JPS61225590A - Heat transferring rate regulator utilizing electric field on high-performance boiling surface - Google Patents
Heat transferring rate regulator utilizing electric field on high-performance boiling surfaceInfo
- Publication number
- JPS61225590A JPS61225590A JP6742285A JP6742285A JPS61225590A JP S61225590 A JPS61225590 A JP S61225590A JP 6742285 A JP6742285 A JP 6742285A JP 6742285 A JP6742285 A JP 6742285A JP S61225590 A JPS61225590 A JP S61225590A
- Authority
- JP
- Japan
- Prior art keywords
- boiling surface
- electrode
- performance
- boiling
- electric field
- 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
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、高性能沸騰面の熱伝達量を電場を利用して調
整する装置に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to an apparatus for adjusting the amount of heat transfer of a high-performance boiling surface using an electric field.
(従来技術)
高性能沸騰面1は、第5図に示すように金属表面に機械
的加工を施したり、焼結金属の表面層を作るなどして多
数の凹凸2をその表面に形成し、場合によりトンネル3
を形成しである。(Prior art) As shown in FIG. 5, the high-performance boiling surface 1 is made by forming a large number of irregularities 2 on the surface by mechanically processing the metal surface or creating a surface layer of sintered metal. Tunnel 3 in some cases
It is formed.
高性能沸騰面1ではその表面の凹凸2の状態いかんによ
って、気泡4が発生する発泡点5と液体が矢印Mのよう
に高性能沸騰面1に対して自然に流下する部分の区別が
一定せず、設計上の困難性のあることが知られている。On the high performance boiling surface 1, depending on the condition of the surface irregularities 2, the distinction between the foaming point 5 where bubbles 4 are generated and the part where the liquid naturally flows down to the high performance boiling surface 1 as shown by arrow M is constant. However, it is known that there are design difficulties.
(発明が解決しようとする問題点)
熱交換器を製造する際に当該高性能沸騰面1の前記発泡
点5の数を予め予測することは困難である。そ−のため
、高性能沸騰面1の発泡点5の数およびそれに関連して
熱伝達量について製品ごとにばらつきがあった。(Problems to be Solved by the Invention) When manufacturing a heat exchanger, it is difficult to predict the number of foaming points 5 of the high performance boiling surface 1 in advance. Therefore, the number of foaming points 5 of the high-performance boiling surface 1 and the related amount of heat transfer varied from product to product.
本発明の目的は、高性能沸騰面において発泡点となる部
分と液体が高性能沸騰面に対して流下する部分とを人為
的に設定できるようにして高性能沸騰面の熱伝達量を促
進、あるいは調整畝設計を簡単化、容易化するための装
置を提供することにある。The purpose of the present invention is to promote the amount of heat transfer on the high-performance boiling surface by making it possible to artificially set the portion of the high-performance boiling surface that becomes the foaming point and the portion where the liquid flows down to the high-performance boiling surface. Another object of the present invention is to provide a device for simplifying and facilitating adjustment ridge design.
(問題点を解決するための手段)
上記目的を達成するため本発明は次のように構成されて
いる。(Means for Solving the Problems) In order to achieve the above object, the present invention is configured as follows.
多数の凹凸を表面に形成し沸騰を促進させる高性能沸騰
面にメツシュ電極を対向して設置し、前記高性能沸騰面
を一方の電極とし、かつメツシュ電極を他方の電極とし
、高性能沸騰面とメツシュ電極との間に高電圧をかける
ように構成されている。A mesh electrode is installed facing a high-performance boiling surface that forms many irregularities on the surface to promote boiling, and the high-performance boiling surface is used as one electrode, and the mesh electrode is used as the other electrode. It is configured to apply a high voltage between the mesh electrode and the mesh electrode.
(作用) 本発明は、次のように作用する。(effect) The invention works as follows.
メツシュ電極と高性能沸騰面の間に高電圧をかける。す
ると、電界のかかっているところでは、マックスウェル
応力で表現される静電気的な圧力がかかっているため、
その場の静圧は電場のかかっていないところよりも小さ
くなり、圧力が小さくなるために、気泡は高性能沸騰面
から強制的に離脱させられる。A high voltage is applied between the mesh electrode and the high performance boiling surface. Then, where an electric field is applied, an electrostatic pressure expressed by Maxwell stress is applied, so
The static pressure there is lower than that without an electric field, and because the pressure is lower, the bubbles are forced to leave the high-performance boiling surface.
つまり、メツシュ電極の細線の下方では電場の働きによ
って気泡が強制離脱され発泡が促進されるため発泡点の
部分となり、それ以外の部分は液体が流下する部分とな
り、高性能沸騰面における作用が人為的に区分されるこ
とになる。In other words, the area below the thin wire of the mesh electrode is the foaming point where the electric field forces the bubbles to separate and promotes foaming, and the other area is where the liquid flows down, causing the effect on the high-performance boiling surface to be artificial. It will be classified according to
(実施例)
次に、本発明の一実施例をPIS1図〜ttS2図に基
づいて説明する。(Example) Next, an example of the present invention will be described based on PIS1 diagram to ttS2 diagram.
ptSi図および第2図に示すように、高性能沸騰面1
と対向して電気導体の細線11をメツシュ状に形成した
メツシュ電極12をわずかの距離をおいて設置する。As shown in the ptSi diagram and Fig. 2, the high performance boiling surface 1
A mesh electrode 12, which is formed from thin electrical conductor wires 11 in a mesh shape, is placed opposite to the electrode 12 with a slight distance therebetween.
