JPH02111410A - Electrode composite diaphragm of electroosmotic press dehydrator - Google Patents
Electrode composite diaphragm of electroosmotic press dehydratorInfo
- Publication number
- JPH02111410A JPH02111410A JP63263524A JP26352488A JPH02111410A JP H02111410 A JPH02111410 A JP H02111410A JP 63263524 A JP63263524 A JP 63263524A JP 26352488 A JP26352488 A JP 26352488A JP H02111410 A JPH02111410 A JP H02111410A
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- plate
- diaphragm
- electrode plate
- electroosmotic
- 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
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Sludge (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、下水汚泥等の被脱水処理液を加圧により圧搾
脱水しながら直流通電して電気浸透作用により脱水度の
向」二を図る装置、特にフィルタープレス形式の電気浸
透圧搾脱水機に使用される電極が複合された圧搾ダイA
・フラムの改良構造に関する。[Detailed Description of the Invention] (Industrial Application Field) The present invention aims at increasing the degree of dehydration by electroosmotic action by applying direct current to a liquid to be dehydrated, such as sewage sludge, while compressing and dehydrating it under pressure. Pressing die A combined with electrodes used in a device, especially a filter press type electroosmotic press dehydrator
・Regarding the improved structure of the flam.
(従来の技術)
フィルタープレス形式の電気浸透圧搾脱水機は、例えば
先願にかかる特開昭62−125810号、同一125
811号、同一125812号等に開示されている。第
6図(イ)(ロ)および(ハ)はこの種脱水機の基本構
成と操作段階の概略を示す。(Prior art) A filter press type electroosmotic press dehydrator is disclosed in, for example, Japanese Patent Application Laid-Open No. 62-125810 and No. 125 of the same patent application.
No. 811, No. 125812, etc. Figures 6(a), 6(b) and 6(c) schematically show the basic configuration and operating steps of this type of dehydrator.
第6図(イ)の段階では、フィルタープレスの濾枠(a
)(a)をその間に濾布(b)(b)、ダイヤフラム(
C)を挾んで閉じ締付け、被脱水処理液の汚泥を原液入
口(d)から原液ポンプにより濾布間に圧太し、濾布を
透過した濾水を濾水出口(e)から排出して1次脱水す
る。第6図(ロ)の段階では、ダイヤフラム(C)の背
面側に圧搾圧力を導入して前面側に膨張させ、さらに固
化した汚泥ケーキ中の水分を搾出して2次脱水する。こ
の圧1窄脱水の後期の段階で濾室内のダイヤフラム側の
電極(「)と対の電極(「゛)との間に直流通電して電
気浸透脱水作用によりさらに脱水を促進し3次脱水する
。その後、第6図(ハ)のように濾枠(a)(a)の開
き濾布(b) (b)を引下げて最終脱水ケーキ(g)
を機外に取出す。At the stage shown in Figure 6 (a), the filter frame (a) of the filter press is
) (a) between which the filter cloth (b) (b) and the diaphragm (
C) is clamped and tightened, the sludge of the liquid to be dewatered is compressed between the filter cloths from the raw solution inlet (d) by the raw solution pump, and the filtrate that has passed through the filter cloth is discharged from the filtrate outlet (e). Perform primary dehydration. In the stage shown in FIG. 6(b), squeezing pressure is introduced to the back side of the diaphragm (C) to expand it to the front side, and further water in the solidified sludge cake is squeezed out for secondary dehydration. At the latter stage of this pressure 1 dehydration, a direct current is applied between the electrode on the diaphragm side ('') in the filter chamber and the opposite electrode ('') to further promote dehydration through electroosmotic dehydration, resulting in tertiary dehydration. Then, as shown in Figure 6 (c), open the filter frame (a) and pull down the filter cloth (b) to remove the final dehydrated cake (g).
Take it out of the machine.
前記の機械的加圧の2次脱水では脱水ケーキの含水率は
80〜85%程度に到達させるのが限度で、加圧力、加
圧時間を増しても脱水効果は殆ど上がらない。これに対
して圧搾脱水中に例えば40Vで15分間直流通電して
電気浸透併用圧搾脱水すると、含水率は50%まで低下
し、脱水ケーギ体積を顕著に減少させることができる。In the above-mentioned secondary dehydration using mechanical pressure, the moisture content of the dehydrated cake can only reach about 80 to 85%, and the dehydration effect hardly improves even if the pressure and time are increased. On the other hand, if the press dehydration is performed in combination with electroosmosis by applying a direct current at 40 V for 15 minutes during press dehydration, the water content can be reduced to 50% and the volume of the dehydration cage can be significantly reduced.
