JPS6161864B2 - - Google Patents

Info

Publication number
JPS6161864B2
JPS6161864B2 JP6423281A JP6423281A JPS6161864B2 JP S6161864 B2 JPS6161864 B2 JP S6161864B2 JP 6423281 A JP6423281 A JP 6423281A JP 6423281 A JP6423281 A JP 6423281A JP S6161864 B2 JPS6161864 B2 JP S6161864B2
Authority
JP
Japan
Prior art keywords
dust
ground electrode
filter
charging
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.)
Expired
Application number
JP6423281A
Other languages
Japanese (ja)
Other versions
JPS57180448A (en
Inventor
Keizo Ootsuka
Tsugita Yukitake
Makoto Shimoda
Shoichi Sawahata
Kazuichi Saito
Koichi Nemoto
Hiroshi Asano
Hidetada Tanaka
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.)
Hitachi Plant Technologies Ltd
Original Assignee
Hitachi Plant Technologies 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 Hitachi Plant Technologies Ltd filed Critical Hitachi Plant Technologies Ltd
Priority to JP6423281A priority Critical patent/JPS57180448A/en
Publication of JPS57180448A publication Critical patent/JPS57180448A/en
Publication of JPS6161864B2 publication Critical patent/JPS6161864B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は、集じん装置に係り、特に高抵抗ダス
トを効果的に捕集する静電処理ろ過方式による集
じん装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a dust collector, and particularly to a dust collector using an electrostatic treatment filtration method that effectively collects high-resistance dust.

火力発電用ボイラの燃料は、従来、主に重油が
用いられてきたが、周知の通り、石油事情により
石炭を燃料とする発電プラントが計画されてい
る。この石炭は、重油に比べ燃焼排ガス中のダス
ト量が数100倍と高く、排出規制を満足させるた
めには高性能の集じん装置の設置が必要である。
Conventionally, heavy oil has been mainly used as fuel for boilers for thermal power generation, but as is well known, due to the oil situation, power plants that use coal as fuel are being planned. This coal produces several hundred times more dust in its combustion exhaust gas than heavy oil, and requires the installation of high-performance dust collectors to meet emission regulations.

石炭を燃料とした燃焼排ガス中のダストは、炭
種によつて見掛固有電気抵抗ρ(以下、単にρと
称する)が大幅に異り、その値は1010Ω−cmから
1013Ω−cmに達するものもある。一般の電気集じ
ん装置によつて1012Ω−cmを超えるダストを捕集
しようとすると、逆電離現象を起して集じん率が
著しく低下することがある。この対策として、無
水硫酸(SO3)やスチーム又は水などを添加して
調質することにより、ダストのρを低下させる方
法が一部に実施されてきたが、ランニングコスト
が高く、運転制御が難しいなどの欠点がある。
The apparent specific electrical resistance ρ (hereinafter simply referred to as ρ) of dust in the combustion exhaust gas from coal as fuel varies greatly depending on the type of coal, and its value ranges from 10 Ω-cm to 10 Ω-cm.
Some reach 10 13 Ω-cm. If a general electrostatic precipitator is used to collect dust exceeding 10 12 Ω-cm, a reverse ionization phenomenon may occur and the dust collection rate may drop significantly. As a countermeasure to this problem, some methods have been implemented to reduce the ρ of the dust by adding sulfuric anhydride (SO 3 ), steam, or water to heat it, but this method requires high running costs and requires operational control. It has drawbacks such as being difficult.

