JPH0975775A - Magnetic field moving type magnetic separator - Google Patents

Magnetic field moving type magnetic separator

Info

Publication number
JPH0975775A
JPH0975775A JP7239583A JP23958395A JPH0975775A JP H0975775 A JPH0975775 A JP H0975775A JP 7239583 A JP7239583 A JP 7239583A JP 23958395 A JP23958395 A JP 23958395A JP H0975775 A JPH0975775 A JP H0975775A
Authority
JP
Japan
Prior art keywords
magnetic field
magnetic
substance
water
magnetic separation
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
JP7239583A
Other languages
Japanese (ja)
Inventor
Norihide Saho
典英 佐保
Hisashi Isokami
尚志 磯上
Minoru Morita
穣 森田
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP7239583A priority Critical patent/JPH0975775A/en
Publication of JPH0975775A publication Critical patent/JPH0975775A/en
Pending legal-status Critical Current

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  • Water Treatment By Electricity Or Magnetism (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

PROBLEM TO BE SOLVED: To magnetically separate and easily remove magnetic matter from water to be treated without a rotary mechanism part by setting a magnetic field control means for individually and in point of time changing the intensity of a magnetic field generated by plural magnetic field generating means statically arranged on the anti-adsorptive surface side of static surface adsorbing a material to be removed on a magnetic separating part. SOLUTION: Magnetic flocs in water to be treated 12 are adsorbed and accumulated on the surface of magnetic separation plates 21 by the generated magnetic field of excited electromagnets. A group of magnetic flocs accumulated in the generated magnetic field of electromagnets 20d in the lowest part is at least partially moved to the magnetic field of electromagnets 20c of a larger generated magnetic field by demagnetizing the electromagnets 20d and is absorbed in a group of magnetic flocs accumulated in the magnetic field of the electromagnets 20c. After that, when the electromagnets 20c are demagnetized, at least a part of the group of the magnetic flocs is moved to the magnetic field side of electromagnets 20b of a large generated magnetic field and is absorbed in a group of magnetic flocs accumulated in the magnetic field of the electromagnets 20b.

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、水浄化用の磁気分離装
置に係り、特に磁気分離物を処理水から連続的に除去す
る磁気分離装置及びこの磁気分離装置を用いた水浄化装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a magnetic separation device for water purification, and more particularly to a magnetic separation device for continuously removing magnetic separation products from treated water and a water purification device using this magnetic separation device.

【0002】[0002]

【従来の技術】従来この種の磁気分離装置の例として、
化学工学、第45巻、第4号(1981年)第226頁
から231頁に、磁界発生手段の例えば永久磁石を回転
円盤に固定し、磁性物を永久磁石表面に吸着して被処理
水から分離、除去する構造が記載されている。
2. Description of the Related Art Conventionally, as an example of this type of magnetic separation device,
Chemical Engineering, Vol. 45, No. 4 (1981) pp. 226-231, magnetic field generating means, for example, a permanent magnet is fixed to a rotating disk, and a magnetic substance is adsorbed on the surface of the permanent magnet to be treated water. The structure for separating and removing is described.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、従来の
技術では吸着した磁性物を除去するために、永久磁石を
配置した回転円盤の半分以上が、被処理水の通水流路の
気液自由界面上に露出する必要があり、また、円盤に配
置した永久磁石群に均一に被処理水が接触するような流
路構成が必要である。このため、回転円盤の外周形状に
沿った流路形成を行う必要があり、流路が複雑となり、
かつ回転円盤の永久磁石群、特に回転円盤の内周部側と
外周部側に配置した永久磁石に均一に磁性物を吸着する
ことが困難で、磁気分離性能が低下する問題があった。
また、磁性物を含んだ被処理水内に回転円盤の回転軸が
さらされることになり、回転機構部の信頼性が低下する
問題もあった。また、磁界発生手段が静止し、磁性物吸
着面体が相対的に移動する場合においても、磁性物を保
持した吸着面体が水中を回転する機構が必要となり、回
転機構部の信頼性が低下する問題もあった。また、被処
理水の磁気分離部に回転円盤の下半分しか利用できない
ため、流路断面が狭くなり、所望の処理流量を得るため
には、2倍の流路断面が必要となり、装置が大型化する
問題があった。
However, in the prior art, in order to remove the adsorbed magnetic substance, more than half of the rotating disk on which the permanent magnet is arranged is on the gas-liquid free interface of the water flow passage of the water to be treated. It is necessary to be exposed to the inside of the disk, and the flow path structure is required so that the water to be treated comes into uniform contact with the permanent magnet group arranged on the disk. Therefore, it is necessary to form a flow path along the outer peripheral shape of the rotating disk, which complicates the flow path.
Moreover, it is difficult to uniformly attract the magnetic substance to the permanent magnet group of the rotating disk, especially to the permanent magnets arranged on the inner peripheral side and the outer peripheral side of the rotating disk, and there is a problem that the magnetic separation performance is deteriorated.
In addition, there is a problem that the rotary shaft of the rotary disk is exposed to the water to be treated containing the magnetic substance, which lowers the reliability of the rotary mechanism. Further, even when the magnetic field generating means is stationary and the magnetic substance attracting face body moves relatively, a mechanism for rotating the attracting face body holding the magnetic substance in water is required, and the reliability of the rotating mechanism part is deteriorated. There was also. Further, since only the lower half of the rotating disk can be used for the magnetic separation part of the water to be treated, the flow passage cross section becomes narrow, and a double flow passage cross section is required to obtain a desired treatment flow rate, and the apparatus is large. There was a problem to turn.

【0004】本発明の目的は、回転機構部なしに被処理
水から磁性物を磁気分離、除去する磁気分離装置を提供
することにある。
An object of the present invention is to provide a magnetic separation device which magnetically separates and removes magnetic substances from water to be treated without a rotating mechanism.

【0005】[0005]

【課題を解決するための手段】本発明はこのような課題
を解決するためになされたもので、上記目的は磁界発生
手段群を静止させ、磁界発生手段群の磁界を電気的に、
かつ被処理水と相対的に移動させることによって達成で
きる。
SUMMARY OF THE INVENTION The present invention has been made to solve such a problem, and the object is to make the magnetic field generating means group stationary and to electrically generate the magnetic field of the magnetic field generating means group.
And it can be achieved by moving it relative to the water to be treated.

【0006】上記の課題を解決するための本発明になる
第1の手段は、磁性を有する被除去物質を含む被処理水
から、磁界発生手段を有する磁気分離部の被除去物質吸
着面に、前記被除去物を吸着させて分離する浄化装置に
おいて、前記磁気分離部の静止した接水面である被除去
物質吸着面の非接水面側に、静止した複数の磁界発生手
段を配置し、該複数の磁界発生手段が発生する磁場強度
を個別に時間的に変化させる磁界制御手段を有してなる
磁場移動式磁気分離装置である。
A first means of the present invention for solving the above-mentioned problems is to remove the water to be removed containing the substance to be removed having magnetism, from the water to be removed of the magnetic separation portion having the magnetic field generating means to the substance to be removed adsorption surface. In the purifying device for adsorbing and separating the object to be removed, a plurality of stationary magnetic field generating means are arranged on the non-water contact surface side of the material to be removed adsorption surface, which is the stationary water contact surface of the magnetic separation unit, The magnetic field movement type magnetic separation device having magnetic field control means for individually temporally changing the magnetic field strength generated by the magnetic field generation means.

