JPH0313517B2 - - Google Patents

Info

Publication number
JPH0313517B2
JPH0313517B2 JP60153172A JP15317285A JPH0313517B2 JP H0313517 B2 JPH0313517 B2 JP H0313517B2 JP 60153172 A JP60153172 A JP 60153172A JP 15317285 A JP15317285 A JP 15317285A JP H0313517 B2 JPH0313517 B2 JP H0313517B2
Authority
JP
Japan
Prior art keywords
fluid
panel
hollow
discharge pipe
supply pipe
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 - Lifetime
Application number
JP60153172A
Other languages
Japanese (ja)
Other versions
JPS6213995A (en
Inventor
Eiji Fukumoto
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SAKAE SANGYO KK
Original Assignee
SAKAE SANGYO KK
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 SAKAE SANGYO KK filed Critical SAKAE SANGYO KK
Priority to JP15317285A priority Critical patent/JPS6213995A/en
Publication of JPS6213995A publication Critical patent/JPS6213995A/en
Publication of JPH0313517B2 publication Critical patent/JPH0313517B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、熱交換用中空パネルを適当間隔置き
に複数枚並列配置して一体化し、これら各中空パ
ネル内に熱交換用流体を流通させるようにしたパ
ネル型熱交換器であつて、主として、熱交換の対
象となる流体の貯蔵槽内又は当該流体の流路中に
セツトして使用され、各中空パネル内を流通する
流体と各中空パネル間の隙間内に位置する流体又
は当該間隙内を流通する流体との間で熱交換を行
わせるようにしたパネル型熱交換器に関するもの
である。
Detailed Description of the Invention (Industrial Field of Application) The present invention involves arranging a plurality of hollow panels for heat exchange in parallel at appropriate intervals and integrating them, and allowing a fluid for heat exchange to flow through each of these hollow panels. It is a panel type heat exchanger that is mainly used by being set in a storage tank of a fluid to be heat exchanged or in a flow path of the fluid, and the fluid flowing through each hollow panel and each hollow The present invention relates to a panel type heat exchanger that exchanges heat with a fluid located in a gap between panels or a fluid flowing in the gap.

(従来の技術及びその問題点) 前記のようなパネル型熱交換器は、並列配置さ
れている多数枚の各中空パネルをその並列方向に
貫通する流体供給管路と流体排出管路とを備え、
前記流体供給管路を流通する流体が各中空パネル
内に分流し、各中空パネル内の所定流路を流動し
た熱交換作用後の流体が前記流体排出管路内に合
流し排出されるように構成されるものであるが、
従来のこの種のパネル型熱交換器に於いては、前
記流体供給管路及び排出管路が次のように構成さ
れていた。
(Prior art and its problems) The above-mentioned panel type heat exchanger includes a fluid supply pipe line and a fluid discharge pipe line that pass through each of a large number of hollow panels arranged in parallel in the parallel direction. ,
The fluid flowing through the fluid supply pipe is divided into each hollow panel, and the fluid flowing through a predetermined flow path in each hollow panel and subjected to heat exchange is merged into the fluid discharge pipe and discharged. It is composed of
In the conventional panel heat exchanger of this type, the fluid supply pipe and the discharge pipe were constructed as follows.

即ち、各中空パネルを形成する両側のプレート
に相対向するように設けられた貫通穴夫々から短
い筒状体を溶接により固着突設し、隣接する中空
パネル間で両パネルから突出する前記筒状体を互
いに嵌合させると共に、この嵌合箇所で両筒状体
を互いに溶接により固着結合することにより、各
中空パネルをその並列方向に貫通する流体供給管
路、或いは流体排出管路が構成されていた。
That is, a short cylindrical body is fixedly protruded by welding from each of the through holes provided so as to face each other in the plates on both sides forming each hollow panel, and the cylindrical body protruding from both panels is provided between adjacent hollow panels. By fitting the bodies into each other and firmly connecting both cylindrical bodies to each other by welding at this fitting location, a fluid supply conduit or a fluid discharge conduit passing through each hollow panel in the parallel direction is constructed. was.

このような構成の従来のパネル型熱交換器で
は、並列配置された多数枚の中空パネルが前記流
体供給管路及び排出管路によつて弁解不可能に一
体化されている。一般にこの種のパネル型熱交換
器では、前記各中空パネル間の間隙は20mm前後
と非常に狭いので、前記のように各中空パネルを
互いに分離することが出来なければ、この中空パ
ネル間の間隙を流通する流体のスケールが中空パ
ネルの表面に付着しても、清掃除去することは殆
ど不可能である。従つて従来のパネル型熱交換器
は、各中空パネル間の間隙を流通させる流体がス
ケールの発生付着の殆ど無いものである場合にの
み使用されており、用途が大幅に限定される結果
となつていた。
In a conventional panel heat exchanger having such a configuration, a large number of hollow panels arranged in parallel are inexcusably integrated by the fluid supply pipe and the discharge pipe. Generally, in this type of panel heat exchanger, the gap between the hollow panels is very narrow, around 20 mm, so if the hollow panels cannot be separated from each other as described above, the gap between the hollow panels Even if scale from the flowing fluid adheres to the surface of the hollow panel, it is almost impossible to clean it off. Therefore, conventional panel-type heat exchangers are used only when the fluid flowing through the gaps between the hollow panels has almost no scale buildup, which greatly limits its applications. was.

