JPH08252479A - Method for electric dust collection and apparatus therefor - Google Patents

Method for electric dust collection and apparatus therefor

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Publication number
JPH08252479A
JPH08252479A JP9579495A JP9579495A JPH08252479A JP H08252479 A JPH08252479 A JP H08252479A JP 9579495 A JP9579495 A JP 9579495A JP 9579495 A JP9579495 A JP 9579495A JP H08252479 A JPH08252479 A JP H08252479A
Authority
JP
Japan
Prior art keywords
dust
dust collecting
collecting electrode
electrode
discharge
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.)
Pending
Application number
JP9579495A
Other languages
Japanese (ja)
Inventor
Ikuo Tochisawa
郁夫 栃澤
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP9579495A priority Critical patent/JPH08252479A/en
Publication of JPH08252479A publication Critical patent/JPH08252479A/en
Pending legal-status Critical Current

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Abstract

PURPOSE: To carry out dust collection work by low electric field strength without efficiency lowering while preventing a reverse electric dissociation phenomenon in the electric collection of dust having a high electric resistance value. CONSTITUTION: The second dust collecting electrode 6 is installed at a position close to a discharge electrode 2 to which direct current high voltage is applied and also close to one or both ends of a grounded main dust collecting electrode 4, to maintain the conductivity of the surface of the electrode 6. In this way, the ionic charge of charged dust accumulated on the main electrode 4 is discharged along the surface of the electrode 6 so that the grounding electric potential of the surface of the electrode 4 is maintained substantially.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は空気中の塵埃の電気集塵
に関するものであり、特に電気抵抗値の高い塵埃の電気
集塵に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to electric dust collection of dust in the air, and more particularly to electric dust dust having a high electric resistance value.

【0002】[0002]

【従来技術と問題点】空気中に浮遊する微細な塵埃を捕
集する方法として、電気集塵が国内外で古くより行われ
ている。
2. Description of the Related Art As a method of collecting fine dust floating in the air, electrostatic dust collection has been performed in Japan and abroad for a long time.

【0003】電気集塵の原理は、広い面積をもち、通常
はアースされた集塵極にたいして、先端が鋭角を形成す
る放電極に、直流高電圧、通常は負極性直流高電圧を印
加し、コロナ放電を発生させ、その中を塵埃を通過させ
る。其の際塵埃は高電圧により、両電極間に生成される
負極性イオンおよび自由電子(以下単にイオンと称す
る)を吸着し負極性に帯電し、クーロン力により強く放
電極に反発し、両電極間を集塵極に向かって飛行し、衝
突付着し、集塵されるものである。それゆえ空気の流れ
または塵埃の進行方向にたいし、直角方向に放電極と集
塵極を配置すれば、生成されたイオンが確実に塵埃と衝
突し、従って均一に帯電する。またその帯電率はイオン
の発生量が多いほど高くなり、従って高い集塵効率を得
ることが出来ることになる。しかるにイオンの発生量
は、電流量が多いほど多く、従って放電極への印加電圧
が高いほどイオン発生量が多くなる。また印加電圧が高
いほど電界強度が強くなり、帯電した塵埃にたいしクー
ロン力が強く働く。すなわち電圧は二重に効果を発揮し
集塵効率を高める。しかし電圧を上げ電界強度を上げ過
ぎるとスパークが発生し、アーク放電となり、均一なコ
ロナ放電が形成されないため、逆に塵埃の帯電率が低下
し、集塵効率が低下するのみならず、大電流が流れ電源
を破壊したり電極を破損したりする。またアーク放電や
スパークが発生しないとしても、電圧を上げ電界強度を
過度に強くすると、空気中のガスが分解し有害なガスが
発生するので、できるだけ低い電界強度で集塵すること
が望まれている。
The principle of electrostatic precipitating is to apply a high DC voltage, usually a negative DC high voltage, to a discharge electrode having a wide area and normally forming a sharp angle with respect to a grounded dust collecting electrode. A corona discharge is generated and dust passes through it. At that time, the dust adsorbs negative ions and free electrons (hereinafter simply referred to as ions) generated between both electrodes due to high voltage and is negatively charged, and strongly repels the discharge electrode due to Coulomb force. It flies toward the dust collecting pole between the two, collides with and adheres to the dust collecting pole. Therefore, if the discharge electrode and the dust collecting electrode are arranged at right angles to the direction of the air flow or the direction of the dust, the generated ions will surely collide with the dust and thus be uniformly charged. Further, the charging rate becomes higher as the amount of generated ions increases, so that high dust collection efficiency can be obtained. However, the amount of generated ions increases as the amount of current increases, and thus the amount of generated ions increases as the voltage applied to the discharge electrode increases. Also, the higher the applied voltage, the stronger the electric field strength, and the stronger the Coulomb force against the charged dust. That is, the voltage exerts a double effect and enhances the dust collection efficiency. However, if the voltage is raised and the electric field strength is raised too much, a spark will be generated, and an arc discharge will not be generated, and a uniform corona discharge will not be formed. Flows, which may damage the power supply or damage the electrodes. Even if arc discharge or spark does not occur, if the voltage is raised and the electric field strength is excessively increased, the gas in the air is decomposed and harmful gas is generated.Therefore, it is desired to collect the dust at the lowest electric field strength. There is.

