JP3355773B2 - Cyclone - Google Patents

Cyclone

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Publication number
JP3355773B2
JP3355773B2 JP6301094A JP6301094A JP3355773B2 JP 3355773 B2 JP3355773 B2 JP 3355773B2 JP 6301094 A JP6301094 A JP 6301094A JP 6301094 A JP6301094 A JP 6301094A JP 3355773 B2 JP3355773 B2 JP 3355773B2
Authority
JP
Japan
Prior art keywords
cylindrical portion
discharge electrode
collecting member
dust collecting
dust
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
JP6301094A
Other languages
Japanese (ja)
Other versions
JPH07265732A (en
Inventor
恒雄 小林
光雄 長岡
伸行 阿部
Original Assignee
石川島播磨重工業株式会社
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 石川島播磨重工業株式会社 filed Critical 石川島播磨重工業株式会社
Priority to JP6301094A priority Critical patent/JP3355773B2/en
Publication of JPH07265732A publication Critical patent/JPH07265732A/en
Application granted granted Critical
Publication of JP3355773B2 publication Critical patent/JP3355773B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Cyclones (AREA)
  • 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】本発明は、気流中に含まれている
粉粒体を分離するためのサイクロンに関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cyclone for separating powders contained in an air stream.

【0002】[0002]

【従来の技術】セメントプラント等の粉粒体を使用する
工程、或いは粉粒体を気流中で乾燥、燃焼、仮焼、熱交
換する等の物理的及び化学的反応処理するような分野に
おいては、処理した粉粒体を気流中から分離する作業が
行われる。このような粉粒体の分離には一般に、サイク
ロン、電気集塵機等が使用されている。
2. Description of the Related Art In a process of using a granular material such as a cement plant, or in a field where the granular material is subjected to a physical and chemical reaction treatment such as drying, burning, calcining and heat exchange in an air stream. Then, an operation of separating the treated powder and granular material from the airflow is performed. Generally, a cyclone, an electrostatic precipitator, or the like is used for separating such a granular material.

【0003】従来から使用されているサイクロンの一例
を図5の縦断面図によって説明すると、縦方向に配置し
た円筒部1の上部には、接線方向に入口部2が設けられ
ており、円筒部1の下部には、下方が小径になる円錐部
3が一体的に設けられている。また円筒部1の中心に
は、縦方向の排気内筒部4が、円筒部1の上端を塞いで
いる上面よりも上方に突出するように設けられている。
An example of a conventionally used cyclone will be described with reference to a longitudinal sectional view of FIG. 5. An inlet 2 is provided in a tangential direction at an upper portion of a cylindrical portion 1 arranged in a vertical direction. A conical portion 3 having a smaller diameter at the lower portion is provided integrally with a lower portion of 1. At the center of the cylindrical portion 1, a vertical exhaust inner cylindrical portion 4 is provided so as to protrude above an upper surface that covers an upper end of the cylindrical portion 1.

【0004】粉粒体を含んでいる気流は接線方向の入口
部2から円筒部1の中に流入し、円筒部1の中で旋回流
となり、粉粒体は遠心力で円筒部1の内壁に沿いながら
落下して円錐部3の下端から取り出される。粉粒体を分
離した気流は排気内筒部4の中を上昇し、排気内筒部4
の上端から取り出される。
[0004] The air flow containing the granular material flows from the tangential inlet portion 2 into the cylindrical portion 1 and turns into a swirling flow in the cylindrical portion 1, and the granular material is centrifugally moved to the inner wall of the cylindrical portion 1. And fall out from the lower end of the conical part 3. The air flow from which the powder and the granular material have been separated rises in the exhaust inner cylinder 4 and the exhaust inner cylinder 4
Taken out from the top of

【0005】また従来から使用されている電気集塵機
は、正電圧を印加した集塵部材と負電圧を印加した放電
極との間を粉粒体を含んでいる気流を通過させ、マイナ
スに帯電した粉粒体をプラスの電位になっている集塵部
材に吸引して気流から分離する。
In a conventional electric dust collector, an airflow containing powder particles is passed between a dust collecting member to which a positive voltage is applied and a discharge electrode to which a negative voltage is applied, and is negatively charged. The powder is sucked into the dust collecting member having a positive potential and separated from the airflow.

