JPS5886387A - Heat exchanger - Google Patents
Heat exchangerInfo
- Publication number
- JPS5886387A JPS5886387A JP18577681A JP18577681A JPS5886387A JP S5886387 A JPS5886387 A JP S5886387A JP 18577681 A JP18577681 A JP 18577681A JP 18577681 A JP18577681 A JP 18577681A JP S5886387 A JPS5886387 A JP S5886387A
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- pipes
- outer shell
- columnar member
- heat
- 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
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
- F24H1/10—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium
- F24H1/12—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium
- F24H1/14—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium by tubes, e.g. bent in serpentine form
- F24H1/16—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium by tubes, e.g. bent in serpentine form helically or spirally coiled
- F24H1/165—Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium by tubes, e.g. bent in serpentine form helically or spirally coiled using fluid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
- F24H1/22—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating
- F24H1/40—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water tube or tubes
- F24H1/43—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water tube or tubes helically or spirally coiled
-
- 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
-
- 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
- F28D7/04—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 spirally coiled
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
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、軽くて耐蝕
性にすぐれ、かつ、熱交換効率の良好な熱交換器に関す
るものである。。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat exchanger, and more particularly to a heat exchanger that is lightweight, has excellent corrosion resistance, and has good heat exchange efficiency. .
一般に、例えば、瞬間湯沸しなどに使用されている熱交
換器は、銅または銅合金により作られているものであり
、そして、銅または銅合金は熱伝導性が良好、であるの
で熱交換効率がよいが、′Ｎ量が重いということがあり
、また、都市ガス又は、フロパンガスの燃焼により腐蝕
する場合があるので肉厚を厚くしなければならず、１．
門がより重くなるという問題がある、例えは、第６図に
示すように、箱壁体２０内を矢印の方向に燃焼ガスが流
れて管２１と熱交換する場合に上記のようなことが起る
のである。Generally, heat exchangers used for instant water heating, for example, are made of copper or copper alloys, and copper or copper alloys have good thermal conductivity, so heat exchange efficiency is low. However, the N content may be heavy, and the wall thickness must be thick because it may corrode due to combustion of city gas or flopane gas.1.
There is a problem that the gate becomes heavier. For example, as shown in FIG. It happens.
本発明は、従来瞬間湯沸しなどに使用されてきている銅
または銅合金により作られた熱交換器に比して、比較的
に軽く、熱交換率も良好で、さらに、耐蝕性にもすぐれ
た熱交換器を提供するものである。Compared to heat exchangers made of copper or copper alloys that have been conventionally used for instant water heating, the present invention is relatively lighter, has a better heat exchange rate, and has excellent corrosion resistance. It provides a heat exchanger.
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設けたことにある１、
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 is characterized in that a plurality of tubes arranged in parallel are spirally wound through a support attached to a columnar body or an outer shell.1. The heat exchanger according to the 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
、螺旋状の管等の拐料について説明する、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、角柱等であシ、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、耐蝕材料であれは
よく、例えに、Ｆｅ系材料が好適で、純鉄、鉄合金、不
銹鋼、また、耐蝕性金属、合金、銅、銅合金また、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。In the heat exchanger according to the present invention, the pillars, supports, spiral tubes, etc. will be explained. First, the pillars include cylinders with both ends closed, rectangular cylinders, etc. Alternatively, it may be a cylinder, a prism, etc., with a hole provided in the middle to allow exhaust gas to pass through. This material may be any heat-resistant and corrosion-resistant material; for example, Fe-based materials are preferred, as well as pure iron, iron alloys, stainless steel, corrosion-resistant metals, alloys, copper, copper alloys, and aluminum and aluminum alloys. can be used.
しかして、柱状体は中が空胴で両端の密閉された円筒体
、角筒体等が熱交換器を軽くシ、かつ、材料の節約にも
なるので好都合で４＞る１、次に、支持体は棒状、壕だ
、コ字状の何れでもよく、柱状体、或いは、外殻の伺Ｊ
１．かに取付けて管を支持するもので、管の重音Ｖ（−
１ＭＩえる程度の強度、取付は数とすればよく、使用飼
料も柱状体と同様のものでよい。Therefore, a columnar body is hollow inside and closed at both ends, such as a cylindrical body or a rectangular cylinder, which makes the heat exchanger light and saves materials, so it is convenient. The support may be rod-shaped, trench-shaped, U-shaped, columnar, or shaped like an outer shell.
