JPH06304569A - Electrolytic flocculation device - Google Patents

Electrolytic flocculation device

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Publication number
JPH06304569A
JPH06304569A JP5119034A JP11903493A JPH06304569A JP H06304569 A JPH06304569 A JP H06304569A JP 5119034 A JP5119034 A JP 5119034A JP 11903493 A JP11903493 A JP 11903493A JP H06304569 A JPH06304569 A JP H06304569A
Authority
JP
Japan
Prior art keywords
anode
electrolytic
liquid
positively charged
cathode
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
JP5119034A
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 JP5119034A priority Critical patent/JPH06304569A/en
Publication of JPH06304569A publication Critical patent/JPH06304569A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To separate and remove colloidal components and suspended components which are dispersed in an electrolyte, with precision and even with a simple filtration adsorbent by charging and neutralizing them by ions, flocculating them by the ion bridging action and the van der Waals force and aggregating them by the agitating force by floating flow of gas bubbles. CONSTITUTION:In a liquid tank 1, cathodic cylinders 3 of physically and chemically stable graphite, etc., and anodic cylinders 4 of aluminum and iron, etc., which have both the charging neutralization and bridging action and generate positively charged ions are provided on insulating rings 6 having makeup liquid openings 5. Therefore, particulates in tap water, sewage, cutting liquid for machine tools and washing liquid are flocculated to facilitate the filtration and adsorption thereof.

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、酸素気泡による攪拌力及び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イオン
により、凝集浮上させ、濾過分離を容易とした電解凝集
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. , The impurities that cause troubles are hydrogenated by electrolysis, the stirring force by oxygen bubbles and the charge neutralization of colloidal particles, and the ions from the anode that sometimes perform a crosslinking action are used to flocculate and facilitate separation by filtration. It concerns electrolytic aggregation.

【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、懸濁するスラッジを効果的、即効的に分離除
去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 oil and sludge that were emulsified and suspended 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 has been nothing that can effectively and promptly separate and remove white turbidity, emulsified oil content, and sludge that diffuses and suspends, which is mixed in a cleaning liquid used in an aqueous cleaning machine.

【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,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 positively charged ions from the anode neutralize the negatively charged colloidal components dispersed in the electrolyte solution,
It enables flocculation and flocculation by the force of Van der Waals, and by generating levitation convection in the entire liquid tank by hydrogen bubbles from the cathode, for example, micro flocs of several tens of microns collide with each other, and several hundreds of microns or more. The feature is that solid-liquid separation and oil-water separation can be performed with high accuracy even by agglomerating even up to simple 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。
According to the present invention, a cathode material is a material which is physically and chemically stable and is electrically conductive in a liquid tank incorporated in equipment such as clean water, sewage treatment, and a washing machine, and a system. Is a material that has conductivity and generates positively charged ions when electrolysis is applied, and neutralizes the negative charges of the colloidal components and suspension components in the electrolyte solution that should be removed. It is intended to provide an electrolytic coagulation device capable of forming flocs by being coupled by a Vars force.

【0006】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、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 obtain a positively charged hydroxide polymer polyvalent ion which works most effectively for charge neutralization by using aluminum, iron, copper, zinc or the like as an anode. An electrolytic flocculation device is provided.

【0007】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:
The present invention provides an electrolytic coagulation device capable of reinforcing the formation of flocs by using a material having a cross-linking action at the same time as charge neutralization such as aluminum and iron for the anode.