ダストのρに全く影響を受けない集じん方式と
して、バグフイルタによるろ過集じん装置があ
る。この装置は、集じん効率は高いが、最大の欠
点は捕集されたダストによつてフイルタの目詰り
が起り、通風損失が上昇することである。フイル
タに捕集されたダストの払い落し方法として、フ
イルタに振動を与えるか又は加圧空気による逆洗
方式が採用されている。この払い落しは運転中ひ
ん繁に行なわれるためフイルタの寿命を短くする
欠点がある。
As a dust collection method that is completely unaffected by the ρ of dust, there is a filtration and dust collection device using a bag filter. Although this device has high dust collection efficiency, its biggest drawback is that the filter is clogged by the collected dust, increasing ventilation loss. As a method of brushing off the dust collected on the filter, a method of applying vibration to the filter or backwashing with pressurized air is adopted. Since this brushing is frequently performed during operation, it has the disadvantage of shortening the life of the filter.

ろ過集じん方式で、フイルタへ導入するダスト
に電荷を与えると、集じん効率は向上しかつ、通
風損失の上昇を無荷電に比べ抑制できることが知
られている。この静電処理ろ過方式によればフイ
ルタの払い落し回数が減り、フイルタの寿命を長
く維持することが可能となる。ダストに電荷を与
える手段は、従来の電気集じん装置の電極構成を
有するコロナ放電によるものであるが、高抵抗ダ
ストを処理する場合には前述の電気集じん装置と
同様に逆電離を起して帯電ダストは中和され、ダ
ストヘ充分に電荷を与えることができないという
欠点がある。
It is known that in the filtration dust collection method, if the dust introduced into the filter is charged, the dust collection efficiency will be improved and the increase in ventilation loss can be suppressed compared to when there is no charge. According to this electrostatic treatment filtration method, the number of times the filter is removed is reduced, and the life of the filter can be maintained for a long time. The means of applying electric charge to dust is by corona discharge, which has the electrode configuration of a conventional electrostatic precipitator, but when processing high-resistance dust, it causes reverse ionization like the electrostatic precipitator described above. The disadvantage is that the charged dust is neutralized and the dust cannot be sufficiently charged.

本発明の目的は、上記した欠点を排除し、通常
のコロナ放電場では逆電離を起す高抵抗ダストで
も充分な電荷を与え、帯電したダストをフイルタ
で捕集する集じん装置を提供するものである。
An object of the present invention is to eliminate the above-mentioned drawbacks, and to provide a dust collection device that provides sufficient charge even to high-resistance dust that causes reverse ionization in a normal corona discharge field, and that collects the charged dust with a filter. be.

すなわち本発明は、ダストに電荷を与える荷電
部と、帯電ダストを捕集するフイルタとを有す
る、いわゆる静電凝集ろ過装置において、荷電部
を構成する接地極の表面に堆積するダスト層の表
面電界強度を空間電界強度以下に保持せしめるも
のである。ダスト層の表面電界強度を所定の値以
下に保持する手段としては、接地極の表面を直接
ブラシや布帛または弾性体などでぬぐつて脱塵す
ることによつて行うことができる。とくに、接地
極を被処理ガスの流れていない領域に移動せしめ
て脱塵すれば、電荷を失つたダストの再飛散も少
なく、また脱塵するための機器配置も容易にな
る。
That is, the present invention provides a so-called electrostatic coagulation filtration device that has a charged part that charges dust and a filter that collects the charged dust. This is to keep the strength below the spatial electric field strength. The surface electric field strength of the dust layer can be maintained below a predetermined value by directly wiping the surface of the ground electrode with a brush, cloth, elastic body, or the like to remove dust. In particular, if the ground electrode is moved to an area where the gas to be treated is not flowing to remove dust, there will be less dust that has lost its charge and it will be less likely to be scattered again, and the equipment for removing dust will be easier to arrange.

以下、本発明に係る集じん装置の原理構成を第
1図の実施例系統図に基づいて詳細に説明する。
1は荷電部で放電極と接地極から構成されてい
る。
Hereinafter, the principle structure of the dust collector according to the present invention will be explained in detail based on the embodiment system diagram shown in FIG.
Reference numeral 1 denotes a charging section, which is composed of a discharge electrode and a ground electrode.

