JPS62227493A - Apparatus for flotation concentration of sludge - Google Patents

Apparatus for flotation concentration of sludge

Info

Publication number
JPS62227493A
JPS62227493A JP61070085A JP7008586A JPS62227493A JP S62227493 A JPS62227493 A JP S62227493A JP 61070085 A JP61070085 A JP 61070085A JP 7008586 A JP7008586 A JP 7008586A JP S62227493 A JPS62227493 A JP S62227493A
Authority
JP
Japan
Prior art keywords
anode plate
cathode plates
sludge
electrolytic cell
suspended substance
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.)
Granted
Application number
JP61070085A
Other languages
Japanese (ja)
Other versions
JPH0331118B2 (en
Inventor
Eiichi Ishigaki
栄一 石垣
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.)
Ishigaki Mechanical Industry Co Ltd
Original Assignee
Ishigaki Mechanical Industry Co Ltd
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 Ishigaki Mechanical Industry Co Ltd filed Critical Ishigaki Mechanical Industry Co Ltd
Priority to JP61070085A priority Critical patent/JPS62227493A/en
Publication of JPS62227493A publication Critical patent/JPS62227493A/en
Publication of JPH0331118B2 publication Critical patent/JPH0331118B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Physical Water Treatments (AREA)
  • Treatment Of Sludge (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PURPOSE:To continuously treat a large quantity of a raw liquid, by arranging a large number of cathode plates in an electrolytic cell in parallel and providing an anode plate in opposed relation to the middle of the cathode plates. CONSTITUTION:A large number of cathode plates 2 are fixedly provided to an electrolytic cell in parallel and an anode plate 3 is provided so as to position at the intermediate part of the cathode plates 2 in a rotatable manner. When a current is supplied while the anode plate 3 is rotated, the suspended substance in a raw liquid floats up by air bubbles generated in the electrode plate parts to form a conc. layer to a liquid surface part. The conc. suspended substance is scraped by a skimmer 5 to be taken out through a trough. A scraper 4 is slid with the surface of the anode plate 3 to remove the contaminant on the surface of the anode plate 3. By this method, electrolytic discharge is not interrupted and the suspended substance is smoothly raised and concn. efficiency can be enhanced.

Description

【発明の詳細な説明】 「産業上の利用分野」 この発明は、下水汚泥等の浮上濃縮装置の改良に関する
。従来、下水汚泥等の浮上濃縮装置としでは、汚泥中に
加圧空気を吹き込んで、微細な気泡によって、原液中の
浮遊物を浮上分離するもの、また、汚泥を電気分解して
電極部に発生する水素ガスや酸素ガスによって浮遊物を
浮上させるものがあるが、この発明は、その後者の改良
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION "Field of Industrial Application" The present invention relates to an improvement in a flotation concentration device for sewage sludge, etc. Conventionally, flotation and concentration equipment for sewage sludge, etc., involves blowing pressurized air into the sludge and using fine air bubbles to float and separate suspended matter in the raw solution, and also by electrolyzing the sludge and generating it at the electrode part. There are devices that levitate floating objects using hydrogen gas or oxygen gas, and this invention relates to an improvement of the latter.

「従来の技術」 従来、この種電気分解による浮上濃縮装置としては、例
えば、実公昭52−55163号があり、この考案は、
電極板面が汚れて、電解効率が低下するのを防止するた
めに、その処理水の一部を循環させて、その循環路中に
電極板を位置させたものである。
"Prior Art" Conventionally, as a flotation concentration device using this type of electrolysis, there is, for example, Utility Model Publication No. 52-55163, and this device is
In order to prevent the electrode plate surface from getting dirty and reducing electrolysis efficiency, a portion of the treated water is circulated and the electrode plate is placed in the circulation path.

