JPH0468006B2 - - Google Patents

Info

Publication number
JPH0468006B2
JPH0468006B2 JP60263289A JP26328985A JPH0468006B2 JP H0468006 B2 JPH0468006 B2 JP H0468006B2 JP 60263289 A JP60263289 A JP 60263289A JP 26328985 A JP26328985 A JP 26328985A JP H0468006 B2 JPH0468006 B2 JP H0468006B2
Authority
JP
Japan
Prior art keywords
plate
filter
electrode
diaphragm
compressed
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
Application number
JP60263289A
Other languages
Japanese (ja)
Other versions
JPS62121613A (en
Inventor
Sadaaki Saito
Shiro Kondo
Shigeru Sano
Haruo Hamazaki
Masayuki Nakamura
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.)
KURITA KIKAI SEISAKUSHO KK
SHINKO PANTETSUKU KK
Original Assignee
KURITA KIKAI SEISAKUSHO KK
SHINKO PANTETSUKU KK
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 KURITA KIKAI SEISAKUSHO KK, SHINKO PANTETSUKU KK filed Critical KURITA KIKAI SEISAKUSHO KK
Priority to JP60263289A priority Critical patent/JPS62121613A/en
Publication of JPS62121613A publication Critical patent/JPS62121613A/en
Publication of JPH0468006B2 publication Critical patent/JPH0468006B2/ja
Granted legal-status Critical Current

Links

Landscapes

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

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は圧搾ダイヤフラムを備えたフイルター
プレス型電気浸透脱水機、特にその電極を備える
圧搾濾板の構造の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a filter press type electroosmotic dehydrator equipped with a squeeze diaphragm, and particularly to an improvement in the structure of a squeeze filter plate equipped with an electrode.

(従来の技術) 汚泥の圧搾脱水過程で汚泥中に直流電流を通ず
ると、単に圧搾するだけでは脱水できない汚泥中
の水分も電気浸透作用により外部に移動して脱水
が促進される。圧搾ダイヤフラムを備えたフイル
タープレスなどの回分式圧搾脱水機に電気浸透作
用を併用すると、ベルトプレスなどの連続式圧搾
脱水機と較べて、充分な通電時間を与えることが
でき、脱水過程で通電むらが生じにくいことか
ら、効果的な脱水処理ができ脱水ケーキの含水率
を著しく低下させることができる。
(Prior Art) When a direct current is passed through the sludge during the sludge compression and dewatering process, water in the sludge that cannot be dehydrated simply by squeezing moves to the outside due to electroosmosis, thereby promoting dewatering. When electroosmosis is used in combination with a batch-type compressing dehydrator such as a filter press equipped with a compressing diaphragm, it is possible to provide sufficient energization time compared to a continuous compressing dehydrator such as a belt press, thereby eliminating uneven energization during the dehydration process. Since this does not easily occur, effective dehydration treatment can be performed and the water content of the dehydrated cake can be significantly reduced.

例えば、高分子凝集剤を添加して95〜97%含水
率に予備濃縮した下水汚泥を、圧搾ダイヤフラム
を有するフイルタープレスに供給し3Kg/cm2の圧
搾圧力で約20分間圧搾脱水した場合の脱水ケーキ
含水率は80〜85%であり、これ以上の圧搾圧力、
圧搾時間をかけても含水率低下の効果は少いが、
前記フイルタープレスを電極構造を組込んだもの
として、圧搾脱水の途中で電極板の間に40Vの直
流電圧をかけ約15分間電気浸透脱水を行うと、脱
水クーキの含水率は60%前後にまで低下し、脱水
ケーキの体積は圧搾脱水のみのものと比較して
1/2以下となる。
For example, sewage sludge that has been preconcentrated to a water content of 95 to 97% by adding a polymer flocculant is fed to a filter press with a pressing diaphragm and dehydrated by pressing at a pressing pressure of 3 kg/cm 2 for about 20 minutes. Cake moisture content is 80-85%, no more pressing pressure,
Even if the pressing time is increased, the effect of reducing the moisture content is small, but
If the filter press is equipped with an electrode structure and electroosmotic dehydration is performed by applying a DC voltage of 40 V between the electrode plates during compression dehydration for about 15 minutes, the moisture content of the dehydrated cookie will drop to around 60%. The volume of the dehydrated cake is 1/2 or less compared to that obtained only by pressing and dehydration.