このように電気浸透脱水機の電極は、直流通電による電
気化学的作用により消耗する他、−体結合されたダイヤ
フラムからの圧搾による強力な機械的作用力を受けるの
で、従来、ステンレス象1、ニッケル鋼、白金被1貰チ
タニウム(反、炭素焼結板等からなる各種の材料および
構造の電極が提案され使用されている。In this way, the electrodes of an electroosmotic dehydrator are not only worn out by the electrochemical action caused by direct current, but also receive strong mechanical action from the compression from the diaphragm, which is connected to the body. Electrodes of various materials and structures have been proposed and used, including steel, platinum-coated titanium, carbon sintered plates, etc.
(発明が解決しようとする課題)
電気浸透脱水機のダイヤフラムに一体結合される電極は
金属板製とすれば曲げ強度が大きい点で有利な構造にす
ることができるが電気化学作用の点でそれぞれ弱点があ
る。炭素焼結板等の電極は電気浸透作用に有利な材質の
ものにする必要があり、特殊な炭素材製となるので、概
ね脆硬で変形せず、強度上分割構造にしないと大きな受
圧力により破損するが、可撓性のダイヤフラムに分割電
極を取付ける構造とする場合、各分割電極の均等な通電
の困難、個別補強構造、取付構造の複雑化、電極経由通
水路の確保の困難、電極反応の影響を受は易い点等に関
し弱点がある。(Problems to be Solved by the Invention) If the electrodes that are integrally connected to the diaphragm of an electroosmotic dehydrator are made of metal plates, they can have an advantageous structure in terms of high bending strength, but they have different structures in terms of electrochemical action. There are weaknesses. The electrode, such as a carbon sintered plate, must be made of a material that is advantageous for electroosmotic action, and since it is made of a special carbon material, it is generally brittle and does not deform, and for strength reasons, it will receive a large amount of pressure unless it has a split structure. However, if the split electrode is attached to a flexible diaphragm, it will be difficult to apply electricity evenly to each split electrode, the individual reinforcement structure will be complicated, the mounting structure will be complicated, it will be difficult to secure a water passage through the electrode, and the electrode will be damaged. It has weaknesses in that it is easily influenced by reactions.
本発明は、従来技術のこれらの弱点が解消乃至軽減され
た電気浸透圧搾脱水機の電極複合ダイヤフラムの改良構
造を創作することを課題とする。An object of the present invention is to create an improved structure of an electrode composite diaphragm for an electroosmotic press-dehydrator in which these weaknesses of the prior art are eliminated or alleviated.
(課題を解決するための手段)
前記課題は、本発明においては、フィルタープレス型電
気浸透圧搾脱水機の電極複合ダイヤフラムとして、可撓
性のダイヤフラム基板とのその表面側に添設される電極
板とからなり、電極板が各独立の分割電極板により構成
され、かつダイヤフラム基板が分割電極板群に対応する
中央の領域を埋込み金属芯により補強されてその電極側
に各分割型)へと金属芯とを電気接続する各給電板が露
出する以外の領域は絶縁性、耐蝕性被膜により被覆され
た複合構造とすることにより達成される。(Means for Solving the Problem) In the present invention, as an electrode composite diaphragm of a filter press type electroosmotic press dehydrator, an electrode plate attached to a surface side of a flexible diaphragm substrate is provided. The electrode plate is composed of each independent divided electrode plate, and the diaphragm substrate is reinforced with an embedded metal core in the center area corresponding to the divided electrode plate group, and the electrode side is made up of metal (each divided type). This is achieved by forming a composite structure in which areas other than the exposed areas of each power supply plate electrically connected to the core are covered with an insulating and corrosion-resistant coating.
(作 用)
本発明においては、次の諸作用により従来技術の問題点
が解決される。(Function) In the present invention, the problems of the prior art are solved by the following functions.
