JP2556050Y2 - Heat exchange fins - Google Patents
Heat exchange finsInfo
- Publication number
- JP2556050Y2 JP2556050Y2 JP1990405422U JP40542290U JP2556050Y2 JP 2556050 Y2 JP2556050 Y2 JP 2556050Y2 JP 1990405422 U JP1990405422 U JP 1990405422U JP 40542290 U JP40542290 U JP 40542290U JP 2556050 Y2 JP2556050 Y2 JP 2556050Y2
- Authority
- JP
- Japan
- Prior art keywords
- heat exchange
- corrugated
- plate
- inlet
- outlet
- 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 - Fee Related
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
【0001】[0001]
【産業上の利用分野】この考案は熱交換器、特に円形の
熱交換室を有する熱交換器に用いられる熱交換フィンに
関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger, and more particularly to a heat exchange fin used in a heat exchanger having a circular heat exchange chamber.
【0002】[0002]
【従来の技術】円形の熱交換室を有する熱交換器として
は、実開昭61ー96172号に記載されたようないわ
ゆる多板式のハウジング付のものや、実公昭59−28
219号に記載されたいわゆる積層式のハウジング不要
のものがある。いずれも2枚の平行な円形プレートの周
縁をプレートに設けたフランジ部で閉塞し、円形の中心
に対し対称位置に1対の開口を設けてその一方を流入
口、他方を流出口として熱交換室を形成させ、その内部
に流体を流してプレートを介して熱交換を行うものであ
る。前記開口は、2枚のプレートに共に設けられてお
り、平行に配列された複数の熱交換室の開口が連接され
て、各熱交換室を連通する流入通路および流出通路を形
成している。2. Description of the Related Art As a heat exchanger having a circular heat exchange chamber, a heat exchanger having a so-called multi-plate type housing as described in Japanese Utility Model Application Laid-Open No. 61-96172, and a Japanese Utility Model Application No. 59-28 are used.
There is a so-called laminated housing that does not require a housing described in Japanese Patent No. 219. In each case, the peripheral edges of two parallel circular plates are closed by flanges provided on the plates, and a pair of openings are provided at symmetrical positions with respect to the center of the circle, and one of them is used as an inlet and the other is used as a heat exchanger. A chamber is formed, and a fluid flows through the chamber to exchange heat via a plate. The openings are provided on the two plates together, and the openings of the plurality of heat exchange chambers arranged in parallel are connected to form an inflow passage and an outflow passage that communicate each heat exchange chamber.
【0003】熱交換室内には、流入口から流出口へ直線
的に向かう流れを妨げて乱流を起こさせて攪拌し、かつ
流れを偏向させて熱交換室の周辺部まで行きわたらせ、
プレート上の無効な伝熱面を無くし、更に伝熱面積を増
加させるため、コルゲート形の熱交換フィンが設けられ
ている。In the heat exchange chamber, turbulent flow is hindered by obstructing the flow linearly flowing from the inlet to the outlet, and the flow is deflected to spread to the periphery of the heat exchange chamber.
Corrugated heat exchange fins are provided to eliminate ineffective heat transfer surfaces on the plate and further increase the heat transfer area.
【0005】[0005]
【考案が解決しようとする課題】上記のような熱交換フ
ィンは、円形の熱交換室のほヾ全面にわたって設けられ
ていた。従って流体に対する抵抗が高く、流体の圧力損
失が大となってしまい、圧力損失が所望の値以下に収ま
る熱交換器を設定することが困難となる場合が少くな
い。The heat exchange fins as described above have been provided over almost the entire surface of the circular heat exchange chamber. Therefore, the resistance to the fluid is high, and the pressure loss of the fluid is large, and it is not often difficult to set a heat exchanger in which the pressure loss falls below a desired value.
【0006】[0006]
【課題を解決するための手段】この考案の熱交換フィン
は、円形をなす熱交換室の流入口と流出口をそれぞれ囲
んで設けた1対のコルゲートピースでなり、両コルゲー
トピースは互に間隔をあけて配設されるとともに、外郭
形状は一部に円弧部分を有し、この部分を熱交換室の周
縁に沿わせたものである。The heat exchange fin according to the present invention comprises a pair of corrugated pieces which surround the inlet and the outlet of the circular heat exchange chamber, respectively, and the two corrugated pieces are spaced from each other. The outer shape has a circular arc portion in part, and this portion is formed along the periphery of the heat exchange chamber.
