JP3334067B2 - Magnetic separation device and water treatment device with magnetic separation device - Google Patents

Magnetic separation device and water treatment device with magnetic separation device

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Publication number
JP3334067B2
JP3334067B2 JP23958295A JP23958295A JP3334067B2 JP 3334067 B2 JP3334067 B2 JP 3334067B2 JP 23958295 A JP23958295 A JP 23958295A JP 23958295 A JP23958295 A JP 23958295A JP 3334067 B2 JP3334067 B2 JP 3334067B2
Authority
JP
Japan
Prior art keywords
magnetic
water
magnetic separation
treated
separation unit
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 - Fee Related
Application number
JP23958295A
Other languages
Japanese (ja)
Other versions
JPH0975631A (en
Inventor
典英 佐保
尚志 磯上
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
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Filing date
Publication date
Application filed by Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP23958295A priority Critical patent/JP3334067B2/en
Priority to DE19637711A priority patent/DE19637711C2/en
Priority to US08/715,324 priority patent/US5944986A/en
Publication of JPH0975631A publication Critical patent/JPH0975631A/en
Application granted granted Critical
Publication of JP3334067B2 publication Critical patent/JP3334067B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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、磁気分離装置に係り、
特に高速で被処理液体から該液体中の浮遊固形物や、藻
類、菌類などの浮遊生物等の不要物を除去、浄化できる
磁気分離装置及び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,
In particular, the present invention relates to a magnetic separation device capable of removing and purifying unnecessary substances such as suspended solids in the liquid and floating organisms such as algae and fungi from the liquid to be treated at high speed, and a water purification device using the magnetic separation device.

【0002】[0002]

【従来の技術】従来、この種の固液分離技術を応用した
河川、貯水池等の原水や廃水等の水浄化装置としては、
磁気的吸引力を利用して、2段階の磁気分離工程を有し
た特開昭55ー132684号公報記載の磁気分離装置
が、また分離後の脱水濃縮方法としては、特開昭55ー
61979号公報記載の処理方法が、それぞれ提案され
ていた。
2. Description of the Related Art Conventionally, as a water purification device for raw water or wastewater of rivers and reservoirs to which this kind of solid-liquid separation technology is applied,
The magnetic separation apparatus described in JP-A-55-132684 having a two-stage magnetic separation step utilizing magnetic attraction is disclosed in JP-A-55-61979. Each of the processing methods described in the gazettes has been proposed.

【0003】[0003]

【発明が解決しようとする課題】特開昭55ー1326
84号公報に記載された装置では、廃水中の被処理物質
の多くが非磁性および反磁性物質である廃水に対し、廃
水中に予め強磁性の磁気種子を添加分散させ、上記廃水
中の被処理物質と磁気種子とを凝集剤等の作用で凝集さ
せ、上記被処理物質と磁気種子との磁性凝集体を磁気的
にろ過し、廃水中の被処理物質を廃水から分離する磁気
的処理方法が記載されている。ここで、この磁気的ろ過
手段として、第1段目で比較的大型の磁性凝集体を磁気
的に沈降させ、所定の保持時間内に沈降しえなかった比
較的微細な粒径の磁性凝集体を、第2段目で磁気的にろ
過し、処理水を得る方法を示している。
Problems to be Solved by the Invention JP-A-55-1326
In the apparatus described in Japanese Patent Publication No. 84, a ferromagnetic magnetic seed is added and dispersed in the wastewater in advance with respect to the wastewater in which most of the substances to be treated in the wastewater are non-magnetic and diamagnetic substances. A magnetic treatment method for aggregating a treated substance and a magnetic seed by the action of a coagulant or the like, magnetically filtering a magnetic aggregate of the treated substance and the magnetic seed, and separating a treated substance in wastewater from wastewater. Is described. Here, as the magnetic filtration means, a relatively large magnetic aggregate is magnetically settled in the first stage, and a magnetic aggregate having a relatively fine particle size that cannot be settled within a predetermined holding time is used. Is magnetically filtered at the second stage to obtain treated water.

