JPS58108389A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPS58108389A JPS58108389A JP20852181A JP20852181A JPS58108389A JP S58108389 A JPS58108389 A JP S58108389A JP 20852181 A JP20852181 A JP 20852181A JP 20852181 A JP20852181 A JP 20852181A JP S58108389 A JPS58108389 A JP S58108389A
- Authority
- JP
- Japan
- Prior art keywords
- tubes
- heat exchanger
- outer shell
- spiral
- aluminum
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/02—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
- F28D7/022—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of two or more media in heat-exchange relationship being helically coiled, the coils having a cylindrical configuration
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
【発明の詳細な説明】
本1ili4は熱交1m8)K関し、さらに評しくは、
軽くて耐蝕性にすぐれ、かつ、熱交換効率0jLif1
に熱交換IIIK関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention 1ili4 relates to a heat exchanger 1m8)K, and more particularly,
Light, with excellent corrosion resistance, and heat exchange efficiency of 0jLif1
This relates to heat exchange IIIK.
、 一般忙、例えば、瞬間湯沸しなどに使用されてい
る熱交換器は、銅また紘銅合金によ)作られているもの
であり、そして、銅また紘銅合金は熱伝導性が良好であ
るOて熱交換率がよいが、重量が重いとhうことが63
1%また、都市ガス、tたは、プロパンガスの燃焼によ
シ腐蝕する場合があるので内厚を厚ぐしなければねらず
、重量がよ勤重くなるという問題があったのである。Heat exchangers used in general applications, such as instantaneous water heating, are made of copper or copper alloys, and copper and copper alloys have good thermal conductivity. O has a good heat exchange rate, but if it is heavy, it may cause problems.63
In addition, since combustion of city gas, t, or propane gas may cause corrosion, the inner thickness must be increased, which poses the problem of increased weight.
また、メッキ工場やクリーニング場等にをいて大量に蒸
気を使用するための石油、原油等をm@させるボイラー
勢の排ガスを利用する熱交換器4、石油、原油等の燃焼
ガス中の硫黄分の影響によって熱交換器の腐蝕が激しく
度々取替えなければならなかった。In addition, a heat exchanger 4 that uses the exhaust gas of a boiler that converts oil, crude oil, etc. into m@ in plating factories, cleaning shops, etc. that use large amounts of steam, and sulfur content in combustion gases such as oil, crude oil, etc. Due to the effects of heat exchangers, the heat exchangers were severely corroded and had to be replaced frequently.
例えば、オ6図に示す銅、又は、銅合金により作られて
いる熱交換器においては、箱状体20内を矢印方向に高
温の燃焼ガスが通る間に管21内の水と熱交換するもの
であるが、上記したように腐蝕に対して、箱状体20を
厚くする必要が69、重量が重くなシ、その上、熱交換
効率も決して良好なものとけいえないものである。For example, in a heat exchanger made of copper or copper alloy as shown in Fig. 6, the high temperature combustion gas passes through the box-shaped body 20 in the direction of the arrow while exchanging heat with water in the tube 21. However, as mentioned above, it is necessary to make the box-shaped body 20 thick in order to prevent corrosion69, the weight is heavy, and the heat exchange efficiency cannot be said to be good.
本発明は上記し交熱交換器の現状に鑑みなされ7’j4
(7)テ%都市ガス、プロパンガス、また、石油、原油
、重油等の燃焼に際しても、それらの燃焼ガスに対して
極めて耐蝕性に優れ、さらに、熱交換効率も抜群な熱交
換器を提供するものである。The present invention was developed in view of the current state of heat exchangers as described above.7'j4
(7) Provide a heat exchanger that has excellent corrosion resistance against combustion gases such as city gas, propane gas, oil, crude oil, and heavy oil, and also has outstanding heat exchange efficiency. It is something to do.