【0007】[0007]
【作用】流入口から熱交換室へ入った流体は流入口周囲
のコルゲートピースによって乱流となって攪拌されると
ともに、流れは偏向して熱交換室の周辺部に到り、プレ
ートの周辺部を介して熱交換を行う。流出口周囲のコル
ゲートピースでは周辺に分散した流れを短絡的に流出口
に集中させることなく、流出口周囲から万遍なく流入さ
せてプレートの伝熱面の無効部分を無くする。[Function] Fluid entering the heat exchange chamber from the inlet is agitated as a turbulent flow by the corrugated piece around the inlet, and the flow is deflected to the periphery of the heat exchange chamber, and the periphery of the plate. The heat exchange takes place through. In the corrugated piece around the outlet, the flow dispersed around the outlet is not short-circuited and concentrated at the outlet, but flows uniformly from around the outlet to eliminate an ineffective portion of the heat transfer surface of the plate.
【0008】この場合、熱交換室内の全面に熱交換フィ
ンを配設したものに較べて、フィン自体の伝熱面積は中
央部に間隔をあけた分だけ少なくなるが、フィンは2流
体間の直接の熱授受面ではなく、プレートへの熱の搬送
を行うものであるから、フィン自体の伝熱面積の減少に
よる影響は比較的少ない。また流れを乱流化する作用
と、偏向させて熱交換室の周辺に行きわたらせる作用は
主に流入口付近において顕著に発揮されるから、前記の
間隔を設けたことによる影響は比較的少ない。また流体
抵抗はほぼ熱交換フィンの配設面積に比例するから、中
央部の広幅な部分に間隔をあけたことにより配設面積の
減少が著しく、圧力損失の低下は顕著である。従って熱
交換作用の減少を小さく抑制しながら、圧力損失の減少
は顕著である。In this case, the heat transfer area of the fin itself is reduced by the space at the center as compared with the case where the heat exchange fins are arranged on the entire surface in the heat exchange chamber. Since the heat is transferred to the plate instead of the direct heat transfer surface, the effect of the decrease in the heat transfer area of the fin itself is relatively small. In addition, the effect of turbulent flow and the effect of deflecting and spreading around the heat exchange chamber are remarkably exhibited mainly in the vicinity of the inlet, so that the influence of the provision of the above-mentioned interval is relatively small. . Further, since the fluid resistance is almost proportional to the area where the heat exchange fins are arranged, the arrangement area is significantly reduced and the pressure loss is remarkably reduced by providing an interval in a wide portion at the center. Therefore, the decrease in pressure loss is remarkable while the decrease in heat exchange action is suppressed to a small extent.
【0009】[0009]
【実施例】図1に実施例を示す熱交換フィン1はコルゲ
ートピース2、2の2片でなる。コルゲートピース2、
2は同形であって、外郭形状は円弧部3aと直線部3b
とで形成され、ほヾ中央に開口4を有するコルゲートフ
ィンである。コルゲートの形状は図3に示すような周知
のもので千鳥状に配列した多数の直立壁5の間に多数の
スリット開口6が形成されている。直立壁5は外郭の直
線部3bと平行である。DESCRIPTION OF THE PREFERRED EMBODIMENTS A heat exchange fin 1 shown in FIG. Corrugated piece 2,
2 has the same shape, and the outer shape is an arc portion 3a and a straight portion 3b
And a corrugated fin having an opening 4 substantially at the center. The shape of the corrugate is a known one as shown in FIG. 3, and a number of slit openings 6 are formed between a number of upright walls 5 arranged in a staggered manner. The upright wall 5 is parallel to the outer straight portion 3b.