一方、製造面に於いては、前記のように各中空
パネルから両側に短い筒状体を溶接により固着突
設しなければならない点と、隣接する両中空パネ
ル間の極めて狭い空間内で両筒状体を溶接により
接合しなければならない点とによつて、製造コス
トが極めて高くつく欠点があつた。特に、前記の
ように隣接する両中空パネル間の極めて狭い空間
内で両筒状体の嵌合部を全周にわたつて溶接する
ことは手作業では不可能であり、従つて専用の自
動溶接機を必要としていた。
On the other hand, in terms of manufacturing, as mentioned above, short cylindrical bodies must be fixed and protruded from each hollow panel on both sides by welding, and both cylindrical bodies must be fixedly protruded from each hollow panel in an extremely narrow space between two adjacent hollow panels. The manufacturing cost is extremely high due to the fact that the shaped bodies must be joined by welding. In particular, it is impossible to manually weld the fitting part of both cylindrical bodies over the entire circumference within the extremely narrow space between both adjacent hollow panels as described above, so a special automatic welding method is required. I needed a machine.

実公昭53−33878号は複数の伝熱単子をパツキ
ン材を介して積重ねボルトによつて締結した熱交
換器を開示している。しかしこれはボルトによる
ので伝熱単子やパツキンの位置決めができない。
Utility Model Publication No. 53-33878 discloses a heat exchanger in which a plurality of heat transfer units are fastened together by stacking bolts via packing material. However, since this uses bolts, it is not possible to position the heat transfer unit or packing.

(問題点を解決するための手段) 本発明は上記のような従来の問題点を解決し得
るパネル型熱交換器を提案するものであつて、そ
の特徴は、2枚のプレートを両者間に流路を形成
するように互いに接合して構成された熱交換用中
空パネルに流体供給管と流体排出管とを各別に貫
通させる貫通穴を設け、この貫通穴の周囲に於い
て前記両側プレート間に、当該両側プレート間の
間隔が狭くなるのを阻止し且つ放射状の流通路と
これに連通する内周環状溝とを有する補強リング
を介装し、外周に軸方向に延びる流通穴を備えた
流体供給管及び流体排出管に所要枚数の前記中空
パネルを、各中空パネル間に於いて前記流体供給
管及び排出管にこれらの外径にほぼ等しい内径の
環状シール材を外嵌させた状態で、管軸方向に引
き抜き分解可能に嵌合し、締結一体化した点にあ
る。
(Means for Solving the Problems) The present invention proposes a panel-type heat exchanger that can solve the conventional problems as described above, and its feature is that two plates are placed between them. A through hole is provided through which a fluid supply pipe and a fluid discharge pipe pass through the heat exchange hollow panel which are joined to each other to form a flow path, and a through hole is provided between the two plates on both sides around the through hole. A reinforcing ring is interposed to prevent the gap between the two side plates from narrowing and has a radial flow path and an inner annular groove communicating with the flow path, and a flow hole extending in the axial direction on the outer periphery is provided. A required number of hollow panels are provided around the fluid supply pipe and the fluid discharge pipe, and an annular sealing material having an inner diameter approximately equal to the outer diameter of these is fitted between the hollow panels. , are fitted together so that they can be pulled out and disassembled in the tube axis direction, and are fastened and integrated.

(作用) 上記のような本発明の構成に於いては、前記流
体供給管及び排出管の周囲の空間が、各中空パネ
ル及び各中空パネル間の前記環状シール材により
外界に対し完全に隔離されている。このため流体
供給管内に供給された流体は、この管周面の流通
穴から各中空パネル内の前記補強リングの放射状
流通路を経由して各中空パネル内に分流し、そし
てこの中空パネル内の流路を流動した流体は、前
記流体排出管の外側に位置する前記補強リングの
放射状流通路から管周面の流通穴を経由して当該
排出管内へ合流する。
(Function) In the configuration of the present invention as described above, the space around the fluid supply pipe and the discharge pipe is completely isolated from the outside world by each hollow panel and the annular sealing material between each hollow panel. ing. Therefore, the fluid supplied into the fluid supply pipe is divided into each hollow panel from the circulation hole in the pipe peripheral surface via the radial flow path of the reinforcing ring in each hollow panel, and then flows into each hollow panel. The fluid flowing through the flow path joins into the discharge pipe from the radial flow passage of the reinforcing ring located outside the fluid discharge pipe via the communication hole on the pipe peripheral surface.

従つて、互いに熱交換作用させる2流体の内の
一方の流体(第一流体)を本発明パネル型熱交換
器に供給するようにし、この本発明パネル型熱交
換器を他方の第二流体の貯蔵槽内又は当該第二流
体の流通路内にセツトして使用することにより、
前記のように各中空パネル内を流動する第一流体
と、各中空パネル間の間隙内に位置するか又は当
該間隙内を流動する第二流体との間で所定の熱交
換作用を行わせることが出来る。
Therefore, one fluid (the first fluid) of the two fluids that exchange heat with each other is supplied to the panel heat exchanger of the present invention, and the panel heat exchanger of the present invention is connected to the other fluid, the first fluid. By setting it in the storage tank or the flow path of the second fluid,
Performing a predetermined heat exchange action between the first fluid flowing within each hollow panel as described above and the second fluid located in or flowing within the gap between each hollow panel. I can do it.

