-11 | Liebherr-Hausgeräte Ochsenhausen GmbH | Multi channel and/or microchannel-evaporator for cooling and/or freezing device, has edge areas connecting sides with one another, where evaporator is designed such that sides are turned towards each other and run parallel to each other |
JP6182429B2 (en) * | 2013-11-06 | 2017-08-16 | 株式会社ケーヒン・サーマル・テクノロジー | Evaporator |
JP2018048798A (en) * | 2016-09-16 | 2018-03-29 | 東芝ライフスタイル株式会社 | refrigerator |
JP6795012B2 (en) * | 2018-05-31 | 2020-12-02 | 株式会社デンソー | Heat exchanger and corrugated fins |
CN110741217B (en) * | 2017-06-12 | 2021-11-09 | 株式会社电装 | Heat exchanger and corrugated fin |
-
2002
- 2002-09-10 JP JP2002263915A patent/JP3903888B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
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JP2004101074A (en) | 2004-04-02 |
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