【0004】この方法は、第2段目の磁気的ろ過装置を
強磁性のステンレスウール等の強磁性ろ過媒体を外部か
ら電磁石および永久磁石等の励磁媒体により励磁する高
勾配磁気フィルタ分離方式とし、強磁性ろ過媒体に磁性
凝集体がある程度蓄積したのち、浄化運転を一時停止
し、処理水を用いて強磁性ろ過媒体に蓄積した磁性凝集
体を洗浄脱離させる逆洗運転を行い、磁性凝集体を含む
逆洗水を洗浄水槽に一時蓄積する方法であるが、この逆
洗水は多くの処理水を含んでいる。したがって、逆洗水
から磁性凝集体を再度濃縮する工程が必要であるがその
処理方法については、記載されていない。また、第1段
目で沈降させた磁性凝集体の高速の処理方法に関しても
記載がなくこのままでは、逆洗水の処理までを含めた、
装置全体としての高速浄化運転を行なうにはどうすれば
良いか、明らかではない。
In this method, the second-stage magnetic filtration device is a high gradient magnetic filter separation system in which a ferromagnetic filtration medium such as ferromagnetic stainless wool is externally excited by an excitation medium such as an electromagnet and a permanent magnet. After a certain amount of magnetic aggregates have accumulated in the ferromagnetic filtration medium, the purification operation is temporarily stopped, and a backwash operation is performed in which the magnetic aggregates accumulated in the ferromagnetic filtration medium are washed and desorbed using treated water, and the magnetic aggregates are removed. Is a method of temporarily accumulating backwash water containing water in a wash water tank, but this backwash water contains a large amount of treated water. Therefore, a step of reconcentrating the magnetic aggregates from the backwash water is required, but the treatment method is not described. Further, there is no description about a high-speed treatment method for the magnetic aggregates settled in the first stage.
It is not clear how to perform a high-speed purification operation of the entire apparatus.

【0005】一方、特開昭55ー61979号公報に
は、高勾配磁気分離方式における逆洗後の磁性凝集体を
含む洗浄水の高速処理方法が開示されている。これは、
例えば永久磁石を円周上に配置した回転円盤を洗浄水槽
内に設置し、この永久磁石表面で直接磁性凝集体を洗浄
水から分離する、回転磁気分離装置を使用した方法であ
る。しかし、本公知例では、高勾配磁気分離器で全ての
磁性凝集体を捕捉蓄積するため、分離部が短期間に磁性
凝集体で閉塞し、逆洗運転周期が短くなり浄化運転の高
速化が阻害される欠点がある。また、原水中の磁性凝集
体の全てが逆洗洗浄水中に含まれるため、大量の磁性凝
集体を回転磁気分離装置で分離しなければならず、逆洗
水浄化の高速化が困難である。
On the other hand, Japanese Patent Application Laid-Open No. 55-61979 discloses a high-speed treatment method of washing water containing magnetic aggregates after backwashing in a high gradient magnetic separation system. this is,
For example, a method using a rotating magnetic separation device in which a rotating disk having permanent magnets arranged on a circumference is installed in a washing water tank, and magnetic aggregates are separated directly from the washing water on the surface of the permanent magnet. However, in this known example, since all the magnetic aggregates are captured and accumulated by the high gradient magnetic separator, the separation unit is closed by the magnetic aggregates in a short time, the backwashing operation cycle is shortened, and the purification operation is speeded up. There are drawbacks that are hindered. Also, since all of the magnetic aggregates in the raw water are contained in the backwash water, a large amount of magnetic aggregates must be separated by a rotating magnetic separation device, and it is difficult to speed up the purification of the backwash water.

