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JP5705461B2 - Electric dust collector - Google Patents
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JP5705461B2 - Electric dust collector - Google Patents

Electric dust collector Download PDF

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JP5705461B2
JP5705461B2 JP2010121669A JP2010121669A JP5705461B2 JP 5705461 B2 JP5705461 B2 JP 5705461B2 JP 2010121669 A JP2010121669 A JP 2010121669A JP 2010121669 A JP2010121669 A JP 2010121669A JP 5705461 B2 JP5705461 B2 JP 5705461B2
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electrode
particulate matter
cylindrical
cylindrical electrode
casing
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JP2011245429A (en
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将隆 吉田
将隆 吉田
貴誌 乾
貴誌 乾
康史 三塚
康史 三塚
瑞慶覧 章朝
章朝 瑞慶覧
一美 川上
一美 川上
山本 俊昭
俊昭 山本
由泰 江原
由泰 江原
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Fuji Electric Co Ltd
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Description

本発明は、粒子状物質(PM:Particulate Matter)を含有する例えば内燃機関の排気ガス等の粒子状物含有ガス中から粒子状物質を除去するようにした電気集塵装置に関する。   The present invention relates to an electrostatic precipitator configured to remove particulate matter from particulate matter-containing gas such as exhaust gas of an internal combustion engine that contains particulate matter (PM).

内燃機関から排出される排気ガスには、NOx、SOxの他、炭素を主成分とする粒子状物質などの有害物質が含まれている。人間が呼吸により粒子状物質を体内に吸い込むと様々な健康被害が発生することが知られており、粒子状物質を効率良く除去する粒子状物質除去装置の開発が望まれている。
このような粒子状物質除去装置として、排気ダクト中に、フィルタを設置する方向があるが、フィルタは目詰まりし易く、圧力損失が大きいなどの課題がある。これに対して電気集塵装置は、目詰まりせず、圧力損失が小さいため、内燃機関の排気ダクトに取り付けるには有効である。
Exhaust gas discharged from an internal combustion engine contains NOx, SOx, and harmful substances such as particulate matter containing carbon as a main component. It is known that various human health hazards occur when a human inhales particulate matter into the body by breathing, and development of a particulate matter removing device that efficiently removes particulate matter is desired.
As such a particulate matter removing device, there is a direction in which a filter is installed in the exhaust duct. However, the filter is easily clogged and has problems such as a large pressure loss. On the other hand, the electrostatic precipitator is not clogged and has a small pressure loss.

このような電気集塵方式の粒子状物質除去装置としては、例えば図8に示すように、粒子状物質を含むガス流れの中に放電電極101と、この放電電極101と対向して設けられたろ過装置102と、放電電極101及びろ過装置102間に高電圧を印加する高圧電源103と、ろ過装置102を通過するガス流を調節する抽気用送風機104と、排気ガスを吸引する主送風機105とを備えた除じん装置が知られている(例えば、特許文献1参照)。同様に、図9に示すように、抽気用送風機104を省略し、これに代えてガス出口を2つに分流させて、各ガス出口に圧損調整用のダンパ110を設けるようにした除じん装置も知られている(例えば、特許文献1参照)。   For example, as shown in FIG. 8, a discharge electrode 101 and a discharge electrode 101 are provided in the gas flow containing the particulate matter so as to face the discharge electrode 101 as an electric dust collection system. A filtration device 102, a high-voltage power supply 103 that applies a high voltage between the discharge electrode 101 and the filtration device 102, a bleeder fan 104 that adjusts a gas flow that passes through the filtration device 102, and a main blower 105 that sucks exhaust gas Is known (for example, refer to Patent Document 1). Similarly, as shown in FIG. 9, the bleeder 104 is omitted, and instead of this, the gas outlet is divided into two, and a dust drop adjustment damper 110 is provided at each gas outlet. Is also known (see, for example, Patent Document 1).

また、図10及び図11に示すように、粒子状物質を含むガス流れの中に放電電極101と、この放電電極101と対向して設けられた対向電極107をもつろ過装置102と、放電電極101及びろ過装置102間に高電圧を印加する高圧電源103と、ろ過手段102内又はその背面に閉鎖された閉鎖空間108を備えた除じん装置が知られている(例えば、特許文献2参照)。   Further, as shown in FIGS. 10 and 11, a discharge device 101 in a gas flow containing particulate matter, a filtration device 102 having a counter electrode 107 provided to face the discharge electrode 101, and a discharge electrode There is known a dust removal apparatus including a high voltage power supply 103 that applies a high voltage between the filter 101 and the filtration device 102, and a closed space 108 that is closed in or on the back of the filtration means 102 (see, for example, Patent Document 2). .

