JPH0433484B2 - - Google Patents
Info
- Publication number
- JPH0433484B2 JPH0433484B2 JP62090029A JP9002987A JPH0433484B2 JP H0433484 B2 JPH0433484 B2 JP H0433484B2 JP 62090029 A JP62090029 A JP 62090029A JP 9002987 A JP9002987 A JP 9002987A JP H0433484 B2 JPH0433484 B2 JP H0433484B2
- Authority
- JP
- Japan
- Prior art keywords
- side electrode
- cathode side
- substances
- electrode
- dehydrator
- 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 - Lifetime
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/24—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using an endless pressing band
- B30B9/241—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using an endless pressing band co-operating with a drum or roller
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Sludge (AREA)
Description
〔産業上の利用分野〕
この発明は、例えば下水処理場に発生した余剰
汚泥,あるは食品その他の工業分野で発生するス
ラリー状物質の泥漿を被脱水処理物として、この
被脱水処理物を電気浸透作用により脱水処理する
電気浸透式脱水機に関する。
〔従来の技術〕
頭記した電気浸透式脱水機に付いては、例えば
特開昭60−25597号公報にて各種方式のものが開
示れており、ここでまず第3図により従来におけ
る回転ドラム型連続処理式の電気浸透式脱水機の
構成概要を説明する。図においては、1はその外
周面上に耐電食性高い材料で作られた陽極側電極
1aを被着した回転ドラムであり、該回転ドラム
1は図示されてない架台に軸受を介して軸支され
ている。またこの回転ドラム1の周域一部に対向
してエドレス構造のフイルタベルト2,および該
フイルタベルト2と重ね合わせた陰極電極を兼ね
るキヤタピラ構造の金属製プレスコンベア3がス
プロケツト4a〜4dの間に張架されており、フ
イルタベルト2と回転ドラム1との対向面との間
に入口から出口に向けて電極間の間隙が漸次縮減
する泥漿圧搾通路5を画成している。またフイル
タベルト2,プレスコンベア3を介して前記汚泥
圧搾通路5の下方には系外の排水路に通じる濾水
受皿6が設置されている。
ここで前記スプロケツトには駆動モータ7が伝
動結合され、また泥漿圧搾通路5に対しその入口
側には汚泥供給ホツパ8,出口側にはフイルタベ
ルト2に対向して汚泥の脱水ケーを剥離回収する
スクレーパ9が配備され、さらに前記プレスコン
ベア3に対し泥漿圧搾通路5の背後域にはプレス
コンベアの周面に沿つてプレス装置10が配備さ
れている。なお11はプレス装置10の取付け位
置調整用ボルト、12は油圧シリンダある。一
方、前記した回転ドラム1の軸端に取付けた給電
用のスリツプリング1bと陰極側電極であるプレ
スコンベア3と接するスプロケツト4aの支軸と
の間には給電ブラシ13を介して直流電源装置1
4が接続されている。
上記の構成で駆動モータ7を回転し、かつ電源
装置14より陽極側電極と陰極側電極との間に直
流電圧を印加した状態で、ホツパ8を通じて泥漿
圧搾通路5内へ被脱水処理物である泥漿15を供
給すると、泥漿15は回転ドラム1とフイルタベ
ルト2との間に挟まれた状態で汚泥圧搾通路内を
出口側に向けて矢印P方向に搬送され、かつこの
搬送行程で泥漿15には機械的な圧搾力に加え
て、対向電極間に形成された電場により電気浸透
作用が加わるようになる。この電気浸透作用によ
り泥漿15の懸濁粒子は直流電界の下で陽極側に
移動する力を受けるのに対し、汚泥15の含有水
は正に帯電して陰極側に流動するとともに、前記
の機械的な圧搾力も加わつてフイルタベルト2を
透過して脱水濾過され、さらにプレスコンベア3
の板面に形成された排水路より濾水受皿6に流下
して系外に排水処理される。一方、通路5内で脱
水処理された泥漿15は低含水率となつてケーキ
化され、その脱水ケーキ16が通路5の出口側か
らスクレーパ9を経て分離回収されて焼却処分,
ないしはコンポスト化し肥料として再利用され
る。
〔発明が解決しようとする問題点〕
ところで、上記構成の電気浸透式脱水機で下水
汚泥等を脱水処理した場合には運転の経過ととも
に次記のような問題点が派生する。
すなわち下水処理場で発生した汚泥を被脱水処
理物として前記電気浸透式脱水機で脱水処理運転
したところ、運転時間の経過とともに陰極側電極
であるプレスコンベアの表面に白色の固形物質が
析出生成し、かつこの固形物質が層状を成して付
着堆積することが観察された。しかもこの固形物
質の付着量が増すにしたがつて電気浸透式脱水機
の消費電力が増加するとともに、プレスコンベア
の排水路が付着物質で閉塞されて濾液の排水が円
滑に行われなくなる等して脱水効率が大幅に低下
することが確認された。
そこで発明者は前記した白色の生成物質を採取
し、その化学成分に付いてけい光X線分析装置に
より分析したところ、次表のような定量分析結果
を得た。
[Industrial Field of Application] This invention uses, for example, excess sludge generated in sewage treatment plants, or sludge of slurry-like substances generated in food and other industrial fields as a material to be dehydrated, and the dewatered material is subjected to electricity treatment. This invention relates to an electroosmotic dehydrator that performs dehydration through osmosis. [Prior Art] Regarding the above-mentioned electroosmotic dewatering machine, various types are disclosed in, for example, Japanese Patent Application Laid-Open No. 60-25597. An overview of the configuration of a continuous process type electroosmotic dehydrator will be explained. In the figure, 1 is a rotating drum having an anode side electrode 1a made of a material with high