JPH06343971A - Alternative current electrolytic flocculation apparatus - Google Patents

Alternative current electrolytic flocculation apparatus

Info

Publication number
JPH06343971A
JPH06343971A JP16400793A JP16400793A JPH06343971A JP H06343971 A JPH06343971 A JP H06343971A JP 16400793 A JP16400793 A JP 16400793A JP 16400793 A JP16400793 A JP 16400793A JP H06343971 A JPH06343971 A JP H06343971A
Authority
JP
Japan
Prior art keywords
liq
aluminum
liquid
electrodes
electrode
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.)
Pending
Application number
JP16400793A
Other languages
Japanese (ja)
Inventor
Shigeo Tochikubo
窪 滋 夫 栃
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TYK Corp
Original Assignee
TYK Corp
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 TYK Corp filed Critical TYK Corp
Priority to JP16400793A priority Critical patent/JPH06343971A/en
Publication of JPH06343971A publication Critical patent/JPH06343971A/en
Pending legal-status Critical Current

Links

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PURPOSE:To neutralize electric charges of a colloidal component and a suspended component dispersed in a liq. with a polyvalent ion of positive charge, aggromelate them by the actions of crosslinking of an insoluble hydroxide and van der Waals force, associate the aggromelation by means of floating and stirring forces of hydrogen and oxygen bubbles and separate and remove them with a high accuracy by means of a simple filtering and adsorption material. CONSTITUTION:A cathode cylinder 3 of a physically and chemically stable graphite and an aluminum or iron anode cylinder 4 producing ions with positive charge having both actions of neutralization of electric charge and crosslinking are arranged on an insulation ring 6 with an opening 5 for a stored soln. in a liq. tank 1. It is possible thereby to flocculate fine particles in city water, waste water, cutting liq. and washing liq. for a machine and to make filtering and adsorption easy.

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、水道水,下水などに含
まれる懸濁,コロイド成分,水系洗浄液中の油分,スラ
ッジ,更にまた、水溶性切削液中の乳化油,微粒子な
ど、液中に分散し、不具合の原因となる不純物を電解に
よって生じる水素,酸素気泡による攪拌力、コロイド粒
子などの荷電中和と、時により架橋作用を果たす陽極か
らの正荷電の多価イオン,溶解性ポリマーイオン,不溶
性の水酸化物により凝集浮上させ、濾過分離を容易とし
た交流電解凝集に関するものである。
BACKGROUND OF THE INVENTION The present invention relates to suspensions, colloidal components contained in tap water, sewage, etc., oils and sludges in water-based cleaning fluids, and emulsion oils and fine particles in water-soluble cutting fluids. Positively charged polyvalent ions from the anode that disperse into the anode and cause impurities to cause problems such as stirring force by hydrogen and oxygen bubbles generated by electrolysis, charge neutralization of colloidal particles, and sometimes cross-linking, soluble polymer The present invention relates to AC electrolytic coagulation in which flocculation and flotation are facilitated by ionic and insoluble hydroxide to facilitate separation by filtration.

【0002】[0002]

【従来の技術】従来、上下水道での固液分離には、広大
な施設面積と多くの処理時間を要し、問題が多かった。
また、水系洗浄液中に乳化,懸濁した油分,スラッジを
有効に除去し、循環使用出来る簡易な手段はなかった。
更に、俗称“エマルジョン”と称される乳化油を含む切
削液の廃液から切削油を分離除去し、水分だけをまま排
出出来る手段もなかった。更にまた、水系洗浄機に使用
される洗浄液中に混入し、白濁,エマルジョン化する油
分,拡散,懸濁するスラッジを効果的、速効的に分離除
去し、水のみそのまま排出出来るものはなかった。
2. Description of the Related Art Conventionally, solid-liquid separation in water and sewage has been problematic because it requires a vast facility area and a long processing time.
Further, there is no simple means for effectively removing oil and sludge that have been emulsified and suspended in the water-based cleaning liquid and can be circulated for use.
Further, there is no means for separating and removing cutting oil from waste liquid of cutting fluid containing emulsified oil, which is commonly called "emulsion", and discharging only water as it is. Furthermore, there is no one that can effectively and quickly separate and remove white turbidity, emulsified oil content, sludge that diffuses and suspends when mixed in a cleaning liquid used in a water-based cleaning machine, and only water can be discharged as it is.

