JPS6122685Y2 - - Google Patents

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Publication number
JPS6122685Y2
JPS6122685Y2 JP1981076343U JP7634381U JPS6122685Y2 JP S6122685 Y2 JPS6122685 Y2 JP S6122685Y2 JP 1981076343 U JP1981076343 U JP 1981076343U JP 7634381 U JP7634381 U JP 7634381U JP S6122685 Y2 JPS6122685 Y2 JP S6122685Y2
Authority
JP
Japan
Prior art keywords
dust collector
positive electrode
liquid
collected
negative 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
JP1981076343U
Other languages
Japanese (ja)
Other versions
JPS57187660U (en
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 filed Critical
Priority to JP1981076343U priority Critical patent/JPS6122685Y2/ja
Publication of JPS57187660U publication Critical patent/JPS57187660U/ja
Application granted granted Critical
Publication of JPS6122685Y2 publication Critical patent/JPS6122685Y2/ja
Expired legal-status Critical Current

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  • Electrostatic Separation (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Description

【考案の詳細な説明】 本考案は油等の絶縁性液体を静電的に浄化する
浄化装置に関し、効率のよい集塵を行うことを目
的とする。
[Detailed Description of the Invention] The present invention relates to a purification device that electrostatically purifies an insulating liquid such as oil, and an object of the present invention is to perform efficient dust collection.

従来の液体の静電浄化装置を第1図により説明
すると、1は油等の絶縁性液体の流入口2と流出
口3とをそれぞれ設けた金属製のケースで、内部
には間に多孔質の集塵体6を介在させた正電極4
と負電極5とが交互に縦に配列してある。7は前
記電極4,5および集塵体6とケース1との間に
設けた絶縁枠である。
A conventional liquid electrostatic purification device is explained with reference to Fig. 1. 1 is a metal case provided with an inlet 2 and an outlet 3 for an insulating liquid such as oil, and a porous case inside. A positive electrode 4 with a dust collector 6 interposed therebetween.
and negative electrodes 5 are alternately arranged vertically. Reference numeral 7 denotes an insulating frame provided between the electrodes 4 and 5, the dust collector 6, and the case 1.

流入口2より流入した液体は電極4,5間の集
塵体6を通過するとき中の不溶解物質が同集塵体
6に静電集塵される。しかし、上記の構成では流
入口2より流入した液体中の微粒子がそのまま集
塵体6に入るため、一回の通過あたりの集塵効率
があまり良好といえず、確実な浄化を行うには時
間をかけて、何回も集塵体を通過させなければな
らなかつた。また、集塵されるほとんどの不溶解
物質がそのままの大きさで集塵される傾向がある
ので、集塵体の大きさが有効に使われず、その寿
命劣化が著しかつた。
When the liquid flowing in from the inlet 2 passes through the dust collector 6 between the electrodes 4 and 5, undissolved substances therein are electrostatically collected on the dust collector 6. However, in the above configuration, the fine particles in the liquid that flowed in from the inlet 2 enter the dust collector 6 as they are, so the dust collection efficiency per pass is not very good, and it takes a long time to perform reliable purification. The dust collector had to be passed through the dust collector several times. Furthermore, since most of the insoluble substances collected tend to be collected in the same size as they are, the size of the dust collecting body is not used effectively, resulting in a significant deterioration of its lifespan.

本考案は上記従来の欠点を解消したもので、以
下その実施例を第2〜3図に基いて説明する。
The present invention eliminates the above-mentioned conventional drawbacks, and examples thereof will be described below with reference to FIGS. 2 and 3.

第2〜3図において、11は油等の絶縁性の液
体の流入口12を下部に、流出口13を上部にそ
れぞれ設けた金属性のケースで、内部に正電極1
4と負電極15とが交互に縦設してあり、さらに
これら両電極14,15間には多孔質の集塵体1
6が介在させてある。また前記電極14,15を
ケース11の底面との間で、しかも流入口12の
下流側に位置して網状をなした透過正電極17が
設けてある。そして前記正電極14、負電極15
及び透過正電極17は絶縁枠18を介してケース
11と絶縁されており、また正電極14と透過正
電極17は高圧電源19のプラス側、負電極15
とケース11はマイナス側に接続され、しかもケ
ース11は接地されている。
In Figures 2 and 3, reference numeral 11 denotes a metal case with an inlet 12 for insulating liquid such as oil at the bottom and an outlet 13 at the top, and a positive electrode 1 inside.
4 and negative electrodes 15 are arranged vertically alternately, and a porous dust collector 1 is arranged between these electrodes 14 and 15.
6 is interposed. Further, a net-shaped transparent positive electrode 17 is provided between the electrodes 14 and 15 and the bottom surface of the case 11, and located on the downstream side of the inlet 12. And the positive electrode 14 and the negative electrode 15
The transparent positive electrode 17 is insulated from the case 11 via the insulating frame 18, and the positive electrode 14 and the transparent positive electrode 17 are connected to the positive side of the high voltage power supply 19 and the negative electrode 15.
The case 11 is connected to the negative side, and the case 11 is grounded.

