JPH06328080A - Electrolytic ion cohesion device - Google Patents

Electrolytic ion cohesion device

Info

Publication number
JPH06328080A
JPH06328080A JP14706693A JP14706693A JPH06328080A JP H06328080 A JPH06328080 A JP H06328080A JP 14706693 A JP14706693 A JP 14706693A JP 14706693 A JP14706693 A JP 14706693A JP H06328080 A JPH06328080 A JP H06328080A
Authority
JP
Japan
Prior art keywords
anode
cathode
aluminum
electrolytic ion
iron
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
JP14706693A
Other languages
Japanese (ja)
Inventor
Shigeo Tochikubo
滋夫 栃窪
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 JP14706693A priority Critical patent/JPH06328080A/en
Publication of JPH06328080A publication Critical patent/JPH06328080A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To separate and remove accurately even by means of a simple filter adsorption material by performing charged neutralizing colloidal particles and suspension particles dispersed in electrolyte by means of eluted ions from an anode, carrying out the cohesion of irons by the crosslinking action of an insoluble hydroxide an the van der Walls force and agitating and agglomerating ions by means of floating flow of gaseous foams. CONSTITUTION:Cathode cylinders 3 and anode cylinders 4 are set on an insulated ring 6 with a replenishing liquid opening 5 in a liquid tank 1. Therefore, the cohesion of fine particles in service water, sewage and cutting liquid and washing liquid for a machine tool is carried out to make the filter 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、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、酸素気泡による撹拌力及び荷電中和と時により架
橋作用を果たす陽極からのイオン、不溶性水酸化物によ
り凝集、集塊し、浮上もしくは沈殿させ、濾過、吸着分
離を容易とした電解イオン凝集装置に関するものであ
る。
BACKGROUND OF THE INVENTION The present invention relates to a suspension contained in tap water, sewage, etc., a colloid component, an oil component in an aqueous cleaning liquid, sludge, an emulsified oil in a water-soluble cutting fluid, fine particles, etc. , Hydrogen generated by electrolysis of impurities that cause troubles, agitation force by oxygen bubbles and ions from the anode that perform charge neutralization and sometimes cross-linking action, and aggregate, agglomerate, float or precipitate by insoluble hydroxide, The present invention relates to an electrolytic ion aggregating apparatus that facilitates filtration and adsorption separation.

【0002】[0002]

【従来の技術】従来、上下水道での固液分離には、広大
な施設面積と処理時間を要し、問題が多った。また、水
系洗浄液中に乳化、懸濁した油分、コロイド成分を有効
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”と称される乳化液を含む切削
液の廃液から切削油を分離除去し、水分だけをそのま
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、懸濁するコロイド、懸濁成分を効果
的、速効的に分離除去、水の排出を可能とするものはな
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 processing time. In addition, there is no simple means for effectively removing oil and colloidal components that have been emulsified and suspended in an aqueous cleaning liquid and can be circulated for use. Further, there is no means for separating and removing cutting oil from the waste liquid of cutting liquid containing an emulsified liquid, commonly called "emulsion", and discharging only water as it is. Furthermore, it is possible to effectively and quickly separate and remove the white turbidity, oil that becomes an emulsion, oil that diffuses, suspends colloids, and suspended components that are mixed in the cleaning liquid used in the water-based cleaning machine, and discharge water. There was nothing.

【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 absorption property such as polypropylene and polyethylene, and disperses the oil film on the liquid surface and the emulsified oil component. It was proposed to remove and separate the fine particles that are present. However, unlike the coarse suspension, the oil and particles finely divided into the colloidal region were not able to be filtered and adsorbed as they were.