【0010】コルゲートピース2、2は円形のプレート
10に載置される。プレート10は中心に対し対称位置
の周縁寄り開口11、11を有し、一方が流入口、他方
が流出口となっている。プレート10は2枚が1対とな
り、周縁に1対のフランジ12a、12b(図4)が設
けられて互にかしめ合わされて閉塞され、プレート1
0、10の間に熱交換室13(図4)を形成し、内部に
熱交換フィン1が収納される。コルゲートピース2の円
弧部3aは熱交換室の周縁すなわちフランジ12a、1
2bのかしめ部分に接近させて沿わせてあり、開口4は
プレート10の開口11と同心になっている。2つのコ
ルゲートピース2、2は開口11、11に対応して配設
され双方の直線部3b、3bはプレート10の中心部に
間隔dをあけて対向し平行している。プレート10の中
心には取付けボルト用の孔14が設けられる。The corrugated pieces 2 are mounted on a circular plate 10. The plate 10 has openings 11 and 11 near the periphery which are symmetrical with respect to the center. One is an inlet and the other is an outlet. The plate 10 is a pair of two plates, and a pair of flanges 12a and 12b (FIG. 4) are provided on the periphery, and the plates are caulked together and closed.
A heat exchange chamber 13 (FIG. 4) is formed between 0 and 10 and the heat exchange fins 1 are housed therein. The arc portion 3a of the corrugated piece 2 is located at the periphery of the heat exchange chamber, that is, the flange 12a,
The opening 4 is concentric with the opening 11 of the plate 10 so as to approach the caulked portion 2b. The two corrugated pieces 2, 2 are arranged corresponding to the openings 11, 11, and both straight portions 3b, 3b are opposed to and parallel to the center of the plate 10 with an interval d. At the center of the plate 10 is provided a hole 14 for a mounting bolt.
【0011】熱交換室13は、プレート10の孔14の
内側周縁がシールリング15で閉鎖される。各熱交換室
13は、開口11の外側周縁に環状のスペーサ16、孔
14の外側周縁に環状のスペーサ17を重ねて積層さ
れ、各開口11と各スペーサ16とによって流入通路1
8、流出通路19が形成される。このように積層された
複数の熱交換室13は第2流体の入口パイプ、出口パイ
プを有するハウジング20内に収容され、流入通路1
8、流出通路19はハウジング20を貫通し外部に連通
する連通路がそれぞれ設けられる。流入通路18から入
り各熱交換室13を流れ流出通路19から流出する第1
流体は、潤滑用のオイルであり、第2流体は冷却水であ
って、ハウジング20内は冷却水ジャケットとなる。こ
うして多板式のオイルクーラ21が形成される。In the heat exchange chamber 13, the inner peripheral edge of the hole 14 of the plate 10 is closed by a seal ring 15. Each of the heat exchange chambers 13 is formed by stacking an annular spacer 16 on the outer periphery of the opening 11 and an annular spacer 17 on the outer periphery of the hole 14.
8. Outflow passage 19 is formed. The plurality of heat exchange chambers 13 stacked as described above are housed in a housing 20 having an inlet pipe and an outlet pipe for the second fluid, and
8. The outflow passage 19 is provided with a communication passage which penetrates the housing 20 and communicates with the outside. The first flow which enters from the inflow passage 18 and flows through each heat exchange chamber 13 and flows out from the outflow passage 19
The fluid is oil for lubrication, the second fluid is cooling water, and the inside of the housing 20 becomes a cooling water jacket. Thus, a multi-plate oil cooler 21 is formed.
【0012】図2に示す第2実施例の熱交換フィン7
は、コルゲートピース8、8の2片でなる。コルゲート
ピース8の開口4および直立壁5、スリット開口6を有
するコルゲート形状は、コルゲートピース2と同じであ
る。コルゲートピース8の外郭形状は、円弧部9aと曲
線部9bとでなる。円弧部9aはコルゲートピース2の
円弧部3aよりやゝ短かくされ、円弧部9aの両端を連
結して凸状の曲線部9bが形成される。The heat exchange fins 7 of the second embodiment shown in FIG.
Consists of two pieces, corrugated pieces 8 and 8. The corrugated shape of the corrugated piece 8 having the opening 4, the upright wall 5, and the slit opening 6 is the same as the corrugated piece 2. The outer shape of the corrugated piece 8 includes an arc portion 9a and a curved portion 9b. The arc portion 9a is slightly shorter than the arc portion 3a of the corrugated piece 2, and a convex curved portion 9b is formed by connecting both ends of the arc portion 9a.
