JPH06328081A - Multicylindrical electrode electrolytic cohesion device - Google Patents

Multicylindrical electrode electrolytic cohesion device

Info

Publication number
JPH06328081A
JPH06328081A JP14706793A JP14706793A JPH06328081A JP H06328081 A JPH06328081 A JP H06328081A JP 14706793 A JP14706793 A JP 14706793A JP 14706793 A JP14706793 A JP 14706793A JP H06328081 A JPH06328081 A JP H06328081A
Authority
JP
Japan
Prior art keywords
anode
cathode
cylindrical
electrode electrolytic
ions
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
JP14706793A
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 JP14706793A priority Critical patent/JPH06328081A/en
Publication of JPH06328081A publication Critical patent/JPH06328081A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/463Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrocoagulation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46152Electrodes characterised by the shape or form
    • C02F2001/46157Perforated or foraminous electrodes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PURPOSE:To separate and remove accurately even by means of a simple filter adsorption material by performing the charged neutralization of colloid particles and suspension particles dispersed in electrolyte by means of ions, carrying out the cohesion of ions by means of crosslinking action of an insoluble hydroxide and van der Waals force and agglomerating the ions by the agitating force by means of floating flow of oxygen and hydrogen foams. CONSTITUTION:Graphite cathode cylinders 3 of physical and chemical stability and anode cylinders 4a and 4b of aluminum, iron or the like having the charged neutralization and crosslinking action combinedly and generating cations are set on an insulated ring 6 with a replenishing liquid opening 5 in a liquid tank 1. Therefore, the cohesion of fine particles and oil content 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、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,電解による陽イオ
ンの荷電中和と、時により架橋作用を果たす陽極からの
不溶性の水酸化物により凝集,集塊浮上させ、濾過吸着
分離を容易にした多重円筒状電極電解凝集装置に関する
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 liquids, and emulsified oils and fine particles in water-soluble cutting liquids. Impurities that disperse and cause problems are stirred by hydrogen and oxygen bubbles generated by electrolysis, charge neutralization of cations by electrolysis, and sometimes aggregated and agglomerated by insoluble hydroxide from the anode that performs a crosslinking action. The present invention relates to a multi-cylindrical electrode electrolytic aggregating device which is floated and facilitates filtration 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無かった。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 processing time. Also,
There was no simple means to effectively remove the emulsified and suspended oil and sludge in the water-based cleaning liquid and to use them in a circulating manner. Furthermore,
There was no means to separate and remove the cutting oil from the waste fluid of the cutting fluid containing the emulsified liquid, which is commonly called "emulsion", and to discharge only the water as it is. Furthermore, there is no one that can effectively and quickly separate and remove white turbidity, emulsified oil, and sludge that diffuses and suspends by being mixed in a cleaning liquid used in an aqueous washer, 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
は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 or polyethylene, and disperses the oil film on the liquid surface or the emulsified oil component. It was proposed to remove and separate fine particles. However, unlike the coarse suspension, the oil and particles that have been reduced 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、本発明の電解凝
集装置は、洗浄機などの液槽内に、陰極に不溶性の材料
を用い、陽極にはイオン化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により液中に分
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、更に同時に発生する不溶性の
水酸化物の架橋作用により例えば、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,油水分離が出来る特徴を要旨とする。
That is, the electrolytic aggregating apparatus of the present invention is an electrolytic device comprising an insoluble material for the cathode and an ionizable material for the anode in a liquid tank such as a washing machine. Provided, the negatively charged colloidal components dispersed in the liquid are charged and neutralized by positively charged ions from the anode, enabling aggregation and flocculation by the force of Van der Waals, and by hydrogen bubbles from the cathode. By generating floating convection in the entire liquid tank, and by the cross-linking action of insoluble hydroxide that occurs at the same time, micro flocs of several tens of microns collide with each other to agglomerate to several hundreds of microns or more. The feature is that solid-liquid separation and oil-water separation can be performed with high accuracy by filtration and adsorption.

