JPH02197793A - Horizontal evaporating tube for heat exchanger - Google Patents
Horizontal evaporating tube for heat exchangerInfo
- Publication number
- JPH02197793A JPH02197793A JP28669289A JP28669289A JPH02197793A JP H02197793 A JPH02197793 A JP H02197793A JP 28669289 A JP28669289 A JP 28669289A JP 28669289 A JP28669289 A JP 28669289A JP H02197793 A JPH02197793 A JP H02197793A
- Authority
- JP
- Japan
- Prior art keywords
- tube
- cylindrical body
- evaporating
- horizontal
- heat transfer
- 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
Links
- 238000001704 evaporation Methods 0.000 title claims abstract description 39
- 230000008020 evaporation Effects 0.000 claims description 31
- 239000012530 fluid Substances 0.000 claims description 22
- 239000000428 dust Substances 0.000 abstract description 9
- 239000007788 liquid Substances 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 230000000694 effects Effects 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はヒートパイプの原理を応用した熱交換器の水平
蒸発管の改良に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an improvement of a horizontal evaporation tube of a heat exchanger applying the principle of a heat pipe.
ヒートパイプとは排気した密閉管内に作動液を封入し、
その一端を加熱して作動液を蒸発させ、他端で凝縮させ
て熱を放出させるもので、優れた熱伝達特性を有し、超
然伝導体とも呼ばれている。A heat pipe is a sealed tube that is evacuated and filled with working fluid.
It heats one end to evaporate the working fluid, and condenses it at the other end to release heat.It has excellent heat transfer properties and is also called a transcendental conductor.
この原理を応用し、蒸発管と凝縮管を蒸気管と凝縮液管
で連結することにより閉回路を形成し、内部を排気して
作動液を封入した熱交換器が開発され、排熱回収を始め
種々の用途に用いられている。Applying this principle, a heat exchanger has been developed in which a closed circuit is formed by connecting the evaporation tube and the condensation tube with a steam tube and a condensate tube, the inside is evacuated, and the working fluid is sealed. It has been used for various purposes.
このような熱交換器の交換熱量には蒸発管内の熱伝達率
の占める割合が大きく、特に蒸発を伴う管内には気相部
と液相部を形成し、気相部での熱伝達率が非常に低℃・
ところから蒸発管を垂直に設置して環状流を形成するこ
とにより熱伝達率の向上を計っている。しかしながら蒸
発管の長さに比べて環状流の有効長さが短いため、熱伝
達率はそれほど高くはならない。また加熱に排ガスのよ
うなダストを含む熱源を用いると、蒸発管の外表面にダ
ストが付着し、管外面の熱伝達率を低下する。The heat transfer coefficient in the evaporation tube accounts for a large proportion of the amount of heat exchanged in such a heat exchanger.In particular, in the tube that involves evaporation, a gas phase and a liquid phase are formed, and the heat transfer coefficient in the gas phase is Very low ℃・
Therefore, the evaporator tubes are installed vertically to form an annular flow in order to improve the heat transfer coefficient. However, since the effective length of the annular flow is short compared to the length of the evaporator tube, the heat transfer coefficient is not very high. Furthermore, when a heat source containing dust such as exhaust gas is used for heating, the dust adheres to the outer surface of the evaporation tube, reducing the heat transfer coefficient on the outer surface of the tube.
従ってこれを除去する必要があるが、管外面には伝熱面
積を拡大するためフィンが設けられており、ダストの除
去は極めて困難であった。Therefore, it is necessary to remove this dust, but since fins are provided on the outer surface of the tube to increase the heat transfer area, it has been extremely difficult to remove the dust.
本発明者等はこれに鑑み種々検討の結果、先にダスト対
策が容易で、高い管内熱伝達率が得られる熱交換器を開
発し、特願昭59−43532号及び特願昭59−45
150号として、提案した。In view of this, as a result of various studies, the inventors of the present invention first developed a heat exchanger that could easily take measures against dust and obtain a high heat transfer coefficient in the pipes.
I proposed it as No. 150.
この熱交換器は大略第2図に示すように蒸発管(1)を
水平に配設し、凝縮管(2)と蒸発管fl)を蒸気管(
3)と凝縮液管(4)により連結し、内部を排気して作
動液(5)を封入すると共に、蒸発管(1)内に一定量
の作動液(5)を保持できるようにしたものである。こ
の熱交換器によれば蒸発管+1)の外面に付着したダス
トを水洗又は/及びショットクリーニングシステムによ
り容易に除去することができる。As roughly shown in Figure 2, this heat exchanger has an evaporator tube (1) arranged horizontally, and a condensing tube (2) and an evaporator tube fl) connected to a steam tube (
3) is connected to the condensate pipe (4), the inside is evacuated and the working fluid (5) is sealed, and a certain amount of the working fluid (5) can be held in the evaporation pipe (1). It is. According to this heat exchanger, dust adhering to the outer surface of the evaporator tube +1) can be easily removed by water washing and/or a shot cleaning system.