「発明が解決しようとする問題点」 然しながら、上述のような従来装置では、電極板面を清
掃するのに、処理水の一部の流動を同州するだけである
ので、充分に清掃することができず、また、構造的にも
大容量、大能力の処理装置は実現し追い。
``Problems to be Solved by the Invention'' However, in the conventional device as described above, in order to clean the electrode plate surface, only a portion of the treated water is passed through the flow, so it is not necessary to thoroughly clean the electrode plate surface. However, structurally speaking, processing equipment with large capacity and capacity is on the verge of being realized.

「問題点を解決するための手段」 そこで、この発明においては、電極板面を、5v掃する
のに、機械的手段を用いて、晟極板面に付着した汚れを
確実に除去し、電解能力が低下するのを防止するととも
に、多数の電極板を用いて大量の原液を連続して処理す
ることができる装置を実現したものであシ、その要旨と
するところは、電解+J内に多数の陰極板を並列すると
ともに、これら陰極板の中間には、電解槽に支架した回
転4i111に設けた陽極板を相対向させて設け、この
陽極板の回転周辺部分に高ませてスクレーバを設け、さ
らに、槽内液面部分に浮上物の掻取装置を設けたもので
ある。
"Means for Solving the Problem" Therefore, in the present invention, when cleaning the electrode plate surface by 5V, mechanical means are used to reliably remove the dirt adhering to the electrode plate surface, and the electrolytic We have realized a device that can continuously process a large amount of raw solution using a large number of electrode plates while preventing the capacity from decreasing. The cathode plates are arranged in parallel, and in the middle of these cathode plates, an anode plate provided on a rotating 4i111 supported by an electrolytic cell is provided facing each other, and a scraper is provided elevated around the rotation of this anode plate, Furthermore, a device for scraping floating objects is provided at the liquid level in the tank.

「作 用」 この発明に係る装置は、上述のように構成されて2す、
従って、°電極板に通’tdすると電@仮の表面には、
水素や酸素等の微細な気泡が生じ、この気泡が浮上する
際に、原液中の浮遊物に付着して浮上させ、液面部に浮
遊物の濃縮層が形成される。そして、このa綿層は、適
宜、掻取られて原液と分遣されるものであるが、この一
連のa縮分離操作過程において、この発明では、陽極板
の回転周辺部分に臨ませて、その表面の付着物の掻取装
置が設けであるので、その表面部に汚れや気泡が残溜す
ることがな(、極面が常に清浄で高い電解能力を維持す
る。すなわち、陽極板の表面には酸素が発生し、この酸
素が極板と反応して酸化物を造シ、通電を阻害するので
あるが、この酸化物を除去することができるのである。
"Function" The device according to the present invention is configured as described above, and has two functions:
Therefore, when passed through the electrode plate, the electric current on the temporary surface is
Fine bubbles of hydrogen, oxygen, etc. are generated, and when these bubbles float to the surface, they adhere to floating substances in the stock solution and float, forming a concentrated layer of floating substances on the liquid surface. This a-cotton layer is appropriately scraped off and separated from the undiluted solution, but in this series of a-condensation separation operations, in the present invention, the Since the device is equipped with a device to scrape off deposits on the surface, dirt and air bubbles will not remain on the surface (and the electrode surface will always be clean and maintain high electrolytic capacity. In other words, the surface of the anode plate Oxygen is generated, and this oxygen reacts with the electrode plates to form oxides, which obstruct the conduction of electricity, but this oxide can be removed.

また、陽極板が回転しているので、正、負の極板間の原
液が流動し、浮遊物を停滞させることなく、浮上せしめ
ることができる。
Furthermore, since the anode plate is rotating, the undiluted solution flows between the positive and negative electrode plates, allowing floating objects to float without being stagnant.

