JPS6257622A - Electroosmotic dehydrator - Google Patents

Electroosmotic dehydrator

Info

Publication number
JPS6257622A
JPS6257622A JP60196934A JP19693485A JPS6257622A JP S6257622 A JPS6257622 A JP S6257622A JP 60196934 A JP60196934 A JP 60196934A JP 19693485 A JP19693485 A JP 19693485A JP S6257622 A JPS6257622 A JP S6257622A
Authority
JP
Japan
Prior art keywords
plate
filter
conductive plate
conductive
filter plate
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
JP60196934A
Other languages
Japanese (ja)
Other versions
JPH0513686B2 (en
Inventor
Shiro Kondo
史朗 近藤
Shigeru Sano
佐野 滋
Haruo Hamazaki
浜崎 晴夫
Masayuki Nakamura
政行 中村
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 Machinery Manufacturing Co Ltd
Shinko Pfaudler Co Ltd
Original Assignee
Kurita Machinery Manufacturing Co Ltd
Shinko Pfaudler 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 Kurita Machinery Manufacturing Co Ltd, Shinko Pfaudler Co Ltd filed Critical Kurita Machinery Manufacturing Co Ltd
Priority to JP60196934A priority Critical patent/JPS6257622A/en
Publication of JPS6257622A publication Critical patent/JPS6257622A/en
Publication of JPH0513686B2 publication Critical patent/JPH0513686B2/ja
Granted legal-status Critical Current

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

Abstract

PURPOSE:To efficiently carry out dehydration by expanding an elastic member to allow an electrically conductive plate on the anode side to approach the cathode side and conducting a DC current while reducing the interval between both conductive plates when an unfiltered liq. in a filter chamber is dehydrated by electroosmosis. CONSTITUTION:An electrically conductive plate 4 on the cathode side is provided on the opposite surface of a filter plate 1 and a conductive plate 5 on the anode side is furnished on the surface of a squeeze filter plate 3 opposite to the filter plate 1, filter cloths 6 and 6 are laid over filter frames 2 and 2 to cover both faces, the filter frame 2 is inserted between the filter plate 1 and the squeeze filter plate 3 and a filter chamber 7 is formed. An unfiltered liq. is forced into the filter chamber 7, a DC voltage is impressed on the conductive plates 4 and 5, compressed air is introduced to expand an elastic membrane 18 and the conductive plate 5 is moved. The liq. component is passed through the filter cloth 6 on the cathode side and discharged from a filtrate recovery passage of the filter plate 1. The solid component is drawn to the anode side, remains in the filter chamber 7 and is subjected to electroosmotic dehydration.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、汚泥など濾過すべき原液に直流を流しなから
シ濾過を行う電気浸透脱水装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to an electroosmotic dewatering apparatus that performs filtration by passing a direct current through a raw solution such as sludge to be filtered.

従来の技術 従来より、汚泥等の濾過あるいは加圧脱水の過程で汚泥
中に直流電流を流すと、汚泥中の水分が電気浸透作用で
外部に移動し、脱水が促進されることが知られており、
各種脱水機に電気浸透を併用する試みがなされている。
Conventional Technology It has long been known that when direct current is passed through sludge during filtration or pressurized dewatering, water in the sludge moves to the outside through electroosmosis, promoting dewatering. Ori,
Attempts have been made to use electroosmosis in combination with various dehydrators.

この−例として、走行する2枚のろ布に汚泥をはさみ、
連続的に脱水処理を行なうベルトプレス形式の加圧脱水
機に電気浸透を併用するものがある。この場合には、通
電時間が十分に取れず、また、ろ布の走行に従い、汚泥
の厚み、含水率、電気抵抗等が変化するため、電流分布
が不均一となるといった問題がある。これに対しフィル
タプレス等の四分式加圧脱水機では、」二記のような問
題が少ないので、加圧と電気浸透を併用してケーキ含水
率を低下させる点て最ら効果的である。この電気浸透を
利用したフィルタプレスの一例としては次のらのがある
(特公昭37−14034号)。
As an example, if sludge is sandwiched between two moving filter cloths,
There is a belt press type pressure dehydrator that performs continuous dehydration treatment that also uses electroosmosis. In this case, there is a problem that the energization time is insufficient, and the thickness, water content, electrical resistance, etc. of the sludge change as the filter cloth runs, resulting in uneven current distribution. On the other hand, with a four-section pressure dehydrator such as a filter press, there are fewer problems such as those mentioned above, so it is most effective to reduce the moisture content of the cake by using both pressure and electroosmosis. . An example of a filter press using electroosmosis is the following (Japanese Patent Publication No. 37-14034).