【0004】ところで集塵極に衝突した塵埃は、吸着し
たイオンの電荷を放出し、クーロン力を失うが、塵埃自
身が電気絶縁性を持っていれば、ファンデアワールス力
による比較的弱い力で集塵極と付着し堆積する。また堆
積した塵埃は電気絶縁性を保有していても、適度の導電
性を持っていれば、塵極表面の極性、すなわちアース電
位を維持するので、負極性に帯電した新しい塵埃が集塵
極に衝突し、放電し、付着できる。それゆえ集塵作業の
進行により、堆積した塵埃は厚みに比例して電気抵抗値
を次第に増大させるが、槌打ちにより塵埃を適宜の時間
間隔で剥離すれば、その導電性を回復し、集塵作業を安
定して継続できることになる。すなわち適度の電気抵抗
値(通常概ね10〜1011Ω−cm)のとき高い電
気集塵効率が得られる。また塵埃相互も上記の適度な電
気抵抗値を保有すれば、ファンデアワールス力で付着
し、その粒径を増大させる。それゆえ集塵操作が進行す
ると、堆積した塵埃粒子の大きさは、衝突前の塵埃の大
きさに比し、数10倍〜数千倍の大きさに成長すること
になる。それゆえ集塵極を塵埃濃度に応じ適宜の頻度、
通常は数分に1回程度の頻度で槌打ちを行えば、堆積し
肥大した塵埃は集塵極から剥離され、風速に打ち勝って
重力により落下するので、サブミクロンの粒子も、集塵
装置の下部に配設されるホッパーに回収することが可能
となる。
By the way, the dust that has collided with the dust collecting electrode releases the electric charge of the adsorbed ions and loses the Coulomb force. However, if the dust itself has an electric insulating property, it is relatively weak due to the Van der Waals force. It adheres to the dust collecting electrode and accumulates. Even if the accumulated dust has electrical insulation, if it has an appropriate conductivity, the polarity of the dust electrode surface, that is, the ground potential is maintained, so that new negatively charged dust collects dust. Can collide with, discharge and attach. Therefore, as the dust collection work progresses, the accumulated dust gradually increases the electric resistance value in proportion to the thickness, but if the dust is peeled off at an appropriate time interval by hammering, its conductivity is recovered and the dust is collected. The work can be continued stably. That is, when the electric resistance value is appropriate (usually approximately 10 4 to 10 11 Ω-cm), high electric dust collection efficiency can be obtained. Further, if each dust has the above-mentioned appropriate electric resistance value, it adheres by the Van der Waals force and increases its particle size. Therefore, as the dust collection operation progresses, the size of the accumulated dust particles grows several tens to several thousand times the size of the dust before the collision. Therefore, the dust collection electrode should be set at an appropriate frequency depending on the dust concentration.
Usually, if hammering is performed once every few minutes, the accumulated and enlarged dust is separated from the dust collecting electrode, overcomes the wind speed and falls due to gravity, so that even sub-micron particles are collected by the dust collector. It is possible to collect the hopper in the lower part.

