JPS605277Y2 - Heat exchanger - Google Patents

Heat exchanger

Info

Publication number
JPS605277Y2
JPS605277Y2 JP12104680U JP12104680U JPS605277Y2 JP S605277 Y2 JPS605277 Y2 JP S605277Y2 JP 12104680 U JP12104680 U JP 12104680U JP 12104680 U JP12104680 U JP 12104680U JP S605277 Y2 JPS605277 Y2 JP S605277Y2
Authority
JP
Japan
Prior art keywords
heat exchanger
water
outer tube
heat
inner tube
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
Application number
JP12104680U
Other languages
Japanese (ja)
Other versions
JPS5746295U (en
Inventor
博史 平田
通行 藤島
Original Assignee
松下電器産業株式会社
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 松下電器産業株式会社 filed Critical 松下電器産業株式会社
Priority to JP12104680U priority Critical patent/JPS605277Y2/en
Publication of JPS5746295U publication Critical patent/JPS5746295U/ja
Application granted granted Critical
Publication of JPS605277Y2 publication Critical patent/JPS605277Y2/en
Expired legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/40Solar thermal energy, e.g. solar towers

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【考案の詳細な説明】 本考案は、一方の流体より他方の流体へと熱伝導する熱
交換器において、流体が互いに混じり合わないようにす
るとともに、熱伝導効率を高めることを目的としたもの
である。
[Detailed description of the invention] The purpose of this invention is to prevent fluids from mixing with each other and to improve heat transfer efficiency in a heat exchanger that conducts heat from one fluid to another. It is.

一般に太陽熱を利用して熱源を得ようとした場合、集熱
器で得た温水を給湯水として利用するのが簡単であり広
く用いられているが、日本に於ける中部地方以北では冬
期には水の凍結によって集熱器が破壊することがある。
Generally, when trying to obtain a heat source using solar heat, it is easy and widely used to use hot water obtained from a heat collector for hot water supply, but in the Chubu region and north of Japan, in winter The collector may be destroyed by freezing of the water.

そのために従来は第1図のごとく集熱器1の水回路と、
給湯器2の水回路を分離し、しかも凍結しないように加
圧ジスターン又は加圧ポンプ3にてホース4、バルブ5
を経由して集熱器1及び熱交換器6内部に不凍剤等を含
む不凍液を注入するようにしている。
For this purpose, conventionally, as shown in Figure 1, the water circuit of the heat collector 1,
Separate the water circuit of the water heater 2, and connect the hose 4 and valve 5 with a pressurized cylinder or pressurized pump 3 to prevent it from freezing.
An antifreeze solution containing an antifreeze agent or the like is injected into the heat collector 1 and the heat exchanger 6 via the heat collector 1 and the heat exchanger 6.

すなわち集熱器1により太陽熱より熱を受け、バルブA
、バルブ8を開け、ポンプ9にて不凍液を循環させ、熱
交換器6で給湯器2内の水を加熱するようになっている
のである。
That is, the heat collector 1 receives heat from the sun, and the valve A
, the valve 8 is opened, the antifreeze is circulated by the pump 9, and the water in the water heater 2 is heated by the heat exchanger 6.

なお不凍液の膨張収縮は膨張タンク10にて吸収される
Note that the expansion and contraction of the antifreeze is absorbed by the expansion tank 10.

また第2図、第3図は、給湯器2の正面図と断面図であ
るが、給水口11より供給された水は上述のごとくタン
ク12に取何けられた熱交換器6の外表面から熱伝導に
よって加熱され給湯口13より屋内等へ温水として供給
される。
Furthermore, FIGS. 2 and 3 are a front view and a sectional view of the water heater 2, and water supplied from the water supply port 11 is transferred to the outer surface of the heat exchanger 6 which is transferred to the tank 12 as described above. The water is heated by heat conduction and supplied as hot water indoors etc. from the hot water supply port 13.

なお14は水抜き用のドレン口であり、熱交換器6及び
タンク12は外部電源式電気防食等によって防食されて
おり、15がその電極である。
Note that 14 is a drain port for draining water, and the heat exchanger 6 and tank 12 are protected against corrosion by externally powered cathodic protection, and 15 is an electrode thereof.