【0006】[0006]

【発明が解決しようとする課題】従来のセメント原料の
予熱装置に用いられているサイクロンによる集塵効率は
通常で90%程度、最大でも96%程度であり、それ以
上の集塵効率は望めなかった。また粉粒体の粒径が20
μm以下となると極端に集塵効率が悪化し、粒径が1μ
m程度の粒子は補集できない欠点があった。
The efficiency of dust collection by a cyclone used in a conventional preheating apparatus for cement raw materials is usually about 90%, and at most about 96%, and a further higher dust collection efficiency cannot be expected. Was. The particle size of the powder is 20
If it is less than μm, the dust collection efficiency is extremely deteriorated,
There was a disadvantage that particles of about m could not be collected.

【0007】また従来から使用されている電気集塵機
は、気流の粉塵含有濃度が高い場合に前段に予備集塵機
の設置が必要となり、また集塵部材と放電極とが気流の
流れに平行に配置されている電気集塵機においては、気
流を遅い速度で流動させないと集塵されずに下流側にパ
スされ易いために、気流の速度を最大でも1.5m/秒
程度とする必要があり、従って気体の量が多い場合に
は、電気集塵機の断面積が大きくなる欠点があった。
[0007] Further, in the conventional electric precipitator, when the dust content of the air stream is high, it is necessary to install a pre-collector in the preceding stage, and the dust collecting member and the discharge electrode are arranged in parallel to the flow of the air stream. In such an electric dust collector, if the air flow is not flown at a low speed, the dust is not collected and is likely to pass downstream, so that the air flow speed needs to be at most about 1.5 m / sec. When the amount is large, there is a disadvantage that the cross-sectional area of the electric precipitator increases.

【0008】本発明はこのような従来の欠点を除去し、
集塵効率の高いサイクロンを提供することを目的とする
ものである。
The present invention eliminates such conventional disadvantages,
It is an object to provide a cyclone with high dust collection efficiency.

【0009】[0009]

【課題を解決するための手段】本発明のサイクロンは、
縦方向の円筒部の上部に接線方向に設けられた入口部
と、前記円筒部の下部に設けられ下方が小径になる円錐
部と、前記円筒部の天井の中心に垂下して設けられ上端
前記円筒部の上方に突出した排気内筒部と、該排気内
筒部の下端よりも前記入口部側に設けられ負電圧が印加
された放電極と、該放電極よりも下方に設けられ正電圧
が印加された集塵部材とを備えたことを特徴とするもの
である。
The cyclone of the present invention comprises:
An inlet portion provided tangentially at an upper portion of the vertical cylindrical portion, a conical portion provided at a lower portion of the cylindrical portion and having a smaller diameter at a lower portion, and an upper end provided at a center of a ceiling of the cylindrical portion so as to hang down.
There the exhaust cylinder portion projecting above the cylindrical portion, and a discharge electrode to which a negative voltage is applied is provided on the inlet side of the lower end of the exhaust in the cylinder portion, it is provided below the dissipating electrode A dust collecting member to which a positive voltage is applied.

【0010】[0010]

【作用】放電極と集塵部材とによる電界のために粒子は
電荷を持ち、細粒同士が凝集して見掛けの粒子径が大き
くなり、円筒部内での遠心力で気流から分離すること
と、集塵部材に吸引されて捕集されることにより、気流
に含まれる粉粒体の量は極めて少なくなる。
[Function] Due to the electric field generated by the discharge electrode and the dust collecting member, the particles have a charge, and the fine particles aggregate to increase the apparent particle size, and are separated from the airflow by centrifugal force in the cylindrical portion. By being sucked and collected by the dust collecting member, the amount of the granular material contained in the airflow is extremely reduced.

【0011】[0011]

【実施例】以下、本発明の実施例を図を参照して説明す
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings.

