JP2959190B2 - Dust removal method of electric precipitator for motorway tunnel - Google Patents

Dust removal method of electric precipitator for motorway tunnel

Info

Publication number
JP2959190B2
JP2959190B2 JP14796891A JP14796891A JP2959190B2 JP 2959190 B2 JP2959190 B2 JP 2959190B2 JP 14796891 A JP14796891 A JP 14796891A JP 14796891 A JP14796891 A JP 14796891A JP 2959190 B2 JP2959190 B2 JP 2959190B2
Authority
JP
Japan
Prior art keywords
dust
electric
collection rate
dust collection
particle size
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 - Fee Related
Application number
JP14796891A
Other languages
Japanese (ja)
Other versions
JPH04346852A (en
Inventor
昌広 宮本
和照 新貝
義弘 蓑輪
武男 高橋
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP14796891A priority Critical patent/JP2959190B2/en
Publication of JPH04346852A publication Critical patent/JPH04346852A/en
Application granted granted Critical
Publication of JP2959190B2 publication Critical patent/JP2959190B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Electrostatic Separation (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、自動車道トンネル内
の空気を清浄化する電気集じん機の粉じん除去方法に関
し、詳しくは電気集じん機の集じん電極に捕集された粉
じんを除去する時期の到来を判定する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for removing dust from an electric dust collector for purifying air in a motorway tunnel, and more particularly, to removing dust collected on a dust collecting electrode of the electric dust collector. The present invention relates to a method for determining the arrival of time.

【0002】[0002]

【従来の技術】図2は自動車道トンネル内の空気を清浄
化する電気集じん機の概略縦断面図、図3はその集じん
ユニットの拡大正面図である。図において、1は図示し
ない自動車道トンネルに通じるバイパス通路で、電気集
じん機はこのバイパス通路1内に設置されている。3は
電気集じん機のケーシング、2はケーシング3の後端部
に設けられた送風機で、送風機2によってバイパス通路
1内に吸い込まれたトンネル内汚染空気Aはケーシング
3内に導かれ、清浄空気A’となってケーシング3の後
端から再びバイパス通路1を通してトンネル内に戻され
る。
2. Description of the Related Art FIG. 2 is a schematic longitudinal sectional view of an electric precipitator for purifying air in a motorway tunnel, and FIG. 3 is an enlarged front view of the precipitator. In the figure, reference numeral 1 denotes a bypass passage leading to a motorway tunnel (not shown), and an electric precipitator is installed in the bypass passage 1. Reference numeral 3 denotes a casing of the electric precipitator, and reference numeral 2 denotes a blower provided at a rear end of the casing 3. A 'is returned to the tunnel from the rear end of the casing 3 through the bypass passage 1 again.

【0003】8はケーシング3内に設けられた集じんユ
ニットで、図3に示すように交互に配置された複数枚の
接地電極板20及び高電圧電極板21からなる集じん電
極を有している。高電圧電極板21には電源6から高電
圧が印加される。7は帯電ユニットで、集じんユニット
8の上流側に配置されている。9はエアブローノズル
で、集じんユニット8の下流側に配置され、エアブロー
ライン11を介してコンプレッサ10から供給される圧
縮空気を集じんユニット8に向かって噴射し、集じん電
極20,21に捕集された粉じんをケーシング3内に吹
き落として除去する。吹き落とされた粉じんはケーシン
グ3の底部の排出プレナム12からダスト回収ライン1
4を介してダスト分離回収器13に回収される。4及び
5はケーシング3の先端開口及び後端開口をそれぞれ開
閉するためのダンパで、集じん時には開き、ダストの回
収時には閉じる。
[0003] Reference numeral 8 denotes a dust collecting unit provided in the casing 3, which has dust collecting electrodes composed of a plurality of ground electrode plates 20 and high voltage electrode plates 21 which are alternately arranged as shown in FIG. 3. I have. A high voltage is applied to the high voltage electrode plate 21 from the power supply 6. Reference numeral 7 denotes a charging unit, which is arranged on the upstream side of the dust collection unit 8. Reference numeral 9 denotes an air blow nozzle, which is disposed downstream of the dust collecting unit 8, injects compressed air supplied from the compressor 10 through the air blow line 11 toward the dust collecting unit 8, and captures the dust on the dust collecting electrodes 20 and 21. The collected dust is blown down into the casing 3 and removed. The blown-down dust passes from a discharge plenum 12 at the bottom of the casing 3 to a dust collection line 1.
4 and collected by the dust separation and collection device 13. Dampers 4 and 5 for opening and closing the front and rear openings of the casing 3, respectively, open when collecting dust and close when collecting dust.

