JPH0122821B2 - - Google Patents
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- Publication number
- JPH0122821B2 JPH0122821B2 JP13995983A JP13995983A JPH0122821B2 JP H0122821 B2 JPH0122821 B2 JP H0122821B2 JP 13995983 A JP13995983 A JP 13995983A JP 13995983 A JP13995983 A JP 13995983A JP H0122821 B2 JPH0122821 B2 JP H0122821B2
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- Prior art keywords
- wall
- upper edge
- solvent solution
- tank
- Prior art date
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Description
【発明の詳細な説明】
産業上の利用分野
この発明は電気絶縁性溶剤溶液中に誘導静電場
を利用した静電式瀘過装置の改良に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention This invention relates to an improvement in an electrostatic filtration device that utilizes an induced electrostatic field in an electrically insulating solvent solution.
従来技術
この出願に先立つて、電気絶縁性溶剤溶液中に
誘導静電場を利用した汚水ないしは廃液の瀘過装
置が本発明者によつて発明されており、例えば特
公昭40−15549号公報、特公昭51−3941号、特公
昭51−3942号公報及び特公昭51−23742号公報な
どに開示されている。これらの装置は、電気絶縁
性溶剤溶液を収容したタンクに、被処理液を導入
するための入口と処理済液を排出するための出口
とを設けるとともに、前記溶剤溶液層の液面より
上方の位置において、浮遊不純物排出口を付設
し、一方、前記タンク内部に前記溶剤溶液内にお
いて一対の電極を配置し、この電極間に高圧直流
電圧を印加するものであり、前記被処理液入口か
ら導入した被処理液の含有する有機物質を前記一
対の電極によつて形成される静電場の作用で前記
溶剤溶液中に溶解せしめ、かつ溶剤溶液層の上面
に形成される中間層の浮遊不純物を前記浮遊不純
物排出口から排出し、かつ前記中間層の上面に形
成される処理済液層の処理済水を前記処理済液出
口から排出するようにしたものである。Prior Art Prior to filing this application, the present inventor had invented a filtration device for sewage or waste water that utilizes an induced electrostatic field in an electrically insulating solvent solution. It is disclosed in Japanese Patent Publication No. 51-3941, Japanese Patent Publication No. 51-3942, Japanese Patent Publication No. 23742-1984, etc. These devices provide a tank containing an electrically insulating solvent solution with an inlet for introducing the liquid to be treated and an outlet for discharging the treated liquid. At the same time, a pair of electrodes is arranged in the solvent solution inside the tank, and a high-voltage DC voltage is applied between the electrodes, which is introduced from the inlet of the liquid to be treated. The organic substance contained in the treated liquid is dissolved in the solvent solution by the action of the electrostatic field formed by the pair of electrodes, and the floating impurities in the intermediate layer formed on the upper surface of the solvent solution layer are dissolved in the solvent solution. Floating impurities are discharged from the discharge port, and treated water of a treated liquid layer formed on the upper surface of the intermediate layer is discharged from the treated liquid outlet.
この種の従来の静電式瀘過装置によつて、汚水
ないしは廃液は非常に効率よく処理され、不純物
含有量の少ない処理済水を排出できるようになつ
たが、被処理液に溶解されていたガスが静電場で
分離され浮上する際に伴なう、溶剤及び水いずれ
にも溶けないガム質や溶剤の微粒子の混入は避け
られず、処理済水を排水規準に合わせて排水する
ためには更に二次処理を必要とすることが多い。
なお、排水の有機物質含有量に対する規制は近年
ますます厳しくなつてきている。 With this type of conventional electrostatic filtration device, wastewater or waste water can be treated very efficiently and treated water with low impurity content can be discharged, but it is possible to discharge treated water with low impurity content, but it is possible to discharge treated water with low impurity content. When the gas is separated in an electrostatic field and floats to the surface, the contamination of gum and solvent particles that are insoluble in both solvent and water is unavoidable. often require further secondary processing.