高電圧電源4より放電極に負の直流高電圧を印
加すると接地極と間にコロナ放電が生起し、入口
ダクト5より流入したダストは負に帯電される。
帯電されたダストはバグハウス6に導入されてフ
イルタ7によつて捕捉され、清浄ガスは出口ダク
ト8より排出される。
When a negative DC high voltage is applied to the discharge electrode from the high voltage power supply 4, corona discharge occurs between the discharge electrode and the ground electrode, and the dust flowing in from the inlet duct 5 is negatively charged.
The charged dust is introduced into the baghouse 6 and captured by the filter 7, and the clean gas is discharged from the outlet duct 8.

フイルタ7の材質はガラス、耐熱ナイロン、テ
フロン等の繊維体であつて、排ガス温度に耐うる
ものであれば如何なるものでもよい。フイルタ7
の幾何学的形状は円筒型、平板型など如何なる形
状でもよい。フイルタ7への捕集機構は機械的な
ろ過作用のほかに静電的凝集力によつて捕促され
るもので、従来のフイルタ単独より集じん効率は
高い。また、従来のフイルタ単独に比べ、帯電ダ
ストの捕集における通風損失の上昇を抑制する作
用は、帯電ダストによりフイルタ7の表面電位が
上昇し、導入された帯電ダストがフイルタ表面で
ジヤンピング作用によつて互に凝集し、ダスト層
にボイドが形成されるためと推定される。
The material of the filter 7 may be any fibrous material such as glass, heat-resistant nylon, or Teflon, as long as it can withstand the exhaust gas temperature. Filter 7
The geometrical shape may be any shape such as a cylindrical shape or a flat plate shape. The dust collection mechanism for the filter 7 is one in which dust is collected by electrostatic cohesive force in addition to mechanical filtration, and the dust collection efficiency is higher than that of a conventional filter alone. In addition, compared to a conventional filter alone, the effect of suppressing the increase in ventilation loss when collecting charged dust is that the surface potential of the filter 7 increases due to the charged dust, and the introduced charged dust is caused by a jumping effect on the filter surface. It is presumed that this is because the particles aggregate together and form voids in the dust layer.

いま、第1図において、入口ダクト5より例え
ば1012Ω−cmを超える高抵抗ダストが流入する
と、荷電装置1内のコロナ放電は、接地極に僅か
に捕集されたダスト層によつて逆電離が起り、帯
電ダストの多くは中和され、荷電装置1の効果は
激減する。したがつて、接地極表面を常に清浄に
保つことができれば、高抵抗ダストでも荷電を安
定して継続できる。第2図は、このための移動電
極型帯電部の構造図、第3図は回転電極型の略図
を示す。
Now, in FIG. 1, when high resistance dust exceeding, for example, 10 12 Ω-cm flows in from the inlet duct 5, the corona discharge inside the charging device 1 is reversed by the dust layer slightly collected on the ground electrode. Ionization occurs, much of the charged dust is neutralized, and the effectiveness of the charging device 1 is drastically reduced. Therefore, if the surface of the ground electrode can be kept clean at all times, charging can be maintained stably even with high resistance dust. FIG. 2 shows a structural diagram of a moving electrode type charging section for this purpose, and FIG. 3 shows a schematic diagram of a rotating electrode type charging section.

第2図において、付着ダストの除去機構を説明
する。接地極3は短かい複数の板に分割され、上
下のスプロケツト9,10とリンクチエーン11
によつて駆動され、ローラ12の間を通る間に電
極表面に付着したダストを除去する方式である。
ローラ12は、接地極板の移動方向と逆向きに回
転される。
Referring to FIG. 2, a mechanism for removing attached dust will be explained. The ground electrode 3 is divided into a plurality of short plates, and is connected to the upper and lower sprockets 9 and 10 and the link chain 11.
This is a method in which the dust attached to the electrode surface is removed while the electrode passes between the rollers 12.
The roller 12 is rotated in a direction opposite to the direction of movement of the ground plate.