【0004】図3に示すように、接地電極板20は集じ
んユニット8の枠体19に支持され、高電圧電極板21
は高電圧電極18に固定されている。高電圧電極18は
電極支持棒16に固定され、電極支持棒16は絶縁碍子
15に固定されている。更に、絶縁碍子15は枠体19
に固定された取付台17に固定されている。なお、エア
ブローライン11からの圧縮空気は絶縁碍子15にも噴
射され、そこに堆積した粉じんを吹き落とす。
As shown in FIG. 3, a ground electrode plate 20 is supported by a frame 19 of a dust collecting unit 8 and a high voltage electrode plate 21 is provided.
Are fixed to the high voltage electrode 18. The high-voltage electrode 18 is fixed to the electrode support bar 16, and the electrode support bar 16 is fixed to the insulator 15. Further, the insulator 15 is provided with a frame 19.
Is fixed to a mounting table 17 fixed to the mounting table 17. The compressed air from the air blow line 11 is also injected into the insulator 15 to blow off the dust accumulated there.

【0005】[0005]

【発明が解決しようとする課題】このような構成の電気
集じん機において、集じん電極20,21に捕集された
粉じん量が一定の限界値を超えると、捕集された粉じん
が空中に飛散するいわゆる再飛散現象が発生し、集じん
率が低下する。そのため、連続運転する場合には運転途
中において集じん電極に捕集された粉じんの除去を行
う。その場合、従来は一般に長時間タイマの採用により
適当と考えられる一定の運転時間を計測し、その運転時
間の経過ごとに粉じんの除去を行っていた。
When the amount of dust collected by the dust collecting electrodes 20 and 21 exceeds a certain limit value in the electric dust collector having such a configuration, the collected dust is left in the air. The so-called re-scattering phenomenon of scattering occurs, and the dust collection rate decreases. Therefore, in the case of continuous operation, the dust collected on the dust collecting electrode is removed during the operation. In that case, conventionally, a constant operation time considered appropriate by using a long time timer is generally measured, and dust is removed each time the operation time elapses.

【0006】しかしながら、集じん電極での粉じんの堆
積状況はトンネル内交通量や気象条件などによるトンネ
ル内空気の汚染程度に影響され、一定時間ごとに機械的
に粉じん除去を行う従来方法では適切なタイミングを得
ることが困難であった。そこで、この発明は、集じん電
極での現実の粉じん堆積状態に合わせて、適切なタイミ
ングで粉じんの除去を行い、電気集じん機の運転効率を
高めることのできる自動車道トンネル用電気集じん機の
粉じん除去方法を提供することを目的とするものであ
る。
However, the state of dust accumulation at the dust collecting electrode is affected by the degree of contamination of the air in the tunnel due to traffic volume in the tunnel, weather conditions, and the like, and is not suitable for the conventional method of mechanically removing dust at regular intervals. It was difficult to get the timing. Therefore, the present invention provides an electric dust collector for a motorway tunnel that can remove dust at an appropriate timing in accordance with the actual dust accumulation state at the dust collecting electrode and can increase the operation efficiency of the electric dust collector. It is an object of the present invention to provide a method for removing dust.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
に、この発明は、電気集じん機の集じん率を粉じんの粒
径別に求め、その結果から粉じんの除去を行う時期を判
定するものとする。その際、粒径があるレベル以上の粉
じんの集じん率が極端に悪化した時点で粉じんを除去す
るのがよい。
SUMMARY OF THE INVENTION In order to achieve the above object, the present invention obtains the dust collection rate of an electric dust collector for each particle size of the dust, and determines the time to remove the dust from the result. And At this time, it is preferable to remove the dust when the dust collection rate of the dust having a particle size of a certain level or more extremely deteriorates.