resistance to electrolytic corrosion adhered to its outer peripheral surface, and the rotating drum 1 is supported by a mount (not shown) via a bearing. ing. Further, a filter belt 2 with an endless structure faces a part of the circumference of the rotating drum 1, and a metal press conveyor 3 with a caterpillar structure, which also serves as a cathode electrode and overlapped with the filter belt 2, is installed between the sprockets 4a to 4d. A slurry squeezing passage 5 is defined between the filter belt 2 and the opposing surface of the rotating drum 1, in which the gap between the electrodes gradually decreases from the inlet to the outlet. Further, below the sludge pressing passage 5 via the filter belt 2 and the press conveyor 3, a filtrate receiving tray 6 is installed which communicates with a drainage channel outside the system. Here, a drive motor 7 is transmission-coupled to the sprocket, and a sludge supply hopper 8 is provided on the inlet side of the slurry squeezing passage 5, and a sludge dewatering case is separated and collected on the outlet side facing the filter belt 2. A scraper 9 is provided, and a press device 10 is provided along the circumferential surface of the press conveyor 3 in an area behind the slurry squeezing passage 5 with respect to the press conveyor 3. Note that 11 is a bolt for adjusting the mounting position of the press device 10, and 12 is a hydraulic cylinder. On the other hand, a DC power supply 1 is connected via a power supply brush 13 between the power supply slip ring 1b attached to the shaft end of the rotating drum 1 and the support shaft of the sprocket 4a which is in contact with the press conveyor 3, which is the cathode side electrode.
4 are connected. With the above configuration, the drive motor 7 is rotated, and a DC voltage is applied between the anode side electrode and the cathode side electrode from the power supply device 14, and the material to be dehydrated is transferred into the slurry squeezing passage 5 through the hopper 8. When the slurry 15 is supplied, the slurry 15 is conveyed in the direction of arrow P toward the exit side in the sludge pressing passage while being sandwiched between the rotating drum 1 and the filter belt 2, and in this conveyance process, the slurry 15 is In addition to the mechanical squeezing force, an electroosmotic effect is applied due to the electric field formed between the opposing electrodes. Due to this electroosmotic action, the suspended particles in the sludge 15 receive a force that moves them toward the anode under a DC electric field, whereas the water contained in the sludge 15 is positively charged and flows toward the cathode, and the water contained in the sludge 15 is positively charged and flows toward the cathode. The compressing force is also applied, the filter belt 2 passes through the filter belt 2, the water is dehydrated and filtered, and then the press conveyor 3
The filtered water flows down to the drain tray 6 from a drainage channel formed on the plate surface and is drained out of the system. On the other hand, the slurry 15 that has been dehydrated in the passage 5 has a low water content and is turned into a cake, and the dehydrated cake 16 is separated and collected from the outlet side of the passage 5 via a scraper 9, and is incinerated.
