JPS6031810A - Electrostatic filter apparatus - Google Patents
Electrostatic filter apparatusInfo
- Publication number
- JPS6031810A JPS6031810A JP13995983A JP13995983A JPS6031810A JP S6031810 A JPS6031810 A JP S6031810A JP 13995983 A JP13995983 A JP 13995983A JP 13995983 A JP13995983 A JP 13995983A JP S6031810 A JPS6031810 A JP S6031810A
- Authority
- JP
- Japan
- Prior art keywords
- wall
- liquid
- treated
- upper edge
- 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.)
- Granted
Links
- 239000007788 liquid Substances 0.000 claims abstract description 41
- 239000002904 solvent Substances 0.000 claims abstract description 37
- 239000012535 impurity Substances 0.000 claims abstract description 27
- 238000001914 filtration Methods 0.000 claims description 15
- 239000000725 suspension Substances 0.000 claims description 4
- 239000011810 insulating material Substances 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 27
- 239000006228 supernatant Substances 0.000 abstract description 4
- 239000007787 solid Substances 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 3
- 230000004888 barrier function Effects 0.000 abstract 3
- 238000000926 separation method Methods 0.000 abstract 1
- 230000005686 electrostatic field Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 230000005484 gravity Effects 0.000 description 2
- 239000008235 industrial water Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical group ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 229950011008 tetrachloroethylene Drugs 0.000 description 1
- 230000002618 waking effect Effects 0.000 description 1
Landscapes
- Electrostatic Separation (AREA)
Abstract
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
た静電式濾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
この出願に先立って、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濾過装置が本発明者に
よって発明されており、例えば特公昭40−15549
号公報、特公昭51−3941号、特公昭51−394
2号公報及び特公昭51−23742号公報などに開示
されている。Prior Art Prior to this application, the present inventor had invented a filtration device for sewage or waste liquid that utilizes an induced electrostatic field in an electrically insulating solvent solution.
Publication, Special Publication No. 51-3941, Special Publication No. 51-394
This method is disclosed in Japanese Patent Publication No. 2 and Japanese Patent Publication No. 51-23742.
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って形成される
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。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 liquid to be treated 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 into the floating impurities. The treated liquid layer is discharged from the discharge port, and the treated water in the 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濾過装置によって、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ったが、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。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 the gases dissolved in the treated liquid can be discharged. When separated and floated in an electrostatic field, the contamination of gum and solvent particles that are insoluble in both solvent and water is unavoidable. Often requires further processing.
なお、排水の有機物質含有量に対する規制は近年ますま
す厳しくなってきている。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濾過装置
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濾
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ットを形成し、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ットへ浴出するようにしたも
のであって、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 a pocket is formed between the inner wall and the outer wall. The upper edge is formed above the liquid level of the solvent solution, so that suspended impurities in the intermediate layer formed on the upper surface of the solvent solution layer bathe out 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−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. , its mouth is located below the upper ends 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
に伴って浮上する溶剤やガム質を、邪摩板の存在によっ
てポケット側に流出させず、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。In other words, in the present invention, the presence of the jam 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 collects them in the gutter located inside the jam plate. The purpose is to collect clean water without any 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、後者によっ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 allows the floating impurities to be completely prevented from flowing out of the friction plate, and the latter allows the floating of the impurities to be more effectively suppressed.
