JPH023918B2 - - Google Patents

Info

Publication number
JPH023918B2
JPH023918B2 JP6742585A JP6742585A JPH023918B2 JP H023918 B2 JPH023918 B2 JP H023918B2 JP 6742585 A JP6742585 A JP 6742585A JP 6742585 A JP6742585 A JP 6742585A JP H023918 B2 JPH023918 B2 JP H023918B2
Authority
JP
Japan
Prior art keywords
flow
liquid
pipe
electrode
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.)
Expired
Application number
JP6742585A
Other languages
Japanese (ja)
Other versions
JPS61225592A (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 JP6742585A priority Critical patent/JPS61225592A/en
Publication of JPS61225592A publication Critical patent/JPS61225592A/en
Publication of JPH023918B2 publication Critical patent/JPH023918B2/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、電場を利用して管路中の二相流の流
動特性を改善する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method of improving the flow characteristics of two-phase flow in a conduit using an electric field.

(従来技術) 従来、管路内を流れる水、フロン等の液体に対
し熱伝達して沸騰させる熱交換器においては、流
れの方向において気泡流、環状流、噴霧流、蒸気
流となり、このうち気泡流、環状流の部分で熱伝
達があまり良好でなく、かつ液体を圧送するため
の圧力損失が環状流の位置で大きく液体の流量を
気体の流量に合致させんとすることが困難である
という問題点があつた。
(Prior art) Conventionally, in a heat exchanger that transfers heat to a liquid such as water or fluorocarbon flowing in a pipe to boil it, the flow direction is a bubble flow, annular flow, spray flow, or vapor flow. Heat transfer is not very good in the bubble flow and annular flow areas, and the pressure loss for pumping the liquid is large at the annular flow position, making it difficult to match the liquid flow rate to the gas flow rate. There was a problem.

この問題点を明らかにするために、第2図にお
いて熱交換器内の管路1を流れる液体の流動特性
を示す。管路1を流れる液体2に管路1外の熱Q
が伝達されるため液体2中に気体3が気泡として
あらわれ二相流となる。
In order to clarify this problem, FIG. 2 shows the flow characteristics of the liquid flowing through the pipe line 1 in the heat exchanger. Heat Q outside the pipe 1 is applied to the liquid 2 flowing through the pipe 1.
is transmitted, gas 3 appears as bubbles in liquid 2, resulting in a two-phase flow.

この二相流は、流れの始めの方では均一な気泡
流である(A域)。流れにしたがつて管路1の中
央付近は気体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域)。次
に、液体2が液滴となる噴霧流となる(C域)。
そして最後に、蒸気となる(D域)。
This two-phase flow is a uniform bubble flow at the beginning of the flow (region A). According to the flow, the gas 3 flows near the center of the pipe 1, and the liquid 2 forms an annular flow that flows in a circular shape near the inner wall surface 4 of the pipe 1 (region B). Next, the liquid 2 becomes a spray stream in which droplets form (region C).
Finally, it becomes steam (region D).

(発明が解決しようとする問題点) 従来の熱交換器の管路1における前記A域では
気泡を管路1の内面壁4付近へ集合させることに
より境界層を乱して熱伝達効率を上げるようにす
ることが望ましく、前記B域の環状流に相当する
箇所においては液体2と管路1の内壁面4の摩擦
が大きく中央にある気体3が大量に流れるのに対
し液体2の流量が少ないものとなつていた。すな
わち、熱伝達が望ましくないことと液体2を圧送
するための圧力損失が大きいため、蒸気と液体と
の好ましい流れとすることができない問題があつ
た。
(Problems to be Solved by the Invention) In the area A of the conduit 1 of the conventional heat exchanger, air bubbles are gathered near the inner wall 4 of the conduit 1 to disturb the boundary layer and increase heat transfer efficiency. It is desirable that the flow rate of the liquid 2 is large in the part corresponding to the annular flow in the region B, where the friction between the liquid 2 and the inner wall surface 4 of the pipe line 1 is large and the gas 3 in the center flows in large quantities. It was becoming less and less. That is, since heat transfer is undesirable and the pressure loss for pumping the liquid 2 is large, there is a problem in that it is not possible to achieve a desirable flow of vapor and liquid.

