JPH02192932A - Manufacture of resin fine tube heat exchanger - Google Patents

Manufacture of resin fine tube heat exchanger

Info

Publication number
JPH02192932A
JPH02192932A JP1012659A JP1265989A JPH02192932A JP H02192932 A JPH02192932 A JP H02192932A JP 1012659 A JP1012659 A JP 1012659A JP 1265989 A JP1265989 A JP 1265989A JP H02192932 A JPH02192932 A JP H02192932A
Authority
JP
Japan
Prior art keywords
heat transfer
predetermined
tube
heat exchanger
adhesive
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
Application number
JP1012659A
Other languages
Japanese (ja)
Inventor
Masanori Kawazoe
政宣 川添
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.)
Daikin Industries Ltd
Original Assignee
Daikin Industries Ltd
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 Daikin Industries Ltd filed Critical Daikin Industries Ltd
Priority to JP1012659A priority Critical patent/JPH02192932A/en
Publication of JPH02192932A publication Critical patent/JPH02192932A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F21/00Constructions of heat-exchange apparatus characterised by the selection of particular materials
    • F28F21/06Constructions of heat-exchange apparatus characterised by the selection of particular materials of plastics material
    • F28F21/062Constructions of heat-exchange apparatus characterised by the selection of particular materials of plastics material the heat-exchange apparatus employing tubular conduits

Abstract

PURPOSE:To make the arranging density of many fine heat transfer tubes made of resin uniform, to realize a zigzaglike fluid passage structure and to improve heat exchanging efficiency by coating the many heat transfer tubes with adhesive, winding them on a core rod of a predetermined structure as a rolled heat transfer tube, and engaging it with a baffle plate. CONSTITUTION:Heat transfer tubes 11 each made of many synthetic resin fine tubes are aligned in parallel at an equal interval. They are coated at a predetermined interval in a stripe shape with adhesive 12. The discs of core rods 5 are abutted against the corresponding adhesive coating parts from the coated end side, and adhesively wound on the outer surface while adhesively rotating. Thus, a ringlike adhesive layer 6 sealed from the inner surface side to the outer surface side is formed at the adhered part on the outer surface of the disc 4, bundled, and an inner partition chamber 13 is formed. The discs 4 are disposed on non-corresponding predetermined adhesive layer 6 to be engaged with a ringlike baffle plate 7 to form an outer partition wall 12. Eventually, a predetermined ending process is performed on the respective heat transfer tubes 11. The rolled heat transfer tube body 10 is contained and installed in a tube body 1 through the baffle plate 7.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、樹脂細管製熱交換器の製造方法に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a method for manufacturing a resin tube heat exchanger.

(従来技術) 近年、合成樹脂製伝熱管を用いた多管式シェル型熱交換
器の開発が進められているが、合成樹脂製伝熱管は、金
属製伝熱管に比べて熱伝導率が極端に低いため、耐圧性
の低下およびゴミ詰まりの無いこと等を考慮した上で、
できるだけ伝熱管径を小さくして細管状に形成し且つ伝
熱管肉厚を薄くすることにより、熱抵抗の低減と伝熱面
積の増大とを図るようにして熱交換効率を向上させるよ
うにしている。
(Prior art) In recent years, development of multi-tube shell heat exchangers using synthetic resin heat exchanger tubes has been progressing, but synthetic resin heat exchanger tubes have extremely low thermal conductivity compared to metal heat exchanger tubes. Considering that the pressure resistance is low and there is no dust clogging, etc.,
By reducing the diameter of the heat transfer tube as much as possible, forming it into a thin tube shape, and reducing the wall thickness of the heat transfer tube, the heat exchange efficiency is improved by reducing thermal resistance and increasing the heat transfer area. There is.