第1図は本発明の電極構造の適用対象ともなる
電気浸透脱水機の1例を示し、第2図はそのフイ
ルター板枠組の分離開放状態の斜視図を示す。こ
れらを援用してこの種脱水機全体の概要を説明す
る。
FIG. 1 shows an example of an electroosmotic dehydrator to which the electrode structure of the present invention is applied, and FIG. 2 shows a perspective view of the filter plate framework in a separated and open state. Using these, an overview of this type of dehydrator as a whole will be explained.

プレス機の親板1と可動板2との間には、濾板
3と圧搾濾板4との間に濾枠5を介在させこれら
の組の適宜数を介在させて締付けて閉じる。濾板
3には一方の電極板6を固定する。この電極6は
多孔通水性板とする。濾枠5にはその両面の全面
にわたる濾布7を掛けその中抜腔を濾室8とす
る。圧搾濾板4には可燒性のダイヤフラム9を設
けこれに他方の電極板10を取付ける。
A filter frame 5 is interposed between a filter plate 3 and a compressed filter plate 4 between the main plate 1 and the movable plate 2 of the press, and an appropriate number of these sets are interposed and closed by tightening. One electrode plate 6 is fixed to the filter plate 3. This electrode 6 is made of a porous water permeable plate. A filter cloth 7 is hung over the entire surface of both sides of the filter frame 5, and the hollow space thereof is used as a filter chamber 8. A sinterable diaphragm 9 is provided on the compressed filter plate 4, and the other electrode plate 10 is attached to this.

脱水操作は次の順序で行う。すなわち、原汚泥
を原汚泥用板枠貫通孔11を通して濾枠5の濾室
8内に圧入し、両側の濾布7を透過した瀘液を濾
板3からまた圧搾濾板4から瀘液用板枠貫通孔1
2a12bに排出する。原汚泥の濾室内充満およ
び送給圧による濾過が終ると原汚泥の送給を停止
し、圧搾空気を圧搾空気用板枠貫通孔13から圧
搾濾板4のダイヤフラム9の背後に送給してダイ
ヤフラム9を膨張させ濾室に充満した汚泥の圧搾
脱水を行う。次いで電極板6,10間に直流電圧
を印加して電気浸透脱水を行う。
The dehydration operation is performed in the following order. That is, raw sludge is press-fitted into the filter chamber 8 of the filter frame 5 through the raw sludge plate frame through hole 11, and the filtrate that has passed through the filter cloths 7 on both sides is transferred from the filter plate 3 and from the compressed filter plate 4 for filtrate use. Plate frame through hole 1
Discharge to 2a12b. When the filling of the filter chamber with the raw sludge and the filtration by the supply pressure are completed, the supply of the raw sludge is stopped, and compressed air is supplied from the compressed air plate frame through hole 13 to the back of the diaphragm 9 of the compressed filter plate 4. The diaphragm 9 is expanded to compress and dewater the sludge filling the filter chamber. Next, a DC voltage is applied between the electrode plates 6 and 10 to perform electroosmotic dehydration.

ダイヤフラム9に電極10を併せ設けることが
必要な圧搾濾板4の1例は先願特願昭60−196934
の第12および13図に開示されており、第5図
はその縦断側面図である。
An example of a compressed filter plate 4 that requires a diaphragm 9 and an electrode 10 is disclosed in the earlier patent application No. 1969-1960.
12 and 13, and FIG. 5 is a longitudinal sectional side view thereof.

