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JPS6340585B2 - - Google Patents
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JPS6340585B2 - - Google Patents

Info

Publication number
JPS6340585B2
JPS6340585B2 JP16518581A JP16518581A JPS6340585B2 JP S6340585 B2 JPS6340585 B2 JP S6340585B2 JP 16518581 A JP16518581 A JP 16518581A JP 16518581 A JP16518581 A JP 16518581A JP S6340585 B2 JPS6340585 B2 JP S6340585B2
Authority
JP
Japan
Prior art keywords
liquid
dust collector
electrode plate
electrode plates
contact
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
JP16518581A
Other languages
Japanese (ja)
Other versions
JPS5867363A (en
Inventor
Masaaki Kayama
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP56165185A priority Critical patent/JPS5867363A/en
Publication of JPS5867363A publication Critical patent/JPS5867363A/en
Publication of JPS6340585B2 publication Critical patent/JPS6340585B2/ja
Granted legal-status Critical Current

Links

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  • Electrostatic Separation (AREA)

Description

【発明の詳細な説明】 本発明は塵埃などの不純物を含む絶縁油等、液
体の静電式浄液装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an electrostatic liquid purification device for liquids such as insulating oil containing impurities such as dust.

従来のこの種の装置を第1図、第2図および第
3図について説明する。1は浄化される液体2を
収容するタンク、3は金属製の浄化槽である。4
は浄化槽3の下部に取付けた給入管で、浄化槽3
の内部に開口する多数の孔5を有する。6は浄化
槽3に絶縁板7を介して取付けたコ型の高圧側の
電極板、8は浄化槽3と共に対向電極を形成する
アース側の電極板である。9は電極板6,8およ
び浄化槽3の間に介装した多孔性又は繊維質の絶
縁物質よりなる集塵体、10はその支持体であ
る。11は浄化槽3の上部に設けた排出管、12
は蓋板、13はパツキングである。14は浄化槽
3の底部に形成される粗塵の溜り室である。15
はタンク1と給入管4および排出管11とを結合
するホースである。16は高圧側の電極板6と対
向電極(浄化槽3およびアース側の電極板8)と
の間に印加される直流高電圧電源である。
A conventional device of this type will be described with reference to FIGS. 1, 2, and 3. 1 is a tank containing a liquid 2 to be purified, and 3 is a metal septic tank. 4
is the supply pipe installed at the bottom of the septic tank 3.
It has a large number of holes 5 that open into the inside of the tube. 6 is a U-shaped high voltage side electrode plate attached to the septic tank 3 via an insulating plate 7, and 8 is a ground side electrode plate which forms a counter electrode together with the septic tank 3. 9 is a dust collector made of a porous or fibrous insulating material interposed between the electrode plates 6, 8 and the septic tank 3, and 10 is a support thereof. 11 is a discharge pipe installed at the top of the septic tank 3; 12
13 is a lid plate, and 13 is a packing. Reference numeral 14 denotes a coarse dust storage chamber formed at the bottom of the septic tank 3. 15
is a hose that connects the tank 1 with the supply pipe 4 and the discharge pipe 11. 16 is a DC high voltage power supply applied between the electrode plate 6 on the high voltage side and the counter electrode (electrode plate 8 on the septic tank 3 and the ground side).

上記の構成において、塵埃を含む液体2は、タ
ンク1からホース15によつて給入管4に送られ
て孔5から浄化槽3内に入り、粗塵は溜り室14
に沈下し、細塵を含む液体は集塵体9の間を通つ
て上昇する。この間、浄化槽3の内部に形成され
る電界によつて液体中に含まれる細塵は荷電して
電極板6,8又は浄化槽3に吸引され、あるいは
集塵体9によつて捕集される。塵埃の除去された
液体は、排出管11からホース15によつてタン
ク1にもどる。
In the above configuration, the liquid 2 containing dust is sent from the tank 1 to the supply pipe 4 via the hose 15 and enters the septic tank 3 through the hole 5, and the coarse dust is stored in the storage chamber 14.
The liquid containing fine dust rises through the space between the dust collectors 9. During this time, fine dust contained in the liquid is charged by the electric field formed inside the septic tank 3 and is attracted to the electrode plates 6 and 8 or the septic tank 3, or collected by the dust collector 9. The liquid from which dust has been removed returns to the tank 1 from the discharge pipe 11 via the hose 15.