本尭1jiK係ゐ熱交換器の特徴とするところは、並列
に並べた複数の管を 柱状体或いは外殻に取付けた支持
体を介して螺旋状に捲回してから、この複数の管を*に
並べて螺旋状に111回した構造とし、かつ、仁の麿文
体の柱状体、管1.支持体及び外殻をアルオニりム又は
アルオニウム合金で被覆したことKある。The feature of this heat exchanger is that multiple tubes arranged in parallel are wound spirally through a support attached to a columnar body or outer shell, and then these multiple tubes are It has a structure of 111 turns in a spiral pattern, and the pillars and tubes of Jin's Marobuntai. The support and the outer shell are sometimes coated with an aluminium or an aluonium alloy.
本発明に係る熱交換器について以下詳細に説明する。The heat exchanger according to the present invention will be explained in detail below.
本発明に係る熱交換器において、柱状体、支持体、また
%螺旋状の管等の材料について説明する。In the heat exchanger according to the present invention, materials for the columns, supports, spiral tubes, etc. will be explained.
先づ、柱状体としては、両端が閉じた形状の円筒体、角
筒体等、或いは、円柱、角柱等であり、真中に排ガスを
通す孔を設けておいてもよい。この材料は、耐熱、耐蝕
材料であればよく、例えば、Fe系材料が好適で、純鉄
、鉄合讐、不銹鋼、 また、耐蝕性金属、合金、鋼、銅
合金1几、アルミニウム、アルミニウム合金を使用する
ことができる。しかして、柱状体は中が空胴で両端の管
網された円筒体、角筒体等とすれば熱交換器を軽くし、
かつ、材料の節約にもなるので好都合である。First, the columnar body may be a cylindrical body, a prismatic body, etc. with both ends closed, or a cylinder, a prismatic body, etc., and a hole may be provided in the center for passing the exhaust gas. This material may be any heat-resistant and corrosion-resistant material. For example, Fe-based materials are preferred, such as pure iron, iron alloys, stainless steel, corrosion-resistant metals, alloys, steel, copper alloys, aluminum, aluminum alloys, etc. can be used. However, if the columnar body is hollow inside and has a pipe network at both ends, such as a cylindrical body or a square cylinder, the heat exchanger can be made lighter;
Moreover, it is convenient because it saves materials.
次に、支持体は棒状、を次、コ字状の何れでもよく、柱
状体、或いは、外殻の何れかに取付けて管を支持するも
ので、管の重量に耐える程度の強度、取付は数とすれば
よく、使用材料も柱状体と同様のものでよい。Next, the support body may be rod-shaped, U-shaped, or U-shaped, and should be attached to either a columnar body or an outer shell to support the tube, and must have enough strength to withstand the weight of the tube, and must be attached to the tube. The number of columns may be sufficient, and the material used may be the same as that of the columnar bodies.
管の材料は、Fe系材料が好適であり、例えば、純鉄、
鉄合金、不銹鋼、ま次、耐蝕性金属または合金さらに、
鋼、銅合金、アルはニウム、アルオニウム合金等が使用
でき耐蝕性金属または合金としては、Tit Zr*
T4 Mol Nb +Tit Zr* Ta。The material of the tube is preferably Fe-based material, such as pure iron,
Ferrous alloys, non-rusting steels, steel, corrosion-resistant metals or alloys, and
Steel, copper alloy, aluminum alloy, aluminum alloy, etc. can be used. Corrosion-resistant metals or alloys include Tit Zr*
T4 Mol Nb + Tit Zr* Ta.
Mo、 Nbの合金、不銹鋼、銅や銅合金、および−
、アルミニウム、アルミニウム合金を使用することがで
きる。Mo, Nb alloys, stainless steel, copper and copper alloys, and -
, aluminum, and aluminum alloys can be used.
しかして、本発明に係る熱交換器においては、管の形状
は、先づ管を並列に密着させて湛ぺて柱状体の囲シに螺
旋状1/CWA回し、支持体によって複数個所で支えら
れており、そして、この螺旋回数は多い程良いが、熱交
換車、材料の強度等から適当に選定すればよく、さらに
、この並列に並べた11F数の管を**状に捲回してか
ら、この複数の管を縦列KMべて螺旋状に捲回して縦列
の螺旋状管とするのであるが、この捲回数も多い寝良い
が、熱交換率、材料の強度勢から適当に選定するのがよ
い。Therefore, in the heat exchanger according to the present invention, the shape of the tubes is such that first, the tubes are closely connected in parallel and turned around the enclosure of the columnar body in a spiral shape of 1/CWA, and are supported at multiple locations by supports. The higher the number of spirals, the better, but it should be selected appropriately based on the heat exchanger, the strength of the material, etc.Furthermore, the number of spirals arranged in parallel can be wound in a ** shape. Therefore, the plurality of tubes are wound in a spiral shape in a column KM to form a column of spiral tubes.Although it is preferable to have a large number of windings, the number of turns should be selected appropriately based on the heat exchange rate and the strength of the material. It is better.