第3図においては、回転型接地極3に接触して
ブラシ13を配し、上記と同様の効果を得るもの
である。
In FIG. 3, a brush 13 is placed in contact with the rotary ground electrode 3 to obtain the same effect as described above.

荷電装置1における逆電離の発生を防止すべく
接地極3の移動あるいは回転速度は、ダストの電
気抵抗ρと接地極に付着するダスト層の厚さによ
つて異なり、最適値に保つことが必要である。
In order to prevent the occurrence of reverse ionization in the charging device 1, the movement or rotation speed of the ground electrode 3 varies depending on the electrical resistance ρ of the dust and the thickness of the dust layer adhering to the ground electrode, and must be kept at an optimal value. It is.

第1図において、ダスト層表面の電界強度はダ
ストの帯電率を検出するセンサ16、絶縁碍子1
7、帯電率検出器13によつて測定する。荷電装
置1によつて帯電されたダストが静電的誘引力に
よつて帯電率検出センサ16に付着すると、ダス
トがもつ帯電量に応じて、帯電率検出センサ16
の電位は上昇する。この電位は、帯電率検出器1
3でもつて常時計測される。この帯電率検出器1
3からの電位を示す信号は、電位比較器14へ導
びかれ、ここで設定した電位と比較され、その時
の帯電電位の差に相当する信号が、接地極の移動
あるいは回転を制御する制御装置15送られ、接
地極3の移動あるいは回転を最適値に保ち、逆電
離の発生を防止する。
In FIG. 1, the electric field strength on the surface of the dust layer is measured by a sensor 16 that detects the charge rate of the dust, and an insulator 1.
7. Measure by the charge rate detector 13. When the dust charged by the charging device 1 adheres to the charge rate detection sensor 16 due to electrostatic attraction, the charge rate detection sensor 16 changes depending on the amount of charge that the dust has.
The potential of increases. This potential is the charge rate detector 1
3, it is always measured. This charge rate detector 1
The signal indicating the potential from 3 is led to the potential comparator 14, where it is compared with the set potential, and a signal corresponding to the difference in charging potential at that time is sent to a control device that controls the movement or rotation of the ground electrode. 15 is sent to keep the movement or rotation of the ground electrode 3 at an optimal value and prevent the occurrence of back ionization.

帯電率検出センサ16の構造は丸棒、角棒、管
形、金網、多孔板など如何なる形状でもよく、帯
電ダストが通過するダスト内へ設けられている。
帯電率検出器13は静電電位計の如き計測器でも
つて、帯電電位は容易に計測できる。
The structure of the charge rate detection sensor 16 may be any shape such as a round bar, a square bar, a tube shape, a wire mesh, a porous plate, etc., and is provided in the dust through which the charged dust passes.
The charging rate detector 13 can easily measure the charging potential using a measuring instrument such as an electrostatic electrometer.