すなわち、第17図に示すように、隣接した導電性炉板
40.40fJl:>F布41.41 テ囲マレター室
42を形成するとととらに、該炉室42を二分するよう
に導電板43を両I仮40.40間に絶縁性バッキング
44を介してはさみ込み、Y板40と導電板43との間
に、炉板側が沈殿物粒子に荷電している電荷と同じ符号
の極となるように、直流電圧を荷電するように構成する
。そして、上記V室42内に原液を圧入して、原液の圧
力による加圧脱水と並行して、炉板40と導電板43と
の間にI板側が沈殿物粒子に荷電している電圧と同じ符
号になるように直流電圧を通電して、電気泳動現象及び
電気浸透現象を生せしめ、沈殿物粒子は導電板側に移動
する一方、液体はI右側の導電板側に移動してろ室外に
排出されるようにして、デ布41の表面に固い脱水固体
層が形成されて著しくシ濾過抵抗が増大するのを排除し
てシ濾過を効率良く行うようにした乙のである。
That is, as shown in FIG. 17, in addition to forming the adjacent conductive furnace plates 40. is sandwiched between both I temporary 40.40 via an insulating backing 44, and between the Y plate 40 and the conductive plate 43, the furnace plate side becomes a pole with the same sign as the charge charged on the sediment particles. The device is configured to charge a DC voltage as shown in FIG. Then, the stock solution is pressurized into the V chamber 42, and in parallel with pressurized dehydration due to the pressure of the stock solution, a voltage is applied between the furnace plate 40 and the conductive plate 43 so that the I plate side is charged with the precipitate particles. DC voltage is applied with the same sign to cause electrophoresis and electroosmosis phenomena, and the precipitate particles move toward the conductive plate, while the liquid moves to the conductive plate on the right side of I and exits the filter chamber. This is to prevent the formation of a hard dehydrated solid layer on the surface of the cloth 41, which would significantly increase the filtering resistance, and to efficiently perform filtering.

発明が解決しようとする問題点 しかしながら、上記構造の乙のでは、炉板間に形成した
戸室内の炉板と導電板との間隔が固定されているため、
)濾過がある程度進み、炉室内の液体が少なくなると、
汚泥の電気抵抗が増加するので、電極間に高い電圧を加
えて十分に電気浸透現象を生じさせるための電流値を維
持する必要がある。また、ろ室内では原液供給個所とそ
の他の個所とで汚泥濃度差が生じ、この汚泥濃度差によ
り電気抵抗に差が生じて、均一な電流分布が得られない
ため、電気浸透脱水を効率良く行うことができないとい
った問題があった。
Problems to be Solved by the Invention However, in the above structure B, since the distance between the furnace plate and the conductive plate in the door formed between the furnace plates is fixed,
) When the filtration progresses to a certain extent and the liquid in the furnace chamber decreases,
Since the electrical resistance of the sludge increases, it is necessary to maintain a current value sufficient to cause electroosmosis by applying a high voltage between the electrodes. In addition, in the filter chamber, a difference in sludge concentration occurs between the raw solution supply point and other points, and this difference in sludge concentration causes a difference in electrical resistance, making it impossible to obtain a uniform current distribution, making electroosmotic dehydration more efficient. The problem was that I couldn't do it.

従って、本発明の目的は、上記問題を解決することにあ
って、濾過が進み、1室内の液体成分が少なくなっても
、炉室内の原液に対して効率良く電気浸透脱水を行うこ
とができる電気浸透脱水装置を提供することにある。
Therefore, an object of the present invention is to solve the above-mentioned problem, and even if the filtration progresses and the liquid components in one chamber decrease, it is possible to efficiently perform electroosmotic dehydration on the raw liquid in the furnace chamber. An object of the present invention is to provide an electroosmotic dehydration device.

問題点を解決するための手段 上記目的を達成するために、本発明は、一方の電極に対
して他方の電極が移動できるように構成した。すなわち
、隣接したろ板間にろ布により囲まれたろ室を形成する
とともに、一方の>PFi、に第1導電板を備える一方
、上記一方のp仮は、炉板本体の他方の>F仮に対向す
る面に弾性膜を備えるととらに、該弾性膜を膨張させろ
流体を弾性膜と上記>F板本体との間に供給する流体供
給通路を上記?板本体に備え、かつ該弾性膜の外面に上
記第1導電板を固定して、上記弾性膜の弾性膨張により
該第1導電板か上記第2導電板側に移動するように構成
し、上記他方のP板に第2導電板を備え、上記第1導電
板と第2導電板に夫々相反ずろ電極を接続して上記−室
内の原液に直流電圧を印加し、原液に対して電気浸透脱
水を行うように構成した。
Means for Solving the Problems In order to achieve the above object, the present invention is configured such that one electrode can be moved relative to the other electrode. That is, a filter chamber surrounded by a filter cloth is formed between adjacent filter plates, and one >PFi is provided with a first conductive plate, while the above one Pfi is connected to the other >Ffi of the furnace plate main body. In addition to providing an elastic membrane on the opposing surfaces, a fluid supply passage is provided to inflate the elastic membrane and supply fluid between the elastic membrane and the >F plate main body. The first conductive plate is provided on the plate main body and is fixed to the outer surface of the elastic membrane so that the first conductive plate moves toward the second conductive plate due to elastic expansion of the elastic membrane, A second conductive plate is provided on the other P plate, and staggered electrodes are connected to the first conductive plate and the second conductive plate, respectively, and a DC voltage is applied to the stock solution in the chamber to perform electroosmotic dehydration on the stock solution. It was configured to do this.