また、外殻は柱状体と回IIK耐熱、耐蝕材料とするの
がよく、柱状体と同じ材料とするのがよい。Further, the outer shell is preferably made of a heat-resistant and corrosion-resistant material similar to that of the columnar body, and is preferably made of the same material as the columnar body.
被覆にアルミニウム酸いはアルミニウム合金を用いるの
は、熱伝導度が嵐好であること、腐蝕に対して強いこと
、および、管、間隙体、柱、状体を強11に密着させる
と七ができるととによるものである。なお、アルミニウ
ム合金に鉄約5%以下含有させるとより耐蝕性が向上す
る・
このようなアルミニウムまたはアルミニウム合金の被覆
を施すに杜、アルミニウムまた岐アルン二りム合金を溶
解しておいて、この溶融アルミニウムまた紘γル2ニウ
ム合金中に並列に並べた管を支持体を介して彼数回螺旋
状に捲回してから、この複数の管を縦に並べて螺旋状に
捲回した構造を設けた柱状体を浸漬してから、引嬌げて
乾燥させると熱交換器ができ上るのである。The reason why aluminum acid or aluminum alloy is used for the coating is that it has good thermal conductivity, is resistant to corrosion, and that if the pipe, gap, column, or shaped body is tightly attached, it will be It depends on what you can do. Corrosion resistance is further improved when the aluminum alloy contains about 5% or less iron. In order to apply such a coating of aluminum or aluminum alloy, the aluminum or aluminum alloy must be melted before applying this coating. A structure is created in which tubes arranged in parallel in molten aluminum or aluminum alloy are spirally wound several times through a support, and then the plurality of tubes are arranged vertically and wound in a spiral. A heat exchanger is completed by soaking the columnar bodies and then pulling them out to dry.
この方法以外に柱状体、支持体、並列及び縦列の螺旋状
管を別々にアルミニウムま几はアルきニウム合金の被覆
を上記のように施してから、並列、及び、縦列の螺旋状
管を支持体を介して柱状体に設置してから、加熱炉で加
熱して管、支持体、及び、柱状体を密着させて熱交換器
とするのである。In addition to this method, the columnar body, the support, and the parallel and vertical spiral tubes are separately coated with aluminum alloy as described above, and then the parallel and vertical spiral tubes are supported. After installing it on the columnar body through the tube, it is heated in a heating furnace to bring the tube, support, and columnar body into close contact with each other to form a heat exchanger.
壜几、外殻の内側も上記と同じようにして被覆するので
ある。The inside of the bottle and outer shell are also coated in the same manner as above.
次に、本発明に係る熱交換器について図面に示す例によ
り具体的に説明する。Next, the heat exchanger according to the present invention will be specifically explained using an example shown in the drawings.
第1図は本発明に係る熱交換器の側面図、第2図は第1
図A−A矢視図、第3図は本発明に係る熱交換器を湯沸
し器に適用した例を示す一部切欠側面図、牙4図は並列
側及び縦列側の螺旋状管の給水部と排水部の概略断面図
で、第5図は他の例を示し、第6図は従来の熱交換器の
斜視図である。Figure 1 is a side view of a heat exchanger according to the present invention, and Figure 2 is a side view of a heat exchanger according to the present invention.
Fig. 3 is a partially cutaway side view showing an example in which the heat exchanger according to the present invention is applied to a water heater, and Fig. 4 shows the water supply section of the spiral pipes on the parallel side and the vertical side. FIG. 5 shows another example, and FIG. 6 is a perspective view of a conventional heat exchanger.
牙1図、第2図において、柱状体1の複数個所(第1図
では5個所)に二字状に1例えば、溶接等により支持体
3を取付け、この支持体3,3間に螺旋状の管2.2.
