JPH0732850B2 - Electrode compound diaphragm of electroosmotic dewatering machine - Google Patents

Electrode compound diaphragm of electroosmotic dewatering machine

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Publication number
JPH0732850B2
JPH0732850B2 JP63263524A JP26352488A JPH0732850B2 JP H0732850 B2 JPH0732850 B2 JP H0732850B2 JP 63263524 A JP63263524 A JP 63263524A JP 26352488 A JP26352488 A JP 26352488A JP H0732850 B2 JPH0732850 B2 JP H0732850B2
Authority
JP
Japan
Prior art keywords
electrode
diaphragm
plate
electrode plate
dewatering machine
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
JP63263524A
Other languages
Japanese (ja)
Other versions
JPH02111410A (en
Inventor
史朗 近藤
健 諏訪
滋 佐野
Original Assignee
神鋼パンテック株式会社
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Filing date
Publication date
Application filed by 神鋼パンテック株式会社 filed Critical 神鋼パンテック株式会社
Priority to JP63263524A priority Critical patent/JPH0732850B2/en
Publication of JPH02111410A publication Critical patent/JPH02111410A/en
Publication of JPH0732850B2 publication Critical patent/JPH0732850B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • 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、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
向上を図る装置、特にフイ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ヤフ
ラムの改良構造に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention relates to a device for improving the degree of dehydration through electroosmosis by direct current application while pressing and dehydrating a liquid to be dehydrated such as sewage sludge by pressurization. In particular, it relates to an improved structure of a squeezing diaphragm in which electrodes are combined for use in a filter press type electroosmotic dewatering machine.

(従来の技術) フイ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−125811、同−12
5812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 dewatering machine is disclosed in, for example, Japanese Patent Application Laid-Open Nos. 62-125810, -125811 and -12.
No. 5812 is disclosed. FIGS. 6 (a), (b) and (c) show the basic structure of this type of dehydrator and the outline of its operating steps.

第6図(イ)の段階では、フイ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入し、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。この圧搾脱水の後期の段階で濾室内のダイヤフラム
側の電極(f)と対の電極(f′)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 of FIG. 6 (a), the filter frames (a) and (a) of the filter press are sandwiched between the filter cloths (b) and (b) and the diaphragm (c) to be tightened to remove the sludge of the liquid to be dehydrated. From the stock solution inlet (d), a stock solution pump is pressed between the filter cloths, and the filtered water that has passed through the filter cloth is discharged from the filtered water outlet (e) for primary dehydration. At the stage of FIG. 6 (b), the diaphragm (c)
The squeezing pressure is introduced to the back side to expand it to the front side, and the water in the solidified sludge cake is squeezed for secondary dehydration. At the latter stage of this squeezing dehydration, a direct current is applied between the diaphragm-side electrode (f) and the paired electrode (f ') in the filter chamber to further promote dehydration by the electroosmotic dehydration action and perform tertiary dehydration. Then, as shown in FIG. 6 (c), the filter frames (a) (a)
The open filter cloths (b) and (b) are pulled down and the final dehydrated cake (g) is taken 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
ーキ体積を顕著に減少させることができる。
In the mechanical dehydration secondary dehydration described above, the water content of the dehydrated cake is
The limit is to reach 80-85%, and the dehydration effect hardly increases even if the pressure and time are increased. On the other hand, when squeezing and dehydrating together with electro-osmosis by applying a direct current for 15 minutes at 40 V during squeezing and dehydrating, the water content decreases to 50%, and the dehydrated cake volume 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、一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、ステンレス鋼、ニッケル鋼、白金被覆チタニ
ウム板、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。
As described above, the electrode of the electroosmotic dehydrator is consumed by an electrochemical action due to direct current application, and receives a strong mechanical action force due to squeezing from the integrally connected diaphragm, so that the conventional stainless steel, nickel steel, Electrodes of various materials and structures such as platinum-coated titanium plates and carbon sintered plates have been proposed and used.