【0005】しかし電気抵抗値が過度に高い珪酸塩類や
高分子樹脂などの塵埃の場合、塵埃の堆積に伴い集塵極
表面の電気的抵抗値が次第に増大し、衝突した塵埃から
の放電がスムーズに行われなくなる。また集塵極の形状
や、槌打ちの強さ、頻度や方向より、塵埃の剥離が均一
に行われず、集塵極の1部に塵埃の付着しない部分と塵
埃が残留する部分が発生する。この場合塵埃がもつイオ
ン電荷は、剥離した部分や、静電遮蔽され塵埃付着の少
ない面にたいし沿面放電するので、集塵効率は大きく低
下するものの集塵効果が持続される。しかし時間の経過
とともに、それらの部分も絶縁性の高い塵埃で被覆さ
れ、ついには全面的に被覆される。それゆえ集塵極表面
に放電極と極性を等しくする電荷が次第に蓄積され、放
電極と集塵極表面との空間電界強度が低下するため、ほ
とんど放電しなくなり、イオンの発生量が著しく減少す
る。それゆえ帯電しない塵埃が大量に発生し、集塵極に
塵埃が近ずかず、また帯電した1部の塵埃が集塵極に近
ずいても反発され集塵極に衝突しなくなる。それゆえ集
塵効率が大きく低下する。そこで放電極への印加電圧を
上昇させると、集塵極表面での反発力に勝って放電電流
が増加し、堆積が進行する。しかし印加電圧を次第に高
くしていくと、、終に塵埃の保有する電気抵抗にたいし
局部的に破壊電圧を越え、その部分の電気抵抗値が極端
に低下するため、その部分で一種のアーク放電が形成さ
れる。そのため両電極間の電気抵抗値が極端に低下し、
従って通常より大電流が流れるが、コロナ放電が均一に
形成されないため、イオンが塵埃と均一に衝突せず、塵
埃の帯電率が低下し、集塵効率が著しく低下する。また
堆積した塵埃がクーロン力で付着しているため、剥離に
強い衝撃が必要なため、槌打ちにより、塵埃の逃散量が
大きくなり、集塵効率を低下させた。この現象は一般に
逆電離現象と称されていて、上述のごとく電気抵抗値の
大きい塵埃が集塵極全面を被覆し、印加電圧が塵埃の破
壊電圧を局部的に超えたときに発生し、集塵効率を大き
く低下させた。
However, in the case of dust such as silicates or polymer resins having an excessively high electric resistance value, the electric resistance value on the surface of the dust collecting electrode gradually increases as the dust accumulates, and the discharge from the colliding dust is smooth. No longer done. Further, due to the shape of the dust collecting electrode, the strength of hammering, the frequency and the direction, the dust is not evenly peeled off, and a part of the dust collecting electrode where no dust adheres and a part where dust remains remain. In this case, since the ionic charge of the dust discharges along the surface of the separated portion or the surface of the dust that is electrostatically shielded and has little dust adhesion, the dust collection efficiency is greatly reduced, but the dust collection effect is maintained. However, with the lapse of time, those portions are also covered with dust having high insulating properties, and finally covered entirely. Therefore, electric charges having the same polarity as that of the discharge electrode are gradually accumulated on the surface of the dust collecting electrode, and the spatial electric field strength between the discharge electrode and the surface of the dust collecting electrode is reduced. . Therefore, a large amount of uncharged dust is generated, the dust does not approach the dust collecting electrode, and even if a part of the charged dust approaches the dust collecting electrode, it is repelled and does not collide with the dust collecting electrode. Therefore, the dust collection efficiency is greatly reduced. Therefore, when the voltage applied to the discharge electrode is increased, the repulsive force on the surface of the dust collecting electrode is overcome to increase the discharge current and the deposition proceeds. However, when the applied voltage is gradually increased, the electrical resistance of dust finally exceeds the breakdown voltage locally, and the electrical resistance value of that part drops extremely. A discharge is formed. Therefore, the electric resistance value between both electrodes decreases extremely,
Therefore, a larger current than usual flows, but since the corona discharge is not uniformly formed, the ions do not uniformly collide with the dust, the charge rate of the dust is reduced, and the dust collection efficiency is significantly reduced. In addition, since the accumulated dust adheres with Coulomb force, a strong impact is required for peeling, so hammering causes a large amount of dust to escape and reduces dust collection efficiency. This phenomenon is generally called the reverse ionization phenomenon, and as described above, dust with a large electric resistance value covers the entire surface of the dust collecting electrode, and it occurs when the applied voltage locally exceeds the breakdown voltage of the dust. Dust efficiency was greatly reduced.