【0006】しかしながら、近年、水処理装置の浄化処
理量の大容量化に伴い、磁気分離部の処理水の流速の高
速化と、連続的浄化および逆洗洗浄水の濃縮運転が必要
となっている。前記したように、高速化には磁気凝集体
をその大きさにより2段階で捕捉排除する磁気分離装置
が有利であるが、第1段目の磁気分離器は分離した大型
の磁性凝集体を連続的に流路から排除しなければならな
い。
[0006] However, in recent years, with the increase in the purification capacity of the water treatment apparatus, it has become necessary to increase the flow rate of the treated water in the magnetic separation unit, and to continuously purify and concentrate the backwash water. I have. As described above, a magnetic separator that captures and eliminates magnetic aggregates in two stages according to their size is advantageous for speeding up, but the first-stage magnetic separator continuously separates large magnetic aggregates. Must be excluded from the flow path.

【0007】また、逆洗洗浄水の濃縮までを含めた浄化
装置として高速化を図るためには、逆洗洗浄水からの磁
性凝集体の分離を高速化する必要がある。
[0007] Further, in order to increase the speed of the purifying apparatus including the concentration of the backwash water, it is necessary to speed up the separation of the magnetic aggregates from the backwash water.

【0008】本発明の目的は、磁気分離部の処理水の流
速の高速化と、逆洗のための浄化運転停止時間を短縮し
て浄化処理量を増加できる磁気分離装置を提供するにあ
る。
[0008] It is an object of the present invention to provide a magnetic separation apparatus capable of increasing the flow rate of treated water in a magnetic separation section and shortening the purification operation stop time for backwashing to increase the purification processing amount.

【0009】[0009]

【課題を解決するための手段】上記目的は、第1の手段
として、磁場発生用第1磁石の磁場内に磁性細線を充填
した高勾配磁気フィルタで被処理水中の磁性凝集体を吸
着捕捉する第1磁気分離部と、被処理水中を前記被処理
水と相対的に移動する第2磁性物体の磁場を利用して被
処理水中の磁性凝集体を吸着捕捉する第2磁気分離部と
を含んでなり、前記第2磁気分離部、前記被処理水の
浄化運転時の流れ方向において前記第1磁気分離部の上
流側に配置され、かつ、該第2磁気分離部吸着捕捉さ
れた前記磁性凝集体を連続的に除去する除去手段を備え
る磁気分離装置において、第2磁気分離部の被処理水出
側と第1磁気分離部の被処理水入り側を接続する配管
に、弁を介装した洗浄液出口配管を介して第3磁気分離
部を接続し、この第3磁気分離部を、前記洗浄液出口配
管を経て流入する逆洗水中を該逆洗水と相対的に移動す
る第3磁性物体の磁場を利用して前記逆洗水中の磁性凝
集体を連続的に吸着捕捉するものとするとともに、前記
第3磁性物体に吸着捕捉された前記磁性凝集体を連続的
に除去する除去手段を備えることにより達成される。
The first object of the present invention is to adsorb and capture magnetic aggregates in water to be treated by a high gradient magnetic filter in which a magnetic wire is filled in a magnetic field of a first magnet for generating a magnetic field. A first magnetic separation unit; and a second magnetic separation unit that adsorbs and captures magnetic aggregates in the water to be treated using a magnetic field of a second magnetic object that moves in the water to be treated relative to the water to be treated. in result, the second magnetic separation unit, wherein disposed upstream of said first magnetic separation unit in the flow direction during the cleaning operation of the water to be treated, and said the second magnetic separation portion is adsorbed captured Equipped with a removing means for continuously removing magnetic aggregates
Of the water to be treated in the second magnetic separation unit.
Connecting the side of the first magnetic separation unit with the water to be treated
, A third magnetic separation via a washing liquid outlet pipe with a valve
The third magnetic separation unit is connected to the washing liquid outlet.
Move the backwash water flowing through the pipe relative to the backwash water.
The magnetic flux in the backwash water using the magnetic field of the third magnetic object.
While continuously collecting and capturing the aggregates,
The magnetic agglomerates adsorbed and captured by the third magnetic object are continuously
This is achieved by providing a removing means for removing the water .