Note that regulations regarding the organic substance content of wastewater have become increasingly strict in recent years.
発明の目的
本発明は、溶剤やガム質などの不純物をほとん
ど含まない処理済水を直接取り出すことのできる
静電式瀘過装置を提供することを目的とする。OBJECTS OF THE INVENTION An object of the present invention is to provide an electrostatic filtration device that can directly take out treated water that contains almost no impurities such as solvents or gums.
発明の構成及び効果
本発明の装置は、電気絶縁性溶剤溶液を収容し
たタンクに、被処理液を導入するための入口を設
け、前記タンク内部に前記溶剤溶液内において一
対の電極を配置し、この電極間に高圧直流電圧を
印加するようにした静電式瀘過装置において、前
記タンクの側壁を二重壁にして、その内側壁と外
側壁との間にポケツトを形成し、前記内側壁の上
縁は前記溶剤溶液の液面よりも上方に形成し、溶
剤溶液層の上面に形成される中間層の浮遊不純物
が前記内側壁の上縁から前記ポケツトへ溢出する
ようにしたものであつて、内側壁と外側壁の間
に、四方に連続した縦型の邪摩板を配置し、更に
この邪摩板の外側と内側にそれぞれ四方に連続し
た樋を設けたものである。Structure and Effects of the Invention The apparatus of the present invention provides a tank containing an electrically insulating solvent solution with an inlet for introducing the liquid to be treated, and a pair of electrodes arranged in the solvent solution inside the tank. In this electrostatic filtration device in which a high DC voltage is applied between the electrodes, the side wall of the tank is made into a double wall, a pocket is formed between the inner wall and the outer wall, and the inner wall The upper edge is formed above the liquid level of the solvent solution so that floating impurities in the intermediate layer formed on the upper surface of the solvent solution layer overflow from the upper edge of the inner wall into the pocket. A vertical jamb board that is continuous in all directions is placed between the inner wall and the outside wall, and a gutter that is continuous in all directions is provided on the outside and inside of this board.
上記邪摩板は、上端が内側壁上縁より上方に位
置し、下端が内側壁上縁と同一又はそれより少し
下方に位置するものであり、また樋は同じ高さに
口を有し、その口は邪摩板及び外側壁の上端より
下方で内側壁上縁より上方に位置する。 The upper end of the jama board is located above the upper edge of the inner wall, and the lower end is located at the same level as or slightly below the upper edge of the inner wall, and the gutter has an opening at the same height, The mouth is located below the upper edge of the jamb and the outer wall and above the upper edge of the inner wall.
すなわち、本発明では、被処理液に溶解されて
いたガスに伴つて浮上する溶剤やガム質を、邪摩
板の存在によつてポケツト側に流出させず、邪摩
板の内側に存在する樋に集め、邪摩板の外側の樋
には不純物のない清水を集めようとするものであ
る。 That is, in the present invention, the presence of the bar plate prevents the solvent and gum that float up with the gas dissolved in the liquid to be processed from flowing out to the pocket side, and the gutter present inside the bar plate is The purpose is to collect clean water with no impurities in the gutter outside the jama board.
なお、本発明では邪摩板の内側に位置する樋は
邪摩板近くに設けるのが好ましく、またタンクの
内側壁内部で内側壁上縁近くに平面状の多孔性整
流板を設けるのが好ましい。前者により浮上した
不純物の邪摩板外部への流出を完全に防止でき、
後者によつて不純物の浮上をより効果的に抑制で
きる。 In addition, in the present invention, it is preferable that the gutter located inside the jama plate be provided near the jama plate, and it is also preferable to provide a planar porous rectifier plate inside the inner wall of the tank near the upper edge of the inner wall. . The former can completely prevent the floating impurities from flowing out to the outside of the jamb plate,
The latter makes it possible to more effectively suppress floating of impurities.