(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け易い点等に関
し弱点がある。
(Problems to be Solved by the Invention) If the electrode integrally connected to the diaphragm of the electroosmotic dehydrator is made of a metal plate, it can have an advantageous structure in that it has a large bending strength. There is a weakness. Electrodes such as carbon sintered plates need to be made of a material that is advantageous for electroosmotic action.Because they are made of a special carbon material, they are generally brittle and do not deform. However, if the split electrode is attached to a flexible diaphragm, it is difficult to evenly energize each split electrode, individual reinforcement structure, complicated mounting structure, difficult to secure water passage through electrode, electrode There is a weakness in that it is easily affected by the reaction.

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。
It is an object of the present invention to create an improved structure of an electrode composite diaphragm of an electroosmotic dewatering machine in which these weak points 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、フイルタープレス型電
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, the above-mentioned problem is, as an electrode composite diaphragm of a filter press type electroosmotic dewatering machine, a flexible diaphragm substrate and an electrode plate attached to the surface side thereof. The electrode plate is composed of independent split electrode plates, and the diaphragm substrate is embedded in the central region corresponding to the split electrode plate group and is reinforced by the metal core, and each split electrode and the metal core are provided on the electrode side. It is achieved by forming a composite structure in which the regions other than exposing the respective power supply plates for electrically connecting are electrically insulating and corrosion resistant coatings.

(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。
(Operation) In the present invention, the problems of the prior art are solved by the following actions.

(I)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膜構造であるので、
背面側に使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。
(I) Since the diaphragm substrate has a peripheral region other than the central region where the metal core is present, since it has a film structure of a flexible material of the substrate,
It moves to the front side by the pressing pressure used on the back side and expands to perform the original pressing action.

(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 back side of them, and each split electrode plate is prevented from being subjected to a large bending force due to the squeezing pressure. Therefore, the electrode is less likely to be damaged.

(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) Energization to each divided electrode plate is performed by pressing each divided electrode plate by pressing force to each corresponding power feeding plate exposed on the surface side through the metal core, If electricity is applied, an even energization state can be obtained for each divided electrode plate. Even with the divided electrode structure, it is not necessary to establish 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) Since the metal core in the diaphragm base is entirely covered with an insulating and corrosion-resistant coating except for the power supply plate to be circumferentially sealed, an acid generated on the surface of the electrode during the electrolytic reaction,
Completely corrosion resistant protection against alkali.

(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 in close contact with the power feeding plate and can be connected by a simple stop screw, the divided electrode plate can be easily attached / detached or 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 dewatering machine of the present invention will be specifically described with reference to the examples shown in FIGS.

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図に示すフイ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。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。
FIG. 1 is a perspective view of a unit electrode composite diaphragm of an embodiment of the present invention as seen from the front side. The diaphragm of this composite structure corresponds to a composite of the diaphragm (c) and the electrode (f) of the filter press type dewatering machine shown in FIG. 6, and includes a filter frame (a) and a filter cloth (b). , Paired electrodes (f ') cooperate in a manner similar to that described for FIG. Therefore, it is composed 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 electrode plates (2A). 1), only one of them is shown in the attached state attached to the front surface side of the substrate (1).