【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、陰極素材は、
物理的,化学的に安定、且つ、導電性を有する素材を、
陽極には導電性を有し、電解通電時に、正荷電のイオン
を発生する素材によりそれぞれ円筒状に構成、陰極を挟
んで内外に二重の陽極を設置、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。
In the present invention, the cathode material is placed in a device such as tap water, sewage treatment, a washing machine, etc.
Material that is physically and chemically stable and has conductivity
The anode has conductivity, and each is made into a cylindrical shape by a material that generates positively charged ions when electrolysis is energized.Double anodes are installed inside and outside with the cathode sandwiched, which should be removed from the electrolyte solution, colloid Charge and neutralize the negative charge of components and suspension components,
It is intended to provide an electrolytic aggregating device capable of forming flocs by being coupled by a Van der Waals force.

【0006】本発明の他の目的とするところは、二重円
筒状陽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リマー
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 in the double cylindrical anode,
It is an object of the present invention to provide an electrolytic coagulation device capable of obtaining positively charged hydroxide polymer polyvalent ions that work most effectively for charge neutralization.

【0007】また、本発明の他の目的とするところは、
二重円筒状陽極にアルミニュウム,鉄など電解時に、イ
オンによる荷電中和と同時に不溶性の水酸化物による架
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:
Provided is an electrolytic flocculation device capable of reinforcing floc formation by using a material having a cross-linking action by insoluble hydroxide at the same time as charge neutralization by ions during electrolysis such as aluminum and iron in a double cylindrical anode. .

【0008】さらにまた、本発明の他の目的とするとこ
ろは、強い浮上攪拌対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、円筒状陰極は下部に液層
からの補給口を開口し、また、両面で対峙する二重円筒
状陽極には液中に没する全周の複数の開口により内筒内
側の液、液層の循環対流を可能とし、陰極両面の水素ガ
スと陽極からの酸素ガスの浮上対流により、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 effectively and promptly agglomerate micro flocs by strong floating and stirring convection, so that the cylindrical cathode has a replenishment port from the liquid layer at the bottom. The double-cylindrical anode that is open and confronts both sides has multiple openings around the entire circumference that are submerged in the liquid to enable circulation and convection of the liquid and liquid layers inside the inner cylinder. The present invention provides an electrolytic flocculation device capable of flocculating and aggregating oil components by levitation convection of oxygen gas from, and further aggregating floc of particles due to charge neutralization of positively charged ions from the anode.

【0009】[0009]

【課題を解決するための手段】即ち、本発明の電解凝集
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、陰極は物理的,化学的に安定した素材により
形成し、陽極は導電性で、電解時に正の荷電のイオンを
発生し、分散成分の荷電中和を行い、同時に発生する不
溶性の水酸化物により凝集と架橋と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, according to the electrolytic coagulation apparatus of the present invention, the cathode is formed of a physically and chemically stable material in a liquid tank in which colloid, particles with a suspension diameter, and oil are dispersedly present. However, the anode is electrically conductive, generates positively charged ions during electrolysis, neutralizes the charge of the dispersed components, and is composed of a material that can be simultaneously aggregated and crosslinked by insoluble hydroxide that occurs at the same time, It is characterized in that the removed substance dispersed in the liquid tank is agglomerated and easily separated.

【0010】[0010]

【作用】次ぎに、本発明の電解装置について以下実施例
を詳しく説明する。
Next, examples of the electrolysis apparatus of the present invention will be described in detail below.

【0011】図中1は液槽中に、陰極素材として黒鉛、
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、設置した電解凝集装置の構成を示す斜視断面図で
ある。
In the figure, reference numeral 1 indicates graphite as a cathode material in a liquid tank.
FIG. 3 is a perspective cross-sectional view showing the configuration of an electrolytic aggregating apparatus that is formed and installed in a cylinder using aluminum as the anode material.