邪摩板の外側の樋は処理済水すなわち清水の排
出量を増すため分枝させてもよく、また複数本設
けてもよい。 The gutter outside the jama plate may be branched to increase the amount of treated water or fresh water discharged, or a plurality of gutter may be provided.
次に、図面に示す一例に従つて本発明を更に詳
しく説明する。 Next, the present invention will be explained in more detail according to an example shown in the drawings.
第1図において、1は瀘過タンク、2は瀘材で
ある溶剤溶液の流入口で、タンク1の底部に開口
している。3はタンク1の底部中央の適当な高さ
に取り付けた被処理(瀘過)液の導入口で、前後
方向に適当な長さを有し、その外周面に多数の比
較的小径孔を有しており、またその上方にはさら
に多数の微小孔を有する整水板4が配置してあ
る。5は溶剤溶液層である。前記溶剤溶液内には
陽極6と陰極7とからなる一対の電極が配置さ
れ、陰極7はタンク1の中央中心部に位置し、高
圧電源に接続されるに対し、陽極6は陰極7の外
側においてこの陰極7に対面し、接地されてい
る。さらに詳細に述べると、陰極7は断面V字形
をなし、前記方向にのびる左右一対の平担な傾斜
外面8を有するものであり、一方陽極6は、この
陰極7と火花放電を起さない適当な間隔を置いて
配置され、前記陰極7の両傾斜外面8に夫々対面
する左右一対の平担な傾斜面9を有し、この陽極
6の両傾斜内面9の下縁間には前記被処理液導入
口3より大きい開口部が形成されている。この陽
極6は、陽極吊持部材(図示されていない)を介
してタンク蓋(図示されていない)に固定されて
いる。陽極6の傾斜内面9と陰極7の傾斜外面8
は火花放電を起さない適当な間隔を有し、その間
に、前後方向にのびる左右一対の接触帯域10を
形成している。 In FIG. 1, 1 is a filtration tank, and 2 is a filtration material, an inlet for a solvent solution, which is opened at the bottom of the tank 1. 3 is an inlet for the liquid to be treated (filtered) installed at an appropriate height in the center of the bottom of the tank 1, and has an appropriate length in the front-rear direction, and has a large number of relatively small-diameter holes on its outer circumferential surface. A water regulating plate 4 having a large number of micropores is arranged above it. 5 is a solvent solution layer. A pair of electrodes consisting of an anode 6 and a cathode 7 are arranged in the solvent solution.The cathode 7 is located in the center of the tank 1 and is connected to a high voltage power source, while the anode 6 is located outside the cathode 7. It faces this cathode 7 and is grounded. More specifically, the cathode 7 has a V-shaped cross section and has a pair of left and right flat inclined outer surfaces 8 extending in the above direction, while the anode 6 is made of a suitable material that does not cause spark discharge with the cathode 7. It has a pair of left and right flat inclined surfaces 9 which are arranged at a distance from each other and face both inclined outer surfaces 8 of the cathode 7, respectively, and between the lower edges of both inclined inner surfaces 9 of the anode 6 there is a An opening larger than the liquid introduction port 3 is formed. This anode 6 is fixed to a tank lid (not shown) via an anode suspension member (not shown). Inclined inner surface 9 of anode 6 and inclined outer surface 8 of cathode 7
have an appropriate interval that does not cause spark discharge, and form a pair of left and right contact zones 10 extending in the front-rear direction between them.
陰極7は高圧導電線11に接続されるととも
に、この導電線11を収容した支持管12によつ
て機械的に支持されている。 The cathode 7 is connected to a high-voltage conductive wire 11 and is mechanically supported by a support tube 12 containing the conductive wire 11.
