JPS62172192A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPS62172192A
JPS62172192A JP1516686A JP1516686A JPS62172192A JP S62172192 A JPS62172192 A JP S62172192A JP 1516686 A JP1516686 A JP 1516686A JP 1516686 A JP1516686 A JP 1516686A JP S62172192 A JPS62172192 A JP S62172192A
Authority
JP
Japan
Prior art keywords
airflow
fin
heat exchanger
slit piece
fins
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
JP1516686A
Other languages
Japanese (ja)
Inventor
Osao Kido
長生 木戸
Hiroshi Yoneda
米田 浩
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 JP1516686A priority Critical patent/JPS62172192A/en
Publication of JPS62172192A publication Critical patent/JPS62172192A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

PURPOSE:To obtain high heat transfer rate between a fin and airflow by a method wherein a slit piece, whose fore rim is opposed to airflow, is provided on the surface of the fin and raised-slotted surfaces, forming the slit piece, is formed by a parallel surface and a slanted surface to the fin. CONSTITUTION:A slit piece 5, provided on the surface of a fin 4, is provided so that the fore rim 5a thereof is opposed to airflow B. Accordingly, the development of the temperature boundary layer of the airflow B, which is generated on the surface of the fin 4, is divided by the slit piece 5 and the average thickness of the temperature boundary layer becomes thin. On the other hand, the airflow B, flowing along both surfaces of the fin 4, is mixed orthogonally to the fin 4 by the slanted surface 5c'' of a raised-slotted surface 5c of the slit piece 5 while the airflow B is disturbed highly in a direction along the surface of the fin 4 by the slanted surface 5c'' arranged in zigzag. Thus, a very high heat transfer rate may be obtained between the airflow B and the fin 4 and, further, the heat transfer rate will never be deteriorated even in a heat exchanger, long in the direction of the airflow B, even while flowing to the downstream side of the heat exchanger.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は空調機器や冷凍機器等に用いられる熱交換器に
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 used in air conditioning equipment, refrigeration equipment, etc.

従来の技術 近年、熱交換器の性能向上は目ざましいものがあり、空
気側伝熱面積が大きいことを特徴とする波型フィンを備
えだ熱交換器が自動車用を中心としてすでに実用化され
ている。
Conventional technology In recent years, there has been a remarkable improvement in the performance of heat exchangers, and heat exchangers equipped with wave-shaped fins that have a large heat transfer area on the air side have already been put into practical use mainly for automobiles. .

以下図面を参照しながら、上述した従来の熱交換器につ
いて説明を行なう。
The conventional heat exchanger mentioned above will be explained below with reference to the drawings.

第5図は従来の熱交換器の概略形状を示し、第6図はそ
のフィン形状を示すものである。第5図〜第6図におい
て、1は蛇行状に屈曲した偏平管で直管部1′をほぼ平
行に備えている。2は偏平管1の向かい合う直管部1′
相互間に設けられたフィンで、波型状に一定間隔で偏平
管1に固定されている。3はフィン20表面に設けられ
たルーバ片で、前縁部3aが気流Aと対向し、かつルー
バ面3bが気流Aと傾斜を持って構成されている。
FIG. 5 shows a schematic shape of a conventional heat exchanger, and FIG. 6 shows its fin shape. In FIGS. 5 and 6, reference numeral 1 is a meanderingly bent flat tube having straight tube portions 1' substantially parallel to each other. 2 is a straight pipe part 1' facing the flat pipe 1;
The fins are provided between each other and are fixed to the flat tube 1 in a wave shape at regular intervals. Reference numeral 3 denotes a louver piece provided on the surface of the fin 20, with a front edge 3a facing the airflow A and a louver surface 3b inclined with respect to the airflow A.

以上のように構成された熱交換器について、以下その動
作について説明する。
The operation of the heat exchanger configured as above will be described below.

フィン2のフィン間を流れる気流Aと偏平管1の管内を
流れる熱媒体の間で、フィン2及び偏平管1を介して熱
交換が行なわれる。その際、フィン2の表面に設けられ
たルーバ片3により、フィン2の表面に生じる気流Aの
温度境界層の発達が分断されて温度境界層の平均厚さが
薄くなる効果と、フィン2の両面を流れる気流Aが前記
ルーバ片により混合されて乱される効果により、気流A
とフィン2の間で大きい熱伝達率を得ている。
Heat exchange is performed between the airflow A flowing between the fins of the fins 2 and the heat medium flowing inside the flat tube 1 via the fins 2 and the flat tube 1. At this time, the louver piece 3 provided on the surface of the fin 2 interrupts the development of the temperature boundary layer of the airflow A generated on the surface of the fin 2, reducing the average thickness of the temperature boundary layer, and Due to the effect that the airflow A flowing on both sides is mixed and disturbed by the louver piece, the airflow A
A large heat transfer coefficient is obtained between the fins 2 and fins 2.

