JP2010069360A - Electrostatic dust collector - Google Patents

Electrostatic dust collector Download PDF

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JP2010069360A
JP2010069360A JP2008236550A JP2008236550A JP2010069360A JP 2010069360 A JP2010069360 A JP 2010069360A JP 2008236550 A JP2008236550 A JP 2008236550A JP 2008236550 A JP2008236550 A JP 2008236550A JP 2010069360 A JP2010069360 A JP 2010069360A
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electrode
dust collection
gas flow
particulate matter
dust collecting
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JP4856139B2 (en
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Toshiaki Yamamoto
俊昭 山本
Akio Zukeran
章朝 瑞慶覧
Yasushi Mitsuzuka
康史 三塚
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Fuji Electric Co Ltd
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Fuji Electric Systems Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an electrostatic dust collector which increases the collection efficiency by effectively sending a fine particulate material into the pocket area of electric field zero utilizing ionic air and which prevents the re-scattering by controlling the stripping due to the induction charge of the collected particulate material. <P>SOLUTION: In the electrostatic dust collector in which the gas stream passage to feed a gas containing the particulate material between a discharge electrode and dust collecting electrode that are oppositely arranged is formed and in which high voltage is applied to both electrodes to electrify the particulate material in the gas flowing through the gas stream passage so that it can be collected in the dust collecting electrode, a required number of dust collecting pockets where the space electric field strength in the inner atmosphere to store the particulate material is zero are installed at the opposite face of the dust collecting electrode against the discharge electrode with intervals in the flowing direction of the gas flowing through the gas stream passage. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

この発明は、ディーゼルエンジンの排気ガスや、道路トンネルの排気ガスのように微細な低抵抗粒子状物質を含むガスまたは空気からこの低抵抗粒子状物質を除去するために使用される電気集塵装置に関する。   The present invention relates to an electrostatic precipitator used for removing low-resistance particulate matter from gas or air containing fine low-resistance particulate matter such as exhaust gas of a diesel engine or exhaust gas of a road tunnel. About.

ディーゼル排気ガス、自動車トンネル排気ガスやその他の産業排気ガス等に含まれる微細な粒子状物質を取り除くために電気集塵装置は有用である。電気集塵装置は、コロナ放電によりガス中の粒子状物質に帯電させ、この帯電された粒子状物質をクーロン力によって集塵電極上に引き寄せて捕集するものである。   An electric dust collector is useful for removing fine particulate matter contained in diesel exhaust gas, automobile tunnel exhaust gas, and other industrial exhaust gas. The electrostatic precipitator charges the particulate matter in the gas by corona discharge, and draws and collects the charged particulate matter on the dust collecting electrode by Coulomb force.

電気集塵装置においては粒子状物質の粒径が小さいと帯電量も小さいので作用するクーロン力が弱いため集塵電極により捕集することが困難となる問題がある。   In the electrostatic precipitator, when the particle size of the particulate matter is small, the amount of charge is small, so that the acting Coulomb force is weak, so that it is difficult to collect by the dust collecting electrode.

このような問題を解決するために、特許文献1では、ガス流路を形成するケースの内側に隙間をおいてメッシュ状の集塵電極を配置し、ケースと集塵電極との間の隙間に集塵電極と隣接して集塵フィルタを設け、かつケース内のガス流路中に集塵電極と対向して放電電極を設け、放電電極からの放電によってガス中の粒子状物質に帯電させるとともに放電にともなって発生するイオン風によってガス流をガス流路と集塵フィルタ層との間で循環させながら流すことにより粒子状物質を集塵フィルタ層の空孔内に詰め込んで捕集するようにした電気集塵装置が提案されている。   In order to solve such a problem, in Patent Document 1, a mesh-shaped dust collecting electrode is arranged with a gap inside the case forming the gas flow path, and the gap between the case and the dust collecting electrode is arranged. A dust collection filter is provided adjacent to the dust collection electrode, and a discharge electrode is provided in the gas flow path in the case so as to face the dust collection electrode. The discharge from the discharge electrode charges the particulate matter in the gas. The particulate matter is packed and collected in the pores of the dust collection filter layer by flowing the gas flow between the gas flow path and the dust collection filter layer by the ion wind generated by the discharge. An electrostatic precipitator has been proposed.

この特許文献1の電気集塵装置によれば、放電時に発生するイオン風により帯電量の小さい微細な粒子状物質をメッシュ状集塵電極の裏側の集塵フィルタ層に送り込んで捕集することができるので、微細な粒子状物質を効果的に捕集することができる。   According to the electrostatic precipitator of Patent Document 1, fine particulate matter having a small charge amount can be sent to the dust collecting filter layer on the back side of the mesh dust collecting electrode and collected by ion wind generated at the time of discharge. As a result, fine particulate matter can be collected effectively.

また、特許文献2では、集塵電極の表面に金網、パンチング板等で粒子状物質が滞留する凹凸部を形成し、クーロン力によって集塵電極に捕集される粒子状物質が凹凸部の粒子保持作用によって集塵電極側に保持されるようにした排ガス浄化装置が提案されている。   Moreover, in patent document 2, the uneven | corrugated | grooved part which a particulate matter accumulates on the surface of a dust collection electrode with a metal net, a punching board, etc. is formed, and the particulate matter collected by a dust collection electrode by Coulomb force is the particle | grains of an uneven | corrugated part. There has been proposed an exhaust gas purification apparatus that is held on the dust collecting electrode side by a holding action.

