JPS6021021B2 - Heat exchanger manufacturing method - Google Patents
Heat exchanger manufacturing methodInfo
- Publication number
- JPS6021021B2 JPS6021021B2 JP5557478A JP5557478A JPS6021021B2 JP S6021021 B2 JPS6021021 B2 JP S6021021B2 JP 5557478 A JP5557478 A JP 5557478A JP 5557478 A JP5557478 A JP 5557478A JP S6021021 B2 JPS6021021 B2 JP S6021021B2
- Authority
- JP
- Japan
- Prior art keywords
- mold
- heat exchanger
- pores
- molten metal
- resin
- 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
Links
Landscapes
- Molds, Cores, And Manufacturing Methods Thereof (AREA)
Description
【発明の詳細な説明】
本発明は多数の空隙が連続してなる通気性の高い多孔賞
金属をフィンとして用いた熱交換器およびその製造方法
に関するもので、本発明における熱交換器はファンコイ
ルユニットに用いる対空気用熱交換器、冷凍機、空調機
に用いる対空気用蒸発器、凝縮器など、温度差のある2
流体の間で熱交換させる分野に利用することができる。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat exchanger using a highly air permeable porous metal with a large number of continuous voids as fins, and a method for manufacturing the same. Two devices with a temperature difference, such as air-to-air heat exchangers used in units, refrigerators, air-to-air evaporators and condensers used in air conditioners, etc.
It can be used in the field of exchanging heat between fluids.
本発明に近い技術として、溶解金属中にガスを発生する
物質を投入して、溶解金属を発泡させて得られる発泡金
属体をフィンとして用いる熱交換器や金属粒子を雛結方
法などで接合固着させてフィンとして用いる熱交換器が
知られている。前者は薫続空孔相互の連結部が極めて細
くくびれたり、中に一部独立空孔を生じたりして流体の
通路抵抗が大きくなったり、また全体にわたって一様な
密度に成形することが困難であるなどの問題点がある。
また後者は粒子と粒子の間隙が流体の通るすきまであり
、あまり大きな空隙率を得ることができないし、また製
造時間が長くかかったり、価格が高いなどの問題がある
。以上の問題点からこれらの熱交換器は実用の城に達し
ていない。現在一般に使われているフィン付熱交換器は
板状のフィンを伝熱管に直角にできるだけ密に配列して
、熱交換を行う伝熱面積を大きくするようにしたクロス
フィン形熱交換器が大部分を占めている。このタイプの
熱交換器は伝熱管が蛇行管もしくはへツダ接続形の平行
管であるを問わず、先ずフィンを多列で装置した後、フ
ィンと伝熱管の接続処理を行わねばならず、組立が面鑓
であるばかりでなく、組立工程を多く要して、工期が長
く、生産性に難点があった。さらにクロスフィン形の熱
交換器では、フィンの間隙を流体が流れるため、むやみ
にフィン間隔を狭くして、フィンの数を増して銭熱面積
を大きくすることは流体の通路抵抗の増加および加工上
の制約もあって困難であつた。本発明は従来の熱交換器
が上記の如き問題点を有していることに着目して、新規
な加工技術の採用により問題点の解消を可能にし、かつ
伝熱性能を向上させ、軽量小形化をも可能にしたもので
あって、従釆熱交換器のフィンに相当する部分を、既に
蛇行管などに加工された民熱管の周囲に、一体成型によ
り結着させ得る如くした新規な熱交換器の製造方法を提
供し得ることを特徴とするものである。Technologies similar to the present invention include a heat exchanger that uses a foamed metal body as a fin by introducing a gas-generating substance into the molten metal and foaming the molten metal, and bonding and fixing of metal particles using a broiling method. Heat exchangers that are used as fins are known. In the former case, the connecting parts between continuous pores are extremely thin and constricted, some independent pores are formed inside, which increases the fluid passage resistance, and it is difficult to mold the material to a uniform density throughout. There are problems such as.