発明が解決しようとする問題点 しかしながら上記のような構成では、ルーバ片3による
通風抵抗の増大が著しく大きいことと、フィン20表面
に生じる気流Aの温度境界層が完全に分断されずに下流
へ行くに従って厚くなり、気流Aとフィン2の間の熱伝
達率が下流へ行く程低下することとなり、特に気流A方
向に長い熱交換器の場合に極端に熱交換能力が低下する
という問題点を有していた。
Problems to be Solved by the Invention However, with the above configuration, the increase in ventilation resistance due to the louver pieces 3 is significantly large, and the temperature boundary layer of the airflow A generated on the surface of the fin 20 is not completely separated and flows downstream. As the thickness increases, the heat transfer coefficient between the airflow A and the fins 2 decreases as it goes downstream, which causes the problem that the heat exchange ability is extremely reduced especially in the case of a heat exchanger that is long in the direction of the airflow A. had.

本発明は上記問題点に鑑み、気流方向に長い熱交換器に
おいてもフィンと気流の間の熱伝達率が低下せず、熱交
換能力の大きい熱交換器を提供するものである。
In view of the above-mentioned problems, the present invention provides a heat exchanger that has a large heat exchange capacity without reducing the heat transfer coefficient between the fins and the airflow even in a heat exchanger that is long in the direction of the airflow.

問題点を解決するだめの手段 上記問題点を解決するために本発明の熱交換器は、フィ
ン表面に前縁部が気流と対向するスリット片を設け、か
つスリット片の切起こし面が前記フィンに対して平行な
面と傾斜した面とから形成されているという構成を備え
たものである。
Means for Solving the Problems In order to solve the above problems, the heat exchanger of the present invention has a slit piece on the fin surface whose front edge faces the airflow, and a cut and raised surface of the slit piece facing the fin. It has a configuration in which it is formed of a plane parallel to the plane and a plane inclined to the plane.

作  用 本発明は上記した構成によってフィン表面に生じる気流
の温度境界層の発達がスリット片によって分断されて温
度境界層の平均的な厚さが薄くなると共に、スリット片
を形成する切起こし面のフィンに対して傾斜した面によ
シフイン間を流れる気流がフィン表面に対して垂直方向
に混合されるることとなる。
Effects of the present invention With the above-described configuration, the development of the temperature boundary layer of the airflow generated on the fin surface is divided by the slit pieces, so that the average thickness of the temperature boundary layer becomes thinner, and the cut and raised surfaces forming the slit pieces are The airflow flowing between the fins is mixed in a direction perpendicular to the fin surface due to the surface inclined with respect to the fin.

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〜第4図は本発明の一実施例における熱交換器を
示すものである。第1図〜第4図において、1は偏平管
で従来の構成と同じものである。
1 to 4 show a heat exchanger in one embodiment of the present invention. In FIGS. 1 to 4, numeral 1 denotes a flat tube having the same structure as the conventional one.

4は偏平管1の向かい合う直管部1′相互間に設けられ
たフィンで、波型状に一定間隔で偏平管1に固定されて
いる。5はフィン4の表面に設けられたスリット片で、
前縁部6aが気流Bと対向する方向に設けである。また
スリット片5は、脚部5bと切起こし面5Cとからなり
、更に切起こし面5Cはフィン6に対して平行面5dと
傾斜面5d’とから形成されている。また、前記傾斜面
s d’は気流B方向で千鳥配列となるよう切起こし面
6Cに形成されている。
Fins 4 are provided between the opposing straight pipe portions 1' of the flat tube 1, and are fixed to the flat tube 1 at regular intervals in a wave shape. 5 is a slit piece provided on the surface of the fin 4;
The front edge 6a is provided in a direction facing the airflow B. The slit piece 5 is made up of a leg portion 5b and a cut and raised surface 5C, and the cut and raised surface 5C is formed of a parallel surface 5d and an inclined surface 5d' with respect to the fin 6. Further, the inclined surface s d' is formed on the cut and raised surface 6C so as to be arranged in a staggered manner in the direction of the airflow B.

