JPH0612392Y2 - Liquid withdrawal device - Google Patents

Liquid withdrawal device

Info

Publication number
JPH0612392Y2
JPH0612392Y2 JP1987106944U JP10694487U JPH0612392Y2 JP H0612392 Y2 JPH0612392 Y2 JP H0612392Y2 JP 1987106944 U JP1987106944 U JP 1987106944U JP 10694487 U JP10694487 U JP 10694487U JP H0612392 Y2 JPH0612392 Y2 JP H0612392Y2
Authority
JP
Japan
Prior art keywords
main electrode
electrodes
heat transfer
electrode
tube
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
JP1987106944U
Other languages
Japanese (ja)
Other versions
JPS6415094U (en
Inventor
彰 矢部
正広 花井
Original Assignee
工業技術院長
スーパーヒートポンプ・エネルギー集積システム技術研究組合
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 工業技術院長, スーパーヒートポンプ・エネルギー集積システム技術研究組合 filed Critical 工業技術院長
Priority to JP1987106944U priority Critical patent/JPH0612392Y2/en
Publication of JPS6415094U publication Critical patent/JPS6415094U/ja
Application granted granted Critical
Publication of JPH0612392Y2 publication Critical patent/JPH0612392Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【考案の詳細な説明】 〔考案の目的〕 (産業上の利用分野) 本考案は、例えば冷却器等に使用される凝縮管の外周に
生成される凝縮液膜を電気的に取り除き、凝縮熱伝達を
向上せしめる液体引出装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Purpose of Invention] (Industrial field of application) The present invention is designed to electrically remove a condensate film formed on the outer circumference of a condenser pipe used in, for example, a cooler, to condense heat. The present invention relates to a liquid withdrawal device that improves transmission.

(従来の技術) 省エネルギを推進するには、低温廃熱をいかに有効に活
用するかが重要である。現在、100℃以下の低温廃熱
はほとんど回収されておらず、工場から排出される熱量
の60%近くが100℃以下の低温廃熱であることを鑑
みれば、低温廃熱からのエネルギ回収は石油等の化石燃
料の省力化に不可欠である。
(Prior Art) In order to promote energy saving, it is important to effectively use low temperature waste heat. At present, low-temperature waste heat of 100 ° C. or less is hardly recovered, and considering that nearly 60% of the heat quantity discharged from the factory is low-temperature waste heat of 100 ° C. or less, energy recovery from low-temperature waste heat is not possible. It is indispensable for labor saving of fossil fuels such as oil.

低温廃熱エネルギ回収を行なう場合、冷媒として例えば
フロン等の低沸点媒体を用いて発電等を行なうことが有
効活用の一手段である。
In the case of recovering low-temperature waste heat energy, one of effective means is to perform power generation using a low boiling point medium such as CFC as a refrigerant.

ところが、熱源が低温であるため、火力発電にくらべ発
電効率が極めて低く、また熱源と冷却水との温度差があ
まり高くないため、火力発電と同程度の出力を得るに
は、熱交換器の伝熱面積を数百倍の容量にしなければな
らない。
However, since the heat source is at a low temperature, the power generation efficiency is extremely low compared to thermal power generation, and the temperature difference between the heat source and cooling water is not so high. The heat transfer area must be several hundred times the capacity.

このため、低温廃熱利用の発電プラントでは、熱交換器
の作製コストが極めて大きく、実用化の障害になってい
る。
Therefore, in a power plant using low temperature waste heat, the manufacturing cost of the heat exchanger is extremely high, which is an obstacle to practical use.

最近、熱交換器の熱交換量を飛躍的に向上させる一手段
として、例えば特公昭59−41117号公報、特開昭
59−180298号公報、特開昭59−134495
号公報に見る如く、伝熱管に高電圧を印加し、電位差に
よって伝熱管に付着する凝縮液膜を強制的に取り除き、
凝縮熱伝達を高めるいわゆる液体引出装置が提案されて
いる。これらの技術によれば、従来の熱交換器の熱授受
量にくらべ2倍以上に向上していることが確認されてい
る。
Recently, as one means for dramatically improving the heat exchange amount of a heat exchanger, for example, JP-B-59-41117, JP-A-59-180298, and JP-A-59-134495.
As seen in Japanese Patent Publication, a high voltage is applied to the heat transfer tube to forcibly remove the condensed liquid film adhering to the heat transfer tube due to the potential difference,
So-called liquid withdrawal devices have been proposed which enhance condensation heat transfer. According to these techniques, it has been confirmed that the heat exchange amount of the conventional heat exchanger is more than doubled.

