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JPS5932850Y2 - Multi-plate heat exchanger - Google Patents

Multi-plate heat exchanger

Info

Publication number
JPS5932850Y2
JPS5932850Y2 JP1692778U JP1692778U JPS5932850Y2 JP S5932850 Y2 JPS5932850 Y2 JP S5932850Y2 JP 1692778 U JP1692778 U JP 1692778U JP 1692778 U JP1692778 U JP 1692778U JP S5932850 Y2 JPS5932850 Y2 JP S5932850Y2
Authority
JP
Japan
Prior art keywords
housing
heat exchanger
cooling water
tube
plate heat
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
Application number
JP1692778U
Other languages
Japanese (ja)
Other versions
JPS54120751U (en
Inventor
庸介 鍋島
晃 吉田
Original Assignee
株式会社土屋製作所
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 株式会社土屋製作所 filed Critical 株式会社土屋製作所
Priority to JP1692778U priority Critical patent/JPS5932850Y2/en
Publication of JPS54120751U publication Critical patent/JPS54120751U/ja
Application granted granted Critical
Publication of JPS5932850Y2 publication Critical patent/JPS5932850Y2/en
Expired legal-status Critical Current

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Description

【考案の詳細な説明】 本考案は、多板式熱交換器に係り、熱交換室内の冷却水
がチューブの積層間隔以外を通過することを抑制し、冷
却水の抵抗増加を僅少に止めながら熱交換効率の向上を
はかったものである。
[Detailed description of the invention] The present invention relates to a multi-plate heat exchanger, which suppresses the cooling water in the heat exchange chamber from passing through areas other than the laminated intervals of the tubes, and heats up while minimizing the increase in resistance of the cooling water. This is intended to improve exchange efficiency.

多板式熱交換器のハウジングには通常、砂型鋳物又はダ
イカスト品が用いられる。
Sand castings or die castings are usually used for the housing of multi-plate heat exchangers.

このように溶融金属で型成形すると、鋳型の抜き勾配を
必要とするので側壁内面は開口端に向って拡張された傾
斜面となっている。
When molding molten metal in this way, a draft angle of the mold is required, so the inner surface of the side wall becomes an inclined surface that expands toward the open end.

また寸法精度や表面粗さも比較的粗となるのでエレメン
トとハウジング内面との間隔は所望の値より大きく作ら
ざるをえない。
In addition, the dimensional accuracy and surface roughness are relatively poor, so the distance between the element and the inner surface of the housing must be made larger than a desired value.

第1図は前記によって成形したハウジング3内にエレメ
ント4を収納し、熱交換室11を形成した従来の多板式
熱交換器2を示す一部断面図で、第2図は第1図の矢視
A−A断面図であり、エレメント4を構成するチューブ
10はフランジ9へ直角に積層されているが、ハウジン
グ3の側壁内面6.6′は傾斜しているので、側壁内面
6,6′とエレメント4の長辺縁部13及び短辺縁部1
4における空間は、開口端5で最大となった間隔M、L
となっている。
FIG. 1 is a partial sectional view showing a conventional multi-plate heat exchanger 2 in which an element 4 is housed in a housing 3 molded as described above and a heat exchange chamber 11 is formed, and FIG. The tube 10 constituting the element 4 is stacked on the flange 9 at right angles, but since the inner side wall 6.6' of the housing 3 is inclined, the inner side wall 6,6' and long edge 13 and short edge 1 of element 4
The space at 4 is the maximum distance M and L at the open end 5.
It becomes.

またハウジング頂壁内面とエレメント頂部平坦部との間
には各チューブ間の間隔lよりも大きな間隔1’(第3
図)が存在する。
Furthermore, there is a gap 1' (a third
Figure) exists.

そのため冷却水は抵抗の少ない間隔M、l’を直進して
チューブ10表面に接触せず流れてしまう分の割合が高
くなり熱交換効率の低い熱交換器であった。
Therefore, a high proportion of the cooling water flows straight through the intervals M and l' with low resistance and does not come into contact with the surface of the tube 10, resulting in a heat exchanger with low heat exchange efficiency.

ところが、この間隔M、l’をエレメントの長さQの全
長にわたり閉塞すると冷却水の通過抵抗が高くなってし
まう欠点がある。
However, if these gaps M and l' are closed over the entire length of the element length Q, there is a drawback that the passage resistance of the cooling water becomes high.

