JPS63108195A - Cross fin tube type heat exchanger - Google Patents
Cross fin tube type heat exchangerInfo
- Publication number
- JPS63108195A JPS63108195A JP25178486A JP25178486A JPS63108195A JP S63108195 A JPS63108195 A JP S63108195A JP 25178486 A JP25178486 A JP 25178486A JP 25178486 A JP25178486 A JP 25178486A JP S63108195 A JPS63108195 A JP S63108195A
- Authority
- JP
- Japan
- Prior art keywords
- water
- fin
- pipes
- heat exchanger
- ribs
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 33
- 239000006185 dispersion Substances 0.000 abstract 2
- 238000009423 ventilation Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000005273 aeration Methods 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は空調用熱交換器に係シ、特にパイプが基盤配列
のクロスフィンチューブ形熱交換器に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a heat exchanger for air conditioning, and more particularly to a cross-fin tube heat exchanger having a base arrangement of pipes.
従来の装置は、%開昭61−153392号に記載のよ
うにパイプ列ピッチLをパイプ直径dの1.2倍から1
.4倍の範囲に定めていた。すなわち1.2d(L(1
,4d0その理由は、パイプ間を凝縮水が流れ易く、且
つ伝熱性能が高い範囲を実験的に求めたものである。In the conventional device, the pipe row pitch L is set from 1.2 times the pipe diameter d to 1
.. It was set at a range of 4 times. That is, 1.2d(L(1
, 4d0 The reason is that the range in which condensed water can easily flow between the pipes and the heat transfer performance is high has been experimentally determined.
上記従来技術は、フィン面上の凝縮水をパイプ間に積極
的に集め、且つその凝縮水を積極的に排出する配慮がな
されておらず、その結果露付時の通風抵抗が高く、フィ
ンの下流端から水滴が飛散しやすいという問題点があっ
た。The above conventional technology does not actively collect condensed water on the fin surface between the pipes and actively discharge the condensed water, resulting in high ventilation resistance during dew exposure and There was a problem in that water droplets were likely to scatter from the downstream end.
本発明の目的は.碁盤配列のパイプ間の水切り性を艮<
シ、露付時の通a抵抗を減らし、フィン下流端からの水
滴飛散を防止することにある。The purpose of this invention is. Improving drainage between pipes in a Go board arrangement
Second, the purpose is to reduce aeration resistance during exposure and prevent water droplets from scattering from the downstream end of the fin.
上記目的は、フィン面上のパイプカラー近傍に円弧状の
リブを設けることにより、達成される。The above object is achieved by providing an arc-shaped rib near the pipe collar on the fin surface.
すなわち、パイプカラー周辺の円弧状リブは、フィン面
上に生成された水滴を引き込み、大きな水滴とし、パイ
プ間の中央から積極的に落下させるように働く。従って
、フィン面上の水滴は、パイプ間中央に集められ、パイ
プ間中央部は水滴が絶えず流れ落ちる川のようになって
いる。このように1円弧状リブによって.碁盤配列クロ
スフィンチューブ形熱交換器の水切り性能は向上し、そ
の結果、ムル付き時の通風抵抗を低諷し、フィン下流端
からの水滴飛散を防止することができる。That is, the arcuate ribs around the pipe collar act to draw in water droplets generated on the fin surface, turn them into large water droplets, and actively cause them to fall from the center between the pipes. Therefore, the water droplets on the fin surface are collected at the center between the pipes, and the center between the pipes is like a river in which water droplets are constantly flowing down. In this way, by one circular arc rib. The draining performance of the cross-fin tube heat exchanger in a grid arrangement is improved, and as a result, it is possible to reduce the ventilation resistance at the time of swelling and prevent water droplets from scattering from the downstream end of the fins.
以下1本発明の一実施例を第1図〜第7図により説明す
る。An embodiment of the present invention will be described below with reference to FIGS. 1 to 7.
第1図は1本発明の熱交侠器を、フイ/に平行な面で切
断したものである。パイプ2は基盤配列で、2列の場仕
を示している。フィン面上の切り起こし部3は、たとえ
ば特開昭61−6588号公報に開示された水切り性の
良い形状たとえば切り起こし部3を山形を複数連ねた形
状等になっているのが望ましい。フィン面上で生成され
る凝縮水は。FIG. 1 shows a heat exchanger according to the present invention cut along a plane parallel to the fins. Pipe 2 is a base arrangement, showing a two-row layout. It is desirable that the cut and raised portions 3 on the fin surface have a shape with good drainage properties, such as the shape disclosed in Japanese Patent Laid-Open No. 61-6588, for example, a shape in which the cut and raised portions 3 are arranged in a plurality of chevrons. Condensed water is generated on the fin surface.
リブ5によって、パイプ間中央部に集められ、大きな水
滴となって積極的に排出される。従ってパイプ間中央部
は、川のようになって絶えず水滴が流れている。その結
果空気流れ6のフィン下流端に水滴がたまることが少な
く、水滴の飛散は最小限に抑えることができる。The ribs 5 collect water in the center between the pipes, and the water is actively discharged as large droplets. Therefore, water droplets are constantly flowing in the center between the pipes, like a river. As a result, water droplets are less likely to accumulate at the downstream end of the fins of the air flow 6, and the scattering of water droplets can be minimized.
