JPH0687925B2 - Electro-osmotic dehydrator electrode - Google Patents

Electro-osmotic dehydrator electrode

Info

Publication number
JPH0687925B2
JPH0687925B2 JP62286684A JP28668487A JPH0687925B2 JP H0687925 B2 JPH0687925 B2 JP H0687925B2 JP 62286684 A JP62286684 A JP 62286684A JP 28668487 A JP28668487 A JP 28668487A JP H0687925 B2 JPH0687925 B2 JP H0687925B2
Authority
JP
Japan
Prior art keywords
electrode
belt
wire
net
sludge
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 - Fee Related
Application number
JP62286684A
Other languages
Japanese (ja)
Other versions
JPH01127012A (en
Inventor
幹昌 山口
正孝 吉田
克雄 伊波
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP62286684A priority Critical patent/JPH0687925B2/en
Publication of JPH01127012A publication Critical patent/JPH01127012A/en
Publication of JPH0687925B2 publication Critical patent/JPH0687925B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、下水処理場等で発生する汚泥の脱水処理に
用いる電気浸透式脱水機の電極構造に関する。
TECHNICAL FIELD The present invention relates to an electrode structure of an electroosmotic dehydrator used for dehydrating sludge generated in a sewage treatment plant or the like.

〔従来の技術〕[Conventional technology]

頭記電気浸透式脱水機の代表例として第3図に示すよう
なベルトプレス型のものが従来より知られている。図に
おいて、1は汚泥供給側に配備したホッパ、2はスラリ
通路3に沿って一対のローラ4の間に張架された陰極側
電極を兼ねる搬送ベルト、5は搬送ベルト2の駆動モー
タ、6はスラリ通路3を隔てて前記ベルト2に対向する
よう一対のローラ7の間に張架された陽極側電極を兼ね
るプレスベルト、8は前記陽極側電極,陰極側電極を兼
ねたベルト6,2に電圧を印加する直流電源である。また
前記各ベルト2,6には、耐蝕性の高い金属,カーボン等
の導電材料で作られた排水,ガス抜き溝を有するキャタ
ピラ形ベルト、ないし導電線材で網状に織ったネット状
ベルトが採用されている。
As a typical example of the above-mentioned electroosmotic dehydrator, a belt press type as shown in FIG. 3 has been conventionally known. In the figure, 1 is a hopper arranged on the sludge supply side, 2 is a conveyor belt which also extends between a pair of rollers 4 along a slurry passage 3, and also serves as a cathode side electrode, 5 is a drive motor for the conveyor belt 2, and 6 The reference numeral 8 designates a press belt which is stretched between a pair of rollers 7 so as to face the belt 2 across the slurry passage 3 and which also serves as an anode side electrode, and 8 designates belts 6 and 2 which also serve as the anode side electrode and the cathode side electrode. It is a DC power supply that applies a voltage to the. For each of the belts 2 and 6, a drain belt made of a conductive material such as a metal having high corrosion resistance or carbon, a caterpillar belt having a degassing groove, or a net belt woven in a mesh shape with a conductive wire material is adopted. ing.

かかる電気浸透式脱水機の脱水作用は周知であり、電源
8より各ベルト2,6に電圧を印加し、駆動モータ5で搬
送ベルト2を駆動した状態でホッパ1よりスラリ通路3
へ被脱水処理物である汚泥9を供給することにより、汚
泥はスラリ通路3で入口側から出口側へベルト搬送され
る過程で搬送ベルト2とプレスベルト6との間にサンド
ウィッチ状に挟まれて圧搾力を受けるととに、対向電極
間に形成された電場に基づく電気浸透作用が加わるよう
になる。したがって汚泥中の含まれている水分は正に帯
電して陰極側に流動し、圧搾力により搬送ベルト2を透
過して系外に排水される。これにより汚泥9は脱水さ
れ、スラリ通路3の出口より脱水ケーキ10となって排出
される。また前記の電気浸透に伴って汚泥中の成分が電
気分解して発生したガスも同時にベルト2,6を透過して
放出される。
The dehydration action of such an electroosmotic dehydrator is well known, and a voltage is applied to each of the belts 2 and 6 from a power source 8 so that the drive belt 5 is driven by the drive motor 5 so that the slurry passage 3 is conveyed from the hopper 1.
By supplying the sludge 9 to be dehydrated to the sludge, the sludge is sandwiched between the conveyor belt 2 and the press belt 6 in the process of being conveyed from the inlet side to the outlet side in the slurry passage 3. Upon receiving the squeezing force, the electroosmotic action based on the electric field formed between the counter electrodes is applied. Therefore, the water contained in the sludge is positively charged, flows toward the cathode side, and is transmitted through the conveyor belt 2 by the pressing force to be discharged to the outside of the system. As a result, the sludge 9 is dehydrated, and the dehydrated cake 10 is discharged from the outlet of the slurry passage 3. In addition, the gas generated by the electrolysis of the components in the sludge accompanying the electroosmosis is also transmitted through the belts 2 and 6 and is released.

