JPH0747095B2 - Electro-osmotic dehydrator - Google Patents

Electro-osmotic dehydrator

Info

Publication number
JPH0747095B2
JPH0747095B2 JP1029231A JP2923189A JPH0747095B2 JP H0747095 B2 JPH0747095 B2 JP H0747095B2 JP 1029231 A JP1029231 A JP 1029231A JP 2923189 A JP2923189 A JP 2923189A JP H0747095 B2 JPH0747095 B2 JP H0747095B2
Authority
JP
Japan
Prior art keywords
belt
sludge treatment
treatment container
cathode conductive
sludge
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP1029231A
Other languages
Japanese (ja)
Other versions
JPH02207811A (en
Inventor
幹昌 山口
克雄 伊波
博史 松下
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP1029231A priority Critical patent/JPH0747095B2/en
Publication of JPH02207811A publication Critical patent/JPH02207811A/en
Publication of JPH0747095B2 publication Critical patent/JPH0747095B2/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)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、下水処理場で発生した余剰汚泥などの泥漿を
脱水処理する電気浸透式脱水機に関する。
TECHNICAL FIELD The present invention relates to an electroosmotic dehydrator for dehydrating sludge such as excess sludge generated in a sewage treatment plant.

〔従来の技術〕[Conventional technology]

頭記した電気浸透式脱水機として、第3図に示すような
バッチ処理方式のフィルタプレス型脱水機が知られてい
る。図において、1は枡形の濾板2とその開放端面側に
配した圧搾濾板3との組合せから成る汚泥処理容器であ
り、その頂部には汚泥供給口1aが、下部には濾水排出口
1bが開口している。また濾板2の内部側面には陽極板4
が、陽極板4に対向して圧搾濾板3側には圧搾用ダイヤ
フラム5が装備されていおり、ダイヤフラム5の背後に
は加圧エアの導入口1cが開口している。
As the electroosmotic dehydrator described above, a batch press type filter press dehydrator as shown in FIG. 3 is known. In the figure, reference numeral 1 denotes a sludge treatment container comprising a combination of a square-shaped filter plate 2 and a press filter plate 3 arranged on the open end face side thereof, a sludge supply port 1a is provided at the top thereof, and a drainage discharge port is provided at the lower part thereof.
1b is open. Further, the anode plate 4 is provided on the inner side surface of the filter plate 2.
However, a squeezing diaphragm 5 is provided on the side of the squeezing filter plate 3 facing the anode plate 4, and a compressed air introduction port 1c is opened behind the diaphragm 5.

さらに、前記の汚泥処理容器1に対し、前記陽極板4と
の対向側には容器の内外にまたがる移動式の陰極導電ベ
ルト6,および濾布ベルト7が重ね合わせてダイヤフラム
5の内面上に敷設されている。これらのベルト6,7はエ
ンドレスベルトであって汚泥処理容器1の外方でプーリ
8,9,10の間に張架されており、かつ濾板2と圧搾濾板3
との間を通して汚泥処理容器1の内外を貫通している。
ここで、陰極導電ベルト6は例えば可撓性のある薄手の
金属製ベルト,あるいは導電性のあるカーボン繊維の織
物で作られ、一方の濾布ベルト7はナイロン,テトロン
などの織物で作られている。
Further, with respect to the sludge treatment container 1, on the side facing the anode plate 4, a movable cathode conductive belt 6 extending over the inside and outside of the container, and a filter cloth belt 7 are laid on the inner surface of the diaphragm 5 in an overlapping manner. Has been done. These belts 6 and 7 are endless belts, and pulleys are provided outside the sludge treatment container 1.
It is stretched between 8, 9 and 10, and has a filter plate 2 and a press filter plate 3.
Through the inside and outside of the sludge treatment container 1.
Here, the cathode conductive belt 6 is made of, for example, a flexible thin metal belt or a conductive carbon fiber fabric, while the filter cloth belt 7 is made of a fabric such as nylon or tetron. There is.