この特許文献2の排ガス浄化装置によれば、凹凸部の粒子保持作用によって効率よく粒子状物質を捕集することができる。
WO2005/021161号公報 特開2006−136766号公報
According to the exhaust gas purifying apparatus of Patent Document 2, particulate matter can be efficiently collected by the particle holding action of the uneven portion.
WO2005 / 021161 JP 2006-136766 A

ところが、ガス中に含まれる粒子状物質が、ディーゼル排気ガスに含まれるような炭素を多く含む電気抵抗率の小さい、いわゆる低抵抗粒子状物質である場合には、集塵電極に一旦捕集されると静電気的な保持力を失うためガス流に押し戻されて集塵電極から剥離して飛散する、いわゆる再飛散現象を起こし、電気集塵装置の捕集効率を低下させる問題がある。再飛散現象は、集塵電極に捕集され、凝集肥大化した粒子状物質において顕著となる。再飛散粒子は電気集塵装置の運転中に高電圧電極(放電電極)と接地電極(集塵電極)との間で往復するため、放電電極と集塵電極との間の空間の電界強度が飛散した粒子状物質で形成される空間電荷により低下され、さらに集塵効率の低下を引き起こす。また、時間の経過とともに粒子状物質が放電電極に付着するとイオンの発生を妨げるため、粒子荷電量が減少し、これによっても集塵効率が低下する。   However, when the particulate matter contained in the gas is a so-called low resistance particulate matter containing a large amount of carbon and contained in diesel exhaust gas and having a low electrical resistivity, it is once collected by the dust collecting electrode. Then, since the electrostatic holding power is lost, there is a problem that a so-called re-scattering phenomenon occurs in which it is pushed back into the gas flow and peels off from the dust collecting electrode and scatters, thereby reducing the collection efficiency of the electrostatic precipitator. The re-scattering phenomenon becomes remarkable in the particulate matter collected by the dust collecting electrode and agglomerated and enlarged. Since re-scattered particles reciprocate between the high voltage electrode (discharge electrode) and the ground electrode (dust collection electrode) during operation of the electrostatic precipitator, the electric field strength in the space between the discharge electrode and the dust collection electrode is reduced. It is lowered by the space charge formed by the scattered particulate matter, and further reduces the dust collection efficiency. In addition, if particulate matter adheres to the discharge electrode with the passage of time, the generation of ions is hindered, so that the amount of charged particles decreases, and this also reduces the dust collection efficiency.

なお、近年、電気集塵装置の電極間に印加する電圧を矩形波交流電圧として再飛散現象の発生を抑制する方法が実用化されているが、この方法による再飛散の抑制効果にも限界があり、これを完全に抑制することは困難である。   In recent years, a method has been put into practical use in which the voltage applied between the electrodes of the electrostatic precipitator is a rectangular wave AC voltage to suppress the occurrence of the re-scattering phenomenon. It is difficult to completely suppress this.

また、前記の特許文献1に示されたメッシュ状の集塵電極と集塵フィルタを備えた電気集塵装置の場合は、集塵電極および集塵フィルタの捕集量が増大すると目詰まり状態となるので、これを解消するために集塵電極および集塵フィルタを比較短い周期で再生処理を行わなければならず、メンテナンスに手間がかかる問題もある。   Moreover, in the case of the electric dust collector provided with the mesh-shaped dust collection electrode and dust collection filter which were shown by the said patent document 1, if the collection amount of a dust collection electrode and a dust collection filter increases, it will be clogged and Therefore, in order to solve this problem, the dust collection electrode and the dust collection filter must be regenerated in a comparatively short cycle, and there is a problem that maintenance is troublesome.

前記の特許文献2に示された排ガス浄化装置においても、集塵電極の表面の凹凸部にこの凹凸部の粒子保持作用によって滞留された粒子状物質を定期的に剥離するために、機械的剥離機構を設けなければならないという問題がある。この機械的剥離機構を設ける代わりに、流速の速いガスを所定の時間間隔で瞬間的に流すようにして、粒子状物質を肥大化させた状態で剥離させることも提案されているが、流速の速いガスを所定の時間間隔で瞬間的に流すことが必要となるだけでなく、前記凹凸部に滞留された粒子状物質が誘導荷電されることにより再飛散を起こし、これを完全に防止することができないという問題がある。   In the exhaust gas purifying apparatus disclosed in Patent Document 2 as well, mechanical peeling is performed periodically to peel off the particulate matter retained by the particle holding action of the uneven portions on the uneven portions on the surface of the dust collecting electrode. There is a problem that a mechanism must be provided. Instead of providing this mechanical exfoliation mechanism, it has been proposed to exfoliate particulate matter in an enlarged state by causing a gas with a high flow rate to flow instantaneously at a predetermined time interval. Not only is it necessary to flow a fast gas instantaneously at a predetermined time interval, but re-scattering occurs due to induction charging of the particulate matter retained in the concavo-convex portion, and this can be completely prevented. There is a problem that can not be.