Or it can be composted and reused as fertilizer. [Problems to be Solved by the Invention] By the way, when sewage sludge or the like is dehydrated using the electroosmotic dehydrator having the above configuration, the following problems arise as the operation progresses. In other words, when sludge generated in a sewage treatment plant was used as a dewatering object and the electroosmotic dehydrator was operated for dehydration, a white solid substance was deposited on the surface of the press conveyor, which is the cathode side electrode, as the operating time progressed. , and this solid material was observed to be deposited in layers. Moreover, as the amount of solid matter adhering increases, the power consumption of the electroosmotic dewatering machine increases, and the drainage channel of the press conveyor becomes clogged with the adhering material, making it difficult to drain the filtrate smoothly. It was confirmed that the dehydration efficiency was significantly reduced. Therefore, the inventor collected the above-mentioned white product and analyzed its chemical components using a fluorescent X-ray analyzer, and obtained quantitative analysis results as shown in the following table.
【表】【table】
上記問題点を解決するために、この発明によれ
ば陽極側電極と、該陽極電極と相対向し表面に濾
過部材が重ね合わされた陰極側電極との間に、被
脱水処理物としての泥漿を供給し、前記陽極側電
極,陰極側電極間に直流電圧を印加することによ
り電気浸透作用で泥漿の含有水を陰極側に集め、
ここから前記濾過部材,前記陰極側電極を透過し
て濾液を分離排水すると共に、濾過部材上に堆積
した脱水ケーキをケーキ除去手段により除去する
ようにした電気浸透式脱水機において、前記濾過
部材を前記陰極側電極から分離する区間を設け、
該区間内に、前記陰極側電極の前記濾過部材側表
面に析出生成する付着物質の除去手段を備えて構
成するものとする。
〔作用〕
上記構成において、付着物質の除去手段は例え
ば機械的に付着物質を取り除くブラシ形スクレー
パ,高圧水洗浄装置,超音波洗浄装置,薬液洗浄
装置等であり、この付着物質の除去手段を運転中
に随時作動させることにより陰極側電極の表面に
生成した固形の付着物質が除去される。したがつ
て陰極側電極は付着物質が殆ど堆積されてない清
浄状態で使用可能となり、これにより電気浸透式
脱水機を常に高い脱水効率で稼動させることがで
きるようになる。
〔実施例〕
第1図はこの発明の実施例による電気浸透式脱
水機の全体構成図、第2図は付着物質除去手段と
して陰極側電極に対向配備したブラシ形スクレー
パを示したものであり、第3図に対応する同一部
材には同じ符号が付してある。すなわち電気浸透
式脱水機の基本構造は第3図と同様に構成されて
いるに対し、フイルタベルト2の長さがプレスコ
ンベア3よりも長く構成されており、かつその周
回移動経路の途中箇所でフイルタベルト2はプレ
スコンベア3より分離するように補助プーリ1
7,18に張架され、かつこの分離区間でプレス
コンベア3表面,つまり汚泥側に対面する電極面
側には高圧水噴射ノズル19およびブラシ形スク
レーパ20が対向配備されている。ここで高圧水
噴射ノズル19は高圧水をプレスコンベア3の表
面に向けて噴射するように設置され、一方のブラ
シ形スクレーパ20は第2図のようにベース20
aに例えばステンレス製のワイヤ20bの束を植
設した構造のものであり、ワイヤ20bをプレス
コンベア3の表面に当接して装備されている。
かかる構成において、電気浸透式脱水機の運転
に伴つて先述のように陰極側電極であるプレスコ
ンベア3の表面には水酸化カルシユームを多く含
む白色の固形物質が生成して付着するが、この付
着物質はプレスコンベア3の回転に伴い前記した
ブラシ形スクレーパ20により擦り取られ、高圧
洗浄水の噴射により排出される。したがつてプレ
スコンベア3は付着物のない清浄状態で再び汚泥
圧搾通路4の領域に移動し、ここで陰極側電極と
して電気浸透脱水作用に関与するようになる。こ
れにより電気浸透脱水作用の行われる汚泥圧搾通
路4の領域ではプレスコンベア4が清浄な状態で
陰極側電極として高い通電機能を維持し、同時に
フイルタベルト2を透過した濾液を濾液受皿6に
向けて円滑に排水することができる。
なお付着物質の除去手段としては、図示実施例
で採用したブラシ形スクレーパ,高圧水噴射ノズ
ルの他に、プレスコンベア3の周上に水,薬剤等
の洗浄液を満たした超音波発信器を装備の洗浄槽
を配備し、この洗浄槽内にプレスコンベアを通す
ことにより超音波のキヤビテーシヨン作用で電極
面上の付着物質を除去するようにした超音波洗浄
装置、あるいはプレスコンベア3の周上に例えば
10倍程度に希釈した塩酸溶液等の薬液を満たした
洗浄槽を配備し、この洗浄槽内プレスコンベアを
通すことにより、電極面上の付着物質,特にその
主成分である水酸化カルシウムを溶解除去するよ
うにした薬液洗浄装置等を採用することもでき
る。
さらに上記実施例は加圧ドラム型電気浸透式脱
水機への適用例を示したが、図示実施例おける回
転ドラムに変えてエンドレス構造のプレスベルト
を陽極側電極として用いるベルトプレス方式の電
気浸透式脱水機に付いても同様に実施できること
は勿論である。
〔発明の効果〕
以上述べたようにこの発明によれば、電気浸透
式脱水機に対し、濾過部材を陰極側電極から分離
する区間を設け、この区間内に、陰極側電極の濾
過部材側表面に析出生成する付着物質の除去手段
を備えて構成したことにより、電気浸透脱水機の
運転に伴つて陰極側電極の表面に生成する付着物
質を除去して清浄な状態を維持することができ、
これにより不要な電力損失の増加,濾液の排水機
能の低下を未然に防止して電気浸透脱水機を高い
脱水効率で稼動運転させることができる。
In order to solve the above problems, according to the present invention, a slurry as a material to be dehydrated is placed between an anode side electrode and a cathode side electrode, which faces the anode electrode and has a filtration member superimposed on its surface. By applying a DC voltage between the anode side electrode and the cathode side electrode, the water contained in the slurry is collected on the cathode side by electroosmosis,
In an electroosmotic dehydrator, the filtrate is separated and drained by passing through the filtration member and the cathode side electrode, and the dehydrated cake deposited on the filtration member is removed by a cake removing means. Providing a section separated from the cathode side electrode,