【0003】そこで、本出願人はポリプロピレン,ポリ
エチレンなどの吸水性を有さない化学合成繊維からなる
不織布などの反毛化品を圧縮充填し、液表面の油膜ま
た、エマルジョン化した油分,分散している微粒子を除
去,分離することを提案した。しかし、コロイド領域に
まで微細化した油分,粒子は粗な懸濁質とは異なり、そ
のままでは、濾過吸着出来ない不具合を生じた。
Therefore, the applicant of the present invention compresses and fills an anti-hair-finished product such as a non-woven fabric made of a chemically synthetic fiber having no water-absorbing property such as polypropylene or polyethylene, and the oil film on the liquid surface or the emulsified oil component is dispersed. It was proposed to remove and separate the fine particles that are present. However, unlike the coarse suspension, the oil and particles that have been made finer to the colloidal region have a problem that they cannot be filtered and adsorbed as they are.

【0004】[0004]

【発明が解決しようとする課題】即ち、本発明の交流電
解凝集装置は、洗浄機などの液槽内に、両極に正荷電の
多価イオンを生成する素材を用いて構成した電解具を設
け、陽極からの正荷電のイオンなどにより電解質液中に
分散している負荷電のコロイド成分を荷電中和し、ファ
ン・デア・ヴァールスの力による凝集,フロック化を可
能とし、両極からの水素,酸素気泡により液槽全体に浮
上対流を発生させることにより例えば、数十ミクロンの
マイクロフロック相互を衝突せしめ、数百ミクロン以上
まで集塊させ、簡易な濾過,吸着によっても、高い精度
の固液分離が出来る特徴を要旨とする。
That is, the AC electrolytic coagulation apparatus of the present invention is provided with an electrolytic device constituted by a material for generating positively charged polyvalent ions at both electrodes in a liquid tank such as a washing machine. , The positively charged ions from the anode neutralize the negatively charged colloidal components dispersed in the electrolyte solution, enabling the aggregation and flocculation by the force of Van der Waals, and the hydrogen from both electrodes, By generating levitation convection in the entire liquid tank by oxygen bubbles, for example, micro flocs of several tens of microns collide with each other and agglomerate to several hundreds of microns or more, and high-precision solid-liquid separation is achieved even by simple filtration and adsorption. The feature is the feature.

【0005】本発明は、上水,下水処理,洗浄機などの
装置,システムに組み込まれる液槽中に、両極に導電性
を有し、電解通電時に、正荷電の多価イオンを発生する
素材により構成し、電解質液中の除去すべき、コロイド
成分,懸濁成分の負の電荷を荷電中和し、ファン・デア
・ヴァールス力により結合せしめ、フロック形成するこ
とが出来るようにした電解凝集装置を提供するものであ
る。
The present invention is a material which has conductivity in both electrodes in a liquid tank incorporated in equipment such as clean water, sewage treatment, and a washing machine, and a system, and which generates positively charged polyvalent ions when electrolyzing. Electrolytic flocculation device which is composed of the following components and is capable of forming a floc by neutralizing the negative charges of the colloidal component and the suspension component to be removed in the electrolyte solution and binding them by Van der Waals force. Is provided.

【0006】本発明の他の目的とするところは、両極に
アルミニュウム,鉄,銅,亜鉛などを用い、荷電中和に
最も有効に働く、正荷電の水酸化物ポりマー多価イオン
を得ることが出来る電解凝集装置を提供するものであ
る。
Another object of the present invention is to use aluminum, iron, copper, zinc or the like for both electrodes to obtain a positively charged hydroxide polymer multivalent ion that works most effectively for charge neutralization. It is intended to provide an electrolytic coagulation device that can be used.

【0007】また、本発明の他の目的とするところは、
両極にアルミニュウム、鉄など荷電中和と同時に架橋作
用を有する素材を用いることにより、フロック形成を補
強出来る電解凝集装置を提供するものである。
Another object of the present invention is to:
It is intended to provide an electrolytic coagulation device capable of reinforcing floc formation by using a material having a cross-linking action at the same time as charge neutralization such as aluminum and iron for both electrodes.