ここで、上記導電板を炉板に備えるため、炉板を導電性
のものとして炉板と導電板とが一部品として形成するよ
うにしてもよい。また、隣接P板間にr枠を挟み込み、
炉室を大きくするようにしてもよい。
Here, in order to provide the above-mentioned conductive plate on the furnace plate, the furnace plate and the conductive plate may be formed as one piece by making the furnace plate conductive. Also, insert an r frame between adjacent P plates,
The furnace chamber may be made larger.

進厘し目覚l 上記構成においては、?布で囲まれたろ室内に原液を供
給して濾過を行なったのち、原液供給孔を閉鎖し、原液
供給圧以上の圧力で流体を一方のろ板のろ板本体と弾性
膜との間に供給して、該弾性膜を膨張させ、第1導電板
を第2導電板側に移動させて両導電板間の原液をさらに
圧搾濾過し、次いで、第1.第2導電板に直流電圧を印
加してr室内の原液に対して電気浸透脱水を行う。この
ように、脱水の進行に従い、電極間距離が小さくなり、
電気浸透に必要な十分な電流値が維持される。
Awakening to progress l In the above configuration, ? After the stock solution is supplied into the filter chamber surrounded by cloth and filtered, the stock solution supply hole is closed and the fluid is supplied between the filter plate body and the elastic membrane of one filter plate at a pressure higher than the stock solution supply pressure. Then, the elastic membrane is expanded, the first conductive plate is moved to the second conductive plate side, and the stock solution between both conductive plates is further compressed and filtered. A DC voltage is applied to the second conductive plate to perform electroosmotic dehydration on the stock solution in the r chamber. In this way, as dehydration progresses, the distance between the electrodes decreases,
Sufficient current values necessary for electroosmosis are maintained.

実施例 以下に、本発明にかかる実施例を図面に基づいて詳細に
説明する。
Embodiments Below, embodiments of the present invention will be described in detail based on the drawings.

本実施例にかかる電気浸透脱水装置は、第1゜2.3図
に示すように、圧搾式フィルタプレスの一対のろ板1.
1間に一対のろ枠2.2を挟み込むとともに、該一対の
P枠2.2間に圧搾炉板3を挟み込み、上記各炉板1の
相対する面に陰極側導電板4を固定する一方、圧搾炉板
3のろ板lに相対する面に陽極側導電板5を備え、さら
に、炉枠2.2の両面を夫々覆うようにI布6.6を掛
けてなり、枦仮lと圧搾ろ板3との間に夫々ろ忰2を挟
み込んで、戸枠2の枠内にろ布6.6で囲まれた一室7
を形成し、該−室7内に原液を圧入したのち、上記導電
板4,5に直流電圧を印加して電気浸透脱水を行い、ろ
板lの陰極導電板側に原液中の液体成分が移動してI布
6を通って該炉板2のろ液回収路から機外に排出される
とともに、固体成分は圧搾r仮3の陽極導電板側に引き
寄せられてP室7内に残るようにして、原液に対する電
気浸透脱水を行うものである。なお、第1図中、 15は原液供給孔、30.31は夫々電極接続端子であ
る。また、第3図中、8はp板l、1、ろ枠2,2、圧
搾戸板3の夫々両側部に突設した各把手9.・・・、9
が摺動するガイドレール、IOは駆動装置1!の駆動に
より前後動する可動板であって、駆動装置11の駆動に
より可動板lOが前後動じて、ろ板1,1、r枠2,2
、圧搾炉板3をガイドレール8沿いに前後動させ、親板
12に対して型閉めまたは型開きするものである。
As shown in Fig. 1.2.3, the electroosmotic dewatering apparatus according to this embodiment consists of a pair of filter plates 1.
A pair of filter frames 2.2 are sandwiched between the P frames 2.2 and a pressing furnace plate 3 is sandwiched between the pair of P frames 2.2, and a cathode-side conductive plate 4 is fixed to the opposing surface of each furnace plate 1. , an anode-side conductive plate 5 is provided on the surface of the pressing furnace plate 3 facing the filter plate l, and I cloth 6.6 is hung so as to cover both sides of the furnace frame 2.2, respectively. A chamber 7 surrounded by a filter cloth 6 and 6 is placed within the frame of the door frame 2 by inserting a filter cloth 2 between the filter plate 3 and the compressor filter plate 3 respectively.
After the stock solution is pressurized into the chamber 7, electroosmotic dehydration is performed by applying a DC voltage to the conductive plates 4 and 5, and the liquid components in the stock solution are transferred to the cathode conductive plate side of the filter plate l. The solid components are moved to the outside of the machine through the I cloth 6 and discharged from the filtrate recovery path of the furnace plate 2, and the solid components are drawn to the anode conductive plate side of the compressor 3 and remain in the P chamber 7. This method performs electroosmotic dehydration on the stock solution. In FIG. 1, 15 is a stock solution supply hole, and 30 and 31 are electrode connection terminals, respectively. In addition, in FIG. 3, reference numeral 8 denotes handles 9, 1, 1, 1, filter frames 2, 2, and each handle 9 protruding from both sides of the press door plate 3, respectively. ..., 9
The guide rail on which the slides, IO is the drive device 1! It is a movable plate that moves back and forth by the drive of the drive device 11.
The pressing furnace plate 3 is moved back and forth along the guide rail 8 to close or open the mold relative to the parent plate 12.