タンク1の側壁は二重壁になつており、その外
側壁12と内側壁13の間にポケツト14が形成
されている。ポケツト14は内部に溜つた不純物
を取出しやすいように下方で分割され、タンク1
の四隅で先細りに形成されている。タンク1の上
方で、内側壁13と外側壁12の間に、縦型の邪
摩板15が設けられており、この邪摩板15の内
側と外側に2本の樋16,17が配置されてい
る。(第2図及び第3図参照)。 The side wall of the tank 1 is double walled, and a pocket 14 is formed between the outer wall 12 and the inner wall 13. Pocket 14 is divided at the bottom to facilitate removal of impurities accumulated inside, and tank 1
It is tapered at the four corners. A vertical jamb 15 is provided above the tank 1 between the inner wall 13 and the outer wall 12, and two gutters 16 and 17 are arranged on the inside and outside of the jamb board 15. ing. (See Figures 2 and 3).
内側壁13の上縁18は溶剤溶液層5の液面1
9よりも上方に形成されており、溶剤溶液層5の
上面に形成される中間層20の上澄液が沈降性を
有する浮遊不純物を伴なつてポケツト14に溢出
するようになつており、邪摩板15は内側壁13
と外側壁12の間で内側壁13の上縁18とほぼ
同一の高さから上方に伸びて位置するものであ
り、ガスに伴つて浮上したガム質や溶剤が、ポケ
ツト14に溢出することなく、邪摩板15内部の
処理済液層すなわち水層21中を上昇するように
規制する。 The upper edge 18 of the inner wall 13 is the liquid level 1 of the solvent solution layer 5.
9, and the supernatant liquid of the intermediate layer 20 formed on the upper surface of the solvent solution layer 5 overflows into the pocket 14 with floating impurities having sedimentation properties, which may cause harmful effects. The friction plate 15 is attached to the inner wall 13
It extends upward from approximately the same height as the upper edge 18 of the inner wall 13 between the inner wall 13 and the outer wall 12, and prevents the gum and solvent that floated up with the gas from overflowing into the pocket 14. , the processed liquid layer, that is, the water layer 21 inside the jam plate 15 is regulated to rise.
樋16,17は内側壁13の上縁18より上方
で、邪摩板15の上端22及び外側壁12の上端
23より下方の同一高さにそれぞれの口すなわち
上縁を有するように形成されており、この樋1
6,17によつて処理溶液の液面は規制される。
邪摩板15の内側の樋17には処理済液と共に水
層21を上昇してきた浮遊不純物が流入する。樋
17から排出される処理済液は再び静電式瀘過装
置に送り、処理してもよい。邪摩板15の外側の
樋16にはポケツト14に溢出した処理済液の上
澄液のみが流入するので、樋16から排出される
処理済液はほとんど純水に近く、直接排水できる
ものとなり、工業用水としても利用できるものと
なる。 The gutters 16 and 17 are formed to have respective openings or upper edges at the same height above the upper edge 18 of the inner wall 13 and below the upper end 22 of the jam plate 15 and the upper end 23 of the outer wall 12. This gutter 1
6 and 17 regulate the liquid level of the processing solution.
Floating impurities that have risen in the water layer 21 along with the treated liquid flow into the gutter 17 inside the jam plate 15. The treated liquid discharged from the gutter 17 may be sent to the electrostatic filter again for treatment. Since only the supernatant liquid of the treated liquid overflowing into the pocket 14 flows into the gutter 16 on the outside of the jamb plate 15, the treated liquid discharged from the gutter 16 is almost pure water and can be directly drained. , it can also be used as industrial water.
なお、タンク1内部の内側壁13上縁18近く
には平面状の多孔性整流板24が存在し、これに
よつて中間層20の浮遊不純物の上昇が制限さ
れ、処理効果が高められる。 A planar porous rectifier plate 24 is present near the upper edge 18 of the inner wall 13 inside the tank 1, thereby restricting the rise of floating impurities in the intermediate layer 20 and enhancing the treatment effect.
次に、上記装置を使用した工場廃液の静電処理
方法について簡単に説明する。 Next, a method for electrostatic treatment of factory waste liquid using the above device will be briefly explained.