Furthermore, in the latter case, the gaps between particles are large enough for fluid to pass through, making it impossible to obtain a very large porosity, and there are also problems such as a long manufacturing time and high cost. Due to the above problems, these heat exchangers have not reached the point of practical use. The most commonly used finned heat exchangers at present are cross-fin type heat exchangers, in which plate-shaped fins are arranged as densely as possible at right angles to the heat transfer tubes to increase the heat transfer area for heat exchange. occupies a portion. In this type of heat exchanger, regardless of whether the heat exchanger tubes are meandering tubes or parallel tubes with header connections, the fins must first be installed in multiple rows, and then the fins and the heat exchanger tubes must be connected. Not only was this complicated, but it also required many assembly steps, resulting in long construction times and low productivity. Furthermore, in a cross-fin type heat exchanger, fluid flows through the gaps between the fins, so unnecessarily narrowing the fin spacing and increasing the number of fins to increase the heating area will increase fluid passage resistance and This was difficult due to the above constraints. The present invention focuses on the fact that conventional heat exchangers have the above-mentioned problems.The present invention makes it possible to eliminate the problems by adopting a new processing technology, improve heat transfer performance, and make it lightweight and compact. This is a new heat exchanger that enables the part corresponding to the fins of the secondary heat exchanger to be integrally molded around the civilian heat pipe that has already been processed into a serpentine pipe or the like. The present invention is characterized in that it can provide a method for manufacturing an exchanger.
以下本発明の一実施例を添付図面に従って具体的に説明
する。An embodiment of the present invention will be described in detail below with reference to the accompanying drawings.
第1図は本発明を空気熱交換器に用いたものであり、6
毒熱管1を蛇行状に成型し、その周囲を厚い層をもつマ
ット状に形成したフィンブロック2で伝熱管1の管端部
を露呈させておおつた一体成型の熱交換器であり、フィ
ンブロック2内に伝熱管1が埋設された形態をなしてい
る。Figure 1 shows the use of the present invention in an air heat exchanger, with 6
It is an integrally molded heat exchanger in which a poisonous heat tube 1 is molded into a meandering shape, and the end of the heat transfer tube 1 is exposed and covered with a fin block 2 formed around the fin block 2 in a mat shape with a thick layer. The heat transfer tube 1 is embedded in the heat exchanger tube 2.
さらにフィンブロック2は第2図に示す拡大図のように
細線状、または第3図に示す拡大図のように種々の凹凸
をもった織線状のフィン3がスケルトン状を呈した多孔
質金属であり、空気はスケルトン状をしたフィン3の間
の多数の空隙4を流れるようになっており、伝熱管1内
を流れる冷蝶、水などの流体とフィン3を通して熱交換
を行わせるようになつている。次に第1図、第2図に示
した熱交換器の製法の1例を第4図によって説明する。Further, the fin block 2 is made of porous metal in which the fins 3 have a skeleton shape, either in the form of fine lines as shown in the enlarged view in FIG. 2, or in the form of woven lines with various unevenness as shown in the enlarged view in FIG. The air flows through a large number of gaps 4 between the skeleton-shaped fins 3, and heat is exchanged with a fluid such as cold butterfly or water flowing inside the heat transfer tube 1 through the fins 3. It's summery. Next, an example of a method for manufacturing the heat exchanger shown in FIGS. 1 and 2 will be explained with reference to FIG. 4.
まず発泡ウレタンなどの3次元連続空孔を有する通気性
の良好な樹脂を模型とし、この模型の空孔に流動状の鋳
型材料を満たした後、この中に蛇行状などに成型した榛
熱管1をその管端部が露呈するようにして埋設する。First, a resin with good air permeability that has three-dimensional continuous pores such as foamed urethane is used as a model, and after filling the pores of this model with a fluid molding material, the Shinnetsu tube 1 is molded into a serpentine shape. The pipe is buried so that the end of the pipe is exposed.
鋳型材料としては鋳型用石こう粉末と水からなるスラリ
ー、食塩を添加した石こうと水からなるスラリー、27
0メッシュ以下のSiQ粉末にエチルシリケートと工業
用エチルアルコールと水よりなる粘縞剤を混合したスラ
リー、その他一般の鋳型材料を用いる。次に加熱などの
操作により、鋳型材を硬化させると同時に模型の樹脂を
気化消失させて3次元連続空孔を有するフィン用鋳型5
を成形する。As a mold material, a slurry consisting of gypsum powder for molds and water, a slurry consisting of gypsum and water to which common salt has been added, 27
A slurry prepared by mixing SiQ powder of 0 mesh or less with a viscous streaking agent consisting of ethyl silicate, industrial ethyl alcohol, and water, and other general mold materials are used. Next, by heating or other operations, the mold material is cured, and at the same time, the resin of the model is vaporized and disappeared, resulting in a fin mold 5 having three-dimensional continuous pores.
to form.