しかし、一方そのように肉厚が薄く、しかも管径が小さ
い細管構造のものにすると、自然とblみを生じてしま
い保持が難しい問題がある。そこで、通常該合成樹脂製
伝熱細管を多数本円筒状に結束して使用することが考え
られるが、単に結束状態としたのでは、各細管間の結束
密度を均一にすることが困難で伝熱管外を流通する熱媒
体が全部の伝熱管と接触し得るように均一に流れないで
、偏流を起こすことがあり、一部の伝熱管が熱交換に十
分活かされないという問題がある。そこで、例えば第5
図に示すように複数本の伝熱管束21a〜21eの中心
部に多数の穴を有する中心コア(図示省略)を設けると
ともに該中心コアに伝熱管束と直交する複数枚のバッフ
ルプレート22a〜22dを配置し、該バッフルプレー
ト22a〜22dを介して伝熱管束21a〜21eを管
胴23内に嵌装することにより、伝熱管外を流通する熱
媒体の偏流をなくすようにしたものが既に提案されてい
る(例えば、実開昭62−192088号公報参照)。
However, on the other hand, if a thin tube structure with such a thin wall thickness and a small tube diameter is used, there is a problem in that it is difficult to maintain because blister naturally occurs. Therefore, it is usually considered to use a large number of heat transfer capillary tubes made of synthetic resin tied together in a cylindrical shape, but if they are simply tied together, it is difficult to make the bundling density uniform among the capillary tubes. There is a problem in that the heat medium flowing outside the heat exchanger tubes does not flow uniformly so that it can come into contact with all the heat exchanger tubes, and uneven flow may occur, so that some heat exchanger tubes are not fully utilized for heat exchange. Therefore, for example, the fifth
As shown in the figure, a central core (not shown) having a large number of holes is provided at the center of a plurality of heat exchanger tube bundles 21a to 21e, and a plurality of baffle plates 22a to 22d are provided in the center core to be perpendicular to the heat exchanger tube bundles. It has already been proposed that the heat transfer tube bundles 21a to 21e are arranged inside the tube body 23 via the baffle plates 22a to 22d to eliminate uneven flow of the heat medium flowing outside the heat transfer tubes. (See, for example, Japanese Utility Model Application No. 192088/1988).

そして、この従来技術の構成では、特に熱交換効率の向
上を狙って管束の固定位置が隣合うバッフルプレート相
互間で交互にずれるように構成されている。
In the configuration of this prior art, the fixing positions of the tube bundles are alternately shifted between adjacent baffle plates, particularly with the aim of improving heat exchange efficiency.

(発明が解決しようとする課り ところが、上記従来技術上の構成の場合、伝熱管が複数
の管束に分割されているために複数の管束間の隙間に較
べ各管束部の伝熱管間の隙間が非常に狭くなってしまい
、管束部の中を十分に熱交換流体が流通せず、その熱交
換性能が低下する問題がある。
(The problem that the invention seeks to solve is that in the case of the above-mentioned prior art configuration, the heat exchanger tubes are divided into a plurality of tube bundles, so the gap between the heat exchanger tubes in each tube bundle is smaller than the gap between the plurality of tube bundles.) There is a problem in that the tube bundle becomes very narrow, and the heat exchange fluid does not flow sufficiently through the tube bundle, resulting in a decrease in heat exchange performance.

(課題を解決するための手段) 本発明は、上記の問題を解決することを目的としてなさ
れたもので、例えば第1図〜第3図に示すように、所定
長さの熱交換用樹脂細管11,11・・を多数本並設し
、当該各樹脂細管11.l!・・の並設方向に所定の硬
化性接着剤12.12・・を所定の間隔を置いて複数個
所帯状に塗布して行き、それら各接着剤塗布部の所定間
隔置きの塗布部に対応して内部隔壁機能をもった円板状
の巻取部4.4・・を設けた心棒5を利用して当該多数
本の樹脂細管11.11・・を巻取って行くことにより
ロール状に巻成一体化し、該巻成されたロール状伝熱管
体10の上記接着剤塗布部6゜6・・の所定のものに対
応して外部隔壁機能を持った所定幅のバッフルプレート
7.7・・を嵌合した後、端末処理を施すようにしたこ
とを特徴とするものである。
(Means for Solving the Problems) The present invention has been made for the purpose of solving the above-mentioned problems. For example, as shown in FIGS. A large number of resin tubes 11, 11, etc. are arranged in parallel, and each resin thin tube 11. l! A predetermined curable adhesive 12.12... is applied in a plurality of strips at predetermined intervals in the direction in which the curable adhesives 12, 12, and so on are arranged in parallel. The plurality of resin tubes 11, 11, etc. are wound into a roll using a mandrel 5 provided with a disk-shaped winding part 4,4, which has an internal partition function. Baffle plates 7, 7, 7, 7, 7, 7, 7, 9, 7, 7, 9, 7, 7, 7, 7, 7, 7, 7, and 7, each having an external partition function as an external partition wall, correspond to the adhesive-applied portions 6. After the two are fitted together, terminal processing is performed.

