JP3384096B2 - Electric dust collector - Google Patents
Electric dust collectorInfo
- Publication number
- JP3384096B2 JP3384096B2 JP06387494A JP6387494A JP3384096B2 JP 3384096 B2 JP3384096 B2 JP 3384096B2 JP 06387494 A JP06387494 A JP 06387494A JP 6387494 A JP6387494 A JP 6387494A JP 3384096 B2 JP3384096 B2 JP 3384096B2
- Authority
- JP
- Japan
- Prior art keywords
- dust collecting
- collecting electrode
- gas
- treated
- electrostatic precipitator
- 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
Links
Description
【０００１】[0001]
【産業上の利用分野】本発明は、粉塵等の粒子が混入し
た被処理気体の流路中に設置されて粒子を捕集するため
の電気集塵装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrostatic precipitator for collecting particles by being installed in a flow path of a gas to be treated in which particles such as dust are mixed.
【０００２】[0002]
【従来の技術】一般に、電気集塵装置は放電極と集塵極
との間に高電圧を印加することによりこれら放電極、集
塵極の両電極間にコロナ放電を生じさせ、電界の強い部
分の空気を電離させて荷電帯を発生させる構成のもので
ある。そして、例えば粉塵等の粒子が混入した被処理気
体の流路中にこの電気集塵装置を設置し、被処理気体を
電気集塵装置に導入すると、被処理気体が前記荷電帯に
到達したときに粉塵等の粒子が帯電し、この帯電粒子が
反対電位の集塵極に付着して捕集されるようになってい
る。2. Description of the Related Art Generally, in an electrostatic precipitator, a high voltage is applied between a discharge electrode and a dust collecting electrode to cause corona discharge between the discharge electrode and the dust collecting electrode, so that a strong electric field is generated. This is a configuration in which a portion of the air is ionized to generate a charge band. Then, for example, when the electrostatic precipitator is installed in the flow path of the gas to be treated in which particles such as dust are mixed and the gas to be treated is introduced into the electrostatic precipitator, when the gas to be treated reaches the charge zone, Particles such as dust are electrically charged, and the charged particles are attached to and collected by a dust collecting electrode having an opposite potential.
【０００３】図４は従来一般の電気集塵装置の一例を示
す図であって、被処理気体の流通ダクト１に電気集塵装
置２が接続され、電気集塵装置２の後段にファン７が接
続されている。この電気集塵装置２は、被処理気体の流
れ方向（図中矢印Ｘ方向）に対して垂直方向に設置さ
れ、被処理気体を通過させるための多数の孔３、３、…
が形成された板状の集塵極４と、流れ方向に平行に延び
るとともに両端が針状に形成された放電棒５を有する複
数の放電極６、６、…とが流れ方向に沿って交互に配置
された構成となっている。FIG. 4 is a view showing an example of a conventional general electrostatic precipitator, in which an electric precipitator 2 is connected to a flow duct 1 for a gas to be treated, and a fan 7 is provided in a subsequent stage of the electric precipitator 2. It is connected. This electrostatic precipitator 2 is installed in a direction perpendicular to the flow direction of the gas to be treated (the arrow X direction in the figure), and has a large number of holes 3, 3, ... For passing the gas to be treated.
The plate-shaped dust collecting electrode 4 formed with the discharge electrodes 5 and the plurality of discharge electrodes 6 having the discharge rods 5 extending in parallel to the flow direction and having needle-like ends at both ends are alternately arranged along the flow direction. It is arranged in.
【０００４】[0004]
【発明が解決しようとする課題】しかしながら、前記従
来の電気集塵装置２において、集塵極４の孔３、３、…
はその板厚方向で同一の開口面積を有する孔であり、集
塵極４の被処理気体の流れと対向する面４ａはその流れ
方向に対して垂直となっている。したがって、この集塵
極４の面４ａが被処理気体の流れに対する抵抗となるた
め、この部分における被処理気体の圧力損失が大きくな
ってしまい、被処理気体を吸引すべく電気集塵装置２の
後段に設置したファン７に多大な負荷がかかるといった
問題が生じていた。However, in the conventional electrostatic precipitator 2 described above, the holes 3, 3, ...