【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。物理的,化学的に安定な黒鉛陰
極円筒3と外側のアルミニュウム陽極円筒4a、内側の
4bを電極とした。そして、黒鉛陰極円筒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、アルミニュウム陽極
円筒4a、4b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。アルミニュウム陽極円筒4a、4b全周には循
環開口9を多数設け、アルミニュウム陽極円筒4b内の
液と液槽1全体の液を循環容易としている。液層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 physically and chemically stable graphite cathode cylinder 3, the outer aluminum anode cylinder 4a, and the inner 4b were used as electrodes. An insulating ring 6 having a replenishing liquid opening 5 is provided below the graphite cathode cylinder 3 to insulate the aluminum bottom plate electrode 7 having a full inner diameter, which is placed on the insulating plate 2 forming the bottom of the liquid tank 1. ing. On the other hand, the aluminum anode cylinders 4a, 4b are in full contact with the aluminum bottom plate electrode 7,
Providing a thick flange 8 fitted to the inner diameter of the insulating ring 6,
It is fixed to the aluminum bottom plate electrode 7 with a bolt or the like not shown. A large number of circulation openings 9 are provided around the entire circumference of the aluminum anode cylinders 4a and 4b to facilitate circulation of the liquid in the aluminum anode cylinder 4b and the liquid in the entire liquid tank 1. On the outer peripheral portion of the liquid layer 1, a raw liquid inlet 10 from another device (not shown), a purified liquid outlet 11, and a scum 12 that has flocculated and floated.
The scum discharge port 13 is 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アルミ
ニュウム陽極円筒4a、4bは、フランジ8を介して、
プラス極15となる。外側の黒鉛陰極円筒3には、液面
16の外部からマイナス極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、アルミニュウム陽極円筒4
a、4b、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〕
18b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,鉄など水酸化物は荷
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.
5 is connected, the aluminum anode cylinders 4a and 4b attached in contact with the
It becomes the plus pole 15. A negative electrode 17 is connected to the outer graphite cathode cylinder 3 from outside the liquid surface 16. Aluminum anode cylinder 4 when electrolyzing and electrolyzing in a liquid in which colloidal components, suspension components, etc. (not shown) are dispersed
a, 4b, the aluminum bottom electrode 7, and the flange 8, the trivalent simple ion (Al 3+) 18a and the pH of 4 in the strongly acidic state.
In the vicinity of ~ 5, it binds to hydroxyl ions (OH-) in water,
Positively charged soluble polymer ion [Al8 (OH) 4 + / 20]
18b is generated, and usually has a function of neutralizing the charges of the negatively charged colloid and the suspension component. As a result, the fine particles can be bonded to each other by Van der Waals forces. Furthermore, aluminum, iron and other hydroxides are effective materials because they have a neutralizing effect and at the same time have a cross-linking action that further enhances the bond by Van der Waals. Furthermore, by energizing, the minute bubbles of hydrogen gas on the cathode side and oxygen gas on the anode side, which are generated from the opposite electrode surfaces directly facing each other, become an upward flow from the bottom side, not only floating the flocs, but also causing mutual collision of agglomerated particles. Repeatedly creates a complex effect that greatly advances the agglomeration.

【0014】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〕が生じ、図示していない分散粒子を荷電中和、更に
は、図示していない白色のゲル状水酸化アルミニュウム
は架橋の役目を果たし、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、黒鉛陰極円筒3は120mm
口径、アルミニュウム陽極円筒4aは140mm、4b
は、100mm口径の円筒とし、アルミニュウム陽極円
筒4a内の液の滞留防止と液槽1全体の循環のため、ア
ルミニュウム陽極円筒4a、4bにはパンチングによ
り、無数の8mm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。
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] occurs, the dispersed particles (not shown) are neutralized by charge, and further, the white gelled aluminum hydroxide (not shown) functions as a bridge, and at the same time, hydrogen gas 19 and oxygen generated from the polar surface are generated. As the gas 20 rises, the particles whose surface potential is near the isoelectric point float while forming flocs and agglomerates, and become the scum 12. 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 graphite cathode cylinder 3 is 120 mm
Diameter, aluminum anode cylinder 4a is 140mm, 4b
Is a cylinder having a diameter of 100 mm, and in order to prevent the liquid from staying in the aluminum anode cylinder 4a and to circulate the entire liquid tank 1, a number of circulation openings 9 having a diameter of 8 mm are provided in the aluminum anode cylinders 4a and 4b by punching. There is. still,
If the electrolysis apparatus becomes large and the amount of gas generated increases, there is a danger of explosion. Therefore, it is necessary to dilute the electrolysis apparatus with a large amount of air so that the concentration is below the dangerous point, and completely discharge it to the outside with a duct.