水平蒸発管を用いた上記熱交換器は、ダストの除去が容
易なばかりか、垂直蒸発管を用いた熱交換器とほぼ同等
以上の熱伝達率が得られるも、それほど高い熱伝達率で
はなく、−層の改善が望まれている。The above heat exchanger using horizontal evaporator tubes not only makes it easy to remove dust, but also provides a heat transfer coefficient that is almost equal to or higher than that of the heat exchanger using vertical evaporator tubes, but the heat transfer coefficient is not as high. , - layer improvement is desired.
また高い熱伝達率を得るため、蒸発管の内部に断面鼓状
の管状体を装着したもの(実公昭49−6746号)も
提案されているが、管状体の製作及び蒸発管への装着が
困難であり、蒸気の流通抵抗も大きい等の問題がある。In addition, in order to obtain a high heat transfer coefficient, it has been proposed that a tubular body with a drum-shaped cross section is attached inside the evaporation tube (Utility Model Publication No. 49-6746), but it is difficult to manufacture the tubular body and attach it to the evaporation tube. This is difficult, and there are problems such as high steam flow resistance.
本発明者等は、前述の問題点について更に検討を重ねた
結果、製作が容易で高い熱伝達率が得られる水平蒸発管
を開発したもので、熱交換器の蒸発部に水平に取付け、
内部の作動液を外部より加熱して蒸発させる蒸発管にお
いて、該管内に下部は肢管と密着し、上部は上方に向っ
て肢管の内壁との間に細隙が漸増し、上部軸方向に連続
又は不連続のスリット状の蒸気流通口を形成した薄肉円
筒体を挿入したことを特徴とするものである。As a result of further investigation into the above-mentioned problems, the present inventors have developed a horizontal evaporation tube that is easy to manufacture and provides a high heat transfer coefficient.
In an evaporation tube that heats and evaporates the internal working fluid from the outside, the lower part of the tube is in close contact with the limb canal, and the upper part gradually increases in the upward direction between the inner wall of the limb pipe and the upper axial direction. A thin cylindrical body having continuous or discontinuous slit-shaped vapor flow ports is inserted into the cylindrical body.
即ち本発明は、第1図(イ)、(ロ)に示すように水平
に取付ける蒸発管(1)内に、肢管(1)の内径より幾
分細径の薄肉円筒体(6)であって、下部が肢管と密着
し、上部が上方に向って肢管(1)の内壁との間に細隙
(7)が漸増するように、且つ薄肉円筒体(6)の上部
が軸方向に円筒体(6)の端から端まで連続するスリッ
ト状蒸気流通口(8)を形成した1本の薄肉円筒体(6
)を挿入したものである。この場合薄肉円筒体(6)の
内側下部α1と薄肉円筒体(6)の外側下部αυが作動
液の溜り部で流通口となる。なお上記は薄肉円筒体(6
)の上部軸方向に円筒体(6)の端から端まで連続する
スリット状蒸気流通口(8)を設けた例について説明し
たがこれに限るものではな(、例えば不連続スリット状
、穴状の蒸気流通口を設けてもよい。That is, the present invention has a thin cylindrical body (6) with a diameter somewhat smaller than the inner diameter of the limb tube (1), which is installed in the evaporation tube (1) installed horizontally as shown in FIGS. The upper part of the thin-walled cylindrical body (6) is arranged so that the lower part is in close contact with the limb canal, and the upper part is arranged so that a slit (7) gradually increases between the upper part and the inner wall of the limb canal (1). One thin-walled cylindrical body (6
) is inserted. In this case, the inner lower part α1 of the thin-walled cylindrical body (6) and the outer lower part αυ of the thin-walled cylindrical body (6) serve as reservoirs of hydraulic fluid and flow ports. The above is a thin cylindrical body (6
), the slit-shaped vapor flow port (8) is provided continuously from one end of the cylinder (6) to the other in the upper axial direction, but the invention is not limited to this. A steam vent may be provided.
以上は蒸発管が比較的短尺の場合である。更に蒸発管が
長尺の場合は、作動液が円筒体(6)の内側下部α〔か
ら外側下部aυに流れやすくするため円筒体(6)の下
部作動液溜り部軸方向に、複数個の穴(図示せず)を設
けて作動液流通口としてもよい。なお図において(9)
は管外面に伝熱面積の拡大のために設けたフィンを示す
。The above is a case where the evaporation tube is relatively short. Furthermore, if the evaporation tube is long, a plurality of hydraulic fluid reservoirs are installed in the axial direction of the lower hydraulic fluid reservoir of the cylindrical body (6) in order to facilitate the flow of the working fluid from the inner lower part α [to the outer lower aυ] of the cylindrical body (6). A hole (not shown) may be provided to serve as a hydraulic fluid flow port. In addition, in the figure (9)
indicates the fins provided on the outer surface of the tube to increase the heat transfer area.