この発明は、このような問題点を解決するため、放電に伴って発生するイオン風を利用して集塵効率を向上させるとともに、捕集した粒子状物質の再飛散現象を完全に防止することができ、また、電極の再生処理周期を長くできる電気集塵装置を提供することを課題とするものである。   In order to solve such a problem, the present invention improves the dust collection efficiency by utilizing the ion wind generated along with the discharge, and completely prevents the re-scattering phenomenon of the collected particulate matter. It is another object of the present invention to provide an electrostatic precipitator capable of extending the electrode regeneration processing cycle.

前記の課題を解決するため、この発明は、粒子状物質を含むガスを流すガス流路中に放電電極と集塵電極とを対向配置し、両電極に高電圧を印加して前記ガス流路を流れるガス中の粒子状物質を帯電させて集塵電極により吸引して捕集するようにした電気集塵装置において、前記集塵電極の前記放電電極と対向し、ガス流と接する面に前記ガス流路中を流れるガスの流れ方向に間隔をおいて捕集した粒子状物質を保留する内部空間を備えた集塵ポケットを複数設けたことを特徴とするものである。   In order to solve the above problems, the present invention provides a gas flow path in which a discharge electrode and a dust collection electrode are arranged opposite to each other in a gas flow path for flowing a gas containing particulate matter, and a high voltage is applied to both electrodes. In an electrostatic precipitator that charges and collects particulate matter in the gas flowing through the dust collecting electrode, the surface of the dust collecting electrode that faces the discharge electrode and contacts the gas flow A plurality of dust collection pockets having an internal space for retaining particulate matter collected at intervals in the flow direction of the gas flowing in the gas flow path are provided.

この発明における前記放電電極には、前記集塵ポケットとほぼ同じ間隔で複数の放電部を形成するのがよく、そしてこれらの放電部は、それぞれ前記各集塵ポケットの前端より離れた位置に配置するようにする。   The discharge electrode according to the present invention is preferably formed with a plurality of discharge portions at substantially the same interval as the dust collection pockets, and these discharge portions are arranged at positions separated from the front ends of the respective dust collection pockets. To do.

この発明おいて、前記集塵ポケットは、内部空間の開口と対向した後壁にガス通流口を設けるようにすることができる。また、前記集塵ポケットは、前記集塵電極に導電的に結合してこれと同電位にして、前記内部空間の空間電界強度を零にしたことを特徴とするものである。   In the present invention, the dust collection pocket may be provided with a gas flow port on the rear wall facing the opening of the internal space. Further, the dust collection pocket is characterized in that it is electrically coupled to the dust collection electrode and has the same electric potential so that the space electric field strength of the internal space is zero.

この発明によれば、粒子状物質を含むガスを流すガス流路中に放電電極と集塵電極とを対向配置し、両電極に高電圧を印加して前記ガス流路を流れるガス中の粒子状物質に帯電させて集塵電極により吸引して捕集するようにした電気集塵装置において、前記集塵電極の前記放電電極と対向し、ガス流と接する面に前記ガス流路中を流れるガスの流れ方向に間隔をおいて粒子状物質を保留する内部空間を備えた集塵ポケットを複数設けるようにしているので、帯電された粒子状物質がクーロン力および放電電極の放電によって生じるイオン風によって集塵電極側に押し寄せられて集塵電極により捕捉されるとき、集塵電極の表面に設けられた集塵ポケットの内部空間に閉じ込められる。集塵ポケットに閉じ込められた粒子状物質はガス流路のガス流から遮られるようになり、かつ、集塵ポケットの内部空間は空間電界強度が零となることにより保留された粒子状物質に電荷が誘導されることがなく、誘導電荷による剥離力が発生しないため、粒子状物質の再飛散を完全に防止することができる。   According to the present invention, the discharge electrode and the dust collecting electrode are disposed opposite to each other in the gas flow path for flowing the gas containing the particulate matter, and the particles in the gas flowing through the gas flow path by applying a high voltage to both electrodes. In an electrostatic precipitator that is charged with a particulate material and sucked and collected by a dust collecting electrode, the dust collecting electrode faces the discharge electrode and flows in the gas flow path on a surface in contact with the gas flow Since there are a plurality of dust collection pockets with internal spaces that hold particulate matter at intervals in the gas flow direction, the charged particulate matter generates ion wind generated by the Coulomb force and discharge of the discharge electrode. When trapped by the dust collecting electrode and trapped by the dust collecting electrode, it is trapped in the internal space of the dust collecting pocket provided on the surface of the dust collecting electrode. Particulate matter confined in the dust collection pocket is shielded from the gas flow in the gas flow path, and the internal space of the dust collection pocket is charged by the suspended particulate matter because the space electric field strength becomes zero. Is not induced, and no peeling force due to the induced charge is generated, so that re-scattering of the particulate matter can be completely prevented.

この発明の実施の形態を図に示す実施例に基づいて説明する。   Embodiments of the present invention will be described based on examples shown in the drawings.

図1ないし図3はこの発明の実施例による電気集塵装置の構成を示すもので、図1は部分的な切欠きを含む斜視図、図2には、図1のII−II線に沿う横断面図、図3は図2のIII−III線に沿う縦断面図である。   1 to 3 show the construction of an electrostatic precipitator according to an embodiment of the present invention. FIG. 1 is a perspective view including a partial notch, and FIG. 2 is taken along the line II-II in FIG. FIG. 3 is a transverse sectional view, and FIG. 3 is a longitudinal sectional view taken along line III-III in FIG.