【0015】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50
V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、黒鉛陰極円筒
3とアルミニュウム陽極円筒4a、4bの内外壁から液
面が盛り上がる程の水素気泡が発生し、数秒後には、突
然、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、陰極側では、水素
気泡中で攪拌されるフロックも無数に確認された。
In the actual electrolysis, the current value changes depending on the degree of electrolysis of the sample.
The constant voltage of V was used, and the current value was determined depending on the sample. However, in consideration of safety, the current density was set within the range of 10 A / dm 2 . With a general cleaning agent used in water-based cleaners and a waste liquid containing colloidal components, the electrolysis is high, so a maximum current can be passed, and the graphite cathode cylinder 3 and the aluminum anode cylinders 4a, 4b can be supplied. It was confirmed that hydrogen bubbles generated enough to raise the liquid surface from the inner and outer walls, and a few seconds later, the scums that had agglomerated in millimeters suddenly rose one after another and floated on the water surface. Meanwhile, on the cathode side, countless flocs stirred in hydrogen bubbles were also confirmed.

【0016】尚、陰極は、炭素質などの物理的,化学的
に安定な、陽極と異なる素材によって構成する以外に、
陽極と同一、同種の素材により構成することも可能であ
り、適宜に陽極,陰極を切換え、溶出量を両極均一にす
ることも出来る。また、陰極となった時には、水素ガス
の洗浄効果により、極表面を清浄することにも効果を有
する。
The cathode is made of a material such as carbonaceous material which is physically and chemically stable and is different from the material of the anode.
It is also possible to use the same material as the anode and the same kind of material, and it is also possible to appropriately switch the anode and cathode to make the elution amount uniform on both electrodes. Further, when it becomes a cathode, it has an effect of cleaning the pole surface by the cleaning effect of hydrogen gas.

【0017】次ぎに図1の実施例によって実際に電解凝
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、油分について、ノルマルヘキ
サン法によって分析を行った。表1は相当量の界面活性
剤を含有し、油分はエマルジョン化し、時間経過後も沈
降せず、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溶性の水酸化物
の発生を利用する電解凝集法により、極めて高い精度で
目的を達成し得たことを確認した。
Next, according to the embodiment of FIG. 1, electrolytic coagulation was actually carried out, and then a polypropylene filter cloth having a thickness of 1 mm was used.
After filtration by stacking, the oil was analyzed by the normal hexane method. Table 1 shows that it contained a considerable amount of surfactant, the oil content was emulsified, and did not sediment even after a lapse of time. Originally, it was difficult to separate and remove by mechanical operation alone, and positively charged ions It was confirmed that the purpose could be achieved with extremely high accuracy by the electrolytic coagulation method utilizing generation of insoluble hydroxide.

【0018】[0018]

【表1】 [Table 1]

【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陰極素材と、導
電性を有し、電解時に正荷電のイオンを生じる陽極素材
によって多重円筒状に構成し、電解によって、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, a multi-cylinder is composed of a cathode material which is physically and chemically stable and conductive, and an anode material which is conductive and produces positively charged ions during electrolysis. It is possible to generate positively charged ions by electrolysis, neutralize negatively charged colloids, suspension components, etc., and agglomerate dispersed particles by the force of Van der Waals. Have a real profit that can be done.

【0020】また、本発明による時には、二重円筒状陽
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 double-cylindrical anode material, positively charged hydroxide polymer polyvalent ions are generated to charge the negatively charged particles. It has the practical benefit of allowing neutralization to work most effectively.

【0021】更にまた、本発明による時には、二重円筒
状陽極にアルミニュウム,鉄などの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, the double cylindrical anode is made of a material capable of simultaneously performing charge neutralization and cross-linking such as aluminum and iron,
It has the practical benefit of being able to reinforce the van der Waals bond and promote flocking.