【0004】[0004]

【発明が解決しようとする課題】即ち、本発明の電解イ
オン凝集装置は、洗浄機などの液槽内に、陰極、陽極と
もに同一素材の、電解時には陽極側からは陽イオンを生
じ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、陰極からの水
素、陽極からの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 electrolytic ion aggregating apparatus of the present invention uses the same material for both the cathode and the anode in a liquid tank such as a washing machine, but a material that produces cations from the anode side during electrolysis. By providing an electrolytic tool configured as described above, the negatively charged colloidal components dispersed in the electrolyte solution are neutralized by the positively charged ions from the anode, enabling aggregation and flocking by the force of Van der Waals. By generating floating convection in the entire liquid tank by hydrogen bubbles from the cathode and oxygen bubbles from the anode, for example, micro flocs of several tens of microns collide with each other, agglomerate to several hundreds of microns or more, simple filtration, adsorption Also, the feature is that solid-liquid separation can be performed with high accuracy.

【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汚濁液槽中に、電解通電
時に、陽極となった側からは正荷電のイオンを発生する
同一の素材により両極を構成し、電解質液中の除去すべ
き、コロイド成分、懸濁成分の負の荷電を荷電中和し、
ファン・デア・ヴァールス力により結合せしめ、フロッ
ク成形することが出来るようにした電解イオン凝集装置
を提供するものである。
According to the present invention, the same material that generates positively charged ions from the side that has become the anode during electrolysis in a pollutant tank incorporated in equipment such as clean water, sewage treatment, washing machines and systems, is installed. Both electrodes are constituted by, and the negative charges of the colloid component and the suspension component to be removed in the electrolyte solution are neutralized by charge,
It is intended to provide an electrolytic ion aggregating device which can be coupled by a van der Waals force so as to form a floc.

【0006】本発明の他の目的とするところは、陽極、
陰極ともにアルミニュウム、鉄、銅、亜鉛などを用い、
荷電中和に最も有効に働く、陽極からの正荷電の水酸化
物ポリマー多価イオンを得ることが出来る電解イオン凝
集装置を提供するものである。
Another object of the present invention is to provide an anode,
Aluminum, iron, copper, zinc, etc. are used for the cathode,
It is intended to provide an electrolytic ion aggregating device which can obtain positively charged hydroxide polymer polyvalent ions from an anode, which works most effectively for charge neutralization.

【0007】また、本発明の他の目的とするところは、
陽極、陰極にアルミニュウム、鉄など陽イオン、水酸化
物による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イオン凝
集装置を提供するものである。
Another object of the present invention is to:
Provided is an electrolytic ion aggregating apparatus capable of reinforcing floc formation by using a material having a crosslinking action at the same time as charge neutralization by cations and hydroxides such as aluminum and iron for the anode and the cathode.

【0008】更にまた、本発明の他の目的とするところ
は、陽極及び陰極をアルミニュウム、鉄などの荷電中和
力を持つイオンを生じる素材により構成し、陽極、陰極
とを適宜の時間毎に切換え、陽極側で溶出により摩滅す
る量を平均化し、交換までの時間の延長を計ることが出
来る電解イオン凝集装置を提供するものである。
Still another object of the present invention is that the anode and the cathode are made of a material that produces ions having a charge neutralizing power such as aluminum and iron, and the anode and the cathode are provided at appropriate intervals. It is intended to provide an electrolytic ion aggregating apparatus capable of averaging the amount of abrasion due to elution on the side of switching and on the anode side and prolonging the time until exchange.

【0009】更にまた、本発明の他の目的とするところ
は、陽極にアルミニュウム、鉄など、電解時に生じる不
溶性の水酸化物により架橋し、凝集を堅固とし、更にフ
ロックを大きくし、濾過吸着を容易とすることが出来る
電解イオン凝集装置を提供するものである。
Still another object of the present invention is to crosslink the anode with an insoluble hydroxide such as aluminum or iron produced during electrolysis to make the agglomerates firm, further increase the flocs, and filter and adsorb. It is intended to provide an electrolytic ion aggregating device that can be easily made.