【0012】図1は本発明の一実施例の縦断面図、図2
は図1のII−II断面図であって、縦方向に配置した
円筒部1の上部には、図2に示すように円筒部1の接線
方向に入口部2が設けられており、円筒部1の下部に
は、下方が小径になる円錐部3が一体的に設けられてい
る。また円筒部1の中心には、縦方向の排気内筒部4が
前記円筒部1の天井に垂下して設けられており、該排気
内筒部4は下端が円筒部1の上下中間部に開口し、上端
が円筒部1の上端を塞いでいる上面よりも上方に突出し
て開口している。
FIG. 1 is a longitudinal sectional view of an embodiment of the present invention, and FIG.
FIG. 2 is a cross-sectional view taken along the line II-II of FIG. 1, and an inlet 2 is provided in the tangential direction of the cylinder 1 as shown in FIG. A conical portion 3 having a smaller diameter at the lower portion is provided integrally with a lower portion of 1. In the center of the cylindrical portion 1, a vertical exhaust inner cylindrical portion 4 is provided.
The exhaust inner cylinder portion 4 is provided to hang down from the ceiling of the cylindrical portion 1 , and the lower end of the exhaust inner cylindrical portion 4 is opened at the upper and lower middle portion of the cylindrical portion 1, and the upper end is higher than the upper surface closing the upper end of the cylindrical portion 1. It protrudes and is open.

【0013】排気内筒部4の下端よりもやや上の箇所に
は、網目状の放電極5が、円筒部1の内周と排気内筒部
4の外周との間の全断面に亘って水平に、しかも円筒部
1および排気内筒部4に対して絶縁材14により電気的
に絶縁され、若干振動し得るように設けられている。
At a location slightly above the lower end of the exhaust inner cylinder 4, a mesh-shaped discharge electrode 5 extends over the entire cross section between the inner periphery of the cylindrical portion 1 and the outer periphery of the exhaust inner cylinder 4. It is provided horizontally so as to be electrically insulated from the cylindrical portion 1 and the exhaust inner cylindrical portion 4 by the insulating material 14 and to be able to slightly vibrate.

【0014】また排気内筒部4の下端よりもやや下の箇
所には、多孔板状の集塵部材6が、円筒部1の全断面に
亘って水平に、しかも若干振動し得るように設けられて
いる。
At a position slightly lower than the lower end of the exhaust inner cylindrical portion 4, a perforated plate-shaped dust collecting member 6 is provided so as to be able to vibrate horizontally and slightly over the entire cross section of the cylindrical portion 1. Have been.

【0015】そして直流高圧電源7から放電極5に負電
圧を印加し、集塵部材6に正電圧を印加すると共に、放
電極5及び集塵部材6をそれぞれ別個の槌打ち装置8,
8で振動させることができるようになっている。
Then, a negative voltage is applied to the discharge electrode 5 from the DC high-voltage power supply 7 and a positive voltage is applied to the dust collecting member 6, and the discharge electrode 5 and the dust collecting member 6 are separated from each other by a hammer 8,
8 can be made to vibrate.

【0016】図3は槌打ち装置8の一例を示す正面図で
あって、放電極5及び集塵部材6に固定されている槌打
ち棒9は、円筒部1を密に、しかも摺動可能に貫通して
円筒部1の外に突出している。槌打ち棒9の先端にはカ
ラー部10が一体的に形成されていて、カラー部10と
円筒部1外面との間には、スプリング11が設けられて
いる。このため槌打ち棒9は、スプリング11によって
円筒部1から突出する方向に付勢され、カラー部10が
槌打ちカム12に押し付けられるようになっている。
FIG. 3 is a front view showing an example of the hammering device 8. The hammering bar 9 fixed to the discharge electrode 5 and the dust collecting member 6 can slide the cylindrical portion 1 densely and slidably. And protrudes out of the cylindrical portion 1. A collar portion 10 is integrally formed at the tip of the hammering bar 9, and a spring 11 is provided between the collar portion 10 and the outer surface of the cylindrical portion 1. For this reason, the hammering rod 9 is urged by the spring 11 in a direction protruding from the cylindrical portion 1 so that the collar portion 10 is pressed against the hammering cam 12.

【0017】槌打ちカム12は回転シャフト13に固着
されていて、回転シャフト13と共に槌打ちカム12が
時計方向に回転すると、槌打ちカム12のカラー部10
に当接する箇所は次第に大径になり、スプリング11の
力に抗してカラー部10、槌打ち棒9、放電極5または
集塵部材6を、一体的に円筒部1の内方に向けて移動さ
せるようになる。
The hammering cam 12 is fixed to a rotating shaft 13. When the hammering cam 12 rotates clockwise with the rotating shaft 13, the collar portion 10 of the hammering cam 12 is rotated.
The portion which comes into contact with becomes gradually larger in diameter, and the collar portion 10, the hammering bar 9, the discharge electrode 5 or the dust collecting member 6 is integrally turned toward the inside of the cylindrical portion 1 against the force of the spring 11. They will be moved.

