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JPH0456239B2 - - Google Patents
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JPH0456239B2 - - Google Patents

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Publication number
JPH0456239B2
JPH0456239B2 JP62173779A JP17377987A JPH0456239B2 JP H0456239 B2 JPH0456239 B2 JP H0456239B2 JP 62173779 A JP62173779 A JP 62173779A JP 17377987 A JP17377987 A JP 17377987A JP H0456239 B2 JPH0456239 B2 JP H0456239B2
Authority
JP
Japan
Prior art keywords
condensate
electrode
heat transfer
condensation
condensate discharge
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
JP62173779A
Other languages
Japanese (ja)
Other versions
JPS6419296A (en
Inventor
Akira Yabe
Yutaka Watanabe
Yoshifumi Nakahama
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP17377987A priority Critical patent/JPS6419296A/en
Publication of JPS6419296A publication Critical patent/JPS6419296A/en
Publication of JPH0456239B2 publication Critical patent/JPH0456239B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) この発明は、例えば冷却器等に使用される凝縮
管の外周に生成する凝縮液膜を電気的に取除いて
凝縮熱伝達率を向上するようにした凝縮熱伝達促
進装置に関する。
Detailed Description of the Invention [Objective of the Invention] (Industrial Application Field) This invention electrically removes a condensate film that forms on the outer periphery of a condensing tube used in a cooler, etc. to remove condensation heat. The present invention relates to a condensing heat transfer promoting device that improves the transfer rate.

(従来の技術) 熱交換器の凝縮管の周囲に電極を対峙しこの電
極と凝縮管の相互間に高電圧を印加することによ
り電気流体力学(EHD)的に熱交換時に凝縮管
の表面に生成する凝縮液膜を電極の側へ導き、凝
縮面の液膜を取除いて熱交換器の効率を向上しよ
うとする技術が既に提案されている(例えば、特
開昭56−42096号公報、特公昭59−41117〜8号公
報)。
(Prior art) Electrodes are placed around the condensing tube of a heat exchanger, and a high voltage is applied between the electrode and the condensing tube. Techniques have already been proposed that attempt to improve the efficiency of heat exchangers by guiding the generated condensate film to the electrode side and removing the liquid film on the condensing surface (for example, Japanese Patent Application Laid-Open No. 1983-42096, Special Publication No. 59-41117-8).

この技術においては、凝縮面と電極の間に一定
の間隙が形成されるようにこれらを離間して保持
し、さらに凝縮面が電極によつて被覆される面積
をできるだけ小さくする必要があり、このため電
極には線状のものが一般に用いられている。ま
た、電極に吸引付着した凝縮液は凝縮面から次々
に離脱させて排除しないと凝縮時の熱伝達率を向
上する上で好ましくないが、このため通常は上記
線状の電極を凝縮管の表面から離間させた状態で
らせん状にそのらせん角度が下方へ至るほど大き
くなるように巻回し、凝縮液に作用する重力によ
る落下速度を利用して遠心力を発生させ、この遠
心力によつて凝縮液を外方へ排出するようにして
いる。
In this technique, it is necessary to keep the condensing surface and the electrodes apart so that a certain gap is formed between them, and furthermore, it is necessary to minimize the area of the condensing surface covered by the electrodes. Therefore, wire-shaped electrodes are generally used. In addition, the condensate that has attracted and adhered to the electrode must be removed from the condensation surface one after another, otherwise it is not desirable to improve the heat transfer coefficient during condensation. The condensate is wound in a spiral so that the helical angle increases as it goes downwards, and centrifugal force is generated by using the falling speed of gravity acting on the condensate, and this centrifugal force causes condensation. The liquid is drained outward.