Is a hole having the same opening area in the plate thickness direction, and the surface 4a of the dust collecting electrode 4 facing the flow of the gas to be treated is perpendicular to the flow direction. Therefore, since the surface 4a of the dust collecting electrode 4 becomes a resistance against the flow of the gas to be treated, the pressure loss of the gas to be treated in this portion becomes large, and the electrostatic precipitator 2 of the electrostatic precipitator 2 should suck the gas to be treated. There has been a problem that a large load is applied to the fan 7 installed in the latter stage.
【０００５】本発明は、前記の課題を解決するためにな
されたものであって、集塵極における圧力損失を低下さ
せることにより後段に設置したファンに多大な負荷をか
けることのない電気集塵装置を提供することを目的とす
る。The present invention has been made in order to solve the above-mentioned problems, and reduces the pressure loss at the dust collecting electrode to prevent a large load from being applied to a fan installed in the subsequent stage. The purpose is to provide a device.
【０００６】[0006]
【課題を解決するための手段】前記の目的を達成するた
めに、本発明の電気集塵装置は、被処理気体の流れ方向
に対して垂直となるように設置され、該被処理気体を通
過させるための多数の孔が設けられた板状の集塵極と、
該集塵極から所定距離離間して対向配置された放電極と
を具備してなる電気集塵装置において、前記集塵極に設
けられている孔の開口面積は、該集塵極の板厚方向に沿
って漸次変化するものとされ、かつ該集塵極の前記被処
理気体の流れ方向上流側の表面における開口面積が前記
板厚方向における最小の開口面積より大きくなるものと
されたことを特徴とするものである。In order to achieve the above object, the electrostatic precipitator of the present invention is installed so as to be perpendicular to the flow direction of the gas to be treated, and the gas to be treated passes therethrough. A plate-shaped dust collecting electrode provided with a large number of holes for
In an electrostatic precipitator including a discharge electrode that is opposed to the dust collecting electrode at a predetermined distance from the dust collecting electrode, the opening area of the hole provided in the dust collecting electrode is equal to the plate thickness of the dust collecting electrode. That the opening area on the surface of the dust collecting electrode on the upstream side in the flow direction of the gas to be treated is larger than the minimum opening area in the plate thickness direction. It is a feature.
【０００７】また、前記集塵極に前記流れ方向と垂直な
方向に延びる多数の格子板を備え、それら格子板間の隙
間を前記被処理気体が通過する構成とし、前記格子板の
横断面形状が、くさび型、ひし型、エアロフォイル型、
ベンチュリー管壁型のいずれかの形状となるようにして
も良い。Further, a number of grid plate extending in the flow direction and the direction perpendicular to the current Chirikyoku, the clearance of their these grid plates a configuration that the gas to be treated passes, crossing of the grid plate Surface shape is wedge type, diamond type, aerofoil type,
The shape may be any one of the Venturi tube wall type.
【０００８】[0008]
【作用】本発明の電気集塵装置においては、被処理気体
を通過させる孔の開口面積が集塵極の板厚方向に沿って
漸次変化するものとされ、かつ集塵極の被処理気体の流
れ方向上流側の表面における開口面積が板厚方向におけ
る最小の開口面積より大きくなるように設定されたこと
により、孔が板厚方向で同一の開口面積を有する場合に
比べて、前記集塵極における流れと対向する面の面積が
小さくなる。これにより、被処理気体の流れに対する抵
抗を小さくすることで圧力損失を小さくすることができ
る。In the electrostatic precipitator of the present invention, the opening area of the hole through which the gas to be treated passes is gradually changed in the plate thickness direction of the dust collector, and the gas to be treated of the dust collector is changed. Since the opening area on the surface on the upstream side in the flow direction is set to be larger than the minimum opening area in the plate thickness direction, the dust collecting electrode can be compared with the case where the holes have the same opening area in the plate thickness direction. The area of the surface opposed to the flow at is small. As a result, the pressure loss can be reduced by reducing the resistance to the flow of the gas to be treated.
【０００９】[0009]
【実施例】以下、本発明の第１の実施例を図１ないし図
３を参照して説明する。図１は本実施例の電気集塵装置
８を示す図であって、図中符号１は被処理気体の流通ダ
クト、９はケーシング、１０は集塵極、１１は放電極で
ある。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of the present invention will be described below with reference to FIGS. FIG. 1 is a view showing an electrostatic precipitator 8 of the present embodiment, in which reference numeral 1 is a flow duct for a gas to be treated, 9 is a casing, 10 is a dust collecting electrode, and 11 is a discharge electrode.