【0010】更にまた、本発明の他の目的とするところ
は、陽極、陰極にアルミニュウム、鉄などの同一の素材
を用い、適宜の時間毎に電極を切替えることにより、陽
極となった側は、陽イオンを発生し、陰極となった側
は、発生する水素ガスにより表面を洗浄し、常に表面を
清浄とすることが出来る電解イオン凝集装置を提供する
ものである。
Still another object of the present invention is to use the same material such as aluminum and iron for the anode and the cathode, and switch the electrodes at an appropriate time so that the anode side is The electrolytic ion aggregating apparatus is capable of generating positive ions and acting as a cathode by cleaning the surface with the generated hydrogen gas to constantly clean the surface.

【0011】更にまた、本発明の他の目的とするところ
は、アルミニュウム、鉄などの同一素材による陰極、陽
極を円筒に形成することにより、円筒状間隙に水素、酸
素気泡の上昇流を形成、粒子のフロック化を促進する撹
拌力とすることが出来る電解イオン凝集装置を提供する
ものである。
Still another object of the present invention is to form a cathode and an anode made of the same material such as aluminum and iron in a cylinder to form an upward flow of hydrogen and oxygen bubbles in the cylindrical gap. It is intended to provide an electrolytic ion aggregating apparatus capable of using a stirring force that promotes flocculation of particles.

【0012】更にまた、本発明の他の目的とするところ
は、円筒状に成形したアルミニュウム、鉄などの陰極、
陽極の円周表面に複数の開口を設け、対流を容易にする
ことが出来る電解イオン凝集装置を提供するものであ
る。
Still another object of the present invention is to provide a cathode made of aluminum, iron or the like formed into a cylindrical shape,
It is intended to provide an electrolytic ion aggregating device capable of facilitating convection by providing a plurality of openings on the circumferential surface of an anode.

【0013】[0013]

【課題を解決するための手段】即ち、本発明の電解イオ
ン凝集装置は、コロイド、懸濁径の粒子、油分が分散存
在する液槽中に、導電性の同一の素材で陰極、陽極を構
成し、通電時に陽極から正荷電のイオンと不溶性の水酸
化物を発生させ、分散成分の荷電中和を行い、凝集と架
橋と同時に行うことが出来るように構成、凝集、集塊に
より、容易に分離可能としたことを特徴として構成した
ものである。
That is, the electrolytic ion aggregating apparatus of the present invention comprises a cathode and an anode made of the same conductive material in a liquid tank in which colloid, particles having a suspension diameter, and oil are dispersed. However, when electricity is applied, positively charged ions and insoluble hydroxide are generated from the anode to neutralize the charge of the dispersion component, and the structure can be carried out simultaneously with aggregation and crosslinking. It is characterized by being separable.

【0014】[0014]

【作用】次ぎに、本発明の電解イオン凝集装置について
以下実施例を詳しく説明する。
Next, the electrolytic ion aggregating apparatus of the present invention will be described in detail in the following examples.

【0015】図1は液槽中に、陰極、陽極素材としてア
ルミニュウムを用い、それぞれ円筒に成形、設置した電
解イオン凝集装置の構成を示す斜視断面図である。
FIG. 1 is a perspective sectional view showing the structure of an electrolytic ion aggregating apparatus in which aluminum is used as a cathode and an anode material in a liquid tank, each of which is molded and installed in a cylinder.

【0016】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。陰極3と陽極4を円筒に成形そ
れぞれの電極とした。そして、陰極円筒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、陽極円筒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。陽極円筒4全周には
循環開口9を多数設け、陽極円筒4内の液を陰極円筒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 by welding a PVC plate to the insulating plate 2 at the bottom. The cathode 3 and the anode 4 were formed into a cylinder and used as respective electrodes. And, in the lower part of the cathode cylinder 3,
An insulating ring 6 having a replenishing liquid opening 5 is provided to insulate the aluminum bottom plate electrode 7 having a full inner diameter placed on the insulating plate 2 forming the bottom of the liquid tank 1. On the other hand, the anode cylinder 4 is provided with a thick flange 8 that comes into full contact with the aluminum bottom plate electrode 7 and fits into the inner diameter of the insulating ring 6, and is fixed to the aluminum bottom plate electrode 7 with a bolt or the like not shown. is there. A large number of circulation openings 9 are provided on the entire circumference of the anode cylinder 4 so that the liquid in the anode cylinder 4 can be supplied to the cathode cylinder 3
Easy to circulate inward. On the outer peripheral portion of the liquid tank 1, there are provided a raw liquid inlet 10 from another device (not shown), a purified liquid outlet 11, and a scum outlet 13 of a scum 12 that has flocculated and floated. The gantry 14 is for height determination in order to define electrical insulation from the installation surface.