(作 用) 上記本発明の樹脂細管製熱交換器の製造方法では所定長
さの樹脂細管+ 1.11・・を多数本並設した上で当
該樹脂細管11.11・・の並設方向に所定の硬化性接
着剤12.12・・を複数個所帯状に塗布して行き、該
帯状の接着剤の所定間隔毎の塗布部に対応して内部隔壁
を形成する円板状の巻取部4.4・・を位置せしめロー
ル状に巻成して一体化するようになっている。従って、
該巻成されたロール状の伝熱管体IOは、多数本の樹脂
細管11.11よりなる伝熱管の各々が周方向及び半径
方向共に所定間隔で均密に配設されることになる。
(Function) In the method for manufacturing a resin capillary heat exchanger of the present invention, a large number of resin capillaries +1.11... of a predetermined length are arranged in parallel, and then the resin capillary tubes 11,11... are arranged in parallel. A plurality of predetermined curable adhesives 12, 12, etc. are applied in a strip-like manner, and internal partition walls are formed in correspondence with the coated portions of the strip-shaped adhesive at predetermined intervals. 4.4... are positioned and wound into a roll to be integrated. Therefore,
In the wound roll-shaped heat exchanger tube body IO, heat exchanger tubes each consisting of a large number of resin thin tubes 11, 11 are arranged evenly at predetermined intervals in both the circumferential direction and the radial direction.

そして、さらに上記のように構成されたロール状の伝熱
管体10の外周側所定間隔毎の接着剤塗布部6.6・・
に外部隔壁機能を持ったバッフルプレート7.7・・を
嵌合して結束するとともに最終的に端末処理を施して例
えばシェル筺体内に撓みなく固定して保持される。
Further, adhesive application portions 6.6 are provided at predetermined intervals on the outer circumferential side of the roll-shaped heat transfer tube body 10 configured as described above.
A baffle plate 7, 7, etc. having an external partition function is fitted to the baffle plates 7, 7, etc., and the baffle plates 7, 7, .

(発明の効果) 従って、上記本発明の樹脂細管製熱交換器の製造方法に
よると、比較的容易な方法で、しかも低コストに伝熱管
配役密度が均一で、熱交換流体の偏流がなく熱交換効率
が高い樹脂細管製熱交換器を提供することができるよう
になる。
(Effects of the Invention) Therefore, according to the method for manufacturing a heat exchanger made of resin tubes of the present invention, the heat exchanger tube arrangement density is uniform, there is no uneven flow of the heat exchange fluid, and the heat exchanger can be heated by a relatively easy method and at a low cost. It becomes possible to provide a resin tube heat exchanger with high exchange efficiency.

(実施例) 第1図〜第4図は、本発明の実施例に係る樹脂細管製シ
ェルデユープ型熱交換器のもが成を示している。
(Example) FIGS. 1 to 4 show the construction of a resin tube shell duplex heat exchanger according to an example of the present invention.

先ず第4図は、同樹脂細管製シェルチューブ型熱交換器
の全体的な構成を示しており、図中符号lは所定径の管
胴である。該管胴1の両端には管板2.2が例えば溶接
等の方法によって取り付けられており、該管板2.2を
利用して後述するロール状の伝熱管体10が当該管胴1
内に図示の如く収納固定されるようになっている。また
符号3゜3は各々上記各管板2.2の外側に取付けられ
る蓋である。
First, FIG. 4 shows the overall structure of the shell-tube heat exchanger made of thin resin tubes, and reference numeral 1 in the figure indicates a tube body of a predetermined diameter. Tube sheets 2.2 are attached to both ends of the tube body 1 by a method such as welding, and a rolled heat transfer tube body 10 (described later) is attached to the tube body 1 by using the tube sheets 2.2.
It is designed to be stored and fixed inside as shown in the figure. Reference numeral 3.3 denotes a lid attached to the outside of each tube sheet 2.2.