上記各I仮1は、第4.5図に示すように、その−側面
の上下角部に夫々貫通したろ液回収用貫通孔22.22
に連通しかつ上下方向に延びた多数の縦溝1a、・・・
、laを有する胛液排出用凹部1bを備える。この凹部
ibを有する上記−側面には、上記入角形状導電IfL
4で上記部1bを覆い、かつ該導電板4の外周縁部を多
数のボルト13.・・、13て上記−側面に固着する。
As shown in Fig. 4.5, each of the above I temporary 1 has through-holes 22 and 22 for filtrate recovery penetrated through the upper and lower corners of the side surface thereof, respectively.
A large number of vertical grooves 1a communicating with and extending in the vertical direction,...
, la is provided. The above-mentioned side surface having this recessed portion ib has the above-mentioned rectangular shape conductive IfL.
4 to cover the portion 1b, and the outer peripheral edge of the conductive plate 4 is secured to a large number of bolts 13. ..., 13 and the above-mentioned - adhere to the side surface.

この導電板4は、上記四部1bに対向する部分に多数の
孔4a、・・・、4aを有して、ア液が鎖孔4a、・・
・、4aを通って凹部1b内に入り込み、炉液回収口2
2から排出されるようにする。上記導電板4には、第6
.7図に示すように、炉板lに固定された陰極側の接続
棒14が接続される。なお、第4図中、15は原液供給
用貫通孔、21は圧搾空気供給用貫通孔である。
This conductive plate 4 has a large number of holes 4a, .
・It enters into the recess 1b through 4a and enters the furnace liquid recovery port 2.
Allow it to be discharged from 2. The conductive plate 4 includes a sixth
.. As shown in FIG. 7, a connecting rod 14 on the cathode side fixed to the furnace plate l is connected. In addition, in FIG. 4, 15 is a through hole for supplying the stock solution, and 21 is a through hole for supplying compressed air.

また、上記各I枠2は、第8.9図に示すように、中央
部に貫通した穴2aを有し、該穴内周面2bが、第1O
図に示すように、)戸板1側に向かうに従い上記穴2a
が小径となるように傾斜するとともに、上記炉枠2の上
部角部に貫通した原液供給孔15を備え、該原液供給孔
15を、第8゜11図に示すような3個の貫通孔16.
・・・、16を介して、上記穴2aに連通させて、原液
を原液供給孔15から上記穴2a内に供給できるように
する。なお、?枠工側の一対の貫通孔のうち左側の貫通
孔21は圧搾空気供給用のものであり、右側の貫通孔2
2はI液回収用のものである。
Furthermore, each of the I-frames 2 has a hole 2a penetrating through the center, and the inner circumferential surface 2b of the hole is connected to the first O.
As shown in the figure, the above hole 2a goes toward the door plate 1 side.
The furnace frame 2 is inclined so that it has a small diameter, and is provided with a stock solution supply hole 15 penetrating the upper corner of the furnace frame 2, and the stock solution supply hole 15 is connected to three through holes 16 as shown in FIGS. ..
..., 16 to communicate with the hole 2a, so that the stock solution can be supplied from the stock solution supply hole 15 into the hole 2a. In addition,? Of the pair of through holes on the frame work side, the left through hole 21 is for supplying compressed air, and the right through hole 2 is for supplying compressed air.
2 is for recovering I liquid.