【0010】また、磁場発生用第1磁石の磁場内に磁性
細線を充填した高勾配磁気フィルタで被処理水中の磁性
凝集体を吸着捕捉する第1磁気分離部と、被処理水中を
前記被処理水と相対的に移動する第2磁性物体の磁場を
利用して被処理水中の磁性凝集体を吸着捕捉する第2磁
気分離部とを含んでなり、前記第2磁気分離部が、前記
被処理水の浄化運転時の流れ方向において前記第1磁気
分離部の上流側に配置され、かつ、該第2磁気分離部が
吸着捕捉された前記磁性凝集体を連続的に除去する除去
手段を備える磁気分離装置において、前記第2磁気分離
部の被処理水入り側に接続されて被処理水を供給する導
水管に弁を介装し、前記弁と前記第2磁気分離部の被処
理水入り側との間の導水管に、弁を介装した洗浄液出口
配管を介して前記第2磁気分離部を通過した逆洗水を収
容する処理水槽を接続し、この処理水槽はまた、前記第
1磁気分離部の被処理水出側に接続された導水管に、弁
を介して接続されるようにしてもよい。
[0010] The magnetic field generated by the first magnetic field generating magnet is
Magnetic properties of water to be treated by high gradient magnetic filter filled with fine wire
The first magnetic separation unit that adsorbs and captures aggregates and the water to be treated
The magnetic field of the second magnetic object that moves relatively to the water to be treated is
Magnetism to adsorb and capture magnetic aggregates in the water to be treated
And a second magnetic separation unit,
In the flow direction during the purification operation of the water to be treated, the first magnetic
The second magnetic separation unit is arranged on the upstream side of the separation unit, and
Removal for continuously removing the adsorbed and captured magnetic aggregates
A magnetic separation device comprising: a second magnetic separation device;
To supply the water to be treated
A valve is interposed in the water pipe, and the valve and the second magnetic separation unit are treated.
A cleaning liquid outlet with a valve installed in the water conduit between the water inlet side
Collect the backwash water that has passed through the second magnetic separation section via piping.
Connected to the treatment tank, and the treatment tank is also
(1) A valve is installed in the water pipe connected to the water discharge side of the magnetic separation unit.
May be connected via a .

【0011】[0011]

【0012】[0012]

【作用】磁気分離工程への前処理で形成される磁性凝集
体の大きさや磁性粉の含有量は一定ではなく、大型の磁
性凝集体ほど磁性粉の含有量が多く、磁気面への吸引力
が大きい。これらの大型の磁性凝集体は流速が大きな流
れの中でも第2磁気分離部の磁石面に吸着捕捉され、除
去手段により連続的に流路外に除去される。磁性粉の含
有量が少ない小型の磁性凝集体は第2磁気分離部の磁石
面に吸着捕捉されずに流れに乗って、第2磁気分離部の
後流側に配置した第1磁気分離部に流入し、その高勾配
磁気フィルタに捕捉される。これらの磁性凝集体の大半
は大型の磁性凝集体であり、第2磁気分離部が無い場合
に比べ、高勾配磁気フィルタに堆積する磁性凝集体の量
は半分以下に低減でき、逆洗周期も2倍以上長くなる。
したがって、逆洗周期を長く、つまり、逆洗のための浄
化運転停止時間を短縮することができ、浄化処理量を増
加できる。また、高勾配磁気フィルタに蓄積した小型の
磁性凝集体の量は原水中の磁性凝集体の総量に比べて除
去された大型の磁性凝集体の分だけ少ないので、洗浄水
からの磁性凝集体の分離を高速に行うことができる。
[Function] The size of magnetic agglomerates and the content of magnetic powder formed in the pretreatment to the magnetic separation step are not constant, and the larger the magnetic agglomerates, the greater the content of magnetic powder and the attractive force to the magnetic surface. Is big. These large magnetic aggregates are adsorbed and captured on the magnet surface of the second magnetic separation unit even in a flow having a high flow velocity, and are continuously removed from the flow path by the removing means. The small magnetic agglomerates having a low magnetic powder content ride on the flow without being adsorbed and trapped on the magnet surface of the second magnetic separation unit, and flow into the first magnetic separation unit disposed downstream of the second magnetic separation unit. And enters the high gradient magnetic filter. Most of these magnetic agglomerates are large magnetic agglomerates, and the amount of magnetic agglomerates deposited on the high gradient magnetic filter can be reduced to less than half compared to the case without the second magnetic separation part, and the backwashing cycle can be reduced. More than twice as long.
Therefore, the backwash cycle can be lengthened, that is, the purification operation stop time for backwash can be shortened, and the purification processing amount can be increased. In addition, the amount of small magnetic aggregates accumulated in the high gradient magnetic filter is smaller than the total amount of magnetic aggregates in the raw water by the amount of large magnetic aggregates removed. Separation can be performed at high speed.