まず、電気絶縁性または誘電性で水より比重の
大きい溶剤、例えばパークロルエチレンを瀘過タ
ンク1内に流入口2より流入し、一定の液面19
まで充満させる。 First, a solvent that is electrically insulating or dielectric and has a higher specific gravity than water, such as perchlorethylene, flows into the filtration tank 1 from the inlet 2, and the liquid level 19 is maintained at a constant level.
Fill it up to.
次いで陰極7にマイナス直流高電圧を印加す
る。なお、本発明は内側電極を陽極とし、外側電
極を陰極とすることもでき、この場合は電極7が
陽極で、之に直流プラス高電圧が印加されること
になる。 Next, a negative DC high voltage is applied to the cathode 7. Note that in the present invention, the inner electrode can be used as an anode and the outer electrode can be used as a cathode. In this case, the electrode 7 is an anode, and a DC plus high voltage is applied thereto.
このように準備しておいて、被処理液、好まし
くはタンク1に充満した溶剤すなわちパークロル
エチレンと混合しエマルジヨン化した被処理液を
導入口3からタンク1内に導入する。導入口3に
導入された被処理液は速度が急速に低下し、多数
の小径孔を穿設した導入口3の外周面によつて小
さな粒滴となり、さらにその上方において多数の
微小孔を穿設したゆるやかな山形状の整水板によ
つて、より小さな粒滴となり陰極7の中心に向か
つて比重差により上昇する。 Having been prepared in this way, the liquid to be treated, preferably the liquid to be treated which has been mixed with the solvent filled in the tank 1, ie, perchlorethylene, and formed into an emulsion, is introduced into the tank 1 through the inlet 3. The speed of the liquid to be treated that is introduced into the inlet 3 rapidly decreases, and the liquid is turned into small droplets by the outer peripheral surface of the inlet 3, which has many small diameter holes, and is further formed into small droplets by drilling many micro holes above it. Due to the gently mountain-shaped water regulating plate provided, the droplets become smaller and move toward the center of the cathode 7, rising due to the difference in specific gravity.
陰極7の斜面8に接して負に帯電した粒滴は静
電場の作用で陽極8の方へ高速度で吸引され、陽
極斜面9に達した粒滴は今度は正に帯電し、再び
陰極7に向つて飛散する。粒滴が両極6,7間を
往復飛走する間に被処理液に含まれていた油分は
溶剤溶液5に溶解し、また固形物その他の不純物
も水分から分離され、ゆるやかな速度で上昇し、
固形物その他の浮遊不純物は中間層20を形成
し、水分はその上に水層21を形成する。 The negatively charged droplets that are in contact with the slope 8 of the cathode 7 are attracted toward the anode 8 at high speed by the action of the electrostatic field, and the droplets that reach the anode slope 9 are now positively charged and return to the cathode 7. scatter towards. While the droplets fly back and forth between the poles 6 and 7, the oil contained in the liquid to be treated is dissolved in the solvent solution 5, solids and other impurities are also separated from the water, and the liquid rises at a slow speed. ,
Solids and other suspended impurities form an intermediate layer 20, and moisture forms an aqueous layer 21 above it.
中間層20上面には多孔性整流板24が存在
し、これにより不純物が水層21に上昇するのが
抑制されており、不純物は内側壁13の上縁18
から乱流を起こすことなく効率よくポケツト14
に溢出する。また多孔質整流板24を通つて溶剤
微粒子などの不純物が浮上しても、これらは邪摩
板15の存在によつて邪摩板15外部の水層25
に流出することなく、内側の樋17に流入し、排
出口26から取出される。 A porous rectifying plate 24 is present on the upper surface of the intermediate layer 20, which suppresses impurities from rising into the water layer 21.
Pocket 14 efficiently without causing turbulence
overflowing to. Furthermore, even if impurities such as solvent fine particles float through the porous rectifying plate 24, they will be absorbed by the water layer 25 outside the strain plate 15 due to the presence of the strain plate 15.