【0007】上記の課題を解決するための本発明になる
第2の手段は、磁性を有する被除去物質を含む被処理水
から、該被除去物質を、磁界発生手段を有する磁気分離
部の被除去物質吸着面に吸着させて分離する浄化装置に
おいて、 a.前記磁気分離部が、被処理水が流過する被処理水流
路と、該被処理水流路内に配置され気密筐体に複数の磁
界発生手段を内装し該気密筐体外表面が被除去物質吸着
面となる磁気分離板と、前記複数の磁界発生手段が発生
する磁場強度を個別に順に時間的に変化させる磁界制御
手段と、を含んでなり、 b.前記磁気分離板は、少なくともその被除去物質吸着
面下部が流過する被処理水に没水するように、かつ被除
去物質吸着面が上下方向に延びるように配置され、 c.前記複数の磁界発生手段は、その発生する磁場が、
前記被除去物質吸着面に沿って上下方向に順に並ぶよう
に前記磁気分離板内に配置され、 d.前記磁界制御手段は、前記複数の磁界発生手段の発
生する磁場の強い位置が前記被除去物質吸着面の下部か
ら上部に向かって移動し、該磁場の強い位置の下方に接
して形成される磁場の弱い位置が磁場の強い位置の移動
とともに前記被除去物質吸着面の下部から上部に向かっ
て移動するように、前記複数の磁界発生手段を制御する
ものである、磁場移動式磁気分離装置である。
The second means of the present invention for solving the above-mentioned problems is to remove the substance to be removed from the water to be treated containing the substance to be removed having magnetism in the magnetic separation part having the magnetic field generating means. In a purifying device for adsorbing and separating a removal substance adsorption surface, a. The magnetic separation unit has a treated water flow path through which the treated water flows, and a plurality of magnetic field generating means are provided in an airtight casing arranged in the treated water flow passage, and the outer surface of the hermetic casing adsorbs a substance to be removed. A magnetic separation plate serving as a surface, and magnetic field control means for individually and temporally changing the magnetic field strengths generated by the plurality of magnetic field generation means, b. The magnetic separation plate is arranged such that at least a lower portion of the substance-to-be-removed substance adsorption surface is submerged in the water to be treated and the substance-to-be-removed substance adsorption surface extends vertically. C. The magnetic field generated by the plurality of magnetic field generating means is
Arranged in the magnetic separation plate so as to be lined up and down in order along the removal target adsorption surface, d. In the magnetic field control means, the magnetic field generated by the plurality of magnetic field generation means moves from a lower part to an upper part of the adsorption surface of the substance to be removed, and a magnetic field formed in contact with a lower position of the strong magnetic field. Is a magnetic field moving type magnetic separation device for controlling the plurality of magnetic field generating means so that a weak position of the magnetic field moves from the lower part to the upper part of the substance to be removed adsorption surface along with the movement of the strong magnetic field position. .

【0008】上記第2の手段において、磁気分離板は、
その被除去物質吸着面のすくなくとも一部が水面上にな
るように配置され、被除去物質吸着面の該水面上になる
部分に対向する位置に吸引口を備えた回収管と、該回収
管内部を排気して低圧とする排気手段を備えたものとし
てもよい。
In the second means, the magnetic separator is
A recovery pipe having a suction port at a position facing at least a part of the surface of the substance to be removed that is above the water surface, and a recovery pipe having a suction port It may be provided with an exhaust means for exhausting the gas to a low pressure.

【0009】また、上記第2の手段において、被処理水
流路が密閉流路であり、磁気分離板は、その被除去物質
吸着面全体が水面下になるように配置され、被除去物質
吸着面の上端部分に対向する位置に吸引口を備えた回収
管と、該回収管内部の水を吸引する吸引手段を備えたも
のとしてもよい。
Further, in the second means, the water passage to be treated is a closed passage, and the magnetic separation plate is arranged such that the entire adsorption surface of the substance to be removed is below the water surface. It may be provided with a recovery pipe having a suction port at a position facing the upper end of the above and a suction means for sucking water in the recovery pipe.

【0010】[0010]

【作用】複数の磁界発生手段が発生する磁場の強さを、
個別に時間的に変化させることにより、被除去物質吸着
面の強い磁場が形成される位置を順次連続的に移動させ
ることができる。被除去物質吸着面に被除去物質が吸着
された状態で、強い磁場が形成される位置を順次連続的
に移動させると、吸着された被除去物質は被除去物質吸
着面上で強い磁場の位置の移動につれて磁場の強い位置
に移動する。したがって、装置の機械的な動作を伴うこ
となく、吸着された被除去物質を被除去物質吸着面の所
望の位置に集めることができる。被除去物質が被除去物
質吸着面の所望の位置に集まれば、その位置に吸引口を
対向させた回収管を配置し、回収管内部を低圧に吸引し
て被除去物質を回収管に回収することができる。
[Operation] The strength of the magnetic field generated by the plurality of magnetic field generation means
By individually changing the time, the position where a strong magnetic field is formed on the removal target substance adsorption surface can be sequentially and continuously moved. If the position where a strong magnetic field is formed is sequentially moved while the substance to be removed is adsorbed on the surface to be removed substance adsorbed, the substance to be adsorbed is moved to the position of the strong magnetic field on the surface to be adsorbed substance to be removed. Moves to a position where the magnetic field is strong. Therefore, the adsorbed substance to be removed can be collected at a desired position on the adsorbed substance to be removed surface without the mechanical operation of the device. When the substance to be removed is collected at a desired position on the surface to be adsorbed with the substance to be removed, a recovery pipe with a suction port facing it is arranged at that position, and the substance inside the recovery pipe is sucked to a low pressure to collect the substance to be removed into the recovery pipe. be able to.

【0011】なお、被除去物質を被除去物質吸着面の所
望の位置に集める場合、その所望の位置は、水面下でも
水面上でもよく、どちらであっても、回収管により吸引
回収することができる。
When collecting the substance to be removed at a desired position on the adsorption surface of the substance to be removed, the desired position may be below the water surface or above the water surface. it can.

【0012】[0012]

【実施例】以下、本発明の第1の実施例を図1、図2、
図3により説明する。図1に、湖沼、河川、下水等の原
水を浄化処理する場合の磁気分離装置を用いた浄化装置
の例を示す。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of the present invention will be described below with reference to FIGS.
This will be described with reference to FIG. FIG. 1 shows an example of a purification device using a magnetic separation device when purifying raw water such as lakes, rivers, and sewage.

【0013】水処理する湖沼、河川、下水等の原水に
は、磁気分離工程への前処理として、例えば四三酸化鉄
等の磁性粉と凝集剤としての硫酸バン土やポリ塩化アル
ミニウムが加えられて撹拌され、原水中の固形浮遊物や
藻類、菌類、微生物は、凝集剤によって磁性粉と結合し
コロイド状の多数の磁性を持った磁性凝集体となる。こ
れらの磁性凝集体が磁気分離により吸着捕捉され、原水
中から分離される。以下に説明する実施例においては、
この磁性凝集体(磁性フロック)を被除去物質として説
明するが、磁性凝集体は原水中の固形浮遊物や藻類、菌
類、微生物からなるものだけでなく、のちに述べるよう
な、原水中の不純物、汚濁物などで、磁気分離できるも
のが、本発明における被除去物質である。
To the raw water such as lakes, rivers, and sewage to be treated with water, magnetic powder such as ferric tetroxide and vanadium sulfate or polyaluminum chloride as a coagulant are added as a pretreatment for the magnetic separation process. The solid suspension, algae, fungi, and microorganisms in the raw water are mixed with the magnetic powder by the aggregating agent to form a large number of colloidal magnetic aggregates having magnetism. These magnetic aggregates are adsorbed and captured by magnetic separation and separated from raw water. In the examples described below,
This magnetic aggregate (magnetic floc) will be explained as a substance to be removed. The magnetic aggregate is not limited to solid suspended matter in the raw water, algae, fungi, and microorganisms, but also impurities in the raw water as described later. The substances that can be magnetically separated, such as pollutants, are the substances to be removed in the present invention.