ダイヤフラム基板(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(1a)(第2図参照)
で密接させてこれに取付ける。外周縁部(1a)内の領域
は濾室を形成する。分割電極板(2A)群に対応するその
中央の領域(1b)と外周縁部(1a)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分(1c)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)を通過した汚水は、分
割電極板(2A)の通孔(2a)を通り抜け、中央領域(1
b)の突起(1e)間の谷部の通液路(1e′)、可撓膜部
(1c)の突起(1f)間の谷部の通液路(1f′)および外
周縁部(1a)に設けた濾水口(1g)を経て、機外に流出
するようになっている。
The diaphragm substrate (1) has the same outer shape as the mounting seat of the rectangular frame-shaped filter frame (a), and its outer peripheral edge portion (1a) (see FIG. 2).
And attach it closely. The area inside the outer peripheral edge (1a) forms a filter chamber. A thin flexible film portion (1c) is formed at a substantially constant interval between the central region (1b) corresponding to the divided electrode plate (2A) group and the outer peripheral edge portion (1a), and the substrate (1) The squeezing pressure introduced between the filter frame (b) and the other back-to-back substrate on the back side of the substrate causes the portion (1c) to bend and the central region (1b) to move forward, resulting in a split electrode plate ( 2A) also moves forward and squeezes the sludge introduced through the stock solution inlet (1d) between the filter cloths (b) and (b). The sewage that has passed through the filter cloth (b) passes through the through holes (2a) of the split electrode plate (2A), and the central area (1
The liquid passage (1e ′) in the valley between the protrusions (1e) of b), the liquid passage (1f ′) in the valley between the protrusions (1f) of the flexible membrane (1c), and the outer peripheral edge (1a) ), It is designed to flow out of the machine through the drainage port (1g).

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)を止めナット(7)により接続する。
In the present invention, since the group of four divided electrode plates (2A) is simultaneously reinforced against the squeezing force, in the corresponding central region (1b) of the diaphragm substrate (1), iron, titanium, aluminum or the like having relatively high conductivity is used. Use a good metal plate metal core (3) for the second
As shown in FIG. 5 to FIG. When the metal core (3) is thin and the reinforcing action against a large squeezing force is not sufficient, as shown in FIG. 2, a thick reinforcing plate (4) such as polypropylene is attached to the back surface of the substrate. Then, the feeding cable (6) from the DC power source is connected to the stud (5) protruding from the metal core (3) through the substrate (1) and the reinforcing plate (4) to the rear side by the lock 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、ステンレス鋼製の沈頭ビス(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), a power supply plate (8) made of copper or stainless steel for electrically connecting it to the divided electrode plate (2A) is distributed and arranged at a position corresponding to each divided electrode plate. Then, attach it with the sinking screw (9) made of stainless steel.
As shown in FIG. 1, the power feeding plate (8) is arranged at a position corresponding to the inner side of the four sides of each divided electrode plate (2A). This is the squeezing pressure applied to the divided electrode plate via the power feeding plate. This is to reduce the bending force caused by the bending and to evenly energize 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(1A)で全面的に被覆し、
給電板(8)のみ露出させる。この電面被膜(1A)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(2A)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 back surface of the base body (1) and the flexible film portion (1c) are continuously covered with an insulating and corrosion-resistant front surface coating (1A) made of rubber or the like,
Only the power feed plate (8) is exposed. The projections (1e) are distributed and formed on the electric surface coating (1A), and the divided electrode plate (2A) is brought into contact with the back surface of the divided electrode plate (2A) to feed the feeding plate (8).
Along with supporting from the back all over.

このダイヤフラム基板(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薄い絶縁性シート(10)
を敷し、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、損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。
As shown in FIGS. 3 and 4, the division electrode plate (2A) is attached to the diaphragm substrate (1) by a thin insulating sheet (10) such as polyvinyl chloride in the attachment recess (2b).
And lay it in and fit it into the power supply plate (8) with a plastic screw (11) penetrating therethrough. This attachment can be done with one touch, and the worn 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(1A)より僅かに突出する
ゴム質の環状部(1h)で囲んで置く。この突出量は、分
割電極板(2A)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。
In order to seal each power supply plate (8), as shown in FIGS. 3 and 5, the periphery of the power supply plate (8) is surrounded by a rubber annular portion (1h) slightly protruding from the front surface coating (1A). This protrusion amount is crushed by attachment of the split electrode plate (2A) and squeezing pressure so as to be flush with each other, so that the power supply plate (8) is sealed from the surroundings and electric contact between the power supply plate and the split electrode plate is ensured. 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 compression diaphragm with electrodes of an electroosmotic compression dehydrator, uniform compression pressure can be applied to sludge, and the electrode plate is divided into small areas against the compression pressure. Since each independent split electrode plate bears the split squeezing pressure evenly, strength is maintained and damage does not occur, the current paths to the split electrode plates are simple and short, uniform electrode current is conducted, and electroosmotic dehydration is performed. Corrosion-resistant environment caused by the above is protected against corrosion, and it is possible to obtain effects such as easy attachment and replacement of the divided electrode plates.