特に抵抗は水流が方向変換する、間隔りとM、l’との
接続部が閉塞されたとき著しく高まる。
In particular, the resistance increases significantly when the connection between the spacing and M, l', through which the water flow changes direction, is occluded.

本考案は、上記に鑑みてなれされたものであり、ハウジ
ングとエレメントの形状を変更することなく、冷却水の
抵抗増加を僅少に止めたうえ熱交換効率のすぐれた多板
式熱交換器を提供するものである。
The present invention was developed in view of the above, and provides a multi-plate heat exchanger that minimizes the increase in resistance of cooling water and has excellent heat exchange efficiency without changing the shape of the housing and elements. It is something to do.

以下本考案の実施例を図面により説明する。第3図は本
考案の多板式熱交換器1を示すもので、ハウジング3を
冷却水の上流がら下流にそって断面したものであり、第
4図は第3図の矢視BB断面図である。
Embodiments of the present invention will be described below with reference to the drawings. Fig. 3 shows the multi-plate heat exchanger 1 of the present invention, in which the housing 3 is sectioned along the direction from upstream to downstream of the cooling water, and Fig. 4 is a sectional view taken along arrow BB in Fig. 3. be.

ハウジング3には、後述するエレメント4を収納するに
十分な開口端5が鋳型の抜き勾配を配慮した側壁内面6
,6′によって形成され、一方側壁に冷却本人ロア他方
側壁に冷却水出口8が設けである。
The housing 3 has an open end 5 that is large enough to accommodate an element 4, which will be described later, and a side wall inner surface 6 that takes into consideration the draft angle of the mold.
, 6', and a cooling water outlet 8 is provided on one side wall and a cooling water outlet 8 on the other side wall.

エレメント4はフランジ9の一方平面へチューブ10を
複数段積層して一体的に固着したもので、開口端5を平
板状のフランジ9で着脱自在に閉鎖し熱交換室11を形
成している。
The element 4 is composed of a plurality of tubes 10 stacked and integrally fixed to one plane of a flange 9, and the open end 5 is removably closed by a flat flange 9 to form a heat exchange chamber 11.

12は短管でチューブ10の両端に配置され、チューブ
10を等間隔lに保持すると共にその内部は被冷却流体
の集中路を形成し、フランジ9に設けた出入口とチュー
ブ10内の流路を連通するものである。
12 is a short tube arranged at both ends of the tube 10, and holds the tube 10 at equal intervals l, and its inside forms a concentration path for the fluid to be cooled, and the inlet/outlet provided in the flange 9 and the flow path in the tube 10 are connected to each other. It is something that communicates.

L、Mは前述した従来のものと同様の間隔で、13はエ
レメントの長辺縁部、14は短辺縁部を示し、l′は頂
壁内面15とチューブ平坦部16との間に設けた余裕間
隔で前記間隔lより大である。
L and M are the same spacing as in the conventional one described above, 13 indicates the long edge of the element, 14 indicates the short edge, and l' is provided between the inner surface of the top wall 15 and the flat part 16 of the tube. The margin interval is larger than the interval l.

バッフル17は、その幅Pがエレメント4の長辺縁部長
さQより小さく、エレメント4の長辺縁部13および平
坦部16とハウジング3内面との間ヘコの字状に設けら
れ、長辺縁部13のほぼ中央に位置し、平坦部16に設
けたストッパ18で止着され間隔M、l’を幅Pの占め
る部分だけ閉塞している。
The baffle 17 has a width P smaller than the length Q of the long side edge of the element 4, is provided in a hollow shape between the long side edge 13 and flat part 16 of the element 4, and the inner surface of the housing 3, and has a long side edge length Q. It is located approximately at the center of the portion 13 and is fixed by a stopper 18 provided on the flat portion 16, thereby closing the distance M, l' by the portion occupied by the width P.

バッフル17の幅P、長さQおよび間隔MはP≦Q4M
の関係とする。
The width P, length Q and interval M of the baffle 17 are P≦Q4M
The relationship is as follows.

これは実験によれば前記のように間隔りとMの接触部で
流れ方向が変わるときバッフル17による水路断面の縮
少が加わると、著しく抵抗が高まるが、間隔MとLとの
接触部からバッフル17の幅Pの端面まで2M程度隔っ
ていればこの抵抗が著しく緩和されるからであり、出口
側においても同様である。
According to experiments, when the flow direction changes at the contact area between the spacing M and M, the resistance increases significantly when the baffle 17 reduces the cross section of the waterway, but from the contact area between the spacing M and L. This is because if there is a distance of about 2M to the end face of the width P of the baffle 17, this resistance will be significantly alleviated, and the same is true on the exit side.