図1ないし図3において、電気集塵装置1は、両端にガスの入口2Aと出口2Bを有するガス流路2を形成する筒状の本体ケース3を備える。本体ケース3内には、ガス流路2を間に挟んで対向配置された平板状の電極板により構成された1対の集塵電極4と、この1対の集塵電極4、4の中間にガス流の流れ方向に所定の間隔で立設された複数の放電電極5が設けられている。
放電電極5の外周に集塵電極4に向かって突設されたとげ状電極により放電部5Aが多数形成されている。集塵電極4、4の互いに対向する面には、放電電極5とほぼ同じ間隔で平板を鉤状に屈曲してなるポケット形成部材6Aを結合して複数の集塵ポケット6が形成されている。
1 to 3, the electrostatic precipitator 1 includes a cylindrical main body case 3 that forms a gas flow path 2 having gas inlets 2A and outlets 2B at both ends. In the main body case 3, there is a pair of dust collecting electrodes 4 constituted by flat electrode plates opposed to each other with the gas flow path 2 interposed therebetween, and an intermediate between the pair of dust collecting electrodes 4, 4. A plurality of discharge electrodes 5 erected at predetermined intervals in the gas flow direction are provided.
A number of discharge portions 5A are formed by spine-shaped electrodes projecting from the outer periphery of the discharge electrode 5 toward the dust collection electrode 4. A plurality of dust collection pockets 6 are formed on the surfaces of the dust collection electrodes 4 and 4 facing each other by joining pocket forming members 6A formed by bending a flat plate like a bowl at substantially the same interval as the discharge electrodes 5. .

集塵ポケット6は、ポケット形成部材6Aと集塵電極4とによって囲われ、ガス流路2を流れるガス流から遮られた内部空間を形成する。この集塵ポケット6の内部空間は、図2に矢印で示すガスの流れ方向に対向する前端側の開口を通してガス流路2に通じ、ここから送り込まれた粒子状物質を保留し閉じ込める。   The dust collection pocket 6 is surrounded by the pocket forming member 6 </ b> A and the dust collection electrode 4, and forms an internal space shielded from the gas flow flowing through the gas flow path 2. The internal space of the dust collection pocket 6 leads to the gas flow path 2 through an opening on the front end side opposed to the gas flow direction indicated by an arrow in FIG. 2, and holds and confines the particulate matter fed from here.

本体ケース3の下方には、集塵電極4および集塵ポケット6に保留された粒子状物質を収容するためのホッパ8がケース3と一体に設けられている。ホッパ8と本体ケース3とを仕切る底板7には、集塵ポケット6の内部空間とホッパ8の内部とを連通させるための連通孔7Aが全部の集塵ポケット6に対応して設けられている(図3参照)。   Below the main body case 3, a hopper 8 for housing the particulate matter retained in the dust collection electrode 4 and the dust collection pocket 6 is provided integrally with the case 3. The bottom plate 7 that partitions the hopper 8 and the main body case 3 is provided with communication holes 7 </ b> A for communicating the internal space of the dust collection pocket 6 and the inside of the hopper 8 corresponding to all the dust collection pockets 6. (See FIG. 3).

このように構成された電気集塵装置1のガス流路2には、図示しない送風機等により流路入口2Aからディーゼル粒子(DPM)等の微小の粒子状物質を含むガスが供給され、1〜10m/s程度の流速で流される。このガス流路2内を流れるガスから粒子状物質を除去して浄化するために、集塵電極4と放電電極5との間に図示しない高圧電源から両電極間の平均電界強度が2〜10kV/cm程度となる直流の高電圧を印加する。   The gas flow path 2 of the electrostatic precipitator 1 configured as described above is supplied with a gas containing fine particulate matter such as diesel particles (DPM) from the flow path inlet 2A by a blower (not shown). The flow rate is about 10 m / s. In order to remove and purify the particulate matter from the gas flowing in the gas flow path 2, the average electric field strength between the two electrodes from a high voltage power source (not shown) between the dust collecting electrode 4 and the discharge electrode 5 is 2 to 10 kV. A high DC voltage of about / cm is applied.

これにより、高電圧の印加された放電電極5と集塵電極4との間を流れるガス流中でコロナ放電が発生し、この放電よって、ガス流中の粒子状物質に荷電される。また、放電電極5と集塵電極4との間で放電が発生すると、これに伴って放電する方向、すなわち、放電電極5から集塵電極4への放電電流の最も大きくなる方向にイオン風が発生し、主流体場、すなわちガス流路2のガス流の流線が変わる。荷電された粒子状物質は、クーロン力によって集塵電極4に引き寄せられるとともに、ガス流線に沿って流される粒子状物質がこのイオン風によって、さらにガス流を横切る方へ偏向されて集塵電極4側へ向うため、集塵電極4によって良好に捕集される。   Accordingly, a corona discharge is generated in the gas flow flowing between the discharge electrode 5 and the dust collecting electrode 4 to which a high voltage is applied, and the particulate matter in the gas flow is charged by this discharge. Further, when a discharge is generated between the discharge electrode 5 and the dust collection electrode 4, an ion wind is generated in the direction in which the discharge occurs, that is, the direction in which the discharge current from the discharge electrode 5 to the dust collection electrode 4 becomes the largest. And the main fluid field, that is, the streamline of the gas flow in the gas flow path 2 changes. The charged particulate matter is attracted to the dust collecting electrode 4 by the Coulomb force, and the particulate matter flowing along the gas flow line is further deflected by the ion wind in a direction crossing the gas flow to collect the dust collecting electrode. Since it goes to 4 side, it collects favorably by the dust collection electrode 4.