【0022】更にまた、本発明による時には、多重円筒
状陰極,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 flotation force of the fine bubbles of hydrogen and oxygen from the surface of the multi-cylindrical cathode and the anode facing each other directly stirs the micro flocs to promote the agglomeration. Have the real benefit of being able to

【0023】更にまた、本発明による時には、円筒状陰
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 portion of the cylindrical cathode to facilitate guiding the stock solution for replenishment by the floating upstream, and it is possible to convect the entire liquid tank.

【0024】二重円筒状陽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 a large number of inner liquid circulation openings in the double-cylindrical anode, the inner cylinder side liquid can be smoothly aggregated.

【0025】陽極,陰極に同種、同一の素材を使用し、
適宜陰,陽極を切換えることにより、陽極時に溶出し摩
滅する量を減じ、延命することが出来る実益を有する。
The same material is used for the anode and cathode,
By switching the shade and anode appropriately, the amount of elution and abrasion at the anode can be reduced and the life can be extended.

【0026】陽極,陰極に同種、同一の素材を使用し、
適宜陰,陽極を切換えることにより、陰極時に、発生す
る水素ガスが極表面を洗浄し、洗浄に保つことが出来る
実益を有する。
The same material is used for the anode and cathode,
By appropriately switching the cathode and anode, there is a practical advantage that hydrogen gas generated at the time of the cathode can clean the electrode surface and keep the cleaning.

【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.

【符号の説明】[Explanation of symbols]

1. 液槽 2. 絶縁板 3. 黒鉛陰極円筒 4a,4b アルミニュウム陽極円筒 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 1. Liquid tank 2. Insulation plate 3. Graphite cathode cylinder 4a, 4b Aluminum anode 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. Positive pole 16. Liquid level 17. Negative poles 18a, 18b Positively charged ions 19. Hydrogen gas 20. Oxygen gas