【0008】[0008]

【作用】電気集じん機の集じん率は集じん電極に粉じん
が堆積するに従って次第に低下するが、特に粉じん量が
一定の限界値を超えるとすでに述べた再飛散現象により
集じん率が著しく低下する。したがって、集じん率の推
移を観測し、集じん率が大きく低下した時点を選んで堆
積した粉じんの除去を行うようにすれば、電気集じん機
の運転条件に左右されない適切な清掃のタイミングを得
ることができる。
[Effect] The dust collection rate of the electric dust collector gradually decreases as the dust accumulates on the dust collection electrode. However, especially when the dust amount exceeds a certain limit value, the dust collection rate is significantly reduced due to the re-scattering phenomenon described above. I do. Therefore, by observing the change in the dust collection rate and selecting the point at which the dust collection rate greatly decreases to remove the accumulated dust, it is possible to set an appropriate cleaning timing that is not affected by the operating conditions of the electric dust collector. Obtainable.

【0009】ところで、自動車道トンネル用の電気集じ
ん機の集じん率は一般に質量濃度に基づいて算出されて
おり、この集じん率の目標を例えば80%に置き、これ
が例えば60%以下に低下した場合にはなんらかの処置
を行うようにしている。しかしながら、このような集じ
ん率を目安に集じん電極の清掃を行うと、比較的重量の
大きい、換言すれば粒径の大きい粉じんの捕集がある程
度達成されている内は集じん率が見掛け上良くなるた
め、清掃のタイミングが遅れてしまう可能性がある。ち
なみに、自動車道トンネル内の空気中の粉じんは粒径が
0.3μm以下の微小粒子が多数を占めていることが知ら
れているが、電気集じん機は粉じんの堆積により微小粒
径範囲での捕集性能が特に悪化する。その場合、質量濃
度による集じん率はそれほど低下しないが、微小粉じん
の飛散は空気浄化の観点からは好ましいことではない。
By the way, the dust collection rate of an electric dust collector for a motorway tunnel is generally calculated based on the mass concentration. The target of this dust collection rate is set to, for example, 80%, and this is reduced to, for example, 60% or less. If they do, they take some action. However, if the dust collection electrode is cleaned with such a dust collection rate as a guide, the dust collection rate becomes apparent while the collection of relatively heavy dust, in other words, dust having a large particle diameter, is achieved to some extent. Since the cleaning time is improved, the cleaning timing may be delayed. By the way, the particle size of the dust in the air inside the motorway tunnel is
It is known that a large number of fine particles having a size of 0.3 μm or less occupy a large number. However, the collection performance of the electrostatic precipitator in the fine particle size range is particularly deteriorated due to accumulation of dust. In that case, the dust collection rate by the mass concentration does not decrease so much, but scattering of fine dust is not preferable from the viewpoint of air purification.

【0010】そこで、発明者等は個数濃度に基づく集じ
ん率の変化から集じん電極の粉じんを除去すべき時期を
判定する方法について実験を繰り返した。その結果、集
じん電極に粉じんが次第に堆積し、その量が一定の限界
値を超えると、粒径があるレベル、例えば1μm以上の
粉じんの集じん率が極端に低下し、実験条件によっては
集じん率が見掛け上零、あるいはマイナスになるという
現象が生じることを見出した。その場合、すでに述べた
質量濃度による集じん率は所定値以上の値を示している
ことが多い。
Therefore, the inventors repeated experiments on a method of determining a time to remove dust from the dust collecting electrode from a change in the dust collecting rate based on the number concentration. As a result, the dust gradually accumulates on the dust collecting electrode, and when the amount exceeds a certain limit value, the dust collection rate of the dust having a certain particle size, for example, 1 μm or more, is extremely reduced, and depending on the experimental conditions, the dust collecting rate is extremely low. It has been found that a phenomenon in which the rejection rate is apparently zero or negative occurs. In that case, the dust collection rate based on the mass concentration described above often indicates a value equal to or higher than a predetermined value.