(考案が解決しようとする問題点) ところが、これら技術は、性能向上の点ではすぐれてい
るものの、1つの伝熱管に、同心状に、かつスパイラル
に形成した電極線を数組みにもわけて囲繞しており、ま
た、スパイラル状に配した電極線の末端は半径の極めて
大きい拡口状態になっている関係上、製作・組立工数に
長時間を要するとともに、従来の熱交換器の作製コスト
よりも大幅の増加になっている。また、1つの伝熱管に
は、数組みにもわけて電極線を囲繞しているために安定
した電極線の配置が得られず、このため伝熱管の局部に
高電圧が流れ、絶縁破壊を誘発する危険性がある。
(Problems to be solved by the device) However, although these technologies are excellent in terms of performance improvement, they are divided into several sets of concentric and spirally formed electrode wires in one heat transfer tube. Since it is surrounded and the end of the spirally arranged electrode wire is in an expanded state with an extremely large radius, it takes a long time to manufacture and assemble, and the manufacturing cost of the conventional heat exchanger. It is a big increase. In addition, since the electrode wire is surrounded by several sets in one heat transfer tube, a stable arrangement of the electrode wire cannot be obtained. Therefore, a high voltage flows in the local part of the heat transfer tube, which causes dielectric breakdown. There is a risk of triggering.

そこで、本考案は上記の点に徴し、伝熱管に対して電極
線の配置が安定した配置になるようにして凝縮熱伝達を
一段と向上せしめようとする液体引出装置を提供するこ
とを目的とする。
In view of the above, the present invention has an object to provide a liquid drawing device that further improves the condensation heat transfer by stabilizing the arrangement of the electrode wires with respect to the heat transfer tube. .

〔考案の構成〕[Constitution of device]

(問題点を解決するための手段) 本考案は、上記目的を達成するために、管外表面に対し
一定の間隔をおいて対峙して管軸方向に並行な主電極を
設け、主電極から樹枝状に分れた複数の分電極を自由端
側が漸次上り勾配となるように設け、これらの分電極で
管外表面を同心状に囲繞するとともに、前記主電極から
複数の分電極に分かれる各枝分れの部の下方において、
前記主電極にポケット部を備えた液集合部を設け、上記
分電極に引き寄せられた管外表面からの凝縮液を前記各
分電極に沿って重力の作用でポケット部から液集合部に
集め、この液集合部からの溢液を主電極の外側面に沿っ
て流下させたものである。
(Means for Solving the Problems) In order to achieve the above-mentioned object, the present invention provides a main electrode facing the outer surface of the tube at a constant interval and parallel to the tube axial direction. A plurality of branching electrodes divided in a dendritic manner are provided so that the free end side has a gradual upward slope, and the outer surfaces of the tube are concentrically surrounded by these branching electrodes, and the main electrode is divided into a plurality of branching electrodes. Below the branch,
The main electrode is provided with a liquid collecting portion having a pocket portion, and the condensed liquid from the outer surface of the tube attracted to the dividing electrodes is collected along the dividing electrodes from the pocket portion to the liquid collecting portion by the action of gravity. The overflow liquid from the liquid collecting portion is made to flow down along the outer surface of the main electrode.

(作用) 電極は、幹と枝からなるいわゆるツリー形状になってお
り、その枝は伝熱管に対して同心状に囲繞されているの
で、電極と伝熱管との位置関係は常に一定した距離が保
たれ、安定した配置が得られる。また、電極と伝熱管と
は1対1の関係になるので、従来のように数組みにわけ
て取付けている電極よりも組立工数等は激減する。
(Function) The electrode has a so-called tree shape consisting of a trunk and branches, and since the branches are concentrically surrounded by the heat transfer tube, the positional relationship between the electrode and the heat transfer tube is always constant. A stable and stable arrangement is obtained. Further, since the electrodes and the heat transfer tubes have a one-to-one relationship, the number of assembling steps and the like are drastically reduced as compared with the conventional case where the electrodes are divided into several sets and attached.