上記構成において、流入口12より流入した液
体はケース11と両電極14,15との間に入る
が、そこでは第3図のようにプラスに接続された
透過正電極17とマイナスに接続された負電極1
5との間で新たに電界20が発生しており、この
電界20内にある液中の不溶解物質をなす微粒子
21は分極して互いに引き合い凝集粗大化する。
また透過正電極17とケース11の底面が近接し
て強い電界が発生している配置のものではこの間
の微粒子も凝集する。
In the above configuration, the liquid flowing in from the inlet 12 enters between the case 11 and both electrodes 14 and 15, where the transparent positive electrode 17 is connected to the positive electrode and the transparent positive electrode 17 is connected to the negative electrode as shown in FIG. Negative electrode 1
A new electric field 20 is generated between the liquid and the liquid, and the fine particles 21 that are insoluble substances in the liquid within this electric field 20 are polarized and attracted to each other, causing them to aggregate and become coarse.
Furthermore, if the transmitting positive electrode 17 and the bottom surface of the case 11 are located close to each other and a strong electric field is generated, fine particles between them will also aggregate.

さて、電界20で凝集した粒子は負電極15の
付近の集塵体16にほとんど静電集塵され、分極
しなかつた粒子が正電極14の付近の集塵体16
に集塵される傾向になる。このため、集塵体16
の正電極14側にも負電極15側にも比較的均一
に集塵されるものである。
Now, most of the particles that have aggregated in the electric field 20 are electrostatically collected in the dust collector 16 near the negative electrode 15, and the particles that have not been polarized are collected in the dust collector 16 near the positive electrode 14.
dust tends to be collected. For this reason, the dust collector 16
The dust is collected relatively uniformly on both the positive electrode 14 side and the negative electrode 15 side.

なお、集塵体16の密度を不均一にしておく
と、比較的粗い粒子は密度の粗のところで、細い
粒子は密度の高いところでそれぞれ捕集されるよ
うになり、集塵体16を一層効率良く使え、また
圧力損失も小さくできる。
Note that if the density of the dust collector 16 is made non-uniform, relatively coarse particles will be collected in areas with low density, and fine particles will be collected in areas with high density, making the dust collector 16 more efficient. It is easy to use and can reduce pressure loss.

このように本考案によれば、集塵体で集塵する
までに微粒子を分極させて互いに凝集させること
により、集塵体での集塵効率が上がり、従来より
も時間をかけずに液体の確実な浄化が行え、電力
代も小さくて済む。また、集塵体には微粒子ばか
りでなく、比較的粗い粒子が集塵されるところか
ら、その寿命を長くすることもできる。
In this way, according to the present invention, by polarizing the fine particles and coagulating them together before they are collected by the dust collector, the dust collection efficiency of the dust collector increases, and the liquid can be collected in less time than before. Reliable purification can be performed, and electricity costs can be kept low. Furthermore, since the dust collector collects not only fine particles but also relatively coarse particles, its lifespan can be extended.

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

第1図は従来例を示す断面図、第2図は本考案
実施例を示す断面図、第3図は要部拡大断面図で
ある。 12……流入口、14……正電極、15……負
電極、16……集塵体、17……透過正電極。
FIG. 1 is a sectional view showing a conventional example, FIG. 2 is a sectional view showing an embodiment of the present invention, and FIG. 3 is an enlarged sectional view of a main part. 12... Inflow port, 14... Positive electrode, 15... Negative electrode, 16... Dust collector, 17... Transmissive positive electrode.

Claims (1)

【実用新案登録請求の範囲】 (1) 正、負電極間に多孔質の集塵体を介在させた
集塵部と液体の流入口との間に位置し、かつ同
集塵部の液体流入側で、かつ上記負電極と間隔
をおいて対向する通液性の透過正電極を設けた
液体の静電浄化装置。 (2) 集塵体に粗密の密度変化をもたせた実用新案
登録請求の範囲第1項記載の液体の静電浄化装
置。
[Scope of Claim for Utility Model Registration] (1) Located between a dust collection part in which a porous dust collection body is interposed between positive and negative electrodes and a liquid inlet; A liquid electrostatic purification device comprising a liquid permeable positive electrode facing the negative electrode at a distance from the negative electrode. (2) The liquid electrostatic purification device according to claim 1, in which the dust collector has a density change of density.
JP1981076343U 1981-05-26 1981-05-26 Expired JPS6122685Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1981076343U JPS6122685Y2 (en) 1981-05-26 1981-05-26

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1981076343U JPS6122685Y2 (en) 1981-05-26 1981-05-26

Publications (2)

Publication Number Publication Date
JPS57187660U JPS57187660U (en) 1982-11-29
JPS6122685Y2 true JPS6122685Y2 (en) 1986-07-08

Family

ID=29872036

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1981076343U Expired JPS6122685Y2 (en) 1981-05-26 1981-05-26

Country Status (1)

Country Link
JP (1) JPS6122685Y2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50131072U (en) * 1974-04-10 1975-10-28

Also Published As

Publication number Publication date
JPS57187660U (en) 1982-11-29

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