以上のように構成された熱交換器について、以下その動
作について説明する。
The operation of the heat exchanger configured as above will be described below.

フィン4のフィン間を流れる気流Bと偏平管1の管内を
流れる熱媒体の間で、フィン4及び偏平管1を介して熱
交換が行なわれる。その際、フィン40表面に生じる気
流Bの温度境界層の発達がスリット片6により分断され
て温度境界層の平均厚さが薄くなる。寸だ、スリット片
5の切起こし面5cの傾斜面6c“によりフィン4の両
面を流れる気流Bがフィン4に対して垂直方向に混合さ
れると共に、千鳥配列された傾斜面5dlにより気流B
はフィン4表面に沿う方向にも大きく乱される。
Heat exchange is performed between the airflow B flowing between the fins of the fins 4 and the heat medium flowing inside the flat tube 1 via the fins 4 and the flat tube 1. At this time, the development of the temperature boundary layer of the airflow B generated on the surface of the fin 40 is divided by the slit piece 6, and the average thickness of the temperature boundary layer becomes thinner. The airflow B flowing on both sides of the fins 4 is mixed in the direction perpendicular to the fins 4 by the sloped surface 6c'' of the cut and raised surface 5c of the slit piece 5, and the airflow B is mixed by the staggered sloped surfaces 5dl.
is also greatly disturbed in the direction along the surface of the fin 4.

また、切起こし而5Cは平行面5 c/も備えているだ
め、大きく通風抵抗を増大させることもない。
Moreover, since the cut and raised part 5C also has a parallel surface 5c/, the ventilation resistance does not increase significantly.

以上のように本実施例によれば、フィン4の表面にスリ
ット片5を設け、かつスリット片6を形成する切起こし
面5Cに平行面5 c’と傾斜面50″を気流B方向で
千鳥配列に設けることにより、通風抵抗を大きく増大さ
せることなく、気流Bの温度境界層厚さを平均的に薄く
することと、気流Bの流れを大きく乱して、気流Bとフ
ィン4の間で極めて大きい熱伝達率を得、しかも気流B
はフィン4表面に沿う方向にも大きく乱されるだめ、気
流B方向に長い熱交換器であっても下流へ行くに従って
熱伝達率が低下するということはなく、大きい熱交換能
力を得ることができるa 発明の効果 以上のように本発明は、フィン表面に前縁部が気流と対
向するスリット片を設け、かつスリット片を形成する切
起こし面を前記フィンに対して平行な面と傾斜した面か
ら形成することにより、フィンと気流の間で大きい熱伝
達率を得、かつ気流方向に長い熱交換器でも下流側へ行
くに従って熱伝達率を低下させることなく、熱交換能力
の優れた熱交換器を得ることができる。
As described above, according to this embodiment, the slit piece 5 is provided on the surface of the fin 4, and the cut and raised face 5C forming the slit piece 6 has a parallel surface 5c' and an inclined surface 50'' in a staggered manner in the direction of the airflow B. By providing the fins in an array, it is possible to reduce the thickness of the temperature boundary layer of the airflow B on average without greatly increasing the ventilation resistance, and to greatly disturb the flow of the airflow B, thereby increasing the temperature between the airflow B and the fins 4. Obtains extremely high heat transfer coefficient, and airflow B
is also greatly disturbed in the direction along the surface of the fins 4, so even if the heat exchanger is long in the direction of the airflow B, the heat transfer coefficient will not decrease as it goes downstream, and a large heat exchange capacity can be obtained. Possible a Effect of the Invention As described above, the present invention provides a slit piece whose front edge faces the airflow on the fin surface, and a cut and raised surface forming the slit piece that is inclined with respect to a plane parallel to the fin. By forming the fins into a flat surface, a large heat transfer coefficient can be obtained between the fins and the airflow, and even if the heat exchanger is long in the direction of the airflow, the heat transfer coefficient will not decrease as it goes downstream. You can get an exchanger.