特開平2−63560号公報Japanese Patent Laid-Open No. 2-63560 特開平2−184357号公報JP-A-2-184357

しかしながら、上記特許文献1に記載の図8に示す従来例にあっては、抽気用送風機104によりろ過装置102を通るガスの排気量を調整するが、ろ過装置102はサブミクロンオーダーの大きさである粒子状物質をろ過するためには十分に目が細かいものを使用する必要があるので、ろ過装置102による圧損が大きくなり、抽気用送風機104として、容量が大きなものが必要となる。この場合には、ある程度の時間運転すると、図12に示すように、ろ過装置102に粒子状物質109が詰まって目詰まりが生じて、集塵不可能となるため、ろ過装置102の交換が頻繁に必要となるという未解決の課題がある。逆に、抽気用送風機104の容量が小さい場合には、ろ過装置102を通過する風量が小さいため、図13に示すように、粒子状物質109がろ過装置102の表面付近に集中して補集されることになり、その場合、補集された粒子状物質109が主ガス流に晒されてしまうために、主ガス流の風速が高い条件化では、主ガス流の抗力によってろ過装置102の表面に補集された粒子状物質が引き剥がされて再飛散してしまうという未解決の課題がある。   However, in the conventional example shown in FIG. 8 described in Patent Document 1 described above, the amount of gas passing through the filtration device 102 is adjusted by the extraction blower 104, but the filtration device 102 has a size on the order of submicrons. In order to filter a certain particulate matter, it is necessary to use a sufficiently fine one, so that the pressure loss due to the filtration device 102 becomes large, and the bleed air blower 104 needs to have a large capacity. In this case, if the system is operated for a certain period of time, as shown in FIG. 12, the particulate matter 109 is clogged in the filtration device 102 and clogging occurs, making dust collection impossible. Therefore, the filtration device 102 is frequently replaced. There is an unresolved issue that is necessary for On the other hand, when the capacity of the extraction fan 104 is small, the amount of air passing through the filtration device 102 is small, so that the particulate matter 109 is concentrated near the surface of the filtration device 102 as shown in FIG. In this case, since the collected particulate matter 109 is exposed to the main gas flow, under conditions where the wind speed of the main gas flow is high, the drag of the filter 102 is caused by the drag of the main gas flow. There is an unsolved problem that the particulate matter collected on the surface is peeled off and scattered again.

同様に、特許文献1に記載されている図9に示す従来例にあっても、抽気用送風機を省略することができるが、圧損調整ダンパ110によりろ過装置102の抽気量を調整するので、ろ過装置102としてはサブミクロンオーダーの大きさである粒子状物質をろ過するためには十分に目が細かいものを使用する必要があるので、ろ過装置102による圧損が大きくなり、圧損調整ダンパ110を大きく閉じた状態にする必要がある。この場合、圧損調整ダンパ110による主ガス流の圧損が大きくなるため、送風機105に容量の大きなものが必要となる。また、図12に示すように、ある程度の時間運転すると、ろ過装置102に目詰まりが生じて、集塵不可能となるという未解決の課題がある。逆に、圧損調整ダンパ110の閉じ量が小さい場合には、送風機105の容量は小さくてよいが、ろ過装置102を通過する風量が小さいために、図13に示すように、ろ過装置102の表面に補集された粒子状物質109が引き剥がされ、再飛散が生じてしまうという未解決の課題がある。また、圧損調整ダンパ110のような可動機構は、高温の排ガス中においては、故障の危険性が非常に高いという未解決の課題もある。   Similarly, even in the conventional example shown in FIG. 9 described in Patent Document 1, a blower for extraction can be omitted, but the amount of extraction of the filtration device 102 is adjusted by the pressure loss adjustment damper 110, so that filtration is performed. As the device 102, it is necessary to use a sufficiently fine one in order to filter the particulate matter having a size of the order of submicron. Therefore, the pressure loss due to the filtration device 102 becomes large, and the pressure loss adjusting damper 110 is enlarged. Must be closed. In this case, the pressure loss of the main gas flow caused by the pressure loss adjusting damper 110 becomes large, so that the fan 105 needs to have a large capacity. Further, as shown in FIG. 12, there is an unsolved problem that when the operation is performed for a certain period of time, the filtration device 102 is clogged and dust collection becomes impossible. On the contrary, when the closing amount of the pressure loss adjusting damper 110 is small, the capacity of the blower 105 may be small, but since the amount of air passing through the filtration device 102 is small, the surface of the filtration device 102 as shown in FIG. There is an unsolved problem that the particulate matter 109 collected in the film is peeled off and re-scattering occurs. In addition, the movable mechanism such as the pressure loss adjusting damper 110 has an unsolved problem that the risk of failure is extremely high in high-temperature exhaust gas.

また、特許文献2に記載された図10に示す従来例にあっては、放電電極101と対向電極107との間に生じるイオン風による二次流れは、最大風速2m/s程度である。ろ過装置102はサブミクロンオーダーの大きさである粒子状物質をろ過するためには十分目が細かいものを使用する必要があり、ろ過装置102による圧損が大きいため、イオン風による二次流れのみで、ろ過装置102をガスが十分に通過することが困難であり、図14に示すように、粒子状物質109はろ過装置102の表面付近に集中して補集される。この場合、補集された粒子状物質が主ガス流に晒されてしまうために、主ガス流の風速が高い条件化では主ガス流の抗力によってろ過装置102の表面に補集された粒子状物質109が引き剥がされ、再飛散が生じてしまうという未解決の課題がある。
そこで、本発明は、上記従来例の未解決の課題に着目してなされたものであり、容量の大きな抽気装置を必要とすることなく、目詰まりせずに、高風速条件下でも再飛散しにくく、高い集塵性能を発揮し、故障の可能性が低い電気集塵装置を提供することを目的としている。
Further, in the conventional example shown in FIG. 10 described in Patent Document 2, the secondary flow caused by the ion wind generated between the discharge electrode 101 and the counter electrode 107 has a maximum wind speed of about 2 m / s. It is necessary to use a filtration device 102 that is sufficiently fine to filter particulate matter having a size on the order of submicrons. Since the pressure loss due to the filtration device 102 is large, only a secondary flow caused by an ion wind can be used. It is difficult for the gas to sufficiently pass through the filtration device 102, and the particulate matter 109 is concentrated and collected near the surface of the filtration device 102 as shown in FIG. In this case, since the collected particulate matter is exposed to the main gas flow, the particulate matter collected on the surface of the filtration device 102 by the drag of the main gas flow under conditions where the wind speed of the main gas flow is high. There is an unsolved problem that the substance 109 is peeled off and re-scattering occurs.
Therefore, the present invention has been made paying attention to the above-mentioned unsolved problems of the conventional example, and does not require a large-capacity bleeder and does not clog and re-scatters even under high wind speed conditions. It is an object of the present invention to provide an electrostatic precipitator that is difficult, exhibits high dust collection performance, and has a low possibility of failure.