伝熱管体1.0は、第1図〜第3図に示すように、中心
部に心棒5を有し、該心棒5に所定の間隔で嵌合された
内部隔壁となる円板4.4・・を介して内側に所定の空
間部を形成する状態でロール状に巻成された合成樹脂細
管製の、多数本の伝熱管11.11・・よりなっており
、該ロール状の伝熱管体lOの内周面部側から外周には
所定の間隔でリング状に硬化した接着剤層6,6・・が
形式されており該リング状の接着剤層6.6・・によっ
て結束され、且つ各伝熱管11.11・・間が軸方向に
シールされている。また該伝熱管体IOの上記リング状
接着剤層6.6・・の外周面部には、例えばひとつ置き
に更に大径のバッフルプレート7.7・・が嵌合されて
おり、該バッフルプレート77・・を介して当該ロール
状伝熱管体10の全体が全く撓みなく上記管311内に
嵌装状態で設置されるようになっているとともに該バッ
フルプレート7.7・・が伝熱管体IO外における熱交
換用の隔室12.12・・を形成している。
As shown in FIGS. 1 to 3, the heat transfer tube body 1.0 has a mandrel 5 in the center, and a disk 4.4 serving as an internal partition wall is fitted to the mandrel 5 at a predetermined interval. It consists of a large number of heat transfer tubes 11, 11... made of thin synthetic resin tubes wound into a roll to form a predetermined space inside through the roll-shaped heat transfer tubes. Ring-shaped hardened adhesive layers 6, 6... are formed at predetermined intervals from the inner peripheral surface side to the outer periphery of the body 1O, and are bound by the ring-shaped adhesive layers 6, 6..., and Each heat exchanger tube 11, 11... is sealed in the axial direction. In addition, baffle plates 7.7, which have a larger diameter, are fitted to the outer circumferential surface of the ring-shaped adhesive layers 6.6, . The entire rolled heat transfer tube 10 is installed in a fitted state within the tube 311 without bending at all, and the baffle plates 7,7... are installed outside the heat transfer tube IO. It forms compartments 12, 12, . . . for heat exchange.

また上記バッフルプレート7.7・・は、上記所定間隔
を置いて複数の個所に形成されているリング状の接着剤
層6.6・・の中の少くと1も内側に上記内部隔壁機能
を果す円板4.4・・が存在しないものに対してのみ嵌
合されるようになっており、上記ロール状の伝熱管体!
0が第4図のように管胴1内に嵌装された状態において
上記伝熱管体lOの内側に熱交換用の流体が流通する流
体通路を形成するようになっている(第2図参照)。
In addition, the baffle plates 7.7... have the internal partition function on at least one of the ring-shaped adhesive layers 6.6... formed at a plurality of locations at predetermined intervals. The disc 4.4... is designed to be fitted only to those that do not exist, and the above-mentioned rolled heat transfer tube body!
0 is fitted into the tube body 1 as shown in FIG. 4, a fluid passage through which a heat exchange fluid flows is formed inside the heat transfer tube 10 (see FIG. 2). ).

また上記円板4.4は、該流体通路の両側に位置し、該
流体通路を含んで上記外部隔室12と連通ずる内部隔室
13を形成している。
The discs 4.4 also define an internal compartment 13 which is located on either side of the fluid passageway and communicates with the external compartment 12, including the fluid passageway.

従って、第2図から明らかなように上記伝熱管体10は
、管胴1内に於いて上記伝熱管体外部隔壁としてのバッ
フルプレート7.7・・と上記伝熱管体内部隔壁として
の円板4.4・・とによって、上記所定間隔を保って均
密に@層された多数本の伝熱管11.11・・層を介し
て半径方向にジグザグに熱交換用の流体が流れる内外通
路が形成されることになり、偏流が生じないことはもち
ろん、各伝熱管2.2・・と熱交換用流体との接触、伝
熱効率が大きく向上して特に熱交換性能がよくなる。
Therefore, as is clear from FIG. 2, the heat exchanger tube 10 has baffle plates 7, 7, . 4.4..., the inner and outer passages through which the heat exchange fluid flows in a zigzag manner in the radial direction through the multiple heat transfer tubes 11. As a result, not only no drift occurs, but also the contact between each heat exchanger tube 2,2... and the heat exchange fluid and the heat transfer efficiency are greatly improved, and the heat exchange performance is particularly improved.

ところで、該伝熱管体IOは、次のようにして製造され
る。
By the way, the heat transfer tube body IO is manufactured as follows.

(1)先ず多数本の合成樹脂細管よりなる伝熱管11.
11・・を第1図に示すように等間隔で平行に正確に並
べる。
(1) First, the heat transfer tube 11 is made of a large number of synthetic resin thin tubes.
11... are accurately arranged in parallel at equal intervals as shown in FIG.

(2)次に該並設状態・の伝熱管11.II・・に対し
て所定の間隔で帯状に接着剤12.12・・を塗布する
。該接着剤12.12・・の塗布位置は、上記心棒5側
の円板4の嵌合位置とそれらの中間の上述したリング状
バッフルプレート7.7・・の嵌合位置の各々に対応し
て設定される。
(2) Next, the heat exchanger tubes 11 in the juxtaposed state. Adhesive 12, 12... is applied in strips at predetermined intervals to II.... The application positions of the adhesives 12, 12, etc. correspond to the fitting positions of the disc 4 on the side of the mandrel 5 and the fitting positions of the ring-shaped baffle plates 7, 7, etc. between them. is set.