本発明は、上述のA域、B域の流動特性を改善
するものである。すなわち、本発明の目的は、液
体を管路の中央付近を流れるようにし、気泡を管
路の内壁付近に集めることによつて熱伝達率を向
上させ圧力損失を少なくし小さな動力によつて液
体の流量を多くする方法を提供することにある。
The present invention improves the flow characteristics in the above-mentioned regions A and B. That is, an object of the present invention is to allow the liquid to flow near the center of the pipe and collect bubbles near the inner wall of the pipe, thereby improving the heat transfer coefficient and reducing pressure loss. The purpose of this invention is to provide a method for increasing the flow rate.

(問題点を解決するための手段) 上記目的を達成するために、本発明では次のよ
うに二相流の流動特性を改善している。
(Means for Solving the Problems) In order to achieve the above object, the present invention improves the flow characteristics of two-phase flow as follows.

二相流が流れている管路の中の気泡流及び/或
は環状流の位置に管路の軸方法に沿つて線電極を
設け、線電極の外側を囲んでメツシユ電極を設
け、前記線電極とメツシユ電極との間に高電圧を
かけて、気体を管路の内壁面付近に集め、管路の
中央付近を液体の流れとする。
A wire electrode is provided along the axis of the pipe at a position of bubble flow and/or annular flow in a pipe in which a two-phase flow is flowing, a mesh electrode is provided surrounding the outside of the wire electrode, and a mesh electrode is provided surrounding the outside of the wire electrode. A high voltage is applied between the electrode and the mesh electrode to collect gas near the inner wall surface of the pipe, creating a liquid flow near the center of the pipe.

なお、本発明は熱交換器の流動特性の改善に限
らず、その他液体と気体の二相流一般の流動特性
の改善をも包含する。
Note that the present invention is not limited to improving the flow characteristics of a heat exchanger, but also includes improving the flow characteristics of two-phase flows of liquid and gas in general.

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

線電極とメツシユ電極とに電圧をかけると、線
電極の方がメツシユ電極よりも電界が強いものと
なる。液体よりも誘電率が小さい気体の気泡にお
いて、電界の強い線電極と同じ電極の電荷が気液
界面に生じる。そのため、気泡は電界の弱いメツ
シユ電極の方向にはじき出される。
When a voltage is applied to a wire electrode and a mesh electrode, the electric field of the wire electrode is stronger than that of the mesh electrode. In gas bubbles that have a lower dielectric constant than liquid, the same electrode charge as a wire electrode with a strong electric field is generated at the gas-liquid interface. Therefore, the bubbles are expelled in the direction of the mesh electrode where the electric field is weak.

さらに、メツシユ電極と管内壁との間は電界が
0であるため気泡はメツシユ電極からもはじき出
され、管内壁とメツシユ電極間に存在する。
Further, since the electric field is zero between the mesh electrode and the inner wall of the tube, the bubbles are also repelled from the mesh electrode and exist between the inner wall of the tube and the mesh electrode.

(実施例) 以下に、本発明の一実施例を第1図及び第2図
に基づいて説明する。本実施例は、熱交換器にお
ける液体の流動特性を改善して小さな動力で足り
るようにしたものに関する。
(Example) An example of the present invention will be described below based on FIGS. 1 and 2. This embodiment relates to a heat exchanger in which the flow characteristics of liquid are improved so that a small amount of power is required.

第1図は、熱交換器における上述の管路1のA
域、B域に相当する箇所に流動特性改善のための
装置11を設置したものを示している。
FIG. 1 shows the A of the above-mentioned pipe line 1 in the heat exchanger.
This figure shows that a device 11 for improving flow characteristics is installed at a location corresponding to area and area B.