又、各中空パネルを前記流体供給管及び排出管
の軸方向に締め付けて一体化するとき、各中空パ
ネル間の環状シール材を所期通りのシール効果が
得られるように十分に締め付けても、各中空パネ
ルの両側プレートがその締め付け反力で内側に撓
むことを前記補強リングにより阻止し、各中空パ
ネルの流体流入部及び流出部の空間を一定に確保
し得る。さらに流体供給管、排出管によつて中空
パネル、環状シールの位置決めがなされる。勿
論、各中空パネルの締め付けを解くことにより、
各中空パネル及び環状シール材を前記流体供給管
及び排出管より軸方向に抜き取り、夫々を分離す
ることが出来る。
Furthermore, when the hollow panels are tightened in the axial direction of the fluid supply pipe and the discharge pipe to integrate them, even if the annular sealing material between the hollow panels is sufficiently tightened to obtain the desired sealing effect, The reinforcing ring prevents the plates on both sides of each hollow panel from bending inward due to the reaction force of the tightening, thereby ensuring a constant space between the fluid inlet and outlet of each hollow panel. Further, the hollow panel and the annular seal are positioned by the fluid supply pipe and the discharge pipe. Of course, by unfastening each hollow panel,
Each hollow panel and annular seal can be axially extracted from the fluid supply pipe and the discharge pipe and separated from each other.

(実施例) 以下に本発明の一実施例を添付の例示図に基づ
いて説明する。
(Example) An example of the present invention will be described below based on the attached illustrative drawings.

第1図及び第2図に於いて、1は矩形状の熱交
換用中空パネルであつて、2枚のプレート2間に
ジグザグ状の帯状流路3を形成するように当該流
路3の両側にそつて両プレート2をシーム溶接部
4により互いに接合一体化して構成したものであ
る。第2図では図示省略しているが、前記両プレ
ート2は第3図乃至第5図に示すように、流路3
内に於いても夫々内側に適当形状で凹入させ、こ
の凹入部5内に於いて両プレート2をスポツト溶
接部6により互いに接合し、パネル1の強度アツ
プと流路3の断面積の一定化、及び流路3内を流
動する流体を乱流化して熱交換効率の向上を図る
ことが出来る。勿論、流路3の形状や長さ及び断
面積、或いは前記凹入部5の配置や形状及び大き
さ等は、この熱交換器の使用目的や使用する流体
の種類等に応じて設定すれば良く、図示のものに
限定されない。
In FIGS. 1 and 2, reference numeral 1 denotes a rectangular hollow panel for heat exchange, and a zigzag band-shaped channel 3 is formed between two plates 2 on both sides of the channel 3. Both plates 2 are integrally joined to each other by a seam weld 4. Although not shown in FIG. 2, both plates 2 are connected to the flow path 3 as shown in FIGS. 3 to 5.
Both plates 2 are recessed inwardly in an appropriate shape, and both plates 2 are joined to each other by spot welds 6 within the recessed portions 5, thereby increasing the strength of the panel 1 and keeping the cross-sectional area of the flow path 3 constant. The heat exchange efficiency can be improved by making the fluid flowing in the flow path 3 turbulent. Of course, the shape, length, and cross-sectional area of the flow path 3, or the arrangement, shape, and size of the recessed portion 5 may be set depending on the purpose of use of this heat exchanger, the type of fluid used, etc. , but not limited to what is shown.

前記中空パネル1には、流路3の両端に於いて
両プレート2を外側に膨出させて形成した円形の
幅広部7が設けられており、この各幅広部7に於
いて両側プレート2に、第1図及び第2図に示す
流体供給管8及び流体排出管9を貫通させるため
の貫通穴10(第6図参照)が幅広部7と同心状
態で設けられている。そして第1図、第3図、及
び第6図に示すように前記幅広部7内には、内径
が前記貫通穴10の直径と略等しく且つ外径が前
記幅広部7の内径と略等しい補強用リング11が
挟み込まれている。この補強用リング11は、前
記幅広部7によつて貫通穴10と同心状に位置決
めされるので、両側プレート2を接合する前に一
方のプレート2の幅広部7内に嵌合しておけば良
く、特にプレート2に固着する必要はない。又、
この補強用リング11は第7図にも示すように内
周に環状溝12を備え、この環状溝12内からリ
ング外周面にわたつて周方向適当間隔置きに流通
路13が放射状に穿設されている。
The hollow panel 1 is provided with circular wide portions 7 formed by bulging both plates 2 outward at both ends of the flow path 3. A through hole 10 (see FIG. 6) for passing the fluid supply pipe 8 and fluid discharge pipe 9 shown in FIGS. 1 and 2 (see FIG. 6) is provided concentrically with the wide portion 7. As shown in FIGS. 1, 3, and 6, the wide portion 7 is provided with reinforcement whose inner diameter is approximately equal to the diameter of the through hole 10 and whose outer diameter is approximately equal to the inner diameter of the wide portion 7. A ring 11 for use is inserted. Since this reinforcing ring 11 is positioned concentrically with the through hole 10 by the wide portion 7, it can be fitted into the wide portion 7 of one plate 2 before joining the plates 2 on both sides. It is fine, and there is no particular need to fix it to the plate 2. or,
As shown in FIG. 7, this reinforcing ring 11 has an annular groove 12 on its inner periphery, and flow passages 13 are radially bored from inside this annular groove 12 to the outer circumferential surface of the ring at appropriate intervals in the circumferential direction. ing.

前記流体供給管8及び排出管9は、第1図及び
第2図に示すように支持プレート14に貫通状態
で取り付けられた流体供給主管15と流体排出主
管16の下端に夫々継手管17を介してT字形に
固着突設されたものであつて、遊端にはねじ部1
8を備えると共に、中空パネル1の取り付け領域
には軸方向にそつて延びるスリツト状の流通穴1
9が周方向複数箇所(図示例では4箇所)に設け
られている。
The fluid supply pipe 8 and the discharge pipe 9 are connected through joint pipes 17 to the lower ends of a fluid supply main pipe 15 and a fluid discharge main pipe 16, respectively, which are attached to the support plate 14 in a penetrating state, as shown in FIGS. 1 and 2. It is fixed and protruded in a T-shape, and the free end has a threaded part 1.
8, and a slit-shaped communication hole 1 extending along the axial direction in the mounting area of the hollow panel 1.
9 are provided at multiple locations in the circumferential direction (four locations in the illustrated example).