【0017】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にプラス側1
5を接続すれば、これに接触取り付けられている陽極円
筒4は、フランジ8を介して、プラス極15となる。外
側の陰極円筒3には、液面16の外部からマイナス極1
7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、
陽極円筒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基(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、鉄などは不溶性の水酸
化物を生じ、荷電中和と同時にファン・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
極表面から発生する陰極側の水素ガス、陽極側の酸素ガ
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 principle of agglomeration in this apparatus will be described with reference to the schematic diagram of FIG.
When 5 is connected, the anode cylinder 4 attached in contact with it becomes a positive electrode 15 via the flange 8. The outer cathode cylinder 3 has a negative electrode 1 from the outside of the liquid surface 16.
7 is connected. When electricity is applied and electrolysis is performed in a liquid in which colloidal components, suspension components, etc. (not shown) are dispersed,
From the anode cylinder 4, the aluminum bottom electrode 7, and the flange 8, they are bonded to a trivalent simple ion (Al 3+) 18a in a strongly acidic state and a hydroxyl group (OH −) in water at a pH of about 4 to 5 and are positively charged. Soluble polymer ion [Al 8 (OH) 4 + / 20] 18
b is generated, and usually has a function 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, aluminum, iron, and the like form insoluble hydroxides, have a cross-linking action that further enhances binding by van der Waals at the same time as charge neutralization, and is an effective material. Furthermore, by energizing, the minute bubbles of hydrogen gas on the cathode side and oxygen gas on the anode side generated from the surfaces of the opposite electrodes directly facing each other become an upward flow from the bottom side, not only making the flocs levitate but also causing mutual collision of agglomerated particles. Repeatedly creates a complex effect that greatly advances the agglomeration.