(3)その後、上記心棒5の各円板4.4・・を各々上
記対応する接着剤塗布部に塗布端側から当接し、接着回
転させながら当該円板4.4・・の外周面上にロール状
に接合巻成さ仕て行く。
(3) After that, each disc 4.4 of the mandrel 5 is brought into contact with the corresponding adhesive application part from the application end side, and while the adhesive is rotated, the outer peripheral surface of the disc 4.4 is It is then bonded and wound into a roll.

そして、そのようにして当該円板4.4・・外周面上の
接合部で内周面側から外周面側までシールされた第2図
に示すようなリング状の接着剤層6.6・・を形成する
ことによって結束し、かつ上述した内部隔室13.13
を形成する。
In this way, a ring-shaped adhesive layer 6.6 as shown in FIG. 13.13.
form.

(4)上記(3)のようにして形成されたロール状の伝
熱管体10の外周の上記円板4.4が対応しない所定の
接着剤層6.6・・上に位置して第2図に示すようにリ
ング状のバッフルプレート7゜7・・を嵌合して外部隔
室12.12を形成する。
(4) The disk 4.4 on the outer periphery of the rolled heat transfer tube 10 formed as in (3) above is located on a predetermined adhesive layer 6.6 that does not correspond to the second adhesive layer 6.6. As shown in the figure, ring-shaped baffle plates 7.7 are fitted to form external compartments 12, 12.

(5)最後に熱融着等の方法により各伝熱管11゜11
・・に所定の端末処理を施す。
(5) Finally, each heat exchanger tube 11°11
Perform the specified terminal processing on...

そして、以上のようにして構成された第2図に示すロー
ル状の伝熱管体10が第4図に示すように管胴1内に上
記バッフルプレート7.7・・を介して収納設置される
Then, the roll-shaped heat transfer tube body 10 shown in FIG. 2 and configured as described above is housed and installed in the tube body 1 via the baffle plates 7, 7, etc., as shown in FIG. 4. .

従って、この結果、上記実施例の樹脂細管製シェルチュ
ーブ型熱交換器の構成によると、多数本の樹脂細管製の
伝熱管11に接着剤12を塗布し、所定構造の心棒5に
巻取って行くだけでロール状の伝熱管体IOが容易かつ
高精度に形成される。
Therefore, according to the structure of the shell tube heat exchanger made of resin thin tubes of the above embodiment, adhesive 12 is applied to a large number of resin thin tube heat exchanger tubes 11, and the adhesive 12 is wound around the mandrel 5 having a predetermined structure. A roll-shaped heat exchanger tube IO can be formed easily and with high precision just by going.

そして、それによって上記接着剤12を塗布した巻層部
にリング状の接着剤1116.6・・を形成し、最後に
バッフルプレート7.7・・を嵌合するだけで結束と内
外隔室の形成が共に可能となり、しかも各伝熱管11.
11・・の配設密度の均一化とジグザグ状の効果的な流
体通路構造の実現により・相当な熱交換効率の向上効果
を得ることができるようになる。
Then, a ring-shaped adhesive 1116.6 is formed on the wound layer portion coated with the adhesive 12, and finally, the baffle plates 7, 7, and so on are simply fitted to bind and separate the inner and outer compartments. It is possible to form both heat exchanger tubes 11.
11. By making the arrangement density uniform and realizing an effective zigzag fluid passage structure, it becomes possible to obtain a considerable improvement in heat exchange efficiency.

