JPH0671300A - Concentrator - Google Patents

Concentrator

Info

Publication number
JPH0671300A
JPH0671300A JP4253939A JP25393992A JPH0671300A JP H0671300 A JPH0671300 A JP H0671300A JP 4253939 A JP4253939 A JP 4253939A JP 25393992 A JP25393992 A JP 25393992A JP H0671300 A JPH0671300 A JP H0671300A
Authority
JP
Japan
Prior art keywords
electrodes
electrode
voltage
liquid
concentrated
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.)
Pending
Application number
JP4253939A
Other languages
Japanese (ja)
Inventor
Toshihito Kondo
敏仁 近藤
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.)
Fujita Corp
Original Assignee
Fujita Corp
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 Fujita Corp filed Critical Fujita Corp
Priority to JP4253939A priority Critical patent/JPH0671300A/en
Publication of JPH0671300A publication Critical patent/JPH0671300A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To shorten the time required for concentration and to miniaturize a concentrator by arranging plural electrodes at specified intervals in parallel with the bottom surface in a concentrating tank to connect them to a power source and selectively applying voltage to an arbitrary electrode through a current switching device. CONSTITUTION:In a concentrating tank 1, plural electrodes 2 are arranged from an electrode 21 in the first stage parallel to the bottom surface in order at equal intervals upwards in parallel with each other in a multistage. The electrodes 2 each are independently connected to a current switching device 3 outside the tank. Arbitrary two electrodes 2 are selected and connected to a DC power source 1 to apply DC voltage to them. For example, first the electrodes 26, 28 are selected and used as an anode and a cathode respectively and DC voltage is applied to them to accelerate the sedimentation of suspended particles by an electrophoresis phenomenon. When the setting interface is lowered, the electrodes 27, 25 are selected to accelerate the sedimentation of suspended particles similarly. The operation is repeated in such a manner, and causing the concentration to be promoted.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は泥水または泥状物質の減
容のため水分を除く濃縮装置に関し、特に被濃縮液に直
流電圧を印加して電気泳動現象により濃縮効率を向上さ
せることを目指した。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a concentrating device for removing water to reduce the volume of muddy water or muddy substances, and particularly to improve the concentration efficiency by applying a DC voltage to the liquid to be concentrated by an electrophoretic phenomenon. It was

【0002】[0002]

【従来の技術】従来泥水などを濃縮して減容するとき
は、濾過槽において濾過槽底面の格子上に敷いた濾布を
介して被濃縮液を濾過するか、または濃縮槽において被
濃縮液中の懸濁粒子の沈降を待って上澄み液を除き、濃
縮液を得ていた。
2. Description of the Related Art Conventionally, when concentrating muddy water or the like to reduce its volume, the liquid to be concentrated is filtered through a filter cloth laid on a grid on the bottom of the filter in the filter or the liquid to be concentrated in the tank. The supernatant was removed by waiting for the suspended particles therein to settle to obtain a concentrated solution.

【0003】[0003]

【発明が解決しようとする課題】従来の濾過法による濃
縮では、濾過中の濾布の目詰まりによって発生する濾過
機能の低下を避けることができず、効率良い濃縮という
点では甚だ問題があった。また、濃縮槽中で被濃縮液中
の懸濁粒子の自然沈降を待つ重力沈降法では、懸濁粒子
が負に帯電しているため溶媒和が起こり易く、沈降速度
が極めて遅くなり、濃縮に長時間を要していた。そこで
本発明は、被濃縮液に直流電圧を印加して、電気泳動現
象により懸濁粒子の沈降速度を速め、濃縮効率を上げる
ことを目的とした。
In the concentration by the conventional filtration method, the deterioration of the filtration function caused by the clogging of the filter cloth during the filtration cannot be avoided, and there is a serious problem in terms of efficient concentration. . In the gravity settling method, which waits for the spontaneous settling of suspended particles in the liquid to be concentrated in the concentrating tank, the suspended particles are negatively charged, so that solvation easily occurs, and the sedimentation speed becomes extremely slow. It took a long time. Therefore, the present invention has an object to increase the concentration efficiency by applying a DC voltage to the liquid to be concentrated to accelerate the sedimentation speed of the suspended particles by an electrophoretic phenomenon.

