JPS6029304B2 - Charging method of electrostatic precipitator - Google Patents
Charging method of electrostatic precipitatorInfo
- Publication number
- JPS6029304B2 JPS6029304B2 JP6422281A JP6422281A JPS6029304B2 JP S6029304 B2 JPS6029304 B2 JP S6029304B2 JP 6422281 A JP6422281 A JP 6422281A JP 6422281 A JP6422281 A JP 6422281A JP S6029304 B2 JPS6029304 B2 JP S6029304B2
- Authority
- JP
- Japan
- Prior art keywords
- voltage
- discharge
- dust
- electrostatic precipitator
- 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
Links
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- Electrostatic Separation (AREA)
Description
【発明の詳細な説明】
本発明は固有電気抵抗の高いダストを補集する集塵装置
の荷電方式に係り、特に排煙条件の変化する状態におい
て使用するに好適な電気集塵装置荷電方式に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a charging method for a dust collector that collects dust having a high specific electrical resistance, and particularly to a charging method for an electrostatic precipitator suitable for use under changing smoke exhaust conditions. .
一般に、集塵装置というのは、粉粒体の諭送末端におい
て気体から固体粒子を分離する蒲集器や、プロセスガス
中から有効成分の粒子を分離するもの、あるいは反応ガ
ス中から固体成分を取り除いて清浄ガスをつくるための
ものなども含め、いわゆるガス中の微分子を分離補集す
る装置のことである。In general, a dust collector is a collector that separates solid particles from the gas at the feeding end of powder or granules, a device that separates particles of active ingredients from process gas, or a device that separates solid components from reaction gas. It refers to equipment that separates and collects so-called fine molecules in gas, including those used to remove them to create clean gas.
そして、一般に電気集塵といえば直流高電圧によってコ
ロナ放電を発生させ、ガス中の粒子を帯電させて(放電
極部)、この帯電粒子を亀場内で電気力により、ガスと
分離する(集塵極部)機構をもつ粒子静電補集方式をい
うのである。電気集塵における粒子の分離移動速動はサ
ブミクロンの範囲で重力あるいは遠心力による沈降速度
のように急激に低下することがないから超微粒子に特に
有効な集塵方式である。従来の電気集塵装置の電極部は
第1図に示す如き構成を有している。Generally speaking, electrostatic precipitation involves generating a corona discharge using a high DC voltage, charging particles in the gas (discharge electrode part), and separating the charged particles from the gas by electric force in the Kameba (dust collection). This refers to a particle electrostatic collection system with a mechanism (extreme). Electrostatic precipitation is a particularly effective dust collection method for ultrafine particles because the speed of separation and movement of particles in the submicron range does not drop as sharply as the sedimentation speed due to gravity or centrifugal force. The electrode section of a conventional electrostatic precipitator has a configuration as shown in FIG.
すなわち、線状の放電極1が所定間隔毎に複数個一列に
設けられており、この一列に設けられた放電極1を挟み
所要間隙をもって板状の集塵極2が設けられている。こ
の放電極1と集塵極2は、集塵器外ワク3内にそれぞれ
設置されている。また、集塵極3はアース線5を介して
接地されており、また、放電極1には高電圧線4が接続
されている。このような構成において、放電極1には高
電圧線4を介して負の直流にパルス又は交流を重畳した
高電圧が印加される。That is, a plurality of linear discharge electrodes 1 are provided in a row at predetermined intervals, and plate-shaped dust collection electrodes 2 are provided with a required gap between the discharge electrodes 1 provided in the row. The discharge electrode 1 and the dust collection electrode 2 are respectively installed inside the workpiece 3 outside the dust collector. Further, the dust collection electrode 3 is grounded via a ground wire 5, and a high voltage line 4 is connected to the discharge electrode 1. In such a configuration, a high voltage obtained by superimposing a pulse or an alternating current on a negative direct current is applied to the discharge electrode 1 via the high voltage line 4.