【0018】図2中での電解凝集の原理を詳述すれば、
電解によってアルミニュウムの正荷電多価イオン(Al
3+)18aまたはポリマーイオン〔Al 8(OH)4+/2
0〕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
粒子はフロック化し、同時に生じる不溶性の水酸化アル
ミニュウムにより架橋され、結合を強固とし、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、陰極円筒3は120mm
径、陽極円筒4は100mm径の円筒とし、陽極円筒4内
の液の滞留を防ぐため、陽極円筒4にはパンチングによ
り、無数の3mm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、試験に於いては直流30Vの定電
圧とし、電流値は試料による成り行きとしたが、安全性
を考慮し、電流密度は、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、陰極円筒3の内壁から液
面が盛り上がる程の水素気泡が発生し、数秒後には、陽
極円筒4の外周面の酸素気泡中に、突然、ミリ単位で集
塊したスカムが次々に急浮上して、水面に浮かぶのが確
認出来た。その間、陰極側では、水素気泡中で撹拌され
るフロックも無数に確認することが出来た。
The principle of electrolytic aggregation in FIG. 2 will be described in detail.
Positively charged multiply charged ions of aluminum (Al
3+) 18a or polymer ion [Al 8 (OH) 4 + / 2
[0] 18b occurs, the dispersed particles (not shown) are charge-neutralized, and at the same time, as the hydrogen gas 19 and the oxygen gas 20 generated from the polar surface rise, the particles whose surface potential is near the isoelectric point are flocculated. At the same time, the scum 12 is crosslinked by insoluble aluminum hydroxide that is generated simultaneously, strengthens the bond, and floats while stacking the agglomerates. As a result, a new stock solution from the outside is introduced from the replenisher opening 5, and the same steps are performed. In the illustrated embodiment, the cathode cylinder 3 is 120 mm
The diameter and the anode cylinder 4 are 100 mm in diameter, and in order to prevent the retention of the liquid in the anode cylinder 4, the anode cylinder 4 is provided with innumerable circulation openings 9 having a diameter of 3 mm by punching. It should be noted that, since the size of the electrolyzer becomes large and the amount of gas generated increases, there is a danger of explosion. Therefore, it is necessary to dilute with a large amount of air so that the concentration is below the dangerous point, and to completely discharge it to the outside by a duct. In the actual electrolysis, the current value changes depending on the degree of electrolysis of the sample. In the test, a constant voltage of 30 V DC was used, and the current value was decided depending on the sample. The range was set so as not to exceed 10 A / dm 2 . In the waste liquid containing the general cleaning agent and colloidal components used in the water-based cleaning machine, since the electrolysis is high, the upper limit of current can be passed, and the liquid level rises from the inner wall of the cathode cylinder 3. It was confirmed that, after a few seconds, the hydrogen bubbles were generated, and after a few seconds, the scum agglomerated in millimeters suddenly suddenly floated in the oxygen bubbles on the outer peripheral surface of the anode cylinder 4 and floated on the water surface. During that time, on the cathode side, countless flocs stirred in hydrogen bubbles could be confirmed.

【0019】図3は陰極平板21、陽極平板22、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 is characterized in that a cathode flat plate 21, an anode flat plate 22 and a gap serving as a liquid passage are provided in the lower portion, and both electrodes are arranged at the same height as the housing 23 so that the scum overflows in the upper portion. It is composed.

【0020】表1は、図1の実施例によって実際に電解
イオン凝集を行った後、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、油分についてのノル
マルヘキサン法によって分析した結果である。試料中に
は相当量の界面活性剤を含有され、油分はエマルジョン
化し時間経過後も沈降、浮上せず、本来、機械的操作だ
けでは、分離除去が困難であったものであり、正荷電の
イオンと不水溶性の水酸化物の発生を利用する電解イオ
ン凝集法により、極めて高い精度で目的を達成し得たこ
とを確認した。
Table 1 shows the results obtained by actually electrolytically aggregating ions according to the embodiment shown in FIG. 1, and then filtering two 1 mm-thick polypropylene filter cloths by superposition, and then analyzing the oil content by the normal hexane method. Is. The sample contained a considerable amount of surfactant, and the oil did not emulsify and did not settle or float even after a lapse of time. Originally, it was difficult to separate and remove by mechanical operation alone. It was confirmed that the objective could be achieved with extremely high accuracy by the electrolytic ion agglutination method utilizing the generation of ions and water-insoluble hydroxide.

【0021】[0021]

【表1】 [Table 1]

【0022】[0022]

【発明の効果】上述のように、本発明による時には導電
性を有し、電解時に正荷電のイオンを生じる同一の素材
によって、陽極、陰極を構成し、電解によって、陽極に
は、正荷電のイオンを発生させ、負の電荷を持ったコロ
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, the anode and the cathode are made of the same material that is electrically conductive and produces positively charged ions during electrolysis, and by electrolysis, the anode is positively charged. It produces ions, neutralizes the charge of negatively charged colloids, suspended components, etc., and aggregates dispersed particles by the force of Van der Waals.

【0023】また、本発明による時には、陽極、陰極材
にアルミニュウム、鉄、銅、亜鉛などを用いることによ
り、陽極からは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最も有効に作用さ
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 for the anode and cathode materials, positively charged hydroxide polymer polyvalent ions are generated from the anode to generate negatively charged particles. It has a practical advantage that charge neutralization can be most effectively operated.

