JPH0229597A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPH0229597A
JPH0229597A JP17783888A JP17783888A JPH0229597A JP H0229597 A JPH0229597 A JP H0229597A JP 17783888 A JP17783888 A JP 17783888A JP 17783888 A JP17783888 A JP 17783888A JP H0229597 A JPH0229597 A JP H0229597A
Authority
JP
Japan
Prior art keywords
heat transfer
fins
heat exchanger
wavy
flow
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.)
Pending
Application number
JP17783888A
Other languages
Japanese (ja)
Inventor
Hiroto Miyake
弘人 三宅
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Refrigeration Co
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 Matsushita Refrigeration Co filed Critical Matsushita Refrigeration Co
Priority to JP17783888A priority Critical patent/JPH0229597A/en
Publication of JPH0229597A publication Critical patent/JPH0229597A/en
Pending legal-status Critical Current

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To obtain a heat exchanger improved in the heat transfer performance thereof by a method wherein the heat exchanger is constituted of wavy fins, arranged in parallel and the flow of air flows therebetween, and heat transfer tubes, inserted into the wavy fins orthogonally thereto and liquid flows therethrough, while connecting slanted surfaces between the wavy parts of the wavy fins and flat parts around the collars of the fins are provided with cut-and-raised parts. CONSTITUTION:In a heat exchanger employing wavy heat transfer fins, the leading edge effect of boundary layer is generated in the flow of air, flowing along connecting slanted surfaces 15, by the cut-and-raised surfaces of cut-and-raised parts 16 while a part of the flow of air flows through the holes of the cut-and-raised parts to the peripheries of heat transfer tubes in a neighboring space partitioned by the fins. The flow of the inflow air 17 is mixed with the flow of air 18 flowing along the connecting slanted surfaces in the neighboring space and the condition of turbulent flow is generated whereby the heat transfer rate of the surfaces of the fins may be improved and a dead water area 19 after the heat transfer tubes may be reduced since the turbulent flow flows into the directions of the heat transfer tubes. The leading edge effect of boundary layer, the improvement of the surface heat transfer rate of the fin due to turbulent flow effect and effective reduction of the dead water area after the heat transfer tube may be obtained more effectively compared with a heat exchanger obtained so far.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、冷凍冷蔵機器および空調機器に広く用いられ
ている、冷媒と空気等の流体間で熱の授受を行なう熱交
換器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a heat exchanger that transfers heat between a refrigerant and a fluid such as air, which is widely used in refrigeration equipment and air conditioning equipment.

従来の技術 近年、機器の高効率化が求められている中、熱交換器へ
の着霜現象を伴う冷凍冷蔵機器や空気熱源ヒートポンプ
の室外機等に用いられる熱交換器の効率向上が急務であ
る。
Conventional technology In recent years, there has been a demand for higher efficiency in equipment, and there is an urgent need to improve the efficiency of heat exchangers used in refrigeration equipment and outdoor units of air source heat pumps, which are prone to frost formation on heat exchangers. be.

以下、図面を参照しながら従来の熱交換器の一例につい
て説明する。第4図、第6図および第6図は従来の熱交
換器を示す。第4図は熱交換器の斜視図、1は@熱フィ
ンで多数並行に並べられている。2は伝熱管で、前記伝
熱フィン1に直角に挿入されていや。第6図は伝熱フィ
ン1の平面図、第6図は伝熱フィン1の断面図である。
An example of a conventional heat exchanger will be described below with reference to the drawings. 4, 6 and 6 show conventional heat exchangers. FIG. 4 is a perspective view of a heat exchanger, and 1 is a large number of heat fins arranged in parallel. A heat transfer tube 2 is inserted into the heat transfer fin 1 at right angles. 6 is a plan view of the heat transfer fin 1, and FIG. 6 is a sectional view of the heat transfer fin 1.

空気は伝熱フィン1間を流れ、冷媒は伝熱管2内を流れ
熱交換する。
Air flows between the heat transfer fins 1, and refrigerant flows within the heat transfer tubes 2 to exchange heat.

@熱フィン1は熱伝達率向上のため、表面を波状に成形
しであるが、伝熱管2を挿入するためのカラー3を成形
するため、カラー3の回シに平坦部4および波状部6と
平坦部4の接続斜面6を有したものとなっている。
@The surface of the heat fin 1 is formed into a wavy shape in order to improve the heat transfer coefficient, but in order to form the collar 3 into which the heat transfer tube 2 is inserted, a flat part 4 and a wavy part 6 are formed on the rotation of the collar 3. and a connecting slope 6 between the flat portion 4 and the flat portion 4.