【0014】図1に示す水浄化装置は、貯水池1の原水
をフィルタ3を介装した導水管2を通して汲みあげるポ
ンプ4と、このポンプ4の吐出側に導水管2Aで接続さ
れ汲みあげられた原水6を一時貯溜する原水貯槽5と、
モータ10で回転駆動される撹拌機11を内装し、導水
管2Aで前記原水貯槽5に接続され撹拌槽9と、導水管
2Aに導管8で接続された薬剤調整装置7と、撹拌槽9
に弁13を介装した導水管14で接続された浄化磁気分
離容器15と、この浄化磁気分離容器15の出側に一端
を接続され、他端を前記貯水池1に接続した導水管16
と、浄化磁気分離容器15に吸引管17で接続されたス
ラッジ槽18と、を含んで構成されている。なお、原水
や処理水を移動させるためのポンプや水頭差及び吸引管
に負圧を発生させる手段については、図示ならびに説明
を省略した。
The water purifying apparatus shown in FIG. 1 has a pump 4 for pumping raw water from a reservoir 1 through a water conduit 2 having a filter 3 and a discharge pipe 2A connected to the discharge side of the pump 4. Raw water storage tank 5 for temporarily storing raw water 6,
A stirrer 11 which is rotationally driven by a motor 10 is internally provided, and a stirring tank 9 is connected to the raw water storage tank 5 by a water guiding tube 2A, a medicine adjusting device 7 connected by a conduit 8 to the water guiding tube 2A, and a stirring tank 9
A purifying magnetic separation container 15 connected to a purifying magnetic separation container 15 via a valve 13 and a water guiding pipe 16 having one end connected to the outlet side of the purifying magnetic separation container 15 and the other end connected to the reservoir 1.
And a sludge tank 18 connected to the purified magnetic separation container 15 by a suction pipe 17. A pump for moving the raw water and the treated water and a means for generating a negative pressure in the head difference and the suction pipe are not shown and described.

【0015】上記構成の装置の運転操作は、次のように
行われる。貯水池1の原水は導水管2から大きなゴミを
取るためのフィルタ3を通してポンプ4で原水貯槽5に
一旦蓄えられる。この原水6に、薬剤調整装置7から四
三酸化鉄の磁性粉とポリ塩化アルミニウム等の凝集剤が
導管8を通じて加えられ、撹拌槽9に送りこまれる。撹
拌槽9に送りこまれた原水6は、撹拌槽9でモータ10
で回転する撹拌機11で撹拌され、原水中の固形浮遊物
や藻類、菌類、微生物は、凝集剤によって磁性粉と結合
しコロイド状の多数の磁性を持った磁性凝集体となる。
磁性凝集体を含む前処理水12は、弁13を経て導水管
14を通り、浄化磁気分離容器15内に流入する。浄化
磁気分離容器15では、磁性凝集体が分離除去され、浄
化された処理水は導水管16を通り水源に戻る。一方、
浄化磁気分離容器15で分離、除去された磁性凝集体
は、吸引管17による吸引で取り出され、スラッジ槽1
8に貯蔵される。スラッジ槽18に貯蔵された磁性凝集
体は、この後脱水処理された後焼却されたり、磁性粉を
回収された後埋立等に廃棄されたり等の最終処分が行わ
れる。
The operation of the apparatus having the above structure is carried out as follows. Raw water in the reservoir 1 is temporarily stored in a raw water storage tank 5 by a pump 4 through a filter 3 for removing large dust from the water conduit 2. A magnetic powder of ferric tetroxide and an aggregating agent such as polyaluminum chloride are added to the raw water 6 from a chemical adjusting device 7 through a conduit 8 and sent to a stirring tank 9. The raw water 6 sent to the stirring tank 9 is supplied to the motor 10 in the stirring tank 9.
The solid suspended matter, algae, fungi, and microorganisms in the raw water, which are agitated by the agitator 11 that rotates at, are combined with the magnetic powder by the aggregating agent to form a large number of colloidal magnetic aggregates having magnetism.
The pretreated water 12 containing magnetic aggregates passes through the valve 13 and the water conduit 14 and flows into the purified magnetic separation container 15. In the purification magnetic separation container 15, the magnetic aggregates are separated and removed, and the purified treated water passes through the water conduit 16 and returns to the water source. on the other hand,
The magnetic agglomerates separated and removed in the purification magnetic separation container 15 are taken out by suction through the suction pipe 17, and the sludge tank 1
8 is stored. The magnetic agglomerates stored in the sludge tank 18 are then subjected to dewatering and then incinerated, or the magnetic powder is recovered and then disposed of in landfill or the like for final disposal.

【0016】図2は磁場移動式磁気分離装置である浄化
磁気分離容器15の構造を示している。浄化磁気分離容
器15は、上部が開放された前処理水流路19と、この
前処理水流路19に内装され過半部が没水した平板状で
気密の筐体である複数の磁気分離板21と、各磁気分離
板21に内装されたレーストラック状の磁界発生手段で
ある電磁石20A,20B,20C,20Dと、電磁石
20A〜20Dに配線23A,23Bで接続された磁界
制御手段である電源22と、前記磁気分離板21それぞ
れの水面上の位置に対向して配置された吸引口26を有
する回収管25と、該回収管25に接続された吸引管1
7と、を含んで構成されている。
FIG. 2 shows the structure of a purification magnetic separation container 15 which is a magnetic field moving type magnetic separation device. The purified magnetic separation container 15 includes a pretreatment water channel 19 having an open upper portion, and a plurality of magnetic separation plates 21 which are a flat plate-like and airtight housing in which the pretreatment water channel 19 is submerged and a majority of which is submerged. , Electromagnets 20A, 20B, 20C and 20D which are racetrack-shaped magnetic field generating means installed in each magnetic separation plate 21, and a power source 22 which is magnetic field control means connected to the electromagnets 20A to 20D by wirings 23A and 23B. , A recovery pipe 25 having a suction port 26 arranged so as to face the water surface of each of the magnetic separation plates 21, and a suction pipe 1 connected to the recovery pipe 25.
7 is included.

【0017】磁気分離板21の平板面が被除去物質吸着
面をなしており、磁気分離板21は、厚み面が前処理水
の流れに垂直になるように(被除去物質吸着面が前処理
水の流れに平行するように)、かつ被除去物質吸着面が
ほぼ鉛直になるように配置され、上端部は前処理水流路
19の上端より上方に出ている。前記回収管25の吸引
口26は、被除去物質吸着面が前処理水流路19の上端
より上方に出ている部分に対向して配置され、両側に被
除去物質吸着面があるところでは、回収管25の両側に
吸引口26が設けられている。
The flat surface of the magnetic separation plate 21 serves as a surface for adsorbing the substance to be removed, and the magnetic separation plate 21 has a thickness surface perpendicular to the flow of the pretreatment water (the surface for adsorbing the substance to be removed is pretreated). It is arranged so as to be parallel to the flow of water) and the adsorption surface of the substance to be removed is substantially vertical, and the upper end portion is above the upper end of the pretreatment water channel 19. The suction port 26 of the recovery pipe 25 is arranged so as to face the portion where the substance-to-be-removed adsorbing surface is located above the upper end of the pretreatment water flow path 19, and where the substance-to-be-removed substance adsorbing surface is present on both sides. Suction ports 26 are provided on both sides of the pipe 25.