【0013】熱交換フィン7を収容する熱交換室35
(図5)は、2枚の円形のプレート30を積層し、その
周縁を斜に起立させて設けたフランジ31同士を重ねて
閉塞することにより形成される。プレート30には開口
32、32が中心に対し対称の位置に設けられ、コルゲ
ートピース8の開口4は開口32と同心になるように配
設される。双方の曲線部9a,9aがプレート30の中
心部分に間隔をあけて対向する。開口32、32に対し
直角方向の対応する位置にホールフランジ33aを有す
る開口33が設けられ、中央にボルト取付用及び戻り通
路用の孔34がホールフランジ34aを付けて設けられ
る。A heat exchange chamber 35 for accommodating the heat exchange fins 7
(FIG. 5) is formed by laminating two circular plates 30 and overlapping and closing flanges 31 provided with their peripheral edges rising obliquely. Openings 32, 32 are provided in the plate 30 symmetrically with respect to the center, and the opening 4 of the corrugated piece 8 is arranged so as to be concentric with the opening 32. Both curved portions 9a, 9a face the central portion of the plate 30 with an interval. An opening 33 having a hole flange 33a is provided at a position perpendicular to the openings 32, 32, and a hole 34 for bolt attachment and a return passage is provided at the center with the hole flange 34a.
【0014】プレート30は同じ向きで90°ずつ周方
向に位相をずらせながら重ね合わせると、開口32とフ
ランジ33aとが交互に接続される。こうして熱交換室
35はプレート30を共有してその上下に連続した層状
に形成され、フランジ33aによって各熱交換室35は
交互に1層おきに連通する第1流体流路と第2流体流路
に区画される。フランジ33aは同軸上に重なって第1
流体の流入通路36、流出通路37および第2流体の流
入、流出通路(図示せず)を形成する。積層された熱交
換室35に上端板38、下端板39が取付けられ、上下
端板38,39のいずれかに、流入通路36、流出通路
37を外部に連通させる開口が設けられる。こうして第
1流体をオイル、第2流体を冷却水とするオイルクーラ
40が形成される。41はオイルを孔34でなる戻り通
路へ戻すためのオイルカバー、42は冷却水の出入路と
なる水カバーである。図示のように熱交換フィン7をオ
イル側の熱交換室35にのみ設けたが、更に水側の熱交
換室にも設けることができる。When the plates 30 are overlapped in the same direction while being shifted in the circumferential direction by 90 °, the openings 32 and the flanges 33a are connected alternately. In this manner, the heat exchange chambers 35 are formed in a layer continuous with the plate 30 in a continuous manner above and below the plate 30. The first and second fluid flow paths alternately communicate with each other every other layer by the flange 33a. Is divided into The flange 33a is coaxially overlapped with the first
A fluid inflow passage 36, an outflow passage 37, and an inflow / outflow passage (not shown) for the second fluid are formed. An upper end plate 38 and a lower end plate 39 are attached to the stacked heat exchange chambers 35, and one of the upper and lower end plates 38, 39 is provided with an opening for communicating the inflow passage 36 and the outflow passage 37 to the outside. Thus, an oil cooler 40 is formed in which the first fluid is oil and the second fluid is cooling water. Reference numeral 41 denotes an oil cover for returning oil to the return passage formed by the holes 34, and reference numeral 42 denotes a water cover serving as a passage for cooling water. Although the heat exchange fins 7 are provided only in the heat exchange chamber 35 on the oil side as shown in the figure, they can be further provided in the heat exchange chamber on the water side.
【0015】熱交換フィン2と熱交換フィン7とは等面
積であり圧力損失の減少程度は等しいが、流体の流れの
偏向量を多くして多量に周辺部に向かわせるためには側
方に抵抗が少ない熱交換フィン7のほうがすぐれてい
る。熱交換フィンの外部形状は、熱交換室の形状により
限定されるものではない。熱交換フィン7の曲線部9b
の形状も限定されない。またコルゲートの形状も特定の
ものに限定されない。The heat exchange fins 2 and the heat exchange fins 7 have the same area and the same degree of reduction in pressure loss. The heat exchange fins 7 having less resistance are better. The external shape of the heat exchange fin is not limited by the shape of the heat exchange chamber. Curved portion 9b of heat exchange fin 7
Is not limited. Also, the shape of the corrugate is not limited to a specific one.