【0006】それゆえ逆電離現象を防止するため、種々
の方法が試みられている。例えば集塵極の表面に水を流
して、集塵極表面の導電性を維持する方法や、集塵極表
面の塵埃をブラシなどで掻き取る方法などが行われてい
る。これらの方法は逆電離を防止するには効果的である
が、容積効率が悪く装置コストが高価となり、また装置
構造が複雑となるため、メンテナンスコストが高価とな
るのみならず、処理する空気が焼却炉などの高温空気の
場合、適用が困難であった。また放電極に印加する高電
圧波形としては、単なる直流高電圧の他、直流パルス高
電圧や、直流高電圧に直流パルス高電圧を重畳したもの
などが用いられている。放電極にパルス波形電圧を印加
するとアーク放電を形成するのに必要な電界強度が高く
なるので印加最高電圧を高くすることができる。それゆ
え集塵効率の向上効果がある程度得られるものの、その
効果は電源コストの増大に比して小さいのみならず、一
方印加電圧を上げ電界強度を強くし、アーク放電が発生
する電界強度に近ずくと、有害なガスの発生量も著しく
増大するため好ましくない。また塵埃が強いクーロン力
で付着しているため、槌打ちにおいて強い衝撃を与えざ
るを得ず、効率低下を招いていた。
Therefore, various methods have been tried in order to prevent the reverse ionization phenomenon. For example, a method of flowing water on the surface of the dust collecting electrode to maintain the conductivity of the surface of the dust collecting electrode, a method of scraping off the dust on the surface of the dust collecting electrode with a brush or the like are used. Although these methods are effective in preventing reverse ionization, volume efficiency is low and the device cost is high, and the device structure is complicated, so not only maintenance cost is high, but also the air to be processed is In case of high temperature air such as incinerator, it was difficult to apply. Further, as the high voltage waveform applied to the discharge electrode, not only a simple DC high voltage but also a DC pulse high voltage, a DC high voltage superimposed with a DC pulse high voltage, and the like are used. When the pulse waveform voltage is applied to the discharge electrode, the electric field strength required to form the arc discharge increases, so that the maximum applied voltage can be increased. Therefore, although the effect of improving the dust collection efficiency can be obtained to some extent, the effect is not only small in comparison with the increase in the power supply cost, but on the other hand, the applied voltage is increased to increase the electric field strength, and the electric field strength near the arc discharge is generated. If it is removed, the amount of harmful gas generated is significantly increased, which is not preferable. In addition, since the dust adheres with a strong Coulomb force, a strong impact must be given when hammering, resulting in a decrease in efficiency.

【0007】本発明は従来の問題点に鑑みて、電気抵抗
値の高い塵埃を含む空気にも適用して逆電離の発生しな
い、従って特別に電圧を上げなくとも、集塵効率を低下
させない、電気集塵方法と電気集塵装置を提供するもの
である。
In view of the problems of the prior art, the present invention is applied to air containing dust having a high electric resistance value so that reverse ionization does not occur, and therefore the dust collection efficiency is not reduced even if the voltage is not increased specially. An electric dust collecting method and an electric dust collecting apparatus are provided.

【0008】[0008]

【問題を解決する手段】問題解決のために、本発明が提
供する手段は、鉛直方向に配設した放電極に直流高電圧
を印加し、アースした主集塵極を前記放電極に対峙して
鉛直方向に配設して行う電気集塵において、前記主集塵
極の一端または両端の近い位置に、細い線または狭い面
で形成され、アースされた第2集塵極を鉛直方向に配設
し、該第2集塵極の表面の導電性を常に保持して行うこ
とを特徴とするとするものであり、第2集塵極の表面の
塵埃を除去し導電性を保持する手段が、第2集塵極が鉛
直軸回りに回転し、掻き取り機により掻き取るものであ
ることと、固定された第2集塵極表面の塵埃を、鉛直軸
回りに回転する掻き取り機により掻き取るものであるこ
とを含むものである。
In order to solve the problem, the means provided by the present invention is to apply a high DC voltage to a vertically arranged discharge electrode so that a grounded main collecting electrode faces the discharge electrode. In a vertical dust collecting operation, a second dust collecting electrode, which is formed by a thin line or a narrow surface and is grounded, is placed vertically near one or both ends of the main dust collecting electrode. Is provided, and the conductivity of the surface of the second dust collecting electrode is always maintained, and the means for removing the dust on the surface of the second dust collecting electrode to maintain the conductivity is The second dust collecting electrode rotates about the vertical axis and is scraped by a scraper, and the dust on the surface of the fixed second dust collecting electrode is scraped by a scraper rotating about the vertical axis. It includes things that are things.