なお、前記脱水工程での脱水進行に伴う汚泥9の減容分
を補償してスラリ通路全域で十分の圧搾力を加えるとと
もに、同時にスラリ通路全域で汚泥への良好な通電分布
を得るために、スラリ通路3は入口側よりも出口側で電
極間の通路断面が狭まるようにプレスベルト6が搬送ベ
ルト2に対して傾斜配備されている。また実際の電気浸
透式脱水機では、汚泥の電気抵抗,脱水進行に伴う汚泥
の電気抵抗増加を考慮して実用的にスラリ通路3の入口
側ではベルト間の間隔が10mm前後、出口側では5mm程度
に設定されている。
In addition, in order to compensate for the reduced volume of the sludge 9 due to the progress of dehydration in the dehydration step and apply a sufficient squeezing force in the entire slurry passage, at the same time, to obtain a good distribution of electricity to the sludge in the entire slurry passage, In the slurry passage 3, the press belt 6 is inclined with respect to the conveyor belt 2 so that the passage cross section between the electrodes is narrower on the outlet side than on the inlet side. In an actual electro-osmotic dehydrator, the belt spacing is practically 10 mm on the inlet side of the slurry passage 3 and 5 mm on the outlet side in consideration of the increase in the electrical resistance of sludge and the electrical resistance of sludge accompanying the progress of dehydration. It is set to a degree.

一方、前記のように実際の脱水機ではスラリ通路3を隔
てて対向し合う電極兼用のベルト2と6との間の間隔が
5〜10mm程度の狭い間隔に設定されていることから、長
期運転によりベルト2,6に弛みが生じたり,あるいはベ
ルト2,6を掛けたローラ4,7側での支持構造に撓みが生じ
てベルト間の相対位置がずれたりすると、陽極側のベル
ト6と陰極側のベルト2とが直接接触し合って電気的に
短絡する状態が惹起することががある。しかもこのよう
な電極間の直接接触による短絡が発生するとこの短絡部
分に大きな電流が集中的に流れて正常な電気浸透脱水が
行えなくなる他、電源側に障害を与えたり電極を兼ねた
ベルト自身も破損される事態を招くおそれがある。
On the other hand, as described above, in the actual dehydrator, the interval between the electrode-use belts 2 and 6 that face each other across the slurry passage 3 is set to a narrow interval of about 5 to 10 mm, and thus long-term operation is not possible. If the belts 2 and 6 are loosened due to this, or if the supporting structure on the rollers 4 and 7 side on which the belts 2 and 6 are hung is deflected and the relative positions between the belts are displaced, the belt 6 on the anode side and the cathode side The belt 2 on the side may directly contact with each other to cause an electrical short circuit. Moreover, when such a short circuit occurs due to direct contact between the electrodes, a large current flows intensively in this short circuit section, and normal electroosmotic dehydration cannot be performed.In addition, the belt itself that also acts as an electrode and also acts as an electrode It may cause damage.

