JPH023917B2 - - Google Patents

Info

Publication number
JPH023917B2
JPH023917B2 JP6742385A JP6742385A JPH023917B2 JP H023917 B2 JPH023917 B2 JP H023917B2 JP 6742385 A JP6742385 A JP 6742385A JP 6742385 A JP6742385 A JP 6742385A JP H023917 B2 JPH023917 B2 JP H023917B2
Authority
JP
Japan
Prior art keywords
pipe
heat
conduit
electric field
electrode
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
JP6742385A
Other languages
Japanese (ja)
Other versions
JPS61225591A (en
Inventor
Akira Yabe
Takao Takeya
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 JP6742385A priority Critical patent/JPS61225591A/en
Publication of JPS61225591A publication Critical patent/JPS61225591A/en
Publication of JPH023917B2 publication Critical patent/JPH023917B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/16Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying an electrostatic field to the body of the heat-exchange medium

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、管路を流れる熱媒体を沸騰させて熱
媒体を行なう熱交換器において電場を利用して熱
伝達を促進する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method of promoting heat transfer using an electric field in a heat exchanger that boils a heat medium flowing through a pipe.

(従来技術) 管路外からの熱によつて管路を流れるフロン、
水等の熱媒体を沸騰させて熱伝達を行なう熱交換
器がある。
(Prior art) Freon flowing through the pipe due to heat from outside the pipe,
There is a heat exchanger that transfers heat by boiling a heat medium such as water.

第3図を参照して、この熱交換器(図示省略)
の管路1内の熱媒体2が管路1外からの熱Qを受
けてどのように変化するか示す。液体2状態の熱
媒体は、熱Qを受けて沸騰する。
Referring to Fig. 3, this heat exchanger (not shown)
The figure shows how the heat medium 2 inside the pipe line 1 changes when it receives heat Q from outside the pipe line 1. The heat medium in the liquid 2 state receives the heat Q and boils.

管路1の最初では、気体3は気泡として液体2
の中に発生し二相流となる(A領域)。次の段階
では、管路1の中央付近に気体3が流れ、液体2
は管路1の内壁面4付近を環状に流れる環状流と
なる(B領域)。次に、液体2は噴霧流になる
(C領域)。最後に、液体2はすべて気化して蒸気
5となる(D領域)。
At the beginning of conduit 1, gas 3 forms bubbles in liquid 2.
A two-phase flow occurs in the area (A region). In the next stage, gas 3 flows near the center of pipe 1, and liquid 2
becomes an annular flow that flows in an annular manner near the inner wall surface 4 of the conduit 1 (region B). The liquid 2 then becomes a spray stream (region C). Finally, all of the liquid 2 is vaporized and becomes vapor 5 (region D).

この蒸気5は、熱交換器を出てから発電用ター
ビン等に送られる。
After leaving the heat exchanger, this steam 5 is sent to a power generation turbine or the like.

(発明が解決しようとする問題点) ところが、上記状態におけるC領域の噴霧流で
は、微細液滴6が管路1の中の全体にわたり均一
に存在するため管路1の外からの熱Qが微粒液滴
6に伝わりにくく、完全に気化して蒸気となるD
領域まで時間がかかるものとなつていた。そのた
め、噴霧流のC領域から蒸気のD領域までの管路
1の長さが長いものが要求されることになり、熱
交換器の小型化を阻害する原因の一つとなつてい
た。
(Problem to be Solved by the Invention) However, in the spray flow in region C in the above state, the fine droplets 6 are uniformly present throughout the pipe 1, so the heat Q from outside the pipe 1 is D is difficult to transmit to the fine droplets 6 and completely vaporizes into vapor.
It was taking a long time to reach the area. Therefore, a long pipe line 1 from the spray flow area C to the steam D area is required, which is one of the reasons for hindering the miniaturization of the heat exchanger.