【００１０】電気集塵装置８は被処理気体の流通ダクト
１の途中に接続されており、ケーシング９内に複数の集
塵極１０と複数の放電極１１とが交互に配置された構成
となっている（図１では１組の集塵極１０と放電極１１
のみを示す）。そして、電気集塵装置８の後段にはファ
ン７が設置されており、被処理気体は図中左から右（矢
印Ｘの方向）に向けて流れるようになっている。The electrostatic precipitator 8 is connected in the middle of the flow duct 1 for the gas to be treated, and has a structure in which a plurality of dust collecting electrodes 10 and a plurality of discharge electrodes 11 are alternately arranged in a casing 9. (In FIG. 1, one set of dust collecting electrode 10 and discharge electrode 11
Only shown). Then, a fan 7 is installed in the latter stage of the electrostatic precipitator 8 so that the gas to be treated flows from the left to the right in the figure (direction of arrow X).
【００１１】集塵極１０は、図２に示すように、支持枠
１２と、この支持枠１２に取り付けられた鉛直方向に延
びる多数の格子板１３、１３、…で構成されており、鉛
直方向に延びるこれら格子板１３間の隙間（孔）１４を
被処理気体が通過するようになっている。そして、図１
に示すように、この集塵極１０全体は被処理気体の流れ
方向に対して垂直となるようにケーシング９に取り付け
られている。As shown in FIG. 2, the dust collecting electrode 10 is composed of a support frame 12 and a large number of lattice plates 13, 13, ... Attached to the support frame 12 and extending in the vertical direction. The to-be-processed gas passes through the gaps (holes) 14 between the lattice plates 13 extending in the direction. And FIG.
As shown in, the entire dust collecting electrode 10 is attached to the casing 9 so as to be perpendicular to the flow direction of the gas to be treated.
【００１２】また、各格子板１３は水平断面の形状がく
さび型をなしており、くさびの頂点側が流れの上流側を
向くように支持枠１２に固定されている。そして、図３
（ａ）に示すように、隣接する格子板１３、１３間の最
小開口寸法ｔは従来の格子板（２点鎖線で示す）の場合
と比べて同等程度に設定されている。Each grid plate 13 has a wedge-shaped horizontal cross section, and is fixed to the support frame 12 so that the apex side of the wedge faces the upstream side of the flow. And FIG.
As shown in (a), the minimum opening size t between the adjacent lattice plates 13 and 13 is set to be approximately the same as that of the conventional lattice plate (shown by the two-dot chain line).
【００１３】一方、図２に示すように、放電極１１は、
支持枠１５に対して鉛直方向に固定された複数の支持部
材１６、１６、…と、各支持部材１６に鉛直方向一定間
隔おきに取り付けられた水平方向に延びる複数の放電棒
１７、１７、…とからなるものである。そして、放電棒
１７の先端は放電強度を高めるために針状に形成され、
この先端が集塵極１０に対向するように配置されてい
る。On the other hand, as shown in FIG.
A plurality of supporting members 16, 16 fixed in the vertical direction with respect to the support frame 15, and a plurality of horizontally extending discharge rods 17, 17, which are attached to the supporting members 16 at regular intervals in the vertical direction. It consists of and. And, the tip of the discharge rod 17 is formed in a needle shape in order to enhance the discharge strength,
The tip is arranged so as to face the dust collecting electrode 10.
【００１４】また、放電極１１と集塵極１０との間に高
電圧を印加するための高電圧印加装置２４が設けられて
いる。A high voltage applying device 24 for applying a high voltage is provided between the discharge electrode 11 and the dust collecting electrode 10.
【００１５】上記構成の電気集塵装置８を使用する際に
は、高電圧印加装置２４により放電極１１と集塵極１０
との間に高電圧を印加すると、放電棒１７、１７、…の
先端から集塵極１０に向けて強度の高いコロナ放電が生
じ、荷電帯が形成される。そこで、ファン７を作動させ
て電気集塵装置８内に粉塵等の粒子が混入した被処理気
体を導入すると、被処理気体が前記荷電帯に到達したと
きに粉塵等の粒子が帯電し、この帯電粒子が反対電位の
集塵極１０に付着してこれが捕集される。When the electrostatic precipitator 8 having the above structure is used, the high voltage applying device 24 is used to discharge the electrode 11 and the precipitator 10.