このための安全対策として、従来では第4図のようにス
ラリ通路内で搬送ベルト2の表面に沿って絶縁材のロー
プ11を多数条張り巡らしたり、あるいは第5図のように
ベルト2,6の表面に絶縁性のベルト条の濾布12を重ね合
わせ、これによりベルト2,6の排水,排ガス機能を確保
しつつ、不測にベルト2,6同士が直接接触した際に電気
的が短絡が発生するのを防止するようにした方法で対処
している。
As a safety measure for this, conventionally, a large number of ropes 11 made of an insulating material are stretched around the surface of the conveyor belt 2 in the slurry passage as shown in FIG. 4, or the belts 2, 6 are provided as shown in FIG. The filter cloth 12 made of an insulating belt is superposed on the surface of the belt, which ensures the drainage and exhaust gas functions of the belts 2 and 6, and also causes an electrical short circuit when the belts 2 and 6 come into direct contact with each other unexpectedly. We are dealing with it in a way that prevents it from happening.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

ところで第4図,第5図に示した従来の短絡事故防止対
策の構造では次記のような欠点がある。すなわちベルト
2,ないしは6に別な絶縁ロープ11,あるいは絶縁濾布12
を付加した構造では、スラリ通路3を画成するベルト間
の間隔の一部を絶縁ロープ11,絶縁濾布12が占有して電
極面を覆うようになるために、スラリ通路3が空間的に
制限を受ける他,実質的に電極間の電気抵抗が増大して
電気浸透脱水に要する消費電力量が増加する。しかも単
にベルトにロープ,濾布等を重ね合わせただけでは、運
転の途中で外力によりベルトとロープ,濾布の間がずれ
たり偏ったりして、遂にはベルトから脱落してしまう事
態になることがあり、これを防止するための保持構造が
複雑でその保守管理も厄介である。
By the way, the conventional structure for preventing short circuit accidents shown in FIGS. 4 and 5 has the following drawbacks. Ie belt
Insulation rope 11 or insulation filter cloth 12 for 2 or 6
In the structure in which is added, since the insulating rope 11 and the insulating filter cloth 12 occupy a part of the interval between the belts defining the slurry passage 3 to cover the electrode surface, the slurry passage 3 is spatially separated. In addition to being limited, the electrical resistance between the electrodes substantially increases and the power consumption required for electroosmotic dehydration increases. Moreover, if the rope, filter cloth, etc. are simply superposed on the belt, the belt, the rope, and the filter cloth may be displaced or biased due to external force during operation, and eventually the belt may fall off. However, the maintenance structure for preventing this is complicated and its maintenance is troublesome.

この発明は上記の点にかんがみ成されたものであり、そ
の目的は脱水進行に伴う排水,排ガス,および汚泥粒子
の捕集機能をいささかも損なわず、しかも従来方式のよ
うに電極兼用のベルト間に短絡防止用の絶縁部材を特別
に介在付設させることなく、ベルトの弛み等に起因して
対向電極が直接接触した場合でも電気的な短絡の発生を
確実に防止できるようにした電気浸透脱水機の電極を提
供することにある。
The present invention has been conceived in view of the above points, and its purpose is not to impair the collection function of wastewater, exhaust gas, and sludge particles accompanying the progress of dehydration in any way, and, moreover, as in the conventional method, the belt between electrodes also serves as a belt. An electro-osmotic dehydrator that can reliably prevent the occurrence of an electrical short even if the counter electrode comes into direct contact due to belt slack, etc. To provide the electrode of.

〔問題点を解決するための手段〕[Means for solving problems]

上記問題点を解決するために、この発明によれば、導電
線材,絶縁線材の一方の縦糸,他方を横糸として織成さ
れたネットとして成り、かつ少なくともスラリ通路との
対向面側で導電線材がネット面へ突き出さないように絶
縁線材の内側に織り込んで構成するものとする。
In order to solve the above-mentioned problems, according to the present invention, a conductive wire material, a net woven with one warp thread of the insulating wire material and the other as a weft thread, and the conductive wire material is provided at least on the side facing the slurry passage. It shall be woven into the inside of the insulated wire so that it does not stick out to the net surface.

〔作用〕[Action]

上記の構成で、導電線材は耐蝕性の高い金属線材,絶縁
線材は合成繊維の糸であり、かつ直線状に伸張した金属
線材を横糸,絶縁線材を縦糸にしてベルト状装置を構成
したものである。
With the above structure, the conductive wire is a metal wire having high corrosion resistance, the insulating wire is a synthetic fiber thread, and the belt-shaped device is configured by using the linearly stretched metal wire as the weft thread and the insulating wire as the warp thread. is there.