第4図は、荷電装置の接地極を移動電極型とし
入口ガス温度150℃で、ダストのρが1013Ω−cm
の高抵抗ダストを含むガスを処理した場合の接地
極の移動速度と印加電圧、放電電流及び帯電率検
出器の電位との関係の実験結果を示す。接地極3
を移動しない場合は、いわゆる逆電離を生じ、放
電電流が異状に多く流れる。このとき、接地極を
移動していくと、図に示すように放電電流が減少
していき、ある一定速度以上ではほぼ一定値に近
づく。このような条件下で、ダストの帯電率(電
位)を検出すると、放電電流の変化とほゞ対象的
に変化している。つまり、逆電離が生じている領
域では電位が低いが、正常域になると高い電位を
示している。このように接地極を移動(又は回
転)することにより逆電離を防止でき、しかも、
ダストの帯電率の測定によつて、放電現象の正、
異常を把握できるので、帯電率検出器の信号でも
つて接地極の移動速度を制御することができる。
Figure 4 shows that the ground electrode of the charging device is a moving electrode type, the inlet gas temperature is 150°C, and the dust ρ is 10 13 Ω-cm.
The experimental results of the relationship between the moving speed of the ground electrode, the applied voltage, the discharge current, and the potential of the electrification rate detector are shown when processing a gas containing high-resistance dust. Ground electrode 3
If it is not moved, so-called reverse ionization occurs, and an abnormally large amount of discharge current flows. At this time, as the ground electrode is moved, the discharge current decreases as shown in the figure, and approaches a nearly constant value above a certain speed. When the charge rate (potential) of the dust is detected under such conditions, it changes almost symmetrically with the change in the discharge current. In other words, the potential is low in the region where reverse ionization occurs, but the potential is high in the normal range. By moving (or rotating) the ground electrode in this way, reverse ionization can be prevented, and
By measuring the electrification rate of dust, we can determine whether the discharge phenomenon is positive or not.
Since abnormalities can be detected, the moving speed of the ground electrode can be controlled using the signal from the charge rate detector.

次に第5図は、本発明の他の実施例を示す装置
系統図である。この場合は上記、第4図の説明で
明らかなように、ダストの帯電率と放電電流が密
接な関係にあることに着目し、ダストの帯電率を
一定値に制御する間接的手段として、放電電流を
高電圧電源4Aに設けられた放電電流検出器によ
り検出し、電流比較器14Aと移動制御装置15
を介して接地極3を移動(又は回転)し、前記放
電電流が一定値になるように制御するものであ
る。すなわち、荷電装置を流れる放電電流は、高
電圧電源4Aに設けられた放電電流検出器によつ
て常時監視され、この検出器からの放電電流を示
す信号は、電流比較器14Aへ導びかれ、ここで
設定した電流と比較され、そのときの放電電流の
差に相当した信号が移動制御装置15へ送られ、
該信号に応じた制御用信号が接地極駆動部(図示
せず)へ送られる。
Next, FIG. 5 is an apparatus system diagram showing another embodiment of the present invention. In this case, as is clear from the explanation of Fig. 4 above, focusing on the close relationship between the dust charge rate and the discharge current, discharge The current is detected by a discharge current detector provided in the high voltage power supply 4A, and the current is detected by the current comparator 14A and the movement control device 15.
The ground electrode 3 is moved (or rotated) via the ground electrode 3 to control the discharge current to a constant value. That is, the discharge current flowing through the charging device is constantly monitored by a discharge current detector provided in the high voltage power supply 4A, and a signal indicating the discharge current from this detector is guided to the current comparator 14A. It is compared with the current set here, and a signal corresponding to the difference in discharge current at that time is sent to the movement control device 15,
A control signal corresponding to the signal is sent to a ground electrode drive section (not shown).

上記実施例の場合も第1図の実施例と同様に、
接地極移動速度を適正値に制御し、荷電装置の逆
電離を防止することができる。
In the case of the above embodiment, similarly to the embodiment of FIG.
By controlling the ground electrode moving speed to an appropriate value, it is possible to prevent reverse ionization of the charging device.

以上、本発明によれば、従来、帯電が困難とさ
れている高抵抗ダストを適正な電力でもつて正常
に帯電でき、これに伴なつて、集じん率が高く、
かつ、通風損失の増加を抑制できる優れたろ過集
じん装置を提供できる。
As described above, according to the present invention, high-resistance dust, which has conventionally been considered difficult to charge, can be charged normally with appropriate power, and along with this, the dust collection rate is high,
Moreover, it is possible to provide an excellent filtration and dust collection device that can suppress an increase in ventilation loss.