(【)ダイヤフラム基体は金属芯の存在する中央の領域
以外の周領域は基体の可撓性材料の11り構造であるの
で、背面側に作用する圧搾圧力により前面側に移動し膨
張して本来の圧搾作用を遂行する。([) The circumferential area of the diaphragm base other than the central area where the metal core exists is made of a flexible material, so it moves to the front side and expands due to the squeezing pressure acting on the back side. Performs the squeezing action of
(II)電極は分割されていても、それらの背後側に接
するダイヤフラム基体の金属芯により一括して補強作用
を受け、各分割電極板は圧搾圧力による大きな曲げ作用
力が加わらないようになっているので、電極の破損が生
じ難い。(II) Even if the electrodes are divided, they are collectively reinforced by the metal core of the diaphragm base that is in contact with the rear side, and each divided electrode plate is prevented from being subjected to large bending force due to squeezing pressure. Therefore, damage to the electrodes is less likely to occur.
(III)各分割電極板に対する通電は、金属芯を経由
しその表面側に露出する各対応給電板に各分割電極板が
圧搾力により圧接することによりなされるので、金属芯
の一部に対し通電すれば各分割電極板に対する均等な通
電状態が得られる。分割電極構造であっても相互間に電
気的連結をとる必要はない。(III) Electricity is applied to each divided electrode plate by pressing each divided electrode plate into contact with each corresponding power supply plate exposed on the surface side through the metal core, so that a part of the metal core is When energized, a uniform energization state can be obtained for each divided electrode plate. Even with a split electrode structure, there is no need for electrical connection between them.
(IV)ダイヤフラム基体における金属芯は、周シール
される給電板以外は絶縁性、耐蝕性被膜により全面被覆
されているので、電解反応時に電極の表面に発生する酸
、アルカリに対して完全に耐蝕的に防護される。(IV) The metal core of the diaphragm base is completely covered with an insulating and corrosion-resistant coating, except for the power supply plate that is sealed around the periphery, so it is completely corrosion-resistant against acids and alkalis generated on the surface of the electrode during electrolytic reactions. protected.
(V)個別分割電極は給電板に密接しかつ簡単な止めビ
スにより結合可能であるので分割電極板の着脱、取替え
が容易である。(V) Since the individual divided electrodes are closely connected to the power supply plate and can be connected with a simple set screw, the divided electrode plates can be easily attached/detached and replaced.
(実施例)
以下、本発明の電気浸透圧搾脱水機の電極複合ダイヤフ
ラムを第1〜5図に示す実施例に即して具体的に説明す
る。(Example) Hereinafter, the electrode composite diaphragm of the electroosmotic press-dehydrator of the present invention will be specifically described with reference to Examples shown in FIGS. 1 to 5.
第1図は本発明実施例の1単位の電極複合ダイヤフラム
を正面側からみた斜視図である。この複合構造のダイヤ
フラムは、第6図に示すフィルタープレス型圧搾脱水機
のダイヤフラム(C)および電極(f)の複合体に相当
するものであって、濾枠(a)、濾布(b)、対の電極
(f゛)とともに第6図について説明したのと同様にし
て協働作用する。FIG. 1 is a perspective view of one unit of an electrode composite diaphragm according to an embodiment of the present invention, viewed from the front side. This composite structure diaphragm corresponds to the composite of the diaphragm (C) and electrode (f) of the filter press type compressor dehydrator shown in FIG. 6, and includes a filter frame (a), a filter cloth (b) , and the counter electrode (f') cooperate in the same manner as described with respect to FIG.
そのため、天然ゴム、ネオプレンゴム等の可撓性材料の
ダイヤフラム基板(1)と電極板(2)とからなり、電
極板(2)はこの例では4分割された各独立の分割電極
板(2A)となり、第1図にはその1つだけが基板(1
)の表面側に添設された取付状態で示されている。Therefore, it consists of a diaphragm substrate (1) made of a flexible material such as natural rubber or neoprene rubber, and an electrode plate (2). In this example, the electrode plate (2) is divided into four independent divided electrode plates (2A ), and only one of them is the substrate (1
) is shown attached to the front side.