第3図は一電極対の側面断面図であり、電極板
6,8間に集塵体9が流入側から流出側まで均一
に挿入されており、被浄化液体は矢印の方向に進
むように構成されている。
FIG. 3 is a side sectional view of one electrode pair, in which a dust collector 9 is inserted uniformly between the electrode plates 6 and 8 from the inflow side to the outflow side, and the liquid to be purified moves in the direction of the arrow. It is configured.

この従来の構成において、油中の水適のように
不溶性の液体も電極板6,8又は集塵体9に捕集
されると共に凝集し、これが集塵体9の下方に順
次たまつていく。しかし、電極板6,8間に水分
で導通状態が形成されると、電極板6,8間の電
圧は低下し、電界がほとんど形成されなくなり、
浄液効果が無くなる。又高圧電流が流れることに
なり、発熱が非常に大きくなり危険な状態にな
る。このため、高圧過電流防止装置を設けて、一
定以上の電流が流れた場合には、高圧電源を断路
するように構成していた。
In this conventional configuration, insoluble liquids such as water in oil are also collected by the electrode plates 6, 8 or the dust collector 9 and aggregated, which then accumulates below the dust collector 9. . However, when a conductive state is formed between the electrode plates 6 and 8 due to moisture, the voltage between the electrode plates 6 and 8 decreases, and almost no electric field is formed.
The purifying effect will be lost. Also, high voltage current will flow, which will generate a lot of heat, creating a dangerous situation. For this reason, a high-voltage overcurrent prevention device is provided to disconnect the high-voltage power supply when a current exceeding a certain level flows.

本発明はこのような従来の装置を改良するもの
である。
The present invention improves upon such conventional devices.

以下第4図を用いて本発明の一実施例について
説明する。ここで従来と同一部分は同一符号を付
している。電極板6,8間に挿入された多孔性又
は繊維質の絶縁物質より形成された集塵体21は
被浄化液体の流入側が電極板6又は8と接触しな
いよう傾斜面22に構成されている。一方被浄化
液体の流出側は流入側で接触しなかつた電極板6
又は8と接触するように反対側に傾斜面23が構
成されている。
An embodiment of the present invention will be described below with reference to FIG. Here, the same parts as the conventional one are given the same reference numerals. A dust collecting body 21 made of a porous or fibrous insulating material inserted between the electrode plates 6 and 8 has an inclined surface 22 so that the inlet side of the liquid to be purified does not come into contact with the electrode plates 6 or 8. . On the other hand, the outflow side of the liquid to be purified is the electrode plate 6 that did not come in contact with the inflow side.
An inclined surface 23 is configured on the opposite side so as to be in contact with or 8.

この構成において、被浄化液体が流入すると、
油中の水滴のように不溶性導電体の液体は、電極
板6,8及び集塵体21で捕集される。その濃度
は流入側が高く流出側が低い。導電性液体濃度の
高い流入側に、従来例のように多孔性の集塵体を
電極板6及び8に接するように設ければ、電極板
間の導通状態を助長する結果を招くため、本発明
の実施例では一電極板6又は8と接触しないよう
に構成し、捕集された液体が集塵体21の下方に
蓄積されても電極板6,8間は導通状態が起らな
い。又流出側においては、導電性液体が集塵体2
1に接触することなく浄化槽3外に流出すること
のないよう流入側で接触しなかつた電極板6又は
8と集塵体21が接触するよう構成し、被浄化液
体は必ず多孔性の集塵体21を通過させるため高
捕集効率を得ることができる。
In this configuration, when the liquid to be purified flows in,
Insoluble conductive liquid, such as water droplets in oil, is collected by the electrode plates 6 and 8 and the dust collector 21. Its concentration is high on the inflow side and low on the outflow side. If a porous dust collector is provided on the inlet side where the conductive liquid concentration is high so as to be in contact with the electrode plates 6 and 8 as in the conventional example, this will result in promoting electrical conduction between the electrode plates. In the embodiment of the invention, one electrode plate 6 or 8 is configured so as not to come into contact with the other electrode plates 6 or 8, so that even if the collected liquid is accumulated below the dust collector 21, no electrical conduction occurs between the electrode plates 6 and 8. Also, on the outflow side, the conductive liquid flows into the dust collector 2.
In order to prevent the liquid from flowing out of the septic tank 3 without contacting the septic tank 3, the dust collector 21 is configured so that the electrode plate 6 or 8, which did not come in contact on the inflow side, comes into contact with the dust collector 21, and the liquid to be purified is always collected in a porous dust collector. Since it passes through the body 21, high collection efficiency can be obtained.

