JPS6086383A - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPS6086383A
JPS6086383A JP19359583A JP19359583A JPS6086383A JP S6086383 A JPS6086383 A JP S6086383A JP 19359583 A JP19359583 A JP 19359583A JP 19359583 A JP19359583 A JP 19359583A JP S6086383 A JPS6086383 A JP S6086383A
Authority
JP
Japan
Prior art keywords
tubes
heat exchanger
outer shell
attached
parallel
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.)
Granted
Application number
JP19359583A
Other languages
Japanese (ja)
Other versions
JPH0245785B2 (en
Inventor
Kiyoteru Takayasu
高安 清輝
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)

Abstract

PURPOSE:To improve heat exchanging efficiency particularly by a method wherein a plurality of tubes, arranged in parallel, are wound in spiral and are attached to a column body and an outer shell in a heat exchanger for a tap- controlled hot-water heater or the like and similar tubes are provided in zigzag with those tubes. CONSTITUTION:Support bodies 3 are attached to a column body 1 at a plurality of places by welding or the like and a plurality of tubes 2, arranged in parallel under being contacted closely with each other and formed in spiral, is disposed on the support bodies 3 around the column body 1. The support bodies 3 are being attached to the column body 1, however, they can be attached to the outer shell 5. A plurality of tubes 4, arranged in parallel so as to be contacted with each other, is arranged in zigzag to the plurality of tubes 2 above-described and is disposed on the support bodies 3 attached to the inside of the outer shell 5. It is necessary to contact the plurality of tubes 2, 4 with each other, the tubes 2 with the column body 1 and the tubes 4 with the outer shell 5 through support bodies 3.

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、熱交憾器の肉厚を厚くしな
ければならす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
いことと相俟って熱交換功率が悪い。
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 or propane gas may cause corrosion, there is a problem that the heat exchanger must be thicker and heavier. For example, the third
In the heat exchanger shown in the figure, 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. Combined with the thick layer, 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
べた複数の管が螺旋状に捲回されて柱状体或いは外殻に
取付けた支持体を介して設けられ、さらに、この柱状体
に螺旋状に捲回されて並列に並べた複数の管と互い違い
に、かつ、外側に並列に並べた複数の管が螺旋状に捲回
されて柱状体或いは外殻に取付けた支持体を介して設け
られていることにある。
The heat exchanger according to the present invention is characterized in that a plurality of tubes arranged in parallel are spirally wound and provided via a support attached to a columnar body or an outer shell. A plurality of tubes are wound in a spiral and arranged in parallel alternately, and a plurality of tubes are arranged in parallel on the outside are wound in a spiral and are connected through a support attached to a columnar body or an outer shell. That's what it has to offer.

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。
Columnar bodies and outer shells used in the heat exchanger according to the present invention,
The materials of the support and tube 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、中央部に徘ガス孔を設けるこ
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、材料の
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 a wandering gas hole in the center, or a columnar body with a hollow inside and sealed at both ends. By doing so, the heat exchanger can be made lighter, and furthermore, materials can be saved. The material of this columnar body may be any heat-resistant and corrosion-resistant material, such as pure iron, iron alloy, stainless steel, etc.
Corrosion-resistant metal, or copper, copper alloy or 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は数とすれば
よく、材料も柱状体と同し材料でよい。
The support may have a rod-like shape, a U-shape, etc.
Since the tube is supported by being attached to either the columnar body or the outer shell, the strength to withstand the weight of the tube and the number of attachments may be determined by the number of attachments, and 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トる。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、T1、Z「、Ta、 MO,Nll、■
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っては不銹鋼、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 include T1, Z'', Ta, MO, Nll, ■
Depending on the type of combustion gas and the type of liquid to be flowed, stainless steel, copper, copper alloys, aluminum, and aluminum alloys may also be used.

しh化て、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、がっ、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。
Therefore, in the heat exchanger according to the present invention, the shape of the tubes is such that first, a plurality of tubes are closely arranged in parallel, wound spirally around a columnar body, and then attached to a columnar body or an outer shell. In addition, a plurality of tubes wound spirally around a columnar body are arranged closely in parallel, and a plurality of tubes are arranged in close contact with each other in parallel on the outside. They are arranged through supports that are arranged in parallel and spirally wound and attached to a columnar body or an outer shell, and are supported by a plurality of supports. The heat exchange efficiency improves as the number of tubes arranged in parallel and the number of tubes wound in a spiral shape increase, but depending on the type of fuel and fluid used, the strength of the material, etc. Just choose.

3一 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。
31 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に取付けであるが外殻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. Shape and place. In this case, there are three tubes 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 attached to the columnar body 1, but 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って、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, and a plurality of tubes 4 are arranged in close contact with each other and arranged in parallel on the outside and are wound. It is placed on a support 3 attached to the inside of 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.