ダイヤフラノ1基板(1)は角枠状の濾枠(a)の取付
座と外形を同じとし、その外周縁部(la) (第2図
参照)で密接させてこれに取付ける。外周縁部(la)
内の領域は濾室を形成する。分割電極板(2八)群に対
応するその中央の領域(1b)と外周縁部(la)との
間にはほぼ一定間隔で薄肉の可撓膜部(1c)が形成さ
れ、基板(1)の背面側に濾枠(b)乃至は背合せの他
の基板との間に導入された圧搾圧力によりこの部(lc
)で撓曲して中央領域(1b)が前進し、分割電極板(
2A)もともに前進し、濾布(b)(b)間に原液口(
1d)を通じて導入された汚泥を圧搾する。濾布(b)
を透過した汚水は、分割電極板(2八)の通孔(2a)
を通り抜け、中央領域(lb)の突起(1e)間の谷部
の通液路(le’) 、可撓膜部(1c)の突起(1f
)間の谷部の通液路(If’)および外周縁部(la)
に設けた濾水口(Ig)を経て、機外に流出するように
なっている。The diaphragm 1 substrate (1) has the same external shape as the mounting seat of the rectangular filter frame (a), and is attached to it in close contact with its outer peripheral edge (la) (see FIG. 2). Outer periphery (la)
The area within forms the filter chamber. Thin flexible membrane portions (1c) are formed at approximately regular intervals between the central region (1b) corresponding to the group of divided electrode plates (28) and the outer peripheral edge (la), and the substrate (1 ) on the back side of this part (lc
), the central region (1b) moves forward, and the divided electrode plate (
2A) move forward together, and the stock solution opening (
Squeezing the sludge introduced through 1d). Filter cloth (b)
The wastewater that has permeated through the through holes (2a) of the divided electrode plate (28)
, the liquid passageway (le') in the valley between the protrusions (1e) in the central region (lb), and the protrusion (1f) in the flexible membrane part (1c).
) and the outer peripheral edge (la) of the valley between
The water flows out of the machine through an inlet (Ig) installed in the machine.
本発明では4つの分割電極板(2A)群を圧搾力に対し
て同時に補強するため、ダイヤフラム基板(1)の対応
する中央領域(1b)内に鉄、チタニウム、アルミニウ
ム等の導電性の比較的良い金属板製の金属芯(3)を、
第2〜5図に示すように、埋込み状態にして設ける。金
属芯(3)が薄くて大きい圧搾力に対する補強作用が充
分でない場合は、第2図に示すように、基板の背面にポ
リプロピレン等の厚い補強板(4)を添設する。そして
金属芯(3)から基板(1)、補強板(4)を貫通して
後方に突出する植込みボルト(5)に直流電源からの給
電ケーブル(6)を止めナツト(7)により接続する。In the present invention, in order to simultaneously reinforce the four divided electrode plate (2A) groups against squeezing force, conductive materials such as iron, titanium, aluminum, etc. A metal core (3) made of a good metal plate,
As shown in FIGS. 2 to 5, it is provided in an embedded state. If the metal core (3) is too thin to provide sufficient reinforcement against large squeezing forces, a thick reinforcing plate (4) made of polypropylene or the like is attached to the back surface of the substrate, as shown in FIG. Then, a power supply cable (6) from a DC power source is connected to a stud bolt (5) that protrudes rearward from the metal core (3) through the substrate (1) and the reinforcing plate (4) using a locking nut (7).
金属芯(3)の前面側には、それと分割電極板(2A)
とを電気接続するための銅またはステンレス鋼製の給電
板(8)を各分割電極板に対応する位置に分布させて配
置し、ステンレス鋼製の枕頭ビス(9)により取付ける
。給電板(8)は第1図にみられるように各分割電極板
(2A)の4辺内寄りに対応する位置に配置されている
が、これは給電板を経て分割電極板に加わる圧搾圧力か
らする曲げ力の軽減を図り、分割電極板への均等通電を
図るためである。On the front side of the metal core (3), there is a split electrode plate (2A).
Copper or stainless steel power supply plates (8) for electrical connection are distributed and arranged at positions corresponding to each divided electrode plate, and are attached using stainless steel head screws (9). As shown in Figure 1, the power supply plate (8) is placed at a position corresponding to the inner side of each of the four sides of each divided electrode plate (2A), but this is due to the squeezing pressure applied to the divided electrode plate through the power supply plate. This is to reduce the bending force caused by the split electrode plate and to uniformly conduct electricity to the divided electrode plates.
そして給電板(8)以外の金属芯(3)の前面領域は、
基体(1)の後面、可撓膜部(1c)に連続するゴム質
等の絶縁性、耐蝕性の前面被膜(IA)で全面的に被覆
し、給電板(8)のみ露出させる。この前面被膜(1八
)には前記の突起(1e)が分布形成されており、分割
電極板(2A)の背面に接して分割電極板(2^)を給
電板(8)とともに背面から全面的に支持する。The front area of the metal core (3) other than the power supply plate (8) is
The rear surface of the base body (1) is entirely covered with an insulating and corrosion-resistant front coating (IA) made of rubber or the like that continues to the flexible membrane portion (1c), leaving only the power supply plate (8) exposed. The aforementioned protrusions (1e) are formed in a distributed manner on this front surface film (18), and the divided electrode plate (2^) is in contact with the back surface of the divided electrode plate (2A), and the divided electrode plate (2^) is attached to the entire surface from the back side together with the power supply plate (8). support.