(発明が解決しようとする問題点) 上記のように電極を不等ピツチのらせん状に巻
回して凝縮液を排出するようにするには、凝縮管
の下方でらせん角度を45°程度にする必要があり、
このようにらせん角度を大きくすると凝縮面積に
対する電極の密度が小さくなつてしまい充分な凝
縮排除を行なうことができない。また、凝縮液の
量が多くなると電極に沿つて流れる凝縮液速度が
速くなつて外方へ飛散してしまい、隣接する他の
凝縮管に流出液が付着して全体の熱伝達率が低下
してしまうという不都合があつた。
(Problem to be Solved by the Invention) In order to discharge the condensate by winding the electrode in a spiral with unequal pitches as described above, the helical angle should be approximately 45° below the condensing tube. There is a need,
When the helical angle is increased in this manner, the density of the electrode relative to the condensation area becomes small, making it impossible to remove condensation sufficiently. In addition, when the amount of condensate increases, the velocity of the condensate flowing along the electrode increases and it scatters outward, causing the effluent to adhere to other adjacent condensate tubes and reducing the overall heat transfer coefficient. I had the inconvenience of having to do this.

本発明は、凝縮面積に対する電極の密度を増加
し、さらに凝縮液を円滑に排出することのできる
凝縮伝達促進装置を得ることを目的としている。
An object of the present invention is to obtain a condensation transfer promoting device that can increase the density of electrodes relative to the condensation area and can also smoothly discharge condensate.

〔発明の構成〕[Structure of the invention]

(問題点を解決するための手段) 本発明に係る凝縮熱伝達促進装置は、上述した
目的を達成するために、ほぼ鉛直な凝縮管の外周
にその軸線に対し一定角度で傾斜するように対峙
されるリング状の電極を多段に配設し、これら各
電極の軸方向最下方に位置する部位に外方に突出
する毛細管現象を利用した凝縮排出部を設けたも
のである。
(Means for Solving the Problems) In order to achieve the above-mentioned object, the condensing heat transfer promoting device according to the present invention is provided with a condensing tube arranged on the outer periphery of a substantially vertical condensing tube so as to be inclined at a constant angle with respect to its axis. In this system, ring-shaped electrodes are arranged in multiple stages, and a condensation discharge part that protrudes outward and utilizes capillary phenomenon is provided at the lowest position in the axial direction of each of these electrodes.

凝縮液排出部は凝縮液を例えば毛細管現象によ
つて電極から円滑に流出できるようにし、さらに
この凝縮液排出部先端が懸架される凝縮液導出幹
路が付加される。
The condensate discharge part allows the condensate to flow out smoothly from the electrode by, for example, capillary action, and is further provided with a condensate lead-out main path on which the tip of the condensate discharge part is suspended.

(作用) 上記の構成において、ガス凝結時に凝縮管1と
電極2の間に高電圧が印加されると凝縮管の表面
で凝結して生じた凝縮液は電気流体力学的作用に
よつて電極に引き寄せられて電極との間を架流
し、傾斜したリング状の電極を伝わつて軸方向最
下方に位置する凝縮液排出部に流れる。しかして
凝縮液はこの凝縮液排出部から凝縮液導出幹路に
流れ下方へ自然流下することとなる。
(Function) In the above configuration, when a high voltage is applied between the condensation tube 1 and the electrode 2 during gas condensation, the condensate that condenses on the surface of the condensation tube is transferred to the electrode by electrohydrodynamic action. The liquid is attracted to flow between the electrodes, passes through the slanted ring-shaped electrode, and flows to the condensate discharge section located at the lowest position in the axial direction. Therefore, the condensate flows from the condensate discharge part to the condensate outlet main path and naturally flows downward.

(実施例) 第1図および第2図は本発明の一実施例を示す
もので、内部を冷媒が流れるようになされた凝縮
管1の外周にはその軸に対し一定角度で傾斜する
ようリング状の電極2が凝縮管1に対峙した状態
でスペーサ3によつて凝縮管1から離間して配置
された支持棒4に取着されて多段に配設されてい
る。電極2は第2図に示すように全体が長楕円形
の帯状もしくは線状であつて、その長軸方向一端
には凝縮液排出部5が形成され、凝縮管1の外周
に配設されたときに各部が凝縮管1の表面から等
距離に位置し、かつそのとき軸方向の最下方に凝
縮液排出部5が位置するように構成されている。
(Embodiment) Figures 1 and 2 show an embodiment of the present invention, in which a ring is attached to the outer periphery of the condensing pipe 1, through which a refrigerant flows, so as to be inclined at a constant angle with respect to its axis. The shaped electrodes 2 are attached to support rods 4 which are spaced apart from the condensation tube 1 by spacers 3 while facing the condensation tube 1, and are arranged in multiple stages. As shown in FIG. 2, the electrode 2 is entirely oblong in the form of a strip or a line, and a condensate discharge part 5 is formed at one end in the long axis direction, and is disposed around the outer periphery of the condensation tube 1. Each part is located at an equal distance from the surface of the condensing tube 1, and the condensate discharge part 5 is located at the lowest position in the axial direction.