1. This is a device that is attached to a crab to support the pipe, and prevents heavy sound V (-
The strength is sufficient to reach 1 MI, the number of attachments may be limited, and the feed used may be the same as for 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、不銹銅、また、耐蝕性余端または合金さらに、
銅、銅合金、アルミニウム、アルミニウム合金等が使用
でき、またこのパイプは一重構造と二重構造との両方の
形状が使用できる。The material of the tube is preferably Fe-based material, such as pure iron,
Iron alloys, non-corrosive copper, and also corrosion-resistant extra ends or alloys,
Copper, copper alloy, aluminum, aluminum alloy, etc. can be used, and the pipe can have both a single structure and a double structure.
また、管二重構造、即ち、複合構造とすることは、管内
側は耐蝕性金属または合金で、外側がＦｅ系材料とした
構造をいうものである３、耐蝕性金属または合金として
は、Ｔｉ 、Ｚｒ 、Ｔａ 、Ｍｏ。In addition, a double tube structure, that is, a composite structure, refers to a structure in which the inner side of the tube is made of a corrosion-resistant metal or alloy and the outer side is made of Fe-based material3.The corrosion-resistant metal or alloy is made of Ti. , Zr, Ta, Mo.
ＮｂやＴ ｒ 、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。Nb, alloys of T r , Zr + Ta, Mo 2 +Nb, stainless steel, copper and copper alloys, 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、管を並列に密着させて並べて柱状体の囲りに螺旋状
に捲回して設けるものであって、支持体によって複数個
所で支えられている。そして、この螺旋に捲回する回数
は多い程良いが、熱交換率、材料の強度等から適当に選
定すればよい。Therefore, in the heat exchanger according to the present invention, the shape of the tubes is such that the tubes are arranged in close contact with each other in parallel and are spirally wound around the columnar body, and the tubes are provided at multiple locations by the support. I feel supported. The number of spiral windings is preferably as large as possible, but it may be selected appropriately based on the heat exchange rate, the strength of the material, etc.
また、外殻は柱状体と同様に耐熱、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 like the columnar body, and is preferably made of the same material as the columnar body.
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７、
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６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、第４図は螺旋
状管の給水部と排水部の概略断面図、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。Next, the heat exchanger according to the present invention will be specifically explained using examples shown in the drawings.
Fig. 6 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 is a schematic cross-section of the water supply part and drainage part of the spiral pipe. Figures 5 and 5 show other examples, and Figure 6 is a perspective view of a conventional heat exchanger.
第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）にコ字状に、例えは、溶接等により支持体
６を増刊け、この支持体６，５間に螺旋状の管２，２．
２（第１図では６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６，５は第１
図ではコ字状となっているが、一本の支持体３１に支持
させてもよく、また、即、１図で幻、支持体６は柱状体
１に取付けられているが、この支持体を外殻に数句けて
もよい（第５図参照）。１だ、この螺旋状管２゜２．２
は互に密着させて流体、例えば、管の隙間、管と柱状体
、外殻との隙間から燃焼ガスが漏れ々いように形成し、
かつ、柱状体１と外殻５（第６図）との間隔内に丁度挾
１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、螺旋状管２，２．２と充分接触させるためである
。In FIGS. 1 and 2, additional supports 6 are added in a U-shape at multiple locations (5 locations in FIG. 1) on the columnar body 1, for example by welding, and between the supports 6 and 5. Spiral tube 2,2.
2 (in Fig. 1, there are six tubes, but any number of tubes may be used as long as there are two or more). These supports 6, 5 are the first
Although it has a U-shape in the figure, it may be supported by a single support 31; You may write several words on the outer shell (see Figure 5). 1, this spiral tube 2°2.2
are in close contact with each other so that fluid, such as combustion gas, leaks from the gaps between the tubes, the gaps between the tubes and the columnar body, and the outer shell;
In addition, it is necessary to provide a width that is just enough to fit within the distance between the columnar body 1 and the outer shell 5 (FIG. 6). As will be explained later,
This is to allow the high temperature fluid, for example combustion gas, to flow in a helical manner and to make sufficient contact with the helical tubes 2, 2.2.