【0018】電磁石20A〜20Dは、さきに述べたよ
うに、それぞれレーストラック状(長円形)に形成さ
れ、直線部が上下になるような配置で、磁気分離板21
内に上下に順に積み重なる形(電磁石20Dが一番下で
電磁石20Aが一番上になる形)で内装されている。電
磁石20A〜20Dは、磁気分離板の互いに対向する面
に対称的に磁場を形成し、磁気分離板の両側の外表面を
共に被除去物質吸着面にしている。電源22は、電磁石
20A〜20Dに給電し、それぞれ個別にその発生磁界
の強さを変化できるようになっており、あらかじめ設定
されたパターンに基づいて各電磁石の励磁、消磁のタイ
ミング、励磁、増磁、減磁、消磁の長さを制御する。
As described above, the electromagnets 20A to 20D are each formed in a racetrack shape (elliptical shape), and are arranged such that the straight line portions are vertically arranged.
The interiors are stacked inside one another in a vertically stacked manner (electromagnet 20D is at the bottom and electromagnet 20A is at the top). The electromagnets 20A to 20D symmetrically form magnetic fields on the surfaces of the magnetic separation plate that face each other, and both outer surfaces of the magnetic separation plate are adsorption surface for the substance to be removed. The power supply 22 supplies power to the electromagnets 20A to 20D and can individually change the strength of the generated magnetic field. Based on a preset pattern, the excitation and demagnetization timings of each electromagnet, the excitation, and the increase. Controls the length of magnetism, demagnetization, and demagnetization.

【0019】なお、前記スラッジ槽18は、吸引管17
に接続された真空排気装置30と、この真空排気装置3
0に接続されたスラッジタンク27と、真空排気装置3
0に接続された放気管28と、スラッジタンク27に接
続された取り出し管29と、を含んで構成されている。
The sludge tank 18 has a suction pipe 17
The vacuum exhaust device 30 connected to the
Sludge tank 27 connected to 0 and vacuum exhaust device 3
It is configured to include an air discharge pipe 28 connected to 0 and a take-out pipe 29 connected to the sludge tank 27.

【0020】以下、上記構成の装置の動作を説明する。
ポンプ4により貯水池1から汲みあげられた原水6は、
原水貯槽5に一時貯溜されたのち、撹拌槽9に送りこま
れる。撹拌槽9に送りこまれる原水6には、薬剤調整装
置7から磁性粉(四三酸化鉄)と凝集剤(ポリ塩化アル
ミニウム)が混入され、撹拌槽9で撹拌されて、原水中
の固形浮遊物や藻類、菌類、微生物は、凝集剤によって
磁性粉と結合しコロイド状の多数の磁性を持った磁性凝
集体となる。固形浮遊物や藻類、菌類、微生物が磁性凝
集体となった原水を前処理水12と呼ぶ。前処理水12
は撹拌槽9から、浄化磁気分離容器15に送られ、前処
理水流路19を紙面垂直方向に流れる。
Hereinafter, the operation of the apparatus having the above structure will be described.
The raw water 6 pumped from the reservoir 1 by the pump 4 is
After being temporarily stored in the raw water storage tank 5, it is sent to the stirring tank 9. Magnetic powder (ferric tetroxide) and a flocculant (polyaluminum chloride) are mixed into the raw water 6 sent to the stirring tank 9 from the chemical regulator 7 and stirred in the stirring tank 9 to obtain a solid suspension in the raw water. The algae, fungi, and microorganisms are bound to the magnetic powder by the aggregating agent to form a large number of colloidal magnetic aggregates having magnetism. Raw water in which solid suspended matter, algae, fungi, and microorganisms become magnetic aggregates is called pretreated water 12. Pre-treated water 12
Is sent from the stirring tank 9 to the purification magnetic separation container 15 and flows through the pretreatment water channel 19 in the direction perpendicular to the paper surface.

【0021】前処理水12中の磁性凝集体(以下、磁性
フロックともいう)は、励磁された電磁石の発生磁界に
よって、磁気分離板21の表面(被除去物吸着面)に吸
着され蓄積される。図3に示すように、最下部の電磁石
20Dの発生磁界に蓄積した磁性フロック群24Dは、
電磁石20Dを減磁することにより、より発生磁界の大
きい電磁石20Cの磁界側に少なくともその一部が移動
し、電磁石20Cの磁界内に蓄積している磁性フロック
群24Cに吸収される。この後、電磁石20Cを減磁す
れば、発生磁界の大きい電磁石20Bの磁界側に少なく
とも磁性フロック群24Cの一部が移動し、電磁石20
Bの磁界内に蓄積している磁性フロック群24Bに吸収
される。この後、電磁石20Dを増磁し処理水中の磁性
フロックを再び吸着する。このようにして磁性フロック
群は前処理水12の気液界面側に移動し、気相部の電磁
石20Aの発生磁界内まで移動する。
Magnetic agglomerates (hereinafter also referred to as magnetic flocs) in the pretreated water 12 are adsorbed and accumulated on the surface (adhesion surface of the object to be removed) of the magnetic separation plate 21 by the magnetic field generated by the excited electromagnet. . As shown in FIG. 3, the magnetic flock group 24D accumulated in the magnetic field generated by the lowermost electromagnet 20D is
By demagnetizing the electromagnet 20D, at least a part of the electromagnet 20C moves to the magnetic field side of the electromagnet 20C having a larger generated magnetic field, and is absorbed by the magnetic floc group 24C accumulated in the magnetic field of the electromagnet 20C. Thereafter, if the electromagnet 20C is demagnetized, at least a part of the magnetic floc group 24C moves to the magnetic field side of the electromagnet 20B having a large generated magnetic field, and the electromagnet 20C
It is absorbed by the magnetic floc group 24B accumulated in the magnetic field of B. After that, the electromagnet 20D is magnetized and the magnetic flocs in the treated water are adsorbed again. In this way, the magnetic floc group moves to the gas-liquid interface side of the pretreated water 12 and moves into the magnetic field generated by the electromagnet 20A in the gas phase.

【0022】磁性フロック群が気相部の電磁石20Aの
発生磁界内まで移動したら、スラッジ槽18内の磁性フ
ロック回収手段例えば真空排気装置30により、吸引管
17を通じて回収管25内を負圧にし、電磁石20Aを
減磁もしくは消磁する。これにより、電磁石20Aの発
生磁界内に移動していた磁性フロック群は、吸引口26
から回収管25に吸引されて磁気分離板21の表面(被
除去物吸着面)から分離され、回収管25に回収され
る。回収管25に回収された磁性フロック群は、次いで
吸引管17を通って真空排気装置30に導かれ、ここで
空気と分離されてスラッジタンク27に回収される。分
離された空気は放気管28から大気に放出される。ま
た、スラッジタンク27に回収された磁性フロック群
は、取り出し管29を通じて取り出され、脱水処理や磁
性粉回収処理を行った後、焼却、埋立等の最終処分に付
される。
When the magnetic floc group has moved into the magnetic field generated by the electromagnet 20A in the vapor phase portion, the magnetic floc recovery means in the sludge tank 18, for example, the vacuum exhaust device 30, makes the inside of the recovery pipe 25 a negative pressure through the suction pipe 17. The electromagnet 20A is demagnetized or demagnetized. As a result, the magnetic flock group, which has moved into the magnetic field generated by the electromagnet 20A, becomes
Is sucked into the recovery pipe 25, separated from the surface of the magnetic separation plate 21 (adsorption surface of the object to be removed), and collected in the recovery pipe 25. The magnetic floc group collected in the collection pipe 25 is then guided to the vacuum exhaust device 30 through the suction pipe 17, where it is separated from air and collected in the sludge tank 27. The separated air is discharged to the atmosphere through the air discharge pipe 28. The magnetic flocs collected in the sludge tank 27 are taken out through the take-out pipe 29, subjected to dehydration treatment and magnetic powder collection treatment, and then subjected to final disposal such as incineration and landfill.