このときの粒子状物質を載せたガス流の動きの詳細を図4を参照して説明する。   Details of the movement of the gas flow loaded with particulate matter will be described with reference to FIG.

図4は、この発明の動作説明図であり、(A)は、集塵電極4に設けられた集塵ポケット6の間隔と同じ間隔で設けられた放電電極5の放電部がそれぞれと対応する位置にある集塵ポケット6の前端(ガス流の上流側)に接近して配置された状態を示すもので、(B)は、放電電極5の放電部を対応する位置にある集塵ポケット6の前端より離して上流側の集塵ポケット6の後端(ガス流の下流側)に接近して配置した状態を示すものである。   FIG. 4 is a diagram for explaining the operation of the present invention. FIG. 4A corresponds to the discharge portions of the discharge electrodes 5 provided at the same intervals as the intervals of the dust collection pockets 6 provided on the dust collection electrode 4. FIG. 2B shows a state in which the dust collection pocket 6 is located close to the front end (upstream side of the gas flow), and FIG. 2 shows a state of being arranged close to the rear end (downstream side of the gas flow) of the upstream dust collecting pocket 6 apart from the front end of the gas.

先ず、(A)に示すように放電電極5が集塵ポケット6の前端側に接近して配置された状態においては、集塵電極4(ここでは片側を省略している)に設けた3個の集塵ポケット6の内の集塵ポケット62および63と放電電極5のうちの放電電極52および53とがそれぞれ対応する位置にあるものとして示している。放電電極52および53は、それぞれ集塵ポケット62および63の開口している前端側に接近して配置されている。   First, in the state where the discharge electrode 5 is arranged close to the front end side of the dust collection pocket 6 as shown in (A), three pieces provided on the dust collection electrode 4 (here, one side is omitted). The dust collection pockets 62 and 63 in the dust collection pocket 6 and the discharge electrodes 52 and 53 of the discharge electrode 5 are shown as being in corresponding positions. Discharge electrodes 52 and 53 are arranged close to the front end side where dust collection pockets 62 and 63 are opened, respectively.

この状態で、ガス流路2内に粒子状物質を含むガスを流しながら集塵電極4と放電電極5に高電圧を印加する。ガス流路2内を流れるガスの主流はVoで示す。   In this state, a high voltage is applied to the dust collection electrode 4 and the discharge electrode 5 while flowing a gas containing particulate matter in the gas flow path 2. The main flow of the gas flowing in the gas flow path 2 is indicated by Vo.

また、ここでは、集塵ポケット6は集塵電極4に導電的に結合され、集塵電極4と同電位におかれているので、間隔の最も小さくなった放電電極5の外周のとげ状の放電部5Aと集塵ポケット6の開口した側の前端との間で放電電流が最も大きくなり、ここにイオン風Viaが生起する。   Further, here, the dust collection pocket 6 is conductively coupled to the dust collection electrode 4 and is at the same potential as the dust collection electrode 4, so that the spine-shaped outer periphery of the discharge electrode 5 having the smallest interval is formed. The discharge current becomes the largest between the discharge portion 5A and the front end of the dust collection pocket 6 on the side where the dust collection pocket 6 is opened, and the ion wind Via is generated here.

このようなガス流中で発生する放電によって、ガス流に含まれる粒子状物質が荷電される。荷電力の強い比較的大きな粒径の粒子状物質はクーロン力により集塵ポケット6を含めた集塵電極4により引き寄せられ、集塵ポケット6の内部空間に保留され、閉じ込められる。比較的荷電力の弱い粒径の小さい微細な粒子状物質は、ガスの主流線Voに載って流されるが、放電によってこのガス主流線Voを横切る方向にイオン風Viaが発生するので、ガス主流線Voにこのイオン風Viaが加わるため、放電電極5付近のガス流線は、図4(A)の上部に示すベクトル図における合成流Vraで示すように集塵電極側4に方向が偏向される。この結果、微細な粒子状物質も集塵ポケットの上部で流速を増して集塵電極4側へ偏向される。   Due to the discharge generated in such a gas flow, the particulate matter contained in the gas flow is charged. Particulate matter having a relatively large particle size and having a strong charge power is attracted by the dust collecting electrode 4 including the dust collecting pocket 6 by Coulomb force, and is retained and confined in the internal space of the dust collecting pocket 6. The fine particulate matter having a relatively small particle size with a relatively weak charge power is carried on the main flow line Vo of the gas, but since the ion wind Via is generated in the direction crossing the main flow line Vo by the discharge, the main gas flow Since this ion wind Via is applied to the line Vo, the direction of the gas stream line in the vicinity of the discharge electrode 5 is deflected toward the dust collecting electrode side 4 as shown by the combined flow Vra in the vector diagram shown in the upper part of FIG. The As a result, the fine particulate matter is also deflected toward the dust collecting electrode 4 side at an upper portion of the dust collecting pocket with an increased flow velocity.