上記凝縮液排出部5は第2図のようにリング状
の電極2を不連続にしてその端部が互いに平行と
なる直線部6を外方へ突出させて延設し、さらに
その先端を外側へ屈曲して開放部7を形成して構
成される。
As shown in FIG. 2, the condensate discharge part 5 is constructed by discontinuously discontinuing the ring-shaped electrode 2 and extending straight parts 6 whose ends are parallel to each other to protrude outward. The opening part 7 is formed by bending the opening part 7.

しかして、凝縮管1の外周に配設された各電極
2の凝縮液排出部5の先端を連ねる位置に、凝縮
管1と平行に断面コ字形状の凝縮液導出幹路8が
設けられており、各凝縮液排出部5の先端が凝縮
液導出幹路8の内側に懸架されるようになつてい
る。
Therefore, a condensate discharge main path 8 having a U-shaped cross section is provided parallel to the condensation tube 1 at a position connecting the tips of the condensate discharge portions 5 of each electrode 2 disposed on the outer periphery of the condensation tube 1. The tip of each condensate discharge part 5 is suspended inside the condensate discharge main path 8.

上記の構成において、ガス凝結時に凝縮管1と
電極2の間に高電圧が印加されると凝縮管1の表
面で凝結して生じた凝縮液9は、第3図に示すよ
うに電気流体力学的作用によつて電極2に引き寄
せられて電極2との間を架流し、リング状の電極
2を伝わつて軸方向最下方に位置する凝縮液排出
部5に流れる。しかしてこの凝縮液排出部5にお
いて凝縮液9は平行に形成された直線部6の間隙
を通つてさらにその先端の開放部7から凝縮液導
出幹路8へ移り、下方へ自然流下することとな
る。
In the above configuration, when a high voltage is applied between the condensing tube 1 and the electrode 2 during gas condensation, the condensate 9 condensed on the surface of the condensing tube 1 is electrohydrodynamically generated as shown in FIG. The liquid is attracted to the electrode 2 by the mechanical action, flows across the electrode 2, and flows through the ring-shaped electrode 2 to the condensate discharge part 5 located at the lowest position in the axial direction. However, in the condensate discharge part 5 of the lever, the condensate 9 passes through the gap in the straight line part 6 formed in parallel, and further moves from the open part 7 at the tip to the condensate discharge main path 8, and naturally flows downward. Become.

このように凝縮液排出部5に平行な直線部6を
形成してその間隙を凝縮液9が流れるようにすれ
ば、電極2に引き寄せられた多量の凝縮液は上記
間隙を毛細管現象によつて円滑にしかも静的に流
れるので高都合である。
By forming the straight line part 6 parallel to the condensate discharge part 5 and allowing the condensate 9 to flow through the gap, a large amount of condensate drawn to the electrode 2 flows through the gap by capillary action. It is highly convenient because it flows smoothly and statically.

また、上記のように各電極ことに凝縮液排出部
を設けるようにすることで、電極を配設する間隔
を小さくすることができ、この結果凝縮液の排除
が円滑になつて凝縮管表面に形成される液膜が薄
くなり、凝縮熱伝達率を向上することができる。
In addition, by providing a condensate discharge part for each electrode as described above, it is possible to reduce the spacing between the electrodes, and as a result, the condensate can be smoothly discharged and the surface of the condenser tube can be removed. The formed liquid film becomes thinner, and the condensation heat transfer coefficient can be improved.

第4図および第5図は他の実施例を示すもの
で、上記で説明した構成と異なる点は凝縮液排出
部を芯状体10で構成した点てある。すなわち本
実施例においては、凝縮液排出部11は電極2の
軸方向最下方の位置に金網あるいはその他の繊維
を束ねて形成した芯状体10を取着して構成され
ている。この際、芯状体10が取着される電極2
の該当部位にも金網12等を巻回しておくことが
望ましい。
FIGS. 4 and 5 show another embodiment, which differs from the configuration described above in that the condensate discharge section is constructed of a core-shaped body 10. That is, in this embodiment, the condensate discharge part 11 is constructed by attaching a core body 10 formed by bundling wire mesh or other fibers to the lowermost position in the axial direction of the electrode 2. At this time, the electrode 2 to which the core body 10 is attached
It is desirable to wrap a wire mesh 12 or the like around the corresponding part.