【0023】それぞれの電磁石は、磁気分離板21を介
して、前処理水12により冷却される。
Each electromagnet is cooled by the pretreated water 12 via the magnetic separation plate 21.

【0024】本実施例によれば、磁気分離部の磁界発生
手段を静止させ、発生磁界の強さを電気的に、周期的に
変化させることにより、磁性フロック群を移動できるの
で、磁性フロック群の移動のために磁界発生手段を移動
させる機構が必要でなく、磁気分離部の信頼性が大幅に
向上する。
According to the present embodiment, the magnetic floc group can be moved by stopping the magnetic field generating means of the magnetic separation unit and electrically and periodically changing the strength of the generated magnetic field, so that the magnetic floc group can be moved. Since a mechanism for moving the magnetic field generating means for moving the magnetic field is not required, the reliability of the magnetic separation part is significantly improved.

【0025】また、磁界発生手段の大部分を前処理水の
水面下に配置できるので、前処理水の流路断面の大部分
に前処理水を流動できるので、流路部分を大幅に小型化
できる。また、前処理水流動方向に磁性発生手段の磁界
を長く、かつ水深の深さ方向に均一に配置できるので、
長方状の流体流路でも流路断面のどの位置においても均
一に磁性フロックを吸着でき、流路形状による流動圧力
損失を小さくできる。
Further, since most of the magnetic field generating means can be arranged below the surface of the pretreatment water, the pretreatment water can flow over most of the cross section of the passage of the pretreatment water. it can. Further, since the magnetic field of the magnetism generating means can be made long in the pre-treatment water flow direction and can be uniformly arranged in the depth direction of the water depth,
Even in a rectangular fluid channel, magnetic flocs can be evenly adsorbed at any position on the channel cross section, and the flow pressure loss due to the channel shape can be reduced.

【0026】なお、本実施例では流体の流れ方向に1段
の磁気分離板を設けた場合について説明したが、磁気分
離板を流れ方向に複数段設け、深さ方向に同一深さに配
置した電磁石の減磁と増磁のタイミングを異ならせ、絶
えず増磁状態の電磁石が流れ方向に少なくとも1段分存
在するようにすれば更に磁性フロックの捕捉効率を上げ
ることができる。
In the present embodiment, the case where one magnetic separation plate is provided in the fluid flow direction has been described, but a plurality of magnetic separation plates are provided in the flow direction and are arranged at the same depth in the depth direction. If the demagnetizing and magnetizing timings of the electromagnets are made different so that the electromagnets in the magnetized state are constantly present in at least one stage in the flow direction, the trapping efficiency of the magnetic flocs can be further improved.

【0027】また、本実施例においては、レーストラッ
ク状の電磁石のフィールドに相当する部分が空洞になっ
ているが、この部分に鉄芯を配置すれば、磁気分離板表
面での磁場の強さを平均化する効果がある。
Further, in this embodiment, the portion corresponding to the field of the racetrack-shaped electromagnet is hollow, but if an iron core is arranged in this portion, the strength of the magnetic field on the surface of the magnetic separation plate is increased. Has the effect of averaging.

【0028】本発明になる第2の実施例を図4に示す。
本図が図3に示す実施例と異なる点は、磁気分離板21
の表面に、該表面からの高さの異なる強磁性突起物30
A(高さH)、30B(高さL)と、同じく磁気分離板
21の表面からの高さの異なる非磁性突起物31A(高
さH)、31B(高さL)を、同じ高さの物同士それぞ
れ交互に積層し、磁気分離板21表面に更に大きな磁場
勾配を発生させた点である。これにより、前処理水12
中の磁性フロックに対する吸着力を大きくして、捕捉効
率の向上させ、磁性フロック群を移動させる力を大きく
し、さらに表面に凹凸をつけて前処理水の流れの渦部を
作り、この谷の底の部分に磁性フロックを蓄積させるこ
とにより、蓄積した磁性フロックが前処理水の流れの力
で磁気分離板21から剥離することを防止できる効果が
ある。
A second embodiment according to the present invention is shown in FIG.
This drawing is different from the embodiment shown in FIG. 3 in that the magnetic separation plate 21
Of the ferromagnetic protrusions 30 having different heights from the surface of the
A (height H) and 30B (height L) and non-magnetic protrusions 31A (height H) and 31B (height L), which also have different heights from the surface of the magnetic separation plate 21, have the same height. This is the point in which the magnetic field separation plates 21 are alternately laminated to generate a larger magnetic field gradient on the surface of the magnetic separation plate 21. As a result, the pretreated water 12
By increasing the adsorption force to the magnetic flocs in the inside, improving the trapping efficiency, increasing the force to move the magnetic flocs, and making unevenness on the surface to create a vortex part of the flow of pretreatment water, By accumulating the magnetic flocs in the bottom portion, it is possible to prevent the accumulated magnetic flocs from being separated from the magnetic separation plate 21 by the force of the flow of the pretreatment water.

【0029】また、図2の磁気分離板21の表面を、前
処理水流れ方向に波型、山型、台地型等の凹凸加工を施
すことによっても、磁気分離板21の表面に渦部がで
き、前処理水の流れで蓄積した磁性フロックが磁気分離
板21から剥離することを防止できる効果がある。
Further, the surface of the magnetic separation plate 21 of FIG. 2 is subjected to corrugation, ridge, plateau, etc., in the direction of pretreatment water flow, so that the surface of the magnetic separation plate 21 has a vortex portion. Therefore, it is possible to prevent the magnetic flocs accumulated by the flow of the pretreatment water from being separated from the magnetic separation plate 21.

【0030】また、図2の磁気分離板21の表面に、前
処理水流れ方向に波型、山型、台地型等の凹凸加工を施
した強磁性もしくは非磁性の金網、多孔板等の穴明き凹
凸板をとりつけることによっても、磁気分離板21の表
面近傍に渦部ができ、さらに磁性フロックが磁気分離板
21の表面と穴明き凹凸板の間に蓄積し、前処理水の流
れで蓄積した磁性フロックが磁気分離板21から剥離す
ることを防止できる効果がある。
Further, the surface of the magnetic separation plate 21 shown in FIG. 2 is provided with holes such as a ferromagnetic or non-magnetic wire net or a perforated plate, which is corrugated in the direction of the pretreatment water, such as a corrugated shape, a mountain shape, or a plateau shape. By attaching the perforated concave-convex plate, a vortex portion is also formed in the vicinity of the surface of the magnetic separation plate 21, and magnetic flocs are accumulated between the surface of the magnetic separation plate 21 and the perforated concave-convex plate, and are accumulated by the flow of pretreatment water. This has an effect of preventing the magnetic flocs from peeling off from the magnetic separation plate 21.