しかし、この図4(A)に示す放電電極の配置は、放電電極5が集塵ポケット6の前端(ガスの流れ方向に対向する側、すなわち上流側の端部)に接近して設けられているため、ガス流線の偏向が少なく、流速が増すことにより、粒子状物質の集塵ポケット6の内部空間への閉じ込め効果がほとんどなくなり、あまり好ましくない。   However, the arrangement of the discharge electrode shown in FIG. 4A is such that the discharge electrode 5 is provided close to the front end of the dust collection pocket 6 (the side facing the gas flow direction, that is, the upstream end). Therefore, the deflection of the gas stream line is small and the flow velocity is increased, so that the effect of confining the particulate matter in the internal space of the dust collection pocket 6 is almost not preferred.

この粒子状物質の集塵ポケットへの押し込み効果を強くするには、図4の(B)に示すように、放電電極52および53をそれぞれ、対応する位置にある集塵ポケット62および63の前端から離し、その上流側の集塵ポケット61および62の後端側に接近して配置するようにするのがよい。   In order to increase the effect of pushing the particulate matter into the dust collection pocket, as shown in FIG. 4B, the discharge electrodes 52 and 53 are respectively connected to the front ends of the dust collection pockets 62 and 63 at the corresponding positions. It is good to arrange | position from the rear end side of the dust collection pockets 61 and 62 of the upstream from that.

放電電極をこのように配置すると、放電電極52,53と集塵ポケット6を含む集塵電極4との間の間隔が最も小さくなるのは、それぞれ対応する位置にある集塵ポケット62、63に隣接する上流側の集塵ポケット61、62となり、それぞれ上流側に隣接した集塵ポケットの後端付近で放電が発生し、最も大きな放電電流が流れるようになる。   When the discharge electrodes are arranged in this manner, the distance between the discharge electrodes 52 and 53 and the dust collecting electrode 4 including the dust collecting pocket 6 is the smallest in the dust collecting pockets 62 and 63 at the corresponding positions. Adjacent upstream dust collection pockets 61 and 62 are formed, and discharge occurs near the rear end of the dust collection pocket adjacent to the upstream side, respectively, so that the largest discharge current flows.

この結果、この部分に発生するイオン風Vibの流れ方向が、図4(B)に示すベクトル図のようにガス流の上流側を向くようになるため、流路2内を流れるガス主流線Voの方向がベクトル図における合成流Vrbのように深い角度で集塵電極4側へ偏向される。これにより流路2内のガス主流線Voは、合成ガス流Vrbとなって各集塵ポケット6の入口(内部空間の開口部)の前方で集塵電極4側に深く押し込まれるので、ガス流線に沿って移動する荷電された粒子状物質がこの合成ガス流Vrbによって、集塵ポケット6の内部空間に効率よく押し込まれ、粒子状物質の集塵ポケット6への押し込み効果を高めることができ、粒子状物質の捕集効率をより高めることができる。   As a result, the flow direction of the ion wind Vib generated in this portion is directed to the upstream side of the gas flow as shown in the vector diagram of FIG. 4B, and thus the main gas flow line Vo flowing in the flow path 2. Is deflected toward the dust collecting electrode 4 at a deep angle as in the combined flow Vrb in the vector diagram. As a result, the main gas flow line Vo in the flow path 2 becomes a synthesis gas flow Vrb and is pushed deeply into the dust collection electrode 4 in front of the entrance (opening portion of the internal space) of each dust collection pocket 6. The charged particulate matter moving along the line is efficiently pushed into the internal space of the dust collection pocket 6 by the synthesis gas flow Vrb, and the effect of pushing the particulate matter into the dust collection pocket 6 can be enhanced. Moreover, the collection efficiency of particulate matter can be further increased.

ここで、集塵ポケット6の粒子状物質を内部空間は、同電位の集塵電極4および集塵ポケット形成部材6Aによって形成されるので、空間電界強度が零の領域となる。このため、集塵ポケット6の内部空間に閉じ込められた粒子状物質は、荷電された電荷が集塵電極4、および集塵ポケット6を通して放出されて無電荷となり、これに静電誘導による剥離力が働くことがなくなる。また、集塵ポケット6の内部空間に閉じ込められた粒子状物質は、集塵ポケット6によりガス流路2を流れるガス流から遮断され、その影響を受けることがない。この結果、集塵電極の集塵ポケットの内部空間に保留された粒子状物質はここ閉じ込められ、ここから離脱して再飛散することはない。   Here, since the internal space of the particulate matter in the dust collection pocket 6 is formed by the dust collection electrode 4 and the dust collection pocket forming member 6A having the same potential, the space electric field intensity becomes a region of zero. For this reason, the particulate matter confined in the internal space of the dust collection pocket 6 is discharged through the dust collection electrode 4 and the dust collection pocket 6 to become non-charged. No longer works. In addition, the particulate matter confined in the internal space of the dust collection pocket 6 is blocked from the gas flow flowing through the gas flow path 2 by the dust collection pocket 6 and is not affected by it. As a result, the particulate matter retained in the internal space of the dust collection pocket of the dust collection electrode is confined here, and does not leave and rescatter.

集塵ポケットに捕集された粒子状物質の量が増えると、集塵ポケット6の内部空間内から自然に落下して、本体ケース1の底板7の連通孔7Aからホッパ8内に貯留されるようになり、集塵電極4は長期間安定して捕集作用を継続することが可能となるので再生処理周期を大幅に延ばすことができる。   When the amount of the particulate matter collected in the dust collection pocket increases, it naturally falls from the interior space of the dust collection pocket 6 and is stored in the hopper 8 from the communication hole 7A of the bottom plate 7 of the main body case 1. As a result, the dust collecting electrode 4 can stably continue the trapping action for a long period of time, so that the regeneration processing cycle can be greatly extended.