【0008】さらにまた、本発明の他の目的とするとこ
ろは、強い浮上流によるマイクロフロックの集塊を効果
的、即効的に行うため、陰極を筒とし、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
上撹拌流により、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 the cathode a cylinder and the outer cylinder to be any one of the poles in order to effectively and promptly agglomerate the micro flocs by strong floating upstream. A replenishment port from the liquid tank is opened in the lower part, and a plurality of poles inside the inner cylinder are circulated in the inner cylinder, which is the opposing pole facing each other, around the entire circumference submerged in the liquid. The oil is floated and agitated by the floating stir flow of the gas from the opposite electrode surfaces of the outer cylinder in the case where the outer cylinder is installed in close proximity, and the flocculation of particles is further aggregated by the charge neutralization of positively charged ions from the anode. The present invention provides an electrolytic aggregating 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、通電時に正電荷のイオンを発
生し、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, in 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 having a suspension diameter, and oil are dispersed. However, the anode is electrically conductive, generates positively charged ions when energized, neutralizes the charge of the dispersed components, and is composed of a material that can be aggregated and cross-linked at the same time. It aggregates the removed substances dispersed in the liquid tank. However, it is characterized in that it can be 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とアルミニュウム陽極円筒4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。アルミニュウム陽極円筒
4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4内の液を黒鉛陰極円筒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 also by welding a PVC plate to the insulating plate 2 at the bottom. A physically and chemically stable graphite cathode cylinder 3 and an aluminum anode cylinder 4 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 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. There is. A large number of circulation openings 9 are provided on the entire circumference of the aluminum anode cylinder 4 to facilitate circulation of the liquid in the aluminum anode cylinder 4 to the inside of the graphite cathode cylinder 3. 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.

【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4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、アルミ
底板電極7、フランジ8から、強酸性状態では3価の単
純イオン(Al3+)18−1、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〔Al8(OH)4+/20〕18−2が発生し、
通常負荷電のコロイド、懸濁成分の電荷を中和する作用
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 aluminum anode cylinder 4 attached in contact with this becomes a positive electrode 15 via the flange 8. A negative electrode 17 is connected to the outer graphite cathode cylinder 3 from outside the liquid surface 16. When electrolyzing and electrolyzing in a liquid in which colloidal components, suspension components, etc. (not shown) are dispersed, trivalent simple ions (in the strongly acidic state, from the aluminum anode cylinder 4, the aluminum bottom plate electrode 7, and the flange 8) Al 3 +) 18-1, pH of around 4 to 5 binds to hydroxide ion (OH-) in water, and positively charged soluble polymer ion [Al 8 (OH) 4 + / 20 ] 18-2 is formed. Occurs,
Normally, it produces the action of neutralizing the charge of negatively charged colloid and suspension components. As a result, the fine particles can be bonded to each other by Van der Waals forces. Furthermore,
Aluminium, iron, etc. are effective materials because they have a cross-linking action that further enhances the binding by van der Waals as well as the charge neutralization. Furthermore, by energizing, the hydrogen gas on the cathode side and the fine bubbles of oxygen gas on the anode side generated from the surfaces of the two electrodes directly facing each other become an upward flow from the bottom side,
It not only raises the flocs, but also causes repeated agglomeration of the agglomerated particles to produce a combined effect of significantly promoting 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電荷多価イオン(Al
3+)18−1またはポリマーイオン〔Al8(OH)4+
/20〕18−2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、黒鉛陰極円筒3は120mm口径、アルミニュ
ウム陽極円筒4は100mm口径の円筒とし、アルミニ
ュウム陽極円筒4内の液の滞留を防ぐため、アルミニュ
ウム陽極円筒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
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60V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6A/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材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の内壁から液面が盛り
上がる程の水素気泡が発生し、数十秒後には、アルミニ
ュウム陽極円筒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る。
The principle of electrolytic aggregation in FIG. 2 will be described in detail.
By electrolysis, positively charged multiply charged ions of aluminum (Al
3 +) 18-1 or polymer ion [Al 8 (OH) 4 +
/ 20 ] 18-2 is generated, and the dispersed particles not shown are subjected to charge neutralization, and at the same time, as the hydrogen gas 19 and oxygen gas 20 rising from the polar surface rise, the surface potential is near the isoelectric point. Flies while forming flocs and agglomerates and becomes 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 has a diameter of 120 mm, and the aluminum anode cylinder 4 has a diameter of 100 mm. The circulation opening 9 is provided. 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, but in the test, the constant voltage of DC 60V and the current value depended on the sample, but considering the safety,
The current density was within the range of 6 A / dm 2 . With a general cleaning material used in water-based cleaners and a waste liquid containing colloidal components, the electrolyte has a high degree of electrolysis, so a maximum current can be passed, and the liquid surface rises from the inner wall of the graphite cathode cylinder 3. About several tens of seconds after generation of hydrogen bubbles, it can be confirmed that scum suddenly agglomerated in millimeter units suddenly rises in the oxygen bubbles on the outer peripheral surface of the aluminum anode cylinder 4 and floats on the water surface. It was Meanwhile, on the cathode side, innumerable flocs stirred in hydrogen bubbles are also confirmed.

