JPH0245785B2 - - Google Patents

Info

Publication number
JPH0245785B2
JPH0245785B2 JP58193595A JP19359583A JPH0245785B2 JP H0245785 B2 JPH0245785 B2 JP H0245785B2 JP 58193595 A JP58193595 A JP 58193595A JP 19359583 A JP19359583 A JP 19359583A JP H0245785 B2 JPH0245785 B2 JP H0245785B2
Authority
JP
Japan
Prior art keywords
columnar body
close contact
heat exchanger
tubes
outer shell
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
JP58193595A
Other languages
Japanese (ja)
Other versions
JPS6086383A (en
Inventor
Kyoteru Takayasu
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP19359583A priority Critical patent/JPS6086383A/en
Publication of JPS6086383A publication Critical patent/JPS6086383A/en
Publication of JPH0245785B2 publication Critical patent/JPH0245785B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/02Heat-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
    • F28D7/024Heat-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 only one medium being helically coiled tubes, 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)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】 本発明は熱交換器に関し、さらに詳しくは、熱
交換効率の極めて優れた熱交換器に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat exchanger, and more particularly to a heat exchanger with extremely high heat exchange efficiency.

一般に、例えば、瞬間湯沸し等に使用されてい
る熱交換器は、大体において銅または銅合金によ
り作られているものが多く、この銅、銅合金は熱
伝導性が良く熱交換効率がよいが、都市ガスまた
はプロパンガス等の燃焼により腐蝕することがあ
るので、熱交換器の肉厚を厚くしなければならず
重くなるという問題がある。例えば、第3図に示
す熱交換器においては、箱体20内を矢印の方向
に燃焼ガスが流れ、箱体20の外側に捲回されて
いる管21内を流れる流体と熱交換するのである
が、肉厚が厚いことと相俟つて熱交換効率が悪
い。
In general, heat exchangers used for instantaneous water heating, etc., are generally made of copper or copper alloys. Copper and copper alloys have good thermal conductivity and high heat exchange efficiency, but Since combustion of city gas, propane gas, etc. may cause corrosion, there is a problem that the heat exchanger must be thicker and heavier. For example, in the heat exchanger shown in FIG. 3, combustion gas flows inside the box 20 in the direction of the arrow and exchanges heat with the fluid flowing inside the tube 21 wound outside the box 20. However, combined with the thick wall thickness, the heat exchange efficiency is poor.

本発明はこのような1例として説明した熱交換
器に比し、熱交換効率が格段に優れている熱交換
器を提供するものである。
The present invention provides a heat exchanger that has much better heat exchange efficiency than the heat exchanger described as an example.

本発明に係る熱交換器の特徴とするところは、
並列に並べた互いに密着した複数の管が螺旋状に
捲回されて柱状体に取付けた支持体を介して柱状
体に密着して設けられ、さらに、柱状体に密着し
た螺旋状に捲回されて並列に並べた互いに密着し
た複数の管と互い違いに、かつ、外側に並列に並
べた互いに密着した複数の管が螺旋状に捲回され
て外殻に取付けた支持体を介して外殻に密着して
設けられていることにある。
The features of the heat exchanger according to the present invention are as follows:
A plurality of tubes arranged in parallel and in close contact with each other are spirally wound and provided in close contact with the columnar body via a support attached to the columnar body, and further spirally wound in close contact with the columnar body. A plurality of tubes arranged in parallel and in close contact with each other are alternately arranged, and a plurality of tubes arranged in parallel on the outside and in close contact with each other are spirally wound and attached to the outer shell via a support attached to the outer shell. This is because they are placed close together.

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使用する柱状
体、外殻、支持体および管の材料について説明す
る。
Materials for the columnar bodies, outer shell, supports, and tubes used in the heat exchanger according to the present invention will be explained.

柱状体として両端が閉じた形状の円筒体、角筒
体或いは円柱、角柱等の形状とし、中央部に排ガ
ス孔を設けることもでき、また、中が空胴の両端
が密閉された柱状体とすることにより、熱交換器
を軽くでき、さらに、材料節約にもなる。この柱
状体の材料は耐熱、耐蝕性材料であればよく、例
えば鉄系材料の純鉄、鉄合金、不銹鋼、耐蝕性金
属、または、銅、銅合金或いはアルミニウム、ア
ルミニウム合金等も使用できる。
The columnar body can be shaped like a cylinder with both ends closed, a rectangular cylinder, a cylinder, a square column, etc., with an exhaust gas hole in the center, or a columnar body with a hollow inside and sealed at both ends. This allows the heat exchanger to be made lighter and also saves on materials. The material of this columnar body may be any heat-resistant and corrosion-resistant material, and for example, ferrous materials such as pure iron, iron alloys, stainless steel, corrosion-resistant metals, copper, copper alloys, aluminum, aluminum alloys, etc. can also be used.