第2〜5図には1円弧状リブの断面形状の例を示し、第
2図は正面から見て、リブがひっこんでおり、第3図は
出張っている。第4図、第5因は、第2図、第3図を組
合わせたものであり、水滴7が矢印のように落下してい
く。2 to 5 show examples of cross-sectional shapes of single-arc ribs, in which the ribs in FIG. 2 are recessed when viewed from the front, and in FIG. 3 they are protruding. Figures 4 and 5 are a combination of Figures 2 and 3, and water droplets 7 fall in the direction of the arrow.
第7図は、円弧状リブの別の形状で、パイプ間中央部で
2つの円弧状リブがつながった例である。FIG. 7 shows another shape of the arcuate ribs, in which two arcuate ribs are connected at the center between the pipes.
パイプが2列の場合には、パイプ列ピッチLt。When there are two rows of pipes, the pipe row pitch Lt.
フィン奥行りの1/2より大すくシた方が、水滴を集め
る範囲が広がって、水滴の飛散防止にさらに効果がある
。If the fin depth is reduced by more than 1/2, the area where water droplets are collected will be expanded, which will be more effective in preventing water droplets from scattering.
以上のように本発明によれば、フィン面上の水滴を、パ
イプ間に引き込み、排出することができるので、露付時
の通風抵抗を低減させ、フィン下流端からの水滴飛散防
止に顕著な効果がある。As described above, according to the present invention, water droplets on the fin surface can be drawn between the pipes and discharged, thereby reducing ventilation resistance during dew exposure and significantly preventing water droplets from scattering from the downstream end of the fin. effective.
′1lX1図は本発明の一実施例のフィンに平行な断面
図、第2〜5図は第1図のA−A断面で示すリブの形状
例、第6図は水液の挙動を示す模式図。
第7図は別の実施例のフィンに平行な断面図である。
1・・・フィン、2・・・パイプ、3・・・切り起こし
部、4・・・パイプカラー、5・・・リブ、6・・・臣
気流れ、7・・・水滴。Figure '11X1 is a sectional view parallel to the fin of an embodiment of the present invention, Figures 2 to 5 are examples of rib shapes shown in the A-A cross section of Figure 1, and Figure 6 is a schematic diagram showing the behavior of water liquid. figure. FIG. 7 is a sectional view parallel to the fins of another embodiment. 1...fin, 2...pipe, 3...cut and raised part, 4...pipe collar, 5...rib, 6...water flow, 7...water drop.
Claims (2)
成るクロスフイン形熱交換器において、平板フイン面上
のパイプカラー部の近傍に、円弧状のリブを設けたこと
を特徴とするクロスフインチユーブ形熱交換器。1. A cross-fin type heat exchanger consisting of a group of tubes arranged in a Go board arrangement and a group of flat plate fins perpendicular to the cross-fin type heat exchanger, characterized in that an arcuate rib is provided near the pipe collar on the flat plate fin surface. exchanger.
換器において、パイプ列ピッチLが、フイン奥行Dの1
/2より大きいことを特徴とする特許請求の範囲第1項
のクロスフインチユーブ形熱交換器。2. In a cross-finch tube heat exchanger with two rows of pipes arranged in a Go board, the pipe row pitch L is 1 of the fin depth D.
2. The cross-finch tube heat exchanger according to claim 1, wherein the cross-finch tube heat exchanger is larger than /2.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25178486A JPS63108195A (en) | 1986-10-24 | 1986-10-24 | Cross fin tube type heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25178486A JPS63108195A (en) | 1986-10-24 | 1986-10-24 | Cross fin tube type heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63108195A true JPS63108195A (en) | 1988-05-13 |
Family
ID=17227875
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25178486A Pending JPS63108195A (en) | 1986-10-24 | 1986-10-24 | Cross fin tube type heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63108195A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5738168A (en) * | 1995-12-08 | 1998-04-14 | Ford Motor Company | Fin tube heat exchanger |
US7004242B2 (en) * | 2004-06-14 | 2006-02-28 | Advanced Heat Transfer, Llc | Enhanced heat exchanger apparatus and method |
JP2008089237A (en) * | 2006-10-02 | 2008-04-17 | Daikin Ind Ltd | Fin tube type heat exchanger |
-
1986
- 1986-10-24 JP JP25178486A patent/JPS63108195A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5738168A (en) * | 1995-12-08 | 1998-04-14 | Ford Motor Company | Fin tube heat exchanger |
US7004242B2 (en) * | 2004-06-14 | 2006-02-28 | Advanced Heat Transfer, Llc | Enhanced heat exchanger apparatus and method |
JP2008089237A (en) * | 2006-10-02 | 2008-04-17 | Daikin Ind Ltd | Fin tube type heat exchanger |
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