「実施例」 これを図面に基づいて具体的に説明すれば、第1図にお
いて、符号1は電解槽、2は電解槽に多数並列固定した
陰極板である。3は、電解槽1に支架した回転軸に櫛歯
状に多数並列したvk電極板、それぞれが上述の陰極板
2の中間に位置して回転できるように設けである。符号
4は、陽極板3の表面部に臨ませて設けたスクレーバで
、bす、また、5は浮上物掻取用のスキマである。6は
浮上物移送用の)?7.7は分離水の取出口、8はドレ
ン抜きである。尚、第2図に示すものは、陽極板3の半
体を液浸させ、スクレーバ4を気中に設けた一例である
``Example'' This will be explained in detail based on the drawings. In FIG. 1, reference numeral 1 denotes an electrolytic cell, and 2 denotes a large number of cathode plates fixed in parallel to the electrolytic cell. Reference numeral 3 denotes a large number of vk electrode plates arranged in parallel in a comb-teeth shape on a rotating shaft supported on the electrolytic cell 1, each of which is provided so as to be rotatable while being located in the middle of the cathode plate 2 described above. Reference numeral 4 is a scraper provided facing the surface of the anode plate 3, and 5 is a gap for scraping floating objects. 6 is for transporting floating objects)? 7.7 is a separated water outlet, and 8 is a drain. In addition, what is shown in FIG. 2 is an example in which half of the anode plate 3 is immersed in liquid and the scraper 4 is provided in the air.

このように構成した装置で、陽極板3を回転させつつ連
成すると、電極板部に発生する気泡によって、原液中の
浮遊物は浮上し、液面部にam層を形成する。そして、
この$縮された浮遊物は、スキマ5によって掻取り、ト
フフ6を経て取出すことができる。以上の浮遊物の製着
取出し操作において、この発明では、陽極板3の表面に
はスクレーバ4が摺接して、その表面の汚れを除去する
ので、電解能力を低下させることがなく、また、陽極板
3が回転しているので、正、負の極板間の原液が流動す
る。従って、極板間に浮遊物や気泡が停滞することがな
く、電解放電を阻害しないとともに、浮遊物を円滑に浮
上させて、原液と分離することができる。
When the anode plate 3 is connected while being rotated in the apparatus configured as described above, floating matter in the stock solution floats to the surface due to air bubbles generated in the electrode plate portion, and an am layer is formed on the liquid surface portion. and,
This reduced floating material can be scraped off by a skimmer 5 and taken out via a tofu 6. In the above-described operation for producing and removing floating substances, in the present invention, the scraper 4 comes into sliding contact with the surface of the anode plate 3 to remove dirt on the surface, so that the electrolytic ability is not reduced, and the anode Since the plate 3 is rotating, the stock solution flows between the positive and negative electrode plates. Therefore, floating objects and bubbles do not remain between the electrode plates, do not impede electrolytic discharge, and floating objects can be smoothly floated and separated from the stock solution.

「発明の効果」 以上の説明で明らかなように、この発明は、汚泥等の電
解′a縮表装置おいて、気泡の発生する陽極板を陰極板
に対して回転可動するように設けて、その表面部の汚れ
を除去するためのスフv −°パを設けることによって
、常時、陽極板の表面を清浄に保って、電解効率を低下
させることがなく、また、回転する陽極板によって、正
、負の極板間において、原液を流動させることによって
、極板間に気泡や浮遊物が停滞するのを防止して、これ
らを円滑に浮上させるとともに、放電効果を阻害するの
を防止し得て、濃縮効率を格段に高め得るものである。
"Effects of the Invention" As is clear from the above description, the present invention provides an electrolytic reduction apparatus for sludge, etc., in which an anode plate on which air bubbles are generated is provided so as to be rotatable relative to a cathode plate. By providing a wiper to remove dirt from the surface, the surface of the anode plate can be kept clean at all times without reducing the electrolytic efficiency. By flowing the undiluted solution between the negative electrode plates, it is possible to prevent air bubbles and floating objects from stagnation between the electrode plates, allow them to float smoothly, and prevent them from interfering with the discharge effect. Therefore, the concentration efficiency can be greatly improved.