When a high voltage is applied between the discharge rods 17, 17, ..., Corona discharge with high intensity is generated from the tips of the discharge rods 17, 17, ... To the dust collecting electrode 10, and a charge band is formed. Therefore, when the fan 7 is operated to introduce the gas to be treated in which particles such as dust are mixed into the electrostatic precipitator 8, the particles such as dust are electrically charged when the gas to be treated reaches the charge zone, The charged particles adhere to the dust collecting electrode 10 having the opposite potential and are collected.
【００１６】本実施例の電気集塵装置８においては、集
塵極１０の各格子板１３の断面形状がくさび型であり、
くさびの頂点側が流れの上流側を向くように取り付けら
れているため、被処理気体の流れに対する抵抗を小さく
することができ、圧力損失を小さくすることができる。
その結果、電気集塵装置８後段のファン７にかかる負荷
を低減させることができる。In the electrostatic precipitator 8 of this embodiment, each grid plate 13 of the dust collector 10 has a wedge-shaped cross section,
Since the apex side of the wedge is attached so as to face the upstream side of the flow, the resistance to the flow of the gas to be treated can be reduced and the pressure loss can be reduced.
As a result, it is possible to reduce the load on the fan 7 in the latter stage of the electrostatic precipitator 8.
【００１７】また、集塵極１０の構成は前記実施例に限
るものではなく、つぎに集塵極の構成のみを代えた電気
集塵装置の他の実施例について説明する。以下に示す各
実施例の集塵極においても、支持枠１２とこれに取り付
けられた鉛直方向に延びる多数の格子板とからなる構成
は前記第１実施例と同様である。Further, the structure of the dust collecting electrode 10 is not limited to the above-mentioned embodiment, and another embodiment of the electrostatic precipitator in which only the structure of the dust collecting electrode is changed will be described. Also in the dust collecting electrode of each of the following embodiments, the structure including the support frame 12 and a large number of vertically extending lattice plates attached to the support frame 12 is the same as that of the first embodiment.
【００１８】図３（ｂ）は第２実施例の電気集塵装置の
集塵極１８を示す図であって、格子板１９の水平断面の
形状がひし型となっており、ひし型の一つの頂点が流れ
の上流側を向くように支持枠１２に取り付けられてい
る。FIG. 3 (b) is a view showing the dust collecting electrode 18 of the electrostatic precipitator of the second embodiment, in which the lattice plate 19 has a diamond-shaped horizontal cross section. The two vertices are attached to the support frame 12 so as to face the upstream side of the flow.
【００１９】図３（ｃ）は第３実施例の電気集塵装置の
集塵極２０を示す図であって、格子板２１の水平断面の
形状がエアロフォイル（翼）型となっており、長軸方向
が流れ方向に平行となるように取り付けられている。FIG. 3 (c) is a view showing the dust collecting electrode 20 of the electrostatic precipitator of the third embodiment, in which the horizontal cross section of the lattice plate 21 is an airfoil (wing) type. It is attached so that the major axis direction is parallel to the flow direction.
【００２０】図３（ｄ）は第４実施例の電気集塵装置の
集塵極２２を示す図であって、格子板２３の水平断面の
形状がベンチュリー管壁部の型となっている。FIG. 3D is a view showing the dust collecting electrode 22 of the electrostatic precipitator of the fourth embodiment, in which the lattice plate 23 has a horizontal cross-sectional shape which is the shape of the Venturi tube wall portion.
【００２１】上記第２、第３、第４実施例のいずれの集
塵極１８、２０、２２においても、格子板１９、２１、
２３の被処理気体の流れと対向する面積が小さくなるた
め、被処理気体の流れに対する抵抗を小さくすることで
圧力損失を小さくすることができる。具体的には、圧力
損失をｈとすると以下の式で表すことができる。
ｈ＝Ｃd ・｛１／２（ρＶ2 ）｝
Ｃd：抵抗係数
ρ：流体の密度
Ｖ：流体の速度
すなわち、上式より圧力損失ｈは抵抗係数Ｃd と比例関
係にある。In all of the dust collecting electrodes 18, 20, 22 of the second, third and fourth embodiments, the grid plates 19, 21,
Since the area of 23 that faces the flow of the gas to be processed becomes small, the pressure loss can be reduced by reducing the resistance to the flow of the gas to be processed. Specifically, when the pressure loss is h, it can be expressed by the following formula. h = Cd. {1/2 (ρV 2 )} Cd: Resistance coefficient ρ: Fluid density V: Fluid velocity That is, the pressure loss h is proportional to the resistance coefficient Cd from the above equation.