【0008】さらにまた、本発明の他の目的とするとこ
ろは、強い浮上流によるマイクロフロックの集塊を効果
的、速効的に行うため、両極を筒とし、いずれかの極と
なる外筒は下部に液槽からの補給口を開口し、また、対
峙する相手極となる内筒には液中に没する全周に内筒内
側の極の循環を可能とする複数を開口し、内,外筒を近
接設置した内,外筒の対峙する両極表面からのガスの浮
上流により、油分を浮上凝集せしめ、陽極からの正荷電
のイオンの荷電中和による粒子の凝集フロックを一層集
塊することが出来る電解凝集装置を提供するものであ
る。
Still another object of the present invention is to make both poles a cylinder and to form an outer cylinder which becomes either pole in order to effectively and quickly effect the agglomeration of microflocs by a strong floating upstream. A replenishment port from the liquid tank is opened in the lower part, and a plurality of poles that allow circulation of the pole inside the inner cylinder are opened in the inner cylinder which is the opposite electrode facing each other, all around the submerged inside. The oil is floated and agglomerated by the floating gas upstream from the opposite electrodes of the outer cylinder in the case where the outer cylinder is installed in close proximity, and the floc of particles is further aggregated by the charge neutralization of positively charged ions from the anode. It is intended to provide an electrolytic coagulation device that can be used.

【0009】[0009]

【課題を解決するための手段】即ち、本発明の交流電解
凝集装置は、コロイド,懸濁径の粒子、油分が分散存在
する液槽中に、両極は導電性で、通電時に正電荷の多価
イオン,溶解性ポリマーイオン,不溶性水酸化物を生成
し、分散成分の荷電中和を行い、凝集と架橋とを同時に
行うことが出来る素材により構成、液槽中に分散する除
去物を凝集し、容易に分解可能としたことを特徴として
構成したものである。
That is, in the AC electrolytic coagulation apparatus of the present invention, in a liquid tank in which colloid, particles with a suspension diameter, and oil are dispersed, both electrodes are conductive and a large amount of positive charge is applied when electricity is applied. It is composed of materials that generate valent ions, soluble polymer ions, insoluble hydroxides, neutralize the charge of the dispersed components, and can perform coagulation and crosslinking at the same time. Aggregate the removed substances dispersed in the liquid tank. It is characterized in that it can be easily disassembled.

【0010】[0010]

【作用】次ぎに、本発明の電解凝集装置について以下実
施例を詳しく説明する。
Next, the electrolytic coagulation apparatus of the present invention will be described in detail with reference to the following examples.

【0011】図中1は液槽中に、両極の素材としてアル
ミニュウムを用い、それぞれ円筒に成形、設置した交流
電解凝集装置の構成を示す斜視断面図である。
Reference numeral 1 in the drawing is a perspective sectional view showing the structure of an AC electrolytic aggregating apparatus in which aluminum is used as a material for the both electrodes in a liquid tank, each of which is molded and installed in a cylinder.

【0012】そして、この図1において、液槽1は、絶
縁体である塩ビ管を輪切りにし、底の絶縁板2も塩ビ板
を溶接し構成している。アルミニュウム電極外円筒3と
アルミニュウム電極内円筒4を電極とした。そして、ア
ルミニュウム電極外円筒3の下部には、補給液開口5を
有する絶縁環6を設け、液槽1の底を構成する絶縁板2
の上に載せている内径一杯のアルミ底板電極7と絶縁し
ている。一方、アルミニュウム電極内円筒4には、アル
ミ底板電極7に全面接触し、絶縁環6の内径に嵌合され
る肉厚、導電体のフランジ8を設け、図示していないボ
ルトなどでアルミ底板電極7に固定してある。アルミニ
ュウム電極内円筒4全周には循環開口9を多数設け、ア
ルミニュウム電極内円筒4内の液をアルミニュウム電極
外円筒3内側へ循環容易としている。液槽1の外周部に
は、図示していない他の装置などからの原液入口10,
浄化液排出口11,更に凝集浮上したスカム12のスカ
ム排出口13を設けている。架台14は設置面との電気
的絶縁を画するためと高さ決めを行うものである。
In FIG. 1, the liquid tank 1 is constructed by cutting a PVC pipe, which is an insulator, into slices, and also by welding a PVC plate to the insulating plate 2 at the bottom. The outer cylinder 3 of the aluminum electrode and the inner cylinder 4 of the aluminum electrode were used as electrodes. An insulating ring 6 having a replenishing liquid opening 5 is provided below the aluminum electrode outer cylinder 3 to form an insulating plate 2 that constitutes the bottom of the liquid tank 1.
It is insulated from the aluminum bottom plate electrode 7 having a full inner diameter placed on top. On the other hand, the inner cylinder 4 of the aluminum electrode is provided with a flange 8 of a conductor, which has a wall thickness that is in full contact with the aluminum bottom plate electrode 7 and is fitted into the inner diameter of the insulating ring 6, and is connected to the aluminum bottom plate electrode with a bolt or the like not shown. It is fixed at 7. A large number of circulation openings 9 are provided on the entire circumference of the aluminum electrode inner cylinder 4 to facilitate circulation of the liquid in the aluminum electrode inner cylinder 4 to the inside of the aluminum electrode outer cylinder 3. At the outer peripheral portion of the liquid tank 1, a stock solution inlet 10 from another device (not shown),
The cleaning liquid discharge port 11 and the scum discharge port 13 of the scum 12 that has flocculated and floated are provided. The gantry 14 is for height determination in order to define electrical insulation from the installation surface.