It flows into the inner gutter 17 without flowing out to the inside, and is taken out from the outlet 26.
内側壁13の上縁18からポケツト14に溢出
した被処理液は邪摩板15の存在によつて、横に
広がることなく、内側壁13の外面に沿つた幾分
下方への流れを生ずるため、被処理液に含まれる
浮遊不純物は効率よくポケツト14内部に沈降
し、水分は純粋な状態で上層に分離し、きれいな
上澄液として外側壁12と邪摩板15の間に水層
25を形成する。水層25の水は樋16に流入し
て、排出口27から取出される。 Because the liquid to be treated overflowing from the upper edge 18 of the inner wall 13 into the pocket 14 does not spread laterally due to the presence of the baffle plate 15, it flows somewhat downward along the outer surface of the inner wall 13. , floating impurities contained in the liquid to be treated are efficiently settled inside the pocket 14, water is separated into an upper layer in a pure state, and a water layer 25 is formed between the outer wall 12 and the jam plate 15 as a clean supernatant liquid. Form. Water in the water layer 25 flows into the gutter 16 and is taken out from the outlet 27.
内側の樋17を通して排出口26から取出され
た処理済液は溶剤などの不純物を除くために再び
静電式瀘過装置に導入されるなど再処理される
が、外側の樋16を通して排出口27から取出さ
れた水層はほとんど不純物を含まないものであ
り、そのまま排水しても問題がなく、工業用水と
して直接再利用できるものである。 The treated liquid taken out from the outlet 26 through the inner gutter 17 is reprocessed by being introduced into an electrostatic filtration device again to remove impurities such as solvents, but it is taken out from the outlet 27 through the outer gutter 16. The water layer extracted from the water layer contains almost no impurities, so there is no problem in draining it as is, and it can be directly reused as industrial water.
なお、ポケツト14内で貯留される不純物はポ
ケツト14が先すぼまりに形成されているため速
やかに沈降濃縮され、ポケツト14下端の取出口
28から取出される。また、本発明の装置ではタ
ンク1の内側壁13の内面及び電極吊持部材の表
面などをポリ塩化ビニルやテフロンなどの絶縁性
材料で構成することによつて、静電瀘過効果をよ
り高めることができる。 Incidentally, since the pocket 14 is formed with a tapered end, the impurities stored in the pocket 14 are quickly sedimented and concentrated, and are taken out from the outlet 28 at the lower end of the pocket 14. Furthermore, in the device of the present invention, the inner surface of the inner wall 13 of the tank 1 and the surface of the electrode suspension member are made of an insulating material such as polyvinyl chloride or Teflon, thereby further enhancing the electrostatic filtration effect. be able to.
第1図は本発明の装置の一例を示す断面図、第
2図は第1図の装置の側面図、第3図は第1図の
装置から多孔性整流板を取り除いた状態を示す平
面図である。
1……タンク、6……陽極、7……陰極、12
……外側壁、13……内側壁、14……ポケツ
ト、15……邪摩板、16,17……樋、21,
25……水層、24……多孔性整流板。
FIG. 1 is a sectional view showing an example of the device of the present invention, FIG. 2 is a side view of the device shown in FIG. 1, and FIG. 3 is a plan view showing the device shown in FIG. 1 with the porous rectifying plate removed. It is. 1...tank, 6...anode, 7...cathode, 12
... Outer wall, 13... Inner wall, 14... Pocket, 15... Jama board, 16, 17... Gutter, 21,
25...Water layer, 24...Porous current plate.
