JPS5815191B2 - High Echinoden Kaishiyori Souchi - Google Patents

High Echinoden Kaishiyori Souchi

Info

Publication number
JPS5815191B2
JPS5815191B2 JP50115767A JP11576775A JPS5815191B2 JP S5815191 B2 JPS5815191 B2 JP S5815191B2 JP 50115767 A JP50115767 A JP 50115767A JP 11576775 A JP11576775 A JP 11576775A JP S5815191 B2 JPS5815191 B2 JP S5815191B2
Authority
JP
Japan
Prior art keywords
anode
cathode
liquid supply
electrolytic
supply port
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.)
Expired
Application number
JP50115767A
Other languages
Japanese (ja)
Other versions
JPS5239962A (en
Inventor
桑田貴平
前田満雄
追川宏之
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric 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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP50115767A priority Critical patent/JPS5815191B2/en
Publication of JPS5239962A publication Critical patent/JPS5239962A/en
Publication of JPS5815191B2 publication Critical patent/JPS5815191B2/en
Expired legal-status Critical Current

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  • Electrostatic Separation (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Description

【発明の詳細な説明】 この発明は産業排水等の電解凝集処理装置に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an electrolytic coagulation treatment apparatus for industrial wastewater, etc.

従来、排水中のコロイド性汚濁物質は凝集沈澱や加圧浮
上などの凝集処理により除去されていた。
Conventionally, colloidal pollutants in wastewater have been removed by coagulation treatments such as coagulation sedimentation and pressure flotation.

近年これらに加えて電解により金属水酸化物のフロック
を生成し、これにより汚濁物質を除去する電解凝集処理
が注目されるようになった。
In recent years, in addition to these methods, electrolytic coagulation treatment, which generates metal hydroxide flocs by electrolysis and removes pollutants, has attracted attention in recent years.

しかし、従来の電解凝集処理装置の電解構造は、アルミ
ニウム、鉄等のプレート状可溶性陽極及びステンレス、
鉄等のプレート状陰極を多数組合せて用いていた為に、
■電極の利用効率が低い、■電極にスケールを生成しや
すい、■維持管理が容易でない、■電極間隔が比較的大
きく消費電力が大きい等の欠点を有していた。
However, the electrolytic structure of the conventional electrolytic coagulation treatment equipment has a plate-shaped soluble anode made of aluminum, iron, etc., stainless steel, etc.
Because many combinations of plate cathodes such as iron were used,
It had drawbacks such as: - low electrode utilization efficiency; - easy to generate scale on the electrodes; - not easy to maintain; and - relatively large electrode spacing and high power consumption.

これらの欠点を補うものとして、陰極に対して微小間隔
に対向保持された円筒状の陽極を有し、電解液又は処理
すべき排水を陰極に設けられた給液口を通して両電極間
に高速流で送りながら高電流密度で電解する構造を特徴
とする電解凝集処理装置が開発された。
To compensate for these shortcomings, we have a cylindrical anode that is held opposite the cathode at a minute distance, and a high-speed flow of electrolyte or wastewater to be treated between the two electrodes through a liquid supply port provided on the cathode. An electrolytic coagulation processing device has been developed that features a structure that performs electrolysis at a high current density while feeding the material.

しかし、この装置も電極面が円形である為に両電極間を
流れる電解液又は排水の中心速度に比べて周辺速度は小
さくなり、スケール生成の抑制効果が低い等の欠点を有
していた。
However, since this device also has a circular electrode surface, the peripheral velocity of the electrolyte or waste water flowing between the two electrodes is smaller than the central velocity, and this device has drawbacks such as low scale generation suppression effect.

この発明は従来の装置の上記のような欠点を解消するこ
とを目的とし、電解液又は排水の通過速度を両電極間の
どの位置をとっても一定となるようにしたものである。
The purpose of this invention is to eliminate the above-mentioned drawbacks of conventional devices, and the purpose of this invention is to make the passing speed of electrolyte or waste water constant regardless of the position between the two electrodes.