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

第1図は本発明の一実施例における熱交換器のフィン形
状を示す要部斜視図、第2図は第1図の平面図、第3図
は第2図のC−C線の断面図、第4図は第2図のD−D
線の断面図、第5図は従来の熱交換器の形状を示す斜視
図、第6図は第5図のフィン形状を示す要部斜視図であ
る。 4・・・・・・フィン、5・・・・・・スリット片、5
 a・・・・・・前縁部、6b・・・・・・脚部、5C
・・・・・・切起こし面、5c’・・・・・・平行面、
5 c//、・・・・・傾斜面。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名a B  / 第5図 凍6図
Fig. 1 is a perspective view of a main part showing the fin shape of a heat exchanger in an embodiment of the present invention, Fig. 2 is a plan view of Fig. 1, and Fig. 3 is a cross-sectional view taken along line C-C of Fig. 2. , Figure 4 is D-D in Figure 2.
5 is a perspective view showing the shape of a conventional heat exchanger, and FIG. 6 is a perspective view of a main part showing the fin shape of FIG. 5. 4...Fin, 5...Slit piece, 5
a... Front edge, 6b... Leg, 5C
......Cut and raised surface, 5c'...Parallel surface,
5 c//,...slope surface. Name of agent: Patent attorney Toshio Nakao and 1 other persona B / Figure 5, Figure 6

Claims (1)

【特許請求の範囲】[Claims]  蛇行状に屈曲した偏平管と、前記偏平管の間に波形状
に重積したフィンとを備え、前記フィン表面に前縁部が
気流と対向するスリット片を設け、かつスリット片の切
起こし面を前記フィンに対して平行な面と傾斜した面と
から形成したことを特徴とする熱交換器。
A flat tube bent in a serpentine shape and a fin stacked in a wave shape between the flat tubes, a slit piece having a front edge facing the airflow is provided on the surface of the fin, and a cut and raised surface of the slit piece is provided. A heat exchanger characterized in that the fins are formed of a surface parallel to the fins and a surface inclined.
JP1516686A 1986-01-27 1986-01-27 Heat exchanger Pending JPS62172192A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1516686A JPS62172192A (en) 1986-01-27 1986-01-27 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1516686A JPS62172192A (en) 1986-01-27 1986-01-27 Heat exchanger

Publications (1)

Publication Number Publication Date
JPS62172192A true JPS62172192A (en) 1987-07-29

Family

ID=11881214

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1516686A Pending JPS62172192A (en) 1986-01-27 1986-01-27 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS62172192A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2453234A (en) * 2007-09-27 2009-04-01 Toshiba Carrier Corp Heat exchanger
FR2924491A1 (en) * 2007-12-04 2009-06-05 Valeo Systemes Thermiques WIRELESS INTERCALIARY WITH PERSIANS FOR HEAT EXCHANGER
US20150000880A1 (en) * 2008-08-06 2015-01-01 Delphi Technologies, Inc. Heat exchanger with varied louver angles
JP2017161186A (en) * 2016-03-11 2017-09-14 パナソニックIpマネジメント株式会社 Fin tube heat exchanger
EP3255369A1 (en) * 2016-06-08 2017-12-13 Mahle International GmbH Fin element for a heat transferer

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2453234A (en) * 2007-09-27 2009-04-01 Toshiba Carrier Corp Heat exchanger
GB2453234B (en) * 2007-09-27 2010-07-14 Toshiba Carrier Corp Heat exchanger and air conditioner
FR2924491A1 (en) * 2007-12-04 2009-06-05 Valeo Systemes Thermiques WIRELESS INTERCALIARY WITH PERSIANS FOR HEAT EXCHANGER
EP2068106A1 (en) * 2007-12-04 2009-06-10 Valeo Systèmes Thermiques Corrugated fin with louvers for a heat exchanger
JP2009139085A (en) * 2007-12-04 2009-06-25 Valeo Systemes Thermiques Louver type corrugated insert for heat exchanger
US20150000880A1 (en) * 2008-08-06 2015-01-01 Delphi Technologies, Inc. Heat exchanger with varied louver angles
JP2017161186A (en) * 2016-03-11 2017-09-14 パナソニックIpマネジメント株式会社 Fin tube heat exchanger
EP3255369A1 (en) * 2016-06-08 2017-12-13 Mahle International GmbH Fin element for a heat transferer
CN107478085A (en) * 2016-06-08 2017-12-15 马勒国际公司 Fin element for heat exchanger
CN107478085B (en) * 2016-06-08 2021-05-11 马勒国际公司 Fin element for a heat exchanger

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