2(牙1図では3本の管であるが、2本以上であれば何
本でもよい・)を挾持させる。この支持体3.6は第1
図ではコ字状となっているが、一本の支持体3上に支持
させてもよく、また、第1図では支持体6は柱状体1に
敗付けられているが、この支持体3を外殻5に取付けて
もよい(第5WJ参照)。そして、アルξ二りム、アル
ミニウム合金の被覆12が設けである。In FIGS. 1 and 2, supports 3 are attached in two-figure shapes at multiple locations (5 locations in FIG. 1) on the columnar body 1, for example, by welding, etc., and a spiral shape is formed between the supports 3, 3. Tube 2.2.
2 (Three tubes are shown in Fig. 1, but any number of tubes may be used as long as there are two or more). This support 3.6 is the first
Although it is U-shaped in the figure, it may be supported on a single support 3, and although the support 6 is defeated by the columnar body 1 in FIG. may be attached to the outer shell 5 (see 5th WJ). Then, an aluminum ξ dimer and an aluminum alloy coating 12 are provided.
また、この並列の螺旋状管2,2.2は互に密着させて
流体、例えば、燃焼ガスが管の隙間、管と柱状体、外殻
との隙間から漏洩しないように形成し、かつ、柱状体1
と外殻5(第3図)との間隔内KT度挾まれる幅となる
ように設ける必要がある。後述するが、高温の流体、例
えば、燃焼ガスが螺旋状に流れるようにして、螺旋状の
管2,2゜2と充分接触させるためである。そして、さ
らに、この並列に並べ次螺旋状の管2. 2. 2を適
当回数捲回して並列螺旋状管としてから、この複数の管
2. 2. 2を縦Kfltべた状態とし、これを螺旋
状に捲回して縦列螺旋状管2,2.2とするものも熱交
換させて、この2つの並列、縦列の螺旋状管2,2.2
によって一層熱交換効率を向上させるものである。Further, the parallel spiral tubes 2, 2.2 are formed in close contact with each other to prevent fluid, for example, combustion gas, from leaking from the gaps between the tubes, the gaps between the tubes, the columnar body, and the outer shell, and columnar body 1
It is necessary to provide such a width that it is sandwiched by KT within the distance between the outer shell 5 (FIG. 3) and the outer shell 5 (FIG. 3). As will be described later, this is to cause the high temperature fluid, for example, combustion gas, to flow in a spiral pattern and to make sufficient contact with the spiral tubes 2, 2.degree.2. Further, these parallelly arranged next spiral tubes 2. 2. 2 is wound an appropriate number of times to form a parallel spiral tube, and then the plurality of tubes 2. 2. 2 is made into a vertical Kflt solid state, and this is spirally wound to form the vertical spiral tubes 2, 2.2. Heat exchange is also performed to form these two parallel, vertical spiral tubes 2, 2.2.
This further improves heat exchange efficiency.