(実施例) 以下本考案の一実施例を図面を参照して説明する。Embodiment An embodiment of the present invention will be described below with reference to the drawings.

第1図は、この種の分野に適用される熱交換器であっ
て、シェル1には一対のヘッダ2,2が組み込まれ、こ
れらは伝熱管4を介して連通されている。そして、凝縮
流体、例えばフロン等はヘッダ入口5から伝熱管4を経
てヘッダ出口3に流れる間に、シェル入口6からシェル
出口7に流れる被凝縮流体、例えば水と熱の授受を行な
っている。この熱の授受を行なう際、伝熱管4には凝縮
液膜が被膜され、このため熱交換量が思ったように向上
せず、日夜、研究開発が行なわれていた。
FIG. 1 shows a heat exchanger applied to this type of field, in which a shell 1 has a pair of headers 2 and 2 incorporated therein, which are communicated via a heat transfer tube 4. Then, while the condensing fluid, such as CFC, flows from the header inlet 5 to the header outlet 3 via the heat transfer tube 4, the condensed fluid, such as water, flowing from the shell inlet 6 to the shell outlet 7 exchanges heat. When this heat is transferred, the heat transfer tube 4 is coated with a condensate liquid film, so the heat exchange amount does not improve as expected, and research and development have been conducted day and night.

しかして、本考案は伝熱管に生成される凝縮液膜を電位
差を巧みに利用して積極的に取り除くようにしたもので
ある。すなわち、本考案にかかる電極は、第2図に示す
如く、ツリー状に形成されており、幹の部分に相当する
主電極11と枝に相当する分電極12からなる。また、
主電極11には複数の分電極12に分かれる各枝分れ部
の下方で液集合部13が設けられており、この液集合部
13は例えば第2図に示すコ字状切欠きを凹設して構成
される。液集合部13には分電極12を伝って滴下する
凝縮液を受けるポケット部14が付加されており、この
ポケット部14に案内されて液集合部13に集められた
凝縮液は、液集合部13の開口を通って主電極11の外
側に導かれ、主電極11の外側を伝って流下するように
なっている。
Therefore, the present invention is one in which the condensate film generated in the heat transfer tube is positively removed by skillfully utilizing the potential difference. That is, the electrode according to the present invention is formed in a tree shape as shown in FIG. 2, and comprises a main electrode 11 corresponding to a trunk portion and a branch electrode 12 corresponding to a branch. Also,
The main electrode 11 is provided with a liquid collecting portion 13 below each branched portion that is divided into a plurality of branch electrodes 12, and the liquid collecting portion 13 has, for example, a U-shaped notch shown in FIG. Configured. The liquid collecting portion 13 is provided with a pocket portion 14 for receiving the condensed liquid dropped along the distribution electrode 12, and the condensed liquid collected in the liquid collecting portion 13 guided by the pocket portion 14 is the liquid collecting portion 13. It is guided to the outside of the main electrode 11 through an opening 13 and flows down the outside of the main electrode 11.

上記構成を有する電極において、主電極11は、第3図
および第4図に示されるように、伝熱管4の外表面に対
し一定の距離を置いて対峙してその管軸方向に並設され
ており、分電極12は伝熱管4の軸方向に対して右上
り、または左上りに、同心状に囲繞されている。すなわ
ち、複数の分電極12は主電極11から自由端側に向っ
て漸次上り勾配となるように片持梁状に設けられる。
In the electrode having the above structure, the main electrodes 11 are arranged in parallel in the axial direction of the heat transfer tube 4 so as to face the outer surface of the heat transfer tube 4 at a constant distance, as shown in FIGS. 3 and 4. The distribution electrode 12 is concentrically surrounded by the upper right direction or the upper left direction with respect to the axial direction of the heat transfer tube 4. That is, the plurality of distribution electrodes 12 are provided in the shape of a cantilever so as to have a gradual upward slope from the main electrode 11 toward the free end side.