第６図は上記に説明した第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り、即ち、外殻５の底
部に取付けた底板７土に支持体６゜５により支持されて
いる螺旋状管２，２．２が設けられている柱状体１を載
置する。この場合、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する。そして、
この底板７にはガスバーナー８を複数個設はガスＧを供
給され、かつ、外殻５と壁乙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、加熱空気が送られるのでガス
の燃焼を助長する。FIG. 6 shows an example of an instantaneous water heater incorporating the heat exchanger of FIG. A column 1 is placed which is provided with a helical tube 2, 2.2 supported by. In this case, the spiral tubes 2, 2.2 are tightly attached, and the structure is such that no fluid passes between the columnar body 1 and the outer shell 5, and the fluid flows spirally as shown by the arrow. and,
A plurality of gas burners 8 are installed on this bottom plate 7, and gas G is supplied thereto, and an air passage is formed by the outer shell 5 and the wall A, so that air is sent from the inlet 9 to the gas burners 8 in the direction of the arrow. It's okay. This facilitates combustion of the gas as heated air is passed through.
また、螺旋状管２，２．２に液体、例えば、水を送るに
は、第４図に示すように水ＷはパイプＰにより給水部４
に入り、ここから螺旋状の管２゜２．２に送られていき
、熱くなった水は、上記とは逆に、即ち、螺旋状の管２
，２．２から給水部４（排水部１１となる１、）へたま
り、パイプＰから排出されるのである１、
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螺旋状の管２゜２．２内を流して排
水部１１へ達すると、ガスＧよりガスバーナー８に点火
すると、この燃焼ガスは矢印に示すように螺旋状の管２
，２．２に沿って上昇し、その間に、螺旋状の管２，２
．２内を流れる水と高温の燃焼カスとが熱交換して、排
水部１１に流れる水Ｈけ８０″〜９０°（２近くもの温
度とガって排水されて利用され、−・方、燃焼ガスは、
約５０℃程度の低温と／Ｉ：つて煙突１〔］から排出さ
れる。このように、高温の燃焼ガスと螺旋状の管との接
触面積が極めて大きいので、燃焼ガスと螺旋状の管内を
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。In addition, in order to send a liquid, for example, water to the spiral pipes 2, 2.2, water W is sent to the water supply section 4 through a pipe P as shown in FIG.
The hot water enters the spiral tube 2゜2.
, 2.2, the water collects in the water supply section 4 (1, which becomes the drainage section 11), and is discharged from the pipe P. In a water heater, water W is first supplied to the water supply part 4, flows through the spiral pipe 2°2.2, and reaches the drainage part 11. When the gas G ignites the gas burner 8, this combustion gas is a spiral tube 2 as shown by the arrow
, 2.2, between which the spiral tube 2, 2
．． The water flowing through 2 and the high-temperature combustion residue exchange heat, and the water flowing into the drainage section 11 reaches a temperature of 80'' to 90° (nearly 2 degrees) and is drained and used. The gas is
It is discharged from the chimney 1 [] at a low temperature of about 50°C. In this way, since the contact area between the high temperature combustion gas and the spiral pipe is extremely large, the heat exchange rate between the combustion gas and the water flowing inside the spiral pipe is also large, and therefore the temperature of the heated and drained water also decreases. In addition, the exhaust combustion gas is also extremely low temperature.
なお・、第６図において、壁６ｆ設けなくでもよいので
ある（第５図診照）。In addition, in FIG. 6, the wall 6f may not be provided (see FIG. 5).
以上、説明したようＶこ、本発明に係る熱交換器は、燃
焼ガスと螺旋状の管との接触面積が極めて大きいので、
熱交換効率もまた大であり、燃料を有効に利用できる優
れた効果をイ」ｌ−、−（いるものである、As explained above, in the heat exchanger according to the present invention, since the contact area between the combustion gas and the spiral tube is extremely large,
The heat exchange efficiency is also high, and it has an excellent effect of making effective use of fuel.