Claims (1)
処理液を導入するための入口を設け、前記タンク
内部に前記溶剤溶液内において一対の電極を配置
し、この電極間に高圧直流電圧を印加するように
した静電式瀘過装置において、前記タンクの側壁
を二重壁にして、その内側壁と外側壁との間にポ
ケツトを形成し、前記内側壁の上縁は前記溶剤溶
液の溶面よりも上方に形成し、溶剤溶液層の上面
に形成される中間層の浮遊不純物が前記内側壁の
上縁から前記ポケツトへ溢出するようにしたもの
であつて、内側壁と外側壁の間に、四方に連続し
た縦型の邪摩板が存在し、この邪摩板の上端が内
側壁上縁より上方に位置し、下端が内側壁上縁と
同一又はそれより少し下方に位置すること、及び
上記邪摩板の外側と内側にそれぞれ四方に連続し
た樋が設けられており、これらの樋の口の高さが
同一であり、邪摩板及び外側壁の上端より下方で
内側壁上縁より上方に位置することを特徴とする
静電式瀘過装置。 2 内側壁内部で、内側壁上縁近くに平面状の多
孔性整流板が設けられている特許請求の範囲第1
項記載の装置。 3 外側の樋が分枝している特許請求の範囲第1
項又は第2項記載の装置。 4 上記ポケツトが下方で分割され、先すぼまり
に形成されている特許請求の範囲第1項〜第3項
いずれかに記載の装置。 5 内側壁の内面及び電極吊持部材の表面が絶縁
性材料で形成されている特許請求の範囲第1項〜
第4項いずれかに記載の装置。[Scope of Claims] 1. A tank containing an electrically insulating solvent solution is provided with an inlet for introducing the liquid to be treated, a pair of electrodes is arranged in the solvent solution inside the tank, and a pair of electrodes is arranged between the electrodes. In an electrostatic filtration device that applies a high DC voltage, the side wall of the tank is made into a double wall, a pocket is formed between the inner wall and the outer wall, and the upper edge of the inner wall is a double wall. The intermediate layer is formed above the melting surface of the solvent solution so that floating impurities in the intermediate layer formed on the upper surface of the solvent solution layer overflow from the upper edge of the inner wall to the pocket, and the inner wall There is a vertical jama board that is continuous on all four sides between the and outer wall, and the upper end of this jama board is located above the upper edge of the inner wall, and the lower end is the same as or slightly lower than the upper edge of the inner wall. It is located below, and there are continuous gutters in all four directions on the outside and inside of the jama board, and the mouths of these gutters are at the same height, and the gutter is located below the top of the jama board and the outer wall. An electrostatic filtration device characterized by being located above the upper edge of the inner wall. 2. Claim 1, in which a planar porous rectifying plate is provided inside the inner wall near the upper edge of the inner wall.
Apparatus described in section. 3 Claim 1 in which the outer gutter is branched
The device according to paragraph 2 or paragraph 2. 4. The device according to any one of claims 1 to 3, wherein the pocket is divided at the bottom and tapered at the end. 5. Claims 1 to 5, wherein the inner surface of the inner wall and the surface of the electrode suspension member are formed of an insulating material.
The device according to any of paragraph 4.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13995983A JPS6031810A (en) | 1983-07-29 | 1983-07-29 | Electrostatic filter apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13995983A JPS6031810A (en) | 1983-07-29 | 1983-07-29 | Electrostatic filter apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6031810A JPS6031810A (en) | 1985-02-18 |
| JPH0122821B2 true JPH0122821B2 (en) | 1989-04-27 |
Family
ID=15257650
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13995983A Granted JPS6031810A (en) | 1983-07-29 | 1983-07-29 | Electrostatic filter apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6031810A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04200660A (en) * | 1990-11-29 | 1992-07-21 | Toshiyuki Tokumoto | Electrostatic filter |
| JP2967350B1 (en) * | 1998-06-02 | 1999-10-25 | 敏行 ▲とく▼本 | Electrostatic treatment apparatus and waste liquid treatment method using the same |
-
1983
- 1983-07-29 JP JP13995983A patent/JPS6031810A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6031810A (en) | 1985-02-18 |
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