このダイヤフラノ、基板(1)への分割電極板(2A)
の取付けは、第3図、第4図に示すように、その取付用
凹部(2b)にポリ塩化ビニール等のiすい絶縁性シー
ト00)を敷き、貫通するプラスチック材製止めビス(
11)により給電板(8)に嵌込むことにより行う。こ
の取付けはワンタッチででき、tfl耗分割電極板の新
品との取替えも迅速に行うことができる。This diaphragm, divided electrode plate (2A) into the substrate (1)
To install it, as shown in Figures 3 and 4, place an insulating sheet 00) made of polyvinyl chloride or the like in the mounting recess (2b), and insert a plastic fixing screw (00) that passes through it.
11) by fitting it into the power supply plate (8). This installation can be done with one touch, and the TFL worn-out split electrode plate can be quickly replaced with a new one.
各給電板(8)のシールのため、第3図、第5図に示す
ように、その周囲を前面被膜(1八)より僅かに突出す
るゴム質の環状部(1h)で囲んで置く。In order to seal each power supply plate (8), as shown in FIGS. 3 and 5, its periphery is surrounded by a rubber ring (1h) that slightly protrudes from the front surface coating (18).
この突出量は、分割電極板(2^)の取付けおよび圧搾
圧力により押潰され面一となるので、給電板(8)は周
囲からシールされるとともに給電板と分割電極板との通
電接触は確実になされる。This amount of protrusion is crushed and flushed by the mounting and squeezing pressure of the divided electrode plate (2^), so the power supply plate (8) is sealed from the surroundings and the current-carrying contact between the power supply plate and the divided electrode plate is prevented. It will definitely be done.
(発明の効果)
以上のように、本発明によると、電気浸透圧搾脱水機の
電極付圧搾ダイヤフラムとして、汚泥に対する圧搾圧力
の均等な印加が可能で、圧搾圧力に対し電極板は小面積
に分割され各独立の分割電極板は分割圧搾圧力を均等に
支承するので強度上保全され破損が起こらず、分割電極
板への通電径路が簡単で短く均等な電極間通電が行われ
、かつ電気浸透脱水に伴い生ずる腐蝕性環境から耐蝕的
に防護され、分割電極板の取付、取替を容易に行うこと
ができる等の効果が得られる。(Effects of the Invention) As described above, according to the present invention, as a squeezing diaphragm with an electrode for an electroosmotic squeezing dehydrator, it is possible to apply squeezing pressure evenly to sludge, and the electrode plate is divided into small areas in response to the squeezing pressure. Since each independent divided electrode plate supports the divided squeezing pressure equally, the strength is maintained and no damage occurs, and the current path to the divided electrode plates is simple and short, and even current is applied between the electrodes, and electroosmotic dehydration is achieved. Effects such as being protected against corrosion from the corrosive environment that occurs and making it possible to easily attach and replace the split electrode plate can be obtained.