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

第1図は、本発明の一実施例を示す装置系統
図、第2図は移動電極型帯電部の構造、第3図は
回転電極型帯電部の構造、第4図は、本発明によ
る実験結果の説明図、第5図は本発明の他の実施
例を示す装置系統図である。 1…荷電装置、6…フイルタハウジング、7…
フイルタ、16…帯電率検出センサ。
FIG. 1 is an apparatus system diagram showing an embodiment of the present invention, FIG. 2 is the structure of a moving electrode type charging section, FIG. 3 is the structure of a rotating electrode type charging section, and FIG. 4 is an experiment according to the present invention. An explanatory diagram of the results, FIG. 5 is an apparatus system diagram showing another embodiment of the present invention. DESCRIPTION OF SYMBOLS 1... Charging device, 6... Filter housing, 7...
Filter, 16... Charge rate detection sensor.

Claims (1)

【特許請求の範囲】[Claims] 1 ダストを含む被処理ガスの導入部、該導入部
に接続し、前記ダストを帯電せしめるための放電
極と移動式接地極とを有するダスト荷電部、ダス
ト荷電部の風下側にあつてダストを捕集するフイ
ルタ、清浄ガスの排出部を有するものにおいて、
移動式接地極に摺接されて接地極面からダストを
除去する除去手段と、ダスト荷電部とフイルタと
の間に配置されたダストの帯電率を検知するセン
サ若しくは放電極の放電電流を検知するセンサ
と、センサからの検知量と予め定められた設定値
とを比較する比較器と、比較器からの出力信号に
基づいて接地極の移動速度を制御する制御装置
と、から構成されることを特徴とする集じん装
置。
1. An introduction part for a gas to be processed containing dust, a dust charging part connected to the introduction part and having a discharge electrode and a movable ground electrode for charging the dust, and a dust charging part on the leeward side of the dust charging part. In those having a collecting filter and a clean gas discharge part,
A removal means that is in sliding contact with the movable ground electrode and removes dust from the ground electrode surface, and a sensor that detects the charge rate of the dust or that detects the discharge current of the discharge electrode that is arranged between the dust charging section and the filter. It is composed of a sensor, a comparator that compares the detected amount from the sensor with a predetermined set value, and a control device that controls the moving speed of the ground electrode based on the output signal from the comparator. Characteristic dust collection equipment.
JP6423281A 1981-04-30 1981-04-30 Dust collector Granted JPS57180448A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6423281A JPS57180448A (en) 1981-04-30 1981-04-30 Dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6423281A JPS57180448A (en) 1981-04-30 1981-04-30 Dust collector

Publications (2)

Publication Number Publication Date
JPS57180448A JPS57180448A (en) 1982-11-06
JPS6161864B2 true JPS6161864B2 (en) 1986-12-27

Family

ID=13252164

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6423281A Granted JPS57180448A (en) 1981-04-30 1981-04-30 Dust collector

Country Status (1)

Country Link
JP (1) JPS57180448A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6344467U (en) * 1986-09-09 1988-03-25
CN103084036A (en) * 2013-03-01 2013-05-08 武汉景弘环保科技股份有限公司 Electrostatic reinforcing bag type dust collector with reverse electric field

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62201659A (en) * 1986-02-28 1987-09-05 Hitachi Plant Eng & Constr Co Ltd Moving electrode type electrostatic precipitator
CN103230838B (en) * 2013-04-26 2016-04-20 无锡荣达化工环保设备有限公司 A kind of electrostatic field automatic cleaning apparatus
CN107309087A (en) * 2017-08-10 2017-11-03 环球国合(北京)低碳环保科技有限公司 A kind of electromagnetism ash-cleaning type electric precipitation

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6344467U (en) * 1986-09-09 1988-03-25
CN103084036A (en) * 2013-03-01 2013-05-08 武汉景弘环保科技股份有限公司 Electrostatic reinforcing bag type dust collector with reverse electric field
CN103084036B (en) * 2013-03-01 2014-07-16 武汉景弘环保科技股份有限公司 Electrostatic reinforcing bag type dust collector with reverse electric field

Also Published As

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