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

第1図は、本発明の実施例に係る樹脂細管製熱交換器の
ロール状伝熱管体の展開状態(製造過程)の斜視図、第
2図は、同ロール状伝熱管体の斜視図、第3図は、同要
部の断面図、第4図は、同実施例構造のシェルチューブ
型熱交換の一部切欠正面図、第5図は、従来のシェルデ
ユープ型熱交換器の一部切欠正面図である。 1・・・・・管胴 2・・・・・管板 3・・・・・蓋 4・・・・・円板 5・・・・・心棒 6・・・・・リング状接着剤層 7・・・・・バッフルプレート lO・・・・伝熱管体 11・・・・伝熱管 12・・・・接着剤 第1図 第4図 第5図 ゛“第3図
FIG. 1 is a perspective view of a developed state (manufacturing process) of a rolled heat exchanger tube of a resin tube heat exchanger according to an embodiment of the present invention, FIG. 2 is a perspective view of the rolled heat exchanger tube, Fig. 3 is a sectional view of the same essential parts, Fig. 4 is a partially cutaway front view of a shell tube type heat exchanger having the same structure, and Fig. 5 is a partially cutaway front view of a conventional shell duplex type heat exchanger. It is a front view. 1...Tube body 2...Tube sheet 3...Lid 4...Disk 5...Mandrel 6...Ring-shaped adhesive layer 7 ... Baffle plate lO ... Heat transfer tube body 11 ... Heat transfer tube 12 ... Adhesive Fig. 1 Fig. 4 Fig. 5 "Fig. 3

Claims (1)

【特許請求の範囲】[Claims] 1、所定長さの熱交換用樹脂細管(11),(11)・
・を多数本並設し、当該各樹脂細管(11),(11)
・・の並設方向に所定の硬化性接着剤(12),(12
)・・を所定の間隔を置いて複数個所帯状に塗布して行
き、それら各接着剤塗布部の所定間隔置きの塗布部に対
応して内部隔壁機能をもった円板状の巻取部(4),(
4)・・を設けた心棒(5)を利用して当該多数本の樹
脂細管(11),(11)・・を巻取って行くことによ
りロール状に巻成一体化し、該巻成されたロール状伝熱
管体(10)外周部の上記接着剤塗布部(6),(6)
・・の所定のものに対応して外部隔壁機能をもった所定
幅のバッフルプレート(7),(7)・・を嵌合した後
、端末処理を施すようにしたことを特徴とする樹脂細管
製熱交換器の製造方法。
1. Heat exchange resin thin tube (11), (11) of a predetermined length.
A large number of ・ are installed in parallel, each resin thin tube (11), (11)
A predetermined curable adhesive (12), (12
)... is applied in multiple strips at predetermined intervals, and a disc-shaped winding part ( 4),(
4) By winding up the plurality of resin thin tubes (11), (11), etc. using the mandrel (5) provided with..., they are wound into a roll and integrated. The adhesive application portions (6), (6) on the outer periphery of the rolled heat transfer tube (10)
A resin capillary tube characterized in that after fitting baffle plates (7), (7), etc. of a predetermined width with an external partition function corresponding to a predetermined one, terminal treatment is performed. A method for manufacturing a heat exchanger.
JP1012659A 1989-01-20 1989-01-20 Manufacture of resin fine tube heat exchanger Pending JPH02192932A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1012659A JPH02192932A (en) 1989-01-20 1989-01-20 Manufacture of resin fine tube heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1012659A JPH02192932A (en) 1989-01-20 1989-01-20 Manufacture of resin fine tube heat exchanger

Publications (1)

Publication Number Publication Date
JPH02192932A true JPH02192932A (en) 1990-07-30

Family

ID=11811489

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1012659A Pending JPH02192932A (en) 1989-01-20 1989-01-20 Manufacture of resin fine tube heat exchanger

Country Status (1)

Country Link
JP (1) JPH02192932A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20180224211A1 (en) * 2012-03-23 2018-08-09 Raumedic Ag Heat Exchanger for an Oxygenator and Method for Producing Such a Heat Exchanger

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6151536A (en) * 1984-08-22 1986-03-14 Toyota Motor Corp Detecting device for hot water leak of induction furnace
JPS6269135A (en) * 1985-09-20 1987-03-30 Kuraray Co Ltd Liquid leak detector
JPS62268951A (en) * 1986-05-19 1987-11-21 Matsushita Electric Ind Co Ltd Leak water sensor

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6151536A (en) * 1984-08-22 1986-03-14 Toyota Motor Corp Detecting device for hot water leak of induction furnace
JPS6269135A (en) * 1985-09-20 1987-03-30 Kuraray Co Ltd Liquid leak detector
JPS62268951A (en) * 1986-05-19 1987-11-21 Matsushita Electric Ind Co Ltd Leak water sensor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20180224211A1 (en) * 2012-03-23 2018-08-09 Raumedic Ag Heat Exchanger for an Oxygenator and Method for Producing Such a Heat Exchanger
US10955195B2 (en) * 2012-03-23 2021-03-23 Raumedic Ag Heat exchanger for an oxygenator and method for producing such a heat exchanger

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