【0004】[0004]

【課題を解決するための手段】本発明は上記目的を達成
するために、泥水または泥状物質から水分を除く濃縮装
置において、濃縮槽内の下方から上方にかけて、複数の
電極をそれぞれ所定の間隔で底面に平行に配置し、さら
にそれぞれの電極を、電流切り替え装置を介して電源に
接続し、複数の電極から任意に2枚の電極を選択してそ
の電極間に電圧を印加できるように構成した。
In order to achieve the above object, the present invention provides a concentrator for removing water from muddy water or mud-like substances, in which a plurality of electrodes are arranged at predetermined intervals from the lower part to the upper part in the concentration tank. Is arranged in parallel with the bottom surface, and each electrode is connected to a power source through a current switching device, so that two electrodes can be arbitrarily selected from a plurality of electrodes and a voltage can be applied between the electrodes. did.

【0005】[0005]

【作用】濃縮槽内の被濃縮液中の懸濁粒子は、通常負に
帯電しており、その沈降速度は極めて遅い。そこで、被
濃縮液中に電極を浸し、濃縮槽の上方に陰極を配置し、
下方に陽極を配置して、両電極間に直流電圧を印加する
と、電気泳動現象により負に帯電している懸濁粒子が濃
縮槽の下方の陽極に電気的に引きつけられ、懸濁粒子の
沈降が促進される。その結果、被濃縮液は沈降界面を境
にして上層の上澄み層と下層の懸濁粒子の沈降した濃縮
層とに分かれてくる。一方濃縮槽内には、複数の電極が
所定間隔を保持しながら多段平行に配置されており、濃
縮が進んで被濃縮液の容量が減少しても、複数の電極の
うち必ず幾つかの電極は被濃縮液中に浸るようになって
いる。従って、濃縮の進行につれて被濃縮液の容量が減
少し、併せて沈降界面が降下しても、その都度被濃縮液
中に浸っている電極の中から沈降界面を挟むように2つ
の電極を選択し、電流切り替え装置で沈降界面より上方
の電極を電源の陰極側に、沈降界面より下方の電極を電
源の陽極側に接続して、常時2つの電極間に直流電圧を
印加しながら懸濁粒子の沈降を促進することができる。
The suspended particles in the liquid to be concentrated in the concentration tank are usually negatively charged, and the sedimentation speed thereof is extremely slow. Therefore, the electrode is immersed in the liquid to be concentrated, and the cathode is placed above the concentration tank.
When the anode is placed below and a direct current voltage is applied between both electrodes, the suspended particles that are negatively charged by the electrophoretic phenomenon are electrically attracted to the anode below the concentrator, and the suspended particles settle. Is promoted. As a result, the liquid to be concentrated separates into a supernatant layer of the upper layer and a concentrated layer of the suspended particles of the lower layer at the boundary of the sedimentation interface. On the other hand, in the concentrating tank, a plurality of electrodes are arranged in parallel in multiple stages while maintaining a predetermined interval, and even if the capacity of the liquid to be concentrated decreases due to the progress of concentration, some electrodes among the plurality of electrodes must be used. Is soaked in the liquid to be concentrated. Therefore, the two electrodes are selected so that the sedimentation interface is sandwiched from the electrodes immersed in the liquid to be concentrated each time, even if the volume of the liquid to be concentrated decreases as the concentration proceeds and the sedimentation interface also drops. In the current switching device, the electrode above the sedimentation interface is connected to the cathode side of the power supply, and the electrode below the sedimentation interface is connected to the anode side of the power supply, and a DC voltage is constantly applied between the two electrodes to suspend suspended particles. Sedimentation can be promoted.

【0006】[0006]

【実施例】本実施例を、図1により説明する。本発明に
係る濃縮装置では、濃縮槽1内にある多段配置された複
数の電極2(21〜28)で、濃縮槽1内の被濃縮液中
の懸濁粒子の沈降を促進し、その上澄み液を排出して、
被濃縮液の減容及び濃縮ができるようになっている。濃
縮槽1内には、濃縮槽1の底より少し上に底面に平行に
配置された一段目の電極21から、順次等間隔に上方に
向かって複数の電極が、互いに平行になるように多段配
置されている。最上段の電極28の取り付け位置は、濃
縮槽1に規定容量の被濃縮液を満たしたときの水位の高
さより少し低い位置に設定されている。なお、本実施例
では8枚の電極を平行に多段配置したが、勿論濃縮槽の
容量などにより適宜電極の枚数を変えても構わない。ま
た、複数の電極21〜28は、それぞれ濃縮槽1の底面
とほぼ同様の大きさを有しており、さらに、電極面に液
体がスムーズに透過できるように透過用の目を多数設
け、断面が波形の金属製の格子につくられている。
EXAMPLE This example will be described with reference to FIG. In the concentrating device according to the present invention, the plurality of electrodes 2 (21 to 28) arranged in multiple stages in the concentrating tank 1 promote the sedimentation of suspended particles in the liquid to be concentrated in the concentrating tank 1 and the supernatant thereof. Drain the liquid,
The liquid to be concentrated can be reduced in volume and concentrated. In the concentrating tank 1, a plurality of electrodes are arranged in parallel from the first-stage electrode 21 which is arranged slightly above the bottom of the concentrating tank 1 in parallel with the bottom surface and which are arranged at equal intervals in the upward direction. It is arranged. The attachment position of the uppermost electrode 28 is set to a position slightly lower than the height of the water level when the concentration tank 1 is filled with the liquid to be concentrated. In this embodiment, eight electrodes are arranged in parallel in multiple stages, but of course the number of electrodes may be changed depending on the capacity of the concentrating tank. Further, each of the plurality of electrodes 21 to 28 has substantially the same size as the bottom surface of the concentrating tank 1, and further, a large number of permeation eyes are provided on the electrode surface so that liquid can smoothly permeate, Are made on a corrugated metal grid.