また、上記圧搾炉板3は、第12.13図に示すように
、戸板本体3aの両側面に四部3bを夫々備える。この
各凹部3bには、入角形状の導電板支持板17を上記凹
部3bに対して出入自在にはめ込む。この圧搾炉板3に
は、その両側面のほぼ全面を被覆する弾性膜18を圧搾
戸板上側から掛けて、弾性膜18の両端をν板下端にボ
ルト19゜・・、19で固定するとともに弾性膜18の
中央部をI枠本体上部にピン20.20で支持する。上
記陽極側導電板5は、上記導電板支持板17とほぼ同形
状であって、上記弾性膜18を介してこの導電板支持板
17に対向するように導電性ボルト25、・・・、25
で導電板支持板I7に固着する。上記圧搾ろ板3の下部
角部には空気供給用貫通孔21を備えて、該貫通孔21
が、貫通孔24を介して、上記導電板支持板17と戸板
本体3aと弾性膜18との間に形成された隙間23に連
通して、圧搾空気がこの隙間23内に供給されて弾性膜
18が膨張し、導電板支持板I7が陽極側導電板5と一
体的に戸板本体3aに対して上記導電板4側に移動する
ようにする。上記導電板5と圧搾炉板3に固定された2
本の陽極側接続棒26とは弾性的に接続される。すなわ
ち、第14.15図に示すように、陽極側の各接続棒2
6の一端を圧搾戸板3の側部に固定するとともに、該接
続棒26の他端に編組みされて可撓自在なシールド線2
7の一端を導電性ボルト28で固定する一方、該シール
ド線27をU字状に湾曲させてその他端を導電板支持板
17の裏面に、該支持板17と導電板5とを固着する上
記導電性ボルト28aで固定する。従って、弾性膜18
が膨張して導電板5が導電板支持板17とともに一体的
に移動しても、上記シールド線27の湾曲部分が開くだ
けで接続棒26と陽極側導電板5とは常時接続されるよ
うにする。なお、各圧搾ろ板3の上下中央部には、第1
6図(a)に示すように一対の穴3c、3cを備えると
ともに、上記導電板支持板17の穴17aに一端+7b
が嵌合されたガイド17cを固定し、このガイド17c
を上記圧搾ろ板3の穴3C内に移動自在にはめ込んで、
弾性膜18とともに導電板支持板17が移動するとき、
第16図(b)に示ずようにガイド17Cにより導電板
支持板17を介して導電板5がろ板面に対して平行に移
動するようにする。
Further, as shown in FIG. 12.13, the pressing furnace plate 3 includes four parts 3b on both sides of the door plate main body 3a. A conductive plate support plate 17 having an angular shape is fitted into each of the recesses 3b so as to be able to move in and out of the recess 3b. An elastic membrane 18 covering almost the entire surface of both sides of the pressing furnace plate 3 is hung from the upper side of the pressing door plate, and both ends of the elastic membrane 18 are fixed to the lower end of the ν plate with bolts 19°, 19. The center portion of the membrane 18 is supported by pins 20 and 20 on the top of the I-frame body. The anode-side conductive plate 5 has almost the same shape as the conductive plate support plate 17, and the conductive bolts 25, .
and fix it to the conductive plate support plate I7. The lower corner of the pressing filter plate 3 is provided with an air supply through hole 21.
However, the through hole 24 communicates with the gap 23 formed between the conductive plate support plate 17, the door plate main body 3a, and the elastic membrane 18, and compressed air is supplied into this gap 23 to close the elastic membrane. 18 expands, and the conductive plate support plate I7 moves integrally with the anode side conductive plate 5 toward the conductive plate 4 side with respect to the door plate main body 3a. 2 fixed to the conductive plate 5 and the pressing furnace plate 3
It is elastically connected to the anode side connecting rod 26 of the book. That is, as shown in Fig. 14.15, each connecting rod 2 on the anode side
6 is fixed to the side of the pressing door plate 3, and a flexible shield wire 2 is braided to the other end of the connecting rod 26.
7 is fixed with a conductive bolt 28, while the shield wire 27 is bent into a U-shape and the other end is fixed to the back surface of the conductive plate support plate 17, thereby fixing the support plate 17 and the conductive plate 5. It is fixed with conductive bolts 28a. Therefore, the elastic membrane 18
Even if the conductive plate 5 expands and moves together with the conductive plate support plate 17, the curved portion of the shield wire 27 opens, and the connecting rod 26 and the anode side conductive plate 5 are always connected. do. In addition, in the upper and lower center of each pressing filter plate 3,
6 (a), a pair of holes 3c, 3c are provided, and one end +7b is provided in the hole 17a of the conductive plate support plate 17.
fixes the guide 17c fitted with the guide 17c.
is movably fitted into the hole 3C of the squeeze filter plate 3,
When the conductive plate support plate 17 moves together with the elastic membrane 18,
As shown in FIG. 16(b), the conductive plate 5 is moved parallel to the filter plate surface via the conductive plate support plate 17 by the guide 17C.