支持体はその形状は棒状、コの字状等の何れで
もよく、柱状体、外殻の何れかに取付けて管を支
持するものであるから、管の重さに耐える強度お
よび取付け数とすればよく、材料も柱状体と同じ
材料でよい。
The support may be rod-shaped, U-shaped, etc., and is attached to either a columnar body or an outer shell to support the pipe, so it must have enough strength to withstand the weight of the pipe and the number of attachments. The material may be the same as that of the columnar body.

管の材料は、鉄系材料が好適で、例えば、純
鉄、鉄合金、不銹鋼、その他、耐蝕性金属、その
他、銅、銅合金やアルミニウム、アルミニウム合
金等も使用できる。この管は一重でもまた二重で
もどちらも使用できる。この管二重構造(クラツ
ド管)においては、例えば、管内側が耐蝕性金属
とし、管外側が鉄系材料とする。この逆でもよ
い。
The material of the tube is preferably an iron-based material, and for example, pure iron, iron alloy, stainless steel, other corrosion-resistant metals, copper, copper alloy, aluminum, aluminum alloy, etc. can also be used. This tube can be used in both single and double layers. In this double tube structure (clad pipe), for example, the inside of the tube is made of a corrosion-resistant metal, and the outside of the tube is made of an iron-based material. The opposite is also possible.

耐蝕性金属は、Ti,Zr,Ta,Mo,Nb,Vお
よびこれらの合金を使用することができ、燃焼ガ
スの種類や流す液体の種類によつては不銹鋼、
銅、銅合金或いはアルミニウム、アルミニウム合
金を使用してもよい。
Corrosion-resistant metals can include Ti, Zr, Ta, Mo, Nb, V, and alloys thereof, and depending on the type of combustion gas and the type of liquid to be flowed, non-ferrous steel,
Copper, copper alloys, aluminum, and aluminum alloys may also 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、先ず、複数の管を並列に密着させて
並べて柱状体の周囲に螺旋状に捲回して柱状体或
いは外殻に取付けた支持体を介して密着して設
け、さらに、柱状体の周囲に螺旋状に捲回した複
数の管を並列に密着させて並べた管と互い違い
に、かつ、外側に複数の管を並列に密着させて並
べて螺旋状に捲回して柱状体或いは外殻に取付け
た支持体を介して密着して設けられているもので
あり、複数の支持体により支持されている。そし
て、複数の並列に並べる管の数および螺旋状に捲
回する数は夫々多い程熱交換効率は良くなるが、
使用する燃料の種類、流体の種類や、また、材料
の強度等から適宜に選択すればよい。
However, in the heat exchanger according to the present invention,
The shape of the tube is determined by first arranging a plurality of tubes in close contact with each other in parallel, winding them in a spiral around a columnar body, and providing the tubes in close contact with each other via a support attached to the columnar body or outer shell. A columnar body or an outer shell is formed by winding a plurality of tubes in a spiral shape around the periphery of the tubes, alternating with the tubes arranged closely in parallel in parallel, and on the outside by arranging a plurality of tubes in close contact with each other in a spiral shape. It is provided in close contact with the support body attached to the base body, and is supported by a plurality of support bodies. The heat exchange efficiency improves as the number of tubes arranged in parallel and the number of tubes wound in a spiral shape increase.
It may be selected as appropriate based on the type of fuel used, the type of fluid, the strength of the material, etc.

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。
The heat exchanger according to the present invention will be specifically explained using an example shown in the drawings.

第1図において、柱状体1の複数箇所に溶接等
により支持体3を取付け、そして、柱状体1の周
囲で、かつ、この支持体3に管2を複数密着させ
て並列に並べて螺旋状に成形して柱状体1に密着
して載置する。この場合、管2は3本であるが、
2本以上であれば技術的に可能な限り多くできる
が、材料の強度や熱交換器の構成等から適宜に選
択すればよく、また、支持体3はコの字状のもの
でもよい。また。第1図では支持体3は柱状体1
に取付けてあるが外殻5に取付けることもでき
る。
In FIG. 1, supports 3 are attached to a plurality of locations on a columnar body 1 by welding or the like, and a plurality of tubes 2 are arranged in parallel around the columnar body 1 and in close contact with the supports 3 in a spiral shape. It is molded and placed in close contact with the columnar body 1. In this case, there are three pipes 2, but
As long as there are two or more, the number can be as large as technically possible, but they may be selected appropriately depending on the strength of the material, the structure of the heat exchanger, etc. Also, the support 3 may be U-shaped. Also. In FIG. 1, the support 3 is a columnar body 1.
Although it is attached to the outer shell 5, it can also be attached to the outer shell 5.