【0018】槌打ちカム12がさらに時計方向に回転を
続けると、槌打ちカム12のカラー部10に当接する箇
所は急激に小径になり、カラー部10、槌打ち棒9、放
電極5または集塵部材6は、スプリング11の力によっ
て急速に円筒部1から突出する方向に移動する。
As the hammering cam 12 further rotates clockwise, the portion of the hammering cam 12 which comes into contact with the collar portion 10 rapidly decreases in diameter, and the collar portion 10, the hammering bar 9, the discharge electrode 5 or the collecting electrode The dust member 6 rapidly moves in a direction protruding from the cylindrical portion 1 by the force of the spring 11.

【0019】槌打ちカム12が回転を継続することによ
り、放電極5または集塵部材6は左右に振動されること
になる。図中8aはカバーを示す。
As the hammering cam 12 continues to rotate, the discharge electrode 5 or the dust collecting member 6 is vibrated right and left. In the figure, reference numeral 8a denotes a cover.

【0020】次に、図1、図2の装置の作用を説明す
る。
Next, the operation of the apparatus shown in FIGS. 1 and 2 will be described.

【0021】粉粒体を含んでいる気流は矢印aで示すよ
うに接線方向の入口部2から円筒部1の中に流入し、円
筒部1の中で旋回流となり、次第に下降して網目状の放
電極5を通過する。
The air flow containing the granular material flows into the cylindrical portion 1 from the tangential inlet portion 2 as shown by the arrow a, forms a swirling flow in the cylindrical portion 1 and gradually descends to form a mesh. Pass through the discharge electrode 5.

【0022】負電圧が印加されている放電極5を通過す
る際に気流中に含まれている粉粒体は、旋回流による遠
心力で円筒部1の内壁に沿いながら落下すると同時に放
電極5から放電されるマイナスイオンによってマイナス
に帯電され、細粒同士が凝集して見かけの粒子径が大き
くなってプラスの電位になっている集塵部材6に吸引さ
れ、さらに落下して矢印bで示すように円錐部3の下端
から取り出される。
When passing through the discharge electrode 5 to which a negative voltage is applied, the particles contained in the air flow fall along the inner wall of the cylindrical portion 1 due to the centrifugal force of the swirling flow, and at the same time, fall. Is attracted to the dust collecting member 6 which is negatively charged by the negative ions discharged from the fine particles, aggregates the fine particles to each other, and has an apparent particle diameter which is increased to a positive potential, and further falls and is indicated by an arrow b. Is taken out from the lower end of the conical part 3 as shown in FIG.

【0023】径の極めて小さい細粒は放電極5に付着し
たり、特に集塵部材6に吸引されて付着したままの状態
になるので、槌打ち装置8,8で放電極5及び集塵部材
6をそれぞれ振動させると放電極5や集塵部材6に付着
していた細粒は見かけの粒子径が大きくなった状態で振
るい落とされて落下し、円錐部3の下端から取り出され
る。
Since the fine particles having a very small diameter adhere to the discharge electrode 5, and in particular, remain in the state of being attracted to the dust collecting member 6, the hammering devices 8, 8 cause the discharge particle 5 and the dust collecting member to be kept. When each of the vibrators 6 is vibrated, the fine particles adhering to the discharge electrode 5 and the dust collecting member 6 are shaken off and fall in a state where the apparent particle diameter becomes large, and are taken out from the lower end of the conical portion 3.

【0024】微細な粉粒体まで分離された気流は排気内
筒部4の中を上昇し、矢印cで示すように排気内筒部4
の上端から取り出される。
The air flow separated into fine particles rises in the exhaust inner cylinder 4, and as shown by arrow c, the exhaust inner cylinder 4
Taken out from the top of

【0025】図4は本発明の他の実施例の縦断面図であ
って、図1と同一部分には同一符号を付してある。
FIG. 4 is a longitudinal sectional view of another embodiment of the present invention, and the same parts as those in FIG. 1 are denoted by the same reference numerals.

