JPS6231273B2 - - Google Patents
Info
- Publication number
- JPS6231273B2 JPS6231273B2 JP14206681A JP14206681A JPS6231273B2 JP S6231273 B2 JPS6231273 B2 JP S6231273B2 JP 14206681 A JP14206681 A JP 14206681A JP 14206681 A JP14206681 A JP 14206681A JP S6231273 B2 JPS6231273 B2 JP S6231273B2
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- group
- fins
- heat transfer
- fin
- 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
Links
- 239000003507 refrigerant Substances 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000009423 ventilation Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
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
- F28F1/24—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 and extending transversely
- F28F1/32—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 and extending transversely the means having portions engaging further tubular elements
- F28F1/325—Fins with openings
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)
Description
【発明の詳細な説明】
本発明は、空気調和装置等に使用されるフイン
付チユーブ形熱交換器に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a finned tube heat exchanger used in air conditioners and the like.
従来、空気調和装置等における熱交換器とし
て、第1図に示すような形式のフイン付チユーブ
形熱交換器が使用されている。すなわち、フイン
1aを所定間隔ごとに平行に並べられて平板フイ
ン群1を形成し、この平板フイン群1に直角に伝
熱管2を多段にわたつて挿入することにより構成
されている。そして、空気は各平板フイン1aの
相互間を矢印方向に流れて、伝導管2内の冷媒と
熱交換を行う。 BACKGROUND ART Conventionally, a finned tube heat exchanger as shown in FIG. 1 has been used as a heat exchanger in an air conditioner or the like. That is, the fins 1a are arranged in parallel at predetermined intervals to form a flat plate fin group 1, and the heat exchanger tubes 2 are inserted in multiple stages at right angles to the flat plate fin group 1. The air flows in the direction of the arrow between the flat fins 1a and exchanges heat with the refrigerant in the conduction pipe 2.
ところが、かかる構成からなる熱交換器の平板
フイン1aの伝熱面上の温度境界層3の厚さは、
第2図に示す如く空気の流入部からの距離の平方
根に比例して増加するので、空気の流入部から離
れるにしたがつて、空気側熱伝達率が著しく低下
し、熱交換器としての伝達性能が低いという欠点
を有していた。また、この従来の熱交換器を蒸発
器として使用した場合、伝熱管2近傍のフイン1
a表面に凝縮する水滴は、すぐには落下せずフイ
ン1aの表面に溜まつたままとなつて、空気の通
風抵抗を増加させ、伝熱性能をより低下させると
いう欠点も有していた。 However, the thickness of the temperature boundary layer 3 on the heat transfer surface of the flat fin 1a of the heat exchanger having such a configuration is as follows.
As shown in Figure 2, the heat transfer coefficient increases in proportion to the square root of the distance from the air inlet, so the farther away from the air inlet, the air side heat transfer rate decreases significantly, and the heat transfer coefficient as a heat exchanger decreases. It had the disadvantage of low performance. In addition, when this conventional heat exchanger is used as an evaporator, the fin 1 near the heat exchanger tube 2
Water droplets that condense on the surface a do not fall immediately and remain accumulated on the surface of the fin 1a, which increases air ventilation resistance and further deteriorates heat transfer performance.
本発明は、上記従来の欠点を解消するもので、
空気側伝熱面における熱伝達率の著しい向上をは
かり、また熱交換器を蒸発器として使用した場
合、伝熱管近傍のフイン表面に凝縮する水滴の水
切れ性を向上させることを目的とするものであ
る。 The present invention solves the above-mentioned conventional drawbacks,
The purpose is to significantly improve the heat transfer coefficient on the air side heat transfer surface, and also to improve the drainage of water droplets that condense on the fin surface near the heat transfer tubes when the heat exchanger is used as an evaporator. be.
以下、本発明を、その一実施例を示す添付図面
の第3図および第4図を参考に説明する。ここ
で、本発明の熱交換器は基本的に従来と同様の構
成をなし、フインの構造が相違するものである。 Hereinafter, the present invention will be explained with reference to FIGS. 3 and 4 of the accompanying drawings showing one embodiment thereof. Here, the heat exchanger of the present invention basically has the same configuration as the conventional one, except that the structure of the fins is different.