発明が解決しようとする課題 伝熱フィンの性能向上のためには、波状部6の山高さH
を高くすることと、伝熱管間の峰の長さLを長くするこ
とが有利である。これは、伝熱フィン間を流れる空気の
乱れが大きくなることと、伝熱管後流に位置する峰の抵
抗にょシ、空気が伝熱管の後ろまで流れ込み、流れの死
水域7を小さくすることができるからである。しかしな
がら、近年のコストダウンの要求を背景に、伝熱フィン
の材料を薄くしようとすると、材料の破断が発生し、波
状の山高さHをあまシ高くできず、かつ伝熱管間の峰の
長さLもあまり長くできない。このため、空気の流れ8
の乱れも小さく、また、伝熱管後部の死水域7も小さく
ならず伝熱性能が悪いという課題を有していた。
Problems to be Solved by the Invention In order to improve the performance of heat transfer fins, it is necessary to
It is advantageous to increase the peak length L between the heat transfer tubes. This is due to the increased turbulence of the air flowing between the heat transfer fins, and the resistance of the peaks located downstream of the heat transfer tubes, which causes the air to flow to the back of the heat transfer tubes, reducing the dead area 7 of the flow. Because it can be done. However, with the recent demand for cost reduction, when trying to make the material of the heat transfer fins thinner, the material breaks, making it impossible to increase the height H of the undulating fins, and making the ridges between the heat transfer tubes longer. L can't be too long either. Therefore, the air flow 8
turbulence is small, and the dead area 7 at the rear of the heat transfer tube is also not small, resulting in poor heat transfer performance.

そこで本発明は、上記課題に鑑み、波状の山高さをあま
シ高くせず、かつ伝熱管間の峰の長さもあまり長くせず
とも伝熱性能を向上させるものである。
In view of the above-mentioned problems, the present invention aims to improve heat transfer performance without increasing the height of the undulating peaks and without increasing the length of the peaks between the heat transfer tubes too much.

課題を解決するための手段 本発明の熱交換器は、一定間隔で多数平行に並べられ、
その間を気流が流動する波状フィンと、前記波状フィン
に直角に挿入され内部を流体が流動する伝熱管から構成
され、前記波状フィンの波状部とカラー周りの平坦部と
の接続斜面に切り起こしを設けたものである。
Means for Solving the Problems A large number of heat exchangers of the present invention are arranged in parallel at regular intervals,
Consisting of wavy fins through which air flows, and heat transfer tubes inserted perpendicularly into the wavy fins through which fluid flows, the wavy fins are cut and raised on the connecting slope between the wavy part and the flat part around the collar. It was established.

作  用 このように接続斜面に設けた切υ起こしによって、接続
斜面に沿って流れる気流は切り起こし面に衝突し、その
後切り起こしの孔を通して一部の気流が、フィンを隔て
た隣りの空間の伝熱間層りに流れ込むものである。
Function: Due to the cut-and-raised surface provided on the connecting slope, the airflow flowing along the connecting slope collides with the cut-and-raised surface, and then a part of the airflow passes through the cut-and-raised hole and flows into the adjacent space across the fins. It flows into the heat transfer layer.

実施例 以下、本発明の一実施例の熱交換器について図面を参照
しながら説明する。
EXAMPLE Hereinafter, a heat exchanger according to an example of the present invention will be described with reference to the drawings.

第1図は、本発明の一実施例における熱交換器を構成す
る伝熱フィン平面図である。12は熱伝達率向上のため
表面を波状に成形した波状部、13は伝熱管を挿入する
ためのカラー、14はカラー13回りに設けられた平坦
部、16は波状部12と平坦部14とを接続する接続斜
面、16は接続斜面16に設けられた切り起こし、17
は切り起こし16の孔より吹き出す気流、18は接続斜
面を流れる気流、19は伝熱管後部の死水域である。
FIG. 1 is a plan view of heat transfer fins constituting a heat exchanger in an embodiment of the present invention. 12 is a wavy portion whose surface is formed into a wavy shape to improve heat transfer coefficient; 13 is a collar for inserting a heat exchanger tube; 14 is a flat portion provided around the collar 13; and 16 is a wavy portion 12 and a flat portion 14. 16 is a cut and raised connection slope provided on the connection slope 16, 17
18 is the airflow blowing out from the hole in the raised cut 16, 18 is the airflow flowing on the connecting slope, and 19 is the dead area at the rear of the heat exchanger tube.

また第2図は第1図における切9起こし16の詳細図で
ある。
Further, FIG. 2 is a detailed view of the cutting 9 and raising 16 in FIG.