上記目的を達成するために、本発明の一の形態に係る電気集塵装置は、筒状電極と、該筒状電極の中央部に配置される放電電極とを備え、前記筒状電極の内部に集塵対象ガスを通流させた状態で前記筒状電極と前記放電電極間に電圧を印加してコロナ放電を発生させることにより、前記集塵対象ガス中の粒子状物質を帯電させて前記筒状電極側で吸引して捕集する電気集塵装置である。そして、前記筒状電極に前記粒子物質を通過させる貫通孔を複数形成するとともに、前記筒状電極を当該筒状電極より大きな筒状のケーシング電極の内部に配置し、前記筒状電極の外面と前記ケーシング電極の内面との間に、前記粒子状物質を捕集する補集空間が形成され、当該補集空間に複数の補助電極を配置し、前記筒状電極、前記ケーシング電極及び前記補助電極を同一電位としている。 In order to achieve the above object, an electrostatic precipitator according to an embodiment of the present invention includes a cylindrical electrode and a discharge electrode disposed at a central portion of the cylindrical electrode, and the inside of the cylindrical electrode. The particulate matter in the dust collection target gas is charged by applying a voltage between the cylindrical electrode and the discharge electrode in a state where the dust collection target gas is allowed to flow to generate corona discharge. An electrostatic precipitator that sucks and collects on the cylindrical electrode side. Then, a through hole for passing the pre-Symbol particulate material prior Symbol tubular electrode together with forming a plurality of, the cylindrical electrode and placed inside a larger cylindrical casing electrode from the cylindrical electrodes, the tubular electrode A collecting space for collecting the particulate matter is formed between the outer surface of the casing electrode and the inner surface of the casing electrode, and a plurality of auxiliary electrodes are disposed in the collecting space, the cylindrical electrode, the casing electrode, The auxiliary electrodes have the same potential .

この構成によると、放電電極筒状電極間に発生するコロナ放電によって、集塵対象ガス中の粒子状物質を帯電させ、クーロン力によって貫通孔を通じて前記筒状電極の外面と前記ケーシング電極の内面との間に形成される補集空間内に移動させて補集空間内に補集させる。
また、補集空間内に補助電極が配置されているので、粒子状物質の補集領域を拡大して粒子状物質を補集する許容限界量を大幅に増加させることができる。
According to this configuration, the particulate matter in the dust collection target gas is charged by corona discharge generated between the discharge electrode and the cylindrical electrode, and the outer surface of the cylindrical electrode and the inner surface of the casing electrode are passed through the through-hole by Coulomb force. In the collection space formed between the two and the collection space.
Further, since the auxiliary electrode is arranged in the collection space, the allowable limit amount for collecting the particulate matter can be greatly increased by expanding the collection region of the particulate matter.

また、本発明の他の形態に係る電気集塵装置は、前記補集空間に、液体を噴霧するノズルが配置され、当該ノズルから前記補集空間に補集された粒子状物質に液体が噴霧される。
この構成によると、補集空間内においてノズルから液体を噴霧して粒子状物質を湿らせ、液体の表面張力によって粒子状物質の電極との吸着力を増加させて、再飛散を抑制する。
In the electrostatic precipitator according to another aspect of the present invention, a nozzle that sprays liquid is disposed in the collection space, and the liquid is sprayed from the nozzle to the particulate matter collected in the collection space. Is done.
According to this configuration, the liquid is sprayed from the nozzle in the collection space to wet the particulate matter, and the adsorption force of the particulate matter with the electrode is increased by the surface tension of the liquid, thereby suppressing re-scattering.

本発明によれば、内部に放電電極を配置した筒状電極に複数の貫通孔を形成するとともに、筒状電極をケーシング電極で覆うことにより、補集空間を形成したので、放電電極及び筒状電極間にコロナ放電を発生させて、粒子状物質を負に帯電させ、クーロン力によって貫通孔を通じて補集空間内に移動させて、補集空間内で粒子状物質を補集することができ、容量の大きな抽出用送風機を設ける必要がないとともに、貫通孔を粒子状物質に比較して大きな径とすることにより、目詰まりを生じることがなく、さらに高風速条件下でも再飛散しにくく、高い集塵性能を発揮することができ、故障が発生しにくい電気集塵装置を提供することができる。   According to the present invention, since the plurality of through holes are formed in the cylindrical electrode in which the discharge electrode is disposed, and the collecting electrode is formed by covering the cylindrical electrode with the casing electrode, the discharge electrode and the cylindrical shape are formed. Corona discharge is generated between the electrodes, the particulate matter is negatively charged, and moved into the collection space through the through hole by Coulomb force, and the particulate matter can be collected in the collection space, It is not necessary to provide a large-capacity extraction blower, and by making the through-hole have a larger diameter than that of the particulate matter, clogging does not occur, and re-scattering is difficult even under high wind speed conditions. It is possible to provide an electric dust collector that can exhibit dust collection performance and is less likely to fail.