前記中空パネル1は、前記流体供給管8及び排
出管9が各幅広部7の貫通穴10を貫通するよう
に所要枚数が並列配置されるが、このとき継手管
17とこれに隣接する中空パネル1との間、及び
各中空パネル1の間には、前記流体供給管8及び
排出管9に外嵌する環状シール材20と、この環
状シール材20に外嵌するバツクアツプリング2
1とが介装される。勿論、前記環状シール材20
とバツクアツプリング21とは、各中空パネル1
の幅広部7の外側面に当接する。
A required number of the hollow panels 1 are arranged in parallel so that the fluid supply pipe 8 and the discharge pipe 9 pass through the through hole 10 of each wide portion 7. At this time, the joint pipe 17 and the adjacent hollow panel 1 and between each hollow panel 1, there is an annular sealing material 20 that fits over the fluid supply pipe 8 and the discharge pipe 9, and a back-up spring 2 that fits over the annular sealing material 20.
1 is interposed. Of course, the annular sealing material 20
and back spring 21 means each hollow panel 1
It comes into contact with the outer surface of the wide part 7 of the.

前記のように流体供給管8及び排出管9に並列
状にセツトされた各中空パネル1は、最外側の中
空パネル1との間にも環状シール材20とバツク
アツプリング21とを介装した状態で前記流体供
給管8及び排出管9の遊端ねじ部18に螺嵌した
ナツト22の締め付けにより、流体供給管8及び
排出管9の軸方向に締結一体化される。このとき
バツクアツプリング21が機能する状態まで各環
状シール材20が圧縮変形せしめられている。更
に前記流体供給管8及び排出管9の遊端ねじ部1
8にはロツクナツト兼用のキヤツプ23が螺嵌さ
れ、前記流体供給管8及び排出管9の遊端開口部
が閉じられている。
As described above, each hollow panel 1 set in parallel with the fluid supply pipe 8 and the discharge pipe 9 has an annular sealing material 20 and a back-up spring 21 interposed between it and the outermost hollow panel 1. In this state, the fluid supply pipe 8 and the discharge pipe 9 are fastened and integrated in the axial direction by tightening the nuts 22 screwed into the free end threaded portions 18 of the fluid supply pipe 8 and the discharge pipe 9. At this time, each annular seal member 20 is compressed and deformed to a state where the backup spring 21 functions. Furthermore, the free end threaded portions 1 of the fluid supply pipe 8 and the discharge pipe 9
A cap 23 which also serves as a lock nut is screwed into the fluid supply pipe 8 and the free end openings of the fluid supply pipe 8 and the discharge pipe 9 are closed.

尚、各中空パネル1の遊端両コーナー部は、各
中空パネル1のシーム溶接部4を貫通し且つ各中
空パネル1間に於いてスペーサー24が遊嵌せし
められた連結用軸杆25,26と、当該軸杆2
5,26の両端螺軸部に螺嵌されたナツト27
a,27bとによつて同様に締結一体化されてい
る。28は前記両軸杆25,26の中央位置を保
持するためのプレートであつて、前記流体供給管
8及び排出管9の中央に位置する継手管17にブ
ラケツト29及びボルトナツト30を介して取り
付けられている。
In addition, both free end corner portions of each hollow panel 1 are provided with connecting shaft rods 25 and 26 that pass through the seam welded portion 4 of each hollow panel 1 and have a spacer 24 loosely fitted between each hollow panel 1. and the said shaft 2
Nuts 27 screwed into the screw shafts at both ends of 5 and 26
a, 27b, and are similarly fastened and integrated. Reference numeral 28 denotes a plate for holding the center position of both shaft rods 25 and 26, and is attached to the joint pipe 17 located at the center of the fluid supply pipe 8 and discharge pipe 9 via a bracket 29 and a bolt/nut 30. ing.

以上のように構成されたパルス型熱交換器に於
いては、流体供給主管15から供給される流体は
継手管17から流体供給管8内に入り、スリツト
状流通穴19から流出する。この流体は、各中空
パネル1内の補強用リング11の内周環状溝12
から放射状の流通路13を経由して各中空パネル
1内のジグザグ状流路3の一端に流入し、このジ
グザグ状流路3内を流動して他端に至り、流体排
出管9に遊嵌する補強用リング11の放射状流通
路13、内周環状溝12、及び流体排出管9のス
リツト状流通穴19を経由して当該流体排出管9
内に流入し、この流体排出管9内から継手管17
及び流体排出主管16を経由して排出される。
In the pulse type heat exchanger configured as described above, the fluid supplied from the main fluid supply pipe 15 enters the fluid supply pipe 8 from the joint pipe 17 and flows out from the slit-shaped flow hole 19. This fluid flows through the inner annular groove 12 of the reinforcing ring 11 in each hollow panel 1.
The fluid flows from the radial flow path 13 to one end of the zigzag flow path 3 in each hollow panel 1, flows through the zigzag flow path 3, reaches the other end, and loosely fits into the fluid discharge pipe 9. The fluid discharge pipe 9 passes through the radial flow passage 13 of the reinforcing ring 11, the inner circumferential annular groove 12, and the slit-shaped flow hole 19 of the fluid discharge pipe 9.
The fluid flows into the joint pipe 17 from inside this fluid discharge pipe 9.
and is discharged via the fluid discharge main pipe 16.