以上のような波状の伝熱フィンを用いた熱交換器におい
て、接続斜面15に沿って流れる気流は切り起こし16
の切り起こし面によって境界層前縁効果が発生するとと
もに一部の気流は切り起この し孔からフィンを隔て隣シの空間の伝熱管周りに流れ込
む。流れ込んだ気流17は隣りの空間の接続斜面に沿っ
て流れる気流18と混合・乱流状態となりフィン表面熱
伝達率を向上させるとともに、伝熱管方向に流れ込むた
め伝熱管後部の死水域19が減少する。
In the heat exchanger using the wavy heat transfer fins as described above, the airflow flowing along the connection slope 15 is caused by the cut and raised fins 16.
The cut-and-raised surface generates a boundary layer leading edge effect, and a portion of the airflow flows from the cut-and-raised hole into the vicinity of the heat transfer tube in the adjacent space, separating the fins. The inflowing airflow 17 mixes with the airflow 18 flowing along the connecting slope of the adjacent space and becomes turbulent, improving the fin surface heat transfer coefficient, and flowing in the direction of the heat exchanger tube, reducing the dead area 19 at the rear of the heat exchanger tube. .

以上のように本実施例によれば、従来の熱交換器に比べ
境界層前縁効果・乱流効果によるフィン表面熱伝達率の
向上、及び伝熱管後部死水域の減少に効果がある。そこ
で、第3図を用いて、本実施例の熱交換器と従来の熱交
換器との伝熱性能を比較する。第3図において、縦軸の
QA/QBは従来の波状の伝熱フィンを用いた熱交換器
の熱交換能力@Bと本実施例の波状の伝熱フィンを用い
たものの熱交換能力OAとの比を示し、横軸のUFは熱
交換器前面風速を示す。なお、両者熱交換器の仕様は切
り起こしの有無以外に全く同じであり、実験条件も同じ
である。第3図に示すように実用風速域1 m / s
付近において本実施例の熱交換器は従来の熱交換器に比
べ、熱交換能力を15%向上させることができる。
As described above, this embodiment is effective in improving the fin surface heat transfer coefficient due to the boundary layer leading edge effect and turbulence effect and reducing the dead area at the rear of the heat exchanger tube, compared to the conventional heat exchanger. Therefore, using FIG. 3, the heat transfer performance of the heat exchanger of this embodiment and a conventional heat exchanger will be compared. In Fig. 3, the vertical axis QA/QB is the heat exchange capacity @B of the heat exchanger using the conventional wavy heat transfer fins and the heat exchange capacity OA of the heat exchanger using the wavy heat transfer fins of this embodiment. UF on the horizontal axis indicates the wind speed in front of the heat exchanger. The specifications of both heat exchangers are exactly the same except for the presence or absence of cut and raised parts, and the experimental conditions are also the same. As shown in Figure 3, the practical wind speed range is 1 m/s.
In the vicinity, the heat exchanger of this embodiment can improve the heat exchange capacity by 15% compared to the conventional heat exchanger.

発明の効果 以上のように本発明の熱交換器は、波状フィンの波状部
とカラー回りの平坦部との接続斜面に切り起こしを設け
ることにより、境界層前縁効果・乱流効果によるフィン
表面熱伝達率の向上、及び伝熱管後部死水域の減少に効
果があシ、@熱性能の向上をはかった優れた熱交換器を
実現するものである。
Effects of the Invention As described above, the heat exchanger of the present invention has a cut-and-raised part on the connecting slope between the wavy part of the wavy fin and the flat part around the collar, thereby reducing the fin surface due to the leading edge effect of the boundary layer and the turbulent flow effect. It is effective in improving the heat transfer coefficient and reducing the dead zone at the rear of the heat exchanger tube, thereby realizing an excellent heat exchanger with improved thermal performance.

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

第1図は本発明の実施例における熱交換器の伝熱フィン
の平面図、第2図は第1図における切り起こしの詳細図
、第3図は本発明の実施例における熱交換器と従来熱交
換器との伝熱性能比較図、第4図は従来の熱交換器の斜
視図、第5図は従来の伝熱フィンの平面図、第6図は従
来の伝熱フィンの断面図である。 1・・・・・・伝熱フィン、2・・・・・・伝熱管、1
2・・団・波状部、13・・・・・・カラー、14・・
・・・・平坦部、16・・・・・・接続斜面、16・・
・・・・切り起こし、17.18・・・・・・気流。 代理人の氏名 弁理士 粟 野 重 孝 ほか1名図 第 図 12−  渇状別
Fig. 1 is a plan view of heat transfer fins of a heat exchanger according to an embodiment of the present invention, Fig. 2 is a detailed view of the cut and raised portions in Fig. 1, and Fig. 3 is a diagram showing a heat exchanger according to an embodiment of the present invention and a conventional A comparison diagram of heat transfer performance with a heat exchanger, Figure 4 is a perspective view of a conventional heat exchanger, Figure 5 is a plan view of a conventional heat transfer fin, and Figure 6 is a cross-sectional view of a conventional heat transfer fin. be. 1...Heat transfer fin, 2...Heat transfer tube, 1
2... Group/wavy part, 13... Color, 14...
... Flat part, 16 ... Connection slope, 16 ...
...Cut up, 17.18...Airflow. Name of agent: Patent attorney Shigetaka Awano and 1 other person Figure 12- By case