前記実施例においては、集塵電極に設ける集塵ポケットは、前端および上下端が開口し、後端が閉塞された構成のものを示したが、図5に示すように、集塵ポケット6の後端壁に微小の通風孔6Hを設け、集塵ポケット6内でガスの貫流を可能とすることにより、集塵ポケット6内での渦流の発生を抑えることができる。この結果、集塵ポケット内の粒子状物質の渦流による再飛散を防止することができる。   In the above-described embodiment, the dust collection pocket provided in the dust collection electrode has a configuration in which the front end and the upper and lower ends are open and the rear end is closed. However, as shown in FIG. By providing minute ventilation holes 6H on the rear end wall and allowing gas to flow through the dust collection pocket 6, the generation of vortex flow in the dust collection pocket 6 can be suppressed. As a result, re-scattering due to the vortex of the particulate matter in the dust collection pocket can be prevented.

また、この発明で使用する放電電極5は、図6の(a)ないし(e)に示すような各種の形状のものを使用することができる。   In addition, the discharge electrode 5 used in the present invention may have various shapes as shown in FIGS. 6 (a) to 6 (e).

(a)の電極は、細線で構成したものであり、最も構成が簡単となる。(b)の電極は棒状電極に針状の放電部を植え込んだものである。(c)は平板の電極板の両側面を鋸歯状に形成したものである。(d)は棒状電極に星形の平板の放電部を取り付けたものである。(e)は棒状電極に円板状の放電部を結合したものである。   The electrode (a) is constituted by a thin line, and the configuration is the simplest. The electrode (b) is obtained by implanting a needle-like discharge part into a rod-like electrode. (C) forms both side surfaces of a flat electrode plate in a sawtooth shape. (D) is a rod-shaped electrode provided with a star-shaped flat plate discharge portion. (E) is a rod-shaped electrode combined with a disc-shaped discharge portion.

この発明で使用する放電電極はここに示したものに限られるものでなく、その他の形状のものを使用することもできる。   The discharge electrodes used in the present invention are not limited to those shown here, and other shapes can also be used.

この発明の実施例による電気集塵装置の構成を示す、部分的な切欠きを含む斜視図である。It is a perspective view including a partial notch showing the configuration of the electrostatic precipitator according to the embodiment of the present invention. 図1のII−II線に沿う縦断面図である。It is a longitudinal cross-sectional view which follows the II-II line | wire of FIG. 図2のIII−III線に沿う横断面図である。FIG. 3 is a transverse sectional view taken along line III-III in FIG. 2. この発明の動作説明図である。It is operation | movement explanatory drawing of this invention. この発明に使用する集塵ポケット部の第1の変形例を示す断面図である。It is sectional drawing which shows the 1st modification of the dust collection pocket part used for this invention. この発明に使用する放電電極の形状を示す図である。It is a figure which shows the shape of the discharge electrode used for this invention.

符号の説明Explanation of symbols

1:電気集塵装置
2:ガス流路
3:本体ケース
4:集塵電極
5:放電電極
6:集塵ポケット
1: Electric dust collector 2: Gas flow path 3: Body case 4: Dust collection electrode 5: Discharge electrode 6: Dust collection pocket

Claims (4)