すると、放電極1からは負のコロナ放電が発生し、この
コ。ナ放電によって電子及び負イオンがアース電位であ
る集塵極2に移動する。この電子及び負イオンの移動の
際に排煙中のダストが帯電される。この負に帯電された
ダストは放電極1と集塵極2によって作られる電界によ
り集塵極2上に橘集される。この際、ダストの種類、温
度、濃度、流速等排ガス条件が決まれば、電流−電圧特
性は一義的に決まる。Then, a negative corona discharge is generated from the discharge electrode 1. Due to the discharge, electrons and negative ions move to the dust collecting electrode 2 which is at ground potential. During the movement of electrons and negative ions, the dust in the flue gas is charged. This negatively charged dust is collected on the dust collecting electrode 2 by the electric field created by the discharge electrode 1 and the collecting electrode 2. At this time, once the exhaust gas conditions such as the type of dust, temperature, concentration, and flow rate are determined, the current-voltage characteristics are uniquely determined.
高抵抗ダストとして石炭尊蟻ボイラーで発生するフライ
ァッシュを一例に取ると、変動負荷対策として用いられ
る事が多い。そのため、石炭車焼ボイラーの負荷変動も
大きい。袋塵率を低下せることなく、この負荷変動に応
じるためには例えば第2図に示すように、ダスト濃度の
高い状態から低い状態に変わった場合には最適集塵効率
を示す電流−電圧特性はaからbに変化する。したがっ
て、集塵率を低下させることなく集塵するには電流をl
oから1,に減少しなければならない。即ち運転状態は
第2図図示A貼からB点へ移行し、運転電圧はVoから
V.へと大中に変化する。このような電源の変動に1つ
の電源によって追従するには応答速度が遅く又大きな裕
度を必要とする。さらに高抵抗ダストに対しては電流制
御を微細に行う必要があり、広範囲にこれを行なうには
制御系自体非常に大きなものとしなければならないとい
う欠点を有している。また電源容量、制御範囲を逸脱し
、制御不能となる欠点を有する。本発明の目的は、放電
電流を広範囲にわたり微細に制御することのできる電気
集塵装置の荷電方式を提供することにある。本発明は、
放電極を複数群に区分し、各群の電極には直流電圧にパ
ルス電圧又は交流電圧を重畳した電圧、直流電圧、無荷
電の3種の電圧をそれぞれ排煙条件に応じて選択荷電し
、かつパルス電圧液高値:パルス幅、くり返し周波数あ
るいは、交流波高値及び交流の謀電、休止時間を変える
ことにより、放電電流を微細に制御しようというもので
ある。Taking fly ash, which is generated in coal-fired boilers as a high-resistance dust, as an example, it is often used as a countermeasure against fluctuating loads. Therefore, the load fluctuations of coal-fired boilers are also large. In order to respond to this load fluctuation without reducing the bag dust rate, for example, as shown in Figure 2, the current-voltage characteristic that shows the optimum dust collection efficiency when the dust concentration changes from a high state to a low state is necessary. changes from a to b. Therefore, in order to collect dust without reducing the dust collection rate, the current should be l.
It must be decreased from o to 1. That is, the operating state shifts from point A to point B in Figure 2, and the operating voltage changes from Vo to V. It changes to Onaka. In order to follow such fluctuations in the power supply with a single power supply, the response speed is slow and a large margin is required. Furthermore, for high-resistance dust, it is necessary to perform fine current control, and in order to perform this over a wide range, the control system itself has to be very large. It also has the disadvantage of exceeding the power supply capacity and control range, making it uncontrollable. An object of the present invention is to provide a charging method for an electrostatic precipitator that can finely control discharge current over a wide range. The present invention
The discharge electrodes are divided into a plurality of groups, and the electrodes in each group are selectively charged with three types of voltages: a voltage obtained by superimposing a pulse voltage or an AC voltage on a DC voltage, a DC voltage, and an uncharged voltage depending on the smoke exhaust conditions. In addition, by changing the pulse voltage liquid peak value: pulse width, repetition frequency, alternating current peak value, alternating current charge, and pause time, the discharge current is finely controlled.
以下、本発明の実施例について説明する。Examples of the present invention will be described below.
第3図には、本発明の一実施例が示されている。FIG. 3 shows an embodiment of the invention.
図において、10が放電極、11が集塵極である。In the figure, 10 is a discharge electrode, and 11 is a dust collection electrode.