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っ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)は濾材で
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)が配置しである。(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(7)
の電極が配置され、陰ヒ血タンク(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
7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)の面傾斜外面(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)の面傾斜内面(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。In FIG. 1, (1) is a filtration tank, and (2) is a filter medium that is an inlet for a solvent solution, which is opened at the bottom of the tank (1). (3) is an inlet for the treated (filtered) liquid installed at an appropriate height in the center of the bottom of the tank (1). It has a small diameter hole, and above it a water regulating plate (4) having a large number of microholes is arranged. (5) is a solvent solution layer. A pair of electrodes (7) consisting of an anode (6) and a cathode (7) are arranged in the solvent solution, and are located in the center of the anode blood tank (1) and connected to a high voltage power source. On the other hand, the anode (6) faces the cathode (7) on the outside thereof and is grounded. More specifically, the cathode (7) has a 7-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) has a 7-shaped cross section. The anode (7) has a pair of left and right flat sloped surfaces (9) which are arranged at an appropriate interval to prevent spark discharge from occurring and which face the sloped outer surface (8) of the cathode (7), respectively. An opening larger than the treated liquid inlet (3) is formed between the lower edges of the inclined inner surface (9) of 6). This anode (6) is fixed to a tank lid (not shown) via an anode suspension member (not shown).
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。The inclined inner surface (9) of the anode (6) and the inclined outer surface (
8) have an appropriate spacing 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01)に接続されるとともに、
この導電線(11)を収容した支持管(ロ)によって機
械的に支持されている。The cathode (7) is connected to the high voltage conductive wire 01),
It is mechanically supported by a support tube (b) containing the conductive wire (11).
タンク(1)の側壁は二重壁になっており、その外側壁
(ロ)と内側壁03)の間にポケット0→が形成されて
いる。ポケット04)は内部に溜っ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02)の間に、縦型の邪摩板θ5)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Oa) 、 (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 a double wall, and a pocket 0→ is formed between the outer wall (b) and the inner wall 03). Pocket 04) is divided at the bottom to facilitate removal of impurities accumulated inside, and is tapered at the four corners of tank (1). Above the tank (1), on the inner wall (
A vertical jamb plate θ5) is provided between the jamb plate (13) and the outer wall 02), and two gutters Oa) and (17) are arranged on the inside and outside of this jamb plate (15). ing. (See Figures 2 and 3).
内側壁03)の上縁(]8)は溶剤溶液層(5)の液面
09)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に)の上澄液が沈降性を有す
る浮遊不純物を伴なってポケット0→に溢出するように
なっており、邪摩板(15)は内側壁03)と外側壁(
ロ)の間で内側壁(13)の上縁(財)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、ガスに伴って
浮上したガム質や溶剤が、ポケット0→に溢出すること
なく、邪摩板05)内部の処理済液層すなわち水層(2
1)中を上昇するように規制する。The upper edge (]8) of the inner wall 03) is formed above the liquid level 09) of the solvent solution layer (5), and
The supernatant liquid (in the intermediate layer formed on the upper surface) overflows into the pocket 0 → with floating impurities that have sedimentation properties, and the jam plate (15) is formed between the inner wall 03) and the outer side. wall(
It extends upward from almost the same height as the upper edge of the inner wall (13) between the inner wall (13), and the gum and solvent that floated up with the gas overflow into the pocket 0 →. The treated liquid layer, that is, the water layer (2) inside the jama plate 05)
1) Regulate the inside to rise.
樋(16) 、 (17)は内側壁(13)の上縁(]
8)より上方で、邪摩板(15)の上端に)及び外側壁
(ロ)の上縁(ハ)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(
16) 、 (17)によって処理溶液の液面は規制さ
れる。邪摩板05)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濾過
装置に送り、処理してもよい。邪摩板05)の外側の樋
06)にはポケット04)に溢出した処理済液の上澄液
のみが流入するので、樋θ6)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 located at the upper edge of the inner wall (13) (]
8) above the upper end of the jama plate (15)) and the outer wall (b) so as to have respective openings or upper edges at the same height below the upper edge (c) of the outside wall (b); This gutter (
16) The liquid level of the processing solution is regulated by (17). Floating impurities that have risen in the water layer (21) flow together with the treated liquid into the gutter (17) inside the jam plate 05). The treated liquid discharged from the gutter (17) may be sent to the electrostatic filtration device again for treatment. Only the supernatant liquid of the treated liquid overflowing into the pocket 04) flows into the gutter 06) on the outside of the jama plate 05), so the treated liquid discharged from the gutter θ6) is almost pure water and is directly The water can be drained and can also be used as industrial water.