従つて、互いに熱交換作用させる2流体の内の
一方の流体(第一流体)を上記流体供給主管15
に供給するようにし、このパネル型熱交換器を他
方の第二流体の貯蔵槽内又は当該第二流体の流通
路内にセツトして使用することにより、前記第二
流体は、前記各中空パネル1間の間隙内を流動す
る間に各中空パネル1の流路3内を流動する第一
流体との間で熱交換作用を受け、加熱又は冷却を
伴う所期の熱処理が行われる。
Therefore, one of the two fluids (the first fluid) which is caused to exchange heat with each other is supplied to the main fluid supply pipe 15.
By using this panel type heat exchanger by setting it in the storage tank of the other second fluid or in the flow path of the second fluid, the second fluid can be supplied to each of the hollow panels. While flowing in the gap between the hollow panels 1 and 1, it undergoes a heat exchange action with the first fluid flowing in the flow path 3 of each hollow panel 1, and a desired heat treatment involving heating or cooling is performed.

上記のように使用されるパネル型熱交換器は、
次のように分解掃除することが出来る。即ち、連
結用軸杆25,26の遊端に螺嵌されたナツト2
7a,27bを除去して両軸杆25,26を各中
空パネル1から引き抜くと共に各スペーサー24
を除去し、そして流体供給管8及び排出管9の遊
端に螺嵌されているキヤツプ23及びナツト22
を除去することにより、各中空パネル1と環状シ
ール材20及びバツクアツプリング21を前記両
管8,9からの軸方向に引き抜くことが出来る。
この結果、各中空パネル1を単独で自在に取り扱
うことが出来るので、必要な保守作業を簡単容易
に行うことが出来る。
The panel heat exchanger used as above is
It can be disassembled and cleaned as follows. That is, the nut 2 screwed into the free ends of the connecting shafts 25 and 26
7a, 27b and pull out both shaft rods 25, 26 from each hollow panel 1, and each spacer 24.
and the cap 23 and nut 22 screwed onto the free ends of the fluid supply pipe 8 and the discharge pipe 9.
By removing the hollow panels 1, the annular sealing material 20, and the back-up spring 21 can be pulled out in the axial direction from the tubes 8 and 9.
As a result, each hollow panel 1 can be freely handled independently, so that necessary maintenance work can be easily performed.

尚、上記実施例のように中空パネル1に補強用
リング11を位置決めする幅広部7を形成してお
くときは、当該補強用リング11を中空パネル1
の流路3に於ける内巾よりも幅広に形成し得るの
で、この補強用リング11の成形に都合が良くな
るばかりでなく、補強用リング11をプレート2
に溶接する必要もなくなり、組み立てが簡単とな
る。
In addition, when forming the wide part 7 for positioning the reinforcing ring 11 on the hollow panel 1 as in the above embodiment, the reinforcing ring 11 is attached to the hollow panel 1.
Since the reinforcing ring 11 can be formed wider than the inner width of the flow path 3, it is not only convenient to mold the reinforcing ring 11, but also the reinforcing ring 11 can be formed wider than the inner width of the flow path 3 of the plate 2.
There is no need for welding, making assembly easier.

前記補強用リング11の内径を流体供給管8及
び排出管9の外径より適当に大きくして、両者間
に十分な広さの環状空間が形成されるように構成
し、前記流体供給管8及び排出管9に対する中空
パネル1の位置決めは、この中空パネル1の両側
プレート2に設けられた貫通穴10(第6図参
照)によつて行えるように構成した場合には、当
該補強用リング11に設けた内周環状溝12は省
くことが出来る。又、補強用リング11の内周面
と前記流体供給管8及び排出管9の外周面との間
に広い環状空間が形成されなくとも、放射状の流
通路13を周方向に長い長孔とするか又は、前記
流体供給管8及び排出管9に設けられたスリツト
状の流通穴19を周方向に幅広に構成すると共に
前記補強用リング11側の放射状の流通路13を
周方向に小間隔で密に設ける等して、中空パネル
1を前記流体供給管8及び排出管9に取り付けた
とき、必ずスリツト状の流通穴19に放射状の流
通路13が対向するように構成すれば、前記と同
様に補強用リング11には内周環状溝12を設け
なくとも良い。
The inner diameter of the reinforcing ring 11 is made appropriately larger than the outer diameter of the fluid supply pipe 8 and the discharge pipe 9, so that a sufficiently large annular space is formed between them. In the case where the hollow panel 1 is positioned with respect to the discharge pipe 9 using the through holes 10 (see FIG. 6) provided in the plates 2 on both sides of the hollow panel 1, the reinforcing ring 11 The inner circumferential annular groove 12 provided in the inner circumferential groove 12 can be omitted. Moreover, even if a wide annular space is not formed between the inner circumferential surface of the reinforcing ring 11 and the outer circumferential surfaces of the fluid supply pipe 8 and the discharge pipe 9, the radial flow passage 13 can be made into a circumferentially long elongated hole. Alternatively, the slit-shaped flow holes 19 provided in the fluid supply pipe 8 and the discharge pipe 9 are made wide in the circumferential direction, and the radial flow passages 13 on the reinforcing ring 11 side are arranged at small intervals in the circumferential direction. If the hollow panel 1 is arranged so that the radial flow passages 13 always face the slit-shaped flow holes 19 when the hollow panel 1 is attached to the fluid supply pipe 8 and the discharge pipe 9, for example, by disposing them closely together, the same as above can be achieved. In addition, the inner circumferential annular groove 12 may not be provided in the reinforcing ring 11.