第3図は上記に説明した牙1図の熱交換器を組込んだ瞬
間湯沸し器の例を示したものであシ、即ち、外殻5の底
部に取付けた底板7上に支持体へ3によシ支持されてい
る並列螺旋状管2. 2. 2と取付部13に載置され
ている縦列螺旋状lF2,2゜2とが設けられている柱
状体1を載置する。この場合、並列螺旋状管2.2.2
は密着され、かつ、柱状体1と外殻5との間は流体が通
過せず、流体は矢印のように螺旋状に流れるように構成
してから、さらに、この並列螺旋状管2,2.2の下側
に密着している縦列螺旋状管2. 2. 2を外殻5の
下部の取付部12上に載置して、熱源、例えば、ガスバ
ーナー8の近くkなるようにする。。このように、並列
螺旋状管2,2.2の部分は支持体3に、また、縦列螺
旋状管2. 2. 2の部分社取付部13により支えら
れている。そして、上記したJ5に、アルオニり台、ア
ルミニウム合金被覆12がある。そして、この底板7に
はガスノ(−ナー8を複数個設け、ガスGが供給され、
かつ、外殻5と壁6により空気通路を形成して入口9か
らガスバーナー8へ空気を矢印のように送るようにして
もよい。これは、加熱9気が送られるのでガスの燃焼を
助長する。なお、第5図、第6図に示すように、底板7
.及び、取付部13に4アルミニウム、アルミニウム合
金の被覆12を設けた方がよい。FIG. 3 shows an example of an instantaneous water heater incorporating the heat exchanger of FIG. Parallel helical tubes supported by 2. 2. A columnar body 1 is mounted on which a columnar body 1 is provided with a columnar spiral IF2, 2°2 mounted on a mounting portion 13. In this case, parallel spiral tubes 2.2.2
are in close contact with each other, and no fluid passes between the columnar body 1 and the outer shell 5, and the fluid flows spirally as shown by the arrow. .2 tandem spiral tubes in close contact with the underside of 2. 2. 2 is placed on the lower mounting part 12 of the outer shell 5 so that it is close to a heat source, for example a gas burner 8. . In this way, parts of the parallel helical tubes 2, 2.2 are attached to the support 3 and also the tandem helical tubes 2. 2. The second part is supported by a mounting part 13. The above-mentioned J5 includes an aluminum alloy stand and an aluminum alloy coating 12. A plurality of gas nozzles 8 are provided on this bottom plate 7, and gas G is supplied thereto.
In addition, an air passage may be formed by the outer shell 5 and the wall 6, and air may be sent from the inlet 9 to the gas burner 8 in the direction of the arrow. This promotes combustion of the gas as heated air is sent. In addition, as shown in FIGS. 5 and 6, the bottom plate 7
.. It is also preferable to provide the mounting portion 13 with a coating 12 of aluminum or aluminum alloy.
また、縦列螺旋状管2.2.2に液体、例えば、水を送
るに社、第4図に示すものは、給水、排水何れKも使用
できるものであるが、水Wは)(イブPによシ給水部4
に入り、ここから先ず、縦列螺旋状管2,2.2に送ら
れ、次いで、並列螺旋状92.2.2に送られていき、
熱交換されて熱くなった水は、並列螺旋状管2,2.2
端部から給水部4(排水部11となる。)へたまり、ノ
くイブPから排出されるのである。In addition, in the case of sending a liquid, for example, water to the vertical spiral pipe 2.2.2, the one shown in Fig. 4 can be used for either water supply or drainage, but water W is) (Eve P Water supply section 4
from which it is first sent to the tandem spiral tube 2, 2.2 and then to the parallel spiral tube 92.2.2,
The water heated by heat exchange is passed through the parallel spiral pipes 2, 2.2.
It collects in the water supply part 4 (which becomes the drainage part 11) from the end and is discharged from the nokub P.
このような構成を有している本発明に係る熱交換器を使
用した瞬間湯沸し器において、先づ水Wを給水部4へ供
給することによって縦列螺旋状管、及び、並列螺旋状管
2.2.2内を流して排水部11へ達した時に、ガスG
よりガスノ(−ナー8に点火すると、この燃焼ガスは矢
印に示すように、先づ、縦列の螺旋状の管2,2.2に
囲まれ皮部分から、さらに、並列螺旋状管292・ 2
によシ形成される螺旋空間内に沿って上昇し、その間に
、縦列、及び、並列の螺旋状管2,2.2内を流れる水
と高温の燃焼ガスとが熱交換して、排水部11に流れる
水Hは80°〜90℃近くもの温度となって排水されて
利用され、一方、溶焼ガスは、約50℃程度の低温とな
って煙突10から排出される。このように、高温の燃焼
ガスと縦列、及び、並列の螺旋状管との接触面積が極め
て大きいので、燃焼ガスと縦列、並列の螺旋状管内を流
れる水との熱交換率も大きく、従って、加熱されて排、
水される水温も高く、かつ、排出燃焼ガスも極めて低温
となるのである。なお、本発明の熱交換器をボイラーと
組合せても上8ピと同様である。In the instantaneous water heater using the heat exchanger according to the present invention having such a configuration, by first supplying water W to the water supply section 4, the tandem spiral tubes and the parallel spiral tubes 2. 2. When the gas G flows through the interior and reaches the drainage part 11,
When the gas nozzle 8 is ignited, the combustion gas flows, as shown by the arrow, first from the skin surrounded by the vertical spiral tubes 2, 2.2, and then into the parallel spiral tubes 292, 2.