さらに、上記?布6.6は、上記圧搾r仮3の両側面に
上方から掛けるように配置する。また、他のr布6は、
各炉板lと各P枠2との間に挟み込むように配置して、
圧搾)戸板3と炉枠2との間の炉布6と、″>戸板1と
炉枠2との間のろ布6とで炉枠2内にろ布6で囲まれた
I室7を形成するようにして、炉枠2内に供給された原
液のうち、液体成分はI布6を通って炉板l側のろ液回
収用貫通孔22から機外に排出される一方、原液のうち
の固体成分がろ室7内に残るようにする。
Furthermore, the above? The cloth 6.6 is arranged so as to be hung from above on both sides of the compressed cloth 3. In addition, the other r cloth 6 is
Arranged so as to be sandwiched between each furnace plate l and each P frame 2,
Compression) The furnace cloth 6 between the door plate 3 and the furnace frame 2 and the filter cloth 6 between the door plate 1 and the furnace frame 2 create an I chamber 7 surrounded by the filter cloth 6 in the furnace frame 2. The liquid component of the stock solution supplied into the furnace frame 2 passes through the I cloth 6 and is discharged outside the machine from the filtrate collection through hole 22 on the furnace plate L side. The solid components remain in the filter chamber 7.

上記構成によれば、第1図、第2図(a)及び第3図に
示すように、上記駆動装置Itの駆動により可動板10
を親板12側に移動させて各戸板lなどを締め付けて、
第2図(b)に示すように、各炉枠2内にr布6.6で
囲まれたI室7を形成し、該)2室7内にろ枠2の原液
供給孔15.15から原液を圧入する。原液供給孔15
.15を閉じ、圧搾)戸板3の弾性膜18とろ板本体3
a及び導電板支持板17との隙間23に圧搾空気を供給
して弾性膜18を膨張させ、第2図(C)に示すように
、ろ板本体3aに対して導電板支持板17を導電板5と
ともに一体的に?板側に移動させて、原液を圧搾−過す
る。そして、両部電板4.5に直流電圧を印加して、電
気泳動現象を生ぜしめて、原液中の液体成分を戸板1の
陰極導電板4側に移動させる一方、原液中の固体成分を
圧搾1板3の陽極導電板5側に移動させて、電気浸透脱
水を行う。
According to the above configuration, as shown in FIGS. 1, 2(a) and 3, the movable plate 10 is driven by the drive device It.
Move it to the main plate 12 side and tighten each door plate l etc.
As shown in FIG. 2(b), an I chamber 7 surrounded by an R cloth 6.6 is formed in each furnace frame 2, and the stock solution supply holes 15.15 of the filter frame 2 are provided in the two chambers 7. Pressure in the stock solution. Stock solution supply hole 15
.. 15 and press) the elastic membrane 18 of the door plate 3 and the filter plate main body 3
compressed air is supplied to the gap 23 between the filter plate main body 3a and the conductive plate support plate 17 to expand the elastic membrane 18, and as shown in FIG. Integrated with board 5? Move to the plate side and squeeze and filter the stock solution. Then, a DC voltage is applied to the electric plates 4.5 on both sides to cause an electrophoresis phenomenon, and the liquid components in the stock solution are moved to the cathode conductive plate 4 side of the door plate 1, while the solid components in the stock solution are squeezed out. 1 to the anode conductive plate 5 side of the plate 3 to perform electroosmotic dehydration.

この導電板5及び導電板支持板17は、導電板5がろ枠
2の穴2aの内周面2bに接触するまで移動して、さら
に電気浸透脱水を行う。電気浸透脱水が終了すると、駆
動装置itにより可動板10を後退させてろ板1,1,
57’枠2,2、圧搾r仮3を開き、各ろ枠2内に残っ
た原液中の固体成分であるケーキを炉枠2の穴2aから
排出し、このケーキの排出が完了しかつ各ろ布6の洗a
トなどが終了すると、再び、駆動装置11により可動板
lOを而進さ什て1阪1 、 I 、’、戸枠2.2、
圧搾炉板3を親板12側に型閉めして、次の電気浸透脱
水に備える。
The conductive plate 5 and the conductive plate support plate 17 are moved until the conductive plate 5 contacts the inner circumferential surface 2b of the hole 2a of the filter frame 2, and further electroosmotic dehydration is performed. When the electroosmotic dehydration is completed, the movable plate 10 is moved backward by the drive device IT, and the filter plates 1, 1,
57' Frames 2, 2 and compressor 3 are opened, and the cake, which is a solid component in the stock solution, remaining in each filter frame 2 is discharged from the hole 2a of the furnace frame 2. When the discharge of this cake is completed, each Washing the filter cloth 6 a
When the operation is completed, the movable plate 10 is advanced again by the drive device 11, and the door frame 2.2 is moved forward again.
The pressing furnace plate 3 is mold-closed to the parent plate 12 side to prepare for the next electroosmotic dehydration.