本発明に係る電気集塵装置の第1の実施形態を示す中央部を断面とした斜視図である。It is the perspective view which made the cross section the center part which shows 1st Embodiment of the electrical dust collector which concerns on this invention. 粒子状物質の補集状態を示す模式図である。It is a schematic diagram which shows the collection state of a particulate matter. 本発明に係る電気集塵装置の第2の実施形態を示す要部を断面とした斜視図である。It is the perspective view which made the cross section the principal part which shows 2nd Embodiment of the electrostatic precipitator which concerns on this invention. 図3のA−A線上の断面図である。It is sectional drawing on the AA line of FIG. 本発明に係る電気集塵装置の第3の実施形態を示す縦断面図である。It is a longitudinal cross-sectional view which shows 3rd Embodiment of the electrical dust collector which concerns on this invention. 本発明に係る電気集塵装置の第4の実施形態を示す縦断面図である。It is a longitudinal cross-sectional view which shows 4th Embodiment of the electrical dust collector which concerns on this invention. 本発明に係る電気集塵装置の第5の実施形態を示す横断面図である。It is a cross-sectional view showing a fifth embodiment of the electrostatic precipitator according to the present invention. 従来例を示す説明図である。It is explanatory drawing which shows a prior art example. 他の従来例を示す説明図である。It is explanatory drawing which shows another prior art example. さらに他の従来例を示す説明図である。It is explanatory drawing which shows another prior art example. 図10のろ過装置の詳細構成図である。It is a detailed block diagram of the filtration apparatus of FIG. ろ過装置における粒子状物質の補集状態を示す模式図である。It is a schematic diagram which shows the collection state of the particulate matter in a filtration apparatus. ろ過装置における粒子状物質の再飛散状態を示す模式図である。It is a schematic diagram which shows the re-scattering state of the particulate matter in a filtration apparatus. ろ過装置における粒子状物質の再飛散状態を示す模式図である。It is a schematic diagram which shows the re-scattering state of the particulate matter in a filtration apparatus.

以下、本発明の実施の形態を図面に基づいて説明する。
図1は本発明の第1の実施形態を示す中央部を断面とした斜視図である。
図中、1は例えば内燃機関特にディーゼルエンジンの排気ガス中に含まれる炭素を主成分とする粒子径が100μm以下の粒子状物質(PM:Particulate Matter)、特に粒子径が10μm以下の浮遊粒子状物質(SPM:Suspended Particulate Matter)を補集可能な電気集塵装置である。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a perspective view with a cross section taken at the center showing the first embodiment of the present invention.
In the figure, reference numeral 1 denotes, for example, particulate matter (PM: Particulate Matter) having a particle size of 100 μm or less, mainly containing carbon contained in the exhaust gas of an internal combustion engine, particularly a diesel engine, in particular, a suspended particle shape having a particle size of 10 μm or less It is an electrostatic precipitator capable of collecting a substance (SPM: Suspended Particulate Matter).

この電気集塵装置1は、中心部に放電電極2を配置し、この放電電極2と同軸的に例えば円筒状の筒状電極3が配設され、この筒状電極3が例えば方形角筒状のケーシング電極4によって囲まれた構成を有する。そして、放電電極2と筒状電極3との間の空間が粒子状物質5を含む排気ガス6を通過させるガス流路7とされている。
放電電極2は、断面円形の棒状導体2aを有する。この棒状導体2aの外周面には、軸方向に所定間隔を保ち、且つ円周方向に所定間隔(例えば90°)を保って多数の針状電極部2bが突出形成されている。
In the electrostatic precipitator 1, a discharge electrode 2 is arranged at the center, and a cylindrical electrode 3 is disposed coaxially with the discharge electrode 2, for example, and the cylindrical electrode 3 is formed in, for example, a rectangular rectangular tube. The casing electrode 4 is surrounded. A space between the discharge electrode 2 and the cylindrical electrode 3 is a gas flow path 7 through which the exhaust gas 6 including the particulate matter 5 passes.
The discharge electrode 2 has a rod-shaped conductor 2a having a circular cross section. On the outer peripheral surface of the rod-shaped conductor 2a, a large number of needle-like electrode portions 2b are formed so as to protrude at a predetermined interval in the axial direction and at a predetermined interval (for example, 90 °) in the circumferential direction.

筒状電極3は、放電電極2の針状電極部2bと所定間隔を保って対向するように例えば円筒状のステンレスパイプ3aで構成されている。このステンレスパイプ3aは、放電電極2の針状電極部2bと対向する位置に、粒子状物質4の粒子径より十分に大きい直径(例えば数mm程度)を有する多数の貫通孔3bが形成されたパンチングパイプが適用されている。   The cylindrical electrode 3 is composed of, for example, a cylindrical stainless steel pipe 3a so as to face the needle-like electrode portion 2b of the discharge electrode 2 with a predetermined interval. In the stainless steel pipe 3a, a large number of through holes 3b having a diameter (for example, about several mm) sufficiently larger than the particle diameter of the particulate matter 4 are formed at positions facing the needle-like electrode portion 2b of the discharge electrode 2. A punching pipe is applied.

