JPS6235594B2 - - Google Patents
Info
- Publication number
- JPS6235594B2 JPS6235594B2 JP5306483A JP5306483A JPS6235594B2 JP S6235594 B2 JPS6235594 B2 JP S6235594B2 JP 5306483 A JP5306483 A JP 5306483A JP 5306483 A JP5306483 A JP 5306483A JP S6235594 B2 JPS6235594 B2 JP S6235594B2
- Authority
- JP
- Japan
- Prior art keywords
- tube
- metal wire
- spiral
- heat exchanger
- medium
- 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
Links
- 239000002184 metal Substances 0.000 claims description 20
- 239000007788 liquid Substances 0.000 claims description 5
- 230000005484 gravity Effects 0.000 claims 2
- 238000004804 winding Methods 0.000 claims 1
- 230000002093 peripheral effect Effects 0.000 description 4
- 238000007599 discharging Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- KYKAJFCTULSVSH-UHFFFAOYSA-N chloro(fluoro)methane Chemical group F[C]Cl KYKAJFCTULSVSH-UHFFFAOYSA-N 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/16—Arrangements 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】
本発は凝縮伝熱面に付着した媒体の引出装置の
改良に係り、更に詳しくは縦方向に置かれた凝縮
管の外周面に婦着した媒体を効果的に取り出す装
置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a device for extracting a medium attached to a condensing heat transfer surface, and more specifically, to effectively extracting a medium attached to an outer circumferential surface of a condensing tube placed vertically. Regarding equipment.
凝縮伝熱面に高電圧金属線を対向設置し、伝熱
面に凝縮付着した媒体を金属線に引き寄せるよう
にした熱伝達促進装置は公知である。 2. Description of the Related Art A heat transfer promoting device is known in which high voltage metal wires are installed opposite to a condensing heat transfer surface so that the medium condensed and adhered to the heat transfer surface is drawn to the metal wires.
上記公知の熱伝達促進装置では、金属線へ引き
寄せた媒体を如何に迅速かつ簡単に排出するかが
重要な課題となる。 In the above-mentioned known heat transfer accelerator, an important issue is how quickly and easily the medium drawn to the metal wire can be discharged.
すなわち、媒体を迅速に排出すると伝熱面上に
残留する媒体のフイルム厚みが薄くなり、熱伝達
が促進されるものとなる。 That is, when the medium is quickly discharged, the film thickness of the medium remaining on the heat transfer surface becomes thinner, and heat transfer is promoted.
ところが伝熱面が管であり、管外周面に凝縮付
着した媒体を排出させるには、末だ適当な排出手
段が提供されていない。 However, the heat transfer surface is a tube, and no suitable discharge means has yet been provided to discharge the medium condensed on the outer peripheral surface of the tube.
そこで本発明等は縦置きの伝熱管において、管
外周面の凝縮媒体を効果的に排出する液体引出装
置を既に提案した。 Therefore, the present invention and others have already proposed a liquid drawing device for effectively discharging the condensed medium on the outer circumferential surface of the tube in a vertically placed heat transfer tube.
既提案の液体引出装置は縦置きの伝熱管に電極
となる金属線をスパイラル状に巻回し、金属線に
引き寄せた媒体をスパイラル状に落下させて別置
の縦線へ移し、以つて効率よく排出させんとした
ものである。 In the previously proposed liquid extraction device, a metal wire serving as an electrode is wound in a spiral around a vertically placed heat transfer tube, and the medium drawn by the metal wire is dropped in a spiral shape and transferred to a separate vertical wire, thereby efficiently drawing it out. It was intended to be eliminated.
ところが、上記既提案の一本の金属線では付着
媒体の85%を排出させるのが限界であり、それ以
上の媒体の排出は困難である。 However, the single metal wire proposed above has a limit of discharging 85% of the attached medium, and it is difficult to discharge more than that.
本発明の目的は既提案の装置における金属線の
形状を種々検討し、付着媒体の排出効率の良い引
出装置を提供せんとするにある。 An object of the present invention is to study various shapes of metal wires in previously proposed devices, and to provide a drawing device that is efficient in discharging adhesion media.
以下、図によつて詳細に説明する。 This will be explained in detail below using figures.
第1図は本発明が適用される既提案の凝縮熱交
換器の一例を示す断面図である。第2図は第1図
のA部分の拡大図、第3図は第2図のB−B断面
図である。 FIG. 1 is a sectional view showing an example of a previously proposed condensing heat exchanger to which the present invention is applied. 2 is an enlarged view of portion A in FIG. 1, and FIG. 3 is a sectional view taken along line BB in FIG.