The high temperature combustion gas exchanges heat with the water flowing in the vertical and parallel spiral pipes 2, 2.2, and drains into the drainage section. The water H flowing into the chimney 11 reaches a temperature of approximately 80° to 90°C and is drained for use, while the molten gas is discharged from the chimney 10 at a low temperature of approximately 50°C. In this way, since the contact area between the high temperature combustion gas and the vertical and parallel spiral tubes is extremely large, the heat exchange rate between the combustion gas and the water flowing in the vertical and parallel spiral tubes is also large. heated and drained,
The temperature of the water being poured is high, and the exhaust combustion gas is also extremely low. Note that even if the heat exchanger of the present invention is combined with a boiler, it is the same as the upper 8 pi.
しかして、本慟明に係る熱交換器においては、柱状体、
螺旋状の管、支持体、外殻等にアルミニウム、アルミニ
ウム合金が被覆されているので、都市ガス、プロパンガ
スは勿論、例えば、石油、原油、重油等の油類を使用す
る湯沸し器、又、ボイラーでは、燃焼ガス中Kit黄分
が含有され、柱状体1の下部では働鉤ガスは高温のため
ガス体であるが、柱状体1の上部付近、及び支持体3、
並列の螺旋状管、また、縦列螺旋状管(一部)2は硫酸
分を含む水筒が多数付着した状態となシ、また、外殻5
も同じ状態である。しかして、この硫酸分を含む水滴紘
腐蝕性の極めて激しいものであるが、アルさニウム、ア
ルミニウム合金の被覆があるので、被覆の下の金属、合
金の材料を腐蝕することがなく、極めて長時間にわたシ
使用することができるのである。この説明は、燃焼ガス
中の硫黄分のみの腐蝕についてであるが、これ以外の種
々の腐蝕因子が存在して、これらの腐蝕因子が重なって
いるものと考えられる。However, in the heat exchanger according to the present study, the columnar bodies,
Since the spiral tube, support, outer shell, etc. are coated with aluminum or aluminum alloy, it can be used in water heaters that use not only city gas and propane gas, but also oils such as petroleum, crude oil, and heavy oil. In the boiler, the combustion gas contains yellow components, and the working hook gas is a gas at the lower part of the columnar body 1 due to its high temperature, but near the upper part of the columnar body 1 and the support body 3,
The parallel spiral tubes and the vertical spiral tube (part) 2 have many water bottles containing sulfuric acid attached to them, and the outer shell 5
is in the same condition. However, since it has a coating of aluminum or aluminum alloy, it does not corrode the metal or alloy material under the coating, and it can last for an extremely long time. You can use it at any time. Although this explanation relates to corrosion caused only by the sulfur content in the combustion gas, it is thought that various other corrosion factors exist and these corrosion factors overlap.
なお、アルミニウムまたはアルミニウム合金のコーティ
ングを施した熱交換器を加熱して、熱交換器各部の材料
とアルミニウムtたはアルミニウム合金との拡散層(合
金層)を生成させると、熱交換器は極めて強固な構造物
となる。Furthermore, if a heat exchanger coated with aluminum or aluminum alloy is heated to create a diffusion layer (alloy layer) between the material of each part of the heat exchanger and aluminum or aluminum alloy, the heat exchanger will become extremely It becomes a strong structure.
また、本発明に係る熱交換器を構成する材料は極めて薄
くすることができるばかシか、強度も強いものである。Further, the material constituting the heat exchanger according to the present invention can be made extremely thin and has high strength.
そして、これらの材料(上記した種々の材料)を種々組
合せて使用することが可能である。These materials (the various materials mentioned above) can be used in various combinations.
第5図は本発明に係る熱交換器を適用した湯沸し器の他
の例を示し、f6図の壁を省略したものであるが、実施
の態様については、t3図の説明と全く同じである。Fig. 5 shows another example of a water heater to which the heat exchanger according to the present invention is applied, and the wall in Fig. f6 is omitted, but the embodiment is exactly the same as the explanation in Fig. t3. .