The section is provided with a means for removing deposited substances deposited on the filtering member side surface of the cathode side electrode. [Function] In the above configuration, the adhering substance removing means is, for example, a brush-type scraper that mechanically removes the adhering substances, a high-pressure water cleaning device, an ultrasonic cleaning device, a chemical cleaning device, etc. The solid adhesion substance generated on the surface of the cathode side electrode is removed by operating the unit as needed. Therefore, the cathode side electrode can be used in a clean state with almost no deposits of deposits, and as a result, the electroosmotic dehydrator can be operated with high dehydration efficiency at all times. [Embodiment] Fig. 1 is an overall configuration diagram of an electroosmotic dehydrator according to an embodiment of the present invention, and Fig. 2 shows a brush-type scraper disposed opposite to the cathode side electrode as a means for removing adhered substances. Identical parts corresponding to FIG. 3 are given the same reference numerals. In other words, the basic structure of the electroosmotic dewatering machine is similar to that shown in Fig. 3, but the length of the filter belt 2 is longer than that of the press conveyor 3, and the length of the filter belt 2 is longer than that of the press conveyor 3. The filter belt 2 is separated from the press conveyor 3 by an auxiliary pulley 1.
7 and 18, and in this separation section, a high-pressure water injection nozzle 19 and a brush-type scraper 20 are arranged facing each other on the surface of the press conveyor 3, that is, on the electrode surface side facing the sludge side. Here, the high-pressure water injection nozzle 19 is installed to inject high-pressure water toward the surface of the press conveyor 3, and one brush-type scraper 20 is installed on the base 20 as shown in FIG.
The press conveyor 3 has a structure in which a bundle of wires 20b made of stainless steel, for example, is implanted in the press conveyor 3, and the wires 20b are placed in contact with the surface of the press conveyor 3. In this configuration, as the electroosmotic dehydrator operates, a white solid substance containing a large amount of calcium hydroxide is generated and adhered to the surface of the press conveyor 3, which is the cathode side electrode, as described above. As the press conveyor 3 rotates, the substance is scraped off by the brush-type scraper 20 described above, and is discharged by jetting high-pressure cleaning water. The press conveyor 3 is therefore moved again in a clean state free of deposits to the area of the sludge squeezing channel 4, where it takes part in the electroosmotic dewatering action as a cathode electrode. As a result, in the area of the sludge squeezing passage 4 where electroosmotic dehydration is performed, the press conveyor 4 maintains a high current-carrying function as a cathode side electrode in a clean state, and at the same time directs the filtrate that has passed through the filter belt 2 to the filtrate receiving tray 6. Drainage can be done smoothly. In addition to the brush-type scraper and high-pressure water jet nozzle employed in the illustrated embodiment, as a means for removing adhered substances, an ultrasonic transmitter equipped with a cleaning liquid such as water or chemicals on the circumference of the press conveyor 3 is used. An ultrasonic cleaning device is equipped with a cleaning tank, and a press conveyor is passed through the cleaning tank to remove substances adhered to the electrode surface by the cavitation action of ultrasonic waves.