管路1の中に管路1の軸方向に沿つて線電極を
12設け、この線電極12の外側を囲んでメツシ
ユ電極13を設ける。線電極12とメツシユ電極
13は非接触状態である。線電極12とメツシユ
電極13との間に高電圧をかける。14は電源で
ある。
12 wire electrodes are provided in the pipe 1 along the axial direction of the pipe 1, and a mesh electrode 13 is provided surrounding the outside of the wire electrode 12. The wire electrode 12 and the mesh electrode 13 are in a non-contact state. A high voltage is applied between the wire electrode 12 and the mesh electrode 13. 14 is a power source.

線電極12の電界は、メツシユ電極13の電界
よりも強い。気液界面には、電界の強い線電極1
2と同じ電荷(本実施例では正の電荷)が生じ、
気体3は電界の弱いメツシユ電極13の方向には
じき出される。こうして、管路1の内壁面4付近
に気体3が集まり、管路1の中央付近は液体2の
流れとなる。
The electric field of the wire electrode 12 is stronger than the electric field of the mesh electrode 13. At the gas-liquid interface, there is a wire electrode 1 with a strong electric field.
The same charge as 2 (positive charge in this example) is generated,
The gas 3 is expelled in the direction of the mesh electrode 13 where the electric field is weak. In this way, the gas 3 gathers near the inner wall surface 4 of the pipe 1, and the liquid 2 flows near the center of the pipe 1.

液体2が管路1の中央付近を流れるので圧力損
失が少なく、液体2の流量を多くできる。
Since the liquid 2 flows near the center of the pipe line 1, pressure loss is small and the flow rate of the liquid 2 can be increased.

また、気体3がわずかしか生じていない段階に
おいて本実施例を用いて、管路1の内壁面4の境
界層15を乱しより多くの気泡の発生を助けて液
体2に対する熱の伝達量を増大させることも可能
である。つまり、本発明に係る方法を熱交換器に
適用すると、管路1を流れる液体の流量を多くで
きると共に熱伝達量を向上させることも可能であ
る。
In addition, by using this embodiment at a stage when only a small amount of gas 3 is generated, the boundary layer 15 on the inner wall surface 4 of the pipe line 1 is disturbed to help generate more bubbles, thereby reducing the amount of heat transferred to the liquid 2. It is also possible to increase it. That is, when the method according to the present invention is applied to a heat exchanger, it is possible to increase the flow rate of liquid flowing through the pipe line 1 and also to improve the amount of heat transfer.

他の実施例として次のものもある。ガソリン等
の燃料中に空気の気泡を混合し熱機関に送り、有
害ガスの発生を防止する技術がある。この二相流
でも燃料が管路1の内壁面に沿つて流れ、管路1
の中央を空気が流れる環状流となるおそれがあ
る。環状流となると空気が大量に送られ燃料がわ
ずかしか送られないため燃焼上好ましくない。
Other examples include the following. There is a technology that mixes air bubbles into fuel such as gasoline and sends it to a heat engine to prevent the generation of harmful gases. Even in this two-phase flow, the fuel flows along the inner wall surface of the pipe 1, and the fuel flows along the inner wall surface of the pipe 1.
There is a risk of an annular flow in which air flows through the center of the air. An annular flow is unfavorable for combustion because a large amount of air is sent and only a small amount of fuel is sent.

そこで、燃料と気泡の二相流を第1図に示す装
置11と同じものを用いて気泡を管路1の内壁面
4付近に集め、燃料が管路の中央を流れるように
するのである。これによつて、燃料と空気を好ま
しい割合で送ることができる。
Therefore, the two-phase flow of fuel and bubbles is carried out by using the same device 11 shown in FIG. 1 to collect the bubbles near the inner wall surface 4 of the conduit 1 so that the fuel flows through the center of the conduit. This allows fuel and air to be delivered in a preferred ratio.

(発明の効果) 本発明によれば、次の効果を奏する。(Effect of the invention) According to the present invention, the following effects are achieved.