また、11はプーリ8に結合したベルト駆動モータ、12は
汚泥処理容器1を開閉する加圧装置、13は陽極板4と陰
極導電ベルト6との間に電圧を印加する直流電源、14は
集電刷子である。なお、図示されてないがベルト6,7の
移動経路途上にはベルトから付着物を排除する洗浄ノズ
ル,スクレーパなどが配備されている。
Further, 11 is a belt drive motor coupled to the pulley 8, 12 is a pressurizing device for opening and closing the sludge treatment container 1, 13 is a DC power source for applying a voltage between the anode plate 4 and the cathode conductive belt 6, and 14 is a collector. It is an electric brush. Although not shown, cleaning nozzles, scrapers and the like for removing adhered matters from the belts are provided along the moving paths of the belts 6 and 7.

次に上記構成の電気浸透式脱水機の動作を述べる。ま
ず、加圧装置12の操作で汚泥処理容器1を閉じ、同時に
液漏れのないように陰極導電ベルト6,濾布ベルト7を濾
板2と圧搾濾板3との周縁部の間で加圧挟持する。この
状態で汚泥供給口1aより処理容器1内に被脱水処理物で
ある汚泥15を導入し、かつ陽極板4と陰極導電ベルト6
との間に電源13より直流電圧を印加すると、汚泥15を挟
んで対向する陽極板4と陰極導電ベルト6との間に形成
された電場の作用により汚泥に電気浸透作用が働き、汚
泥15に含まれている水分は濾布ベルト7を透過して陰極
導電ベルト6の表面に集まり、さらに陰極導電ベルト6
の表面に形成した導水溝に沿って流下し、濾水排出口1b
より室外に排出される。また、電気浸透脱水の進行に合
わせて加圧エア導入口1cを通じてダイヤフラム5の背後
に加圧エアを吹き込むことによりダイヤフラム5が膨張
し、陰極導電ベルト6,濾布ベルト7が陽極板4の方へ向
けて押圧されて汚泥15に圧搾力が加わる。これにより電
気浸透脱水がさらに効果的に進み、汚泥が低含水率まで
脱水される。
Next, the operation of the electroosmotic dehydrator having the above structure will be described. First, the sludge treatment container 1 is closed by operating the pressurizing device 12, and at the same time, the cathode conductive belt 6 and the filter cloth belt 7 are pressed between the peripheral portions of the filter plate 2 and the press filter plate 3 so as to prevent liquid leakage. Hold it. In this state, sludge 15, which is a substance to be dehydrated, is introduced into the processing container 1 through the sludge supply port 1a, and the anode plate 4 and the cathode conductive belt 6 are
When a DC voltage is applied from the power source 13 to the sludge 15, an electroosmotic action is exerted on the sludge due to the action of the electric field formed between the anode plate 4 and the cathode conductive belt 6 that face each other with the sludge 15 in between, and The contained water permeates the filter cloth belt 7 and collects on the surface of the cathode conductive belt 6.
It flows down along the water guide groove formed on the surface of the drainage outlet 1b.
Is discharged outdoors. In addition, the diaphragm 5 expands by blowing pressurized air behind the diaphragm 5 through the pressurized air inlet 1c as the electroosmotic dehydration progresses, and the cathode conductive belt 6 and the filter cloth belt 7 are directed toward the anode plate 4. The sludge 15 is pressed toward and the pressing force is applied to the sludge 15. As a result, electroosmotic dehydration proceeds more effectively, and the sludge is dehydrated to a low water content.

なお、1回の脱水処理が済むと、処理容器1を開放して
ケーキ化した汚泥を排除するとともに、駆動モータ11の
操作により陰極導電ベルト6,濾布ベルト7を巡回移動
し、前回の処理工程で生じたベルト上の残留付着物を洗
浄,排除するするとともに、次回の脱水処理工程に備え
てベルトの清浄面域を処理容器内に引き込むようにす
る。
When the dehydration process is completed once, the processing container 1 is opened to remove the caked sludge, and the cathode conductive belt 6 and the filter cloth belt 7 are circularly moved by the operation of the drive motor 11 to remove the previous treatment. Residual deposits on the belt generated in the process are cleaned and removed, and the clean surface area of the belt is drawn into the processing container in preparation for the next dehydration process.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

ところで、前記した電気浸透式脱水機では、長期の稼働
実績から、脱水処理工程の繰り返しにより陰極導電ベル
ト6が比較的短期間で破断すると言った事故の多発が認
められている。
By the way, in the electroosmotic dehydrator described above, from the long-term operation record, it has been recognized that the cathode conductive belt 6 is frequently broken in a relatively short period of time due to repeated dehydration treatment steps.