水平蒸発管(1)内に幾分細径の薄肉円筒体(6)を挿
入して、該蒸発管内壁と薄肉円筒体外壁間に上方に向っ
て漸増するような細隙(7)を形成することにより、作
動液の表面張力によって00部の作動液が上部へ押し上
げられ、蒸発管内壁と円筒体外壁との接触面積を増大さ
せ、また細隙は上方に向って漸増するようになっている
ため、発生した気泡、蒸気は、更に加熱されながら、抵
抗な(上部へ押し上げられるため高い熱伝達率が得られ
るもので、細隙は小さいほど有効である。また水平蒸発
管が短い場合は、円筒体(6)内側θGの作動液は、円
筒体(6)の両端開口部から円筒体(6)の外側の液溜
り部aυに供給することができるが、水平蒸発管が長い
場合には、薄肉円筒体の内部11から外部θυへの作動
液の供給が不十分となり、ドライアウトの原因となる。A thin-walled cylindrical body (6) with a somewhat small diameter is inserted into the horizontal evaporation tube (1) to form a slit (7) that gradually increases upward between the inner wall of the evaporation tube and the outer wall of the thin-walled cylinder. As a result, 00 parts of the working fluid is pushed upward by the surface tension of the working fluid, increasing the contact area between the inner wall of the evaporator tube and the outer wall of the cylindrical body, and the slit gradually increases upward. As the bubbles and steam generated are further heated, they are pushed upwards, resulting in a high heat transfer coefficient, and the smaller the slit, the more effective it is.Also, if the horizontal evaporation tube is short, , the working fluid inside the cylinder (6) θG can be supplied from the openings at both ends of the cylinder (6) to the liquid reservoir aυ outside the cylinder (6), but if the horizontal evaporation pipe is long, In this case, the supply of working fluid from the inside 11 of the thin-walled cylinder to the outside θυ becomes insufficient, causing dryout.
この場合は適宜薄肉円筒体の下部作動液溜り部軸方向に
複数個の穴を設けて作動液流通口として、作動液の供給
が十分に行われるようにする。In this case, a plurality of holes are appropriately provided in the axial direction of the lower hydraulic fluid reservoir of the thin-walled cylindrical body to serve as hydraulic fluid flow ports to ensure a sufficient supply of hydraulic fluid.
外径60.5朋、肉厚1.5朋、内径57.5順、長さ
132C1+xのステンレス鋼管の外周に高さ12,7
朋、ピッチ4.5朋のラジアルフィンを取付けた水平蒸
発管と、フィン光径27,113+m、フィン外径51
.25111のフィンチューブからなる凝縮管を用い、
第2図に示す熱サイクルを形成し、水平蒸発管内に第1
図(イ)、(ロ)に示すように、外径45朋、52y1
m、 57IIIm、長さ1000+nm、肉厚1.2
mmのステンレス鋼管の各々の上部軸方向に全長にわた
ってそれぞれ幅15+++mS20mm、30m111
,40朋のスリット状蒸気流通口を形成した円筒体を蒸
発管内に挿入し、管内蒸発熱伝達率を測定し、蒸発管内
に円筒体を挿入しない場合と比較した。A stainless steel tube with an outer diameter of 60.5 mm, a wall thickness of 1.5 mm, an inner diameter of 57.5 mm, and a length of 132C1+x has a height of 12.7 mm on the outer periphery.
Tomo, horizontal evaporation tube with radial fins of pitch 4.5, fin light diameter 27,113+m, fin outer diameter 51
.. Using a condensing tube made of 25111 fin tube,
The thermal cycle shown in Figure 2 is formed, and the first
As shown in figures (a) and (b), the outer diameter is 45mm, 52y1
m, 57IIIm, length 1000+nm, wall thickness 1.2
Width 15+++mS20mm, 30m111 over the entire length in the upper axial direction of each of the stainless steel tubes of mm
A cylindrical body with a slit-shaped vapor flow opening of 40 mm was inserted into the evaporation tube, and the evaporative heat transfer coefficient within the tube was measured and compared with a case in which the cylindrical body was not inserted into the evaporation tube.
その結果a内蒸発熱伝達率は円筒体を挿入しない場合1
500−3000 Kcal /mh″Cであったが、
円筒体を挿入すると4000〜7000Kcal/ih
’c に向上した。また管内蒸発熱伝達率は挿入した
円筒体の外径増大と共に向上し、またスリット幅も狭い
ほど向上し、スリット幅15〜20mm、円筒体の外径
52〜57朋で最も高い管内熱伝達率が得られた。As a result, the evaporative heat transfer coefficient in a is 1 when no cylindrical body is inserted.