しかしながら前記内周環状溝12は、例えば中
ぐり切削加工により簡単容易に形成することが出
来るので、この内周環状溝12を設けて、前記流
体供給管8及び排出管9のスリツト状流通穴19
から補強用リング11の放射状流通路13への流
体の流通を、大きな抵抗を与えることなく円滑に
行わせ得るようにするのが望ましい。しかもこの
内周環状溝12の存在により放射状流通路13が
短くなるので、この流通路13の加工が容易に行
える。このような観点から第8図に示す補強用リ
ング11aのように前記内周環状溝12は、本来
の補強効果が得られる範囲内で深く形成するのが
望ましい。又、第9図に示す補強用リング11b
のように内側環状溝12は、リング内週面側が広
くなつた台形状の断面形状とする等、流体の流通
抵抗を少なくするような任意の断面形状に形成し
得る。
However, the inner circumferential annular groove 12 can be simply and easily formed by, for example, a boring process.
It is desirable to allow fluid to flow smoothly from the reinforcing ring 11 to the radial flow passages 13 of the reinforcing ring 11 without providing significant resistance. Furthermore, the presence of the inner circumferential annular groove 12 shortens the radial flow passages 13, so that machining of the flow passages 13 can be easily performed. From this point of view, it is desirable to form the inner circumferential annular groove 12 as deep as possible within the range where the original reinforcing effect can be obtained, as in the reinforcing ring 11a shown in FIG. Additionally, a reinforcing ring 11b shown in FIG.
The inner annular groove 12 can be formed to have any cross-sectional shape that reduces fluid flow resistance, such as a trapezoidal cross-sectional shape that is wider on the inner ring side.

第10図及び第11図に示す補強用リング11
cは、放射状流通路13の巾よりも内周環状溝1
2の巾を狭くしたものである。又、図示のように
放射状流通路13は周方向に長い角穴としたが、
長円形とする等、放射状流通路13の形状も限定
されない。
Reinforcing ring 11 shown in FIGS. 10 and 11
c is wider than the width of the radial flow path 13.
It is a narrower width of 2. Also, as shown in the figure, the radial flow passage 13 is a rectangular hole that is long in the circumferential direction.
The shape of the radial flow passage 13 is also not limited, such as an oval shape.

第12図及び第13図に示す補強用リング11
dは、内側に向かつて開放する断面溝形の外側環
状体31と外側に向かつて開放する断面溝形の内
側環状体32とから構成され、各環状体31,3
2の円周部で互いに相対向する箇所に放射状流通
路13となる貫通穴33が設けられている。この
ような構造を採用するときは、第14図に示すよ
うに内側環状体32の円周部32aの直径を外側
環状体31の両側内周縁31aの直径より大きく
することにより、内周環状溝12を形成し得る。
Reinforcing ring 11 shown in FIGS. 12 and 13
d is composed of an outer annular body 31 with a groove-shaped cross section that opens toward the inside and an inner annular body 32 with a groove-shaped cross section that opens toward the outside.
Through holes 33, which become radial flow passages 13, are provided at locations facing each other on the circumferential portions of the two. When adopting such a structure, as shown in FIG. 12 may be formed.

以上のように、補強用リング11の構造は特に
限定されない。勿論、成形材料に関しても、各種
金属、プラステイツク、セマミツク等、接触する
流体の種類や作用条件等に照らして最も好ましい
ものを選択すれば良い。又、環状シール材20に
外嵌させたバツクアツプリング21は、各中空パ
ネル1を締結一体化するときに全ての環状シール
材20を一定量圧縮させて、各中空パネル1間の
間隙を均等化し且つ環状シール材20によるシー
ル効果を確実にするのに役立つものであるが、こ
のバツクアツプリング21の使用は、本発明の必
須条件ではない。
As described above, the structure of the reinforcing ring 11 is not particularly limited. Of course, with regard to the molding material, the most preferable one may be selected, such as various metals, plastics, semamides, etc., in light of the type of fluid to be contacted, operating conditions, etc. In addition, the back-up spring 21 fitted onto the annular sealing material 20 compresses all the annular sealing materials 20 by a certain amount when the hollow panels 1 are fastened and integrated, thereby equalizing the gaps between the hollow panels 1. The use of the back-up spring 21 is not an essential condition of the present invention, although it is useful for ensuring the sealing effect of the annular seal member 20.

(発明の効果) 以上のように実施し得る本発明のパネル型熱交
換器は、各中空パネルを環状シール材と交互に流
体供給管及び流体排出管に管軸方向に嵌合締結す
るだけで簡単容易に組み立てることが出来る。し
かも各中空パネルを前記流体供給管及び排出管の
軸方向に締め付けて一体化するとき、各中空パネ
ルの両側プレートがその締め付け反力で内側に撓
むことを補強用リングによつて防止し、各中空パ
ネルの流体流入部及び流出部の空間を一定の巾に
確保し得るので、この中空パネル内への第一流体
の流入を所期通り良好に行わせ得る。又、前記補
強用リングの存在により、中空パネルを形成する
プレートとして必要最小限の厚みの薄板を利用す
ることが出来、経済的に実施することが出来る。
ことが出来る。流体供給管、排出管によつて中空
パネル、環状シール材の位置ぎめができる。
(Effects of the Invention) The panel heat exchanger of the present invention, which can be implemented as described above, can be achieved by simply fitting and fastening each hollow panel to a fluid supply pipe and a fluid discharge pipe alternately with an annular sealing material in the pipe axis direction. Easy to assemble. Moreover, when each hollow panel is tightened in the axial direction of the fluid supply pipe and the discharge pipe to be integrated, the reinforcing ring prevents the plates on both sides of each hollow panel from bending inward due to the reaction force of the tightening, Since the spaces of the fluid inflow and outflow portions of each hollow panel can be secured to a constant width, the first fluid can smoothly flow into the hollow panel as expected. Furthermore, due to the presence of the reinforcing ring, a thin plate with the minimum necessary thickness can be used as the plate forming the hollow panel, which can be implemented economically.
I can do it. The hollow panel and annular sealing material can be positioned by the fluid supply pipe and discharge pipe.