【0026】図4の実施例においては、排気内筒部4の
下端よりも上流側の入口部2に放電極5を設け、漏斗状
の集塵部材15を排気内筒部4の下端下方にある円錐部
3の内側に設けてある。そして放電極5は入口部2に対
し絶縁材14により電気的に絶縁され、槌打ち装置8で
振動させることができるようになっており、集塵部材1
5も槌打ち装置8で振動させることができるようになっ
ていて、直流高圧電源7から放電極5に負電圧を印加
し、集塵部材15に正電圧を印加している。
In the embodiment shown in FIG. 4, a discharge electrode 5 is provided at the inlet 2 upstream of the lower end of the exhaust inner cylinder 4, and a funnel-shaped dust collecting member 15 is provided below the lower end of the exhaust inner cylinder 4. It is provided inside a certain conical portion 3. The discharge electrode 5 is electrically insulated from the inlet 2 by the insulating material 14 and can be vibrated by the hammer 8.
5 can also be vibrated by the hammering device 8. A negative voltage is applied to the discharge electrode 5 from the DC high-voltage power supply 7, and a positive voltage is applied to the dust collecting member 15.

【0027】図4の実施例においては、粉粒体を含んで
いる気流は矢印aで示すように接線方向の入口部2から
流入し、気流中に含まれている粉粒体は放電極5から放
電されるマイナスイオンによってマイナスに帯電する。
In the embodiment shown in FIG. 4, the air flow containing the granular material flows in from the tangential inlet 2 as shown by the arrow a, and the granular material contained in the air flow is discharged from the discharge electrode 5. It is negatively charged by negative ions discharged from.

【0028】粉粒体を含んでいる気流は入口部2から円
筒部1の中に流入して旋回流となり、粉粒体は旋回流に
よる遠心力で円筒部1の内壁に沿いながら落下してプラ
スの電位になっている集塵部材15に吸引され、さらに
落下して矢印bで示すように円錐部3の下端から取り出
される。
The air flow containing the granular material flows into the cylindrical portion 1 from the inlet portion 2 to form a swirling flow, and the granular material falls down along the inner wall of the cylindrical portion 1 by centrifugal force due to the swirling flow. The dust is collected by the dust collecting member 15 which has a positive potential, falls further, and is taken out from the lower end of the conical portion 3 as shown by an arrow b.

【0029】放電極5、集塵部材15を槌打ち装置8で
振動させると、放電極5、集塵部材15に付着していた
細粒は見掛けの粒子径が大きくなった状態で落下し、円
錐部3の下端から取り出される。
When the discharge electrode 5 and the dust collecting member 15 are vibrated by the hammering device 8, the fine particles adhering to the discharge electrode 5 and the dust collecting member 15 fall in a state where the apparent particle diameter becomes large. It is taken out from the lower end of the conical part 3.

【0030】微細な粉粒体まで分離された気流は排気内
筒部4の中を上昇し、矢印cで示すように排気内筒部4
の上端から取り出される。
The air flow separated into fine particles rises in the exhaust inner cylinder 4, and as shown by arrow c, the exhaust inner cylinder 4
Taken out from the top of

【0031】本発明は図示した実施例のみでなく、放電
極5、集塵部材6を複数個設けたり、放電極を挟んで気
流の上流側と下流側に集塵部材を配置するようにした
り、図1の実施例と図4の実施例とを組み合わせて実施
することも可能である。また、放電極5も網目状でな
く、放射状とか多孔板状などの場合、集塵部材6も多孔
板でなく、格子状など色々な形状でも実施可能である。
The present invention is not limited to the embodiment shown in the drawings, but includes a plurality of discharge electrodes 5 and a plurality of dust collection members 6 and a configuration in which dust collection members are disposed upstream and downstream of an air flow with the discharge electrodes interposed therebetween. , The embodiment of FIG. 1 and the embodiment of FIG. 4 can be combined. Further, when the discharge electrode 5 is not in a mesh shape but in a radial shape or a perforated plate shape, the dust collecting member 6 can be implemented in various shapes such as a grid shape instead of a perforated plate.