(発明が解決しようとする問題点) 前記の電気浸透脱水機では、ダイヤフラム9前
面の電極板10がダイヤフラムを貫通する多数の
ボルト14により背後の支持板15に固着する構
造となつているので、ダイヤフラムを背後に圧搾
空気を供給し膨張させ、圧搾脱水する際に、ダイ
ヤフラムの伸びによつて電極板10との間にずれ
が生じ、ボルト14貫通孔からの空気洩れが生じ
て圧搾脱水効果が減殺され、また反覆操作により
取付ボルト14が外れる等の問題があることが知
見された。
(Problems to be Solved by the Invention) The electroosmotic dehydrator described above has a structure in which the electrode plate 10 on the front side of the diaphragm 9 is fixed to the support plate 15 on the back side by a large number of bolts 14 passing through the diaphragm. When compressed air is supplied to the back of the diaphragm to expand it and perform compression dehydration, the diaphragm elongates, causing a gap between it and the electrode plate 10, causing air leakage from the bolt 14 through-hole, which impairs the compression dehydration effect. It was discovered that there were problems such as the mounting bolts 14 coming off due to repeated operations.

本発明は上記の問題点を解決することを目的と
する。
The present invention aims to solve the above problems.

(問題点を解決するための手段) 前記目的は、本発明により、圧搾濾板側の電極
構造をダイヤフラムと電極とを隔離して相互干渉
しないように、しかもそれぞれが本来の機能を発
揮するようにすることにより達成される。
(Means for Solving the Problems) According to the present invention, the above-mentioned object is to separate the diaphragm and the electrode from the electrode structure on the squeeze filter plate side so that they do not interfere with each other, and also so that each of them can perform its original function. This is achieved by making

すなわち、本発明の電気浸透脱水機の電極構造
は、構成としては、圧搾ダイヤフラムを備えたフ
イルタープレス形式の電気浸透脱水機において、
圧搾ダイヤフラムを有する圧搾濾板の電極板を圧
搾ダイヤフラム面と離隔して前後動自在に濾室側
に支持したことを特徴とする。
That is, the electrode structure of the electro-osmotic dehydrator of the present invention is a filter press type electro-osmotic dehydrator equipped with a compression diaphragm.
The present invention is characterized in that the electrode plate of the compressed filter plate having the compressed diaphragm is supported on the filter chamber side so as to be movable back and forth, separated from the compressed diaphragm surface.

(作用) 圧搾濾板側の電極板がダイヤフラム面に固着さ
れていないので、圧搾脱水時におけるダイヤフラ
ムの伸びに起因する問題が解消される。
(Function) Since the electrode plate on the squeeze filter plate side is not fixed to the diaphragm surface, the problem caused by the elongation of the diaphragm during press dehydration is solved.

(実施例) 以下、本発明の電気浸透脱水機の電極構造を第
3および4図に示す実施例により具体的に説明す
る。第3図は本発明電極構造に関する圧搾濾板の
縦断側面図、第4図はその正面図を示す。この圧
搾濾板を適用する電気浸透脱水機の1例は第1図
に示され、そのフイルター板枠組は第2図に示さ
れているので、これに即して詳述する。
(Example) Hereinafter, the electrode structure of the electroosmotic dehydrator of the present invention will be explained in detail with reference to Examples shown in FIGS. 3 and 4. FIG. 3 shows a longitudinal sectional side view of a squeeze filter plate related to the electrode structure of the present invention, and FIG. 4 shows a front view thereof. An example of an electro-osmotic dehydrator to which this compressed filter plate is applied is shown in FIG. 1, and the filter plate framework is shown in FIG. 2, which will be described in detail.

この本発明実施例の圧搾濾板は、中央の圧搾濾
板本体20と両側の中抜腔を有する電極板保持枠
21,21との間にそれぞれ圧搾ダイヤフラム
9,9を挟み沈頭ボルト22により固定する。圧
搾濾板本体20には圧搾空気用板枠貫通孔13に
通ずる連通孔(図示せず)が設けられ、この経路
よりダイヤフラム9との界面に圧搾空気が導入さ
れダイヤフラム9は外側に向つて膨張する。
The compressed filter plate of this embodiment of the present invention has compressed diaphragms 9, 9 sandwiched between the central compressed filter plate main body 20 and electrode plate holding frames 21, 21 having hollow holes on both sides, respectively, and is secured by a sinking bolt 22. Fix it. The compressed filter plate main body 20 is provided with a communication hole (not shown) that communicates with the compressed air plate frame through hole 13, and compressed air is introduced from this path to the interface with the diaphragm 9, and the diaphragm 9 expands outward. do.