Claims (1)

【特許請求の範囲】[Claims]  一定間隔で多数平行に並べられ、その間を気流が流動
する伝熱フィンと、前記伝熱フィンに直角に挿入され内
部を流体が流動する伝熱管とから構成され、前記伝熱フ
ィンの波状部とカラー回りの平坦部との接続斜面に切り
起こしを設けたことを特徴とする熱交換器。
It consists of a large number of heat transfer fins arranged in parallel at regular intervals, through which air flows, and heat transfer tubes inserted at right angles to the heat transfer fins, through which fluid flows, and the wavy portions of the heat transfer fins and A heat exchanger characterized by providing a cut and raised slope on the connecting slope with the flat part around the collar.
JP17783888A 1988-07-15 1988-07-15 Heat exchanger Pending JPH0229597A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17783888A JPH0229597A (en) 1988-07-15 1988-07-15 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17783888A JPH0229597A (en) 1988-07-15 1988-07-15 Heat exchanger

Publications (1)

Publication Number Publication Date
JPH0229597A true JPH0229597A (en) 1990-01-31

Family

ID=16038000

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17783888A Pending JPH0229597A (en) 1988-07-15 1988-07-15 Heat exchanger

Country Status (1)

Country Link
JP (1) JPH0229597A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5203403A (en) * 1991-02-21 1993-04-20 Matsushita Electric Industrial Co., Ltd. Fin-tube heat exchanger
US5738168A (en) * 1995-12-08 1998-04-14 Ford Motor Company Fin tube heat exchanger
WO2006001817A1 (en) * 2004-06-14 2006-01-05 Advanced Heat Transfer Llc Enhanced heat exchanger apparatus and method
US7182127B2 (en) * 2003-09-02 2007-02-27 Lg Electronics Inc. Heat exchanger
US7219716B2 (en) * 2003-09-15 2007-05-22 Lg Electronics, Inc. Heat exchanger
US7261147B2 (en) * 2003-05-28 2007-08-28 Lg Electronics Inc. Heat exchanger
CN104246408A (en) * 2012-04-23 2014-12-24 松下知识产权经营株式会社 Finned tube heat exchanger
JP2020063883A (en) * 2018-10-18 2020-04-23 三星電子株式会社Samsung Electronics Co.,Ltd. Heat exchanger and air conditioner
WO2021098024A1 (en) * 2019-11-21 2021-05-27 广州高澜节能技术股份有限公司 Enhanced heat exchange fin for sleeve-piece-type air cooler

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5203403A (en) * 1991-02-21 1993-04-20 Matsushita Electric Industrial Co., Ltd. Fin-tube heat exchanger
US5738168A (en) * 1995-12-08 1998-04-14 Ford Motor Company Fin tube heat exchanger
US7261147B2 (en) * 2003-05-28 2007-08-28 Lg Electronics Inc. Heat exchanger
US7182127B2 (en) * 2003-09-02 2007-02-27 Lg Electronics Inc. Heat exchanger
US7219716B2 (en) * 2003-09-15 2007-05-22 Lg Electronics, Inc. Heat exchanger
WO2006001817A1 (en) * 2004-06-14 2006-01-05 Advanced Heat Transfer Llc Enhanced heat exchanger apparatus and method
US7004242B2 (en) 2004-06-14 2006-02-28 Advanced Heat Transfer, Llc Enhanced heat exchanger apparatus and method
CN104246408A (en) * 2012-04-23 2014-12-24 松下知识产权经营株式会社 Finned tube heat exchanger
JP2020063883A (en) * 2018-10-18 2020-04-23 三星電子株式会社Samsung Electronics Co.,Ltd. Heat exchanger and air conditioner
WO2021098024A1 (en) * 2019-11-21 2021-05-27 广州高澜节能技术股份有限公司 Enhanced heat exchange fin for sleeve-piece-type air cooler

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