【0013】次ぎにこの装置での凝集原理を図2の模式
図を使って説明すれば、アルミ底板電極7に交流電源の
一端を接続すれば、これに接触取り付けられているアル
ミニュウム電極内円筒4は、フランジ8を介して、導通
極15となる。外側のアルミニュウム電極外円筒3に
は、液面16の外部から別極17を接続している。図示
していないコロイド成分,懸濁成分などが分散している
液中で、通電し、電解すると、アルミニュウム電極円筒
3、4、アルミ底電極7、フランジ8から、強酸性状態
では3価の単純イオン(Al 3+)18a、pHが4〜
5付近では水中の水酸イオン(OH−)と結合し、正荷
電の溶解性ポリマーイオン〔Al 8(OH)4+/20〕18
bが発生し、通常負荷電のコロイド,懸濁成分の荷電を
中和する作用を生じる。結果、微粒子は相互にファン・
デア・ヴァールスの力により結合することが可能とな
る。また更に、アルミニュウム,鉄などの水酸化物はフ
ァン・デア・ヴァールスによる結合を一層高める架橋作
用を有しており、効果的な素材である。更に、通電によ
って、直接対峙する両極表面から水素ガス,酸素ガスの
微細気泡は底側からの上昇流となり、フロックを浮上せ
しめるばかりでなく、凝集粒子相互の衝突をくり返えさ
せて、集塊を大幅に進行させる複合の効果を生む。
Next, the agglomeration principle of this apparatus will be described with reference to the schematic view of FIG. 2. If one end of an AC power source is connected to the aluminum bottom plate electrode 7, the aluminum electrode inner cylinder 4 which is attached in contact with this is connected. Becomes a conducting electrode 15 via the flange 8. Another electrode 17 is connected to the outer aluminum electrode outer cylinder 3 from outside the liquid surface 16. When electrolyzing and electrolyzing in a liquid in which colloidal components, suspension components, and the like (not shown) are dispersed, the aluminum electrode cylinders 3, 4, the aluminum bottom electrode 7, and the flange 8 cause simple trivalent in a strongly acidic state. Ion (Al 3+) 18a, pH 4 ~
In the vicinity of 5, it binds to hydroxide ion (OH-) in water and is a positively charged soluble polymer ion [Al8 (OH) 4 + / 20] 18.
b is generated, which normally has the effect of neutralizing the charge of the negatively charged colloid and the suspension component. As a result, the particles are
It becomes possible to combine by the power of Der Vars. Furthermore, hydroxides such as aluminum and iron have a cross-linking action to further enhance the bond by van der Waals, and are effective materials. Furthermore, by energizing, the minute bubbles of hydrogen gas and oxygen gas from the oppositely facing surfaces of the electrodes become an upward flow from the bottom side, not only floating the flocs, but also causing repeated agglomeration of the agglomerated particles to agglomerate. Produces a complex effect that significantly advances.