【0015】図3は陰極にステンレスの平板21、陽極
にアルミニュウム平板22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。
In FIG. 3, a stainless steel flat plate 21 is used for the cathode, an aluminum flat plate 22 is used for the anode, a space is provided in the lower part to serve as a passage for the liquid, and both electrodes are positioned at the same position as the housing 23 so that the scum overflows at the upper part. It is characterized by the fact that it is arranged side by side.

【0016】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、油分については、ノルマルヘ
キサン法によって、浮遊物質量については、0.1μm
をカットオフのメンブラン濾紙により、吸引濾過後、精
密天秤により、濾過残滓を見る計測方法を行った。ま
た、濁度、色度に関しては、上水用検査規格により行っ
たものである。表1から表3の試料中は相当量の界面活
性剤を含有し、油分はエマルジョン化し、粒子もコロイ
ド状であり、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ばかりであり、
正荷電のイオン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。なお
表1は水溶性切削液の電解凝集試験結果を示したもの、
表2は洗浄液を電解凝集したデータ、そして表3は研削
液を電解凝集したものである。
Next, after electrolytic coagulation was actually carried out according to the embodiment shown in FIG. 1, two 1 mm thick polypropylene filter cloths were used.
After filtration by stacking, the normal hexane method for the oil content and 0.1 μm for the amount of suspended solids
After suction filtration with a cut-off membrane filter paper, a measuring method was performed to see the filter residue with a precision balance. The turbidity and chromaticity were measured according to the water supply inspection standard. The samples in Tables 1 to 3 contained a considerable amount of surfactant, the oil was emulsified, the particles were colloidal, did not sediment even after a lapse of time, and were originally separated and removed only by mechanical operation. Everything was difficult,
It was confirmed that the objective could be achieved with extremely high accuracy by the electrolytic coagulation method utilizing the generation of positively charged ions. Table 1 shows the results of electrolytic coagulation test of water-soluble cutting fluid,
Table 2 shows data obtained by electrolytically aggregating the cleaning liquid, and Table 3 shows data obtained by electrolytically aggregating the grinding liquid.

【0017】[0017]

【表1】 [Table 1]

【0018】[0018]

【表2】 [Table 2]

【0019】[0019]

【表3】 [Table 3]

【0020】[0020]

【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
によって構成し、電解質液中に電解可能に構成し、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 cathode material having physical and chemical stability and conductivity and an anode material having conductivity and generating positively charged ions during electrolysis are used. Electrolyzable in an electrolyte solution, by electrolysis, positively charged ions are generated, and negatively charged colloids, suspended components, etc. are charged and neutralized, and dispersed particles are dispersed by Van der Waals. It has the practical benefit of being able to aggregate by force.

【0021】また、本発明による時には、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 as the anode material, positively charged hydroxide polymer polyvalent ions are generated to most neutralize the charge of the negatively charged particles. It has the practical benefit of being able to work effectively.

【0022】更にまた、本発明による時には、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。
Further, according to the present invention, the anode is made of a material capable of simultaneously performing charge neutralization and crosslinking, such as aluminum and iron, to reinforce the van der Waals bond and to form a flock. Has a real benefit that can be promoted.

【0023】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 hydrogen and oxygen fine bubbles from the surface where the cathode and the anode face each other directly stir the micro flocs,
Has the real benefit of promoting agglomeration.

【0024】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, and the stock replenishing solution can be easily guided by the floating upstream, so that convection of the entire liquid tank is possible.