各側において、中抜の電極板保持枠21の外面
側の内縁には受段部23を形成し、電極板保持枠
の中空腔の全面にわたるゴム等の弾性材料よりな
る弾性支持部材24を張渡し、受段部23に押え
枠25で挟み付け沈頭ねじ26により固定する。
この弾性支持部材24の周部を除外した中央部分
の前面に電極板10を当てがい、背面に当板27
を当てがい、両者を弾性支持部材24を含めて貫
通する沈頭ねじ28により連結する。電極板10
および弾性支持部材24には連通して貫通する通
水孔29を面上に分布させて穿設し、一方当板2
7はその突部27aにより弾性支持部材24の背
部に接し、他の大部分は弾性支持部材との間に通
水間隔があるようにする。こうして電極板10は
ダイヤフラム9とは隔離され、隣接する濾枠5濾
室8側において独立して前後方向に可動に支持さ
れる。電極板10と外部に突出する導電部材30
との間は可燒性のリード線31等により導電接続
し電極板10の前後動を妨げないようにする。
On each side, a receiving step 23 is formed on the inner edge of the outer surface of the hollow electrode plate holding frame 21, and an elastic support member 24 made of an elastic material such as rubber is stretched over the entire hollow cavity of the electrode plate holding frame. Then, it is clamped to the receiving step part 23 with the presser frame 25 and fixed with the sinking screw 26.
The electrode plate 10 is applied to the front side of the central part of the elastic support member 24 excluding the peripheral part, and the contact plate 27 is applied to the back side.
are applied, and the two are connected by a sinking screw 28 that passes through the elastic support member 24 as well. Electrode plate 10
The elastic support member 24 is provided with water holes 29 that communicate with each other and are distributed over the surface.
7 is in contact with the back of the elastic support member 24 by its protrusion 27a, and most of the other parts are provided with a water passage interval between them and the elastic support member. In this way, the electrode plate 10 is separated from the diaphragm 9 and is supported independently and movably in the front and rear directions on the side of the adjacent filter frame 5 and the filter chamber 8. Electrode plate 10 and conductive member 30 protruding to the outside
A conductive connection is made between the electrode plate 10 and the electrode plate 10 by a sinterable lead wire 31 or the like so as not to hinder the back and forth movement of the electrode plate 10.

この実施例では、濾室8への原汚泥圧入時に、
電極板10は汚泥送給圧によつてダイヤフラム9
側に後退移動して当板27がダイヤフラム9に圧
着し、濾布7により濾過された瀘液は電極板1
0、弾性支持部材24の通水孔29を通り、電極
保持枠21の瀘液孔32を通り瀘液用板枠貫通孔
12bを通つて排出される。
In this embodiment, when the raw sludge is injected into the filter chamber 8,
The electrode plate 10 is connected to the diaphragm 9 by the sludge feeding pressure.
The contact plate 27 is pressed against the diaphragm 9 by moving backward to the side, and the filtrate filtered by the filter cloth 7 is transferred to the electrode plate 1.
0, it passes through the water passage hole 29 of the elastic support member 24, passes through the filtrate hole 32 of the electrode holding frame 21, and is discharged through the filtrate plate frame through hole 12b.

次に圧搾空気を貫通孔13から圧搾濾板本体2
0とダイヤフラム9との間隙に送給してダイヤフ
ラム9を膨張させると、電極板10は前進するダ
イヤフラム9に押されて電極板6に近付く方向に
移動する。この際、ダイヤフラム9には濾室8の
側に向うボルト孔が全く存在しないので圧搾脱水
時に、空気洩れ等が起る怖はない。
Next, compressed air is passed through the through holes 13 to the compressed filter plate main body 2.
When the electrode plate 10 is fed into the gap between the electrode plate 0 and the diaphragm 9 to expand the diaphragm 9, the electrode plate 10 is pushed by the advancing diaphragm 9 and moves in a direction approaching the electrode plate 6. At this time, since there are no bolt holes in the diaphragm 9 facing toward the filter chamber 8, there is no risk of air leakage during compression dewatering.

電極6,10間の直流通電による電気浸透脱水
を支障なく行い得ることは勿論である。
Of course, electroosmotic dehydration can be performed without any problem by direct current flowing between the electrodes 6 and 10.