高性能沸騰面1を一方の電極とし、かつ前記メツシュ電
極12を他方の電極とし、高性能沸騰面1とメ・ンシュ
電極12との間に高電圧をかける。The high-performance boiling surface 1 is used as one electrode, the mesh electrode 12 is used as the other electrode, and a high voltage is applied between the high-performance boiling surface 1 and the mesh electrode 12.
電極間にはマックスウェル応力に相当する静電気的な圧
力が働いており、この力は気泡4を縦長にするだけで、
気泡4のメツシュ電極12方向の移動に対しては圧力が
静電気的な圧力分低い状況になるので気泡4は高性能沸
騰面1から強制的に離脱される。Electrostatic pressure equivalent to Maxwell stress is acting between the electrodes, and this force only makes the bubble 4 vertically long.
With respect to the movement of the bubbles 4 in the direction of the mesh electrode 12, the pressure becomes lower by the amount of electrostatic pressure, so the bubbles 4 are forcibly separated from the high-performance boiling surface 1.
このように高性能沸騰面1のうちメツシュ電極12の細
!11の下方部分Aでは、電場によりて気泡4の強制離
脱され発泡が促進され発泡点5の部分となる。これに対
して、高性能沸騰面1のうちメツシュ電極12の下方部
分A以外の部分Bは、液体が矢印Mのように自然に流下
する部分となる。In this way, the mesh electrode 12 of the high-performance boiling surface 1 is thin! In the lower part A of 11, the electric field forces the bubbles 4 to separate and promotes foaming, resulting in a foaming point 5. On the other hand, a portion B of the high-performance boiling surface 1 other than the lower portion A of the mesh electrode 12 is a portion where the liquid naturally flows down as shown by arrow M.
メツシュ電極12によって高性能沸騰面1の表面を発泡
点5の部分と液体が自然流下する部分とに人為的に設定
できるので、高性能沸騰面1の熱伝達量を望みのものに
調節でき、さらには熱伝達をさらに促進することもでき
る。Since the mesh electrode 12 allows the surface of the high-performance boiling surface 1 to be artificially set at the foaming point 5 and the region where the liquid naturally flows down, the amount of heat transfer on the high-performance boiling surface 1 can be adjusted to the desired value. Furthermore, heat transfer can be further promoted.
また、メツシュ電極12と高性能沸騰面1との間にかけ
る電圧が高い場合は電圧の低い場合に比べて気泡4を強
制離脱させ発泡を促進する効果が大きい。このことを利
用して、電圧の高低を可変にして発泡促進の程度を変え
熱伝達量を調節することもできる。Furthermore, when the voltage applied between the mesh electrode 12 and the high-performance boiling surface 1 is high, the effect of forcibly separating the bubbles 4 and promoting foaming is greater than when the voltage is low. Utilizing this fact, it is also possible to vary the level of voltage to change the degree of foaming promotion and adjust the amount of heat transfer.
さらに、本発明では電場によって発泡が促進されるため
、熱伝達量も電場をかけない場合に比べて促進されるこ
とは明白である。Furthermore, in the present invention, since foaming is promoted by an electric field, it is clear that the amount of heat transfer is also promoted compared to when no electric field is applied.
次に、本発明の別の実施例を第3図および第4図に基づ
いて説明する。Next, another embodiment of the present invention will be described based on FIGS. 3 and 4.
第3図および#S4図に示すように、本実施例のメツシ
ュ電極12は、細線11の間隔が狭ν1箇所を設け、メ
ツシュに広狭を形成してしする。As shown in FIG. 3 and #S4, the mesh electrode 12 of this embodiment has one narrow space ν between the thin wires 11 to form wide and narrow regions in the mesh.
メツシュ電極12と高性能沸騰面1との間に高電圧をか
ると、メツシュの狭い箇所Cにおいて第4図の矢印Nに
示すように細線11の狭い間から液体がジェット対流と
して強制上昇する。When a high voltage is applied between the mesh electrode 12 and the high-performance boiling surface 1, liquid is forced to rise as a jet convection from between the narrow lines 11 in the narrow portion C of the mesh as shown by the arrow N in FIG. 4.
メツシュ電極12の細線11下方部分以外の部分Bでは
液体が自然流下し、かつ電場によって細線11の下方の
気泡4が強制離脱されることは前に述べた実施例と同じ
である。As in the previous embodiment, the liquid flows down naturally in the portion B of the mesh electrode 12 other than the portion below the thin wire 11, and the air bubbles 4 below the thin wire 11 are forcibly removed by the electric field.
本実施例では、高性能沸騰面1を発泡点5の部分と液体
が流下する部分に人為的に設定可能な他、電場による上
記ジェット対流による熱伝達促進効果も奏する。In this embodiment, the high-performance boiling surface 1 can be artificially set at the foaming point 5 and the part where the liquid flows down, and also has the effect of promoting heat transfer by the jet convection caused by the electric field.