【0031】また、図3で強磁性突起物30A、30B
と非磁性突起物31A、31Bの代わりに、強磁性金属
のメタルウールを用いても、大きな磁気勾配を得られる
ので、磁性フロックの捕捉効率を向上させることができ
る。
Further, in FIG. 3, ferromagnetic protrusions 30A and 30B are provided.
Even if metal wool of a ferromagnetic metal is used instead of the non-magnetic protrusions 31A and 31B, a large magnetic gradient can be obtained, so that the trapping efficiency of magnetic flocs can be improved.

【0032】本発明になる第3の実施例を図5に示す。
本実施例が図2,3に示す実施例と異なる点は、磁気分
離板21内の電磁石20A、20B、20C、20D、
の横に電磁石20E、20F、20Gを半ピッチずらし
て配置した点にある。本構造により、磁気分離板21の
表面の磁性フロック群を移動させる時、電磁石20D、
20G、20C、20F順に減磁することにより、磁気
分離板21の表面の磁界変化をよりスムースに行うこと
ができ、磁性フロックが前処理水の流れによって剥離し
にくくなる効果がある。
FIG. 5 shows a third embodiment according to the present invention.
This embodiment differs from the embodiments shown in FIGS. 2 and 3 in that the electromagnets 20A, 20B, 20C, 20D in the magnetic separation plate 21 are
The electromagnets 20E, 20F and 20G are arranged beside each other with a half pitch shift. With this structure, when the magnetic flock group on the surface of the magnetic separation plate 21 is moved, the electromagnet 20D,
By demagnetizing in order of 20G, 20C, and 20F, the magnetic field on the surface of the magnetic separation plate 21 can be changed more smoothly, and the magnetic flocs are less likely to be separated due to the flow of pretreatment water.

【0033】本発明になる第4の実施例を図6に示す。
本実施例が図2に示す実施例と異なる点は、磁気分離板
21および吸引口26、回収管25を大気と隔離された
密閉型の前処理水流路19内に配置した点にある。本構
造により、前処理水は前処理水流路19を満管状態(満
水状態)で流動しており、磁性フロック群は吸引口26
から前処理水の一部とともに回収管25に回収される。
したがって、前処理水流路19内が高圧の状態でもより
圧力が低い回収管25に磁性フロック群を排除でき、図
1の浄化装置のポンプ4の吐出側から導水管16の出口
までのラインを満管状態で運転でき、水を装置内で循環
させるためのポンプを最小限にする事ができる。また、
前処理水流路19から前処理水が溢れでることも防止で
きる。なお、この実施例では、回収管25を前処理水流
路19の上方に配置したが、回収管25をそれぞれどの
部位に配置してもよく、磁性フロック群が吸引口26に
移動するように電磁石20A、20B、20C、20D
の磁界を制御すれば良い。
FIG. 6 shows a fourth embodiment according to the present invention.
The present embodiment is different from the embodiment shown in FIG. 2 in that the magnetic separation plate 21, the suction port 26, and the recovery pipe 25 are arranged in a sealed pretreatment water channel 19 which is isolated from the atmosphere. With this structure, the pretreated water flows in the pretreated water channel 19 in a full state (full state), and the magnetic floc group has the suction port 26.
Is recovered in the recovery pipe 25 together with part of the pretreated water.
Therefore, even if the inside of the pretreatment water flow path 19 is in a high pressure state, the magnetic floc group can be eliminated in the recovery pipe 25 having a lower pressure, and the line from the discharge side of the pump 4 to the outlet of the water guiding pipe 16 of the purifying device of FIG. It can be operated as a pipe, and the pump for circulating water in the equipment can be minimized. Also,
It is possible to prevent the pretreated water from overflowing from the pretreated water channel 19. Although the recovery pipe 25 is arranged above the pretreatment water channel 19 in this embodiment, the recovery pipe 25 may be arranged at any position, and the electromagnet is moved so that the magnetic floc group moves to the suction port 26. 20A, 20B, 20C, 20D
It suffices to control the magnetic field.

【0034】以上の実施例では、電磁石に常電導磁石を
使用した場合に付いて説明したが、この電磁石に超電導
磁石を使用すれば発生磁界がさらに大きくすることがで
き、磁性フロックの捕捉効率、移動力がさらに向上する
効果がある。この場合、磁気分離板21は真空断熱容器
となり、超電導磁石は液体ヘリウムや液体窒素等の冷媒
や機械式、電子式冷凍機で直接、間接的に冷却される。
電磁石の形状もレーストラック以外の例えば円筒形状や
それらの組み合わせでもよく、要は磁性フロック群を吸
引口近傍に移動できる様な任意の磁石形状であればよ
い。
In the above embodiments, the case where the normal conducting magnet is used as the electromagnet has been described. However, when the superconducting magnet is used as the electromagnet, the generated magnetic field can be further increased, and the magnetic floc trapping efficiency, This has the effect of further improving the movement power. In this case, the magnetic separation plate 21 serves as a vacuum heat insulating container, and the superconducting magnet is directly or indirectly cooled by a refrigerant such as liquid helium or liquid nitrogen or a mechanical or electronic refrigerator.
The shape of the electromagnet may be, for example, a cylindrical shape other than the race track, or a combination thereof, as long as it is an arbitrary magnet shape that can move the magnetic floc group to the vicinity of the suction port.

【0035】また、以上の実施例では電磁石による磁気
分離部を主の磁気分離器として使用した場合について説
明したが、本磁気分離部が副の磁気分離要素として使用
し、本磁気分離部の後段に高勾配磁気分離要素、例えば
高勾配磁気フィルタを組み合わせた場合でも、前段の磁
気分離要素として磁性フロック群の第1次吸着、除去装
置として、同様な効果を生じる。
Further, in the above embodiment, the case where the magnetic separation part by the electromagnet is used as the main magnetic separator has been described. However, this magnetic separation part is used as the sub magnetic separation element, and the latter stage of this magnetic separation part is used. Even when a high-gradient magnetic separation element, for example, a high-gradient magnetic filter is combined with, a similar effect can be obtained as a primary adsorption / removal device for the magnetic floc group as the preceding magnetic separation element.

【0036】また、磁気分離板21の表面にフッ素樹脂
等の剥離促進皮膜を付けることにより、表面に吸着した
磁性フロック群の磁場変化による移動を容易にし、除去
効率を向上することができる。
Further, by applying a peeling promoting film such as a fluororesin on the surface of the magnetic separation plate 21, it is possible to facilitate the movement of the magnetic floc group adsorbed on the surface due to the change in the magnetic field and improve the removal efficiency.

【0037】また、気密性の磁気分離板内に配置した電
磁石群の冷却を、板内に浄化処理水を導いて流動させて
冷却すれば、電磁石の冷却をさらに促進することができ
る。
Further, if the electromagnet group arranged in the airtight magnetic separation plate is cooled by guiding and flowing purified water into the plate, the cooling of the electromagnet can be further promoted.