このようにして成形されたフィン用鋳型5を金型6内に
入れ、下部にるつぼ7を有する圧力容器8内にセットす
る。るつぼ7内には、電気ヒータなどの加熱源9により
加熱されて溶融した金属10が満されている。この金属
材料としては、AI、Cuなどの熱伝導性の良好な材料
の他に、Fe及び一般の鉄系合金やPb、Sn、Zn、
Mgなどの非鉄系合金についても用いることが可能であ
る。次にるつぼ7内の溶融金属10を空気吹込口11か
らの圧縮空気などにより数気圧に加圧し、加圧による力
で、溶融金属10を運適口12を介してフィン用鋳型5
の空孔内に充填する。その後復圧して溶融金属10が凝
固した後、フィン用銭極5を金型6から取出し、鋳型材
料を除去する。これにより蛇行状の伝熱管1の周囲には
、細線状のフィン3がスケルトン状を呈した連続空孔を
有する多孔質金属のフィンブロック2が一体成型により
結着される。別の製法としては、フィンブロックの成型
時に5毒熱賛挿入用の孔を設けて、この孔に伝熱管を挿
入後、前述の実施例のように鋳造法により成型するもの
である。The fin mold 5 thus formed is placed in a metal mold 6 and set in a pressure vessel 8 having a crucible 7 at the bottom. The crucible 7 is filled with metal 10 that has been heated and melted by a heating source 9 such as an electric heater. This metal material includes materials with good thermal conductivity such as AI and Cu, as well as Fe and general iron alloys, Pb, Sn, Zn,
Non-ferrous alloys such as Mg can also be used. Next, the molten metal 10 in the crucible 7 is pressurized to several atmospheres using compressed air from the air inlet 11, and the molten metal 10 is passed through the injection port 12 into the fin mold 5 by the force of the pressurization.
Fill in the pores of. After the pressure is restored and the molten metal 10 is solidified, the fin electrode 5 is taken out from the mold 6 and the mold material is removed. As a result, around the meandering heat exchanger tube 1, a porous metal fin block 2 having continuous pores in which thin wire-like fins 3 take on a skeleton shape is integrally molded. Another manufacturing method is to provide a hole for inserting the heat exchanger when molding the fin block, insert the heat transfer tube into the hole, and then mold the fin block by a casting method as in the above embodiment.
既ち、3次元連続空孔を有する樹脂模型の空孔に、流動
状の鋳型材料を満した後、この中に樹脂模型と同種類の
材料からなる棒状体をその両端が蕗呈するようにして埋
設する。次に加熱などにより樹脂模型と綾状体とを消失
させて3次元連続空孔と貫通孔とを有するフィン用鋳型
を成形する。次にこの貫通孔にU字形に成型された穂熱
管または真直な伝熱管を挿入後、加圧により溶融金属を
この鋳型空孔内に充填し、溶融金属が凝固した後鋳型材
料を除去する。このような方法では、鋳型ができてから
伝熱管を挿入するので、虎熱管とフィンブロックとの接
合が良好になる。炭熱管の周囲にフィンブロックを成型
する方法としては、上記の如くあらかじめ蛇行させた伝
熱管をフィンブロックの鋳型内に埋設し、上記の鋳造法
により一体成型で結着する方法の他に、【1}フィンブ
ロックの成型時に伝熱管挿入用穴を設け、この穴に伝熱
管を挿入し舷管して結着する方法、{2ー儀熱管の表面
にフィン材より低温度で溶融する低融点金属のo−材を
塗布し、辰熱管をフィンブロック成型時に設けられた穴
に挿入後加熱操作によりロー材を溶融させて結着する方
法、糊伝熱管をフィンブロック成型時に設けられた穴に
挿入後、伝熱管に高周波電流を流して伝奏熱管を加熱し
、伝熱管近傍のフィンブロックを溶融して結着する方法
、{4}伝熱管表面に塗布したロー材を高周波加熱によ
り溶融して結着する方法などがある。しかい1ーの方法
は、伝熱管とフィンブロックとの接触熱抵抗が大きく、
‘2、‘3}の方法は接触熱抵抗は小さいが加熱操作が
必要となり、特に糊の方法は加熱時間こそ短くできるが
フィンブロックが溶解する比較的高い温度まで加熱しな
ければならない。また{4)の方法は、接触熱抵抗が小
さく、加熱時間が短く、加熱温度も低いが、製作工程が
増し、いずれの方法も製作工程の単純化、炭熱管とフィ
ンブロックとの良好な結着などの面から好ましくない。
以上の製法により製作された熱交換器において、熱交換
される空気はフィンブロック2におけるスケルトン状を
したフィン3の間の無数の蓮通空隙4を流路抵抗を殆ん
ど受けることなく、速やかに流れ、この流通過程におい
て伝熱管1内の流体とフィン3を適して効率よく熱の授
受が行われる。After filling the pores of a resin model with three-dimensional continuous pores with a fluid mold material, a rod-shaped body made of the same type of material as the resin model is placed in the pores so that both ends thereof are curved. Bury it. Next, the resin model and the twill-shaped body are made to disappear by heating or the like to form a fin mold having three-dimensional continuous holes and through holes. Next, after inserting a U-shaped heat exchanger tube or a straight