なお、タンク(1)内部の内側壁03)上縁08)近く
には平面状の多孔性整流板(ハ)が存在し、これによっ
て中間層に)の浮遊不純物の上昇が制限され、処理効果
が高められる。In addition, there is a planar porous rectifying plate (c) near the inner wall 03) and upper edge 08) inside the tank (1), which limits the rise of floating impurities in the middle layer) and improves the treatment effect. is enhanced.
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、例えばノ(−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(10)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 chloroethylene, flows into the filtration tank (1) from the inlet (2) and is filled to a certain level (10). .
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). In addition, 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(りに充満した溶剤すなわちパークロルエチレンと混
合しエマルジョ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)の外周面によっ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って、より小さな粒滴となり陰極(
7)の中心に向かって比重差により上昇する。After being prepared in this way, the liquid to be treated, preferably the liquid to be treated which has been mixed with the solvent, i.e. perchlorethylene, filled in the tank and made into an emulsion, is introduced into the tank (1) from the inlet (3). The speed of the liquid to be treated that is introduced into the inlet (3) decreases rapidly, and the liquid is turned into small droplets by the outer circumferential surface of the inlet (3), which has many small diameter holes, and furthermore, a large number of minute droplets are formed above the inlet (3). A gently mountain-shaped water regulating plate with holes drilled in it allows the droplets to become smaller and reach the cathode (
7) rises toward the center 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)に向って飛散する。粒滴が両極(6)。The negatively charged droplets 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 slope (9) of the anode are in turn It becomes positively charged and scatters toward the cathode (7) again. The droplet has both poles (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に)を形成し、水分はそ
の上に水層0◇を形成する。During the reciprocating flight between (7) and 5), 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 rate to become solid. Contaminants and other floating impurities form an intermediate layer ), and water forms an aqueous layer 0◇ above it.
中間層に)上面には多孔性整流板(ハ)が存在し、これ
により不純物が水層に上昇するのが抑制されており、不
純物は内側壁03)の上縁(18)から乱流を起こすこ
となく効率よくポケットθ→に浴出する。また多孔質整
流板e4を通って溶剤微粒子などノ不純物が浮上しても
、これらは邪摩板(1つの存在によって邪摩板に)外部
の水層に)に流出することなく、内側の樋(17)に流
入し、排出口(ハ)から取出される。There is a porous rectifying plate (c) on the upper surface of the middle layer (03), which suppresses impurities from rising into the water layer, and the impurities pass through the turbulent flow from the upper edge (18) of the inner wall (03). Efficiently bathe into pocket θ→ without waking it up. In addition, even if impurities such as solvent particles float through the porous rectifying plate e4, they will not flow into the water layer (into the water layer on the outside) and will flow into the inner gutter. (17) and is taken out from the outlet (c).
内側壁(18)の上縁(18)からポケットθ→に浴出
した被処理液は邪摩板05)の存在によって、横に広が
ることなく、内側壁(13)の外面に沿った幾分下方へ
の流れを生ずるため、被処理液に含まれる浮遊不純物は
効率よくポケット04)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(ロ)
と邪摩板05)の間に水層に)を形成する。水層(ハ)
の水は樋06)に流入して、排出口に)から取出される
。The liquid to be treated that has leaked from the upper edge (18) of the inner wall (18) into the pocket θ→ does not spread laterally due to the presence of the jamb plate 05), but rather spreads along the outer surface of the inner wall (13). Due to the downward flow, floating impurities contained in the liquid to be treated efficiently settle inside the pocket (04), and water is separated in a pure state to the upper layer, which is transferred to the outer wall (2) as a clean supernatant liquid.
A water layer) is formed between the and the jama plate 05). Water layer (c)
The water flows into the gutter 06) and is removed from the outlet).