本発明の目的は、上記C領域の噴霧流における
熱伝達を促進させることにより噴霧流から蒸気と
なる領域の管路1を短縮化し、もつて熱交換器を
小型化することにある。
An object of the present invention is to shorten the pipe line 1 in the region where the spray flow becomes steam by promoting heat transfer in the spray flow in the C region, thereby downsizing the heat exchanger.

(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では、次のよう
に噴霧流の熱伝達を促進している。
(Means for Solving the Problems) In order to achieve the above object, the present invention promotes heat transfer of the spray stream as follows.

管路のうち熱媒体が噴霧流となる箇所に管路の
断面中心部を囲むメツシユ電極を設置し、管路を
一方の電極とし、かつ前記メツシユ電極を他方の
電極として管路とメツシユ電極との間に高電圧を
かける。
A mesh electrode surrounding the center of the cross section of the pipe is installed at a location in the pipe where the heat medium becomes a spray flow, and the pipe is used as one electrode, and the mesh electrode is used as the other electrode to connect the pipe and the mesh electrode. Apply high voltage between the two.

(作用) 本発明は、次のように作用する。(effect) The invention works as follows.

メツシユ電極と管路との間に高電圧をかける
と、メツシユ電極と管路との間に電場がつくられ
る。メツシユ電極内、つまり管路1の中央部分に
は電場がなく、ここに気体が集まる。気体は電界
の強い所から電界の弱い所に弾き出される力を受
けるからである。
When a high voltage is applied between the mesh electrode and the conduit, an electric field is created between the mesh electrode and the conduit. There is no electric field in the mesh electrode, that is, in the center of the conduit 1, and gas collects there. This is because the gas is subjected to a force that causes it to be ejected from an area where the electric field is strong to an area where the electric field is weak.

一方、気体よりも誘電率の大きい液滴は電界の
弱いところから電界の強いところに引き入れられ
る力を受けるので、微細液滴は管路の内壁面付近
に集まる。したがつて、微細液滴は管路の外から
の熱を受け気化しやすくなる。
On the other hand, droplets with a higher dielectric constant than gas are subjected to a force that draws them from an area with a weak electric field to an area with a strong electric field, so the fine droplets gather near the inner wall surface of the conduit. Therefore, the fine droplets receive heat from outside the conduit and are easily vaporized.

(実施例) 以下に、本発明の一実施例を第1図〜第2図に
基づいて説明する。本実施例において熱交換器
(図示省略)は管路を流れる熱媒体を沸騰させて
熱伝達を行なうものである。そして、第1図およ
び第2図は、管路1において従来では噴霧流とな
る箇所(上記C領域)を示したものである。
(Example) An example of the present invention will be described below based on FIGS. 1 and 2. In the present embodiment, the heat exchanger (not shown) transfers heat by boiling the heat medium flowing through the pipes. FIGS. 1 and 2 show locations in the pipe line 1 that would conventionally form a spray flow (region C).

本実施例では、管路1の断面中心を囲むメツシ
ユ電極11を設置する。そして、管路1自体を一
方の電極とし、かつ前記メツシユ電極11を他方
の電極として管路1とメツシユ電極11との間に
高電圧をかける。12は電源である。
In this embodiment, a mesh electrode 11 surrounding the center of the cross section of the conduit 1 is installed. Then, a high voltage is applied between the conduit 1 and the mesh electrode 11, with the conduit 1 itself serving as one electrode and the mesh electrode 11 serving as the other electrode. 12 is a power source.

メツシユ電極11と管路1の間に電場がつくら
れる。メツシユ電極11内、つまり管路1の中央
付近13には電場がなく、ここに気体3が集ま
る。気体3は電界の強い所から電界の弱い所に弾
き出される力を受けるからである。
An electric field is created between the mesh electrode 11 and the conduit 1. There is no electric field within the mesh electrode 11, that is, near the center 13 of the conduit 1, and the gas 3 gathers here. This is because the gas 3 receives a force that is ejected from a place where the electric field is strong to a place where the electric field is weak.