さて、伝熱管4に被膜する凝縮液を取り除くに当って
は、主電極11と伝熱管12との間に高電圧を印加す
る。すると、伝熱管4の管外表面に発生した凝縮液は、
電位差によって分電極12側に引き寄せられ、引き寄せ
られた凝縮液は分電極12をつたわって重力の作用でポ
ケット部14に案内されて液集合部13に集められる。
このように集められた凝縮液は、一且、液集合部13に
溜められた後、溢液だけが主電極11の外側面をつたわ
って下方に流下する。
Now, in removing the condensate that coats the heat transfer tube 4, a high voltage is applied between the main electrode 11 and the heat transfer tube 12. Then, the condensate generated on the outer surface of the heat transfer tube 4 is
Due to the potential difference, the condensed liquid is attracted to the side of the distribution electrode 12, and the condensate thus drawn is guided by the pocket portion 14 by the action of gravity and collected in the liquid collecting portion 13 by the action of gravity.
The condensate collected in this way is once stored in the liquid collecting section 13, and then only the overflow flows through the outer surface of the main electrode 11 and flows downward.

〔考案の効果〕[Effect of device]

以上説明したように、本考案によれば、電極を主電極と
分電極とからなるツリー状の形状に形成し、その分電極
を自由端側が漸次上り勾配となるように配設して伝熱管
に同心状に囲繞してあるから、伝熱管と電極とはふぞろ
いがなく安定した位置関係が保たれ、一段と良好な凝縮
性能を得ることができる。また、伝熱管の管外表面に発
生した凝縮液は電位差により分電極側に引き寄せられ、
引き寄せられた凝縮液は下り勾配の分電極に沿って重力
の作用でポケット部を経て液集合部に集められる。液集
合部に集められた凝縮液の溢液は主電極の外側面を伝っ
て流下せしめられ、流下液が伝熱管側に飛散するのを未
然に防止しているので、伝熱管の伝熱性能を充分に維持
でき、損うことがない。さらに、1つの伝熱管には1つ
の電極を配設することで足り、複数の電極を配設する必
要がないので、製作コスト、組立工数の面で一段と激減
する等の効果を奏する。
As described above, according to the present invention, an electrode is formed in a tree-like shape including a main electrode and a split electrode, and the split electrode is arranged so that the free end side has a gradual upward slope, and Since the heat transfer tubes and the electrodes are concentrically surrounded by each other, a stable positional relationship between the heat transfer tubes and the electrodes is maintained, and a better condensation performance can be obtained. Further, the condensate generated on the outer surface of the heat transfer tube is attracted to the split electrode side due to the potential difference,
The attracted condensate is collected by the action of gravity along the descending gradient electrode through the pocket portion to the liquid collecting portion. The overflow of the condensate collected in the liquid collecting part is made to flow down along the outer surface of the main electrode, preventing the falling liquid from scattering to the heat transfer tube side, so the heat transfer performance of the heat transfer tube Can be fully maintained and is not damaged. Further, it suffices to dispose one electrode in one heat transfer tube, and it is not necessary to dispose a plurality of electrodes. Therefore, there are effects such as a drastic reduction in manufacturing cost and assembly man-hours.

【図面の簡単な説明】 第1図は本考案の液体引出装置に適用される熱交換器の
一例を示す概略図、第2図は本考案に係る液体引出装置
に用いられる電極の形状を示す模式図、第3図は本考案
の液体引出装置に用いられる伝熱管と電極との組立状態
を示す図、第4図は第3図のIV−IV矢視方向切断断面図
である。 4……伝熱管、11……主電極、12……分電極、13
……液集合部、14……ポケット部。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic view showing an example of a heat exchanger applied to a liquid drawing apparatus of the present invention, and FIG. 2 shows shapes of electrodes used in the liquid drawing apparatus of the present invention. FIG. 3 is a schematic view showing an assembled state of a heat transfer tube and an electrode used in the liquid drawing apparatus of the present invention, and FIG. 4 is a sectional view taken along line IV-IV of FIG. 4 ... Heat transfer tube, 11 ... Main electrode, 12 ... Minute electrode, 13
...... Liquid collecting part, 14 ...... Pocket part.