【0009】[0009]

【作用】上記の手段によれば、主集塵極の端部の近い位
置に導電性を常に維持した第2集塵極が配設されている
ので、主集塵極表面に衝突した電気抵抗値の高い塵埃が
主集塵極の全面を被覆、堆積しても、塵埃に付着したイ
オンの電荷は、沿面放電により第2集塵極に向かって常
に放出される。従って逆電離が発生しない。それゆえ主
集塵極には塵埃がファンデアワールス力による弱い力で
付着し、成長し、堆積する。それゆえ槌打ちにより容易
に剥離落下し、ホッパーに回収される。一方第2集塵極
の表面は掻き取り機などにより、表面の塵埃が除去され
るので、その導電性を失わず、第2集塵極から剥離した
塵埃は、放電極からのイオンにより再帯電し、または帯
電塵埃と衝突、成長し主集塵極に向かう。また第2集塵
極は、主集塵極に比してその面積が小さいので、高い容
積効率の集塵装置が得られる。
According to the above-mentioned means, since the second dust collecting electrode which always maintains the conductivity is arranged near the end of the main dust collecting electrode, the electric resistance which collides with the surface of the main dust collecting electrode. Even if the dust having a high value covers and deposits on the entire surface of the main dust collecting electrode, the electric charges of the ions attached to the dust are always discharged toward the second dust collecting electrode due to the creeping discharge. Therefore, reverse ionization does not occur. Therefore, dust adheres, grows and deposits on the main dust collecting electrode with a weak force due to the Van der Waals force. Therefore, it is easily peeled off and dropped by hammering, and is collected in the hopper. On the other hand, since the dust on the surface of the second dust collecting electrode is removed by a scraper or the like, its conductivity is not lost, and the dust separated from the second dust collecting electrode is recharged by the ions from the discharge electrode. Or collides with charged dust and grows toward the main dust collecting pole. Further, since the area of the second dust collecting electrode is smaller than that of the main dust collecting electrode, a dust collecting device having high volume efficiency can be obtained.

【0010】本発明による第2集塵極の作用につき以下
に実施例に基ずきさらに詳細に説明する。すなわち図1
は本発明において第2集塵極を回転させる実施例を示す
水平断面図であり、図2は掻き取り機を回転させる実施
例を示す水平断面図である。
The operation of the second dust collecting electrode according to the present invention will be described in more detail based on the following examples. That is, FIG.
Is a horizontal sectional view showing an embodiment of rotating the second dust collecting electrode in the present invention, and FIG. 2 is a horizontal sectional view showing an embodiment of rotating the scraping machine.

【0011】[0011]

【実施例】図1、図2において2は放電極であり、4は
主集塵極であり、5は主集塵極4の端部であり、6は第
2集塵極である。また8は掻き取り機であり、集塵装置
10の内部に配設されている。20は直流高電圧電源で
あり、22は空気の流れ方向を示す。
1 and 2, 2 is a discharge electrode, 4 is a main dust collecting electrode, 5 is an end of the main dust collecting electrode 4, and 6 is a second dust collecting electrode. Further, 8 is a scraping machine, which is arranged inside the dust collector 10. Reference numeral 20 is a DC high voltage power supply, and 22 is a flow direction of air.

【0012】放電極2はステンレス線またはピアノ線な
どの細い線で形成され、主集塵極4の面に対峙し配設さ
れている。放電極2の数は処理する空気量に応じて決定
される。また放電極2には直流電源20により負極性直
流高電圧が定法に従って印加される。この場合放電極2
に印加する電圧は特別に高くする必要がなく、コロナ放
電が形成され、スパークが確実に発生しない程度の電界
強度に設定すればよい。また本発明においては、逆電離
が発生しないので、平坦な波形の直流高電圧を印加すれ
ばよいがこれに限定されるものではなく、直流高電圧を
ベース電圧とするパルス高電圧を重畳したパルス高電圧
も用い得る。しかしその場合も、印加する最高電圧によ
って形成される電界強度がスパークを確実に発生しない
強さとするのが、有害物質を発生させないので好まし
い。
The discharge electrode 2 is formed of a thin wire such as a stainless wire or a piano wire, and is disposed so as to face the surface of the main dust collecting electrode 4. The number of discharge electrodes 2 is determined according to the amount of air to be processed. Further, a negative DC high voltage is applied to the discharge electrode 2 by a DC power source 20 according to a standard method. In this case, discharge electrode 2
It is not necessary to particularly increase the voltage applied to the device, and it is sufficient to set the electric field strength to the extent that corona discharge is formed and the spark is not reliably generated. Further, in the present invention, since reverse ionization does not occur, it is sufficient to apply a DC high voltage having a flat waveform, but the present invention is not limited to this, and a pulse in which a pulse high voltage having a DC high voltage as a base voltage is superimposed is superimposed. High voltage may also be used. However, also in that case, it is preferable that the electric field strength formed by the maximum voltage applied is such that sparks are not reliably generated, since harmful substances are not generated.