以上のような構成の場合熱交換器6内を流れる不凍液が
給湯器2内の水中に混入すると色々な面で不都合が生じ
る。
In the case of the above configuration, if the antifreeze flowing through the heat exchanger 6 gets mixed into the water inside the water heater 2, various problems will occur.

このような場合に前述した二重管式の熱交換器6が用い
られる。
In such a case, the double-tube heat exchanger 6 described above is used.

すなわち第4図〜第6図に熱交換器6の詳細を示し、熱
交換器6は、内管16と外管17とからなり、内管16
は外管17により支持されており、外管17はフランジ
18に固定されており、フランジ18はタンク12側面
に固定されている。
That is, details of the heat exchanger 6 are shown in FIGS. 4 to 6, and the heat exchanger 6 is composed of an inner tube 16 and an outer tube 17.
is supported by an outer tube 17, and the outer tube 17 is fixed to a flange 18, which is fixed to the side surface of the tank 12.

外管17の外側はスパイラル状にされているので内管1
6と外管17との間にスパイラル状の連続した通路21
が形成され、外管17はフランジ18より外側に於いて
切断されている。
Since the outside of the outer tube 17 is spiral-shaped, the inner tube 1
6 and the outer tube 17 is a continuous spiral passage 21.
is formed, and the outer tube 17 is cut outside the flange 18.

このため内管16か又は外管17が腐食したりして内管
16と外管17の間に水が入った場合、その水はスパイ
ラル状の通路21を介して開口17aよりタンク12外
へ流出するようになっている。
Therefore, if the inner tube 16 or the outer tube 17 corrodes and water enters between the inner tube 16 and the outer tube 17, the water will flow out of the tank 12 from the opening 17a through the spiral passage 21. It's starting to leak out.

また内管16と外管17は密着部19と、スパイラル部
20より組み合わされているが、密着部19では内管1
6と外管17とが均一に密着しているために、内管16
から外管17への熱移動は良く、そのため熱効率は良い
In addition, the inner tube 16 and the outer tube 17 are combined through a close contact portion 19 and a spiral portion 20. In the close contact portion 19, the inner tube 1
6 and the outer tube 17 are in uniform contact with each other, the inner tube 16
The heat transfer from the tube to the outer tube 17 is good, so the thermal efficiency is good.

しかし、スパイラル部20では内部が中空の通路21と
なっているので、給水口11より冷水が供給された場合
などは通路21に空気中の水分が結露腰この結露水は空
気中の窒素、酸素、二酸化炭素を含むので、PH値が酸
性の腐食性を示腰内管16又は外管17をこの通路21
側より腐食させてしまうという欠点があった。
However, since the spiral part 20 has a hollow passage 21 inside, when cold water is supplied from the water supply port 11, moisture in the air condenses in the passage 21. This condensed water is caused by nitrogen and oxygen in the air. , since it contains carbon dioxide, the pH value shows acidic and corrosive properties.
The drawback was that it corroded from the sides.

本考案は、このような従来の欠点を一掃したものであり
、その一実施例として第7図のごとくスパイラル状の通
路21に、粉末状の防食物質22を充積したものである
The present invention eliminates these conventional drawbacks, and as an example thereof, as shown in FIG. 7, a spiral passage 21 is filled with a powdered anticorrosion substance 22.

この防食物質22は亜硝酸塩、リン酸、クロム酸塩、モ
リブデン酸塩、安息香酸塩又は硅酸塩のような金属の防
錆に対して効果のある物質であるので、結露水から内管
16と外管17の腐食を防止するとともに、この防食物
質22により通路21内が空洞でなくなり、しかもこの
防食物質22の方が空気より熱伝導性が良いので、熱交
換器6の熱交換効率が高くなる。
This anti-corrosion substance 22 is a substance effective in preventing corrosion of metals, such as nitrite, phosphoric acid, chromate, molybdate, benzoate or silicate, so that condensation water can be protected from the inner pipe 16. In addition to preventing corrosion of the outer tube 17, the anti-corrosion substance 22 eliminates the cavity inside the passage 21, and since the anti-corrosion substance 22 has better thermal conductivity than air, the heat exchange efficiency of the heat exchanger 6 is improved. It gets expensive.