ケーシング電極4は、筒状電極3の外周側に筒状電極3の外周面に対して所定距離離れて対向する導電性を有する角枠板部4aと、この角枠板部4aの軸方向両端面と筒状電極3の軸方向両端面との間を連結する端板部4bとで構成されている。そして、筒状電極3の外周面とケーシング電極4の角枠板部4a及び端板部4bの内周面とで補集空間としての半閉空間8が形成されている。この半閉空間8は、筒状電極3の貫通孔3aを介してガス流路7と連通されている。
また、放電電極2とケーシング電極4との間には、ケーシング電極4に正極を接続し、放電電極2に負極を接続した例えば103〜105ボルト程度の高電圧を印加する高圧電源9が接続され、この高圧電源9の正極側が接地されている。
The casing electrode 4 includes a rectangular frame plate portion 4a having conductivity facing the outer peripheral surface of the cylindrical electrode 3 at a predetermined distance on the outer peripheral side of the cylindrical electrode 3, and both axial ends of the rectangular frame plate portion 4a. It is comprised by the end-plate part 4b which connects between the surface and the axial direction both end surfaces of the cylindrical electrode 3. As shown in FIG. A semi-closed space 8 as a collecting space is formed by the outer peripheral surface of the cylindrical electrode 3 and the inner peripheral surfaces of the square frame plate portion 4 a and the end plate portion 4 b of the casing electrode 4. This semi-closed space 8 communicates with the gas flow path 7 through the through hole 3 a of the cylindrical electrode 3.
Further, between the discharge electrode 2 and the casing electrode 4, there is a high voltage power source 9 for applying a high voltage of about 10 3 to 10 5 volts, for example, having a positive electrode connected to the casing electrode 4 and a negative electrode connected to the discharge electrode 2. The high-voltage power supply 9 is connected to the positive electrode side and grounded.

次に、上記第1の実施形態の動作を説明する。
高圧電源9から放電電極2と筒状電極3及びケーシング電極4との間に高電圧を印加することにより、放電電極2の針状電極部2bの先端から筒状電極3に向けてガス流路7を横切るコロナ放電が生じる。
この状態で、ガス流路7に内燃機関等から排出される粒子状物質5を含む粒子状物質含有ガスとしての排気ガスを流すと、粒子状物質5はコロナ放電を浴びて帯電する。そして、放電電極2と筒状電極3間の電界により粒子状物質5にクーロン力が働き、筒状電極3へ向けて運動を始める。粒子状物質5は質量を持つために、慣性力によってそのまま筒状電極3の貫通孔3bを通過して半閉空間(補集空間)8に導かれる。
Next, the operation of the first embodiment will be described.
By applying a high voltage between the discharge electrode 2 and the cylindrical electrode 3 and the casing electrode 4 from the high-voltage power supply 9, the gas flow path is directed from the tip of the needle electrode portion 2 b of the discharge electrode 2 toward the cylindrical electrode 3. Corona discharge across 7 occurs.
In this state, when an exhaust gas as a particulate matter-containing gas containing particulate matter 5 discharged from an internal combustion engine or the like is caused to flow through the gas flow path 7, the particulate matter 5 is charged by corona discharge. The Coulomb force acts on the particulate matter 5 by the electric field between the discharge electrode 2 and the cylindrical electrode 3 and starts to move toward the cylindrical electrode 3. Since the particulate matter 5 has a mass, it passes through the through-hole 3b of the cylindrical electrode 3 as it is and is guided to the semi-closed space (collection space) 8 by inertia force.

この半閉空間8では、流れ場は非常に緩やかなため、粒子状物質5は流れ場の影響を受けにくく、粒子状物質5は自分自身の電荷と筒状電極3及びケーシング電極4間の電位差による電気影像力を受けて、図2に模式的に示すように、筒状電極3の外周面及びケーシング電極4の内周面に移動付着して補集される。なお、数値解析によれば、ガス流路7における排気ガス主流の流速に比べ、半閉空間8の大部分で約1/20〜1/10程度、局所的に1/4程度の流速となることが確認されている。   In this semi-closed space 8, the flow field is very gentle, so that the particulate matter 5 is not easily affected by the flow field, and the particulate matter 5 has its own charge and the potential difference between the cylindrical electrode 3 and the casing electrode 4. 2 is received and collected on the outer peripheral surface of the cylindrical electrode 3 and the inner peripheral surface of the casing electrode 4 as schematically shown in FIG. According to the numerical analysis, compared with the flow rate of the main flow of the exhaust gas in the gas flow path 7, the flow rate is about 1/20 to 1/10 in most of the semi-closed space 8 and locally about 1/4. It has been confirmed.