第1図は本発明実施例の電気浸透圧搾脱水機の電極複合
ダイヤフラムを示すその正面側からみた一部分割電極板
取外し状態の斜視図、第2図はその電源接続を示す端部
の断面図、第3図はその分割電極板取付を示す端部の断
面図、第4図はその局部拡大断面図、第5図はその組立
前のダイヤフラム基板の給電板部分の断面図、第6図(
イ)はフィルタープレス型電気浸透圧搾脱水機の基本構
成と1操作段階を示す継断側面図、第6図(ロ)はその
異る操作段階の縦断側面図、第6図(ハ)はそのさらに
異なる操作段階の縦断側面図である。
(1)・・・ダイヤフラム基板、(IA)・・・前面被
膜、(la)・・・外周縁部、(1b)・・・中央領域
、(1c)・・・可撓膜部、(ld)・・・原液口、(
le) (If) ”・突起、(le’)(lf’)・
・・通液路、(1g)・・・濾水口、(lh)・・・環
状部、(2)・・・電極板、(2A)・・・分割電極板
、(2a)・・・通孔、(2b)・・・取付用凹部、(
3)・・・金属芯、(4)・・・補強板、(5)・・・
植込みボルト、(6)・・・給電ケーブル、(7)・・
・止めナツト、(8)・・・給電板、(9)・・・枕頭
ビス、00)・・・シート、(11)・・・止めビス、
(a)・・・濾枠、(b)・・・濾布、(C)・・・ダ
イヤフラム、(d)・・・原液入口、(e)・・・濾水
出口、(f)(f’)・・・電極、(2)・・・脱水ケ
ーキ。
第3図
(イ)
′す・
シ1
図
(ロン
第 42
(八ンFIG. 1 is a perspective view of an electrode composite diaphragm of an electro-osmotic press dehydrator according to an embodiment of the present invention, as seen from the front side with a partially divided electrode plate removed; FIG. 2 is a sectional view of the end showing the power connection; Fig. 3 is a cross-sectional view of the end showing the attachment of the divided electrode plate, Fig. 4 is a locally enlarged cross-sectional view, Fig. 5 is a cross-sectional view of the power supply plate portion of the diaphragm board before assembly, and Fig. 6 (
A) is a cross-sectional side view showing the basic configuration and one operating stage of a filter press type electroosmotic press-dehydrator, Fig. 6(B) is a vertical sectional side view of the different operating stages, and Fig. 6(C) is the same. FIG. 7 is a longitudinal side view of a further different stage of operation; (1)...Diaphragm substrate, (IA)...Front coating, (la)...Outer peripheral edge, (1b)...Central region, (1c)...Flexible film part, (ld )...Stock solution port, (
le) (If) ”・Protrusion, (le') (lf')・
...Liquid passage, (1g)...Drainage port, (lh)...Annular part, (2)...Electrode plate, (2A)...Divided electrode plate, (2a)...Connection Hole, (2b)...Mounting recess, (
3)...Metal core, (4)...Reinforcement plate, (5)...
Studded bolt, (6)...Power cable, (7)...
- Locking nut, (8)... Power supply plate, (9)... Pillow head screw, 00)... Seat, (11)... Locking screw,
(a)... Filter frame, (b)... Filter cloth, (C)... Diaphragm, (d)... Stock solution inlet, (e)... Filtrate outlet, (f) (f ')...electrode, (2)...dehydrated cake. Figure 3 (a)
Claims (1)
ヤフラムとして、可撓性のダイヤフラム基板とその表面
側に添設される電極板とからなり、電極板が各独立の分
割電極板により構成されかつダイヤフラム基板がその分
割電極板群に対応する中央の領域を埋込み金属芯により
補強されてその電極側に各分割電極と金属芯とを電気接
続する各給電板が露出する以外の領域は絶縁性、耐蝕性
被膜により被覆されていることを特徴とする電気浸透圧
搾脱水機の電極複合ダイヤフラム。The electrode composite diaphragm of the filter press type electroosmotic press dehydrator is composed of a flexible diaphragm substrate and an electrode plate attached to the surface side of the flexible diaphragm substrate, and the electrode plate is composed of independent divided electrode plates, and the diaphragm substrate The central region corresponding to the divided electrode plate group is reinforced with an embedded metal core, and the area other than the exposed power supply plate that electrically connects each divided electrode and the metal core on the electrode side is insulating and corrosion resistant. An electrode composite diaphragm for an electroosmotic press dehydrator, characterized in that it is covered with a film.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63263524A JPH0732850B2 (en) | 1988-10-19 | 1988-10-19 | Electrode compound diaphragm of electroosmotic dewatering machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63263524A JPH0732850B2 (en) | 1988-10-19 | 1988-10-19 | Electrode compound diaphragm of electroosmotic dewatering machine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02111410A true JPH02111410A (en) | 1990-04-24 |
| JPH0732850B2 JPH0732850B2 (en) | 1995-04-12 |
Family
ID=17390735
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63263524A Expired - Lifetime JPH0732850B2 (en) | 1988-10-19 | 1988-10-19 | Electrode compound diaphragm of electroosmotic dewatering machine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0732850B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0291609U (en) * | 1988-12-28 | 1990-07-20 | ||
| JP2014073480A (en) * | 2012-10-05 | 2014-04-24 | Fuji Xerox Co Ltd | Diaphragm for filter press and solid-liquid separator |
-
1988
- 1988-10-19 JP JP63263524A patent/JPH0732850B2/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0291609U (en) * | 1988-12-28 | 1990-07-20 | ||
| JP2014073480A (en) * | 2012-10-05 | 2014-04-24 | Fuji Xerox Co Ltd | Diaphragm for filter press and solid-liquid separator |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0732850B2 (en) | 1995-04-12 |
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