この点について発明者等が原因を究明したところ、その
原因は以下に述べる理由であることが判明した。すなわ
ち、陰極導電ベルト6,濾布ベルト7を汚泥処理容器1の
濾板2と圧搾濾板3との間に挟持固定した状態で背後か
らダイヤフラム5を加圧操作すると、ダイヤフラム5に
押されてベルト6,7は容器内部の自由面域のみが強制的
に変形するようになる。この場合に、ナイロンなどの繊
維織物で作られた濾板ベルト7は弾力があって伸張力に
対する耐久性が大であり、数%程度伸張しても加圧力が
なくなれば元の状態に復元する。これに対して、金属あ
るいはカーボン繊維などの弾性の低い塑性材料で作られ
た陰極導電ベルト6は、伸張力の繰り返し荷重で材料が
疲労し、ついには疲労破壊を起こしてベルトが破断する
に至る。
When the inventors investigated the cause of this point, it was found that the reason was as follows. That is, when the cathode conductive belt 6 and the filter cloth belt 7 are sandwiched and fixed between the filter plate 2 and the press filter plate 3 of the sludge treatment container 1, when the diaphragm 5 is pressed from behind, the diaphragm 5 is pushed by the diaphragm 5. The belts 6 and 7 are forced to deform only in the free surface area inside the container. In this case, the filter plate belt 7 made of a fiber woven fabric such as nylon has elasticity and has a high durability against an extension force, and even if it is extended by about several percent, it returns to its original state when the pressing force disappears. . On the other hand, in the cathode conductive belt 6 made of a plastic material having low elasticity such as metal or carbon fiber, the material is fatigued by the repeated load of the stretching force, and finally the fatigue fracture occurs and the belt is broken. .

本発明は上記の点にかんがみなされたものであり、脱水
処理工程でのダイヤフラム加圧操作の繰り返しによって
も陰極導電ベルトが破断するなどのトラブル発生を防止
し、その耐久性向上が図れるようにした電気浸透式脱水
機の構造を提供することを目的とする。
The present invention has been made in view of the above points, and prevents the occurrence of troubles such as breakage of the cathode conductive belt even by repeating the diaphragm pressurizing operation in the dehydration treatment step, and makes it possible to improve its durability. An object is to provide a structure of an electroosmotic dehydrator.

〔課題を解決するための手段〕[Means for Solving the Problems]

上記課題を解決するために、本発明の電気浸透式脱水機
においては、陰極導電ベルトを、汚泥処理容器の上側な
らびに下側を貫通する引き出し部分を通して摺動可能に
汚泥処理容器外部に引き回すと共に、汚泥処理容器外部
の濾布ベルトと切り離された区間で、固定プーリおよび
この陰極導電ベルトに一定の張力を与える移動可能なプ
ーリを介して張架するものとする。
In order to solve the above problems, in the electroosmotic dehydrator of the present invention, the cathode conductive belt is slidably drawn to the outside of the sludge treatment container through a drawer portion that penetrates the upper side and the lower side of the sludge treatment container, In the section separated from the filter cloth belt outside the sludge treatment container, it is stretched via a fixed pulley and a movable pulley that gives a constant tension to the cathode conductive belt.

〔作用〕[Action]

上記の構成で、陰極導電ベルトは汚泥処理容器に対し、
その容器内を貫通する引出し部分で摺動可能に引回して
あり、かつダイヤフラムの加圧操作による汚泥処理容器
内での自由な変位を許容するように、ベルト途中にテン
ションプーリを配備して一定張力を加えるように張架さ
れている。
With the above configuration, the cathode conductive belt is for the sludge treatment container,
It is slidably drawn around the drawer part that penetrates the container, and a tension pulley is installed in the middle of the belt so that it can be freely displaced in the sludge treatment container by the pressure operation of the diaphragm. It is stretched to apply tension.

これにより、脱水処理工程でダイヤフラムの加圧操作で
陰極導電ベルトが背面から押圧力を受けると、ベルトは
無理に伸張変形されることなく、ダイヤフラムの膨張に
従動してベルト自身が処理容器内に引き込まれるように
なる。したがって陰極導電ベルトに過大な内部応力の加
わるおそれがなく、脱水処理工程の繰り返しによっても
ベルトが破断すると言ったトラブルが回避できる。
As a result, when the cathode conductive belt receives a pressing force from the back surface due to the pressing operation of the diaphragm in the dehydration process, the belt is not stretched and deformed forcibly, and the belt itself is moved into the processing container by the expansion of the diaphragm. You will be drawn in. Therefore, there is no fear that an excessive internal stress will be applied to the cathode conductive belt, and it is possible to avoid the trouble that the belt breaks even if the dehydration treatment process is repeated.