なお、第1図、第3図、第5図で柱状体1を底板7上に
載置した例を説明しであるが、例えば、外殻5内に耐熱
、耐蝕性の綱等により柱状体1を懸吊してもよく、柱状
体1を半分程度の長さとしてもよい。1, 3, and 5 are examples in which the columnar body 1 is placed on the bottom plate 7. 1 may be suspended, or the length of the columnar body 1 may be reduced to about half.
以上説明したように、本発明に係る熱交換器によれば、
アルミニウムtaUアルSニウム合金ニよる被覆がある
ので熱伝導性が極めて良好て、かつ、表面にアル2すが
形成され耐蝕性に4すぐれており、その上軽量てあシ、
熱交換器として極めてすぐれた性能を有しているもので
ある。As explained above, according to the heat exchanger according to the present invention,
Since it is coated with aluminum (TAU) and aluminum (S) alloy, it has extremely good thermal conductivity, and has an aluminum layer formed on the surface, which provides excellent corrosion resistance.
It has extremely excellent performance as a heat exchanger.
第1図は本JiIi明に係る熱交換器の概略側面図、第
2図は第111のA−ム矢視図、第3図は本発明に係る
熱交換器が瞬間湯沸し器に適用された場合の一部切欠概
略図、第4図は給水部(排水部)の断面図、牙5図は伽
の例を示す概略図、第6図は従来の熱交換器の斜視図で
ある。
1〜柱状体、 2〜螺旋状の管、 3〜支持体、4〜給
水部、 5〜外殻、 6〜壁、 7〜底板、8〜バー
ナー、 9〜入口、 10〜#l突、11〜排水部、
12〜被II、 b5t+−付S。Fig. 1 is a schematic side view of the heat exchanger according to the present invention, Fig. 2 is a view from the direction of arrow A in Fig. 111, and Fig. 3 shows the heat exchanger according to the present invention applied to an instantaneous water heater. FIG. 4 is a cross-sectional view of a water supply section (drainage section), FIG. 5 is a schematic diagram showing an example of a cage, and FIG. 6 is a perspective view of a conventional heat exchanger. 1 - columnar body, 2 - spiral tube, 3 - support body, 4 - water supply part, 5 - outer shell, 6 - wall, 7 - bottom plate, 8 - burner, 9 - inlet, 10 - #l protrusion, 11 ~Drainage section,
12 to II, S with b5t+-.
Claims (1)
支持体を介して螺旋状に捲回してから、この複数の管を
INK!ぺて螺旋状に捲回した構造とし、かつ、この組
立体の柱状体、管、支持体及び外殻管アルミニラム又祉
アル電二りム合金で被覆したことを特徴とする熱交換器
。The multiple tubes that can be played in parallel are wound spirally through a support attached to a columnar body or outer shell, and then the multiple tubes are INK! 1. A heat exchanger having a spirally wound structure, and having a columnar body, a tube, a support body, and an outer shell tube covered with an aluminum or aluminum alloy.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20852181A JPS58108389A (en) | 1981-12-23 | 1981-12-23 | Heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20852181A JPS58108389A (en) | 1981-12-23 | 1981-12-23 | Heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58108389A true JPS58108389A (en) | 1983-06-28 |
Family
ID=16557547
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20852181A Pending JPS58108389A (en) | 1981-12-23 | 1981-12-23 | Heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58108389A (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4417043Y1 (en) * | 1966-08-30 | 1969-07-23 | ||
JPS5169250A (en) * | 1974-12-12 | 1976-06-15 | Eiichi Uratani | Rasenryuronoaru netsukookanki |
JPS51119539A (en) * | 1975-04-11 | 1976-10-20 | Kikuo Okumura | Heat exchanger |
-
1981
- 1981-12-23 JP JP20852181A patent/JPS58108389A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4417043Y1 (en) * | 1966-08-30 | 1969-07-23 | ||
JPS5169250A (en) * | 1974-12-12 | 1976-06-15 | Eiichi Uratani | Rasenryuronoaru netsukookanki |
JPS51119539A (en) * | 1975-04-11 | 1976-10-20 | Kikuo Okumura | Heat exchanger |
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