【0007】また、それぞれの電極2は、槽外に設けら
れた電流切り替え装置3に互いに独立に接続され、適宜
電流切り替え装置3で、濃縮槽1内の複数の多段配置さ
れた電極21〜28から任意の2枚の電極を選択して、
2枚の電極のうち下側にある電極を陽極に、上側にある
電極を陰極として、随時槽外にある直流電源4に接続し
て、2つの電極間に直流電圧が印加できるようになって
いる。上記直流電圧を2つの電極間に印加することによ
り、2つの電極間の負に帯電している懸濁粒子を電気泳
動現象により濃縮槽の下方の陽極側に沈降させ、懸濁粒
子が減少した被濃縮液の上層の上澄み液を、濃縮槽上方
側壁の開閉弁5aを有した排出管5により、適宜排出で
きるようになっている。さらに、濃縮槽下方側壁には、
開閉弁6aを有した排出管6が設けられており、上澄み
液を排出した後の濃縮液を排出できるようになってい
る。
Each of the electrodes 2 is independently connected to a current switching device 3 provided outside the tank, and the plurality of electrodes 21 to 28 arranged in multiple stages in the concentration tank 1 are appropriately connected by the current switching device 3. Select any two electrodes from
Of the two electrodes, the lower electrode is used as an anode and the upper electrode is used as a cathode, which is connected to a DC power source 4 outside the tank, so that a DC voltage can be applied between the two electrodes. There is. By applying the above DC voltage between the two electrodes, the negatively charged suspended particles between the two electrodes were settled to the anode side below the concentrating tank by the electrophoretic phenomenon, and the suspended particles were reduced. The supernatant liquid of the upper layer of the liquid to be concentrated can be appropriately discharged through a discharge pipe 5 having an opening / closing valve 5a on the upper side wall of the concentration tank. Furthermore, on the lower side wall of the concentration tank,
A discharge pipe 6 having an on-off valve 6a is provided so that the concentrated liquid after discharging the supernatant liquid can be discharged.

【0008】つまり、適宜上澄み液を排出して濃縮が進
行していくと、それに伴って次第に被濃縮液の液面が下
がるが、その都度被濃縮液中に浸っている電極から、被
濃縮液の上澄み層と濃縮層の界面である沈降界面を挟む
ように2枚の電極を選択し、電流切り替え装置によって
随時沈降界面より上方の電極を陰極に、下方の電極を陽
極にして直流電圧を印加させながら、懸濁粒子の沈降を
促進させることができるようになっている。例えば、最
初は電極26と28を選択し、電極26を陽極に、電極
28を陰極として直流電圧を印加して懸濁粒子の沈降を
促進し、沈降界面が下がった時点で、電極27と25を
選択し、電極25を陽極に、電極27を陰極にしてさら
に直流電圧を印加し、懸濁粒子の沈降を促進するという
具合に、この操作を繰り返しながら直流電圧を印加して
濃縮を進めるのである。
That is, as the supernatant liquid is appropriately discharged and the concentration proceeds, the liquid surface of the liquid to be concentrated gradually lowers accordingly, but the liquid to be concentrated is discharged from the electrode immersed in the liquid to be concentrated each time. Select two electrodes so as to sandwich the sedimentation interface, which is the interface between the supernatant layer and the concentrated layer, and apply a DC voltage by the current switching device with the electrode above the sedimentation interface as the cathode and the electrode below as the anode. Meanwhile, it is possible to accelerate the sedimentation of suspended particles. For example, first, the electrodes 26 and 28 are selected, and a direct current voltage is applied with the electrode 26 as an anode and the electrode 28 as a cathode to promote the sedimentation of suspended particles, and when the sedimentation interface is lowered, the electrodes 27 and 25 are formed. Then, DC voltage is further applied by using the electrode 25 as an anode and the electrode 27 as a cathode to promote the sedimentation of suspended particles. By repeating this operation, the DC voltage is applied to promote concentration. is there.