【0014】図2中での交流電解凝集の原理を詳述すれ
ば、陰,陽の切り変わる一瞬の、アルミニュウム電極外
円筒3がマイナス、アルミニュウム電極内円筒4がプラ
ス極であると想定したものであり、電解によってアルミ
ニュウムの正電荷多価イオン(Al 3+)18aまたは
ポリマーイオン〔Al 8(OH)4+/20〕18bが生じ、
図示していない分散粒子を荷電中和、同時に極表面から
発生している水素ガス19、酸素ガス20の上昇につ
れ、表面電位が等電点付近となった粒子はフロック化と
集塊を重ねながら浮上し、スカム12となる。つれて、
補給液開口5からは外部の新しい原液が導入され、同じ
工程を踏むことになる。図示実施例では、アルミニュウ
ム電極外円筒3は120mm口径、アルミニュウム電極
内円筒4は100mm口径の円筒とし、アルミニュウム
電極内円筒4内の液の滞留を防ぐため、アルミニュウム
電極内円筒4にはパンチングにより、無数の3mm口径
の循環開口9を設けている。尚、電解装置が大型化し、
ガス発生量が多くなると爆発の危険が出て来るので、危
険点以下の濃度となるよう多量の空気で薄め、ダクトに
より室外へ、完全に放出する必要がある。実際の交流電
解においては、試料の電解度によって電流値が変わって
くるが、試験に於いては電圧値は試料による成り行きと
したが、電流値は10A/dm2を越えない範囲とし
た。水系洗浄機に使用されている一般的洗浄剤とコロイ
ド成分が入った廃却液では、電解度が高いため、上限一
杯の電流を流すことが出来、両電極の対峙面から液面が
盛り上がる程の水素気泡が発生し、数秒後には、ミリ単
位で集塊したスカムが次々に急上昇して、水面に浮かぶ
のが確認出来た。その間気泡中で攪拌されるフロックも
無数に確認された。
Explaining in detail the principle of AC electrolytic aggregation in FIG. 2, it is assumed that the outer cylinder 3 of the aluminum electrode is the negative pole and the inner cylinder 4 of the aluminum electrode is the positive pole in a moment when the positive and negative transitions occur. And electrolysis produces positively charged multiply charged ions of aluminum (Al 3+) 18a or polymer ions [Al 8 (OH) 4 + / 20] 18b,
Charge neutralization of dispersed particles (not shown), and at the same time, as the hydrogen gas 19 and oxygen gas 20 generated from the pole surface rise, the particles whose surface potential is near the isoelectric point flock and aggregate. Surfaced and became scum 12. Hang up,
A fresh new stock solution is introduced from the replenisher opening 5, and the same steps are performed. In the illustrated embodiment, the aluminum electrode outer cylinder 3 has a diameter of 120 mm, and the aluminum electrode inner cylinder 4 has a diameter of 100 mm. An infinite number of circulation openings 9 having a diameter of 3 mm are provided. In addition, the size of the electrolyzer becomes larger,
If the amount of gas generated increases, there is a danger of explosion. Therefore, it is necessary to dilute the gas with a large amount of air so that the concentration is below the danger point, and to completely discharge it to the outside with a duct. In the actual AC electrolysis, the current value changes depending on the degree of electrolysis of the sample. In the test, the voltage value was determined by the sample, but the current value was within the range of 10 A / dm 2 . The waste liquid containing the common cleaning agent and colloidal components used in water-based cleaners has a high degree of electrolysis, so the maximum current can be passed, and the liquid level rises from the confronting surface of both electrodes. After several seconds, hydrogen bubbles were generated, and after a few seconds, it was confirmed that scum aggregated in millimeters suddenly soared and floated on the water surface. During that time, countless flocs were also confirmed which were stirred in the bubbles.

【0015】図3は両極にアルミニュウム平板21、2
2を用い、下部には液の通路となる空隙を設け、上部に
はスカムをオーバーフローさせるよう両極をハウジング
23と同位置の高さに並べることを特徴として構成した
ものである。
FIG. 3 shows aluminum plates 21 and 2 on both electrodes.
No. 2 is used, and a gap serving as a passage for the liquid is provided in the lower portion, and both electrodes are arranged at the same height as the housing 23 so as to overflow the scum in the upper portion.

【0016】次ぎに図1の実施例によって、製鋼所での
洗浄廃液を実際に交流電解凝集を行った後、ポリプロピ
レンの1ミリ厚の濾過布を2枚重ねによって濾過の後、
BOD,CODをそれぞれ、JIS KO102の2
1、JIS KO102の17により分析を行った。表
1は、当実施例によるものであり、参考に掲げた表2の
同じ液の直流による処理の結果と比し、かなり数値が低
くなっているものの、実用に耐えるものと判断される。
Next, according to the embodiment shown in FIG. 1, the washing waste liquid in the steel mill was actually subjected to AC electrolytic coagulation, and after being filtered with two 1 mm thick polypropylene filter cloths,
BOD and COD are 2 of JIS KO102 respectively
1. The analysis was carried out according to JIS KO102-17. Table 1 is based on this example, and is considerably lower than the result of the direct current treatment of the same liquid in Table 2 given as a reference, but it is judged to be practical.