このように、上記第1の実施形態によれば、単に放電電極2及び筒状電極3間のガス流路7に排気ガスを通流させるだけで、抽気手段としての送風機等を設ける必要がない。また、排気ガスの流れを妨げるダンパ等を設ける必要もないので、排気ガスの圧力損失を少なくすることができる。さらに、筒状電極3に形成した貫通孔3bの径を粒子状物質5の粒子径にかかわらず大きな径に形成することができるので、この分の圧力損失も小さく抑制することができる。さらに、粒子状物質5が半閉空間8を構成する筒状電極3の外周面やケーシング電極4の内周面で補集するので、両電極3及び4の表面積に応じた多量の粒子状物質5の補集を許容することができるとともに、貫通孔3bは極めて目詰まりしにくく、目詰まりによる補集障害を生じることを確実に防止することができる。さらにまた、半閉空間8の流れ場が小さいために、一度補集した粒子状物質5の再飛散が生じにくい。また、ダンパや送風機等の可動部が存在しないために、故障の可能性が極めて低いという種々の効果を得ることができる。   Thus, according to the first embodiment, the exhaust gas is simply passed through the gas flow path 7 between the discharge electrode 2 and the cylindrical electrode 3, and there is no need to provide a blower or the like as a bleeder. . Further, since it is not necessary to provide a damper or the like that obstructs the flow of exhaust gas, the pressure loss of exhaust gas can be reduced. Furthermore, since the diameter of the through-hole 3b formed in the cylindrical electrode 3 can be formed to a large diameter regardless of the particle diameter of the particulate matter 5, it is possible to suppress the pressure loss correspondingly. Further, since the particulate matter 5 is collected on the outer peripheral surface of the cylindrical electrode 3 constituting the semi-closed space 8 and the inner peripheral surface of the casing electrode 4, a large amount of particulate matter corresponding to the surface areas of both electrodes 3 and 4 is obtained. 5 can be allowed, and the through-hole 3b is extremely difficult to be clogged, so that it is possible to reliably prevent a collection failure due to clogging. Furthermore, since the flow field of the semi-closed space 8 is small, it is difficult for the particulate matter 5 collected once to re-scatter. In addition, since there are no movable parts such as dampers and blowers, various effects that the possibility of failure is extremely low can be obtained.

次に、本発明の第2の実施形態を図3及び図4について説明する。
この第2の実施形態では、排気ガス流量を増大させることが可能としたものである。
すなわち、第2の実施形態では、図3及び図4に示すように、前述した第1の実施形態における図1の構成において、複数例えば2つの放電電極2A及び2Bを個別に内装した2つの筒状電極3A及び3Bを軸直角方向に両者間に所定の半閉空間8を形成するように同一平面状に並行配置されている。そして、各筒状電極3A及び3Bの外周側を、所定間隔を保って角筒状のケーシング電極4で覆うようにしている。この図3の構成において、図1との対応部分には同一符号を付し、その詳細説明はこれを省略する。
Next, a second embodiment of the present invention will be described with reference to FIGS.
In the second embodiment, the exhaust gas flow rate can be increased.
That is, in the second embodiment, as shown in FIGS. 3 and 4, in the configuration of FIG. 1 in the first embodiment described above, a plurality of, for example, two tubes each having two discharge electrodes 2A and 2B are individually provided. The parallel electrodes 3A and 3B are arranged in parallel in the same plane so as to form a predetermined semi-closed space 8 between them in the direction perpendicular to the axis. And the outer peripheral side of each cylindrical electrode 3A and 3B is covered with the square cylindrical casing electrode 4 at predetermined intervals. In the configuration of FIG. 3, the same reference numerals are given to the portions corresponding to those in FIG.

この第2の実施形態においては、放電電極2A及び2Bと筒状電極3A及び3Bとで2つのガス流路7A及び7Bが形成されるので、排気ガスの通流面積を増加させて、排気ガスの流速を抑制することができる。大流量の排気ガスでも粒子状物質5の良好な補集機能を発揮することができる。この場合、粒子状物質5を補集すべき排気ガス流量が多いときには、排気ガス流量に応じて放電電極2及び筒状電極3の組数を増加させればよく、ガス流路7の排気ガス流速を適正に制御して、良好な集塵性能を発揮することができる。   In the second embodiment, since the two gas flow paths 7A and 7B are formed by the discharge electrodes 2A and 2B and the cylindrical electrodes 3A and 3B, the exhaust gas flow area is increased and the exhaust gas is increased. The flow rate of can be suppressed. A good collection function of the particulate matter 5 can be exhibited even with a large flow rate of exhaust gas. In this case, when the exhaust gas flow rate for collecting the particulate matter 5 is large, the number of sets of the discharge electrode 2 and the cylindrical electrode 3 may be increased according to the exhaust gas flow rate, and the exhaust gas in the gas flow path 7 is increased. It is possible to appropriately control the flow rate and exhibit good dust collection performance.

次に、本発明の第3の実施形態を図5について説明する。
この第3の実施形態においては、半閉空間8内における粒子状物質5の補集性能を向上させるようにしたものである。
すなわち、第3の実施形態では、図5に示すように、筒状電極3及びケーシング電極4で構成される半閉空間8内に筒状電極3の貫通孔3bを除く外周面とケーシング電極4の四隅との間に例えば4つの補助電極11を放射状に設けるようにしている。
この第3の実施形態によると、半閉空間8内に4つの補助電極11が付加されているので、これら補助電極11の表面積分だけ粒子状物質5の補集面積を増加させることができる。このため、粒子状物質5の補集許容量を前述した第1の実施形態に比較して大幅に増加させることができる。
Next, a third embodiment of the present invention will be described with reference to FIG.
In the third embodiment, the collection performance of the particulate matter 5 in the semi-closed space 8 is improved.
That is, in the third embodiment, as shown in FIG. 5, the outer peripheral surface excluding the through hole 3 b of the cylindrical electrode 3 and the casing electrode 4 in the semi-closed space 8 constituted by the cylindrical electrode 3 and the casing electrode 4. For example, four auxiliary electrodes 11 are provided radially between the four corners.
According to the third embodiment, since the four auxiliary electrodes 11 are added in the semi-closed space 8, the collection area of the particulate matter 5 can be increased by the surface integral of these auxiliary electrodes 11. For this reason, the collection allowable amount of the particulate matter 5 can be significantly increased as compared with the first embodiment described above.