したがって電極を兼ねた汚泥搬送ベルト,プレスベルト
に上記のベルト状ネットを採用することにより、運転の
最中にベルトの弛み等が原因で陽極側と陰極側のベルト
同士が直接接触した場合でも、ネットを構成する絶縁線
材同士が触れ合うだけで導電線材同士が接触することが
なく電気的な短絡発生を防止できる。またネット面上で
は導電線材の大半域が露呈しており、電気浸透脱水工程
ではこの導電線材の露呈部分と汚泥との接触により汚泥
への必要な通電を十分確保される。しかもこのネットは
導電線材と絶縁線材とが一体となるように織られている
ものであり、外力により導電線材と絶縁線材とがばらば
らになることも無く、かつその織り目密度を適宜に選定
することにより良好な排水,排ガス,および汚泥分子の
捕集機能を持たせることができる。
Therefore, by adopting the above belt-shaped net for the sludge transfer belt that also serves as an electrode and the press belt, even when the belts on the anode side and the cathode side directly contact each other due to slack of the belt during operation, It is possible to prevent the occurrence of an electrical short circuit without the conductive wire materials contacting each other simply by contacting the insulating wire materials forming the net. Further, most of the conductive wire is exposed on the net surface, and in the electroosmotic dehydration step, the exposed portion of the conductive wire and the sludge are brought into contact with each other to sufficiently secure the necessary energization to the sludge. Moreover, this net is woven so that the conductive wire and the insulating wire are integrated, and the conductive wire and the insulating wire are not separated by an external force, and the density of the meshes should be appropriately selected. Can provide good drainage, exhaust gas, and sludge molecule collection functions.

〔実施例〕〔Example〕

第1図,第2図は本発明実施例によるベルト状ネットに
編成された電極の構造を示す平面図,断面図であって図
中、13が導電線材,14が絶縁線材で、両者を横糸,縦糸
にして電極を兼ねたベルト状ネット15が織成されてい
る。
1 and 2 are a plan view and a sectional view showing the structure of an electrode knitted into a belt-like net according to an embodiment of the present invention, in which 13 is a conductive wire and 14 is an insulating wire, both of which are weft threads. A belt-like net 15 which is a warp and also serves as an electrode is woven.

ここで発明者が製作した例を述べると、横糸となる導電
線材13には耐蝕性の高いステンレスを材料とする0.17mm
φの細線を7本束ねて撚り合わせた撚り線が、縦糸とな
る絶縁線材14には14デニールのナイロン繊維を15本束ね
た糸を4本撚り合わせたナイロンマルチフィラメント糸
を使用し、かつ横糸の織り密度を31本/1in,縦糸の織り
密度を52本/1inとして導電線材13である横糸を直線状に
伸張した状態で織成して厚さ0.71mmのベルト状ネット15
を製作した。
Here, the example manufactured by the inventor will be described. The conductive wire material 13 serving as the weft thread is made of stainless steel with high corrosion resistance of 0.17 mm.
The twisted wire is made by bundling seven φ fine wires and twisting them. The insulating wire material 14 is a nylon multifilament yarn in which four 14 denier nylon fibers are twisted together and the weft yarn is used. The weaving density of the warp yarns is 31 yarns / in and the warp yarn density is 52 yarns / 1 in.
Was produced.

このようにして織制されたネット15は、第2図の断面で
示すように直線状態に並ぶ導電線材13が芯線となって絶
縁線材14で包み込まれるようにネットの層内中央に織り
込まれており、ネット15の表裏の外面には絶縁線材14が
並んでいて導電線材13がネット面へ突き出すことがな
い。またこのネットについての通気性は30cc/cm2/secで
あった。
The net 15 woven in this manner is woven in the center of the net layer so that the conductive wire 13 arranged in a straight line as shown in the cross section of FIG. Insulating wire rods 14 are lined up on the front and back outer surfaces of the net 15, so that the conductive wire rods 13 do not stick out to the net face. The air permeability of this net was 30 cc / cm 2 / sec.