【0017】[0017]

【表1】 [Table 1]

【0018】[0018]

【表2】 [Table 2]

【0019】[0019]

【発明の効果】上述のように、本発明による時には、物
理的、化学的に安定且つ導電性を有する導電性を有し、
電解時に正荷電の多価イオンを生じる素材によって構成
し、電解によって、正荷電のイオンを発生させ、負荷電
のコロイド,懸濁成分などを荷電中和し、分散する粒子
をファン・デア・ヴァールスの力によって凝集させるこ
とが出来る実益を有する。
As described above, according to the present invention, it has a physically and chemically stable and electrically conductive property.
It is composed of a material that produces positively charged multiply charged ions during electrolysis. By electrolysis, positively charged ions are generated to neutralize the negatively charged colloids and suspension components, and disperse particles into van der vars. Has the practical benefit of being able to aggregate by the force of.

【0020】また、本発明による時には、両極材にアル
ミニュウム,鉄,銅,亜鉛などを用いることにより、正
荷電の水酸化物ポリマー多価イオンを発生させ、負荷電
の粒子の荷電中和を有効に作用させることが出来る実益
を有する。
Further, according to the present invention, by using aluminum, iron, copper, zinc or the like as the bipolar material, positively charged hydroxide polymer polyvalent ions are generated to effectively neutralize the charge of the negatively charged particles. Have the real benefit of being able to act on.

【0021】更にまた、本発明による時には、両極にア
ルミニュウム,鉄など、電解時に荷電中和と架橋作用を
同時に可能とする素材により構成することによって、フ
ァン・デア・ヴァールスの結合を補強し、フロック化を
促進することが出来る実益を有する。
Furthermore, according to the present invention, both electrodes are made of a material capable of simultaneously performing charge neutralization and cross-linking during electrolysis, such as aluminum and iron, to reinforce the van der Waals coupling, and to block flocs. There is a real benefit that can promote

【0022】更にまた、本発明による時には、両極が相
互に直接対峙する表面からの水素,酸素の微細気泡の強
い浮上力によって、マイクロフロックを攪拌し、集塊を
促進することが出来る実益を有する。
Furthermore, according to the present invention, the strong floating force of the fine bubbles of hydrogen and oxygen from the surface where the two electrodes directly face each other can stir the microflocs and promote the agglomeration. .

【0023】更にまた、本発明による時には、外円筒電
極の下部に開口部を設け、浮上流によって補給原液を誘
導容易とし、液槽全体の対流を可能とした実益を有す
る。
Furthermore, according to the present invention, an opening is provided in the lower portion of the outer cylindrical electrode, and the replenishing stock solution can be easily guided by the floating upstream, so that convection of the entire liquid tank is possible.

【0024】内円筒電極に内側の液の循環開口を多数設
けることにより、内筒側液も円滑に凝集することが出来
る実益を有する。
By providing the inner cylindrical electrode with a large number of circulation openings for the inner liquid, the inner cylinder side liquid can be condensed smoothly.

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

【図1】本発明の電解凝集装置を説明する一部断面を含
む斜視断面図である。
FIG. 1 is a perspective cross-sectional view including a partial cross-section for explaining an electrolytic aggregating apparatus of the present invention.

【図2】本発明の凝集、集塊を説明する模式断面図であ
る。
FIG. 2 is a schematic cross-sectional view illustrating aggregation and agglomeration of the present invention.

【図3】陰極、陽極をそれぞれ平板を用いた実施例を示
す一部断面図を含む斜視図である。
FIG. 3 is a perspective view including a partial cross-sectional view showing an embodiment using a flat plate for each of a cathode and an anode.

【符号の説明】[Explanation of symbols]

1. 液槽 2. 絶縁板 3. アルミニュウム内電極円筒 4. アルミニュウム外電極円筒 5. 補給液開口 6. 絶縁環 7. アルミ底板電極 8. フランジ 9. 循環開口 10. 原液入口 11. 浄化液排出口 12. スカム 13. スカム排出口 14. 架台 15. 導通極 16. 液面 17. 別極 18a,18b 正荷電のイオン 19. 水素ガス 20. 酸素ガス 21.22 アルミニュウム平板 23. ハウジング 1. Liquid tank 2. Insulation plate 3. Aluminum inner electrode cylinder 4. Aluminum outer electrode cylinder 5. Replenisher opening 6. Insulation ring 7. Aluminum bottom plate electrode 8. Flange 9. Circulation opening 10. Stock solution inlet 11. Purification liquid outlet 12. Scum 13. Scum outlet 14. Stand 15. Conducting electrode 16. Liquid level 17. Separate poles 18a, 18b Positively charged ions 19. Hydrogen gas 20. Oxygen gas 21.22 Aluminum flat plate 23. housing