内側の樋0ηを通して排出口(ハ)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濾過装
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(ハ)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 (c) through the inner gutter 0η is reprocessed by being introduced into the electrostatic filtration device again to remove impurities such as solvents.
The water layer taken out from the outlet (c) through the drain port (c) contains almost no impurities, and there is no problem in draining it as is, and it can be directly reused as industrial water.
なお、ポケット04)内で貯留される不純物はポケット
0→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、ポケット0→下端の取出口から取出される。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って、静電
濾過効果をより高めることができる。Note that the impurities stored in pocket 04) are quickly sedimented and concentrated because pocket 0→ is formed with a tapered tip, and are taken out from the outlet at the lower end of pocket 0→. 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 enhancing the electrostatic filtration effect. can be increased.
第1図は本発明の装置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03)・・・・・−・・・・・・・・
内側壁(14) ・・・・・・・・・・・・・・・ポケ
ット(15) ・・・・・−・・・・−・・邪摩板(1
a)、 (17) ””−””・樋0I)、に)・・・
・・−・−・・水層@4−・・・・・・・−・−・・多
孔性整流板特許出願人 徳 本 敏 行
同 徳 本 健 奇
第3図
手続補正書
1、事件の表示 昭和58年特許頴第13!;1959
号2、発明の名称 静電式濾過装置
3、補正をする者
事件との関係 特許出願人
6、補正により増加する発明の数
(1) 明細書、特許請求の範囲の項を別紙の通り補正
する。
12)同書、第13頁第7行、「取出口」とある勿、「
取出口+28) Jと補正する。
2、特許請求の範囲
(1) 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濾過装置に
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ットを形成し、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晟し、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lケラトへ浴出するようにしたものであっ
て、内4Inと外側壁の間に、四方に連続した縦型O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油過装置。
(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。
(11) 外側の樋が分校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) 上記ポケッ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。FIG. 1 is a sectional view showing an example of the device of the present invention, and FIG.
1 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. (1)-・・・・・・・・・・・・・・・Tank (6)・・・・
・・・・・・・・・・・・Anode (7) ・・・・・・
・・・・・・−・Cathode (12) ・・・・・・・・・・
...Outside wall 03) ...
Inner wall (14) ・・・・・・・・・・・・・・・Pocket (15) ・・・・・・−・・・・・・・・・・・・Jama board (1
a), (17) “”-””・Gutter 0I), ni)...
・ - ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・ ・Display 1985 Patent No. 13! ;1959
No. 2, Title of the invention Electrostatic filtration device 3, Relationship with the case of the person making the amendment Patent applicant 6, Number of inventions to be increased by the amendment (1) Amend the description and scope of claims as attached. do. 12) The same book, page 13, line 7, it says ``outlet'', but ``
Output port + 28) Correct as J. 2. 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 the electrode In an electrostatic filtration device in which a high DC voltage is applied between the tank, 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 shaped 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 bathe out from the upper edge of the inner wall to the l kerato. Between the inner wall and the outer wall, there is a vertical Ojama board that is continuous in all four directions, and the upper end of this jama board is above the upper edge of the inner wall. An electrostatic oil filtration device characterized in that the heights of the mouths of these gutters are the same and are located below the upper ends of the jam plate and the outer wall and above the upper edge of the inner wall. (2) The device according to claim 1, wherein a planar porous rectifying plate is provided inside the inner wall near the upper edge of the inner wall. (11) Claim 1 in which the outer gutter is separated
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 tip. (5) The device according to any one of claims 1 to 4, wherein the inner surface of the inner wall and the surface of the electrode suspension member are formed of an insulating material.