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

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)はフイルタープレス型電気浸透圧搾脱水機の基本
構成と1操作段階を示す縦断側面図、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、(1A)……前面被膜、
(1a)……外周縁部、(1b)……中央領域、(1c)……
可撓膜部、(1d)……原液口、(1e)(1f)……突起、
(1e′)(1f′)……通液路、(1g)……濾水口、(1
h)……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)……止めナット、
(8)……給電板、(9)……沈頭ビス、(10)……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、
(g)……脱水ケーキ。
FIG. 1 is a perspective view showing an electrode composite diaphragm of an electroosmotic dewatering machine according to an embodiment of the present invention in a state where a partially divided electrode plate is removed from the front side, and FIG. 2 is a cross-sectional view of an end showing a power supply connection thereof, FIG. 3 is a sectional view of an end portion showing the attachment of the divided electrode plate, FIG. 4 is a partially enlarged sectional view of the same, FIG. 5 is a sectional view of a power feeding plate portion of a diaphragm substrate before assembly, and FIG. ) Is a vertical side view showing the basic structure and one operation stage of a filter press type electroosmotic dehydrator, FIG. 6 (b) is a vertical side view of the different operation stage, and FIG. 6 (c) is further different. It is a vertical side view of an operation stage. (1) …… diaphragm substrate, (1A) …… front coating,
(1a) …… Outer peripheral part, (1b) …… Central region, (1c) ……
Flexible membrane, (1d) …… undiluted solution mouth, (1e) (1f) …… protrusion,
(1e ') (1f') ... liquid passage, (1g) ... drainage port, (1
h) ...... annular part, (2) ...... electrode plate, (2A) ...... split electrode plate, (2a) ...... through hole, (2b) ...... mounting recess, (3)
…… Metal core, (4) …… Reinforcement plate, (5) …… Implant bolt, (6) …… Power supply cable, (7) …… Lock nut,
(8) ...... power supply plate, (9) ...... sinking screw, (10) ...... sheet, (11) ...... stop screw, (a) ...... filter frame, (b) ...
... filter cloth, (c) ... diaphragm, (d) ... undiluted solution inlet, (e) ... filtered water outlet, (f) (f ') ... electrode,
(G) …… Dehydrated cake.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】フイ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。
1. An electrode composite diaphragm of a filter press type electroosmotic dewatering machine, which comprises a flexible diaphragm substrate and an electrode plate attached to the surface side thereof, and the electrode plates are formed by independent split electrode plates. The area other than the area where the diaphragm substrate is configured and the central area corresponding to the divided electrode plate group is embedded and reinforced by the metal core to expose each power supply plate electrically connecting each divided electrode and the metal core to the electrode side. An electrode composite diaphragm for an electroosmotic dewatering machine, characterized by being coated with an insulating and corrosion-resistant coating.
JP63263524A 1988-10-19 1988-10-19 Electrode compound diaphragm of electroosmotic dewatering machine Expired - Lifetime JPH0732850B2 (en)

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 JPH02111410A (en) 1990-04-24
JPH0732850B2 true 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)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH055924Y2 (en) * 1988-12-28 1993-02-16
JP6167497B2 (en) * 2012-10-05 2017-07-26 富士ゼロックス株式会社 Diaphragm for filter press and solid-liquid separator

Also Published As

Publication number Publication date
JPH02111410A (en) 1990-04-24

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