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

修1図は、この発明を施した浮上濃縮装置の概略の縦断
側面図、第2図は、同じく他の実施例の縦断側面図であ
る。 符号説明 1、電解槽   2.陰極板   3.陽極板4、 ス
クレーバ   5. スキマ
Fig. 1 is a schematic longitudinal sectional side view of a flotation concentration device according to the present invention, and Fig. 2 is a longitudinal sectional side view of another embodiment. Code explanation 1, electrolytic cell 2. Cathode plate 3. Anode plate 4, scraper 5. gap

Claims (3)

【特許請求の範囲】[Claims] (1)電解槽1内に多数の陰極板2を並列するとともに
、これら陰極板2の中間には、電解槽1に支架した回転
軸に設けた陽極板3を相対向させて設け、この陽極板3
の回転周返部分に臨ませてスクレーパ4を設け、さらに
、槽内液面部分に浮上物の掻取装置5を設けてなる汚泥
等の浮上濃縮装置。
(1) A large number of cathode plates 2 are arranged in parallel in an electrolytic cell 1, and an anode plate 3 provided on a rotating shaft supported on the electrolytic cell 1 is provided between these cathode plates 2 so as to face each other. Board 3
A flotation concentration device for sludge, etc., which is provided with a scraper 4 facing the rotating part of the tank, and further provided with a scraping device 5 for floating matter at the liquid level in the tank.
(2)上記陽極板3が液中に没入させてある特許請求の
範囲第(1)項記載の汚泥等の浮上濃縮装置。
(2) A flotation concentration device for sludge, etc., as set forth in claim (1), wherein the anode plate 3 is immersed in a liquid.
(3)上記陽極板3の半体が液没させてある特許請求の
範囲第(1)項記載の汚泥等の浮上濃縮装置。
(3) A flotation concentration device for sludge, etc., as set forth in claim (1), wherein half of the anode plate 3 is submerged in liquid.
JP61070085A 1986-03-28 1986-03-28 Apparatus for flotation concentration of sludge Granted JPS62227493A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61070085A JPS62227493A (en) 1986-03-28 1986-03-28 Apparatus for flotation concentration of sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61070085A JPS62227493A (en) 1986-03-28 1986-03-28 Apparatus for flotation concentration of sludge

Publications (2)

Publication Number Publication Date
JPS62227493A true JPS62227493A (en) 1987-10-06
JPH0331118B2 JPH0331118B2 (en) 1991-05-02

Family

ID=13421345

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61070085A Granted JPS62227493A (en) 1986-03-28 1986-03-28 Apparatus for flotation concentration of sludge

Country Status (1)

Country Link
JP (1) JPS62227493A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991013029A1 (en) * 1990-02-28 1991-09-05 Wilfred Anthony Murrell Water cleaning system
JP2005144311A (en) * 2003-11-14 2005-06-09 Hitachi Kiden Kogyo Ltd Sludge electrolyzer
CN105565438A (en) * 2016-03-11 2016-05-11 上海丁香环境科技有限公司 Automatic scale-scrapping type water treatment device
CN106006864A (en) * 2016-06-27 2016-10-12 南京师范大学 Modular rotation parallel multi-disc type electric flocculation device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991013029A1 (en) * 1990-02-28 1991-09-05 Wilfred Anthony Murrell Water cleaning system
JP2005144311A (en) * 2003-11-14 2005-06-09 Hitachi Kiden Kogyo Ltd Sludge electrolyzer
JP4511820B2 (en) * 2003-11-14 2010-07-28 株式会社日立プラントテクノロジー Sludge electrolyzer
CN105565438A (en) * 2016-03-11 2016-05-11 上海丁香环境科技有限公司 Automatic scale-scrapping type water treatment device
CN106006864A (en) * 2016-06-27 2016-10-12 南京师范大学 Modular rotation parallel multi-disc type electric flocculation device

Also Published As

Publication number Publication date
JPH0331118B2 (en) 1991-05-02

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