凝縮熱交換器1は上下にヘツダー2,3を有
し、各ヘツダー2,3の間を伝熱管4で連絡して
いる。凝縮さるべき媒体は入口5から入り、ケー
シング6内に充たされている。伝熱管4の外周面
に凝縮付着された媒体はケーシング6の下部で集
合され、出口7から取り出される。媒体を冷却す
る冷媒は入口8から入り、出口9から外部へ流出
する。 The condensing heat exchanger 1 has headers 2 and 3 on the upper and lower sides, and the headers 2 and 3 are connected through heat transfer tubes 4. The medium to be condensed enters through the inlet 5 and fills the casing 6. The medium condensed and deposited on the outer peripheral surface of the heat transfer tube 4 is collected at the lower part of the casing 6 and taken out from the outlet 7. A refrigerant for cooling the medium enters from an inlet 8 and flows out from an outlet 9.
伝熱管4は縦置きとなつており、該伝熱管4と
平行に4本の縦線10が略等位相間隔で伝熱管回
りに設けられている。 The heat exchanger tube 4 is placed vertically, and four vertical lines 10 are provided around the heat exchanger tube in parallel with the heat exchanger tube 4 at approximately equal phase intervals.
縦線10を固定するため、該縦線10に固着さ
れたリング線11が適宜の間隔で上下方向に複数
個設けられている。伝熱管4の回りを巻回し、か
つ下方へ向かつて進行する金属線からなるスパイ
ラル12が設けられる。スパイラル12は縦線1
0に固定され、伝熱管外周面と0.5〜5mm間隙を
持つて対向設置されている。 In order to fix the vertical line 10, a plurality of ring wires 11 fixed to the vertical line 10 are provided in the vertical direction at appropriate intervals. A spiral 12 made of a metal wire is provided that winds around the heat exchanger tube 4 and advances downward. Spiral 12 is vertical line 1
0, and is installed facing the outer peripheral surface of the heat exchanger tube with a gap of 0.5 to 5 mm.
スパイラル12の下端は伝熱管4から少しはな
れて設置された別の縦線13に固定されている。
スパイラル12は伝熱管4の長手方向に所定数取
付けられる。この個数は伝熱管4の長さ及びスパ
イラル長さによつて異なるが、スパイラル12は
480゜巻回され、取付けの間隔50〜60mmとするも
のが一例として上げられる。 The lower end of the spiral 12 is fixed to another vertical wire 13 installed a little apart from the heat exchanger tube 4.
A predetermined number of spirals 12 are attached to the heat exchanger tube 4 in the longitudinal direction. This number varies depending on the length of the heat exchanger tube 4 and the spiral length, but the spiral 12
An example is one that is wound 480 degrees and has an installation interval of 50 to 60 mm.
上記の如く構成された本発明装置では、金属線
からなるスパイラル12が次のように帯状となつ
ている。 In the device of the present invention configured as described above, the spiral 12 made of metal wire is shaped like a band as follows.
第4図のイはスパイラル12が一本の偏平な帯
状金属線で構成されている。伝熱管4に対し偏平
な面が対向することにより、電極面積が増大する
ものとなつている。 In FIG. 4A, the spiral 12 is composed of a single flat metal wire. Since the flat surface faces the heat exchanger tube 4, the electrode area increases.
ロは4本の四形金属線を一列に束ねてスパイラ
ル12を構成したもので、これによつても同様の
効果が得られる。 B is a spiral 12 made by bundling four square metal wires in a row, and the same effect can be obtained with this.
上記の如く構成された本発明の作用は以下のと
おりである。 The operation of the present invention configured as described above is as follows.
先ず第1〜3図を参照して説明する。 First, explanation will be given with reference to FIGS. 1 to 3.
入口5から入つた蒸気は伝熱管4の外周面に凝
縮付着する。スパイラル12は4000V〜15000Vの
高電圧となつており、この電圧は縦線10又は縦
線13を介して印加される。蒸気はフロン、アン
モニア、有機液体などであり、凝縮液はスパイラ
ル12へ引き寄せられる。このため、凝縮液はス
パイラル12に沿つて流下し、スパイラル12の
端部からケーシング6内の底部へ落下する。縦線
13は必らずしも必要なものではないが、スパイ
ラル12の端部から滴下する凝縮液のガイドとし
て設けるものである。 Steam entering from the inlet 5 condenses and adheres to the outer peripheral surface of the heat transfer tube 4. The spiral 12 has a high voltage of 4000V to 15000V, and this voltage is applied via the vertical line 10 or the vertical line 13. The vapor is chlorofluorocarbon, ammonia, organic liquid, etc., and the condensate is drawn to the spiral 12. Therefore, the condensate flows down along the spiral 12 and falls from the end of the spiral 12 to the bottom inside the casing 6. Although the vertical line 13 is not absolutely necessary, it is provided as a guide for the condensate dripping from the end of the spiral 12.