第3図において、平板フイン1aは一定間隔で
バーリングされたフインカラー部1bを有し、こ
のフインカラー部1bに伝熱管2が挿入されてお
り、矢印方向に流れる空気と直交する方向、すな
わち伝熱管2の段方向において隣接する伝熱管2
の相互間に、伝熱管2を段方向に結ぶ直線に沿つ
て凹凸条4が設けられ、またその左右に複数個の
切り起し5,6,7,8が設けられている。 In FIG. 3, the flat plate fin 1a has a fin collar portion 1b which is barred at regular intervals, and a heat transfer tube 2 is inserted into the fin collar portion 1b, and the heat transfer tube 2 is inserted in the direction perpendicular to the air flowing in the direction of the arrow. Heat exchanger tubes 2 adjacent in the step direction of the heat tubes 2
An uneven strip 4 is provided between the heat exchanger tubes 2 along a straight line connecting the heat exchanger tubes 2 in the step direction, and a plurality of cut-outs 5, 6, 7, and 8 are provided on the left and right sides thereof.
この切り起し5,6,7,8の一部5,6は第
4図に示す如く凹凸条4を境として左右に、平板
フイン1a面に対して一定の傾斜度および方向に
なるように平板フイン1aの表裏面に切り起され
ている。また残りの切り起し7,8は平板フイン
1面に対して前記切り起し5,6と同一傾斜度お
よび方向になるように平板フイン1aの片面に交
互に切り起されている。また、切り起し5,6,
7,8は平板フイン1aの表裏両面又はいずれか
片面で通風方向に開口する開口部9,10,1
1,12を有する。 Parts 5, 6 of these cut-outs 5, 6, 7, 8 are arranged to have a constant inclination degree and direction with respect to the surface of the flat plate fin 1a, to the left and right with the uneven strip 4 as a boundary, as shown in FIG. It is cut and raised on the front and back surfaces of the flat plate fin 1a. The remaining cut-outs 7 and 8 are cut and raised alternately on one side of the flat plate fin 1a so as to have the same inclination and direction as the cut-outs 5 and 6 with respect to the flat plate fin 1 side. Also, cut and raise 5, 6,
7, 8 are openings 9, 10, 1 that are open in the ventilation direction on both the front and back sides of the flat plate fin 1a or on either one side.
1, 12.
上記構成において、平板フイン1aに凹凸条4
および切り起し5,6,7,8を設けているた
め、平板フイン1aは空気の流通方向に短いフイ
ン(熱交換片)が並んだ状態となり、凹凸条4お
よび切り起し5,6,7,8上にそれぞれ形成さ
れる温度境界層の厚さは薄く、しかも空気は開口
部9,10,11,12を通つてフインの裏側か
ら表側へ流れ込むので、空気流の混合および乱れ
が促進され、また凹凸条4により空気の流れが乱
されるため、伝熱性能が大幅に向上する。 In the above configuration, the uneven strips 4 are provided on the flat plate fin 1a.
Since the flat plate fins 1a have short fins (heat exchange pieces) lined up in the air flow direction, the uneven strips 4 and the cut-outs 5, 6, 8 are provided. The thickness of the temperature boundary layer formed on each of the fins 7 and 8 is thin, and the air flows from the back side of the fin to the front side through the openings 9, 10, 11, and 12, promoting mixing and turbulence of the air flow. Moreover, since the air flow is disturbed by the uneven strips 4, the heat transfer performance is greatly improved.
さらに、この熱交換器を蒸発器として使用した
場合、平板フイン1aの面上の伝熱管2の近傍に
発生する凝縮水は凹凸条4の毛細管現象によつて
落下の促進がなされるため水切れ性が向上する。
その結果、切り起し5,6,7,8の開口部9,
10,11,12は凝縮水によつて閉塞されるこ
ともなく、切り起し5,6,7,8は、温度境界
層の厚さを薄くする効果を長時間にわたつて維持
することができる。 Furthermore, when this heat exchanger is used as an evaporator, the condensed water generated near the heat exchanger tubes 2 on the surface of the flat plate fins 1a is accelerated to fall due to the capillary phenomenon of the uneven strips 4, so that water drains easily. will improve.
As a result, the openings 9 of the cut-outs 5, 6, 7, 8,
10, 11, and 12 are not blocked by condensed water, and the cut-outs 5, 6, 7, and 8 can maintain the effect of reducing the thickness of the temperature boundary layer for a long time. can.