(発明の効果) 本発明では、次の効果を奏する。(Effect of the invention) The present invention has the following effects.
高性能沸騰面を発泡点の部分と液体が自然流下する部分
に人為的に設定することによって当該高性能沸騰面の熱
伝達量を任意のものに設定できる。By artificially setting the high-performance boiling surface at the foaming point and the region where the liquid naturally flows down, the heat transfer amount of the high-performance boiling surface can be set to an arbitrary value.
また、電場によって気泡が強制離脱され発泡が促進され
るので、電場をかけない場合に比べて熱伝達量が増大す
る。Furthermore, the electric field forcibly removes the bubbles and promotes foaming, so the amount of heat transfer increases compared to when no electric field is applied.
第1図は、本発明の一実施例に係る断面図、第2図は、
第1図の実施例の平面図、
第3図は、本発明の他の実施例に係る断面図、第4図は
、第3図の実施例の平面図、
第5図は、高性能沸騰面の断面図である。
1:高性能沸騰面
2二凹凸
12:メツシュ電極
第1図
第2Fl!J
第3図
第4図
第5図FIG. 1 is a sectional view according to an embodiment of the present invention, and FIG.
FIG. 3 is a sectional view of another embodiment of the present invention; FIG. 4 is a plan view of the embodiment of FIG. 3; FIG. 5 is a high-performance boiling FIG. 1: High performance boiling surface 2 2 unevenness 12: Mesh electrode Figure 1 Figure 2 Fl! J Figure 3 Figure 4 Figure 5
Claims (1)
能沸騰面(1)にメッシュ電極(12)を対向して設置
し、前記高性能沸騰面(1)を一方の電極とし、かつメ
ッシュ電極(12)を他方の電極とし、高性能沸騰面(
1)とメッシュ電極(12)との間に高電圧をかけるこ
とを特徴とする高性能沸騰面の電場を利用した熱伝達量
調整装置。A mesh electrode (12) is installed facing a high-performance boiling surface (1) that forms a large number of irregularities (2) on the surface to promote boiling, and the high-performance boiling surface (1) is used as one electrode, and The mesh electrode (12) is the other electrode, and the high-performance boiling surface (
1) A heat transfer amount adjusting device using an electric field of a high-performance boiling surface, which is characterized by applying a high voltage between the mesh electrode (12) and the mesh electrode (12).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6742285A JPS61225590A (en) | 1985-03-29 | 1985-03-29 | Heat transferring rate regulator utilizing electric field on high-performance boiling surface |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6742285A JPS61225590A (en) | 1985-03-29 | 1985-03-29 | Heat transferring rate regulator utilizing electric field on high-performance boiling surface |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61225590A true JPS61225590A (en) | 1986-10-07 |
Family
ID=13344455
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6742285A Pending JPS61225590A (en) | 1985-03-29 | 1985-03-29 | Heat transferring rate regulator utilizing electric field on high-performance boiling surface |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61225590A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5072780A (en) * | 1988-11-18 | 1991-12-17 | Agency Of Industrial Science & Technology, Ministry Of International Trade & Industry | Method and apparatus for augmentation of convection heat transfer in liquid |
US5769155A (en) * | 1996-06-28 | 1998-06-23 | University Of Maryland | Electrohydrodynamic enhancement of heat transfer |
CN109631651A (en) * | 2018-12-06 | 2019-04-16 | 华北电力大学 | A kind of local auto-adaptive controllable immersing coupling micro-structure enhanced boiling heat transfer method |
CN109855075A (en) * | 2018-12-06 | 2019-06-07 | 华北电力大学 | A kind of Boiling Heat Transfer Surfaces of wall surface micro-structure coupling localizing electrode |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS496409A (en) * | 1972-05-10 | 1974-01-21 | ||
JPS5837496A (en) * | 1981-08-31 | 1983-03-04 | Agency Of Ind Science & Technol | Transmitting device of boiling heat |
-
1985
- 1985-03-29 JP JP6742285A patent/JPS61225590A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS496409A (en) * | 1972-05-10 | 1974-01-21 | ||
JPS5837496A (en) * | 1981-08-31 | 1983-03-04 | Agency Of Ind Science & Technol | Transmitting device of boiling heat |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5072780A (en) * | 1988-11-18 | 1991-12-17 | Agency Of Industrial Science & Technology, Ministry Of International Trade & Industry | Method and apparatus for augmentation of convection heat transfer in liquid |
US5769155A (en) * | 1996-06-28 | 1998-06-23 | University Of Maryland | Electrohydrodynamic enhancement of heat transfer |
CN109631651A (en) * | 2018-12-06 | 2019-04-16 | 华北电力大学 | A kind of local auto-adaptive controllable immersing coupling micro-structure enhanced boiling heat transfer method |
CN109855075A (en) * | 2018-12-06 | 2019-06-07 | 华北电力大学 | A kind of Boiling Heat Transfer Surfaces of wall surface micro-structure coupling localizing electrode |
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