更に、防食物質22は水に溶解すると乾燥時よりも体積
は減少する、即わち、固体の状態では、粉末の状態であ
るが、水に溶解すると、体積が減少するので、容易に結
露水の通過する空間は確保でき、本来の通路21の役割
(内管16又は外管17が仮に腐食したときでも流体を
給湯器2外へ排出する。
Furthermore, when the anticorrosion substance 22 is dissolved in water, its volume decreases compared to when it is dry. In other words, when it is in a solid state, it is in a powder state, but when it is dissolved in water, its volume decreases, so that it easily collects condensed water. The space for passage of fluid can be secured, and the original role of the passage 21 (even if the inner pipe 16 or the outer pipe 17 corrodes, the fluid is discharged to the outside of the water heater 2).

)を十分に果たす。以上のように本考案によれば内管内
の液体と外管外の液体が混入することがないので安全で
あり、しかも防食物質を設けることにより内管と外管の
間の熱伝導が良くなるので、その熱交換効率が高くなる
). As described above, according to the present invention, the liquid inside the inner tube does not mix with the liquid outside the outer tube, so it is safe, and the provision of anticorrosion material improves heat conduction between the inner tube and the outer tube. Therefore, the heat exchange efficiency becomes high.

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

第1図は本考案の前程となる熱交換器のシステム構成国
、第2図、第3図は同器の一部切欠正面図と一部切欠側
面図、第4図、第5図は同器の要部側面断面図と要部拡
大断面図、第6図は第5図A部の拡大断面図、第7図は
本考案の一実施例にかかる熱交換器の要部断面図である
。 16・・・・・・内管、17・・・・・・外管、21・
・・・・・通路、22・・・・・・防食物質。
Figure 1 shows the country of the system configuration of the heat exchanger that was developed earlier in the present invention, Figures 2 and 3 are a partially cutaway front view and side view of the heat exchanger, and Figures 4 and 5 are the same. FIG. 6 is an enlarged sectional view of section A in FIG. 5, and FIG. 7 is a sectional view of essential parts of a heat exchanger according to an embodiment of the present invention. . 16...Inner pipe, 17...Outer pipe, 21.
...Aisle, 22...Anti-corrosion substance.

Claims (1)

【実用新案登録請求の範囲】 1 内部を流体が通過する金属製の内管と、外表面に別
の流体が接触する金属製の外管を二重管構造にするとと
もに、外管と内管の間に、亜硝酸塩、リン酸塩、クロム
酸塩、モリブデン酸塩、安息香酸塩のうち一つ又は複数
を主成分とする防食物質を介在させたことを特徴とする
熱交換器。 2 内管と外管との間に、スパイラル状の通路を設け、
この通路に防食物質を設けたことを特徴とする実用新案
登録請求の範囲第1項に記載の熱交換器。
[Claims for Utility Model Registration] 1. A metal inner tube through which a fluid passes, and a metal outer tube whose outer surface is in contact with another fluid. A heat exchanger characterized in that an anticorrosion substance containing one or more of nitrite, phosphate, chromate, molybdate, and benzoate as a main component is interposed between the heat exchangers. 2 A spiral passage is provided between the inner tube and the outer tube,
The heat exchanger according to claim 1, characterized in that this passage is provided with an anticorrosive substance.
JP12104680U 1980-08-25 1980-08-25 Heat exchanger Expired JPS605277Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12104680U JPS605277Y2 (en) 1980-08-25 1980-08-25 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12104680U JPS605277Y2 (en) 1980-08-25 1980-08-25 Heat exchanger

Publications (2)

Publication Number Publication Date
JPS5746295U JPS5746295U (en) 1982-03-15
JPS605277Y2 true JPS605277Y2 (en) 1985-02-18

Family

ID=29481725

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12104680U Expired JPS605277Y2 (en) 1980-08-25 1980-08-25 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS605277Y2 (en)

Also Published As

Publication number Publication date
JPS5746295U (en) 1982-03-15

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