A cleaning tank filled with a chemical solution such as a 10-fold diluted hydrochloric acid solution is installed, and by passing it through a press conveyor inside the cleaning tank, substances adhering to the electrode surface, especially calcium hydroxide, which is its main component, are dissolved and removed. It is also possible to employ a chemical cleaning device or the like designed to do this. Furthermore, although the above embodiment shows an example of application to a pressure drum type electroosmotic dehydrator, a belt press type electroosmotic dehydrator uses an endless press belt as the anode side electrode instead of the rotating drum in the illustrated embodiment. Of course, the same method can be applied to a dehydrator. [Effects of the Invention] As described above, according to the present invention, an electroosmotic dehydrator is provided with a section separating the filtration member from the cathode side electrode, and within this section, the surface of the cathode side electrode on the filtration member side is By being configured with a means for removing adherent substances that are deposited and generated on the surface of the cathode side electrode, it is possible to maintain a clean state by removing the adhered substances that are generated on the surface of the cathode side electrode as the electroosmotic dehydrator is operated.
This allows the electroosmotic dehydrator to operate with high dewatering efficiency by preventing unnecessary increases in power loss and deterioration of the filtrate drainage function.
第1図は本発明実施例による電気浸透式脱水機
の全体構成図、第2図は第1図おける付着物除去
手段として例示したブラシ形スクレーパの斜視構
造図、第3図は従来おける電気浸透式脱水機の全
体構成図である。各図において、
1……回転ドラム、1a……陰極側電極、2…
…フイルタベルト、3……陰極側電極を兼ねたプ
レスコンベア、4……汚泥圧搾通路、14……直
流電源、15……汚泥、16……脱水ケーキ、1
9……高圧水噴射ノズル、20……ブラシ形スク
レーパ。
Fig. 1 is an overall configuration diagram of an electroosmotic dehydrator according to an embodiment of the present invention, Fig. 2 is a perspective structural diagram of a brush-type scraper exemplified as a deposit removal means in Fig. 1, and Fig. 3 is a conventional electroosmotic dehydrator. FIG. 1 is an overall configuration diagram of a type dehydrator. In each figure, 1... Rotating drum, 1a... Cathode side electrode, 2...
... Filter belt, 3 ... Press conveyor that also serves as a cathode side electrode, 4 ... Sludge squeezing passage, 14 ... DC power supply, 15 ... Sludge, 16 ... Dehydrated cake, 1
9...High pressure water jet nozzle, 20...Brush type scraper.