heat transfer tube into the through hole, molten metal is filled into the mold cavity under pressure, and after the molten metal has solidified, the mold material is removed. In this method, the heat exchanger tubes are inserted after the mold is made, so that the heat exchanger tubes and the fin blocks are bonded well. As a method for molding a fin block around a coal-fired tube, in addition to the method of embedding a meandering heat exchanger tube in advance in the mold of the fin block as described above and bonding it together by integral molding using the above-mentioned casting method. 1) A method of creating holes for heat exchanger tube insertion when molding the fin block, inserting the heat exchanger tubes into these holes, and connecting them with a gangway. A method in which a metal O-material is applied, a cinnabar tube is inserted into a hole made during fin block molding, and the brazing material is melted and bonded by a heating operation, and a glue heat transfer tube is inserted into a hole made during fin block molding. After insertion, a high-frequency current is passed through the heat transfer tube to heat the heat transfer tube, and the fin blocks near the heat transfer tube are melted and bonded. {4} The brazing material applied to the surface of the heat transfer tube is melted by high frequency heating. There are several methods of binding. In method 1, the contact thermal resistance between the heat transfer tube and the fin block is large;
Methods '2 and '3} have a small contact thermal resistance, but require heating operations. In particular, the glue method can shorten the heating time, but must be heated to a relatively high temperature at which the fin block melts. In addition, method {4) has a small contact thermal resistance, a short heating time, and a low heating temperature, but it requires an additional manufacturing process. Unfavorable in terms of appearance etc.
In the heat exchanger manufactured by the above-mentioned manufacturing method, the air to be heat exchanged quickly passes through the numerous open spaces 4 between the skeleton-shaped fins 3 of the fin block 2 with almost no flow resistance. During this flow process, heat is efficiently exchanged between the fluid in the heat transfer tube 1 and the fins 3.
本発明の熱交換器におけるフィン3は網目状3次元的に
配置されているので、板状フィンに較べ伝熱面積を増加
させることができ、さらに網目状に流体の通路が入り組
んでいるため、常に流体が縄拝され温度境界層の発達を
減ずる効果があり、高い銭熱性能を出すことができ、極
めて有効に熱の授受を行うことができる。Since the fins 3 in the heat exchanger of the present invention are arranged three-dimensionally in a mesh shape, the heat transfer area can be increased compared to plate-shaped fins, and furthermore, since the fluid passages are intricately arranged in the mesh shape, Fluid is constantly flowing through the system, which has the effect of reducing the development of a temperature boundary layer, resulting in high thermal performance and extremely effective transfer of heat.
一般の熱交換器において、空気との熱伝達率はh広d‐
n (一般にn>0)但しh:熱伝達率、d:代表直
径
として表わされることは周知である。In a general heat exchanger, the heat transfer coefficient with air is h wide d-
It is well known that n (generally n>0) is expressed as h: heat transfer coefficient and d: representative diameter.