第5図はチューブ10を平面的に示した第3図のE−E
断面図である。
FIG. 5 is a plan view of the tube 10 taken along the line E-E in FIG. 3.
FIG.

なお、本実施例に用いたバッフル17は、間隔M、l’
よりも薄く圧縮成形した膨潤性の吸水性高分子、たとえ
ばポリビニールホルマールを用いたので、冷却水で湿潤
されると前記の圧縮方向と逆向に膨張して側壁内面6と
頂壁内面15に密着する。
Note that the baffle 17 used in this example has an interval of M, l'
Since a swellable water-absorbing polymer, such as polyvinyl formal, which is compression-molded to a thinner thickness is used, when moistened with cooling water, it expands in the opposite direction to the compression direction and adheres tightly to the inner surface of the side wall 6 and the inner surface of the top wall 15. do.

従ってハウジング内面の抜き勾配や粗い表面に対しては
金属材料で形状を合致させるよりも容易かつ確実に密着
させられる。
Therefore, it can be more easily and reliably adhered to the draft angle or rough surface of the inner surface of the housing than by matching the shape with a metal material.

この考案は上記の構成で戒るから側壁内面6と頂壁内面
15にそって間隔M、l’を直進している冷却水を、バ
ッフル17によってその進路が阻害され蛇行流となり、
当初から間隔lを直進している冷却水と幅Pにおいて合
流し出口8に向う。
Since this device uses the above-mentioned configuration, the cooling water that is traveling straight along the inner surface of the side wall 6 and the inner surface of the top wall 15 at intervals M and l' is blocked by the baffle 17 and becomes a meandering flow.
It merges with the cooling water that has been traveling straight through the distance l from the beginning at the width P and heads toward the outlet 8.

以上のように本考案は、間隔Mとl′の一部をバッフル
によって縮小したので、冷却水の全てがバッフルを設け
た部分(幅P)においてチューブの積層間隔を通過する
ことになり、上記の合流した冷却水は直接チューブに接
触して流れ冷却効果をあけげ。
As described above, in the present invention, since a part of the distances M and l' are reduced by the baffle, all of the cooling water passes through the stacked tube spacing in the area where the baffle is provided (width P). The combined cooling water flows in direct contact with the tube, creating a cooling effect.

またバッフルの幅Pの前後における間隔M。l′の部分
はバッフルで閉塞されておらず、バッフルの端部からそ
れぞれ2Mの距離だけ離れさせて、冷却水の入口、出口
に連通ずる間隔りの部分と接続させであるから、冷却水
が入口から入って間隔りの部分で拡散するとき、冷却水
はハウジング内全域(B−B断面)に拡がるように誘導
され抵抗を低下させる効果がある。
Also, the distance M before and after the width P of the baffle. The portion l' is not blocked by a baffle, but is connected to a spaced portion communicating with the cooling water inlet and outlet, separated by a distance of 2M from each end of the baffle, so that the cooling water is not blocked. When the cooling water enters from the inlet and diffuses at intervals, it is guided to spread over the entire area within the housing (B-B cross section), which has the effect of lowering the resistance.

またエレメントの末端付近でも出口へ向う方向変換が容
易に行なわれる。
Also, the direction change toward the exit can be easily performed near the end of the element.

従って長さQ全長にわたって間隔M、l’を閉塞したも
のより抵抗が少ないのはもちろん、幅Pの部分で水路断
面が縮少されていても、冷却水が方向をかえる間隔り部
との接続部分は間隔M、l’が閉塞されていないから、
冷却水の抵抗増加は僅少に止めることができる。
Therefore, not only is the resistance lower than that in which the intervals M and l' are closed over the entire length Q, but even if the cross section of the water channel is reduced in the width P part, the connection with the interval part where the cooling water changes direction is possible. Since the intervals M and l' are not occluded in the part,
The increase in resistance of the cooling water can be kept to a minimum.