複数の管2.4夫々は密着させることは勿論のこと、管
2と柱状体1および管4と外殻5とも支4− 特休3を介して密着させることが必要であり、隙間があ
ると燃焼がス等が漏れることになって、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 the 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 supports 4 and 3, so that there are gaps. This is because combustion gas will leak, making it difficult for the high-temperature fluid to flow smoothly in a spiral pattern.

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1
0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
1oにはガスバーナー6が複数個設はガス源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った水
は、螺旋状管2および4を湯槽11に集め、そこがら湯
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, the bottom plate 1 attached to the bottom of the outer shell 5
0, a columnar body 1 is provided with a helical tube 2 placed on a support 3, and a helical body placed on the support 3 alternately with the helical tube 2 and on the outside thereof. A shaped tube 4 is provided. - An outer shell 5 is provided. In addition, when a plurality of gas burners 6 are installed on the bottom plate 1o, gas is supplied from a gas source 7 as shown by the arrow, and in order to supply water as a fluid to the spiral tubes 2 and 4, a water source 8 is provided as shown in the arrow. Water is filled in the water tank 9 as shown in FIG. The hot water is collected, extracted 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、燃焼がスは第2図の矢印に示すよう
に螺旋状管2および4に沿って上昇する過程においで、
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
熱交換して熱くなった水は湯槽11へ流れ、この水の温
度は80〜90°C1或いは沸騰する直前までになって
おり、適宜利用され、一方、1a焼ガスの温度は約50
℃、或いはそれ以下の温度なって煙突12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
めて大トいので、燃焼が又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, the water in the water tank 9 is poured into the spiral tube 2.
and 4 and when it reaches the hot water tank 11, the gas burner 6 is ignited, and the combustion gas rises along the spiral pipes 2 and 4 as shown by the arrow in FIG.
The combustion gas comes into sufficient contact with the spiral tubes 2 and 4, and the water flowing in the spiral tubes 2 and 4 exchanges heat with the combustion gas, and the heated water flows to the hot water tank 11, and the temperature of this water decreases. is 80-90°C1 or just before boiling, and is used as appropriate.On the other hand, the temperature of 1a baking gas is about 50°C.
℃ or lower temperature is discharged from the chimney 12. 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, and the temperature of the heated wastewater is high. The combustion gas also has an extremely low temperature.

なお、加熱源としてガスバーナーに2いて説明したが、
ボイラーの排ガス等にも適用することかできる。
In addition, although I explained using a gas burner as the heating source,
It can also be applied to boiler exhaust gas, etc.

一7= 以−]二説明したように、本発明に係る熱交換器は」1
記の構成を有しているものであるか呟高温の排ガスと螺
旋状管との接触面積が極めて大きいので、熱交換効率も
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。
17=hereinafter -]2 As explained, the heat exchanger according to the present invention is
Since the contact area between the high-temperature exhaust gas and the spiral tube is extremely large, the heat exchange efficiency is also high and the fuel can be used effectively. .

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

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。 8−
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 the heat exchanger according to the present invention, and FIG. 3 is a perspective view of a conventional heat exchanger. It is. 1. Column body, 2.4. Spiral tube, 3. Support body, 5
... Outer shell, 6. Gas burner, 7. Gas source, 8.
Water source, 9... Water tank, 10... Bottom plate, 11... Hot water tank, 12
··chimney. 8-

Claims (1)

【特許請求の範囲】[Claims] 並列に並べた複数の管が螺旋状に捲回されて柱状体或い
は外殻に取付けた支持体を介しで設けられ、さらに、こ
の柱状体に螺旋状に捲回されて並列に並べた複数の管と
互い違いに、かつ、外側に並列に並べた複数の管が螺旋
状に捲回されて柱状体或いは外殻に支持体を介しで設け
られていることを特徴とする熱交換器。
A plurality of tubes arranged in parallel are wound spirally and provided via a support attached to a columnar body or an outer shell. A heat exchanger characterized in that a plurality of tubes are arranged alternately with the tubes and arranged in parallel on the outside, and are spirally wound and provided on a columnar body or an outer shell via a support.
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 true JPS6086383A (en) 1985-05-15
JPH0245785B2 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)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8794820B2 (en) * 2007-03-09 2014-08-05 Sulzer Chemtech Ag Apparatus for the heat-exchanging and mixing treatment of fluid media

Citations (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

Patent Citations (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

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8794820B2 (en) * 2007-03-09 2014-08-05 Sulzer Chemtech Ag Apparatus for the heat-exchanging and mixing treatment of fluid media

Also Published As

Publication number Publication date
JPH0245785B2 (en) 1990-10-11

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