Claims (5)
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濾過装置にお
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ットを形成し、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
縁から前記ポケットへ浴出するようにしたものであって
、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−又はそれより少し下方に
位置すること、又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
濾過装置。(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 are arranged inside the tank in the solvent solution, and a high-voltage DC voltage is applied between the electrodes. In the electrostatic filtration device, 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 formed to absorb the solvent of the solvent solution. The intermediate layer is formed above the surface of the solvent solution layer so that floating impurities in the intermediate layer formed on the upper surface of the solvent solution layer are bathed from the upper edge of the inner wall into the pocket, and the intermediate layer is formed above the inner wall and the outer wall. In between, there is a vertical jama board that is continuous on all four sides, and the upper end of this 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. Furthermore, there are continuous gutters in all four directions on the outside and inside of the above-mentioned jama board, and the mouths of these gutters are at the same height, and the inside wall is located below the upper end of the jama board and the outside wall. An electrostatic filtration device characterized by being located above the upper edge.
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。(2) The device according to claim 1, wherein a planar porous rectifying plate is provided inside the inner wall near the upper edge of the inner wall.
は第2項記載の装置。(3) The device according to claim 1 or 2, wherein the outer gutter is branched.
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。(4) The device according to any one of claims 1 to 3, wherein the pocket is divided at the bottom and tapered at the tip.
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。(5) The device according to any one of claims 1 to 4, wherein the inner surface of the inner wall and the surface of the electrode suspension member are formed of an insulating material.
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 true JPS6031810A (en) | 1985-02-18 |
| JPH0122821B2 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) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5256270A (en) * | 1990-11-29 | 1993-10-26 | Toshiyuki Tokumoto | Electrostatic separating apparatus |
| EP0962241A1 (en) * | 1998-06-02 | 1999-12-08 | Toshiyuki Tokumoto | An electrostatic treating apparatus |
-
1983
- 1983-07-29 JP JP13995983A patent/JPS6031810A/en active Granted
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5256270A (en) * | 1990-11-29 | 1993-10-26 | Toshiyuki Tokumoto | Electrostatic separating apparatus |
| EP0962241A1 (en) * | 1998-06-02 | 1999-12-08 | Toshiyuki Tokumoto | An electrostatic treating apparatus |
| US6123813A (en) * | 1998-06-02 | 2000-09-26 | Tokumoto; Toshiyuki | Electrostatic treating apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0122821B2 (en) | 1989-04-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPH07100302A (en) | Charge coalescer type oil-water separator | |
| KR840000673A (en) | Electrolytic Reduction Battery | |
| EP0035812A1 (en) | Apparatus for the flotation of flocculated solid material in a liquid | |
| JPS6031810A (en) | Electrostatic filter apparatus | |
| JP2541525B2 (en) | Semiconductor substrate processing equipment | |
| JP7712511B2 (en) | Crossflow Precipitation Device and Method of Use - Patent application | |
| US5256270A (en) | Electrostatic separating apparatus | |
| JPH08108173A (en) | Spiral flow type flotation separation apparatus | |
| JP3374746B2 (en) | Anaerobic treatment equipment for organic wastewater | |
| JP2003164705A (en) | Oil/water separation apparatus | |
| CA1057697A (en) | Method and device for breaking stabilized emulsions | |
| SU1411289A1 (en) | Apparatus for electrochemical purification of waste water | |
| JPH0420481Y2 (en) | ||
| JPS5973235A (en) | Electric discharge machining device | |
| KR790001997B1 (en) | Electrostatic Separator | |
| JP2967350B1 (en) | Electrostatic treatment apparatus and waste liquid treatment method using the same | |
| JPH1028968A (en) | Separator of oil and water | |
| JPH0448880Y2 (en) | ||
| RU148103U1 (en) | DEVICE FOR CLEANING OIL-CONTAINING WATERS | |
| JPS5817803A (en) | screen device | |
| SU580879A1 (en) | Apparatus for clarification of waste water | |
| JPS63287594A (en) | Structure of electrolytic floatation and separation tank | |
| JPS60232213A (en) | Electric treatment of liquid | |
| JPH0260362B2 (en) | ||
| JPH0378121B2 (en) |