【0013】主集塵極4は鋼板で形成されアースされ、
空気流れ方向20に平行に、鉛直方向に配設される。主
集塵極4の形状は図1、図2に示す各実施例の他、平板
や、長方形断面が用い得る。いずれの場合も第2集塵極
6に近い部分を先鋭な突端5を具備するように形成すれ
ば、主集塵極4の表面から第2集塵極6への沿面放電が
よりスムーズに行われるので好ましい。主集塵極4の空
気の進行方向の寸法、すなわち長手方向の寸法は、塵埃
濃度や空気量により変えればよいが、通常は放電極との
距離の概ね2倍とすればよいので、高い容積効率が得ら
れる。主集塵極4の数、および放電極2の数は、空気量
や塵埃濃度により、従来通り適宜決定すればよい。また
主集塵極4は図示しない常用の槌打ち装置により、定期
的に、通常は毎分数回の衝撃が与えられ、集塵装置10
の下部に配設された図示しないホッパーにに回収される
が、塵埃はファンデアワールス力で付着しているので、
特別強い衝撃を与える必要がない。またそれゆえ間欠的
な槌打ちの代わりに連続的高速振動または連続的微弱衝
撃を与えることが可能であり、ホッパーに連続的に回収
できる。
The main dust collecting electrode 4 is made of a steel plate and is grounded.
It is arranged in the vertical direction in parallel with the air flow direction 20. The shape of the main dust collecting electrode 4 may be a flat plate or a rectangular cross section in addition to the embodiments shown in FIGS. 1 and 2. In any case, if the portion near the second dust collecting electrode 6 is formed so as to have the sharp tip 5, the creeping discharge from the surface of the main dust collecting electrode 4 to the second dust collecting electrode 6 can be performed more smoothly. It is preferable because it is displayed. The size of the main dust collecting electrode 4 in the air advancing direction, that is, the size in the longitudinal direction may be changed according to the dust concentration and the amount of air, but it is normally about twice the distance from the discharge electrode, and therefore the high volume is high. Efficiency is obtained. The number of main dust collecting electrodes 4 and the number of discharge electrodes 2 may be appropriately determined as in the past depending on the amount of air and the dust concentration. Further, the main dust collecting electrode 4 is regularly and usually impacted several times per minute by a hammering device (not shown), and the dust collecting device 10
Although it is collected in a hopper (not shown) arranged in the lower part of the, since dust is attached by the Van der Waals force,
There is no need to give a particularly strong impact. Therefore, instead of intermittent hammering, continuous high-speed vibration or continuous weak impact can be applied, and the hopper can continuously collect.

【0014】第2集塵極6は導電性材料で形成され、放
電極と平行に主集塵極4の端部5の近い位置に配設され
る。第2集塵極6の数は、放電極1個につき少なくも1
個必要である。その表面の導電性を保持する手段として
は、各種の手段が用い得る。すなわち図1は第2集塵極
6を回転させ、掻き取り機8を固定して第2集塵極6表
面に接触させ塵埃除去する例を示す。この場合第2集塵
極の口径は、回転トルクに耐えるものであればよく特別
に大口径とする必要がない。従って高い容積効率が得ら
れる。また掻き取り機8の接触端には金属製ブラシが埋
め込んであり、確実に塵埃を除去できる。第2集塵極6
には図示しない回転装置により連続的にまたは間欠的に
回転が与えられる。この場合掻き取り機は主集塵極4の
端部5を第2集塵極6と接触させて兼用することも可能
であり、より高い容積効率が得られる。また図2は第2
集塵極6を主集塵極4の端部5と一致させたものであ
り、主集塵極4に比し第2集塵極6の面積が小さいの
で、高い容積効率が得られる。この場合導電性の維持
は、金属製ブラシで形成された掻き取り機8を回転させ
ることにより達成される。第2集塵極6表面の塵埃にた
いする剥離効果は、図1の場合も図2の場合において
も、回転数が大きいほど効果が大きく、通常は1分間に
10回以上必要であり、30〜90回が確実に塵埃を剥
離するので好ましい。また第2集塵極6は、塵埃が掻き
取り機8で常に除去されるのでほとんど堆積しないが、
静電遮蔽材を用いて放電極からの電気力線を遮蔽すれ
ば、さらに確実に塵埃の付着が防止できる。
The second dust collecting electrode 6 is made of a conductive material and is arranged in parallel to the discharge electrode and near the end 5 of the main dust collecting electrode 4. The number of the second dust collecting electrodes 6 is at least 1 for each discharge electrode.
I need one. Various means can be used as means for maintaining the conductivity of the surface. That is, FIG. 1 shows an example in which the second dust collecting electrode 6 is rotated, the scraping machine 8 is fixed, and the second dust collecting electrode 6 is brought into contact with the surface of the second dust collecting electrode 6 to remove dust. In this case, the diameter of the second dust collecting electrode is not limited to a particularly large diameter as long as it can withstand the rotating torque. Therefore, high volume efficiency can be obtained. Further, a metal brush is embedded in the contact end of the scraping machine 8 so that dust can be reliably removed. Second dust collector 6
Is continuously or intermittently rotated by a rotating device (not shown). In this case, the scraper can also use the end part 5 of the main dust collecting electrode 4 by contacting it with the second dust collecting electrode 6, and thus a higher volumetric efficiency can be obtained. 2 is the second
The dust collecting electrode 6 is made to coincide with the end 5 of the main dust collecting electrode 4, and the area of the second dust collecting electrode 6 is smaller than that of the main dust collecting electrode 4, so that high volumetric efficiency can be obtained. In this case, the maintenance of conductivity is achieved by rotating the scraper 8 made of a metal brush. In the case of both FIG. 1 and FIG. 2, the effect of peeling off the dust on the surface of the second dust collecting electrode 6 is greater as the rotation speed is larger, and usually 10 or more times per minute are required. This is preferable because the rotation surely removes dust. Further, the second dust collecting electrode 6 is hardly deposited because the dust is constantly removed by the scraper 8, but
If an electrostatic shield is used to shield the lines of electric force from the discharge electrode, the adhesion of dust can be prevented more reliably.