次に上記ネット15を第3図に示したベルトプレス型電気
浸透脱水機における電極兼用の搬送ベルト2,プレスベル
ト6として用い、汚泥を脱水処理したところによれば、
汚泥粒子をネット15の表面に捕修して汚泥の漏れを阻止
しつつ,同時に電気浸透で電極面に流動して来た水,電
気分解により発生したガスに対して十分な排水,排ガス
機能が確保され、効率のよい脱水性能の得られることが
確保された。これは縦糸と横糸との間に汚泥粒子の透過
阻止と排水,排ガス機能を与える適宜な隙間が存在し、
かつ通電機能に関与する導電線材13は第1図の平面図で
見られるようにその大半域がスラリ通路側に露呈してい
るためである。
Next, the net 15 is used as the conveyor belt 2 and the press belt 6 which also serve as electrodes in the belt press type electroosmotic dehydrator shown in FIG. 3, and the sludge is dehydrated.
While sludge particles are captured on the surface of the net 15 to prevent sludge from leaking, at the same time sufficient drainage and exhaust gas functions are provided for water that has flowed to the electrode surface by electroosmosis and gas generated by electrolysis. It was ensured that efficient dehydration performance was obtained. This is because there is a proper gap between the warp and the weft to prevent sludge particle permeation, drainage, and exhaust gas function.
In addition, the conductive wire 13 involved in the current-carrying function has a large area exposed to the slurry passage side as seen in the plan view of FIG.

また脱水運転の途中で陽極側のプレスベルト6と陰極側
の搬送ベルト2とを故意に弛ませてベルト同士を接触さ
せたが、電気的な短絡は発生せず十分な安全性が確認で
きた。これは先述のように導電線材13がネット表面に突
出してなく、ベルト同士が接触した際にはネット15の絶
縁線材14同士が突き当たって導電線材13の接触を防止す
るためである。しかも苛酷な荷重条件で長期運転した結
果でもネット15の縦糸,横糸の配列に乱れの発生が無
く、電極としての汚泥への通電機能の他、排水,排ガス
機能,並びに電気短絡防止機能が良好に維持でることが
確認されている。
Further, during the dehydration operation, the press belt 6 on the anode side and the conveyor belt 2 on the cathode side were intentionally loosened to bring the belts into contact with each other, but no electrical short circuit occurred and sufficient safety was confirmed. . This is because the conductive wire 13 does not project to the surface of the net as described above, and when the belts contact each other, the insulating wire 14 of the net 15 bumps against each other to prevent the conductive wire 13 from contacting. Moreover, the warp and weft arrangements of the net 15 are not disturbed even after long-term operation under severe load conditions, and the drainage, exhaust gas function, and electrical short-circuit prevention function are excellent in addition to the function of energizing sludge as an electrode. It has been confirmed that it can be maintained.

〔発明の効果〕〔The invention's effect〕

以上述べたようにこの発明によれば、導電線材,絶縁線
材の一方を縦糸,他方を横糸として織成されたネットと
して成り、かつ少なくともスラリ通路との対向面側で導
電線材がネット面へ突き出さないように絶縁線材の内側
に織り込んで電極を構成したことにより、電極として要
求される汚泥への良好な通電機能とともに汚泥粒子の捕
集,排水,排ガス機能を確保しつつ、運転中に電極を兼
ねた陽極側と陰極側のベルト同士が直接接触した場合で
もベルト自身で電極間で電気的な短絡が生じるのを確実
に防止できる。しかも従来の短絡防止策のように電極間
に別な絶縁部材を介在付設する必要がなく、電気浸透脱
水機としての構造,保守面での簡略化が図れる利点も得
られる。
As described above, according to the present invention, a net is formed by weaving one of the conductive wire and the insulating wire as the warp thread and the other as the weft thread, and the conductive wire sticks out to the net surface at least on the side facing the slurry passage. Since the electrode is constructed by weaving it inside the insulated wire to prevent it, while ensuring a good electricity-carrying function to the sludge required for the electrode, as well as collecting, draining, and exhaust gas functions of sludge particles, the electrode is in operation. Even when the belts on the anode side and the cathode side, which also serve as the electrodes, directly contact each other, it is possible to reliably prevent the belt itself from causing an electrical short circuit between the electrodes. Moreover, unlike the conventional short-circuit prevention measure, it is not necessary to additionally provide another insulating member between the electrodes, and there is an advantage that the structure and maintenance of the electroosmotic dehydrator can be simplified.