粒子状物質を含むガスを流すガス流路中に放電電極と集塵電極とを対向配置し、両電極に高電圧を印加して前記ガス流路を流れるガス中の粒子状物質を帯電させて集塵電極により吸引して捕集するようにした電気集塵装置において、前記集塵電極の前記放電電極と対向し、ガス流と接する面に前記ガス流路中を流れるガスの流れ方向に間隔をおいて捕集した粒子状物質を保留する内部空間を備えた集塵ポケットを複数設けたことを特徴とする電気集塵装置。   Disposing a discharge electrode and a dust collecting electrode oppositely in a gas flow path for flowing a gas containing particulate matter, and applying a high voltage to both electrodes to charge the particulate matter in the gas flowing in the gas flow path. In the electrostatic precipitator adapted to be sucked and collected by the dust collecting electrode, an interval in the flow direction of the gas flowing in the gas flow path is opposed to the discharge electrode of the dust collecting electrode and in contact with the gas flow. An electrostatic precipitator comprising a plurality of dust collecting pockets having an internal space for holding particulate matter collected after the storage. 請求項1に記載のものにおいて、前記放電電極には前記集塵ポケットとほぼ同じ間隔で放電部を形成し、該放電部をそれぞれ前記各集塵ポケットの開口した前端から離した位置に配置することを特徴とする電気集塵装置。   2. The discharge electrode according to claim 1, wherein a discharge portion is formed in the discharge electrode at substantially the same interval as the dust collection pocket, and the discharge portion is disposed at a position separated from an open front end of each dust collection pocket. An electric dust collector characterized by that. 請求項1または2に記載のものにおいて、前記集塵ポケットは、前端の開口と対向した後壁にガス通流口を設けたことを特徴とする電気集塵装置。   3. The electrostatic precipitator according to claim 1, wherein the dust collection pocket is provided with a gas flow port on a rear wall facing the front end opening. 請求項1ないし3の何れか1項に記載のものおいて、前記集塵ポケットは、前記集塵電極に導電的に結合して前記集塵電極と同電位として、前記内部空間の空間電界強度を零としたことを特徴とする電気集塵装置。   4. The electric field strength of the internal space according to claim 1, wherein the dust collection pocket is electrically coupled to the dust collection electrode and has the same potential as the dust collection electrode. An electrostatic precipitator characterized by zeroing.
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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011245429A (en) * 2010-05-27 2011-12-08 Fuji Electric Co Ltd Electrostatic precipitator
CN102480894A (en) * 2010-11-22 2012-05-30 鸿富锦精密工业(深圳)有限公司 Container data center
JP2013187989A (en) * 2012-03-07 2013-09-19 Denso Corp Ehd fluid transporting apparatus
WO2014006736A1 (en) * 2012-07-06 2014-01-09 三菱重工メカトロシステムズ株式会社 Dust-collecting device
JP2016217298A (en) * 2015-05-22 2016-12-22 トヨタ自動車株式会社 Exhaust gas purification device
CN106925429A (en) * 2017-05-03 2017-07-07 广州市美控电子科技有限公司 Plane multiple spot discharge electrode plate
CN107427840A (en) * 2015-04-06 2017-12-01 安满能株式会社 Charge device and electrostatic (electric dust) precipitator
CN107477703A (en) * 2017-09-25 2017-12-15 广州市爱因电子有限公司 No material consumption inhales the antibacterial purification of air flat board of haze
CN107664049A (en) * 2017-10-25 2018-02-06 吉林大学 A kind of pressure swing type diesel particulation Electrostatic regenerative system and its control method
CN111691948A (en) * 2020-07-09 2020-09-22 合肥宝发动力技术股份有限公司 Non-maintaining diesel oil granule electricity catcher
KR102208166B1 (en) * 2020-02-27 2021-01-27 주식회사 오피스안건사 Hybrid partition with function for removing fine dust etc.

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4917781B1 (en) * 1968-11-19 1974-05-04
JPS5394362A (en) * 1977-01-31 1978-08-18 Toyo Ink Mfg Co Ltd Aqueous resin dispersion composition
JPS63126569A (en) * 1986-11-14 1988-05-30 Nippon Densetsu Kk Electrostatic precipitator
JPH11156236A (en) * 1997-11-21 1999-06-15 Sumitomo Heavy Ind Ltd Electric precipitator
JP2000189844A (en) * 1998-12-25 2000-07-11 Sumitomo Heavy Ind Ltd Electric dust precipitator

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4917781B1 (en) * 1968-11-19 1974-05-04
JPS5394362A (en) * 1977-01-31 1978-08-18 Toyo Ink Mfg Co Ltd Aqueous resin dispersion composition
JPS63126569A (en) * 1986-11-14 1988-05-30 Nippon Densetsu Kk Electrostatic precipitator
JPH11156236A (en) * 1997-11-21 1999-06-15 Sumitomo Heavy Ind Ltd Electric precipitator
JP2000189844A (en) * 1998-12-25 2000-07-11 Sumitomo Heavy Ind Ltd Electric dust precipitator

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011245429A (en) * 2010-05-27 2011-12-08 Fuji Electric Co Ltd Electrostatic precipitator
CN102480894A (en) * 2010-11-22 2012-05-30 鸿富锦精密工业(深圳)有限公司 Container data center
JP2013187989A (en) * 2012-03-07 2013-09-19 Denso Corp Ehd fluid transporting apparatus
WO2014006736A1 (en) * 2012-07-06 2014-01-09 三菱重工メカトロシステムズ株式会社 Dust-collecting device
CN107427840A (en) * 2015-04-06 2017-12-01 安满能株式会社 Charge device and electrostatic (electric dust) precipitator
JP2016217298A (en) * 2015-05-22 2016-12-22 トヨタ自動車株式会社 Exhaust gas purification device
US9988959B2 (en) 2015-05-22 2018-06-05 Toyota Jidosha Kabushiki Kaisha Exhaust purifying apparatus
CN106925429A (en) * 2017-05-03 2017-07-07 广州市美控电子科技有限公司 Plane multiple spot discharge electrode plate
CN107477703A (en) * 2017-09-25 2017-12-15 广州市爱因电子有限公司 No material consumption inhales the antibacterial purification of air flat board of haze
CN107664049A (en) * 2017-10-25 2018-02-06 吉林大学 A kind of pressure swing type diesel particulation Electrostatic regenerative system and its control method
CN107664049B (en) * 2017-10-25 2024-01-30 吉林大学 Pressure-variable diesel particulate static trapping and regenerating system and control method thereof
KR102208166B1 (en) * 2020-02-27 2021-01-27 주식회사 오피스안건사 Hybrid partition with function for removing fine dust etc.
WO2021172704A1 (en) * 2020-02-27 2021-09-02 주식회사 오피스안건사 Hybrid partition equipped with means for removing fine dust
US11167291B2 (en) 2020-02-27 2021-11-09 Office Angunsa Co., Ltd. Hybrid partition with function of removing fine dust
CN111691948A (en) * 2020-07-09 2020-09-22 合肥宝发动力技术股份有限公司 Non-maintaining diesel oil granule electricity catcher

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