上式はdが4・さし・方が熱伝達率は大きくなることを
示している。本発明による熱交換器のフィン3は非常に
細い紬線状のものが製作可能であり、伝熱性能を一層向
上させることができる。The above formula shows that the heat transfer coefficient becomes larger when d is 4. The fins 3 of the heat exchanger according to the present invention can be manufactured in the form of very thin pongee lines, and the heat transfer performance can be further improved.
以上述べたように、本発明によれば、クロスフィン形熱
交換器と比較して、単位体積当りの伝熱面積も大きくで
き、辰熱性能も高くできるので小形化が可能であり、ま
た多孔質金属は軽量構造であるので、熱交換器全重量を
軽量化し得る。As described above, according to the present invention, compared to a cross-fin type heat exchanger, the heat transfer area per unit volume can be increased, the phosphorescence performance can be increased, and the size can be reduced. Since quality metal has a lightweight structure, the overall weight of the heat exchanger can be reduced.
また製作工程において、あらかじめ伝熱管を蛇行状など
に成型して置いて、その周囲にフィンブロックを鋳造に
より成型したので、フィン伝熱管の接合は鋳造時に行わ
れ、フィンと伝熱管の接合などの面鍵な処理工程が省略
でき、製作が極め簡単になる。さらに溶融金属の冷却固
化時に収縮などによりフィンフロツクと伝熱管との結着
が良好となり、フィンと法熱管の間の熱の伝わりが良く
なる。また樹脂模型を使用しているので、樹脂模型によ
りあらかじめ熱交換器の通路抵抗などを把握できるなど
の利点を有している。In addition, during the manufacturing process, the heat exchanger tubes were formed into a serpentine shape in advance, and the fin blocks were cast around them, so the joining of the fin heat exchanger tubes was done at the time of casting. The production process is extremely simple, as the key processing steps can be omitted. Further, when the molten metal is cooled and solidified, the fin flock and the heat transfer tube are bonded well due to shrinkage, etc., and the heat transfer between the fins and the heat transfer tube is improved. Furthermore, since a resin model is used, it has the advantage that the passage resistance of the heat exchanger can be determined in advance using the resin model.
第1図は本発明による熱交換器の一実施例の斜視図、第
2図は第1図におけるフィンブロックの形状の一例を示
す一部拡大図、第3図は同じくフィンブロックの形状の
他の例を示す一部拡大図、第4図は本発明の製造方法の
一例を説明する図である。
1・・・・・・伝熱管、2・…・・フィンブロック、3
・・・・・・フィン、5・・・・・・フィン用鋳型、7
・・・・・・るつぼ、8・・・・・・圧力容器、10・
・・・・・溶融金属。
浴/函椿で図
第5図
*4図FIG. 1 is a perspective view of an embodiment of the heat exchanger according to the present invention, FIG. 2 is a partially enlarged view showing an example of the shape of the fin block in FIG. 1, and FIG. FIG. 4 is a partially enlarged view showing an example of the manufacturing method of the present invention. 1... Heat exchanger tube, 2... Fin block, 3
...Fin, 5...Mold for fin, 7
... Crucible, 8 ... Pressure vessel, 10.