える。I can do it.

発明の効果 上記構成によれば、ろ室内の原液を電気浸透脱水すると
き、弾性膜を膨張させて陽極側の導電板を陰極側の導電
板に近付けて両導電板間の間隔を小さくしながら、両導
電板間に直流通電するようにしたので、汚泥の電気抵抗
がさほど増加せず、電極間に高い電圧を加えなくとも十
分に電気浸透を生じさせるための電流値を維持すること
ができ、効率の良い脱水処理を行なうことができろ。
Effects of the Invention According to the above configuration, when electroosmotic dehydration is performed on the stock solution in the filtration chamber, the elastic membrane is expanded to bring the conductive plate on the anode side closer to the conductive plate on the cathode side, thereby reducing the gap between both conductive plates. Since direct current was applied between both conductive plates, the electrical resistance of the sludge did not increase significantly, and the current value sufficient to cause electroosmosis could be maintained without applying a high voltage between the electrodes. , to be able to perform efficient dehydration processing.

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

第1図は本発明の一実施例にかかる電気浸透脱水装置の
概略的な要部分解説明図、第2図(a)〜(C)は夫々
上記電気浸透脱水装置の作動を説明する概略説明図、第
3図は上記電気浸透脱水装置の側面図、第4.5図は夫
々戸板の正面図及び断面側面図、第6,7図は夫々接続
棒と導電板との接続状態を説明するための要部正面図及
び要部断面平面図、第8.9図は夫々炉枠の正面図及び
側面図、第10.11図は夫々第8図のX−X線断面図
及び第8図のXI−XI線部分断面図、第12.13図
は夫々圧搾胛板の正面図及び断面側面図、第14゜15
図は夫々接続棒と導電板との接続状態を説明するための
要部正面図及び要部断面平面図、第16図(a) 、 
(b)は夫々圧搾胛板の要部拡大断面図、第17図は従
来の電気浸透脱水装置の要部断面側面図である。 I・・・′/3仮、2・・・炉枠、2a・・・穴、3・
・・圧搾ろ板、4.5 ・導電板、6・・・Y布、7・
・・ろ室、8・・・ガイドレール、9・・・把手、IO
・・・可動板、11・・・駆動装置、12・・・親板、
13.+ 9.25,28.・・・ボルト、14.26
・・・接続環、15 ・原液供給用貫通孔、16.24
・・・貫通孔、17・・導電板支持板、18・・・弾性
膜、20・・・ビン、2I・・・圧搾空気供給用貫通孔
、22・・・f液回収用貫通孔、27・・シールド線。 特許出願人 神鋼ファウドラー株式会社はか1名 代理人 弁理士 青 山 係 ほか2名第1図 第162(a) C 第16図(b)′ 氏 搾 ヂし k I’7c 第17図
FIG. 1 is a schematic exploded view of essential parts of an electroosmotic dehydration device according to an embodiment of the present invention, and FIGS. 2(a) to (C) are respectively schematic explanations explaining the operation of the electroosmotic dehydration device. Figures 3 and 3 are side views of the electroosmotic dewatering device, Figures 4 and 5 are front views and cross-sectional side views of the door plate, respectively, and Figures 6 and 7 respectively explain the connection between the connecting rod and the conductive plate. Figure 8.9 is a front view and side view of the furnace frame, respectively, Figure 10.11 is a cross-sectional view taken along the line X--X of Figure 8, and Figure 8. Figures 12 and 13 are a front view and a cross-sectional side view of the pressing plate, respectively.
The figures are a front view of the main part and a cross-sectional plan view of the main part, respectively, for explaining the connection state between the connecting rod and the conductive plate, and Fig. 16(a).
(b) is an enlarged cross-sectional view of a main part of a pressing plate, and FIG. 17 is a cross-sectional side view of a main part of a conventional electroosmotic dewatering device. I...'/3 provisional, 2...furnace frame, 2a...hole, 3.
... Press filter plate, 4.5 - Conductive plate, 6... Y cloth, 7.
...Filter chamber, 8...Guide rail, 9...Handle, IO
... Movable plate, 11... Drive device, 12... Main plate,
13. +9.25,28. ...Bolt, 14.26
... Connection ring, 15 ・Through hole for stock solution supply, 16.24
... Through hole, 17... Conductive plate support plate, 18... Elastic membrane, 20... Bottle, 2I... Through hole for compressed air supply, 22... Through hole for f liquid recovery, 27 ··Shielded wire. Patent Applicant Shinko Faudler Co., Ltd. (1 agent) Patent Attorney Aoyama and 2 others Figure 1 Figure 162 (a) C Figure 16 (b)' Mr. Shijishik I'7c Figure 17