上記実施例では電極支持部材として電極板保持
枠21の枠内全面に通水可能なゴム板等の弾性支
持部材24を張渡しているが、これに代え電極板
10の周辺部と電極板保持枠21との間を帯状の
弾性部材で接続する構造としてもよい。また電極
板10の移動距離が短い場合には、電極板10を
上部からのみ支持する屈曲自在な吊下部材を使用
してもよい。
In the above embodiment, an elastic support member 24 such as a water-permeable rubber plate is stretched across the entire inside of the electrode plate holding frame 21 as an electrode support member, but instead of this, the peripheral part of the electrode plate 10 and the electrode plate support A structure may be adopted in which the frame 21 is connected to the frame 21 by a band-shaped elastic member. Further, when the moving distance of the electrode plate 10 is short, a bendable hanging member that supports the electrode plate 10 only from above may be used.

また、フイルター板枠組は上記実施例のように
濾板3と圧搾濾板4との間に濾枠5を挟む形式に
限られず、濾枠を有しない脱水機、例えば濾板3
と第3および4図に示す圧搾濾板を交互に配列し
たもの、あるいはこの圧搾濾板のみを配列して、
その間に挟んだ2枚の濾布間に原汚泥を供給でき
るようにした型式の圧搾脱水機にも、本発明電極
構造は適用可能である。
Further, the filter plate framework is not limited to the type in which the filter frame 5 is sandwiched between the filter plate 3 and the compressed filter plate 4 as in the above embodiment, but it is also possible to use a dehydrator without a filter frame, for example, a filter plate 3
and the compressed filter plates shown in FIGS. 3 and 4 are arranged alternately, or only these compressed filter plates are arranged,
The electrode structure of the present invention is also applicable to a type of press dehydrator in which raw sludge can be supplied between two filter cloths sandwiched between them.

(発明の効果) 以上のとおり、本発明の電極構造によると、圧
搾脱水時のダイヤフラムの伸びに起因するトラブ
ルの問題が解消され、それによりこの種フイルタ
ープレス形式の電気浸透脱水機の信頼性を高く
し、維持管理も容易となる。
(Effects of the Invention) As described above, according to the electrode structure of the present invention, the problem of trouble caused by the elongation of the diaphragm during compression dehydration is solved, thereby improving the reliability of this type of filter press type electroosmotic dehydrator. It is also easier to maintain and manage.

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

第1図は本発明の電極構造の適用対策の電気浸
透脱水機の1例の側面図、第2図はそのフイルタ
ー板枠組の分離開放状態の斜視図、第3図は本発
明の1実施例の電気浸透脱水機の電極構造におけ
る圧搾濾板の縦断側面図、第4図はその半部縦断
正面図、第5図は先行技術の圧搾濾板の縦断側面
図である。 1……親板、2……可動板、3……濾板、4…
…圧搾濾板、5……濾枠、6……電極板、7……
濾布、8……濾室、9……圧搾タイヤフラム、1
1……原汚泥用板枠貫通孔、12a,12b……
瀘液用板枠貫通孔、13……圧搾空気用板枠貫通
孔、14……ボルト、15……支持板、20……
圧搾濾板本体、21……電極板保持枠、22……
ボルト、23……受段部、24……弾性支持部
材、25……押え枠、26……ねじ、27……当
板、27a……突部、28……ねじ、29……通
水孔、30……導電部材、31……リード線、3
2……瀘液孔。
Fig. 1 is a side view of an example of an electroosmotic dehydrator to which the electrode structure of the present invention is applied, Fig. 2 is a perspective view of the filter plate framework in a separated and open state, and Fig. 3 is an embodiment of the present invention. FIG. 4 is a longitudinal sectional side view of a compressed filter plate in the electrode structure of an electroosmotic dehydrator, FIG. 4 is a half longitudinal front view thereof, and FIG. 5 is a longitudinal sectional side view of the compressed filter plate of the prior art. 1... Main plate, 2... Movable plate, 3... Filter plate, 4...
...Pressed filter plate, 5...Filter frame, 6...Electrode plate, 7...
Filter cloth, 8... Filter chamber, 9... Compressed tire flam, 1
1...Plate frame through holes for raw sludge, 12a, 12b...
Plate frame through hole for filtrate, 13... Plate frame through hole for compressed air, 14... Bolt, 15... Support plate, 20...
Pressing filter plate main body, 21... Electrode plate holding frame, 22...
Bolt, 23... Step portion, 24... Elastic support member, 25... Holding frame, 26... Screw, 27... Backing plate, 27a... Protrusion, 28... Screw, 29... Water hole , 30... Conductive member, 31... Lead wire, 3
2...Filtrate hole.