第１図は本発明に係る熱交換器の１例を示す概略側面図
、第２図は第１図のＡ−Ａ矢視図、第６図は本発明に係
る熱交換器を適用した瞬間湯沸し器の一部切欠概略側面
図、第４図は給水部（排水部）の断面図、第５図は他の
例を示す一部切欠概略図、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〜煙突、１１〜排水部。
特許出願人 高 安 清 輝＼
４
４１６−
第６図FIG. 1 is a schematic side view showing one example of the heat exchanger according to the present invention, FIG. 2 is a view taken along arrow A-A in FIG. 1, and FIG. 6 is a moment when the heat exchanger according to the present invention is applied. FIG. 4 is a cross-sectional view of the water supply section (drainage section), FIG. 5 is a partially cut-away schematic diagram showing another example, and FIG. 6 is a perspective view of a conventional heat exchanger. It is a diagram. 1 - Column, 2 - Spiral tube, 3 - Support, 4 - Water supply, 5 - Outer shell, 6 - Wall, 7 - Bottom plate, 8 - Burner, 9 - Inlet, 10 - Chimney, 11 - Drainage Department. Patent applicant: Kiyoteru Takayasu＼ 4 416- Figure 6
Claims (1)
支持体を介して螺旋状に捲回して設けたことを特徴とす
る熱交換器。A heat exchanger characterized in that a plurality of tubes arranged in parallel are spirally wound through a support attached to a columnar body or an outer shell.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18577681A JPS5886387A (en) | 1981-11-19 | 1981-11-19 | Heat exchanger |
| AU90627/82A AU9062782A (en) | 1981-11-19 | 1982-11-16 | Heat exchanger |
| EP82110610A EP0080161A3 (en) | 1981-11-19 | 1982-11-18 | Heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18577681A JPS5886387A (en) | 1981-11-19 | 1981-11-19 | Heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS5886387A true JPS5886387A (en) | 1983-05-23 |
Family
ID=16176685
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18577681A Pending JPS5886387A (en) | 1981-11-19 | 1981-11-19 | Heat exchanger |
Country Status (3)
| Country | Link |
|---|---|
| EP (1) | EP0080161A3 (en) |
| JP (1) | JPS5886387A (en) |
| AU (1) | AU9062782A (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01500685A (en) * | 1986-08-21 | 1989-03-09 | バーダー，エミル | Counterflow heat exchanger with spiral tube bundle |
| AT392839B (en) * | 1988-10-21 | 1991-06-25 | Vaillant Gmbh | CONTINUOUS HEAT EXCHANGER |
| DE3925795A1 (en) * | 1989-08-04 | 1991-02-07 | Walter Englmann | Heat exchanger with spiral coils - which guided first medium while second medium flows through pipes forming spirals |
| CN2404087Y (en) * | 2000-01-26 | 2000-11-01 | 淮阴辉煌太阳能有限公司 | Assembled spiral sleeve heat exchanger |
| DE10234238B4 (en) * | 2001-07-25 | 2020-09-17 | Vaillant Gmbh | Heat exchanger |
| CN201488608U (en) * | 2009-07-20 | 2010-05-26 | 杜润强 | Steam cabinet exhaust steam water heat exchange recoverer and external connecting structure thereof |
| CN109405589B (en) * | 2018-11-30 | 2023-10-27 | 华南理工大学 | Spherical heat exchanger with double tube-pass independent heat exchange |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5169250A (en) * | 1974-12-12 | 1976-06-15 | Eiichi Uratani | Rasenryuronoaru netsukookanki |
| JPS5543245B2 (en) * | 1976-06-25 | 1980-11-05 |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE422424A (en) * | ||||
| US1893484A (en) * | 1932-07-26 | 1933-01-10 | Joseph S Belt | Heat exchanger |
| FR2155770A1 (en) * | 1971-10-04 | 1973-05-25 | Ind Chauffage | Spiral tube heat exchanger - with tubes contacting shell to define shell-side flow |
| FR2447528A1 (en) * | 1979-01-23 | 1980-08-22 | Zundel Daniel | Tubular heat exchanger - has multiple helical coils wound around central tube inside cylindrical housing |
| FR2482717A1 (en) * | 1980-05-14 | 1981-11-20 | Psa | Double fluid circuit heat exchanger - has spiral parallel tubes of primary fluid inside container for secondary fluid |
| FR2501832A1 (en) * | 1981-03-13 | 1982-09-17 | Bonneville Simone | Cleaner-heat exchanger for furnace flue - has dust removed centrifugally and heat extracted by internal pipes with finning |
-
1981
- 1981-11-19 JP JP18577681A patent/JPS5886387A/en active Pending
-
1982
- 1982-11-16 AU AU90627/82A patent/AU9062782A/en not_active Abandoned
- 1982-11-18 EP EP82110610A patent/EP0080161A3/en not_active Withdrawn
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5169250A (en) * | 1974-12-12 | 1976-06-15 | Eiichi Uratani | Rasenryuronoaru netsukookanki |
| JPS5543245B2 (en) * | 1976-06-25 | 1980-11-05 |
Also Published As
| Publication number | Publication date |
|---|---|
| AU9062782A (en) | 1983-06-16 |
| EP0080161A2 (en) | 1983-06-01 |
| EP0080161A3 (en) | 1983-11-30 |
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