【0015】第2集塵極6表面に堆積する塵埃を除去す
る手段は、上記に限らず、第2集塵極6を、連続的高速
振動または衝撃により塵埃を剥離してもよい。この場合
第2集塵極6の口径はできるだけ細い方が、付着した塵
埃の剥離が容易なので好ましい。また平板型主集塵極の
端部表面を、上下運動する爪により剥離するものでもよ
い。この場合爪によって剥離された部分が第2集塵極と
なる。さらに塵埃が高分子樹脂類などの場合、圧縮エア
ーによるエアーブローを用いることも可能である。
The means for removing dust accumulated on the surface of the second dust collecting electrode 6 is not limited to the above, and the second dust collecting electrode 6 may be peeled off by continuous high-speed vibration or impact. In this case, it is preferable that the diameter of the second dust collecting electrode 6 is as small as possible, because the attached dust can be easily separated. Alternatively, the end surface of the flat plate-type main dust collecting electrode may be peeled off by a claw that moves up and down. In this case, the portion separated by the claw becomes the second dust collecting electrode. Further, when the dust is polymer resin or the like, it is also possible to use air blow with compressed air.

【0016】本発明においては、主集塵極4の表面を絶
縁材料で被覆してもよく、逆電離現象が発生しないのみ
ならず、第2集塵極6を主集塵極4と離設して、電気抵
抗値の低い塵埃を集塵した場合、ジャンピング現象が発
生しない。それゆえ電気抵抗値の高い塵埃と低い塵埃を
同時にまたは交互に集塵する場合や、集塵作業中に塵埃
の抵抗値が大きく変化する場合、ジャンピング現象も逆
電離現象も発生しないので高い集塵効率が得られる。
In the present invention, the surface of the main dust collecting electrode 4 may be covered with an insulating material so that the reverse ionization phenomenon does not occur, and the second dust collecting electrode 6 is separated from the main dust collecting electrode 4. Then, when dust having a low electric resistance value is collected, the jumping phenomenon does not occur. Therefore, when dust with a high electric resistance value and dust with a low electric resistance value are collected simultaneously or alternately, or when the resistance value of the dust changes significantly during the dust collection work, neither jumping nor reverse ionization phenomenon occurs, so high dust collection Efficiency is obtained.

【0017】[0017]

【発明の効果】本発明によれば、第2集塵極6の表面が
導電性を常に保持し、主集塵極4の表面に堆積する塵埃
のイオンからの電荷を沿面放電により吸収するので逆電
離現象が発生しない。それゆえ集塵効率が大幅に向上す
る。しかも放電極2への印加電圧はコロナ放電を生成す
る程度の電界強度とし、スパークが確実に発生しない程
度の強さにするのみであるから、有害なガスが発生しな
い。また第2集塵極の面積が主集塵極に比して小さいの
で、高い容積効率の電気集塵装置が得られる。
According to the present invention, the surface of the second dust collecting electrode 6 always maintains conductivity, and the charges from the ions of the dust accumulated on the surface of the main dust collecting electrode 4 are absorbed by the creeping discharge. Reverse ionization phenomenon does not occur. Therefore, the dust collection efficiency is significantly improved. Moreover, since the voltage applied to the discharge electrode 2 is set so that the electric field strength is such that corona discharge is generated and the spark is not reliably generated, no harmful gas is generated. Further, since the area of the second dust collecting electrode is smaller than that of the main dust collecting electrode, a high volume efficiency electrostatic precipitator can be obtained.