【0024】更にまた、本発明による時には、電解時
の、陽極側の陽イオン、不溶性の水酸化物による荷電中
和と架橋作用を併せ持つ同一素材により陰極、陽極を構
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, the fan-deer is constituted by forming the cathode and the anode from the same material which has both the cation on the anode side during the electrolysis and the charge neutralization by the insoluble hydroxide and the crosslinking action.・ Has the practical benefit of reinforcing the coupling of Vars and promoting flocking.

【0025】更にまた、本発明による時には、陰極、陽
極が相互に直接対峙する表面からの水素、酸素の微細気
泡の強い浮上対流力によって、マイクロフロックを撹拌
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 flotation and convection force of hydrogen and oxygen fine bubbles from the surface where the cathode and the anode directly face each other can stir the microflocs and promote the agglomeration. Have a real benefit.

【0026】更にまた、アルミニュウム、鉄などの荷電
中和を持つイオンを生じる素材により構成し、陰極に
も、陽極と同一のアルミニュウム、鉄などの素材により
構成、陽極、陰極とを適宜の時間毎に切換え、陽極が溶
出することにより摩滅する量を平均化し、交換までの時
間の延長を計ることが出来る実益を有する。
Furthermore, it is made of a material such as aluminum or iron that produces ions having charge neutralization, and the cathode is also made of the same material as the anode, such as aluminum or iron. By switching to, the amount of wear due to elution of the anode is averaged, and the time until replacement can be extended, which is a real benefit.

【0027】更にまた、陽極、陰極にアルミニュウム、
鉄などの同一の素材を用い、適宜の時間毎に電極を切換
えることにより、陽極となった側は、陽イオンを発生
し、陰極となった側は、発生する水素ガスにより表面を
洗浄し、常に表面を清浄に保つことが出来る実益を有す
る。
Further, aluminum is used for the anode and cathode,
By using the same material such as iron and switching the electrodes at appropriate intervals, the side that became the anode generates cations, and the side that became the cathode cleans the surface with the generated hydrogen gas, It has the practical benefit of keeping the surface clean at all times.

【0028】更にまた、本発明による時には陰極下部に
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 part of the cathode to facilitate the introduction of the replenishing stock solution by the floating upstream, and the convection of the entire liquid tank is possible.

【0029】陽極円筒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 a large number of inner liquid circulation openings in the anode cylinder, there is a practical advantage that the inner cylinder side liquid can also be smoothly aggregated.

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

【図1】本発明の電解イオン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 sectional view including a partial section for explaining an electrolytic ion 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、陽極それぞれ平板を用いた実施例を示す
一部断面を含む斜視図である。
FIG. 3 is a perspective view including a partial cross section 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 陰極円筒 4 陽極円筒 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 プラス極 16 液面 17 マイナス極 18a,18b 正荷電のイオン 19 水素ガス 20 酸素ガス 21 陰極平板 22 陽極平板 23 ハウジング 1 Liquid Tank 2 Insulating Plate 3 Cathode Cylinder 4 Anode Cylinder 5 Replenishing Liquid Opening 6 Insulating Ring 7 Aluminum Bottom Plate Electrode 8 Flange 9 Circulating Opening 10 Raw Liquid Inlet 11 Purifying Liquid Discharging Outlet 12 Scum 13 Stand 15 Positive Electrode 16 Liquid Level 17 Negative electrode 18a, 18b Positively charged ions 19 Hydrogen gas 20 Oxygen gas 21 Cathode plate 22 Anode plate 23 Housing