【0025】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 internal liquid circulation openings in the anode cylinder, there is a practical advantage that the liquid on the inner cylinder side 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. 黒鉛陰極円筒 4. 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 18-1、2 正荷電のイオン 19. 水素ガス 20. 酸素ガス 21. ステンレス平板 22. アルミニュウム平板 23. ハウジング 1. Liquid tank 2. Insulation plate 3. Graphite cathode cylinder 4. 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 pole 18-1, 2 positively charged ion 19. Hydrogen gas 20. Oxygen gas 21. Stainless steel plate 22. Aluminum flat plate 23. housing

Claims (5)

【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構成するこ
とにより、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凝集装置。
1. An electrolyte comprising a cathode formed of a material that is physically and chemically stable and electrically conductive, and an anode that is electrically conductive and that generates positively charged ions during electrolysis. Characterized by colloidal components with a negative charge that are dispersed in the liquid, and suspension components that are neutralized by charge, and the dispersed particles are aggregated by the force of Van der Waals, facilitating filtration and adsorption. And an electrolytic flocculation device.
【請求項2】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
オンを生ぜじめ、荷電中和を効率よくしたことを特徴と
した請求項1の電解凝集装置。
2. Aluminium, iron, etc. are used as the anode material to generate positively charged polyvalent simple ions under strongly acidic conditions and positively charged hydroxylated polymer ions at around pH 4 to 5, resulting in charging. The electrolytic coagulation apparatus according to claim 1, wherein the neutralization is performed efficiently.
【請求項3】陽極にアルミニュウム、鉄などの荷電中和
力と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
ことが出来ることを特徴とした請求項1の電解凝集装
置。
3. The anode is made of a material having a charge neutralizing power and a crosslinking action, such as aluminum and iron, so that the mutual binding force between particles can be enhanced and the flocculating power can be improved. The electrolytic coagulation apparatus according to claim 1.
【請求項4】陰極、陽極を円筒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
の電解凝集装置。
4. By forming a cathode and an anode in a cylinder,
2. An agitating force for efficiently generating hydrogen and oxygen bubbles, forming an ascending flow of bubbles in the cylindrical gap, and promoting flocculation of particles.
Electrolytic flocculation device.
【請求項5】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、対流を容易としたことを特徴とする
請求項1の電解凝集装置。
5. The electrolytic aggregating apparatus according to claim 1, wherein a plurality of openings are provided on the circumferential surfaces of the cathode and the anode formed into a cylindrical shape to facilitate convection.
JP5119034A 1993-04-21 1993-04-21 Electrolytic flocculation device Pending JPH06304569A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5119034A JPH06304569A (en) 1993-04-21 1993-04-21 Electrolytic flocculation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5119034A JPH06304569A (en) 1993-04-21 1993-04-21 Electrolytic flocculation device

Publications (1)

Publication Number Publication Date
JPH06304569A true JPH06304569A (en) 1994-11-01

Family

ID=14751336

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5119034A Pending JPH06304569A (en) 1993-04-21 1993-04-21 Electrolytic flocculation device

Country Status (1)

Country Link
JP (1) JPH06304569A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19645653A1 (en) * 1996-11-06 1998-05-07 Herbert Hosse Filter elements and filter devices
EP2667955A4 (en) * 2011-01-24 2016-11-23 E2Metrix Inc Electrocoagulation for treating liquids
CN108675515A (en) * 2018-07-25 2018-10-19 大连波美科技有限公司 Except silicon electrochemical reaction appts
CN115403196A (en) * 2022-10-08 2022-11-29 青岛理工大学 Composite system for RO concentrated water hardness and organic matter deep removal and application and method thereof
JP2024013187A (en) * 2022-07-19 2024-01-31 重▲慶▼文理学院 Device for recovering organic material from high-salt hardly-decomposable organic wastewater and synchronous storage of energy

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19645653A1 (en) * 1996-11-06 1998-05-07 Herbert Hosse Filter elements and filter devices
EP2667955A4 (en) * 2011-01-24 2016-11-23 E2Metrix Inc Electrocoagulation for treating liquids
CN108675515A (en) * 2018-07-25 2018-10-19 大连波美科技有限公司 Except silicon electrochemical reaction appts
JP2024013187A (en) * 2022-07-19 2024-01-31 重▲慶▼文理学院 Device for recovering organic material from high-salt hardly-decomposable organic wastewater and synchronous storage of energy
CN115403196A (en) * 2022-10-08 2022-11-29 青岛理工大学 Composite system for RO concentrated water hardness and organic matter deep removal and application and method thereof
CN115403196B (en) * 2022-10-08 2023-08-22 青岛理工大学 Composite system for RO concentrated water hardness and organic matter depth removal, application and method thereof

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