さて、本発明ではスパイラル12が帯状である
ため、第4図のイに示す如く図のQに示す量の液
体が管外周面から引き寄せられるので、一本の金
属線と比べて多量の引き寄せ量となる。すなわ
ち、第4図のロに示す如く一本の金属線の場合、
Q1だけ引き寄せるが、帯状金属とすることによ
りQ2の分だけ引き寄せ量が増加する。 Now, in the present invention, since the spiral 12 is strip-shaped, the amount of liquid shown in Q in the figure is drawn from the outer circumferential surface of the tube as shown in A in FIG. becomes. That is, in the case of a single metal wire as shown in Fig. 4B,
It attracts by Q 1 , but by making it a band-shaped metal, the amount of attraction increases by Q 2 .
なお、帯状金属は短径0.5mm、長径2〜4mmが
望ましいが、この数値に限定されるものではな
い。 In addition, although it is preferable that the short axis of the metal strip is 0.5 mm and the long axis is 2 to 4 mm, it is not limited to these values.
上記本発明によると、95%の媒体の引出しが可
能となり、一本の金属線の場合の85%を大きく上
回る高性能を得た。 According to the present invention, it is possible to draw out 95% of the medium, achieving a high performance that greatly exceeds 85% in the case of a single metal wire.
上述の如く本発明によると、伝熱管外周に付着
した媒体を効率よく引き寄せて排出するので、伝
熱効率の向上、熱交換器の小型化、高性能化を得
ることができるものである。 As described above, according to the present invention, the medium adhering to the outer periphery of the heat exchanger tube is efficiently attracted and discharged, so that it is possible to improve heat transfer efficiency, downsize the heat exchanger, and improve its performance.
第1図は本発明が適用される凝縮熱交換器の一
例を示す略断面図、第2図は第1図のA部拡大
図、第3図は第2図のB−B断面図、第4図の
イ,ロは本発明の一実施例を示す断面図である。
4:伝熱管、10:縦線、12:スパイラル。
Fig. 1 is a schematic sectional view showing an example of a condensing heat exchanger to which the present invention is applied, Fig. 2 is an enlarged view of part A in Fig. 1, and Fig. 3 is a sectional view taken along line BB in Fig. 2; 4A and 4B are cross-sectional views showing one embodiment of the present invention. 4: heat exchanger tube, 10: vertical line, 12: spiral.
Claims (1)
し、管外周面に付着した媒体を金属線へ引き寄せ
るようにした装置において、前記管が少なくとも
重力方向に設けられ、前記金属線が前記管外周に
下方に向かつて進行するスパイラルとして巻回さ
れ、かつ巻回末端でスパイラル半径が増大して管
と同方向に置かれた縦線に連結され、前記金属線
が帯状であつて偏平面が管外周面と対向して設置
されることを特徴とする液体引出装置。1. In an apparatus in which a high-voltage metal wire is arranged opposite to the outer circumferential surface of a tube to draw a medium attached to the outer circumferential surface of the tube toward the metal wire, the tube is provided at least in the direction of gravity, and the metal wire is arranged in the direction of gravity. The metal wire is wound around the outer periphery of the tube as a spiral that progresses downward, and the spiral radius increases at the end of the winding and is connected to a vertical wire placed in the same direction as the tube, and the metal wire is strip-shaped and has a flat surface. A liquid drawing device characterized in that the is installed facing the outer circumferential surface of the pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5306483A JPS59180298A (en) | 1983-03-29 | 1983-03-29 | Liquid draining device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5306483A JPS59180298A (en) | 1983-03-29 | 1983-03-29 | Liquid draining device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59180298A JPS59180298A (en) | 1984-10-13 |
JPS6235594B2 true JPS6235594B2 (en) | 1987-08-03 |
Family
ID=12932402
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5306483A Granted JPS59180298A (en) | 1983-03-29 | 1983-03-29 | Liquid draining device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59180298A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61225589A (en) * | 1985-03-29 | 1986-10-07 | Agency Of Ind Science & Technol | Device to promote transferring of heat |
-
1983
- 1983-03-29 JP JP5306483A patent/JPS59180298A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS59180298A (en) | 1984-10-13 |
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