Claims (1)
に濾過部材が重ね合わされた陰極側電極との間
に、被脱水処理部としての泥漿を供給し、前記陽
極側電極,陰極側電極間に直流電圧を印加するこ
とにより電気浸透作用で泥漿の含有水を陰極側に
集め、ここから前記濾過部材,前記陰極側電極を
透過して濾液を分離排水すると共に、濾過部材上
に堆積した脱水ケーキをケーキ除去手段により除
去するようにした電気浸透式脱水機において、前
記濾過部材を前記陰極側電極から分離する区間を
設け、該区間内に、前記陰極側電極の前記濾過部
材側表面に析出生成する付着物質の除去手段を備
えたことを特徴とする電気浸透式脱水機。 2 特許請求の範囲第1項記載の電気浸透式脱水
機において、付着物質の除去手段が電極面に当接
配備して付着物質を機械的に除去するブラシ形ス
クレーパであることを特徴とする電気浸透式脱水
機。 3 特許請求の範囲第1項記載の電気浸透式脱水
機において、付着物質の除去手段が電極面に高圧
水を噴して付着物質を除去する高圧水洗浄装置で
あることを特徴とする電気浸透式脱水機。 4 特許請求の範囲第1項記載の電気浸透式脱水
機において、付着物質の除去手段が超音波のキヤ
ビテーシヨン作用により電極面の付着物質を除去
する超音波洗浄装置であることを特徴とする電気
浸透式脱水機。 5 特許請求の範囲第1項記載の電気浸透式脱水
機において、付着物質の除去手段が電極面の付着
物質を薬剤により溶解除去する薬液洗浄装置であ
ることを特徴とする電気浸透式脱水機。[Scope of Claims] 1. A slurry serving as a dehydration treatment portion is supplied between an anode side electrode and a cathode side electrode which faces the anode side electrode and has a filtration member superimposed on its surface, and the anode side By applying a DC voltage between the electrode and the cathode side electrode, the water containing the slurry is collected on the cathode side by electroosmosis, and from there, it passes through the filtration member and the cathode side electrode to separate and drain the filtrate. In an electroosmotic dehydrator in which a dehydrated cake deposited on a member is removed by a cake removing means, a section is provided to separate the filter member from the cathode side electrode, and within the section, the filter member is separated from the cathode side electrode. An electroosmotic dehydrator characterized by being equipped with a means for removing deposited substances deposited on the surface of a filter member. 2. The electroosmotic dehydrator according to claim 1, wherein the means for removing adhered substances is a brush-type scraper that is placed in contact with the electrode surface to mechanically remove the adhered substances. Osmotic dehydrator. 3. The electroosmotic dehydrator according to claim 1, wherein the means for removing adhered substances is a high-pressure water cleaning device that sprays high-pressure water onto the electrode surface to remove the adhered substances. Type dehydrator. 4. The electroosmotic dehydrator according to claim 1, wherein the means for removing adhering substances is an ultrasonic cleaning device that removes adhering substances from the electrode surface by the cavitation action of ultrasonic waves. Type dehydrator. 5. The electroosmotic dehydrator according to claim 1, wherein the means for removing adhering substances is a chemical cleaning device that dissolves and removes adhering substances on the electrode surface using a chemical.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62090029A JPS63256112A (en) | 1987-04-13 | 1987-04-13 | Electroosmotic dehydrator |
| EP87112336A EP0286714B1 (en) | 1987-04-13 | 1987-08-25 | Electroosmotic dewaterer |
| DE8787112336T DE3785668T2 (en) | 1987-04-13 | 1987-08-25 | DEVICE FOR ELECTROOSMOTIC DRAINAGE. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62090029A JPS63256112A (en) | 1987-04-13 | 1987-04-13 | Electroosmotic dehydrator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63256112A JPS63256112A (en) | 1988-10-24 |
| JPH0433484B2 true JPH0433484B2 (en) | 1992-06-03 |
Family
ID=13987247
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62090029A Granted JPS63256112A (en) | 1987-04-13 | 1987-04-13 | Electroosmotic dehydrator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63256112A (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000202497A (en) * | 1999-01-11 | 2000-07-25 | Nkk Corp | Sludge filtration and concentration equipment |
| JP2006130475A (en) * | 2004-11-09 | 2006-05-25 | Torishima Pump Mfg Co Ltd | Sludge solubilization processor |
| KR100926261B1 (en) * | 2009-05-22 | 2009-11-12 | (주)동일캔바스엔지니어링 | Electrode cleaning device of electro-osmotic sludge reduction device |
| KR101070296B1 (en) * | 2011-06-27 | 2011-10-06 | 주식회사 화인 | Drum-type electric penetration dehydrator saves electricity by narrow gap between anode and cathode |
| JP2014188503A (en) * | 2013-03-28 | 2014-10-06 | Kurita Water Ind Ltd | Electric osmosis dehydrator and washing method of the same |
| CN105036255A (en) * | 2015-06-25 | 2015-11-11 | 宋萌瑶 | Electrolysis device with automatic scraper |
| CN107213689A (en) * | 2017-07-05 | 2017-09-29 | 宁夏共享机床辅机有限公司 | A kind of bolt connection type drum-type paper tape filter |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5157069A (en) * | 1974-11-14 | 1976-05-19 | Inoue Japax Res | DATSUSUISHORISOCHI |
| JPS6136968A (en) * | 1984-07-30 | 1986-02-21 | Nec Corp | solid-state imaging device |
-
1987
- 1987-04-13 JP JP62090029A patent/JPS63256112A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63256112A (en) | 1988-10-24 |
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