以下、本発明の一実施例を図に基づいて説明する。Hereinafter, one embodiment of the present invention will be described based on the drawings.

即ち第1図及び第2図において、1は排液の流入管、2
は鉄、ステンレス、カーボン、グラファイト、白金等よ
りなる陰極、3はこの陰極2に設けられ上記流入管1に
連通する正方形又は長方形状の給液口、4は陰極2及び
後述する陽極6の間隔を微小に保つためのアルミナボー
ルまたはローラ等より成る絶縁スペーサ、5は陰極2に
設けられた絶縁スペーサのガイド溝、6はアルミニウム
、鉄等の可溶性金属、又はカーボン、グラファイト、白
金等の不溶性材料よりなり正方形又は長方形状をしその
辺が給液口3の形辺に平行となるように設けられた陽極
、7はこの陽極6の電解面を常に一定に保っておく必要
があるため、絶縁スペーサ4との接点をたえず変動させ
なければならないので、陽極6を水平方向に往復動させ
るための駆動源と直結する連結軸、8は連結軸7を陽極
6に固定する絶縁固定台、9は陽極6のリード端子、1
0は陰極2のリード端子、11.12は電解層の排液受
槽、13.14は排液の流出管、15は電解槽である。
That is, in FIGS. 1 and 2, 1 is a drain inflow pipe, 2 is
is a cathode made of iron, stainless steel, carbon, graphite, platinum, etc., 3 is a square or rectangular liquid supply port provided on this cathode 2 and communicates with the inflow pipe 1, and 4 is a distance between the cathode 2 and an anode 6, which will be described later. 5 is a guide groove of the insulating spacer provided on the cathode 2, and 6 is a soluble metal such as aluminum or iron, or an insoluble material such as carbon, graphite, or platinum. The anode 7, which has a square or rectangular shape and is installed so that its sides are parallel to the sides of the liquid supply port 3, is insulated because the electrolytic surface of the anode 6 must always be kept constant. Since the point of contact with the spacer 4 must be constantly changed, a connecting shaft is directly connected to a drive source for horizontally reciprocating the anode 6, 8 is an insulated fixing base for fixing the connecting shaft 7 to the anode 6, and 9 is an insulated fixing base. Anode 6 lead terminal, 1
0 is a lead terminal of the cathode 2, 11.12 is a drain tank for the electrolytic layer, 13.14 is a drain pipe, and 15 is an electrolytic cell.

そしてこれらは電解処理装置Aをなお、陰極2に設けら
れた給液口3の大きさは、陽極6が駆動源により往復摺
動させられているため、陽極6の摺動中より小さく構成
されている。
Furthermore, since the anode 6 is slid back and forth by the drive source, the size of the liquid supply port 3 provided in the cathode 2 of the electrolytic treatment apparatus A is smaller than that of the anode 6 while it is sliding. ing.

一方、16は排液供給ポンプ、17は給液バルブ、18
はフロックの浮上促進用の補助電解用電極群、19は浮
上分離槽、20は浮上スカム20のかきとり用スキマー
、22は浮上スカム20を回収する貯槽、23は排液バ
ルブ、24は排液管である。
On the other hand, 16 is a drainage supply pump, 17 is a supply valve, 18
19 is a flotation separation tank, 20 is a skimmer for scraping the floating scum 20, 22 is a storage tank for collecting the floating scum 20, 23 is a drain valve, and 24 is a drain pipe. It is.

そしてこれらは浮上分離装置Bを構成している。These components constitute a flotation separation device B.

次に本実施例により装置の作用について述べる。Next, the operation of the device will be described according to this embodiment.

まず排液供給ポンプ16により送られた排液は、給液バ
ルブ17を介して流入管1に導かれ給液口3より電圧の
印加された陽極6及び陰極2間に高速で流入する。
First, the drained liquid sent by the drained liquid supply pump 16 is guided to the inflow pipe 1 via the liquid supply valve 17, and flows at high speed between the anode 6 and the cathode 2 to which a voltage is applied from the liquid supply port 3.