【0016】[0016]
【考案の効果】この考案の熱交換フィンは、熱交換室の
流入口と流出口とをそれぞれ囲む2片からなり、中央の
広幅部分でフィンの面積を減らし、流れに対し攪拌およ
び偏向の作用が強く働らく流入口、流出口部分にコルゲ
ートピースを置くようにしたから、熱交換作用の低下を
少なく抑制しながら、圧力損失を顕著に減少させること
ができ、仕様に応じた適正な熱交換器が得られる。The heat exchange fin of the present invention is composed of two pieces surrounding the inflow port and the outflow port of the heat exchange chamber respectively. The area of the fin is reduced at the wide portion in the center, and the action of stirring and deflecting the flow is achieved. The corrugated pieces are placed at the inlet and outlet, which work strongly, so that the pressure loss can be significantly reduced while the heat exchange effect is kept low, and the proper heat exchange according to the specifications A vessel is obtained.
【図1】熱交換フィンの実施例を示す図である。FIG. 1 is a view showing an embodiment of a heat exchange fin.
【図2】熱交換フィンの第2の実施例を示す図である。FIG. 2 is a view showing a second embodiment of the heat exchange fin.
【図3】熱交換フィンのコルゲート形状を示す図であ
る。FIG. 3 is a view showing a corrugated shape of a heat exchange fin.
【図4】熱交換室を重ねた多板式熱交換器の図である。FIG. 4 is a diagram of a multi-plate heat exchanger in which heat exchange chambers are stacked.
【図5】熱交換室を重ねた積層式熱交換器の図である。FIG. 5 is a diagram of a stacked heat exchanger in which heat exchange chambers are stacked.
1,7 熱交換フィン 2,8 コルゲートピース 4 開口 3a,9a 円弧部 3b 直線部 9b 曲線部 1,7 Heat exchange fins 2,8 Corrugated piece 4 Opening 3a, 9a Arc part 3b Linear part 9b Curve part
Claims (1)
して形成され、中心に対し対称位置に1対の開口を設け
て流入口、流出口とした熱交換室の内部に配設される熱
交換フィンであって、前記開口を囲み、外郭の一部が熱
交換室の周縁に沿う円弧をなすコルゲートピースの1対
でなり、両コルゲートピースが流入口または流出口を囲
み、かつ両コルゲートピース間に間隙をあけて配設され
た熱交換フィン。1. A heat exchanger which is formed by closing a peripheral edge between parallel circular plates and provided with a pair of openings at symmetrical positions with respect to the center and which is provided as an inlet and an outlet. A heat exchange fin surrounding the opening, a part of the outer shell being a pair of corrugated pieces forming an arc along the periphery of the heat exchange chamber, both corrugated pieces surrounding the inlet or outlet, and Heat exchange fins with a gap between corrugated pieces.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1990405422U JP2556050Y2 (en) | 1990-12-28 | 1990-12-28 | Heat exchange fins |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1990405422U JP2556050Y2 (en) | 1990-12-28 | 1990-12-28 | Heat exchange fins |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04100662U JPH04100662U (en) | 1992-08-31 |
JP2556050Y2 true JP2556050Y2 (en) | 1997-12-03 |
Family
ID=31882845
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1990405422U Expired - Fee Related JP2556050Y2 (en) | 1990-12-28 | 1990-12-28 | Heat exchange fins |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2556050Y2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101243676B1 (en) * | 2010-06-09 | 2013-03-14 | 한라공조주식회사 | Plate-type Heat Exchanger |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6126358B2 (en) * | 2012-11-08 | 2017-05-10 | 株式会社マーレ フィルターシステムズ | Multi-plate oil cooler |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5937985U (en) * | 1982-08-31 | 1984-03-10 | 株式会社土屋製作所 | Plate finch tube for heat exchanger |
JPS63116780U (en) * | 1987-01-20 | 1988-07-28 |
-
1990
- 1990-12-28 JP JP1990405422U patent/JP2556050Y2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101243676B1 (en) * | 2010-06-09 | 2013-03-14 | 한라공조주식회사 | Plate-type Heat Exchanger |
Also Published As
Publication number | Publication date |
---|---|
JPH04100662U (en) | 1992-08-31 |
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