一方、微細液滴6は電界の強い方に引かれる力
を受けるので管路1の内壁面4付近に集まる。し
たがつて、微細液滴6は内壁面に接触する機会が
増え管路1の外からの熱を受け気化しやすくな
る。
On the other hand, the fine droplets 6 are attracted near the inner wall surface 4 of the conduit 1 because they are attracted by the stronger electric field. Therefore, the fine droplets 6 have an increased chance of coming into contact with the inner wall surface, and are more likely to receive heat from outside the pipe line 1 and vaporize.

こうして噴霧流から蒸気になることが早くなる
ため、管路1の長さが短縮することができ、熱交
換器を小型化できる。
In this way, since the spray stream turns into steam more quickly, the length of the pipe line 1 can be shortened, and the heat exchanger can be made smaller.

(発明の効果) 以上述べたように、本発明によれば噴霧流の段
階での熱伝達が促進され早く蒸気になるため、管
路の長さが短縮でき、熱交換器が小型化できる。
(Effects of the Invention) As described above, according to the present invention, heat transfer at the stage of spray flow is promoted and the spray becomes steam quickly, so the length of the pipe can be shortened and the heat exchanger can be downsized.

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

第1図は、本発明の一実施例であり、熱交換器
の管路の縦断面図、第2図は、第1図の−線
断面図、第3図は、従来の熱交換器における管路
内の熱媒体を示した縦断面図である。 1:管路、3:気体、4:管路の内壁面、6:
微細液滴、11:メツシユ電極、C:噴霧流とな
る箇所。
FIG. 1 is a longitudinal sectional view of a pipe line of a heat exchanger according to an embodiment of the present invention, FIG. 2 is a sectional view taken along the - line in FIG. FIG. 3 is a longitudinal cross-sectional view showing a heat medium inside a pipe. 1: pipe line, 3: gas, 4: inner wall surface of pipe line, 6:
Fine droplets, 11: Mesh electrode, C: Point where the spray flow is formed.

【特許請求の範囲】[Claims]

1 二相流が流れている管路1の中の気泡流(A)及
び/或は環状流(B)位置に管路1の軸方法に沿つて
線電極12を設け、線電極12の外側を囲んでメ
ツシユ電極13を設け、前記線電極12とメツシ
ユ電極13との間に高電圧をかけて、気体3を管
路1の内壁面4付近に集め、管路1の中央付近を
液体2の流れとすることを特徴とする電場を利用
した二相流の流動特性の改善方法。
1. A wire electrode 12 is provided along the axis of the pipe 1 at the bubble flow (A) and/or annular flow (B) position in the pipe 1 where the two-phase flow is flowing, and the wire electrode 12 is placed outside the wire electrode 12. A mesh electrode 13 is provided surrounding the line electrode 12, and a high voltage is applied between the wire electrode 12 and the mesh electrode 13 to collect the gas 3 near the inner wall surface 4 of the pipe 1, and the liquid 2 near the center of the pipe 1. A method for improving the flow characteristics of a two-phase flow using an electric field, characterized in that the flow is as follows.

JP6742385A 1985-03-29 1985-03-29 Method to promote transferring of heat utilizing electric field in heat exchanger Granted JPS61225591A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6742385A JPS61225591A (en) 1985-03-29 1985-03-29 Method to promote transferring of heat utilizing electric field in heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6742385A JPS61225591A (en) 1985-03-29 1985-03-29 Method to promote transferring of heat utilizing electric field in heat exchanger

Publications (2)

Publication Number Publication Date
JPS61225591A JPS61225591A (en) 1986-10-07
JPH023917B2 true JPH023917B2 (en) 1990-01-25

Family

ID=13344486

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6742385A Granted JPS61225591A (en) 1985-03-29 1985-03-29 Method to promote transferring of heat utilizing electric field in heat exchanger

Country Status (1)

Country Link
JP (1) JPS61225591A (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
US5769155A (en) * 1996-06-28 1998-06-23 University Of Maryland Electrohydrodynamic enhancement of heat transfer

Also Published As

Publication number Publication date
JPS61225591A (en) 1986-10-07

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