この両電極間の間隙は陰極2に設けられたガイド溝5内
の絶縁スペーサ4により0.5〜1.0rr)/mに保
持され排液はこの間隙を通過する間に電解作用を受ける
The gap between the two electrodes is maintained at 0.5 to 1.0 rr)/m by an insulating spacer 4 in a guide groove 5 provided in the cathode 2, and the drained liquid is subjected to an electrolytic action while passing through this gap.

この電極間隙が微小であるということは通電抵抗を小さ
く、電流密度を大きくとれることを意味し装置として小
型化されるとともに、微小間隙であるため排液を高流速
で均一な流速で流すことができ、電極面へのスケールの
生成を抑制できる。
The small gap between the electrodes means that the resistance to conduction is low and the current density can be high, making the device more compact. It is possible to suppress the formation of scale on the electrode surface.

なお電解は可溶性陽極を用いた場合は、陽極からは金属
水酸化物の凝集フロック、不溶性陽極を用いた場合は酸
素等の酸化性ガスを生成する。
In the electrolysis, when a soluble anode is used, flocs of metal hydroxide are generated from the anode, and when an insoluble anode is used, oxidizing gases such as oxygen are generated from the anode.

一方陰極からは水素等の還元性ガスを生成する。On the other hand, a reducing gas such as hydrogen is generated from the cathode.

電解層の排液は排液受槽11.12に流入し流出管13
.14を経て浮上分離槽19内に導かれ、生成した凝集
フロックは陰極2及び補助電解用電極群18から生成す
る微細気泡を包含し浮上性を有し浮上スカム20となっ
て処理液と分離される。
The drained liquid from the electrolytic layer flows into the drained liquid receiving tank 11.12 and the outflow pipe 13.
.. The flocs are led into the flotation separation tank 19 through the scum 14, and the generated flocs contain fine bubbles generated from the cathode 2 and the auxiliary electrolysis electrode group 18, have a flotation property, and become floating scum 20, which is separated from the processing liquid. Ru.

浮上スカム20はスキーマ21によってかきとられ貯槽
22に回収される。
The floating scum 20 is scraped off by the schema 21 and collected in the storage tank 22.

一方処理液は排液バルブ23を介して排液管24により
放流される。
On the other hand, the processing liquid is discharged through a drain pipe 24 via a drain valve 23 .

なお凝集フロックの成長促進の為浮上分離槽19の入口
で高分子凝集剤を添加することも任意である。
It is also optional to add a polymer flocculant at the entrance of the flotation tank 19 to promote the growth of flocs.