かかる構成によれば、凝縮液を芯状体10から
凝縮液導出幹路8へ芯状体1010による毛細血
管現象を利用して円滑にかつ静的に流すことがで
きる。
According to this configuration, the condensate can flow smoothly and statically from the core body 10 to the condensate lead-out trunk path 8 by utilizing the capillary phenomenon caused by the core body 1010.

なお、上記の説明において凝縮液導出幹路8は
断面コ字状のものを例にしたが、これに限らず円
柱状のものや棒状のものであつても、もちろん差
支えない。
In the above description, the condensate outlet main path 8 is exemplified as having a U-shaped cross section, but is not limited to this, and may of course be cylindrical or rod-shaped.

〔発明の効果〕〔Effect of the invention〕

以上に述べたように本発明に係る凝縮熱伝達促
進装置においては、ほぼ鉛直な凝縮管の外周にそ
の軸線に対し一定角度で傾斜するように対峙され
るリング状の電極を多段に配設し、これら各電極
の軸方向最下方に位置する部位に外方に突出する
毛細管現象を利用した凝縮液排出部を設けたか
ら、リング状電極を凝縮管の周りに高密度に配置
でき、しかも、凝縮管の凝縮面に生成された凝縮
液を、リング状電極の電圧印加による電気流体力
学的な吸引作用と、各リング状電極の傾斜に起因
する重力による液流下作用と、各リング状電極の
最下方位置に設けられた外部に突出する凝縮液排
出部の毛細管作用との相乗的作用により、凝縮管
の凝縮面に生成された凝縮液を、凝縮面より積極
的に吸引して引き剥し、各リング状電極の傾斜に
沿つて静的に案内し、凝縮液排出部の毛細管作用
により円滑に流下させることができ、下方の電極
に飛散したり、案内されて悪影響を与えることも
ないので、凝縮面からの凝縮液の排除が円滑かつ
スムーズになり、凝縮管の表面に形成される液膜
が薄くなつて、常に高い凝縮熱伝達効率を確保す
ることができる。
As described above, in the condensing heat transfer promoting device according to the present invention, ring-shaped electrodes are disposed in multiple stages around the outer periphery of the almost vertical condensing tube so as to be inclined at a constant angle with respect to the axis of the condensing tube. Since a condensate discharge part utilizing capillary phenomenon that protrudes outward is provided at the lowest position in the axial direction of each of these electrodes, it is possible to arrange ring-shaped electrodes in a high density around the condensation tube, and to prevent condensation. The condensate generated on the condensation surface of the tube is absorbed by an electrohydrodynamic suction effect due to the voltage applied to the ring electrodes, a liquid flowing down effect due to gravity due to the inclination of each ring electrode, and the bottom of each ring electrode. Due to the synergistic effect with the capillary action of the condensate discharge part protruding to the outside provided at the lower position, the condensate generated on the condensation surface of the condensation tube is actively sucked and pulled off from the condensation surface, and each The condensate is guided statically along the inclination of the ring-shaped electrode, allowing the condensate to flow down smoothly due to the capillary action of the condensate discharge part, and the condensate does not scatter to the electrode below or be guided and have an adverse effect. The removal of condensed liquid from the surface becomes smooth and smooth, and the liquid film formed on the surface of the condensing tube becomes thinner, so that high condensing heat transfer efficiency can be ensured at all times.