【００２２】そこで、上記の各場合の抵抗係数Ｃd の値
は、従来型の断面形状が長方形の場合（図３（ａ）に２
点鎖線で示す）がＣd ＝１．４であるのに対し、例えば
ひし型の場合（図３（ｂ）に示す）がＣd ＝１．１、エ
アロフォイル型の場合（図３（ｃ）に示す）がＣd ＝
０．０１２というように、従来の場合に比べて抵抗係数
が小さいため、圧力損失が小さくなる。このように、上
記いずれの実施例の場合においても、圧力損失を小さく
することで電気集塵装置後段のファンにかかる負荷を低
減させることができる。Therefore, the value of the resistance coefficient Cd in each of the above cases is 2 when the cross-sectional shape of the conventional type is rectangular (2 in FIG. 3A).
(Shown by the dotted line) is Cd = 1.4, whereas in the case of the diamond type (shown in FIG. 3 (b)) is Cd = 1.1 and in the case of the airfoil type (shown in FIG. 3 (c)). Is shown) is Cd =
Since the resistance coefficient is 0.012, which is smaller than that of the conventional case, the pressure loss is small. As described above, in any of the above-described embodiments, by reducing the pressure loss, it is possible to reduce the load applied to the fan at the subsequent stage of the electrostatic precipitator.
【００２３】なお、前記全ての実施例においては、集塵
極１０、１８、２０、２２における格子板１３、１９、
２１、２３を鉛直方向に延在するものとしたが、この構
成に代えて格子板を水平方向または斜め方向に延在する
ものとしても良い。また、支持枠１２に多数の格子板１
３、１９、２１、２３を取り付けた構成に代えて、集塵
極を多孔板で構成することもできる。この場合でも、隣
接する孔を含み被処理気体の流れ方向に沿った面で切断
した際の集塵極の断面形状がくさび型、ひし型、エアロ
フォイル型、ベンチュリー管壁型のいずれかになるよう
にすれば良い。一方、放電極１１の形状については本実
施例に限ることなく種々の形状のものを用いることがで
きる。In all the above-mentioned embodiments, the grid plates 13, 19, of the dust collecting electrodes 10, 18, 20, 22 are provided.
Although 21 and 23 extend in the vertical direction, the lattice plate may extend in the horizontal direction or the oblique direction instead of this configuration. Further, the support frame 12 has a large number of lattice plates 1
Instead of the structure in which 3, 19, 21, and 23 are attached, the dust collecting electrode may be composed of a perforated plate. Even in this case, the cross-sectional shape of the dust collecting electrode when cut at a surface including the adjacent holes along the flow direction of the gas to be treated is any of wedge type, rhombus type, airfoil type, and Venturi tube wall type. Just do it. On the other hand, the shape of the discharge electrode 11 is not limited to this embodiment, and various shapes can be used.
【００２４】[0024]
【発明の効果】以上、詳細に説明したように、本発明の
電気集塵装置は、被処理気体を通過させる孔が、集塵極
の板厚方向に沿って異なる開口面積を有し、集塵極にお
ける被処理気体の流れ方向上流側の面内での開口面積
が、前記板厚方向における最小の開口面積より大きくな
るように設定されたことにより、孔が板厚方向で同一の
開口面積を有する場合に比べて、前記集塵極における上
流側の面の被処理気体の流れと対向する面積が小さくな
る。これにより、被処理気体の流れに対する流体抵抗を
小さくし、圧力損失を小さくすることができる。その結
果、電気集塵装置後段のファンにかかる負荷を低減させ
ることができる。As described above in detail, in the electrostatic precipitator of the present invention, the holes for passing the gas to be treated have different opening areas along the plate thickness direction of the precipitator, Since the opening area in the surface of the dust electrode on the upstream side in the flow direction of the gas to be processed is set to be larger than the minimum opening area in the plate thickness direction, the holes have the same opening area in the plate thickness direction. The area of the surface of the dust collecting electrode facing the flow of the gas to be treated is smaller than that of the case where Thereby, the fluid resistance to the flow of the gas to be treated can be reduced and the pressure loss can be reduced. As a result, it is possible to reduce the load on the fan at the latter stage of the electrostatic precipitator.
【図１】本発明の第１実施例である電気集塵装置を示す
平断面図である。FIG. 1 is a plan sectional view showing an electrostatic precipitator according to a first embodiment of the present invention.