以上、要するに本発明装置は陽極の電極面を正方形又は
長方形とし、かつ給液口を正方形又は長方形とするとと
もにその辺を上記電極面の辺に平行に配置するとともに
、陽極と陰極間の間隙を微小に保持し、陰極に設けられ
た給液口の大きざを陽極の摺動中より小さくしたので、
電極間を流れる電解液又は被処理液の流速が高速で均一
になり、電極スケール生成の抑制効果を著しく大きくで
き、装置の維持管理をきわめて容易に出来る等の効果が
ある。
In summary, in the device of the present invention, the electrode surface of the anode is square or rectangular, the liquid supply port is square or rectangular, its sides are arranged parallel to the sides of the electrode surface, and the gap between the anode and cathode is The size of the liquid supply port provided on the cathode was made smaller than that of the anode during sliding.
The flow rate of the electrolytic solution or the liquid to be treated between the electrodes becomes high and uniform, the effect of suppressing electrode scale formation can be significantly increased, and the maintenance and management of the apparatus can be made extremely easy.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の電解処理装置の一実施例を示す一部破
断斜視図、第2図は本発明の電解処理装置を用いた排液
処理装置を示すフロー図である。 図において1は流入管、2は陰極、3は給液口、4は絶
縁スペーサ、5はガイド溝、6は陽極、7は連結軸、8
は絶縁固定台、9,10はリード端子、11.12は排
液受槽、13.14は流出管、15は電解槽、16は供
給ポンプ、17は給液バルブ、18は補助電解用電極群
、19は浮上分離槽、20は浮上スカム、21はスキマ
ー、22は貯槽、23は排液バルブ、24は排液管、A
は電解処理装置、Bは浮上分離装置である。 尚図中同一部分は同一符号にて示す。
FIG. 1 is a partially cutaway perspective view showing an embodiment of the electrolytic treatment apparatus of the present invention, and FIG. 2 is a flow diagram showing a waste liquid treatment apparatus using the electrolytic treatment apparatus of the present invention. In the figure, 1 is an inflow pipe, 2 is a cathode, 3 is a liquid supply port, 4 is an insulating spacer, 5 is a guide groove, 6 is an anode, 7 is a connecting shaft, 8
1 is an insulated fixed stand, 9 and 10 are lead terminals, 11.12 is a drainage tank, 13.14 is an outflow pipe, 15 is an electrolytic tank, 16 is a supply pump, 17 is a liquid supply valve, and 18 is a group of electrodes for auxiliary electrolysis. , 19 is a floating separation tank, 20 is floating scum, 21 is a skimmer, 22 is a storage tank, 23 is a drain valve, 24 is a drain pipe, A
is an electrolytic treatment device, and B is a flotation separation device. In addition, the same parts in the figures are indicated by the same reference numerals.

Claims (1)

【特許請求の範囲】 1 互に対向する陽極及び陰極を有し、電解液又は処理
すべき排液を上記陰極に設けられた給液口を通して両電
極間に流し、上記両電極間に電圧を加えることにより汚
濁物質を除去する排液の電解処理装置において、上記陽
極と陰極間に絶縁スペーサを介して対向間隙を微小に保
持するとともに、上記陽極の電極面を正方形もしくは長
方形状にかつ上記給液口の形状を正方形もしくは長方形
状にし、上記給液口の辺を上記陽極の電極面の辺に平行
となるように配置し、 上記絶縁スペーサ上で上記陽極を摺動させる駆動源を設
け、上記給液口を上記陽極の摺動中より小さくしたこと
を特徴とする排液の電解処理装置。
[Claims] 1. It has an anode and a cathode facing each other, an electrolytic solution or a waste liquid to be treated is passed between the two electrodes through a liquid supply port provided on the cathode, and a voltage is applied between the two electrodes. In an electrolytic treatment device for wastewater that removes contaminants by adding an insulating material to the anode, a gap between the anode and the cathode is kept small via an insulating spacer, and the electrode surface of the anode is square or rectangular, and the electrode surface of the anode is formed into a square or rectangular shape, and The liquid inlet has a square or rectangular shape, the side of the liquid supply port is arranged parallel to the side of the electrode surface of the anode, and a drive source is provided to slide the anode on the insulating spacer, An apparatus for electrolytic treatment of waste liquid, characterized in that the liquid supply port is made smaller than when the anode is sliding.
JP50115767A 1975-09-25 1975-09-25 High Echinoden Kaishiyori Souchi Expired JPS5815191B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50115767A JPS5815191B2 (en) 1975-09-25 1975-09-25 High Echinoden Kaishiyori Souchi

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50115767A JPS5815191B2 (en) 1975-09-25 1975-09-25 High Echinoden Kaishiyori Souchi

Publications (2)

Publication Number Publication Date
JPS5239962A JPS5239962A (en) 1977-03-28
JPS5815191B2 true JPS5815191B2 (en) 1983-03-24

Family

ID=14670535

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50115767A Expired JPS5815191B2 (en) 1975-09-25 1975-09-25 High Echinoden Kaishiyori Souchi

Country Status (1)

Country Link
JP (1) JPS5815191B2 (en)

Also Published As

Publication number Publication date
JPS5239962A (en) 1977-03-28

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