〔実施例〕〔Example〕

第1図,第2図は本発明実施例の構成を示すものであ
り、第3図に対応する同一部材には同じ符号が付してあ
る。
1 and 2 show the structure of an embodiment of the present invention, and the same members corresponding to FIG. 3 are designated by the same reference numerals.

すなわち、電気浸透式脱水機としての基本的な構成は第
3図で述べた従来のものと同様であるが、陰極導電ベル
ト6に関してベルトが汚泥処理容器1に対し非拘束的に
引回して張架されている点が異なる。このために、陰極
導電ベルト6は汚泥処理容器1の外部域で濾布ベルト7
と切り離してガイドプーリ16,17,18,およびテンション
プーリ19の間に張架され、かつ汚泥処理容器1に対して
は、圧搾濾板3の上下端面に開口したベルト穴3a,3bを
通して摺動自在に貫通するよう敷設されている。また、
この張架状態で陰極導電ベルト6に一定の張力を与える
ように、前記したテンションプーリ19に例えばエアシリ
ンダ20が結合されている。なお、濾布ベルト7について
は第3図と同様に汚泥処理容器1を貫通する部分が濾板
2と圧搾濾板3の周縁部間に挟持されている。
That is, the basic structure of the electroosmotic dehydrator is the same as that of the conventional one described in FIG. 3, but the cathode conductive belt 6 is stretched around the sludge treatment container 1 without binding. The difference is that it is mounted. For this reason, the cathode conductive belt 6 is provided outside the sludge treatment container 1 in the area outside the filter cloth belt 7.
Separated from the above, it is stretched between the guide pulleys 16, 17, 18 and the tension pulley 19, and slides on the sludge treatment container 1 through belt holes 3a, 3b opened at the upper and lower ends of the squeeze filter plate 3. It is laid so that it can penetrate freely. Also,
An air cylinder 20, for example, is connected to the tension pulley 19 so as to apply a constant tension to the cathode conductive belt 6 in this stretched state. Regarding the filter cloth belt 7, as in FIG. 3, the portion penetrating the sludge treatment container 1 is sandwiched between the peripheral edges of the filter plate 2 and the press filter plate 3.

かかる構成で、汚泥15の脱水処理工程でダイヤフラム6
を加圧操作して容器内部の汚泥15に圧搾力を与えると、
汚泥処理容器1の内部では濾布ベルト7の自由面域が強
制的に伸張変形するのに対し、陰極導電ベルト6は無理
に伸張変形することなく、ダイヤフラム5の膨張変形に
従動してベルト6がベルト穴3a,3bを通して容器内に引
き込まれ、その変位分はベルトの途中に配したテンショ
ンプーリ19の移動で吸収される。
With this configuration, the diaphragm 6 is used in the dehydration process of the sludge 15.
When pressurizing and applying compressive force to the sludge 15 inside the container,
In the sludge treatment container 1, the free surface area of the filter cloth belt 7 is forcibly stretched and deformed, whereas the cathode conductive belt 6 is not stretched and deformed by force, and the belt 6 is driven by the expansion and deformation of the diaphragm 5. Is drawn into the container through the belt holes 3a and 3b, and the displacement is absorbed by the movement of the tension pulley 19 arranged in the middle of the belt.

したがって、陰極導電ベルト6が金属,カーボン繊維な
ど、弾性の低い材料で作られたものであっても、ベルト
自身に過大な引張応力の加わることがなく、これにより
塑性変形,疲労破壊に起因して破断するのが防止でき
る。
Therefore, even if the cathode conductive belt 6 is made of a material with low elasticity such as metal or carbon fiber, excessive tensile stress is not applied to the belt itself, which causes plastic deformation and fatigue fracture. Can be prevented from breaking.

〔発明の効果〕〔The invention's effect〕

本発明による電気浸透式脱水機は、以上説明したように
構成されているので、次記の効果を奏する。
Since the electroosmotic dehydrator according to the present invention is configured as described above, it has the following effects.