───────────────────────────────────────────────────── フロントページの続き 審査官 熊谷 繁 (56)参考文献 特開 昭61−295495(JP,A) ─────────────────────────────────────────────────── --Continued from the front page Examiner Shigeru Kumagai (56) References JP-A-61-295495 (JP, A)

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】管外表面に対し一定の間隔をおいて対峙し
て管軸方向に並行な主電極を設け、主電極から樹枝状に
分れた複数の分電極を自由端側が漸次上り勾配となるよ
うに設け、これらの分電極で管外表面を同心状に囲繞す
るとともに、前記主電極から複数の分電極に分かれる各
枝分れの部の下方において、前記主電極にポケット部を
備えた液集合部を設け、上記分電極に引き寄せられた管
外表面からの凝縮液を前記各分電極に沿って重力の作用
でポケット部から液集合部に集め、この液集合部からの
溢液を主電極の外側面に沿って流下させたことを特徴と
する液体引出装置。
1. A main electrode is provided parallel to the outer surface of the tube at a constant interval in parallel with the tube axis direction, and a plurality of branch electrodes branched in a dendritic manner from the main electrode gradually have an upward slope on the free end side. And the outer surface of the tube is concentrically surrounded by these split electrodes, and a pocket portion is provided in the main electrode below each branch portion that divides the main electrode into a plurality of split electrodes. And a condensate from the outer surface of the tube attracted to the distribution electrodes is collected along the distribution electrodes from the pockets to the liquid collection part by the action of gravity. A liquid drawing device characterized in that the liquid flows down along the outer surface of the main electrode.
JP1987106944U 1987-07-14 1987-07-14 Liquid withdrawal device Expired - Lifetime JPH0612392Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1987106944U JPH0612392Y2 (en) 1987-07-14 1987-07-14 Liquid withdrawal device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1987106944U JPH0612392Y2 (en) 1987-07-14 1987-07-14 Liquid withdrawal device

Publications (2)

Publication Number Publication Date
JPS6415094U JPS6415094U (en) 1989-01-25
JPH0612392Y2 true JPH0612392Y2 (en) 1994-03-30

Family

ID=31340904

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1987106944U Expired - Lifetime JPH0612392Y2 (en) 1987-07-14 1987-07-14 Liquid withdrawal device

Country Status (1)

Country Link
JP (1) JPH0612392Y2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61295495A (en) * 1985-06-24 1986-12-26 Toshiba Corp Condensation heat transfer device

Also Published As

Publication number Publication date
JPS6415094U (en) 1989-01-25

Similar Documents

Publication Publication Date Title
SU1269750A3 (en) Air-cooled steam condenser
EP0794401A2 (en) Steam condensing apparatus
CA1053097A (en) Feedwater heater
JPH0612392Y2 (en) Liquid withdrawal device
CN202199148U (en) Novel spiral finned smoke condenser
SU1657891A1 (en) Heat exchanger for latent heat accumulator
CN106382836A (en) Separation type heat pipe bathing wastewater waste heat recovery system and method
JPS6222960A (en) Device for generating process steam by solar energy
CN112624235A (en) Based on thermoelectric type economic benefits and social benefits condensation structure and sea water desalination device
CN220633072U (en) Gas recovery cooling device
CN210862277U (en) Condenser
JPS56119492A (en) Heat exchanger
CN214620142U (en) Strip-shaped heat collector for disc-type heat collecting system
CN211120126U (en) Evaporator
JPH037877B2 (en)
RU2052757C1 (en) Heat exchanger
CN211836322U (en) Multi-position efficient evaporation and condensation equipment
CN218154878U (en) Solar heat storage and heat and cold supply system
CN209941786U (en) Moisture water making system
EP0074384B1 (en) Heat exchanger
CN208253953U (en) A kind of micro-channel heat exchanger and multi-heat source heat pump system
JPS62228895A (en) Heat transfer promoting device using electric field of condensation heat exchanger
JPS608279Y2 (en) solar heat collector
SU1467309A1 (en) Vertical condenser
CN205606929U (en) Superconducting heat pipe structure and solar collector