更に、各中空パネルの締め付けを解いて各中空
パネル及び環状シール材を前記流体供給管及び排
出管より軸方向に抜き取るだけで簡単容易に分解
し得るので、各中空パネル間の間隙を流動する第
二流体のスケールが各中空パネルの表面に付着し
て熱交換効率が低下したり、第二流体の流通抵抗
が不当に増大したような場合、前記のように分解
して各中空パネルを分離することにより、当該中
空パネルの表面のスケール除去等、必要な保守作
業を極めて簡単容易に行うことが出来る。従つて
本発明のパネル型熱交換器は、スケールが発生付
着し易い第二流体を使用する条件に於いても支障
なく活用し得る。
Furthermore, it can be easily disassembled simply by unfastening each hollow panel and pulling out each hollow panel and annular sealing material from the fluid supply pipe and discharge pipe in the axial direction. If the scale of the two fluids adheres to the surface of each hollow panel, reducing heat exchange efficiency or unduly increasing the flow resistance of the second fluid, disassemble and separate each hollow panel as described above. As a result, necessary maintenance work such as removing scale from the surface of the hollow panel can be performed extremely easily. Therefore, the panel heat exchanger of the present invention can be used without any problem even under conditions where the second fluid is used where scale is likely to be generated and adhered.

又、流体供給管及び流体排出管は、各中空パネ
ルと環状シール材とによつて第二流体の流路とな
る外界に対し完全に隔離され、第二流体と接触す
る恐れが全くないので、前記流体供給管及び流体
排出管は、これら管路内を流通する第一流体との
関係で悪影響の生じない材質の管でありさえすれ
ば良く、第一流体及び第二流体両者の条件を考慮
して材質を選択する必要は全くない。例えば、第
一流体が水、熱湯、水蒸気等である場合は、仮に
第二流体が強酸性のものであつても流体供給管及
び流体排出管は安価な鉄系の材料(SSやSUS等)
で構成されたものを利用することが出来るので経
済的である。
In addition, the fluid supply pipe and the fluid discharge pipe are completely isolated from the outside world by each hollow panel and the annular sealing material, which serves as a flow path for the second fluid, and there is no risk of contact with the second fluid. The fluid supply pipe and the fluid discharge pipe need only be made of a material that does not have an adverse effect in relation to the first fluid flowing in these pipes, and the conditions of both the first fluid and the second fluid should be taken into consideration. There is no need to select the material accordingly. For example, if the first fluid is water, hot water, steam, etc., even if the second fluid is strongly acidic, the fluid supply pipe and fluid discharge pipe are made of inexpensive iron-based materials (SS, SUS, etc.).
It is economical because it can be used with

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

第1図は一部縦断側面図、第2図は一部縦断正
面図、第3図は第1図のA−A線での拡大断面
図、第4図は第1図のB−B線での拡大断面図、
第5図は第4図のC−C線での拡大断面図、第6
図は本発明要部の拡大縦断側面図、第7図は補強
用リングの斜視図、第8図及び第9図は前記補強
用リングの変形例を示す要部の縦断面図、第10
図及び第12図は他の実施例の補強用リングを示
す斜視図、第11図は第10図の要部拡大縦断面
図、第13図は第12図の要部拡大縦断面図、第
14図は第12図に示す補強用リングの変形例を
示す要部の縦断面図である。 1……熱交換用中空パネル、7……中空パネル
幅広部、8……流体供給管、9……流体排出管、
10……貫通穴、11,11a〜11d……補強
用リング、12……内周環状溝、13……放射状
流通路、15……流体供給主管、16……流体排
出主管、19……スリツト状流通穴、20……環
状シール材、21……バツクアツプリング、2
2,27a,27b……ナツト、23……ロツク
ナツト兼用のキヤツプ、24……スペーサー、2
5,26……連結用軸杆、28……軸杆支持プレ
ート。
Fig. 1 is a partially longitudinal side view, Fig. 2 is a partially longitudinal front view, Fig. 3 is an enlarged sectional view taken along line A-A in Fig. 1, and Fig. 4 is a line BB in Fig. 1. Enlarged cross-sectional view at
Figure 5 is an enlarged sectional view taken along line C-C in Figure 4;
7 is a perspective view of a reinforcing ring, FIGS. 8 and 9 are longitudinal sectional views of essential parts showing modified examples of the reinforcing ring, and FIG.
11 and 12 are perspective views showing reinforcing rings of other embodiments, FIG. 11 is an enlarged vertical cross-sectional view of the main parts of FIG. 10, and FIG. 13 is an enlarged longitudinal cross-sectional view of the main parts of FIG. FIG. 14 is a longitudinal cross-sectional view of a main part showing a modification of the reinforcing ring shown in FIG. 12. 1... Hollow panel for heat exchange, 7... Hollow panel wide part, 8... Fluid supply pipe, 9... Fluid discharge pipe,
10...Through hole, 11, 11a to 11d...Reinforcing ring, 12...Inner peripheral annular groove, 13...Radial flow passage, 15...Fluid supply main pipe, 16...Fluid discharge main pipe, 19...Slit Shape circulation hole, 20... Annular sealing material, 21... Backup spring, 2
2, 27a, 27b... Nut, 23... Cap that can also be used as locking nut, 24... Spacer, 2
5, 26... Connecting rod, 28... Axis rod support plate.