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】電解時に、正荷電のイオン,溶解性ポリマ
ーイオンを生成し、液中に分散する負荷電のコロイド,
懸濁成分を荷電中和し、同時に生成される水酸化物によ
って架橋,凝集,集塊を可能とするアルミニュウム,鉄
などを電極とし、交流を通電することによっても、コロ
イド,懸濁成分を凝集させ、固液分離を容易としたこと
を特徴とする交流電解凝集装置。
1. A negatively charged colloid that produces positively charged ions and soluble polymer ions during electrolysis and disperses in a liquid,
Aluminium, iron, etc., which can neutralize the suspension components by charge and crosslink, aggregate, and agglomerate by the hydroxide produced at the same time, are used as electrodes, and the colloid and suspension components are also aggregated by applying an alternating current. An AC electrolysis flocculation device characterized by facilitating solid-liquid separation.
【請求項2】両電極を同一素材により形成したことを特
徴とする請求項1の交流電解凝集装置。
2. The AC electrolytic aggregating apparatus according to claim 1, wherein both electrodes are formed of the same material.
JP16400793A 1993-06-08 1993-06-08 Alternative current electrolytic flocculation apparatus Pending JPH06343971A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16400793A JPH06343971A (en) 1993-06-08 1993-06-08 Alternative current electrolytic flocculation apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16400793A JPH06343971A (en) 1993-06-08 1993-06-08 Alternative current electrolytic flocculation apparatus

Publications (1)

Publication Number Publication Date
JPH06343971A true JPH06343971A (en) 1994-12-20

Family

ID=15784999

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16400793A Pending JPH06343971A (en) 1993-06-08 1993-06-08 Alternative current electrolytic flocculation apparatus

Country Status (1)

Country Link
JP (1) JPH06343971A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102010034A (en) * 2010-12-21 2011-04-13 北京碧水源膜科技有限公司 Preparation device of ferron used for water treatment and application method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102010034A (en) * 2010-12-21 2011-04-13 北京碧水源膜科技有限公司 Preparation device of ferron used for water treatment and application method thereof

Similar Documents

Publication Publication Date Title
US4031006A (en) Vortex coagulation means and method for wastewater clarification
US6663766B1 (en) Electroflocculation process and apparatus
GB1560737A (en) Precipitation
US4149953A (en) Apparatus for removing impurities from waste water
US4123345A (en) Liquid treating apparatus
CN208471632U (en) A kind of turbulent flow electric flocculation device
CN107324458B (en) Electric flocculation pretreatment device and method for fracturing flowback fluid
JPH06328081A (en) Multicylindrical electrode electrolytic cohesion device
JPH06304569A (en) Electrolytic flocculation device
Shin et al. Performance evaluation of electrocoagulation and electrodewatering system for reduction of water content in sewage sludge
Sen et al. Efficient treatment of textile dyeing effluent by electrocoagulation process using aluminium electrode
JPH06343971A (en) Alternative current electrolytic flocculation apparatus
JPH06343970A (en) Electrolytic flocculation apparatus provided with blast discharging tool for scum and gas
JPH06343972A (en) Electrolytic ion flocculation apparatus
JPH06328080A (en) Electrolytic ion cohesion device
JP2017035686A (en) Waste water processing method
Ebrahiem et al. Novel Electrode Design for Removing CNG Lubricant from Wastewater by Using Electrocoagulation
CN109437451A (en) It is a kind of for oil-containing and surface active agent wastewater can reuse equipment and technique
FI95234C (en) Method and apparatus for purifying aqueous solutions or the like
JPH078963A (en) Fluocculation and separation apparatus
US4053386A (en) Electrolytic filter for electrolytically filtering and recovering metals from colloidal suspensions
KR19990001036A (en) Apparatus and method for treating oil and heavy metals in wastewater
SU1006384A1 (en) Method for electrolytically purifying effluents
CN216404051U (en) Condensate water treatment system
JPH0686984A (en) Electrode structure of waste water treatment device