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

第1図はハウジングを一部断面した従来の多板式熱交換
器。 第2図は第1図の矢視A−A断面図。第3図はハウジン
グを一部断面した本考案の多板式熱交換器。 第4図は第3図の矢視B−B断面図。第5図は第3図の
E−E断面図。 2・・・・・・多板式熱交換器、3・・・・・・ハウジ
ング、4・・・・・・エレメント、6・・・・・・側壁
内面、9・・・・・・フランジ、10・・・・・・チュ
ーブ、11・・・・・・熱交換室、12・・・・・・短
管、13・・・・・・長辺縁部、15・・・・・・頂壁
内面、16・・・・・・平坦部、17・・・・・・バッ
フル、P・・・・・・幅、Q・・・・・・長辺縁部長さ
、M、l’・・・・・・間隔。
Figure 1 shows a conventional multi-plate heat exchanger with a partial cross-section of the housing. FIG. 2 is a sectional view taken along the line A-A in FIG. Figure 3 shows the multi-plate heat exchanger of the present invention, with the housing partially cut away. FIG. 4 is a sectional view taken along the line B--B in FIG. 3. FIG. 5 is a sectional view taken along the line EE in FIG. 2...Multi-plate heat exchanger, 3...Housing, 4...Element, 6...Inner surface of side wall, 9...Flange, 10...tube, 11...heat exchange chamber, 12...short tube, 13...long edge, 15...top Wall inner surface, 16... Flat part, 17... Baffle, P... Width, Q... Long edge length, M, l'... ····interval.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] チューブの両端に配設した短管を介して、前記チューブ
が平板状のフランジに複数段積層されたエレメントをハ
ウジング内に収容し、フランジでハウジング開口端を閉
鎖して熱交換室を形成し、ハウジング内のエレメントの
長辺方向に冷却水を流す熱交換器において1、エレメン
トの長辺側外面とハウジングの側壁内面との間隔Mおよ
びハウジングの頂壁内面との間隔l′に、幅Pなるコの
字状のバッフルを長さQのほぼ中央に設けてP≦Q−4
Mとし、前記幅Pの部分のみ間隔M、 l ’を閉塞し
た、多板式熱交換器。
A heat exchange chamber is formed by accommodating an element in which the tube is laminated in multiple stages on a flat flange in a housing via short tubes disposed at both ends of the tube, and closing the open end of the housing with the flange. In a heat exchanger in which cooling water flows in the long side direction of an element in a housing, 1, the distance M between the long side outer surface of the element and the inner surface of the side wall of the housing, and the distance l' between the inner surface of the top wall of the housing, and the width P. A U-shaped baffle is provided approximately in the center of the length Q so that P≦Q-4
M, and a multi-plate heat exchanger in which only the width P portion is closed at intervals M and l'.
JP1692778U 1978-02-13 1978-02-13 Multi-plate heat exchanger Expired JPS5932850Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1692778U JPS5932850Y2 (en) 1978-02-13 1978-02-13 Multi-plate heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1692778U JPS5932850Y2 (en) 1978-02-13 1978-02-13 Multi-plate heat exchanger

Publications (2)

Publication Number Publication Date
JPS54120751U JPS54120751U (en) 1979-08-23
JPS5932850Y2 true JPS5932850Y2 (en) 1984-09-13

Family

ID=28841356

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1692778U Expired JPS5932850Y2 (en) 1978-02-13 1978-02-13 Multi-plate heat exchanger

Country Status (1)

Country Link
JP (1) JPS5932850Y2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6858401B2 (en) 1986-08-13 2005-02-22 Lifescan, Inc. Minimum procedure system for the determination of analytes
US6979571B2 (en) 1999-11-24 2005-12-27 Home Diagnostics, Inc. Method of using a protective test strip platform for optical meter apparatus
US7390665B2 (en) 2001-02-28 2008-06-24 Gilmour Steven B Distinguishing test types through spectral analysis

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6858401B2 (en) 1986-08-13 2005-02-22 Lifescan, Inc. Minimum procedure system for the determination of analytes
US6881550B2 (en) 1986-08-13 2005-04-19 Roger Phillips Method for the determination of glucose employing an apparatus emplaced matrix
US6887426B2 (en) 1986-08-13 2005-05-03 Roger Phillips Reagents test strip adapted for receiving an unmeasured sample while in use in an apparatus
US6979571B2 (en) 1999-11-24 2005-12-27 Home Diagnostics, Inc. Method of using a protective test strip platform for optical meter apparatus
US7390665B2 (en) 2001-02-28 2008-06-24 Gilmour Steven B Distinguishing test types through spectral analysis

Also Published As

Publication number Publication date
JPS54120751U (en) 1979-08-23

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