【0011】上記現象は更に考察したところによれば、
以下の原因によるものと確認された。すなわち、集じん
電極の粉じん量が一定の限界値を超えると各粒径につい
て全般に集じん能力が低下するが、特に低下の程度が大
きい粒径1μm以下の微小粉じんは、集じん電極を通過
して電気集じん機から排出される過程でいくつかの粉じ
ん粒子が集合する、いわゆる凝集現象をきたし、その等
価粒径が元の粒径よりも大きくなる。そのため、電気集
じん機の下流側における粒径1μm以上の個数濃度が大
きくなり、集じん率が見掛け上極端に低下するのであ
る。
The above phenomenon has been further considered,
The following causes were confirmed. That is, when the dust amount of the dust collecting electrode exceeds a certain limit value, the dust collecting ability generally decreases for each particle size, and particularly, the fine dust having a large degree of decrease of 1 μm or less passes through the dust collecting electrode. In the process of being discharged from the electrostatic precipitator, a so-called agglomeration phenomenon occurs in which some dust particles are aggregated, and the equivalent particle size becomes larger than the original particle size. For this reason, the number concentration having a particle diameter of 1 μm or more on the downstream side of the electric dust collector increases, and the dust collection rate apparently decreases extremely.

【0012】また、凝集した微小粒子群は粒径が小さい
ことから重量がそれほどなく、質量濃度による集じん率
は直ちには低下しない。なお、個数濃度により集じん率
の変化を観測する場合に全粒度範囲をまとめて測定する
と、微小粒子の上記凝集により全体の粉じん個数自体は
大きく減少するため、見掛け上集じん率が高くなる。し
たがって、粒径別に個数濃度を測定し、あるレベル以上
の粒径の集じん率をチェックしなければならない。
Further, the aggregated fine particles are small in weight because of their small particle size, and the dust collection rate by mass concentration does not immediately decrease. When the change in the dust collection rate is observed depending on the number concentration, when the entire particle size range is measured collectively, the total dust count itself is greatly reduced due to the aggregation of the fine particles, so that the apparent dust collection rate is increased. Therefore, it is necessary to measure the number concentration for each particle size and check the dust collection rate of a certain size or more.

【0013】[0013]

【実施例】以下、図1に基づいてこの発明の実施例を説
明する。なお、従来例と同一する部分には同一の符号を
付け説明を省略する。図において、電気集じん機から排
出された空気中の粉じん量を粒径ごとに測定するため
に、送風機2の後段にパーティクルカウンタ22の粉じ
ん吸引口23が配置されている。パーティクルカウンタ
22はよく知られるように、空気中に浮遊している粒子
の個数濃度を光散乱方式により浮遊状態のまま測定し、
粒径別に粒子数を計数する機能を持つ装置であり、例え
ば 0.3〜0.5 、 0.5〜1、1〜2、2〜5μmの粒径範
囲別に単位体積空気中の粒子数をカウントできる。
An embodiment of the present invention will be described below with reference to FIG. The same parts as those in the conventional example are denoted by the same reference numerals, and description thereof will be omitted. In the figure, a dust suction port 23 of a particle counter 22 is disposed at a stage subsequent to the blower 2 in order to measure the amount of dust in the air discharged from the electric dust collector for each particle size. As is well known, the particle counter 22 measures the number concentration of particles floating in the air in a floating state by a light scattering method,
This is a device having a function of counting the number of particles for each particle size. For example, the number of particles in unit volume air can be counted for each particle size range of 0.3 to 0.5, 0.5 to 1, 1-2, and 2 to 5 μm.

【0014】パーティクルカウンタ22自体の吸引力は
一般に弱く、通常5〜7m/sである自動車道トンネル
用電気集じん機の風速では直接吸引できないため、サン
プリングホース24を用いて別のポンプ25でデシケー
タ26まで吸引し、デシケータ26内の粉じんをパーテ
ィクルカウンタ22で測定する構成としている。集じん
率を算出するためには集じん前の空気中の粉じんの個数
濃度を測定する必要があるが、図示実施例ではパーティ
クルカウンタ22を電気集じん機の後段にのみ設置し、
集じん前の測定は帯電ユニット7及び集じんユニット8
への電圧印加を停止して行うようにしている。もちろ
ん、パーティクルカウンタを電気集じん機の前段に別途
設置してもよい。
The suction force of the particle counter 22 itself is generally weak, and cannot be directly sucked by the wind speed of an electric precipitator for a motorway tunnel, which is usually 5 to 7 m / s, so that a desiccator is used by another pump 25 using a sampling hose 24. , And the dust in the desiccator 26 is measured by the particle counter 22. In order to calculate the dust collection rate, it is necessary to measure the number concentration of dust in the air before dust collection, but in the illustrated embodiment, the particle counter 22 is installed only at the subsequent stage of the electric dust collector,
The measurement before dust collection is performed by the charging unit 7 and the dust collection unit 8
The application of the voltage is stopped. Needless to say, a particle counter may be separately installed in front of the electric precipitator.