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

【図1】第2集塵極を回転する実施例を示す図FIG. 1 is a diagram showing an embodiment in which a second dust collecting electrode is rotated.

【図2】掻き取り機を回転式とする実施例を示す図FIG. 2 is a diagram showing an embodiment in which the scraper is a rotary type.

【符号の説明】[Explanation of symbols]

2、放電極 4、主集塵極 5、主集塵極端部 6、第2集塵極 8、掻き取り機 2, discharge electrode 4, main dust collecting electrode 5, main dust collecting extreme part 6, second dust collecting electrode 8, scraper

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 鉛直方向に配設した放電極に直流高電圧
を印加し,アースした主集塵極を前記放電極に対峙して
鉛直方向に配設して行う電気集塵において、前記主集塵
極の一端または両端の近い位置に、細い線または狭い面
で形成され、アースされた第2集塵極を鉛直方向に配設
し、該第2集塵極の表面の導電性を常に保持して行うこ
とを特徴とする電気集塵方法
1. An electrostatic precipitator in which a DC high voltage is applied to a vertically arranged discharge electrode and a grounded main dust collecting electrode is arranged vertically in opposition to the discharge electrode. The second dust collecting electrode, which is formed by a thin line or a narrow surface and is grounded, is vertically arranged near one or both ends of the dust collecting electrode, and the conductivity of the surface of the second dust collecting electrode is always maintained. An electrostatic precipitating method characterized by being held
【請求項2】 アースされる主集塵極、直流高電圧が印
加される放電極と、前記主集塵極の一端または両端の近
い位置に配設され、アースされる第2集塵極および、該
第2集塵極の表面に付着した塵埃の除去手段を具備する
電気集塵装置
2. A main dust collecting electrode that is grounded, a discharge electrode to which a high DC voltage is applied, and a second dust collecting electrode that is arranged near one or both ends of the main dust collecting electrode and is grounded. An electrostatic precipitator comprising means for removing dust adhering to the surface of the second dust collector
【請求項3】第2集塵極の表面の塵埃を除去する手段
が、第2集塵極が鉛直軸回りに回転し、掻き取り機によ
り掻き取るものであることを特徴とする請求項2に記載
の電気集塵装置
3. The means for removing dust on the surface of the second dust collecting electrode is characterized in that the second dust collecting electrode rotates around a vertical axis and is scraped by a scraping machine. Electrostatic precipitator described in
【請求項4】第2集塵極の表面の塵埃を除去する手段
が、固定された2集塵極表面の塵埃を、鉛直軸回りに回
転する掻き取り機により掻き取るものであることを特徴
とする請求項2に記載の電気集塵装置
4. The means for removing the dust on the surface of the second dust collecting electrode scrapes off the dust on the surface of the fixed second dust collecting electrode by a scraping machine which rotates around a vertical axis. The electrostatic precipitator according to claim 2.
JP9579495A 1995-03-15 1995-03-15 Method for electric dust collection and apparatus therefor Pending JPH08252479A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9579495A JPH08252479A (en) 1995-03-15 1995-03-15 Method for electric dust collection and apparatus therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9579495A JPH08252479A (en) 1995-03-15 1995-03-15 Method for electric dust collection and apparatus therefor

Publications (1)

Publication Number Publication Date
JPH08252479A true JPH08252479A (en) 1996-10-01

Family

ID=14147361

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9579495A Pending JPH08252479A (en) 1995-03-15 1995-03-15 Method for electric dust collection and apparatus therefor

Country Status (1)

Country Link
JP (1) JPH08252479A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100403015B1 (en) * 2001-02-16 2003-10-23 히다찌 플랜트 겐세쓰 가부시키가이샤 Earth device in movable electrode type electric dust collector
KR101456899B1 (en) * 2013-09-25 2014-10-31 (주)에코솔루텍 Wet Electrostatic Precipitator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100403015B1 (en) * 2001-02-16 2003-10-23 히다찌 플랜트 겐세쓰 가부시키가이샤 Earth device in movable electrode type electric dust collector
KR101456899B1 (en) * 2013-09-25 2014-10-31 (주)에코솔루텍 Wet Electrostatic Precipitator

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