【0038】また、以上で述べた原水とは、河川,ダ
ム,湖沼,海水,貯め池,工業廃水,下水,雨水等の不
純物を含んだ水であり、不純物とは有機物,無機物や微
生物等の物体,金属物,非金属物,土壌,放射性物質,
金属イオン等のものである。特に重金属イオンを含んだ
原水に硫酸第1鉄のような2価の鉄イオンとアルカリを
加えて重金属イオンを水酸化第1鉄の沈殿と共沈させた
あと、空気で酸化して沈殿をフェライト化する。このフ
ェライト化によって重金属は磁性分離ができる。この場
合、重金属イオンのみの分離が目的であれば、凝集剤は
不要となる。したがって、この場合、原水には、前処理
として硫酸第1鉄,アルカリ溶液及び空気を注入し撹拌
槽で処理した後、磁気分離部に前処理水を導くようにす
ればよい。
The raw water mentioned above is water containing impurities such as rivers, dams, lakes, seawater, reservoirs, industrial wastewater, sewage, rainwater, etc. The impurities are organic substances, inorganic substances, microorganisms and the like. Object, metal, non-metal, soil, radioactive material,
For example, metal ions. In particular, divalent iron ions such as ferrous sulfate and alkali are added to raw water containing heavy metal ions to coprecipitate heavy metal ions with the precipitate of ferrous hydroxide, and then oxidized with air to precipitate the precipitates with ferrite. Turn into. This ferritization allows the heavy metal to be magnetically separated. In this case, if the purpose is to separate only the heavy metal ions, the aggregating agent becomes unnecessary. Therefore, in this case, ferrous sulfate, an alkaline solution, and air are injected into the raw water as pretreatment and treated in a stirring tank, and then the pretreated water may be introduced to the magnetic separation unit.

【0039】[0039]

【発明の効果】本発明によれば、磁気分離部の磁界発生
手段を静止させ、順に配列された複数の磁界発生手段が
発生する磁界の強さを電気的に、周期的に変化させるこ
とにより、磁性フロック群を被除去物質吸着面上で移動
させることができるので、磁性フロック群の移動のため
に磁界発生手段を移動させる機構が必要でなく、磁気分
離部の信頼性が向上する。
According to the present invention, the magnetic field generating means of the magnetic separation section is made stationary, and the strength of the magnetic field generated by the plurality of magnetic field generating means arranged in order is electrically and periodically changed. Since the magnetic floc group can be moved on the removal target substance adsorbing surface, a mechanism for moving the magnetic field generating means for moving the magnetic floc group is not required, and the reliability of the magnetic separation unit is improved.

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

【図1】本発明の第1の実施例の浄化装置の要部構成を
示す系統図である。
FIG. 1 is a system diagram showing a main configuration of a purifying device according to a first embodiment of the present invention.

【図2】図1に示す実施例の磁気分離部の構成を示す断
面図である。
FIG. 2 is a cross-sectional view showing the configuration of a magnetic separation unit of the embodiment shown in FIG.

【図3】図2に示す実施例の部分の構造を示す斜視図で
ある。
FIG. 3 is a perspective view showing a structure of a portion of the embodiment shown in FIG.

【図4】本発明の第2の実施例を示す斜視図である。FIG. 4 is a perspective view showing a second embodiment of the present invention.

【図5】本発明の第3の実施例を示す断面図である。FIG. 5 is a sectional view showing a third embodiment of the present invention.

【図6】本発明の第4の実施例を示す断面図である。FIG. 6 is a sectional view showing a fourth embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 貯水池 2,2
A,2B 導水管 3 フィルタ 4 ポン
プ 5 原水貯槽 6 原水 7 薬剤調整装置 8 導管 9 撹拌槽 10 モ
ータ 11 撹拌機 12 前
処理水 13 弁 14 導
水管 15 浄化磁気分離容器(磁場移動式磁気分離装置) 16 導水管 17 吸
引管 18 スラッジ槽 19 前
処理水流路 20A〜20G 電磁石(磁界発生手段) 21 磁
気分離板 22 電源(磁界制御手段) 23A,
23B 配線 24B,24C,24D 磁性フロック群(磁性凝集
体) 25 回収管 26 吸
引口 27 スラッジタンク 28 放
気管 29 取り出し管 30 真
空排気装置
1 Reservoir 2,2
A, 2B Water conduit 3 Filter 4 Pump 5 Raw water storage tank 6 Raw water 7 Chemical agent adjusting device 8 Conduit tank 9 Stirring tank 10 Motor 11 Stirrer 12 Pretreatment water 13 Valve 14 Water guiding pipe 15 Purification magnetic separation container (magnetic separation type magnetic separation device) 16 Water Transfer Pipe 17 Suction Pipe 18 Sludge Tank 19 Pretreatment Water Flow Path 20A-20G Electromagnet (Magnetic Field Generating Means) 21 Magnetic Separation Plate 22 Power Supply (Magnetic Field Controlling Means) 23A,
23B Wiring 24B, 24C, 24D Magnetic Flock Group (Magnetic Aggregate) 25 Recovery Pipe 26 Suction Port 27 Sludge Tank 28 Air Outlet Pipe 29 Extraction Pipe 30 Vacuum Evacuation Device