次に、本発明の第4の実施形態を図6について説明する。
この第4の実施形態でも、前述した第3の実施形態と同様に、半閉空間8内における粒子状物質5の補集性能を向上させたものである。
すなわち、第4の実施形態では、図6に示すように、筒状電極3及びケーシング電極4で構成される半閉空間8内に筒状電極3と同軸的に4つの断面円弧状の補助電極12が形成されている。これら補助電極12は軸方向の両端がそれぞれケーシング電極4の端板部4bに連結され、ケーシング電極4を介して高圧電源9の正極側に接続されている。
Next, a fourth embodiment of the present invention will be described with reference to FIG.
Also in the fourth embodiment, the collection performance of the particulate matter 5 in the semi-closed space 8 is improved as in the third embodiment described above.
That is, in the fourth embodiment, as shown in FIG. 6, the auxiliary electrode having four arcs in cross section coaxially with the cylindrical electrode 3 in the semi-closed space 8 constituted by the cylindrical electrode 3 and the casing electrode 4. 12 is formed. Both ends of the auxiliary electrode 12 in the axial direction are connected to the end plate portion 4 b of the casing electrode 4, and are connected to the positive electrode side of the high-voltage power supply 9 through the casing electrode 4.

この第4の実施形態によると、前述した第3の実施形態と同様に半閉空間8内に4つの補助電極12が形成されているので、これら補助電極11の表面積分だけ粒子状物質5の補集面積を増加させることができる。このため、粒子状物質5の補集許容量を前述した第1の実施形態に比較して大幅に増加させることができる。
なお、上記第3及び第4の実施形態においては、補助電極11及び12を設けた場合について説明したが、これに限定されるものではなく、補助電極11の半径方向の中間部に補助電極12を形成して、さらに粒子状物質5の補集面積を増加させるようにしてもよい。
According to the fourth embodiment, since the four auxiliary electrodes 12 are formed in the semi-closed space 8 as in the third embodiment described above, the amount of the particulate matter 5 by the surface integral of these auxiliary electrodes 11 is increased. The collection area can be increased. For this reason, the collection allowable amount of the particulate matter 5 can be significantly increased as compared with the first embodiment described above.
In the third and fourth embodiments, the case where the auxiliary electrodes 11 and 12 are provided has been described. However, the present invention is not limited to this, and the auxiliary electrode 12 is provided in the middle portion of the auxiliary electrode 11 in the radial direction. May be formed to further increase the collection area of the particulate matter 5.

次に、本発明の第5の実施形態を図7について説明する。
この第5の実施形態では、半閉空間8内に粒子状物質5をより確実に補集するようにしたものである。
すなわち、第5の実施形態では、図7に示すように、ケーシング電極4の軸方向両端の端板部4bにそれぞれ液体をミスト状に噴出するノズル15を配設したことを除いては前述した第1の実施形態における図1と同様の構成を有する。したがって、図7において、図1との対応部分には同一符号を付し、その詳細説明はこれを省略する。ここで、ノズル15から噴霧する液体としては、排気ガス温度が低い場合には、水を使用し、排気ガス温度が高い場合には、融点の高いオイルなどを使用する。
Next, a fifth embodiment of the present invention will be described with reference to FIG.
In the fifth embodiment, the particulate matter 5 is more reliably collected in the semi-closed space 8.
That is, in the fifth embodiment, as shown in FIG. 7, it is described above except that the nozzles 15 for ejecting the liquid in a mist form are arranged on the end plate portions 4b at both ends in the axial direction of the casing electrode 4, respectively. The configuration is the same as in FIG. 1 in the first embodiment. Therefore, in FIG. 7, the same reference numerals are given to the parts corresponding to those in FIG. 1, and the detailed description thereof will be omitted. Here, as the liquid sprayed from the nozzle 15, water is used when the exhaust gas temperature is low, and oil with a high melting point is used when the exhaust gas temperature is high.

この第5の実施形態によると、半閉空間8内にノズル15から液体をミスト状にして噴霧するので、コロナ放電によって帯電されて、クーロン力によって半閉空間8内に導入されて筒状電極3の外周面及びケーシング電極4の内周面に補集された粒子状物質5が液体ミストを浴びることによって湿る。このため、液体の表面張力によって粒子状物質5の筒状電極3又はケーシング電極4との吸着力が増加し、粒子状物質5が筒状電極3又はケーシング電極4の補集面から剥離して再飛散することに対して大きな抑制効果を発揮することができる。   According to the fifth embodiment, since the liquid is sprayed in the semi-closed space 8 from the nozzle 15 in the form of a mist, the liquid is charged by corona discharge and introduced into the semi-closed space 8 by the Coulomb force. The particulate matter 5 collected on the outer peripheral surface 3 and the inner peripheral surface of the casing electrode 4 is wetted by the liquid mist. For this reason, the adsorption force of the particulate matter 5 to the cylindrical electrode 3 or the casing electrode 4 is increased by the surface tension of the liquid, and the particulate matter 5 is peeled off from the collecting surface of the cylindrical electrode 3 or the casing electrode 4. A great suppression effect against re-scattering can be exhibited.