Claims (1)

【特許請求の範囲】[Claims] (1)隣接したろ板(1、3)間にろ布(6、6)によ
り囲まれたろ室(7)を形成するとともに、一方のろ板
(3)に第1導電板(5)を備える一方、上記他方のろ
板(1)に第2導電板(4)を備え、上記第1導電板(
5)と第2導電板(4)に夫々相反する電極を接続して
上記ろ室(7)内の原液に直流電圧を印加し、原液に対
して電気浸透脱水を行うようにした電気浸透脱水装置に
して、 上記一方のろ板(3)は、ろ板本体(3a)の他方のろ
板(1)に対向する面に弾性膜(18)を備えるととも
に、該弾性膜(18)を膨張させる流体を弾性膜(18
)と上記ろ板本体(3a)との間に供給する流体供給通
路(24、21)を上記ろ板本体(3a)に備え、かつ
該弾性膜(18)の外面に上記第1導電板(5)を固定
して、上記弾性膜(18)の弾性膨張により該第1導電
板(5)が上記第2導電板側に移動するようにしたこと
を特徴とする電気浸透脱水装置。
(1) A filter chamber (7) surrounded by filter cloth (6, 6) is formed between adjacent filter plates (1, 3), and a first conductive plate (5) is provided on one filter plate (3). On the other hand, the other filter plate (1) is provided with a second conductive plate (4), and the first conductive plate (
5) and the second conductive plate (4), respectively, and apply a DC voltage to the stock solution in the filtration chamber (7) to perform electroosmotic dehydration on the stock solution. In the apparatus, one filter plate (3) is provided with an elastic membrane (18) on the surface of the filter plate main body (3a) facing the other filter plate (1), and the elastic membrane (18) is expanded. The elastic membrane (18
) and the filter plate main body (3a), the filter plate main body (3a) is provided with a fluid supply passage (24, 21) for supplying fluid between the filter plate main body (3a), and the first conductive plate ( 5) is fixed, and the first conductive plate (5) is moved toward the second conductive plate by elastic expansion of the elastic membrane (18).
JP60196934A 1985-09-05 1985-09-05 Electroosmotic dehydrator Granted JPS6257622A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60196934A JPS6257622A (en) 1985-09-05 1985-09-05 Electroosmotic dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60196934A JPS6257622A (en) 1985-09-05 1985-09-05 Electroosmotic dehydrator

Publications (2)

Publication Number Publication Date
JPS6257622A true JPS6257622A (en) 1987-03-13
JPH0513686B2 JPH0513686B2 (en) 1993-02-23

Family

ID=16366086

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60196934A Granted JPS6257622A (en) 1985-09-05 1985-09-05 Electroosmotic dehydrator

Country Status (1)

Country Link
JP (1) JPS6257622A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02131200A (en) * 1988-11-08 1990-05-18 Shinko Pantec Co Ltd Electroendosmosis dehydration process for service water sludge
JPH02172521A (en) * 1988-12-23 1990-07-04 Shinko Pantec Co Ltd Squeezing filtration structure of electric penetration extractor
US5034111A (en) * 1988-12-28 1991-07-23 Shinko Pantec Co., Ltd. Compressive and electro-osmotic dehydrator
DE10007438C1 (en) * 2000-02-18 2001-06-07 Hoesch & Soehne Eberhard Filter press for filtering suspensions has electrodes for producing an electrical field formed from the pressing fluid chamber filled in the filtration operation with an electrically conducting pressing fluid
JP2002233874A (en) * 2001-02-09 2002-08-20 Nippon Chemicon Corp Electrosmosis apparatus
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

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50143155A (en) * 1974-05-02 1975-11-18

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50143155A (en) * 1974-05-02 1975-11-18

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02131200A (en) * 1988-11-08 1990-05-18 Shinko Pantec Co Ltd Electroendosmosis dehydration process for service water sludge
JPH02172521A (en) * 1988-12-23 1990-07-04 Shinko Pantec Co Ltd Squeezing filtration structure of electric penetration extractor
US5034111A (en) * 1988-12-28 1991-07-23 Shinko Pantec Co., Ltd. Compressive and electro-osmotic dehydrator
DE10007438C1 (en) * 2000-02-18 2001-06-07 Hoesch & Soehne Eberhard Filter press for filtering suspensions has electrodes for producing an electrical field formed from the pressing fluid chamber filled in the filtration operation with an electrically conducting pressing fluid
JP2002233874A (en) * 2001-02-09 2002-08-20 Nippon Chemicon Corp Electrosmosis apparatus
JP4638615B2 (en) * 2001-02-09 2011-02-23 日本ケミコン株式会社 Electroosmosis equipment
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
JPH0513686B2 (en) 1993-02-23

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