この放電極10は、第1群、第0群とに区分されており
、第1群には電源部P,が接続され、第0群には電源部
P2が接続されて、表1に示す如きモードの電圧が印加
されている。この放電極10の区分は排ガスの流れに添
った一つのダクト内の放電極10を一つおきに、又は複
数個ずつ、1群とn群に区分されている。この場合、1
群の放電極数とロ群の放電極数は同数でも異なった数で
も良く変動領域に応じて選択することができる。表
1 荷電電圧モード以上のように放電極を二つの群
に区分し、表1に示すようなモードの電圧を印加するこ
とにより、第4図に示すように1群の電流−電圧特性C
、0群の電流−電圧特性d、及びその和の電流−電圧特
性eなる曲線に分けて考えると、1群の謀電モードを一
定にしロ群の荷電モードを変えることにより第4図の斜
線で示す領域で電流制御を行うことができる。This discharge electrode 10 is divided into a 1st group and a 0th group, the 1st group is connected to the power supply section P, and the 0th group is connected to the power supply section P2, as shown in Table 1. A voltage in such a mode is applied. The discharge electrodes 10 are divided into groups 1 and n, with every other discharge electrode 10 or a plurality of discharge electrodes 10 in one duct along the flow of exhaust gas. In this case, 1
The number of discharge electrodes in the group and the number of discharge electrodes in the group B may be the same or different, and can be selected depending on the fluctuation range. table
1 Charging voltage mode By dividing the discharge electrode into two groups as described above and applying the voltage in the mode shown in Table 1, the current-voltage characteristic C of the first group is obtained as shown in Figure 4.
, the current-voltage characteristic d of the 0 group, and the current-voltage characteristic e of the sum thereof.By keeping the charging mode of the 1 group constant and changing the charging mode of the B group, the diagonal line in Fig. 4 can be obtained. Current control can be performed in the region shown by .
今電圧Voを固定すると1群の運転点Cで12であった
電流をロ群をD点で運転することにより、集塵装置は全
体としてE点で運転することになり13の電流を流すこ
とができ、上記のような群電圧制御を行うことにより大
きな負荷変動にも十分応答し、かつパルス、交流を用い
ることにより微細な制御を行うことができる。また流速
、電離電極ピッチとの相関で上記電圧モ−ドを印加する
ことより、ダストに対する荷電を均一にでき、集塵極に
均一にダストを付着させる事ができ特に高抵抗ダストに
於て生じる局部異常電界を防止でき、すなわち局部的に
発生する全賂絶縁破壊を防止することができる。さらに
はもしたとえ全賂破壊が発生した場合その群の電圧につ
いて一時荷電を休止すれば良く他の群は荷電しているた
め、従来のように全系統一時荷電休止により発生する一
時的集塵率の低下すなわち排出ダストの異常増加を防止
することができる。第1表の直流+交流に関するf,g
については第5図A,Bに示すように直流に重畳する交
流の荷電時間位相を異にする場合である。Now, if the voltage Vo is fixed, the current which was 12 at the operating point C of the first group is operated at the point D of the B group, and the dust collector as a whole will be operated at the point E, and a current of 13 will flow. By performing group voltage control as described above, it is possible to sufficiently respond to large load fluctuations, and by using pulses and alternating current, fine control can be performed. In addition, by applying the above voltage mode in correlation with the flow rate and the ionization electrode pitch, it is possible to uniformly charge the dust, and it is possible to uniformly attach the dust to the dust collecting electrode, which is particularly likely to occur with high-resistance dust. Local abnormal electric fields can be prevented, that is, locally generated total insulation breakdown can be prevented. Furthermore, even if a total breakdown occurs, it is only necessary to temporarily suspend charging for the voltage of that group, and other groups are still charged, so the temporary dust collection rate that occurs by temporarily suspending charging of the entire system as in the past In other words, an abnormal increase in exhaust dust can be prevented. f, g related to DC + AC in Table 1
This is the case where the charging time phase of the alternating current superimposed on the direct current is different, as shown in FIGS. 5A and 5B.
この交流がパルスであっても幻果は変わらない。またこ
こでは電離電極群を2群に区分した場合について説明し
たが3群以上の多数群に区分してもその効果は変わらな
い。Even if this exchange is a pulse, the illusion remains the same. Furthermore, although the case where the ionizing electrode group is divided into two groups has been described here, the effect remains the same even if the ionizing electrode group is divided into three or more groups.