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】物理的、化学的に安定且つ導電性を有する
素材により円筒状に陰極を形成し、陽極には導電性を有
し、電解時に正荷電のイオンを発生する素材をもって陰
極の内外に二重の円筒状に構成することにより、電解質
液中に分散する負荷電のコロイド成分、また懸濁成分な
どを電解により生じる正荷電のイオンにより、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、吸着を容易にしたことを特徴とする
多重円筒状電極電解凝集装置。
1. A cathode is formed in a cylindrical shape from a material that is physically and chemically stable and electrically conductive, and the anode has an electrically conductive material that generates positively charged ions during electrolysis. By constructing a double cylinder into a negative electrode, the negatively charged colloidal components dispersed in the electrolyte solution, and the suspended components are neutralized by positively charged ions generated by electrolysis to disperse the dispersed particles into a fan. A multi-cylinder electrode electrolytic aggregating device characterized by facilitating filtration and adsorption by aggregation due to the force of Der Vars.
【請求項2】陰極を挟んだ二重円筒状の陽極素材にアル
ミニュウム、鉄などを用いることにより、強酸性条件下
では、正荷電の多価単純イオンを、pH4〜5付近では
正荷電の水酸化ポリマーイオンを生ぜしめ、荷電中和を
効率よくしたことを特徴とする請求項1の多重円筒状電
極電解凝集装置。
2. By using aluminum, iron or the like as a double-cylindrical anode material sandwiching a cathode, positively charged polyvalent simple ions are produced under strongly acidic conditions, and positively charged water is produced at around pH 4-5. 2. The multi-cylindrical electrode electrolytic aggregating apparatus according to claim 1, wherein oxidized polymer ions are generated and charge neutralization is made efficient.
【請求項3】陰極の内外に二重円筒状の陽極にアルミニ
ュウム、鉄など陽イオンによる荷電中和力と不溶性の水
酸化物による架橋作用とを併せ持つ素材により構成する
ことにより、粒子相互の結合力を高め、フロック化力を
向上することが出来るようにしたことを特徴とする請求
項1の多重円筒状電極電解凝集装置。
3. Bonding of particles to each other by forming a double-cylindrical anode inside and outside the cathode from a material having both charge neutralization power by cations such as aluminum and iron and crosslinking action by insoluble hydroxide. The multi-cylindrical electrode electrolytic aggregating apparatus according to claim 1, wherein the force is increased and the flocculating force is improved.
【請求項4】陰極を形成する素材が炭素、黒鉛、カーボ
ンファイバーまたは、炭素複合材からなることを特徴と
する多重円筒状電極電解凝集装置。
4. A multi-cylindrical electrode electrolytic aggregating apparatus, characterized in that the material forming the cathode is carbon, graphite, carbon fiber or carbon composite material.
【請求項5】陰極を挟んで、陽極を二重円筒状に形成す
ることにより、水素、酸素気泡を効率よく発生させ、円
筒状間隙に気泡の上昇流を形成、粒子のフロック化を促
進する攪拌力とすることが出来るようにしたことを特徴
とする請求項1の多重円筒状電極電解凝集装置。
5. An anode is formed in a double cylinder shape with a cathode sandwiched therebetween, whereby hydrogen and oxygen bubbles are efficiently generated, an upward flow of bubbles is formed in a cylindrical gap, and flocculation of particles is promoted. The multi-cylindrical electrode electrolytic aggregating apparatus according to claim 1, wherein a stirring force can be used.
【請求項6】陽極を、陰極を挟んで、二重円筒状に構
成、陽極,陰極の全域において直接対峙し、溶出する陽
イオンの量,水素ガスの量に不足を生じなくすることが
出来るようにしたことを特徴とする請求項1の多重円筒
状電極電解凝集装置。
6. The double-cylindrical structure of the anode with the cathode sandwiched between the anode and the cathode so that the anode and the cathode are directly opposed to each other, and the amount of cations and the amount of hydrogen gas to be eluted can be prevented from becoming insufficient. The multi-cylindrical electrode electrolytic aggregating apparatus according to claim 1, characterized in that.
【請求項7】陽極,陰極を構成する素材がアルミニュウ
ム、鉄など同一の素材であって、陽極側では陽イオンと
不溶性の水酸化物を生じ、液中に分散するコロイド,懸
濁成分を荷電中和と架橋作用により凝集,集塊すること
が出来るようにしたことを特徴とする多重円筒状電極電
解凝集装置。
7. Anode and cathode are made of the same material such as aluminum and iron, and cations and insoluble hydroxide are produced on the anode side, and colloids and suspension components dispersed in the liquid are charged. A multi-cylindrical electrode electrolytic aggregating device characterized by being capable of aggregating and agglomerating by neutralizing and cross-linking actions.
【請求項8】円筒状に成形した陰極,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の多重円筒状電極電解凝集装置。
8. The multi-cylindrical electrode electrolytic aggregating apparatus according to claim 1, wherein a plurality of openings are provided on the circumferential surfaces of the cylindrically shaped cathode and anode to facilitate convection.
【請求項9】陰極,陽極が複数の円筒状に構成されたこ
とを特徴とする請求項1の多重円筒状電極電解凝集装
置。
9. The multi-cylindrical electrode electrolytic aggregating apparatus according to claim 1, wherein the cathode and the anode are formed in a plurality of cylindrical shapes.
JP14706793A 1993-05-25 1993-05-25 Multicylindrical electrode electrolytic cohesion device Pending JPH06328081A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14706793A JPH06328081A (en) 1993-05-25 1993-05-25 Multicylindrical electrode electrolytic cohesion device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14706793A JPH06328081A (en) 1993-05-25 1993-05-25 Multicylindrical electrode electrolytic cohesion device

Publications (1)

Publication Number Publication Date
JPH06328081A true JPH06328081A (en) 1994-11-29

Family

ID=15421739

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14706793A Pending JPH06328081A (en) 1993-05-25 1993-05-25 Multicylindrical electrode electrolytic cohesion device

Country Status (1)

Country Link
JP (1) JPH06328081A (en)

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KR100356404B1 (en) * 2000-03-04 2002-10-19 Nmctek Co Ltd Method and apparatus for eliminating specified hazardous substance in water using electric field
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