...molten metal. Bath / Box camellia figure Figure 5 * 4 figure
Claims (1)
の空孔に流動状の鋳型材料を満した後この中に蛇行状な
どに成型した伝熱管をその管端部が露呈するようにして
埋設し、その後加熱などの操作により樹脂模型を消失さ
せて3次元連続空孔を有する鋳型を形成し、次に加圧し
た溶融金属にこの鋳型を接触させることにより溶融金属
を鋳型の空孔内に充填した後溶融金属を凝固させ、その
後鋳型材料を除去することにより、蛇行状の伝熱管の周
囲部に連続の3次元空孔を有する多孔質金属を一体成型
により結着したことを特徴とする熱交換器の製造方法。 2 3次元連続空孔を有する樹脂を模型とし、その模型
の空孔に流動状の鋳型材料を満した後この中に樹脂模型
と同種類の材料からなる棒状体をその両端部が露呈する
ようにして埋設し、その後加熱などの操作により樹脂模
型と棒状体とを消失させて3次元連続空孔と貫通孔を有
する鋳型を形成し、次に貫通孔にU字形などに成型した
伝熱管をその管端部が露呈するようにして挿入した後、
加圧した溶融金属にこの鋳型を接触させることにより溶
融金属を鋳型の空孔内に充填した後溶融金属を凝固させ
、その後鋳型材料を除去することにより、蛇行状の伝熱
管の周囲部に連続の3次元空孔を有する多孔質金属を一
体成型により結着したことを特徴とする熱交換器の製造
方法。[Scope of Claims] 1. A resin having three-dimensional continuous pores is used as a model, and after filling the pores in this pattern with a fluid molding material, a heat transfer tube formed in a serpentine shape or the like is placed inside the resin at the end of the tube. The resin model is buried so that it is exposed, and then the resin model is removed by heating or other operations to form a mold with three-dimensional continuous pores.Then, this mold is brought into contact with pressurized molten metal to remove the molten metal. After filling the pores of the mold, the molten metal is solidified, and then the mold material is removed, thereby forming a porous metal with continuous three-dimensional pores around the serpentine heat transfer tube by integrally molding it. A method for manufacturing a heat exchanger, characterized in that: 2. A resin having three-dimensional continuous pores is used as a model, and after the pores of the model are filled with fluid mold material, a rod-shaped body made of the same type of material as the resin model is placed in the resin model so that both ends thereof are exposed. The resin model and the rod-shaped body are then removed by heating or other operations to form a mold having three-dimensional continuous holes and through holes, and then a heat exchanger tube formed into a U-shape or the like is inserted into the through hole. After inserting the tube with its end exposed,
By bringing this mold into contact with pressurized molten metal, the molten metal fills the holes in the mold, solidifies the molten metal, and then removes the mold material to form a continuous part around the serpentine heat exchanger tube. 1. A method for manufacturing a heat exchanger, characterized in that a porous metal having three-dimensional pores is bonded by integral molding.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5557478A JPS6021021B2 (en) | 1978-05-12 | 1978-05-12 | Heat exchanger manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5557478A JPS6021021B2 (en) | 1978-05-12 | 1978-05-12 | Heat exchanger manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54148127A JPS54148127A (en) | 1979-11-20 |
| JPS6021021B2 true JPS6021021B2 (en) | 1985-05-24 |
Family
ID=13002490
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5557478A Expired JPS6021021B2 (en) | 1978-05-12 | 1978-05-12 | Heat exchanger manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6021021B2 (en) |
-
1978
- 1978-05-12 JP JP5557478A patent/JPS6021021B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54148127A (en) | 1979-11-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPS6242699B2 (en) | ||
| US3262190A (en) | Method for the production of metallic heat transfer bodies | |
| CA1318911C (en) | Device for heat transfer | |
| US3306353A (en) | Heat exchanger with sintered metal matrix around tubes | |
| CN103930223B (en) | Manufacture the method with the metal foaming material of passage and the metal foaming material so obtained | |
| JP2580843B2 (en) | Method for producing base material having porous surface | |
| US3364951A (en) | Heat exchanger | |
| CN103900412A (en) | Through-hole metal foam heat pipe heat exchange device with gradually-changed appearance characteristics | |
| EP0930480A3 (en) | Heat exchanger | |
| US4600052A (en) | Compact heat exchanger | |
| JPS6247617B2 (en) | ||
| JPS6021021B2 (en) | Heat exchanger manufacturing method | |
| JP2580003B2 (en) | Manufacturing method of heat exchanger | |
| CA1185067A (en) | Cast recuperator tube | |
| DE2844520B2 (en) | Method of manufacturing a tubular heat exchanger | |
| JPS63299847A (en) | Production of heat exchanger | |
| CN2294442Y (en) | vented heat exchange element | |
| US3211133A (en) | Fluid heating unit | |
| JP2822015B2 (en) | Pipe for heat exchanger and method for producing the same | |
| JP2000088490A (en) | Heat exchanger | |
| RU2219016C2 (en) | Method for making heat exchange apparatus | |
| CN2297697Y (en) | Air-permeable heat exchange element encasing a fluid conduit | |
| JPH01147294A (en) | Heat exchanger | |
| JPS63101066A (en) | Casting method for cooling hole for cast iron made metallic mold | |
| RU2230201C2 (en) | Radiator |