なお、上記第5の実施形態においては、前述した第1の実施形態にノズル15を付加した場合について説明したが、前述した第2〜第4の実施形態にノズル15を付加するようにしてもよい。
また、上記第1〜第5の実施形態においては、内燃機関から排出される排気ガスに含まれる粒子状物質5を除去する場合について説明したが、これに限定されるものではなく、任意の粒子状物質含有ガスから粒子状物質を除去することができる。
また、上記第1〜第5の実施形態においては、ケーシング電極4が角筒状である場合について説明したが、これに限定されるものではなく、筒状電極3を、半閉空間8を形成して覆うことができればよく、円筒状、多角筒状等の任意の形状とすることができる。
In the fifth embodiment, the case where the nozzle 15 is added to the first embodiment described above has been described. However, the nozzle 15 may be added to the second to fourth embodiments described above. Good.
Moreover, in the said 1st-5th embodiment, although the case where the particulate matter 5 contained in the exhaust gas discharged | emitted from an internal combustion engine was removed was demonstrated, it is not limited to this, Arbitrary particle | grains The particulate matter can be removed from the particulate matter-containing gas.
Moreover, in the said 1st-5th embodiment, although the case where the casing electrode 4 was a rectangular tube shape was demonstrated, it is not limited to this, The semi-closed space 8 is formed for the cylindrical electrode 3 And can be any shape such as a cylindrical shape or a polygonal cylindrical shape.

同様に、筒状電極3についても円筒状に限定されるものではなく、放電電極2の針状電極部2bと対向する内周面と針状電極部2bとの間の距離を等しくすれば任意の形状とすることができる。すなわち、例えば棒状導体2aに針状電極部2bを円周方向に60°(又は45°)間隔で6本(又は8本)形成する場合には、筒状電極3を6角筒状(又は8角筒状)に形成するようにしてもよい。
また、上記第1〜第5の実施形態においては、放電電極2の針状電極部2bを軸方向で全て同一方向に突出させる場合について説明したが、これに限定されるものではなく、針状電極部2bの突出位置が軸方向の各部で円周方向にずらして配置するようにしてもよい。
Similarly, the cylindrical electrode 3 is not limited to a cylindrical shape, and may be arbitrarily provided that the distance between the inner peripheral surface of the discharge electrode 2 facing the needle electrode portion 2b and the needle electrode portion 2b is equal. It can be made into the shape. That is, for example, when six (or eight) acicular electrode portions 2b are formed on the rod-shaped conductor 2a at intervals of 60 ° (or 45 °) in the circumferential direction, the cylindrical electrode 3 is formed in a hexagonal tube shape (or You may make it form in an octagonal cylinder shape.
Moreover, in the said 1st-5th embodiment, although the case where all the acicular electrode parts 2b of the discharge electrode 2 were protruded in the same direction by the axial direction was demonstrated, it is not limited to this, but acicular The protruding position of the electrode part 2b may be shifted in the circumferential direction at each part in the axial direction.

1…電気集塵装置、2…放電電極,2a…棒状導体、2b…針状電極部、3…筒状電極、3a…ステンレスパイプ、3b…貫通孔、4…ケーシング電極、4a…角枠板部、4b…端板部、5…粒子状物質、6…排気ガス、7…ガス流路、8…半閉空間(補集空間)、9…高圧電源、11,12…補助電極、15…ノズル   DESCRIPTION OF SYMBOLS 1 ... Electric dust collector, 2 ... Discharge electrode, 2a ... Rod-shaped conductor, 2b ... Needle-shaped electrode part, 3 ... Cylindrical electrode, 3a ... Stainless steel pipe, 3b ... Through-hole, 4 ... Casing electrode, 4a ... Square frame board 4, 4 ... end plate, 5 ... particulate matter, 6 ... exhaust gas, 7 ... gas flow path, 8 ... semi-closed space (collection space), 9 ... high-voltage power source, 11, 12 ... auxiliary electrode, 15 ... nozzle

Claims (2)

筒状電極と、該筒状電極の中央部に配置される放電電極とを備え、前記筒状電極の内部に集塵対象ガスを通流させた状態で前記筒状電極と前記放電電極間に電圧を印加してコロナ放電を発生させることにより、前記集塵対象ガス中の粒子状物質を帯電させて前記筒状電極側で吸引して捕集する電気集塵装置であって、
記筒状電極に前記粒子物質を通過させる貫通孔を複数形成するとともに、前記筒状電極を当該筒状電極より大きな筒状のケーシング電極の内部に配置し、
前記筒状電極の外面と前記ケーシング電極の内面との間に、前記粒子状物質を捕集する補集空間が形成され、
当該補集空間に複数の補助電極を配置し、
前記筒状電極、前記ケーシング電極及び前記補助電極を同一電位としたことを特徴とする電気集塵装置。
A cylindrical electrode; and a discharge electrode disposed at a central portion of the cylindrical electrode, and a dust collection target gas is allowed to flow inside the cylindrical electrode, and between the cylindrical electrode and the discharge electrode. An electrostatic precipitator that applies a voltage to generate a corona discharge to charge and collect particulate matter in the dust collection target gas and suck it on the cylindrical electrode side,
A through hole for passing the pre-Symbol particulate material prior Symbol tubular electrode together with forming a plurality of, the cylindrical electrode disposed within the large cylindrical casing electrode than the cylindrical electrode,
A collecting space for collecting the particulate matter is formed between the outer surface of the cylindrical electrode and the inner surface of the casing electrode,
A plurality of auxiliary electrodes are arranged in the collection space,
An electrostatic precipitator , wherein the cylindrical electrode, the casing electrode, and the auxiliary electrode have the same potential .
前記補集空間に、液体を噴霧するノズルを配置し、当該ノズルから前記補集空間に補集された粒子状物質に液体を噴霧することを特徴とする請求項1に記載の電気集塵装置。 2. The electrostatic precipitator according to claim 1, wherein a nozzle for spraying liquid is disposed in the collection space, and the liquid is sprayed from the nozzle onto the particulate matter collected in the collection space. .
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