Claims (1)

【特許請求の範囲】 1 2枚のプレートを両者間に流路を形成するよ
うに互に接合して構成された熱交換用中空パネル
に流体供給管と流体排出管とを各別に貫通させる
貫通穴を設け、この貫通穴の周囲に於いて前記両
側プレート間に、当該両側プレート間の間隔が狭
くなるのを阻止し且つ放射状の流通路とこれに連
通する内周環状溝とを有する補強リングを介装
し、外周に軸方向に延びる流通穴を備えた流体供
給管及び流体排出管に所要枚数の前記中空パネル
を、各中空パネル間に於いて前記流体供給管及び
排出管にこれらの外径にほぼ等しい内径の環状シ
ール材を外嵌させた状態で、管軸方向に引き抜き
分解可能に嵌合し、締結一体化したことを特徴と
するパネル型熱交換器。 2 前記中空パネルの貫通穴形成箇所は両側プレ
ートを外側に膨出させて幅広部とし、この幅広部
内に前記補強用リングを嵌合した前記第1項記載
の熱交換器。 3 前記各環状シールには、隣接する中空パネル
間の間〓が一定以下になるのを阻止するバツクア
ツプリングを外嵌させてある前記第1項乃至第2
項の何れかに記載の熱交換器。
[Scope of Claims] 1. A through hole in which a fluid supply pipe and a fluid discharge pipe are respectively penetrated through a hollow panel for heat exchange, which is constructed by joining two plates to each other so as to form a flow path between them. a reinforcing ring provided with a hole, and having a radial flow path and an inner circumferential annular groove communicating with the radial flow path, which prevents the gap between the both side plates from narrowing between the both side plates around the through hole; A required number of the hollow panels are inserted into the fluid supply pipe and the fluid discharge pipe, each having a communication hole extending in the axial direction on the outer periphery. A panel heat exchanger characterized in that an annular sealing material having an inner diameter approximately equal to the diameter is fitted onto the outside, and the panel is fitted in such a manner that it can be pulled out and disassembled in the axial direction of the tube, and is fastened and integrated. 2. The heat exchanger according to item 1, wherein the through-hole forming portion of the hollow panel is formed by bulging both side plates outward to form a wide portion, and the reinforcing ring is fitted into the wide portion. 3. Each of the annular seals is fitted with a back-up spring that prevents the distance between adjacent hollow panels from becoming less than a certain level.
The heat exchanger described in any of paragraphs.
JP15317285A 1985-07-10 1985-07-10 Heat exchanger of panel type Granted JPS6213995A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15317285A JPS6213995A (en) 1985-07-10 1985-07-10 Heat exchanger of panel type

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15317285A JPS6213995A (en) 1985-07-10 1985-07-10 Heat exchanger of panel type

Publications (2)

Publication Number Publication Date
JPS6213995A JPS6213995A (en) 1987-01-22
JPH0313517B2 true JPH0313517B2 (en) 1991-02-22

Family

ID=15556625

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15317285A Granted JPS6213995A (en) 1985-07-10 1985-07-10 Heat exchanger of panel type

Country Status (1)

Country Link
JP (1) JPS6213995A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE462763B (en) * 1989-04-28 1990-08-27 Torell Ab PLATFORM HEAT EXCHANGE / COOLER AND WERE MANUFACTURED TO MANUFACTURE THIS
US5413169A (en) * 1993-12-17 1995-05-09 Ford Motor Company Automotive evaporator manifold
FI104518B (en) * 1997-01-23 2000-02-15 Hadwaco Ltd Oy Heat transfer elements and of the same heat exchanger
US8028410B2 (en) * 2008-12-08 2011-10-04 Randy Thompson Gas turbine regenerator apparatus and method of manufacture
JP6857113B2 (en) * 2017-12-08 2021-04-14 株式会社日阪製作所 Plate heat exchanger

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5333878U (en) * 1976-08-30 1978-03-24

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5333878U (en) * 1976-08-30 1978-03-24

Also Published As

Publication number Publication date
JPS6213995A (en) 1987-01-22

Similar Documents

Publication Publication Date Title
US7004237B2 (en) Shell and plate heat exchanger
US4733722A (en) Shell- and tube-type heat exchangers and their production
US9250022B2 (en) Spiral heat exchanger
US20040069450A1 (en) Component for supporting a filter member, a device including a tubular filter member and said component, a plate heat exchanger including a tubular filter member and said component
JPH0313517B2 (en)
GB2041191A (en) Heat exchanger
JPH0313519B2 (en)
JPH0313518B2 (en)
JPS63502847A (en) Shell and tube heat exchanger
JPH0463318B2 (en)
JPH0313520B2 (en)
NZ243797A (en) Opposed bayonet heat exchanger with spaced baffles: baffles formed by
JPH0313516B2 (en)
JPS59164894A (en) Compression and sealing of tube in multitubular type heat exchanger
JPH0619973Y2 (en) Panel heat exchanger
JPH0446359B2 (en)
JP2000111278A (en) Multitubular heat exchanger
JP2535883Y2 (en) Double tube heat exchanger
JPH0113274Y2 (en)
JP2691162B2 (en) Spiral heat exchanger
JPH0629444Y2 (en) Oil cooler
JPH0645190Y2 (en) Heat exchanger
JPH08622Y2 (en) Fluororesin heat exchanger seal structure
JPS62245093A (en) Panel laminated heat exchanger
JPH087270Y2 (en) Glass-lined multi-tube heat exchanger that can be withdrawn from both ends of the shell