【0015】このような構成の下で、電気集じん機によ
る集じんの前後の粉じんの個数濃度を粒径別に測定し、
例えば粒径1μm以上の粉じんの集じん率が極端に低下
する現象を捕捉する。ここで、極端な低下とは集じん率
が零かそれに近く、あるいはマイナスになるような場合
を意味する。このような現象が発生した場合には、すで
に述べたように、粒径1μm以上の粉じんの集じん率の
低下に加えてそれ以下の粒径の微小粉じんの集じん率が
著しく低下し、集じん電極を通過した微小粉じんが等価
粒径1μm以上の粒子に凝集していると考えてよい。そ
して、このような場合には集じん電極の粉じんの堆積量
が一定の限界値を超えており、電気集じん機の運転を停
止して堆積した粉じんを払い落とすべき時期であると見
なすことができる。
Under such a configuration, the number concentration of dust before and after dust collection by an electric dust collector is measured for each particle size,
For example, a phenomenon in which the dust collection rate of dust having a particle diameter of 1 μm or more is extremely reduced is captured. Here, the extreme decrease means a case where the dust collection rate is zero, close to it, or negative. When such a phenomenon occurs, as described above, in addition to the reduction of the dust collection rate of dust having a particle diameter of 1 μm or more, the dust collection rate of fine dust having a particle diameter of less than 1 μm significantly decreases. It can be considered that the fine dust that has passed through the dust electrode is aggregated into particles having an equivalent particle size of 1 μm or more. In such a case, the amount of accumulated dust on the dust collection electrode exceeds a certain limit, and it may be considered that it is time to stop the operation of the electric dust collector and remove the accumulated dust. it can.

【0015】[0015]

【発明の効果】この発明によれば、あるレベル以上の粒
径の粉じんの集じん率が極端に低下したことから集じん
電極に堆積した粉じんが限界値を超えたものと判定する
ようにしたことにより、電気集じん機をタイミングよく
清掃してその運転効率を高めることができる。
According to the present invention, it is determined that the dust deposited on the dust collecting electrode has exceeded the limit value because the dust collection rate of the dust having a particle size of a certain level or more is extremely reduced. As a result, the electric precipitator can be cleaned in a timely manner to improve the operation efficiency.

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

【図1】この発明の実施例を説明するための電気集じん
機の概略縦断面図である。
FIG. 1 is a schematic longitudinal sectional view of an electric precipitator for explaining an embodiment of the present invention.

【図2】従来例を説明するための電気集じん機の概略縦
断面図である。
FIG. 2 is a schematic vertical sectional view of an electric precipitator for explaining a conventional example.

【図3】図2における集じんユニットの拡大正面図であ
る。
FIG. 3 is an enlarged front view of the dust collecting unit in FIG.

【符号の説明】[Explanation of symbols]

1 集じんユニット 2 送風機 7 帯電ユニット 8 集じんユニット 22 パーティクルカウンタ DESCRIPTION OF SYMBOLS 1 Dust collection unit 2 Blower 7 Charging unit 8 Dust collection unit 22 Particle counter

───────────────────────────────────────────────────── フロントページの続き (72)発明者 高橋 武男 神奈川県川崎市川崎区田辺新田1番1号 富士電機株式会社内 (56)参考文献 特開 昭62−279852(JP,A) 特開 昭62−242838(JP,A) 特開 昭62−183863(JP,A) 特開 昭62−61660(JP,A) (58)調査した分野(Int.Cl.6,DB名) B03C 3/00 - 3/88 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Takeo Takahashi 1-1-1, Tanabe-Nita, Kawasaki-ku, Kawasaki-shi, Kanagawa Prefecture Inside Fuji Electric Co., Ltd. (56) References JP-A-62-279852 (JP, A) JP-A-62-242838 (JP, A) JP-A-62-183863 (JP, A) JP-A-62-6660 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) B03C 3 / 00-3/88