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

第1図は本発明の一実施例に係る凝縮熱伝達促
進装置の要部を示す斜視図、第2図は電極を示す
斜視図、第3図は凝縮液が流れる様子を示す説明
図、第4図は本発明の他の実施例を示す側面図、
第5図は第4図に示した電極の斜視図である。 1……凝縮管、2……電極、3……スペーサ、
4……支持棒、5……凝縮液排出部、6……直線
部、7……開放部、8……凝縮液導出幹路、10
……芯状体。
FIG. 1 is a perspective view showing the main parts of a condensation heat transfer promoting device according to an embodiment of the present invention, FIG. 2 is a perspective view showing electrodes, FIG. 3 is an explanatory view showing how condensate flows, and FIG. 4 is a side view showing another embodiment of the present invention,
FIG. 5 is a perspective view of the electrode shown in FIG. 4. 1... Condensing tube, 2... Electrode, 3... Spacer,
4... Support rod, 5... Condensate discharge part, 6... Straight part, 7... Open part, 8... Condensate lead-out main path, 10
...core body.

Claims (1)

【特許請求の範囲】 1 ほぼ鉛直な凝縮管の外周にその軸線に対し一
定角度で傾斜するように対峙されるリング状の電
極を多段に配設し、これら各電極の軸方向最下方
に位置する部位に外方に突出する毛細管現象を利
用した凝縮液排出部を設けてなることを特徴とす
る凝縮熱伝達促進装置。 2 凝縮液排出部は電極を不連続にしてその両端
部間に間〓を形成して構成される特許請求の範囲
第1項に記載の凝縮熱伝達促進装置。 3 凝縮液排出部は電極の両端部に互いに平行で
外方に突出した直線部を延設し、この直線部間に
間〓を形成して構成される特許請求の範囲第2項
に記載の凝縮熱伝達促進装置。 4 凝縮液排出部は電極に外方に突出するように
取着された芯状体で構成される特許請求の範囲第
1項に記載の凝縮熱伝達促進装置。 5 各電極の凝縮液排出部先端が懸架される凝縮
液導出幹路を備えた特許請求の範囲第2項に記載
の凝縮熱伝達促進装置。
[Claims] 1. Ring-shaped electrodes facing each other at a constant angle with respect to the axis are arranged in multiple stages on the outer periphery of a substantially vertical condensation pipe, and are located at the lowest position in the axial direction of each of these electrodes. 1. A condensation heat transfer promoting device, comprising: a condensate discharge section protruding outward that utilizes capillary phenomenon. 2. The condensation heat transfer promoting device according to claim 1, wherein the condensate discharge section is constructed by discontinuing the electrodes and forming a gap between both ends of the electrodes. 3. The condensate discharge part is configured by extending parallel straight parts extending outward from both ends of the electrode, and forming a gap between the straight parts. Condensation heat transfer accelerator. 4. The condensation heat transfer promoting device according to claim 1, wherein the condensate discharge part is constituted by a core body attached to the electrode so as to protrude outward. 5. The condensation heat transfer promoting device according to claim 2, comprising a condensate lead-out main path in which the tip of the condensate discharge part of each electrode is suspended.
JP17377987A 1987-07-14 1987-07-14 Condensation heat transfer promoting device Granted JPS6419296A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17377987A JPS6419296A (en) 1987-07-14 1987-07-14 Condensation heat transfer promoting device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17377987A JPS6419296A (en) 1987-07-14 1987-07-14 Condensation heat transfer promoting device

Publications (2)

Publication Number Publication Date
JPS6419296A JPS6419296A (en) 1989-01-23
JPH0456239B2 true JPH0456239B2 (en) 1992-09-07

Family

ID=15966993

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17377987A Granted JPS6419296A (en) 1987-07-14 1987-07-14 Condensation heat transfer promoting device

Country Status (1)

Country Link
JP (1) JPS6419296A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02136698A (en) * 1988-11-18 1990-05-25 Agency Of Ind Science & Technol Heat transfer promoting device in convection heat transfer surface
CN102698448A (en) * 2012-05-25 2012-10-03 南京威尔化工有限公司 Climbing film evaporator

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS595837B2 (en) * 1979-09-13 1984-02-07 工業技術院長 Method for promoting condensation heat transfer using electric field
DE3121838C2 (en) * 1981-06-02 1983-07-14 Kunststofftechnik KG, 5210 Troisdorf Plastic heat exchanger and process for its manufacture
JPS60138171U (en) * 1984-02-23 1985-09-12 三菱重工業株式会社 Condenser
JPS6139276U (en) * 1984-08-07 1986-03-12 三菱重工業株式会社 Condenser

Also Published As

Publication number Publication date
JPS6419296A (en) 1989-01-23

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