【0032】[0032]

【発明の効果】本発明は従来のサイクロンが捕集できな
かった微細な粉体も気流から分離することができ、また
粉塵含有濃度が高い気流に対しても従来の電気集塵機の
ように前段に予備集塵機を設置する必要がなく、簡単な
構成で集塵効率を高くできる効果がある。
According to the present invention, fine powders which cannot be collected by the conventional cyclone can be separated from the airflow, and even in the airflow having a high concentration of dust, unlike the conventional electric precipitator, it can be separated in the front stage. There is no need to install a spare dust collector, and there is an effect that the dust collection efficiency can be increased with a simple configuration.

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

【図1】本発明の一実施例の縦断面図である。FIG. 1 is a longitudinal sectional view of one embodiment of the present invention.

【図2】図1のII−II断面図である。FIG. 2 is a sectional view taken along line II-II of FIG.

【図3】槌打ち装置の一例を示す正面図である。FIG. 3 is a front view showing an example of a hammering device.

【図4】本発明の他の実施例の縦断面図である。FIG. 4 is a longitudinal sectional view of another embodiment of the present invention.

【図5】従来のサイクロンの縦断面図である。FIG. 5 is a longitudinal sectional view of a conventional cyclone.

【符号の説明】[Explanation of symbols]

1 円筒部 2 入口部 3 円錐部 4 排気内筒部 5 放電極 6 集塵部材 15 集塵部材 DESCRIPTION OF SYMBOLS 1 Cylindrical part 2 Inlet part 3 Conical part 4 Exhaust inner cylinder part 5 Discharge electrode 6 Dust collecting member 15 Dust collecting member

───────────────────────────────────────────────────── フロントページの続き (72)発明者 阿部 伸行 東京都江東区豊洲三丁目2番16号 石川 島播磨重工業株式会社 豊洲総合事務所 内 (56)参考文献 実開 昭49−130480(JP,U) 実開 昭49−56569(JP,U) (58)調査した分野(Int.Cl.7,DB名) B03C 3/00 - 3/88 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Nobuyuki Abe 3-2-16-1 Toyosu, Koto-ku, Tokyo Ishikawa-jima-Harima Heavy Industries, Ltd. Toyosu Sogo Office (56) References U) Real opening 49-56569 (JP, U) (58) Fields investigated (Int. Cl. 7 , DB name) B03C 3/00-3/88

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 縦方向の円筒部の上部に接線方向に設け
られた入口部と、前記円筒部の下部に設けられ下方が小
径になる円錐部と、前記円筒部の天井の中心に垂下して
設けられ上端が前記円筒部の上方に突出した排気内筒部
と、該排気内筒部の下端よりも前記入口部側に設けられ
負電圧が印加された放電極と、放電極よりも下方に設
けられ正電圧が印加された集塵部材とを備えたことを特
徴とするサイクロン。
1. An inlet portion provided tangentially above a vertical cylindrical portion, a conical portion provided below the cylindrical portion and having a smaller diameter at a lower portion, and a conical portion hanging down from a center of a ceiling of the cylindrical portion. and exhaust cylindrical portion <br/> provided upper end projecting above the cylindrical portion Te, a discharge electrode where the negative voltage is provided to the inlet side is applied from the lower end of the exhaust in the cylinder portion, the A cyclone comprising a dust collecting member provided below the discharge electrode and applied with a positive voltage.
JP6301094A 1994-03-31 1994-03-31 Cyclone Expired - Fee Related JP3355773B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6301094A JP3355773B2 (en) 1994-03-31 1994-03-31 Cyclone

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6301094A JP3355773B2 (en) 1994-03-31 1994-03-31 Cyclone

Publications (2)

Publication Number Publication Date
JPH07265732A JPH07265732A (en) 1995-10-17
JP3355773B2 true JP3355773B2 (en) 2002-12-09

Family

ID=13216929

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6301094A Expired - Fee Related JP3355773B2 (en) 1994-03-31 1994-03-31 Cyclone

Country Status (1)

Country Link
JP (1) JP3355773B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6877224B2 (en) * 2017-04-14 2021-05-26 アマノ株式会社 Electrostatic precipitator
KR102123851B1 (en) * 2018-10-31 2020-06-18 (주)엔퓨텍 Cyclone module capable of removing fine dust and ultrafine dust
KR102435934B1 (en) * 2020-07-22 2022-08-25 심영희 cyclone electric dust collector

Also Published As

Publication number Publication date
JPH07265732A (en) 1995-10-17

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