なお第5図のように、流出部の導電性液体の濃
度によつては、両電極板6,8に接するように集
塵体21を設けても同様の効果を得ることができ
る。
Note that, as shown in FIG. 5, depending on the concentration of the conductive liquid in the outflow portion, the same effect can be obtained even if the dust collector 21 is provided so as to be in contact with both the electrode plates 6 and 8.

また電極板6,8と集塵体21を接触させない
方法として、傾斜面22,23のかわりに絶縁物
で構成したスペーサを用いても同様の効果が得ら
れる。
Furthermore, as a method of preventing the electrode plates 6 and 8 from coming into contact with the dust collector 21, the same effect can be obtained by using spacers made of an insulating material instead of the inclined surfaces 22 and 23.

このように本発明は電極板と集塵体との関連構
成を配慮したことにより、電極板間に高圧電流が
流れる危険が少なく、高捕集効率を得ることがで
きるものである。
In this manner, the present invention takes into consideration the related structure between the electrode plates and the dust collector, thereby reducing the risk of high voltage current flowing between the electrode plates and achieving high collection efficiency.

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

第1図は従来の静電式浄液装置の構成を示す断
面図、第2図は同要部の断面図、第3図は同電極
板部の構成断面図、第4図、第5図はそれぞれ本
発明の実施例を示す電極板部の構成断面図であ
る。 3……浄化槽、6,8……電極板、21……集
塵体。
Figure 1 is a sectional view showing the configuration of a conventional electrostatic liquid purifier, Figure 2 is a sectional view of the main parts, Figure 3 is a sectional view of the electrode plate section, Figures 4 and 5. 2A and 2B are cross-sectional views of the structure of an electrode plate portion showing examples of the present invention, respectively. 3... Septic tank, 6, 8... Electrode plate, 21... Dust collector.

Claims (1)

【特許請求の範囲】[Claims] 1 電界中に被浄化液体を通過させて塵埃及び不
溶性液体を捕集する電極板と、この電極板間に設
けられ、被浄化液体が通過流動する多孔性又は繊
維質で絶縁物質の集塵体とを備え、集塵体の被浄
化液体流入側は、一電極板と接触状態とするとと
もに、他電極板と非接触状態とし、流出側の集塵
体は少なくとも前記他電極板と接触させた静電式
浄液装置。
1. An electrode plate that collects dust and insoluble liquid by passing the liquid to be purified in an electric field, and a porous or fibrous insulating dust collector provided between the electrode plates and through which the liquid to be purified flows. The inflow side of the liquid to be purified of the dust collector is in contact with one electrode plate and in a non-contact state with the other electrode plate, and the dust collector on the outflow side is in contact with at least the other electrode plate. Electrostatic liquid purification device.
JP56165185A 1981-10-15 1981-10-15 Electrostatic liquid purification device Granted JPS5867363A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56165185A JPS5867363A (en) 1981-10-15 1981-10-15 Electrostatic liquid purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56165185A JPS5867363A (en) 1981-10-15 1981-10-15 Electrostatic liquid purification device

Publications (2)

Publication Number Publication Date
JPS5867363A JPS5867363A (en) 1983-04-21
JPS6340585B2 true JPS6340585B2 (en) 1988-08-11

Family

ID=15807452

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56165185A Granted JPS5867363A (en) 1981-10-15 1981-10-15 Electrostatic liquid purification device

Country Status (1)

Country Link
JP (1) JPS5867363A (en)

Also Published As

Publication number Publication date
JPS5867363A (en) 1983-04-21

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