500-3000 Kcal/mh″C,
When inserting the cylindrical body, 4000-7000Kcal/ih
improved to 'c. In addition, the evaporative heat transfer coefficient within the tube increases as the outer diameter of the inserted cylinder increases, and the narrower the slit width, the higher the evaporative heat transfer coefficient becomes. was gotten.
本発明によれば外表面に付着するダストの除去が容易で
あり、蒸発管内部に挿入する薄肉円筒体の製作及び蒸発
管内への挿着が容易であり、且つ管内蒸発熱伝達率を著
しく向上1−て、熱交換器の性能を高めろことができる
顕著な効果を奏するものである。According to the present invention, it is easy to remove dust adhering to the outer surface, it is easy to manufacture a thin-walled cylindrical body to be inserted into the evaporation tube, and it is easy to insert it into the evaporation tube, and the evaporation heat transfer coefficient inside the tube is significantly improved. 1- It has a remarkable effect of improving the performance of the heat exchanger.
第1図(イ)、(ロ)は本発明水平蒸発管の一例を示す
もので、(イ)は側断面図、(olは(イ)のA−A断
面図、第2図は、水平蒸発管を用いた熱交換器の一例を
示す概念図である。
1・・・水平蒸発管、2・・・凝縮管、3・・蒸気管、
4・・・凝縮液管、5・・・作動液、6・・薄肉円筒体
、7・・・細隙、8・・・蒸気流通口、9・・・フィン
、1.0、II・作動液溜り部、流通部。
特許出願人 古河電気工業株式会社Figures 1 (A) and (B) show an example of the horizontal evaporation tube of the present invention, where (A) is a side sectional view, (ol is a sectional view taken along line A-A of (A), and Figure 2 is a horizontal evaporation tube). It is a conceptual diagram showing an example of a heat exchanger using evaporation tubes. 1... Horizontal evaporation tube, 2... Condensing tube, 3... Steam tube,
4... Condensate pipe, 5... Working fluid, 6... Thin cylindrical body, 7... Slit, 8... Steam flow port, 9... Fin, 1.0, II. Operation Liquid reservoir section, distribution section. Patent applicant Furukawa Electric Co., Ltd.
Claims (2)
を外部より加熱して蒸発させる蒸発管において、該管内
に下部は該管と密着し、上部は上方に向つて該管の内壁
との間に細隙が漸増し、上部軸方向に連続又は不連続の
スリット状の蒸気流通口を形成した1本の薄肉円筒体を
挿入したことを特徴とする熱交換器用水平蒸発管。(1) An evaporation tube that is installed horizontally in the evaporation section of a heat exchanger and heats the internal working fluid from the outside to evaporate it. 1. A horizontal evaporation tube for a heat exchanger, characterized in that a single thin-walled cylindrical body is inserted into which a slit gradually increases between the inner wall and a continuous or discontinuous slit-shaped vapor flow port is formed in the upper axial direction.
個の穴を設けて作動液流通口とした特許請求の範囲第1
項記載の熱交換器用水平蒸発管。(2) A plurality of holes are provided in the axial direction of the hydraulic fluid reservoir in the lower part of the thin-walled cylindrical body to form a hydraulic fluid flow port.Claim 1
Horizontal evaporation tube for heat exchanger as described in Section 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28669289A JPH02197793A (en) | 1989-11-02 | 1989-11-02 | Horizontal evaporating tube for heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28669289A JPH02197793A (en) | 1989-11-02 | 1989-11-02 | Horizontal evaporating tube for heat exchanger |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12015884A Division JPS60263096A (en) | 1984-03-07 | 1984-06-12 | Horizontal evaporating tube for heat exchanger |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02197793A true JPH02197793A (en) | 1990-08-06 |
JPH048715B2 JPH048715B2 (en) | 1992-02-17 |
Family
ID=17707742
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP28669289A Granted JPH02197793A (en) | 1989-11-02 | 1989-11-02 | Horizontal evaporating tube for heat exchanger |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02197793A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020017414A1 (en) * | 2018-07-18 | 2020-01-23 | 株式会社デンソー | Thermosiphon heat exchange device |
-
1989
- 1989-11-02 JP JP28669289A patent/JPH02197793A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020017414A1 (en) * | 2018-07-18 | 2020-01-23 | 株式会社デンソー | Thermosiphon heat exchange device |
JP2020012588A (en) * | 2018-07-18 | 2020-01-23 | 株式会社デンソー | Thermosiphon type heat exchange device |
Also Published As
Publication number | Publication date |
---|---|
JPH048715B2 (en) | 1992-02-17 |
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