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】 磁性を有する被除去物質を含む被処理水
から、磁界発生手段を有する磁気分離部の被除去物質吸
着面に、前記被除去物を吸着させて分離する浄化装置に
おいて、前記磁気分離部の静止した被除去物質吸着面の
反吸着面側に、静止した複数の磁界発生手段を配置し、
該複数の磁界発生手段が発生する磁場強度を個別に時間
的に変化させる磁界制御手段を有してなることを特徴と
する磁場移動式磁気分離装置。
1. A purifying apparatus for adsorbing and separating the substance to be removed from the water to be treated containing the substance to be removed, which is adsorbed on a surface of the substance to be removed adsorbing surface of a magnetic separation unit having a magnetic field generating means, wherein A plurality of stationary magnetic field generating means are arranged on the side opposite to the surface to be adsorbed of the substance to be removed which is stationary in the separation section,
A magnetic field moving type magnetic separation device comprising magnetic field control means for individually temporally changing the magnetic field strengths generated by the plurality of magnetic field generation means.
【請求項2】 磁性を有する被除去物質を含む被処理水
から、該被除去物質を、磁界発生手段を有する磁気分離
部の被除去物質吸着面に吸着させて分離する浄化装置に
おいて、 a.前記磁気分離部が、被処理水が流過する被処理水流
路と、該被処理水流路内に配置され気密筐体に複数の磁
界発生手段を内装し前記筐体外表面が被除去物質吸着面
となる磁気分離板と、前記複数の磁界発生手段が発生す
る磁場強度を個別に順に時間的に変化させる磁界制御手
段と、を含んでなり、 b.前記磁気分離板は、少なくともその被除去物質吸着
面下部が流過する被処理水に没水するように、かつ被除
去物質吸着面が上下方向に延びるように配置され、 c.前記複数の磁界発生手段は、その発生する磁場が、
前記被除去物質吸着面に沿って上下方向に順に並ぶよう
に前記磁気分離板内に配置され、 d.前記磁界制御手段は、前記複数の磁界発生手段の発
生する磁場の強い位置が前記被除去物質吸着面の下部か
ら上部に向かって移動し、該磁場の強い位置の下方に接
して形成される磁場の弱い位置が磁場の強い位置の移動
とともに前記被除去物質吸着面の下部から上部に向かっ
て移動するように、前記複数の磁界発生手段を制御する
ものである、ことを特徴とする磁場移動式磁気分離装
置。
2. A purifying apparatus for separating the substance to be removed containing the substance to be removed having magnetism by adsorbing the substance to be removed on the substance-to-be-removed substance adsorbing surface of the magnetic separation unit having a magnetic field generating means, a. The magnetic separation unit has a treated water flow path through which the treated water flows, and a plurality of magnetic field generating means are installed in an airtight casing arranged in the treated water flow passage, and the outer surface of the casing is an adsorption surface of a substance to be removed. And a magnetic field control means for individually and temporally changing the magnetic field strengths generated by the plurality of magnetic field generation means, b. The magnetic separation plate is arranged such that at least a lower portion of the substance-to-be-removed substance adsorption surface is submerged in the water to be treated and the substance-to-be-removed substance adsorption surface extends vertically. C. The magnetic field generated by the plurality of magnetic field generating means is
Arranged in the magnetic separation plate so as to be lined up and down in order along the removal target adsorption surface, d. In the magnetic field control means, the magnetic field generated by the plurality of magnetic field generation means moves from a lower part to an upper part of the adsorption surface of the substance to be removed, and a magnetic field formed in contact with a lower position of the strong magnetic field. Of the plurality of magnetic field generating means so that the weak position of the magnetic field moves from the lower part to the upper part of the adsorption target substance adsorbing surface along with the movement of the strong magnetic field position. Magnetic separation device.
【請求項3】 磁気分離板は、その被除去物質吸着面の
すくなくとも一部が水面上になるように配置され、被除
去物質吸着面の該水面上になる部分に対向する位置に吸
引口を備えた回収管と、該回収管内部を排気して低圧と
する排気手段を備えたことを特徴とする請求項2に記載
の磁場移動式磁気分離装置。
3. The magnetic separation plate is arranged such that at least a part of the surface to be adsorbed of the substance to be removed is on the water surface, and a suction port is provided at a position facing the part of the surface to be adsorbed on the substance to be removed which is on the water surface. The magnetic field moving type magnetic separation apparatus according to claim 2, further comprising: a recovery pipe provided and an exhaust unit configured to exhaust the inside of the recovery pipe to a low pressure.
【請求項4】 被処理水流路が密閉流路であり、磁気分
離板は、その被除去物質吸着面全体が水面下になるよう
に配置され、被除去物質吸着面の上端部分に対向する位
置に吸引口を備えた回収管と、該回収管内部の水を吸引
する吸引手段を備えたことを特徴とする請求項2に記載
の磁場移動式磁気分離装置。
4. The treated water flow path is a closed flow path, and the magnetic separation plate is arranged such that the entire adsorption surface of the substance to be removed is below the surface of the water, and the magnetic separation plate faces the upper end of the adsorption surface of the substance to be removed. The magnetic field transfer type magnetic separation device according to claim 2, further comprising: a recovery pipe having a suction port, and a suction means for sucking water in the recovery pipe.
【請求項5】 磁気分離板には上下方向の複数列の磁界
発生手段が内装され、隣接する磁界発生手段が上下方向
に位置をずらせて配置されていることを特徴とする請求
項2乃至4のうちのいずれかに記載の磁場移動式磁気分
離装置。
5. The magnetic separation plate is internally provided with a plurality of vertical magnetic field generating means, and adjacent magnetic field generating means are arranged so as to be vertically displaced from each other. 2. The magnetic field transfer type magnetic separation device according to any one of 1.
【請求項6】 被除去物質吸着面に凹凸が形成されてい
ることを特徴とする請求項1乃至5のうちのいずれかに
記載の磁場移動式磁気分離装置。
6. The magnetic field transfer type magnetic separation device according to claim 1, wherein the removal target substance adsorption surface is provided with irregularities.
【請求項7】 被除去物質吸着面にテフロン処理が行わ
れていることを特徴とする請求項1乃至5のうちのいず
れかに記載の磁場移動式磁気分離装置。
7. The magnetic field transfer type magnetic separation device according to claim 1, wherein a Teflon treatment is performed on the surface to be adsorbed of the substance to be removed.
【請求項8】 被除去物質吸着面に、強磁性体が断続し
て配置されていることを特徴とする請求項1乃至5のう
ちのいずれかに記載の磁場移動式磁気分離装置。
8. The magnetic field transfer type magnetic separation device according to claim 1, wherein a ferromagnetic substance is intermittently arranged on the surface of the substance to be removed to be adsorbed.
【請求項9】 磁気分離板は平板状に形成され、内装さ
れた磁界発生手段は、磁気分離板の互いに対向する面に
対称的に磁場を形成するものであることを特徴とする請
求項2乃至4のうちのいずれかに記載の磁場移動式磁気
分離装置。
9. The magnetic separation plate is formed in a flat plate shape, and the built-in magnetic field generating means symmetrically forms magnetic fields on the surfaces of the magnetic separation plate facing each other. 5. The magnetic field transfer type magnetic separation device according to any one of 1 to 4.
【請求項10】 水源から原水を汲みあげるポンプと、
汲みあげた原水を一時貯溜する原水貯槽と、該原水貯槽
の原水に磁性粉と凝集剤を混入する手段と、磁性粉と凝
集剤が混入された原水を撹拌して原水中に磁性凝集体を
生成し、前処理水とする手段と、該前処理水に含まれる
前記磁性凝集体を分離除去する磁気分離手段と、前記磁
性凝集体が分離除去された処理水を前記水源に還流させ
る手段と、を含んでなる水浄化装置において、磁気分離
手段が、請求項1乃至9のうちのいずれかに記載の磁場
移動式磁気分離装置を含んで構成されていることを特徴
とする水浄化装置。
10. A pump for pumping raw water from a water source,
A raw water storage tank for temporarily storing the pumped raw water, a means for mixing magnetic powder and a flocculant into the raw water in the raw water storage tank, and stirring the raw water mixed with the magnetic powder and a flocculant to form magnetic aggregates in the raw water. Means for producing and pretreating water, magnetic separating means for separating and removing the magnetic aggregates contained in the pretreated water, and means for refluxing the treated water from which the magnetic aggregates have been separated and removed to the water source. A water purification apparatus comprising: a magnetic field separation type magnetic separation apparatus according to any one of claims 1 to 9;
【請求項11】 磁気分離手段が、磁場移動式磁気分離
装置の後流側に配置された高勾配磁気フィルタを含んで
構成されていることを特徴とする請求項10に記載の水
浄化装置。
11. The water purifying apparatus according to claim 10, wherein the magnetic separating means includes a high gradient magnetic filter arranged on the downstream side of the magnetic field moving type magnetic separating apparatus.
JP7239583A 1995-09-19 1995-09-19 Magnetic field moving type magnetic separator Pending JPH0975775A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7239583A JPH0975775A (en) 1995-09-19 1995-09-19 Magnetic field moving type magnetic separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7239583A JPH0975775A (en) 1995-09-19 1995-09-19 Magnetic field moving type magnetic separator

Publications (1)

Publication Number Publication Date
JPH0975775A true JPH0975775A (en) 1997-03-25

Family

ID=17046953

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7239583A Pending JPH0975775A (en) 1995-09-19 1995-09-19 Magnetic field moving type magnetic separator

Country Status (1)

Country Link
JP (1) JPH0975775A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012511602A (en) * 2008-12-12 2012-05-24 ビーエーエスエフ ソシエタス・ヨーロピア Method for separating metal impurities
CN104209185A (en) * 2014-08-25 2014-12-17 湖南利洁生物化工有限公司 Magnetic material catalyst separating device and system
CN116586189A (en) * 2023-07-14 2023-08-15 济南绿霸农药有限公司 Impurity remover for abamectin water dispersible granule production

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012511602A (en) * 2008-12-12 2012-05-24 ビーエーエスエフ ソシエタス・ヨーロピア Method for separating metal impurities
CN104209185A (en) * 2014-08-25 2014-12-17 湖南利洁生物化工有限公司 Magnetic material catalyst separating device and system
CN104209185B (en) * 2014-08-25 2017-01-11 湖南利洁生物化工有限公司 Magnetic material catalyst separating device and system
CN116586189A (en) * 2023-07-14 2023-08-15 济南绿霸农药有限公司 Impurity remover for abamectin water dispersible granule production
CN116586189B (en) * 2023-07-14 2023-10-20 济南绿霸农药有限公司 Impurity remover for abamectin water dispersible granule production

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