(1)汚泥の脱水処理工程でダイヤフラムを加圧操作し
た際には、陰極導電ベルト自身がダイヤフラムの膨張変
形に従動して変位移動するだけであり、陰極導電ベルト
に過大な引張り応力の加わることがない。
(1) When pressure is applied to the diaphragm in the sludge dewatering process, the cathode conductive belt itself moves only in accordance with the expansion deformation of the diaphragm, and excessive tensile stress is applied to the cathode conductive belt. There is no.

(2)したがって、脱水処理工程を繰り返し行っても、
陰極導電ベルトが破断すると言ったトラブルの発生を防
止して耐久性,信頼性の大幅な向上が図れる。
(2) Therefore, even if the dehydration treatment step is repeated,
It is possible to prevent troubles such as breakage of the cathode conductive belt and greatly improve durability and reliability.

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

第1図は本発明実施例の構成断面図、第2図は第1図に
おける矢視II−II断面図、第3図は従来におけるフィル
タプレス型電気浸透式脱水機の構成断面図である。図に
おいて、 1:汚泥処理容器、1a:汚泥供給口、1b:濾水排出口、3a,3
b:ベルト穴、4:陽極板、5:圧搾用ダイヤフラム、6:陰極
導電ベルト、7:濾布ベルト、13:直流電源、19:テンショ
ンプーリ。
FIG. 1 is a sectional view showing the construction of an embodiment of the present invention, FIG. 2 is a sectional view taken along the line II--II in FIG. 1, and FIG. 3 is a sectional view showing the construction of a conventional filter press type electroosmotic dehydrator. In the figure, 1: Sludge treatment container, 1a: Sludge supply port, 1b: Drainage discharge port, 3a, 3
b: Belt hole, 4: Anode plate, 5: Diaphragm for compression, 6: Cathode conductive belt, 7: Filter cloth belt, 13: DC power supply, 19: Tension pulley.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】容器内部の両側に陽極板と圧搾用ダイヤフ
ラムを対向装備した汚泥処理容器に対し、前記ダイヤフ
ラムの面上に汚泥処理容器の内外にまたがる移動式の陰
極導電ベルト,および濾布ベルトを重ね合わせて敷設し
た電気浸透式脱水機において、前記陰極導電ベルトを、
前記汚泥処理容器の上側ならびに下側を貫通する引き出
し部分を通して摺動可能に前記汚泥処理容器外部に引き
回すと共に、前記汚泥処理容器外部の前記濾布ベルトと
切り離された区間で、固定プーリおよびこの陰極導電ベ
ルトに一定の張力を与える移動可能なプーリを介して張
架したことを特徴とする電気浸透式脱水機。
1. A sludge treatment container having an anode plate and a squeezing diaphragm facing each other on both sides inside the container, and a movable cathode conductive belt extending over the inside and outside of the sludge treatment container on the surface of the diaphragm, and a filter cloth belt. In the electroosmotic dehydrator laid by overlapping, the cathode conductive belt,
The sludge treatment container is slidably routed to the outside of the sludge treatment container through a pull-out portion that penetrates the upper side and the lower side of the sludge treatment container, and a fixed pulley and this cathode are provided in a section separated from the filter cloth belt outside the sludge treatment container. An electro-osmotic dehydrator, which is stretched via a movable pulley that gives a constant tension to a conductive belt.
JP1029231A 1989-02-08 1989-02-08 Electro-osmotic dehydrator Expired - Lifetime JPH0747095B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1029231A JPH0747095B2 (en) 1989-02-08 1989-02-08 Electro-osmotic dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1029231A JPH0747095B2 (en) 1989-02-08 1989-02-08 Electro-osmotic dehydrator

Publications (2)

Publication Number Publication Date
JPH02207811A JPH02207811A (en) 1990-08-17
JPH0747095B2 true JPH0747095B2 (en) 1995-05-24

Family

ID=12270452

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1029231A Expired - Lifetime JPH0747095B2 (en) 1989-02-08 1989-02-08 Electro-osmotic dehydrator

Country Status (1)

Country Link
JP (1) JPH0747095B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102012020636A1 (en) * 2012-10-20 2014-04-24 Forschungszentrum Jülich GmbH Fachbereich Patente Band-shaped chopper for a particle beam
CN115286196B (en) * 2022-08-23 2024-03-26 嘉戎技术(北京)有限公司 Sludge treatment system and treatment method

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