Claims (1)

【特許請求の範囲】 1 圧搾ダイヤフラムを備えたフイルタープレス
形式の電気浸透脱水機において、圧搾ダイヤフラ
ムを有する圧搾濾板の電極板を圧搾ダイヤフラム
面と離隔して前後動自在に濾室側に支持したこと
を特徴とする電気浸透脱水機の電極構造。 2 圧搾濾板に電極板保持枠を固定し、その枠内
に弾性部材を介して電極板を支持した特許請求の
範囲第1項記載の電気浸透脱水機の電極構造。 3 前記弾性部材を、通水手段を有するゴム板と
した特許請求の範囲第2項記載の電気浸透脱水機
の電極構造。
[Scope of Claims] 1. In a filter press type electroosmotic dehydrator equipped with a compressed diaphragm, an electrode plate of a compressed filter plate having a compressed diaphragm is supported on the filter chamber side so as to be movable back and forth, separated from the compressed diaphragm surface. An electrode structure of an electroosmotic dehydrator characterized by the following. 2. The electrode structure for an electroosmotic dehydrator according to claim 1, wherein an electrode plate holding frame is fixed to the pressing filter plate, and the electrode plate is supported within the frame via an elastic member. 3. The electrode structure for an electroosmotic dehydrator according to claim 2, wherein the elastic member is a rubber plate having water passage means.
JP60263289A 1985-11-22 1985-11-22 Electrode structure of electroendosmosis dehydrator Granted JPS62121613A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60263289A JPS62121613A (en) 1985-11-22 1985-11-22 Electrode structure of electroendosmosis dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60263289A JPS62121613A (en) 1985-11-22 1985-11-22 Electrode structure of electroendosmosis dehydrator

Publications (2)

Publication Number Publication Date
JPS62121613A JPS62121613A (en) 1987-06-02
JPH0468006B2 true JPH0468006B2 (en) 1992-10-30

Family

ID=17387400

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60263289A Granted JPS62121613A (en) 1985-11-22 1985-11-22 Electrode structure of electroendosmosis dehydrator

Country Status (1)

Country Link
JP (1) JPS62121613A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106925006A (en) * 2017-03-23 2017-07-07 成都易态科技有限公司 Press filtration unit, filter-pressing device and mud dewatering method

Also Published As

Publication number Publication date
JPS62121613A (en) 1987-06-02

Similar Documents

Publication Publication Date Title
GB1035190A (en) Mechanized heavy duty filter press
GB1271174A (en) Filter press
JPH0468006B2 (en)
RU1820846C (en) Process of dewatering in filter press
JPH0639212A (en) Filter and filtration method
JPH0513686B2 (en)
JP3739049B2 (en) Filter press filter plate
JP3298022B2 (en) Electro-osmotic dehydrator
JP2004082036A5 (en)
JPS63214309A (en) Dehydrator
JPH10202068A (en) Electroosmotic dehydrator
JPS6257623A (en) Electroosmotic dehydrator
JP2947058B2 (en) Filtration press in filter press
GB1330125A (en) Filter presses
CN220758115U (en) Filter plate of compressible filter press
JPH055924Y2 (en)
JPS6041351Y2 (en) Sludge dewatering equipment
JPS6380810A (en) Filter press
JPS62125811A (en) Operating method for electroosmosis dehydrator
JPH0679645B2 (en) Peeling method of dehydrated sludge in electroosmosis dehydrator
JPH03101802A (en) Pressing type filler press
JPH0230006Y2 (en)
JPS61161112A (en) Filter press
JPS63123409A (en) Filtration method
JPH02172521A (en) Squeezing filtration structure of electric penetration extractor

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees