JPS5893A - Fin for heat exchanger - Google Patents
Fin for heat exchangerInfo
- Publication number
- JPS5893A JPS5893A JP9664181A JP9664181A JPS5893A JP S5893 A JPS5893 A JP S5893A JP 9664181 A JP9664181 A JP 9664181A JP 9664181 A JP9664181 A JP 9664181A JP S5893 A JPS5893 A JP S5893A
- Authority
- JP
- Japan
- Prior art keywords
- louver
- fin
- par
- nil
- heat exchanger
- 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
- 238000005452 bending Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 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
- F28F1/126—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
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/02—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by influencing fluid boundary
Abstract
Description
【発明の詳細な説明】
この発明は熱交換器用フィンに係り、特にルームエアコ
ン、カーエアコンなどの蒸発器や凝縮器に好適な熱交換
器用フィンに関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat exchanger fin, and more particularly to a heat exchanger fin suitable for an evaporator or condenser of a room air conditioner, a car air conditioner, or the like.
従来の熱交換器用フィンとして例えばルーツクーコルゲ
ートフィンを第1図〜第3図により説明する。第1図に
示すような熱交換器に使用されるルーバーコルゲートフ
ィンは第2図のような形状になっている。第3図は第2
図のA−A矢印方向の断面図である。第3図における流
入気流の方向に対するフィンの傾斜角度θとルーバーの
傾斜角度rとの間には、次式の関係が成り立つ時、最も
性能が良くなることがわかっている。DESCRIPTION OF THE PREFERRED EMBODIMENTS As a conventional heat exchanger fin, for example, a roots-ku corrugated fin will be explained with reference to FIGS. 1 to 3. The louvered corrugated fin used in the heat exchanger shown in FIG. 1 has a shape as shown in FIG. 2. Figure 3 is the second
It is a sectional view taken in the direction of arrow A-A in the figure. It has been found that the best performance is obtained when the following relationship holds between the inclination angle θ of the fin and the inclination angle r of the louver with respect to the direction of the incoming airflow in FIG. 3.
タタし、tはルーバーの板厚、δ9 はルーバーしかし
この関係が成立つのは第3図に示すように理想的な形状
にルーバーが切られ九時であって、実際のルーバーの切
シロは、第4図に示すようなハリ(切り口のダレ)が出
ることが避けられない。t is the thickness of the louver, and δ9 is the louver. However, this relationship only holds true when the louver is cut into an ideal shape as shown in Figure 3, and the actual cutting edge of the louver is: It is unavoidable that there will be some firmness (sag at the cut end) as shown in Figure 4.
このパリが生ずると、流れは乱されるばかシでなく、ル
ーバーとルーバーの間隙δが小さくなってしまう。この
ため、ルーバー間を流れる流れが少なくなって伝熱性能
が低下してしまうという欠点があった。When this gap occurs, the flow is not only disturbed, but also the gap δ between the louvers becomes smaller. For this reason, there was a drawback that the flow flowing between the louvers was reduced, resulting in a decrease in heat transfer performance.
この発明は上述の事柄にもとづきなされたもので、九と
えパリが生じても、十分な性能が確保できるようにする
ことを目的としたものでおる。This invention was made based on the above-mentioned matters, and is aimed at ensuring sufficient performance even if a failure occurs.
この発明の特徴とするところは、パリが出る方向と反対
方向に、ルーハーヲわずか折り曲げ、ル、<−の間隙δ
を確保して、ルーバーの間の流れが少なくならないよう
にしたことである。The feature of this invention is that the roof is slightly bent in the direction opposite to the direction in which the edges come out, and the gap δ is <-.
This is to ensure that the flow between the louvers does not decrease.
以下、この発明の一冥施例を第5図に従ってさらに具体
的に説明する。Hereinafter, one embodiment of the present invention will be explained in more detail with reference to FIG.
第5図に示す実施例におけるルーバーは、ルーバーの後
流側の長さb′の部分音、パリが出ている方向と反対方
向に、角度γ′だけ折り曲げたものである。角度γ′の
大きさは、パリの平均高さIhとすると次式で与えられ
る。The louver in the embodiment shown in FIG. 5 is bent by an angle γ' in the direction opposite to the direction in which the partial tone of length b' on the downstream side of the louver appears. The magnitude of the angle γ' is given by the following equation, assuming that the average height of Paris is Ih.
sin r ’ = 2 h / b ’
・・・曲・・(3)このように角Lr’ kつけて
折シ曲げることにより、ルーバー間隙δは理想的な状態
と同じ値だけ確保され、高い伝熱性能が得られる。sin r' = 2 h/b'
. . . Curve (3) By bending the louver at an angle Lr' k in this way, the louver gap δ is secured to the same value as in the ideal state, and high heat transfer performance can be obtained.
次に、第6図によプ、この発明の他の実施例について説
明する。ここでは、ルーバーの上fiillJの長さb
′の部分を、パリと反対方向に角度7′だけ曲げている
。γ′とパリの高さhの間には、ヤはり式(3)が成立
する。Next, another embodiment of the present invention will be described with reference to FIG. Here, the length b of the upper fill J of the louver is
' part is bent by an angle of 7' in the opposite direction to Paris. The equation (3) holds true between γ' and the height h of Paris.
第7図は、さらに別の実施例で、ルーバーの上流側も、
下流側も長さb′の部分を角度γ′だけ、パリと反対方
向に曲げている。この時の角度γ′は、次式により与え
られる。FIG. 7 shows yet another embodiment, in which the upstream side of the louver is also
On the downstream side, a portion of length b' is also bent by an angle γ' in the opposite direction to Paris. The angle γ' at this time is given by the following equation.
sin r ’ = h / b’
−”−”(4)さらに、この発明には別の効果もあって
、従来のルーバーはルーバーの長さ方向の力に対して弱
く、変形しやすい欠点があった力へこの発明の折り曲げ
をつけることによってルーバーの剛性が強くなり、変形
しにくくなるという効果が得られるっ以上述べたように
、この発明によれば、ルーバー間隙を狭くすることがな
く、従って高い伝熱性能を維持することができると同時
に、ルーバーの剛性が強くなり、精度の良い製品をつく
ることが可能である。sin r' = h/b'
-"-" (4) Furthermore, this invention has another effect, and the bending of the present invention can overcome the drawback that conventional louvers are weak against forces in the longitudinal direction of the louver and easily deform. By attaching the louver, the rigidity of the louver becomes stronger and the effect of making it difficult to deform can be obtained.As described above, according to the present invention, the louver gap is not narrowed and therefore high heat transfer performance can be maintained. At the same time, the rigidity of the louvers is increased, making it possible to manufacture products with high precision.
第1図は従来の熱交換器用フィンとしてルーバーコルゲ
ートフィンを使用した熱変換器の斜視図、第2図はルー
バーコルゲートフィンの斜視図、第3図および第4図は
第2図のA−A’断面図で第3図は理想的なルーバーの
場合の断面図、第4図は一般的なルーバーの場合の断゛
面図、第5図はこの発明におけるルーバーの断面図、第
6図および第7図はこの発明におけるルーバーの他の例
の断面図である。
1・・・ルーバー、2・・・コルケートフィン、3・・
・バイブ。
¥31 図
第 Z 図
第 3 図
第 4 凹
′″fJ 5 図
?i 6 回Figure 1 is a perspective view of a heat converter using louvered corrugated fins as conventional heat exchanger fins, Figure 2 is a perspective view of louvered corrugated fins, and Figures 3 and 4 are A-A in Figure 2. In the sectional views, Fig. 3 is a sectional view of an ideal louver, Fig. 4 is a sectional view of a general louver, Fig. 5 is a sectional view of the louver according to the present invention, Fig. 6 and FIG. 7 is a sectional view of another example of the louver according to the invention. 1... Louver, 2... Corkated fin, 3...
・Vibe. ¥31 Figure Z Figure 3 Figure 4 Concave'''fJ 5 Figure?i 6 times
Claims (1)
合せ、前記フィンに切り込みを入れて橋状に切り起こし
たルーバーを有する熱交換器用フィンにおいて、前記フ
ィン面を流入気流の方向に対して任意角度(θ)だけ傾
斜するように設け、このフィン面に切り起しを設けてル
ーバー1−形成し、このルーバーを流入気流の方向に対
してフィン面の傾斜方向と反対の方向に任意角度(γ)
だけ傾斜させると共に、前記ルーバーに残ったパリと反
対方向に、ルーバーの任意の中間位置からさらに任意角
度(γ′)だけ傾斜を大きくしたことを特徴とする熱交
換器用フィン。 2、傾斜角度θ、γおよびγ′は次の関係をほぼ満足す
るように設定したことを特徴とする特h/bl≦sin
r ’≦2h/b’ (2)ただ
し、t ニル−パーの板厚 ! δ ニル−パー後端の排除厚三 1.72− Vππ b ニル−パーの長さ R*bニル−パーのレイノルズ数三 −b ν t ニル−パーの間隔 U :空気流速 ν :空気の動粘性係数 h :バリの高さ b′ 二角度γ′だけ折り曲げたルー バ一部分の長さ[Claims] 1. A fin for a heat exchanger that combines a large number of fins and a plurality of heat transfer tubes that pass through the fins, and has a louver cut into a bridge shape by making cuts in the fin, in which the fin surface is used as an inlet. The fin surface is provided so as to be inclined at an arbitrary angle (θ) with respect to the direction of the airflow, and a cut-out is provided on the fin surface to form a louver 1. Any angle in the opposite direction (γ)
A fin for a heat exchanger, characterized in that the fin is inclined by an arbitrary angle (γ') from an arbitrary intermediate position of the louver in a direction opposite to the remaining part of the louver. 2. The inclination angles θ, γ and γ' are set so as to approximately satisfy the following relationship: h/bl≦sin
r'≦2h/b' (2) However, t is the plate thickness of Nir-Par! δ Excluded thickness at rear end of nil-par 31.72- Vππ b Length of nil-par R*b Reynolds number of nil-par 3-b ν t Distance between nil-par U: Air flow velocity ν: Air movement Viscosity coefficient h: Height of burr b' Length of part of louver bent by two angles γ'
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9664181A JPS5893A (en) | 1981-06-24 | 1981-06-24 | Fin for heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9664181A JPS5893A (en) | 1981-06-24 | 1981-06-24 | Fin for heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5893A true JPS5893A (en) | 1983-01-05 |
Family
ID=14170445
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9664181A Pending JPS5893A (en) | 1981-06-24 | 1981-06-24 | Fin for heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5893A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61181971U (en) * | 1985-04-24 | 1986-11-13 | ||
WO2005066566A1 (en) * | 2004-01-07 | 2005-07-21 | Behr Gmbh & Co. Kg | Heat exchanger |
-
1981
- 1981-06-24 JP JP9664181A patent/JPS5893A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61181971U (en) * | 1985-04-24 | 1986-11-13 | ||
WO2005066566A1 (en) * | 2004-01-07 | 2005-07-21 | Behr Gmbh & Co. Kg | Heat exchanger |
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