【0009】また、被濃縮液の沈降界面を自動的に感知
するセンサーを濃縮槽1に設け、センサーの検出信号に
より電流切り替え装置3を制御して、自動的に被濃縮液
中の沈降界面を挟む2枚の電極を選択し、直流電圧を印
加できるようにしてもよい。また、電極は、濃縮槽1の
底面とほぼ同じ大きさの一体の平面状の電極でなくても
よく、複数の電極を共用して電圧の印加面全体をカバー
するようにしてもよい。また、本実施例では下方にある
電極を陽極に、上方にある電極を陰極にしたが、懸濁粒
子が正に帯電している場合は、勿論下方にある電極を陰
極に、上方にある電極を陽極にして、直流電圧を印加し
てもよい。
Further, a sensor for automatically sensing the sedimentation interface of the concentrated liquid is provided in the concentration tank 1, and the current switching device 3 is controlled by the detection signal of the sensor to automatically detect the sedimentation interface in the concentrated liquid. Two electrodes to be sandwiched may be selected so that a DC voltage can be applied. Further, the electrode does not have to be an integrated planar electrode having substantially the same size as the bottom surface of the concentrating tank 1, and a plurality of electrodes may be shared to cover the entire voltage application surface. In the present embodiment, the lower electrode was used as the anode and the upper electrode was used as the cathode. However, when the suspended particles are positively charged, the lower electrode is of course the cathode and the upper electrode is of course. May be used as an anode and a DC voltage may be applied.

【0010】[0010]

【発明の効果】本発明により、濃縮過程の進行に応じて
減容する被濃縮液中の2つの電極間に継続して直流電圧
を印加し続けることができ、懸濁粒子の沈降を促進し、
濃縮効率を大幅に向上することができる。これによっ
て、濃縮槽の処理能力が向上し、従来長時間を要してい
た濃縮時間の短縮及び濃縮装置の小型化が図れる。
According to the present invention, a DC voltage can be continuously applied between two electrodes in a liquid to be concentrated whose volume is reduced in accordance with the progress of the concentration process, which promotes sedimentation of suspended particles. ,
The concentration efficiency can be greatly improved. As a result, the processing capacity of the concentrating tank is improved, and it is possible to shorten the concentrating time and the downsizing of the concentrating device, which conventionally required a long time.

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

【図1】濃縮装置正面の断面説明図である。FIG. 1 is a cross-sectional explanatory view of the front of a concentrating device.

【符号の説明】[Explanation of symbols]

1 濃縮槽 2 電極 3 電流切り替え装置 4 直流電源 1 Concentrator 2 Electrode 3 Current switching device 4 DC power supply

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 泥水または泥状物質から水分を除く濃縮
装置において、濃縮槽内の下方から上方にかけて、複数
の電極をそれぞれ所定の間隔で底面に平行に配置し、さ
らにそれぞれの電極を電流切り替え装置を介して電源に
接続し、複数の電極のうちから任意に2枚の電極を選択
してその電極間に電圧を印加できるように構成したこと
を特徴とする濃縮装置。
1. A concentrator for removing water from muddy water or mud-like substances, wherein a plurality of electrodes are arranged parallel to the bottom surface at a predetermined interval from the lower part to the upper part in the concentrating tank, and further each electrode is switched to a current. A concentrating device characterized in that it is connected to a power source through the device, two electrodes are arbitrarily selected from a plurality of electrodes, and a voltage can be applied between the electrodes.
JP4253939A 1992-08-28 1992-08-28 Concentrator Pending JPH0671300A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4253939A JPH0671300A (en) 1992-08-28 1992-08-28 Concentrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4253939A JPH0671300A (en) 1992-08-28 1992-08-28 Concentrator

Publications (1)

Publication Number Publication Date
JPH0671300A true JPH0671300A (en) 1994-03-15

Family

ID=17258107

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4253939A Pending JPH0671300A (en) 1992-08-28 1992-08-28 Concentrator

Country Status (1)

Country Link
JP (1) JPH0671300A (en)

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