【図２】同装置の集塵極および放電極を拡大視した斜視
図である。FIG. 2 is an enlarged perspective view of a dust collecting electrode and a discharge electrode of the same device.
【図３】本発明の他の実施例における格子板の形状を示
す平断面図である。FIG. 3 is a plan sectional view showing the shape of a lattice plate according to another embodiment of the present invention.
【図４】従来の電気集塵装置の一例を示す平断面図であ
る。FIG. 4 is a plan sectional view showing an example of a conventional electrostatic precipitator.
８ 電気集塵装置 １０、１８、２０、２２ 集塵極 １１ 放電極 １３、１９、２１、２３ 格子板 １４ 隙間（孔） 8 Electric dust collector 10, 18, 20, 22 Dust collector 11 discharge electrode 13, 19, 21, 23 Lattice plate 14 Gap (hole)
───────────────────────────────────────────────────── 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 特開 昭59−209663（ＪＰ，Ａ) 特開 昭56−56248（ＪＰ，Ａ) 実開 昭49−111885（ＪＰ，Ｕ) (58)調査した分野(Int.Cl.7，ＤＢ名) B03C 3/00 - 3/88 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Nobuyuki Abe 3-2-16 Toyosu, Koto-ku, Tokyo Ishikawa Shima Harima Heavy Industries, Ltd. Toyosu General Office (56) Reference Japanese Patent Laid-Open No. 59-209663 (JP, 59-209663) A) Japanese Unexamined Patent Publication No. 56-56248 (JP, A) Actual Development No. 49-111885 (JP, U) (58) Fields investigated (Int.Cl. 7 , DB name) B03C 3/00-3/88
Claims (2)
るように設置され、該被処理気体を通過させるための多
数の孔が設けられた板状の集塵極と、該集塵極から所定
距離離間して対向配置された放電極とを具備してなる電
気集塵装置において、 前記集塵極に設けられている孔の開口面積は、該集塵極
の板厚方向に沿って漸次変化するものとされ、かつ該集
塵極の前記被処理気体の流れ方向上流側の表面における
開口面積が前記板厚方向における最小の開口面積より大
きくなるものとされたことを特徴とする電気集塵装置。1. A plate-shaped dust collecting electrode, which is installed so as to be perpendicular to the flow direction of the gas to be treated and provided with a large number of holes for passing the gas to be treated, and the dust collecting electrode. In the electrostatic precipitator including a discharge electrode that is arranged to face each other at a predetermined distance from, the opening area of the hole provided in the dust collecting electrode is along the plate thickness direction of the dust collecting electrode. Electricity, characterized in that the opening area on the surface of the dust collecting electrode on the upstream side in the flow direction of the gas to be treated is larger than the minimum opening area in the plate thickness direction. Dust collector.
格子板が備えられ、それら格子板間の隙間を前記被処理
気体が通過する構成とされ、 前記格子板の横断面形状が、くさび型、ひし型、エアロ
フォイル型、ベンチュリー管壁型のいずれかの形状とさ
れたことを特徴とする電気集塵装置。In the electric dust collector of claim 2 according to claim 1, wherein the current Chirikyoku the plurality of grid plate extending in the flow direction and perpendicular direction is provided on, its said treated the gap these grid plates An electrostatic precipitator characterized in that a gas passes therethrough, and the cross-sectional shape of the lattice plate is any one of a wedge type, a rhombus type, an aerofoil type, and a Venturi tube wall type.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP06387494A JP3384096B2 (en) | 1994-03-31 | 1994-03-31 | Electric dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP06387494A JP3384096B2 (en) | 1994-03-31 | 1994-03-31 | Electric dust collector |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07265738A JPH07265738A (en) | 1995-10-17 |
| JP3384096B2 true JP3384096B2 (en) | 2003-03-10 |
Family
ID=13241889
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP06387494A Expired - Fee Related JP3384096B2 (en) | 1994-03-31 | 1994-03-31 | Electric dust collector |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3384096B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4983486B2 (en) * | 2007-09-03 | 2012-07-25 | ダイキン工業株式会社 | Dust collector |
| KR101577954B1 (en) * | 2015-09-08 | 2015-12-16 | (주)신영에어텍 | Air Cleaner for Duct Having Support Unit |
-
1994
- 1994-03-31 JP JP06387494A patent/JP3384096B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH07265738A (en) | 1995-10-17 |
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