さらに、この柱状体1の周囲に複数の管2を並
列に密着して並べて螺旋状に成形した管と互い違
いであつて、かつ、外側に複数の管4を密着させ
て並列に並べて捲回して外殻5の内側に取付けた
支持体3に外殻5に密着して載置する。この場合
の管4の数や捲回数は内側の数との兼ね合せで選
択するのがよい。
Further, a plurality of tubes 2 are closely arranged in parallel around this columnar body 1 and formed into a spiral shape, alternating with each other, and a plurality of tubes 4 are closely arranged on the outside in parallel and wound. It is placed on a support 3 attached to the inside of the outer shell 5 in close contact with the outer shell 5. In this case, the number of tubes 4 and the number of turns should be selected in consideration of the number of tubes inside.

これら複数の管2,4夫々は密着させるのは勿
論のこと、管2と柱状体1および管4と外殻5と
も支持体3を介して密着させることが必要であ
り、隙間があると燃焼ガス等が漏れることになつ
て、高温の流体が円滑に螺旋状に流れ難くなるか
らである。
It goes without saying that these plurality of tubes 2 and 4 must be brought into close contact with each other, but also with the tube 2 and the columnar body 1 and the tube 4 and the outer shell 5 through the support body 3. If there is a gap, combustion will occur. This is because gas and the like will leak, making it difficult for the high-temperature fluid to flow smoothly in a spiral pattern.

なお、管を複数密着させて並列に並べて螺旋状
に成形したものを螺旋状管と言うことがある。
Note that a plurality of tubes arranged in close contact with each other in parallel and formed into a spiral shape is sometimes referred to as a spiral tube.

第2図は第1図に示す本発明に係る熱交換器を
組込んだ湯沸し器である。即ち、外殻5の底部に
取付けた底板10上に、支持体3上に載置された
螺旋状管2が設けられている柱状体1およびこの
螺旋状管2と互い違いで、かつ、その外側に支持
体3上に載置された螺旋状管4が設けられている
外殻5が設置されている。また、底板10にはガ
スバーナー6が複数個設けガス源7より矢印のよ
うにガスが供給され、また、螺旋状管2および4
に流体として水を送給するには、水源8より矢印
のように水が水槽9内に満たされ、ここから各螺
旋状管2および4へ水が送給され、そして、熱交
換されて熱くなつた水は、螺旋状管2および4を
湯槽11に集め、そこから湯Hとして取出されて
各用途に送られる。
FIG. 2 shows a water heater incorporating the heat exchanger according to the present invention shown in FIG. That is, on the bottom plate 10 attached to the bottom of the outer shell 5, the columnar body 1 is provided with the spiral tube 2 placed on the support 3, and the columnar body 1 is provided with a spiral tube 2 placed on the support 3, and a columnar body 1 is provided on the bottom plate 10 attached to the bottom of the outer shell 5, and a columnar body 1 is provided with a spiral tube 2 placed on the support body 3, and a columnar body 1 is provided on the bottom plate 10 attached to the bottom of the outer shell 5. An outer shell 5 is provided with a helical tube 4 placed on a support 3 . Further, a plurality of gas burners 6 are provided on the bottom plate 10, and gas is supplied from a gas source 7 as shown by the arrow.
To supply water as a fluid to the water tank 9 from the water source 8 as shown by the arrow, the water is supplied from here to each spiral tube 2 and 4, and then heat exchanged to make it hot. The hot water is collected in the spiral pipes 2 and 4 in a hot water tank 11, from which it is taken out as hot water H and sent to various uses.