したがって、本実施例によれば、排煙条件の大中に変化
する電気集塵装置の制御をその変化城全体にわたって微
細に行なうことができ、高抵抗ダストの均一荷電さらに
は局部異常電界を防止でさすなわち局部的に発生する全
路破壊を防止できる。Therefore, according to this embodiment, it is possible to finely control the electrostatic precipitator over the entire range of changes in smoke exhaust conditions, and prevent uniform charging of high-resistance dust as well as local abnormal electric fields. In other words, it is possible to prevent total path failure that occurs locally.
また、本実施例によれば、たとえ全路破壊を生じてもそ
の群の電圧だけを一時休止するだけで済み、排出ダスト
の一時的異常増加を防止することができる。以上説明し
たように、本発明によれば、放電電流を広範囲にわたり
微細に制御することができる。Further, according to this embodiment, even if a complete circuit breakdown occurs, it is only necessary to temporarily suspend the voltage of that group, and it is possible to prevent a temporary abnormal increase in the amount of discharged dust. As explained above, according to the present invention, discharge current can be finely controlled over a wide range.
第1図は電気集塵装置電極部横断面図、第2図は従釆方
式電気集塵装置における電流−電圧特性図、第3図は本
発明になる電離電極を群区分した電極結線図、第4図は
本発明の効果を示す電流−電圧特性図、第5図は直流+
交流の異なる2種の謀雷電圧モードを示す図である。
符号の説明、1・・・電離電極、2・・・集鰹電極、3
・・・集塵器外ワク。
第1図
第2図
第3図
第4図
第5図FIG. 1 is a cross-sectional view of the electrode part of an electrostatic precipitator, FIG. 2 is a current-voltage characteristic diagram in a secondary type electrostatic precipitator, and FIG. 3 is an electrode connection diagram dividing the ionizing electrodes of the present invention into groups. Fig. 4 is a current-voltage characteristic diagram showing the effects of the present invention, and Fig. 5 is a DC +
It is a figure which shows two types of lightning voltage modes with different alternating current. Explanation of symbols, 1... Ionization electrode, 2... Bonito collecting electrode, 3
...The outside of the dust collector. Figure 1 Figure 2 Figure 3 Figure 4 Figure 5
Claims (1)
を印加しコロナ放電を起こし空間にイオンを供給する複
数個の放電極と、該放電極に対向して設けられ粉塵を付
着させ補集する集塵極とを有する電気集塵装置において
、上記放電極を複数個の群に区分し、直流電圧にパルス
電圧又は交流電圧を重畳した電圧、直流電圧及び無荷電
の3モードのいずれかを排煙条件に応じて前記区分した
各放電極群に荷電することを特徴とする電気集塵装置の
荷電方式。 2 特許請求の範囲第1項記載の発明において、上記電
圧モードは、時間的に変化できるものであることを特徴
とする電気集塵装置の荷電方式。[Scope of Claims] 1. A plurality of discharge electrodes that apply a voltage obtained by superimposing a pulse voltage or an alternating current voltage to a DC voltage to cause corona discharge and supply ions into a space, and a plurality of discharge electrodes that are provided opposite to the discharge electrodes to remove dust. In an electrostatic precipitator having a dust collection electrode for adhesion and collection, the discharge electrode is divided into a plurality of groups, and three modes are applied: a voltage obtained by superimposing a pulse voltage or an AC voltage on a DC voltage, a DC voltage, and an uncharged voltage. A charging method for an electrostatic precipitator, characterized in that each of the divided discharge electrode groups is charged with one of the following according to smoke exhaust conditions. 2. The charging method for an electrostatic precipitator according to the invention as set forth in claim 1, wherein the voltage mode can be changed over time.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6422281A JPS6029304B2 (en) | 1981-04-30 | 1981-04-30 | Charging method of electrostatic precipitator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6422281A JPS6029304B2 (en) | 1981-04-30 | 1981-04-30 | Charging method of electrostatic precipitator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS57180446A JPS57180446A (en) | 1982-11-06 |
JPS6029304B2 true JPS6029304B2 (en) | 1985-07-10 |
Family
ID=13251854
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6422281A Expired JPS6029304B2 (en) | 1981-04-30 | 1981-04-30 | Charging method of electrostatic precipitator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6029304B2 (en) |
-
1981
- 1981-04-30 JP JP6422281A patent/JPS6029304B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS57180446A (en) | 1982-11-06 |
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