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

第1図は本発明実施例による電極構造の平面図、第2図
は第1図の断面図、第3図はベルトプレス型電気浸透脱
水機の構成図、第4図,第5図はそれぞれ従来における
電極間の短絡防止策を示した第3図における矢視X−X
断面図である。各図において、 1:汚泥供給用のホッパ、2:陰極側電極を兼ねた搬送ベル
ト、3:スラリ通路、6:陽極側電極を兼ねたプレスベル
ト、8:電源、9:汚泥、10:脱水ケーキ、13:導電線材、1
4:絶縁線材、15:ベルト状ネット。
1 is a plan view of an electrode structure according to an embodiment of the present invention, FIG. 2 is a sectional view of FIG. 1, FIG. 3 is a configuration diagram of a belt press type electroosmotic dehydrator, and FIGS. 4 and 5 are respectively. The arrow XX in FIG. 3 showing the conventional measure for preventing short circuit between electrodes
FIG. In each figure, 1: hopper for supplying sludge, 2: conveyor belt also serving as cathode side electrode, 3: slurry passage, 6: press belt also serving as anode side electrode, 8: power supply, 9: sludge, 10: dehydration Cake, 13: Conductive wire, 1
4: Insulated wire, 15: Belt net.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】スラリ通路を挟んで陽極側電極と陰極側電
極を対向配備し、電極間に電圧を印加した状態でスラリ
通路に供給した汚泥を電気浸透脱水する電気浸透式脱水
機の電極であって、導電線材,絶縁線材の一方を縦糸,
他方を横糸として織成されたネットとして成り、かつ少
なくともスラリ通路との対向面側で導電線材がネット面
へ突き出さないように絶縁線材の内側に織り込まれてい
ることを特徴とする電気浸透式脱水機の電極。
1. An electrode for an electroosmosis dehydrator, in which an anode-side electrode and a cathode-side electrode are opposed to each other with a slurry passage sandwiched therebetween, and the sludge supplied to the slurry passage is electroosmotically dehydrated while a voltage is applied between the electrodes. One of the conductive wire and the insulated wire is warp yarn,
An electro-osmotic type characterized in that it is formed as a net woven with the other side as a weft thread, and that the conductive wire is woven inside the insulating wire at least on the side facing the slurry passage so as not to project to the net surface. Dehydrator electrode.
【請求項2】特許請求の範囲第1項記載の電極におい
て、導電線材は耐蝕性の高い金属線材,絶縁線材は合成
繊維の糸であり、かつ直線状に伸張した金属線材を横
糸,絶縁線材を縦糸にして織成されたベルト状ネットで
あることを特徴とする電気浸透式脱水機の電極。
2. The electrode according to claim 1, wherein the conductive wire is a metal wire having high corrosion resistance, the insulating wire is a synthetic fiber thread, and the linearly extended metal wire is a weft thread or an insulating wire. An electrode for an electro-osmotic dehydrator, which is a belt-like net woven with warp as a warp yarn.
JP62286684A 1987-11-13 1987-11-13 Electro-osmotic dehydrator electrode Expired - Fee Related JPH0687925B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62286684A JPH0687925B2 (en) 1987-11-13 1987-11-13 Electro-osmotic dehydrator electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62286684A JPH0687925B2 (en) 1987-11-13 1987-11-13 Electro-osmotic dehydrator electrode

Publications (2)

Publication Number Publication Date
JPH01127012A JPH01127012A (en) 1989-05-19
JPH0687925B2 true JPH0687925B2 (en) 1994-11-09

Family

ID=17707631

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62286684A Expired - Fee Related JPH0687925B2 (en) 1987-11-13 1987-11-13 Electro-osmotic dehydrator electrode

Country Status (1)

Country Link
JP (1) JPH0687925B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB0323068D0 (en) 2003-10-01 2003-11-05 Nuground Ltd Dewatering treatment system and method
JP5617240B2 (en) * 2009-12-28 2014-11-05 栗田工業株式会社 Electroosmotic dehydration method and apparatus
KR101070296B1 (en) * 2011-06-27 2011-10-06 주식회사 화인 Drum type electro-osmosis dehydrator for saving electric
CN102503070B (en) * 2011-11-11 2013-03-06 河海大学 Device for reducing water ratio of sludge
CN108314281A (en) * 2018-01-22 2018-07-24 浙江工业大学 A kind of high-voltage pulse electrode system of electrolysis processing deeply dehydrating sludge

Also Published As

Publication number Publication date
JPH01127012A (en) 1989-05-19

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