このような構成を有している本発明に係る熱交
換器を用いた湯沸し器において、先ず、水槽9の
水を螺旋状管2および4に送給して湯槽11へ達
した時に、ガスバーナー6に点火すると、燃焼ガ
スは第2図の矢印に示すように螺旋状管2および
4に沿つて上昇する過程において、燃焼ガスは螺
旋状管2および4と充分に接触することにより、
螺旋状管2および4内を流れる水と燃焼ガスとが
熱交換して熱くなつた水は湯槽11へ流れ、この
水の温度は80〜90℃、或いは沸騰する直前までに
なつており、適宜利用され、一方、燃焼ガスの温
度は約50℃、或いはそれ以下の温度なつて煙突1
2から排出される。このように、燃焼ガスと螺旋
状管との接触面積が極めて大きいので、燃焼ガス
と螺旋状管内を流れる水との熱交換率も大きく、
加熱された排水の温度が高く、かつ、拝出燃焼ガ
スも極めて低温となる。
In the water heater using the heat exchanger according to the present invention having such a configuration, first, when the water in the water tank 9 is fed to the spiral pipes 2 and 4 and reaches the water tank 11, the gas burner 6, the combustion gas rises along the spiral tubes 2 and 4 as shown by the arrow in FIG.
The water flowing through the spiral pipes 2 and 4 exchanges heat with the combustion gas, and the water becomes hot and flows into the hot water tank 11. On the other hand, the temperature of the combustion gas is about 50 degrees Celsius or lower and the chimney 1
It is discharged from 2. In this way, since the contact area between the combustion gas and the spiral tube is extremely large, the heat exchange rate between the combustion gas and the water flowing inside the spiral tube is also large.
The temperature of the heated wastewater is high, and the combustion gas discharged is also extremely low temperature.

なお、加熱源としてガスバーナーについて説明
したが、ボイラーの排ガス等にも適用することが
できる。
Although a gas burner has been described as a heating source, the present invention can also be applied to boiler exhaust gas, etc.

以上説明したように、本発明に係る熱交換器は
上記の構成を有しているものであるから、高温の
排ガスと螺旋状管との接触面積が極めて大きいの
で、熱交換率も大であり、燃料を有効に利用する
ことができるという効果がある。
As explained above, since the heat exchanger according to the present invention has the above configuration, the contact area between the high temperature exhaust gas and the spiral tube is extremely large, so the heat exchange rate is also large. This has the effect that fuel can be used effectively.

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

第1図は本発明に係る熱交換器の概略側面図、
第2図は本発明に係る熱交換器を組込んだ湯沸し
器の概略側面図、第3図は従来の熱交換器の斜視
図である。 1……柱状体、2,4……螺旋状管、3……支
持体、5……外殻、6……ガスバーナー、7……
ガス源、8……水源、9……水槽、10……底
板、11……湯槽、12……煙突。
FIG. 1 is a schematic side view of a heat exchanger according to the present invention;
FIG. 2 is a schematic side view of a water heater incorporating a heat exchanger according to the present invention, and FIG. 3 is a perspective view of a conventional heat exchanger. 1... Column, 2, 4... Spiral tube, 3... Support, 5... Outer shell, 6... Gas burner, 7...
Gas source, 8...water source, 9...water tank, 10...bottom plate, 11...hot water tank, 12...chimney.

Claims (1)

【特許請求の範囲】[Claims] 1 並列に並べた互いに密着した複数の管が螺旋
状に捲回されて柱状体に取付けた支持体を介して
柱状体に密着して設けられ、さらに、柱状体に密
着した螺旋状に捲回されて並列に並べた互いに密
着した複数の管と互い違いに、かつ、外側に並列
に並べた互いに密着した複数の管が螺旋状に捲回
されて外殻に取付けた支持体を介して外殻に密着
して設けられていることを特徴とする熱交換器。
1 A plurality of tubes arranged in parallel and in close contact with each other are spirally wound and provided in close contact with the columnar body via a support attached to the columnar body, and further spirally wound in close contact with the columnar body. A plurality of tubes arranged in parallel and in close contact with each other are alternately arranged, and a plurality of tubes arranged in parallel on the outside in close contact with each other are spirally wound and connected to the outer shell through a support attached to the outer shell. A heat exchanger characterized by being provided in close contact with.
JP19359583A 1983-10-17 1983-10-17 Heat exchanger Granted JPS6086383A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19359583A JPS6086383A (en) 1983-10-17 1983-10-17 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19359583A JPS6086383A (en) 1983-10-17 1983-10-17 Heat exchanger

Publications (2)

Publication Number Publication Date
JPS6086383A JPS6086383A (en) 1985-05-15
JPH0245785B2 true JPH0245785B2 (en) 1990-10-11

Family

ID=16310566

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19359583A Granted JPS6086383A (en) 1983-10-17 1983-10-17 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS6086383A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI404903B (en) * 2007-03-09 2013-08-11 Sulzer Chemtech Ag Equipment for heat exchange and mixing of fluid media

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5798790A (en) * 1980-12-10 1982-06-19 Hitachi Ltd Heat exchanger
JPS5886388A (en) * 1981-11-19 1983-05-23 Kiyoteru Takayasu Heat exchanger

Also Published As

Publication number Publication date
JPS6086383A (en) 1985-05-15

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