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】自動車道トンネル内の空気を清浄化する電
気集じん機の集じん率を粉じんの粒径別に求め、その結
果から前記電気集じん機の集じん電極に捕集された粉じ
んを除去する時期を判定することを特徴とする自動車道
トンネル用電気集じん機の粉じん除去方法。
A dust collection rate of an electric dust collector for purifying air in a motorway tunnel is determined for each particle size of dust, and from the result, the dust collected on a dust collecting electrode of the electric dust collector is determined. A dust removal method for an electric dust collector for a motorway tunnel, characterized by determining a time to remove the dust.
【請求項2】粒径があるレベル以上の粉じんの集じん率
が極端に悪化した時点を集じん電極の粉じんを除去する
時期とすることを特徴とする請求項1記載の自動車道ト
ンネル用電気集じん機の粉じん除去方法。
2. The electric motor for a motorway tunnel according to claim 1, wherein a point in time when the dust collection rate of the dust having a particle diameter of a certain level or more is extremely deteriorated is a time when the dust of the dust collecting electrode is removed. How to remove dust from dust collector.
JP14796891A 1991-05-23 1991-05-23 Dust removal method of electric precipitator for motorway tunnel Expired - Fee Related JP2959190B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14796891A JP2959190B2 (en) 1991-05-23 1991-05-23 Dust removal method of electric precipitator for motorway tunnel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14796891A JP2959190B2 (en) 1991-05-23 1991-05-23 Dust removal method of electric precipitator for motorway tunnel

Publications (2)

Publication Number Publication Date
JPH04346852A JPH04346852A (en) 1992-12-02
JP2959190B2 true JP2959190B2 (en) 1999-10-06

Family

ID=15442174

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14796891A Expired - Fee Related JP2959190B2 (en) 1991-05-23 1991-05-23 Dust removal method of electric precipitator for motorway tunnel

Country Status (1)

Country Link
JP (1) JP2959190B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3970485B2 (en) * 1999-09-17 2007-09-05 松下エコシステムズ株式会社 Electric dust collector for tunnel excavation work

Also Published As

Publication number Publication date
JPH04346852A (en) 1992-12-02

Similar Documents

Publication Publication Date Title
US7901489B2 (en) Electrostatic precipitator with high efficiency
AU2008320310B2 (en) Charging device, air handling device, method for charging, and method for handling air
JP2011092932A (en) Electric dust collector and air cleaner containing the same
CN207222149U (en) A kind of wet electrostatic cyclone dust
AU2008205431A1 (en) Electric dust collector
CN109663670A (en) A kind of automatically cleaning dust arrester
CN101837216B (en) Electrostatic-bag composite dust-collector
JP2959190B2 (en) Dust removal method of electric precipitator for motorway tunnel
KR102024565B1 (en) Device and method for measuring dust
CN1415421A (en) Electrostatic dust collection method in high speed internal circulation and relevant equipment
CN202860353U (en) Efficient dust collector
CN106824537B (en) Plasma electrostatic depuration component and air cleaning facility
CN109331587A (en) It is a kind of can intelligent blanking deduster
JP3427165B2 (en) Electric dust collector
CN108160332B (en) Electric dust collector with filtering type porous anode plate
JPH11517A (en) Two-stage type dust collector and dust collection method
CN203315879U (en) Dust removing equipment
CN203750358U (en) Single-chamber three-electric-field bag-type combined dust collector
CN208612756U (en) A kind of air flow method filter pocket device of electric precipitator
JP3529656B2 (en) Air purifier
CN100512882C (en) Electronic type air cleaner
JPS6233565A (en) Electrostatic type dust precipitator
JPS624457A (en) Method for removing dust in electric dust collector
JPS6261660A (en) Method for removing dust of electric precipitator
CN206463631U (en) A kind of self-priming dedusting recovery system

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080730

Year of fee payment: 9

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 9

Free format text: PAYMENT UNTIL: 20080730

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 10

Free format text: PAYMENT UNTIL: 20090730

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090730

Year of fee payment: 10

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 11

Free format text: PAYMENT UNTIL: 20100730

LAPS Cancellation because of no payment of annual fees