沸騰熱交換器における気泡流、環状流の位置で
熱伝達を向上させることができる。
Heat transfer can be improved at the location of bubble flow and annular flow in boiling heat exchangers.

管路中の二相流において液体を管路の中央付近
を流すので、圧力損失が少なく、多くの流量の液
体を小さな動力で流すことができる。
Since the liquid flows near the center of the pipe in a two-phase flow in the pipe, there is little pressure loss, and a large amount of liquid can be flowed with a small amount of power.

また、二相流を移送する場合において気体だけ
が大量に移送されるということをなくすことがで
きる。
Furthermore, when transferring a two-phase flow, it is possible to avoid transferring only a large amount of gas.

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

第1図は、本発明の一実施例を示す縦断面図、
第2図は、第1図の−線横断面図、第3図
は、従来における熱交換器の管路を流れる液体の
流動特性を示す縦断面図、 1:管路、2:液体、3:気体、4:内壁面、
12:線電極、13:メツシユ電極。
FIG. 1 is a longitudinal sectional view showing an embodiment of the present invention;
FIG. 2 is a cross-sectional view taken along the - line in FIG. 1, and FIG. 3 is a vertical cross-sectional view showing the flow characteristics of liquid flowing through the pipes of a conventional heat exchanger. 1: Pipe line, 2: Liquid, 3 : Gas, 4: Inner wall surface,
12: Line electrode, 13: Mesh electrode.

【特許請求の範囲】[Claims]

1 冷却媒体によつて冷却される凝縮伝熱面に対
して間隔を置いて線電極を設置し、この線電極を
一方の電極とするとともに前記伝熱面を他方の電
極とし、前記伝熱面と前記線電極との間に高電圧
をかけ、伝熱面に凝縮付着した凝縮液を伝熱面か
ら線電極に引き寄せ除去する熱伝達促進装置にお
いて、 前記線電極を負の高電圧とし、該線電極にかか
る高電圧を抵抗を介して負の低電圧として前記伝
熱面にかけ、前記冷却媒体を接地することにより
前記伝熱面と前記冷却媒体との間に負の低電圧を
かけ、伝熱面の防食及びスラツジ付着防止を行う
ことを特徴とする電場を利用した熱伝達促進装置
における腐食防止装置。
1. A wire electrode is installed at a distance from a condensing heat transfer surface that is cooled by a cooling medium, and this wire electrode is used as one electrode, and the heat transfer surface is used as the other electrode, and the heat transfer surface In a heat transfer promoting device that applies a high voltage between the wire electrode and the wire electrode to draw and remove condensate that has condensed and adhered to the heat transfer surface from the heat transfer surface to the wire electrode, the wire electrode is applied with a negative high voltage and the The high voltage applied to the wire electrode is applied to the heat transfer surface as a negative low voltage via a resistor, and the cooling medium is grounded to apply a negative low voltage between the heat transfer surface and the cooling medium, thereby causing the transfer. A corrosion prevention device for a heat transfer promotion device using an electric field, which is characterized by preventing corrosion on a hot surface and preventing sludge adhesion.

JP6742585A 1985-03-29 1985-03-29 Method to improve fluidizing property of two-phase flow utilizing electric field Granted JPS61225592A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6742585A JPS61225592A (en) 1985-03-29 1985-03-29 Method to improve fluidizing property of two-phase flow utilizing electric field

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6742585A JPS61225592A (en) 1985-03-29 1985-03-29 Method to improve fluidizing property of two-phase flow utilizing electric field

Publications (2)

Publication Number Publication Date
JPS61225592A JPS61225592A (en) 1986-10-07
JPH023918B2 true JPH023918B2 (en) 1990-01-25

Family

ID=13344546

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6742585A Granted JPS61225592A (en) 1985-03-29 1985-03-29 Method to improve fluidizing property of two-phase flow utilizing electric field

Country Status (1)

Country Link
JP (1) JPS61225592A (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
JPS61225592A (en) 1986-10-07

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