上記実施例より明らかなように、本発明のフイ
ン付チユーブ形熱交換器は、フイン群の各フイン
における伝熱管群の段方向の相互間隙部に、前記
伝熱管群の段方向に延びる凹凸条を設け、さらに
この前記凹凸条の両側に空気の流通方向に開口し
た複数の切り起しを、フイン表裏面に対して同一
の傾斜度および方向となるように設けたもので、
空気の流れにおいて、温度境界層の厚さを薄く
し、流通空気の混合、乱れを促進するため、空気
側熱伝達率が著しく向上し、さらにこの熱交換器
を蒸発器として使用した場合においても、凹凸条
が伝熱管近傍の水滴の水切れ性を向上させるた
め、長時間にわたつての通風性も良好となり、熱
交換性能を向上させることができる等、種々の効
果を有するものである。 As is clear from the above embodiments, the finned tube heat exchanger of the present invention has an uneven strip extending in the step direction of the heat transfer tube group in the mutual gap in the step direction of the heat transfer tube group in each fin of the fin group. and further provided with a plurality of cutouts opening in the air flow direction on both sides of the uneven strip so as to have the same inclination and direction with respect to the front and back surfaces of the fin,
In the air flow, the thickness of the temperature boundary layer is reduced and the mixing and turbulence of the flowing air is promoted, so the air side heat transfer coefficient is significantly improved, and even when this heat exchanger is used as an evaporator, Since the uneven stripes improve the drainage of water droplets near the heat transfer tube, it has various effects such as good ventilation over a long period of time and improved heat exchange performance.
第1図は従来例を示すフイン付チユーブ形熱交
換器の斜視図、第2図は同熱交換器における熱流
体特性図、第3図は本発明の一実施例におけるフ
イン付チユーブ形熱交換器の平面図、第4図は第
3図のA−A線による同熱交換器の要部断面図で
ある。
1a……平板フイン、1b……フインカラー
部、2……伝熱管、4……凹凸条、5,6,7,
8……切り起し。
Fig. 1 is a perspective view of a conventional finned tube heat exchanger, Fig. 2 is a thermal fluid characteristic diagram of the same heat exchanger, and Fig. 3 is a finned tube heat exchanger according to an embodiment of the present invention. FIG. 4 is a sectional view of the main part of the heat exchanger taken along line A--A in FIG. 3. 1a... Flat plate fin, 1b... Fin collar portion, 2... Heat exchanger tube, 4... Uneven strip, 5, 6, 7,
8...Cut up.
Claims (1)
空気が流れる多数のフインからなるフイン群と、
そのフイン群に多数にわたつて直角に挿入され内
部を冷媒が通過する伝熱管群とよりフイン付チユ
ーブ形熱交換器を構成し、前記フイン群の各フイ
ンにおける前記伝熱管群の段方向の相互間隙部
に、前記伝熱管群の段方向に延びる凹凸条を設
け、さらにこの凹凸条の両側に空気の流通方向に
開口した複数の切り起しを、フイン表裏面に対し
て同一の傾斜度および方向となるように設けたフ
イン付チユーブ形熱交換器。1. A fin group consisting of a large number of fins arranged in parallel at predetermined intervals and through which air flows;
A finned tube heat exchanger is constituted by a group of heat transfer tubes which are inserted perpendicularly into the group of fins and through which a refrigerant passes, and each fin of the group of fins has a plurality of heat transfer tubes inserted in the group at right angles. An uneven strip extending in the direction of the steps of the heat transfer tube group is provided in the gap, and a plurality of cutouts opening in the air flow direction on both sides of the uneven strip are provided with the same inclination and angle with respect to the front and back surfaces of the fins. Tube heat exchanger with fins installed in the same direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56142066A JPS5843396A (en) | 1981-09-08 | 1981-09-08 | Finned tube type heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56142066A JPS5843396A (en) | 1981-09-08 | 1981-09-08 | Finned tube type heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5843396A JPS5843396A (en) | 1983-03-14 |
| JPS6231273B2 true JPS6231273B2 (en) | 1987-07-07 |
Family
ID=15306630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56142066A Granted JPS5843396A (en) | 1981-09-08 | 1981-09-08 | Finned tube type heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5843396A (en) |
-
1981
- 1981-09-08 JP JP56142066A patent/JPS5843396A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5843396A (en) | 1983-03-14 |
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