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】導電性を有する同一素材により陽極、陰極
を構成し、電解時に陽極から正荷電のイオンを発生さ
せ、電解質液中に分散する負の電荷を持ったコロイド成
分、また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し、濾過、吸
着を容易としたことを特徴とする電解イオン凝集装置。
1. A colloidal component having a negative charge and a suspension component which are composed of the same conductive material to form an anode and a cathode, generate positively charged ions from the anode during electrolysis, and are dispersed in an electrolyte solution. Electrolytic ion aggregating device characterized in that the particles are electrically neutralized and the dispersed particles are agglomerated by the force of Van der Waals to facilitate filtration and adsorption.
【請求項2】陽極及び陰極をアルミニュウム、鉄などの
荷電中和力を持つイオンを生じる素材により構成し、陽
極、陰極とを適宜の時間毎に切替え、陽極、陰極の溶出
による摩滅量を平均化し、交換までの時間の延長を計る
ことを特徴とする請求項1の電解イオン凝集装置。
2. An anode and a cathode are made of a material such as aluminum and iron that produces ions having a charge neutralizing power, and the anode and the cathode are switched at appropriate time intervals to average the amount of wear due to the elution of the anode and the cathode. The electrolytic ion aggregating apparatus according to claim 1, characterized in that the time until the replacement is extended is measured.
【請求項3】陽極にアルミニュウム、鉄など、電解時に
生じる不溶性の水酸化物により対象粒子を架橋し、凝集
を堅固とし、更にフロックを大きくすることが出来る請
求項1の電解イオン凝集装置。
3. The electrolytic ion aggregating apparatus according to claim 1, wherein the target particles are crosslinked with an insoluble hydroxide such as aluminum or iron generated during electrolysis at the anode to make the agglomeration firm and to increase flocs.
【請求項4】陽極、陰極にアルミニュウム、鉄などの同
一の素材を用い、適宜の時間毎に電極を切替えることに
より、陽極となった側は、陽イオンを発生し、陰極とな
った側は、発生する水素ガスにより表面を洗浄し、常に
清浄に出来ることを特徴とした請求項1の電解イオン凝
集装置。
4. The same material such as aluminum and iron is used for the anode and the cathode, and by switching the electrodes at appropriate times, the side that becomes the anode generates cations and the side that becomes the cathode becomes 2. The electrolytic ion aggregating apparatus according to claim 1, wherein the surface can be always cleaned by cleaning the surface with generated hydrogen gas.
【請求項5】アルミニュウム、鉄などの同一素材による
陰極、陽極を円筒に形成することにより、円筒状間隙に
水素、酸素気泡の上昇流を形成、粒子のフロック化を促
進する撹拌力とすることが出来ることを特徴とする請求
項1の電解イオン凝集装置。
5. An agitating force that promotes flocculation of particles by forming a rising flow of hydrogen and oxygen bubbles in a cylindrical gap by forming a cathode and an anode of the same material such as aluminum and iron into a cylinder. The electrolytic ion aggregating apparatus according to claim 1, characterized in that
【請求項6】円筒状に成形したアルミニュウム、鉄など
の陰極、陽極の円周表面に複数の開口を設け、対流を容
易にしたことを特徴とする請求項1の電解イオン凝集装
置。
6. The electrolytic ion aggregating apparatus according to claim 1, wherein a plurality of openings are provided on the circumferential surfaces of the cathode and the anode made of aluminum, iron or the like formed in a cylindrical shape to facilitate convection.
JP14706693A 1993-05-25 1993-05-25 Electrolytic ion cohesion device Pending JPH06328080A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14706693A JPH06328080A (en) 1993-05-25 1993-05-25 Electrolytic ion cohesion device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14706693A JPH06328080A (en) 1993-05-25 1993-05-25 Electrolytic ion cohesion device

Publications (1)

Publication Number Publication Date
JPH06328080A true JPH06328080A (en) 1994-11-29

Family

ID=15421717

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14706693A Pending JPH06328080A (en) 1993-05-25 1993-05-25 Electrolytic ion cohesion device

Country Status (1)

Country Link
JP (1) JPH06328080A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7253918B2 (en) 2001-06-20 2007-08-07 Fuji Xerox Co., Ltd. Image processing device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7253918B2 (en) 2001-06-20 2007-08-07 Fuji Xerox Co., Ltd. Image processing device

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