【0013】洗浄水からの磁性凝集体の磁気分離を行な
う第3磁気分離部を設けると、第1磁気分離部の逆洗水
を一旦第3磁気分離部に貯溜し、逆洗終了後直ちに第
1、第2の磁気分離部を使用して浄化運転を再開するこ
とができる。そして、浄化運転と平行して一時貯溜され
た洗浄水中の磁性凝集体の磁気分離を第3磁気分離部で
行なうことにより、逆洗のための浄化運転停止時間を短
縮できる。
When a third magnetic separation unit for magnetically separating magnetic aggregates from the washing water is provided, the backwash water of the first magnetic separation unit is temporarily stored in the third magnetic separation unit, and the backwash water is immediately stored after the backwash. First, the purification operation can be restarted using the second magnetic separation unit. Then, by performing the magnetic separation of the magnetic aggregates in the wash water temporarily stored in parallel with the purification operation in the third magnetic separation unit, the purification operation stop time for backwashing can be reduced.

【0014】[0014]

【実施例】以下、本発明の第1の実施例を図1により説
明する。図示の水浄化装置は、貯水池1の水面下に一端
を開口しフィルタ3を介装した導水管2と、この導水管
2の他端に吸入側を接続したポンプ4と、このポンプ4
の吐出側に導水管2Aで接続された原水貯槽5と、この
原水貯槽5に導水管2Bで接続された磁気分離装置10
0と、磁気分離装置100に弁23を介装した導水管2
2で接続された処理水槽24と、一端を処理水槽24に
接続され他端を前記貯水池1に導かれた導水管25と、
磁気分離装置100に弁30を介装した空気管31で接
続された空気タンク29と、を含んで構成されている。
なお、水を流すためのポンプ、水頭差等については、記
載と説明を省略した。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of the present invention will be described below with reference to FIG. The illustrated water purification apparatus includes a water pipe 2 having one end opened below the water surface of a reservoir 1 and a filter 3 interposed therebetween, a pump 4 having a suction side connected to the other end of the water pipe 2, and a pump 4.
A raw water storage tank 5 connected to the discharge side of the raw water pipe 2A, and a magnetic separation device 10 connected to the raw water storage tank 5 by a water transmission pipe 2B.
0, the water pipe 2 with the valve 23 interposed in the magnetic separation device 100
A treatment water tank 24 connected at 2, a water guide pipe 25 having one end connected to the treatment water tank 24 and the other end guided to the reservoir 1;
And an air tank 29 connected to the magnetic separation device 100 by an air pipe 31 with a valve 30 interposed therebetween.
The description and description of a pump for flowing water, a head difference, and the like are omitted.

【0015】磁気分離装置100は、前記原水貯槽5に
導水管2Bで接続されモータ10で駆動される撹拌機1
1を有してなる撹拌槽9と、導水管2Bに導管8で接続
された薬剤調整装置7と、撹拌槽9に導水管13で接続
された第2磁気分離部110と、第2磁気分離部110
の被処理水出側に弁19を介装した導水管20で接続さ
れた第1磁気分離部21と、弁19と第1磁気分離部2
1の間の導水管20に弁27を介装した洗浄液出口配管
26で接続された第3磁気分離部120と、を含んで構
成されている。前記導水管22及び前記空気管31は、
第1磁気分離部21の処理水出側に接続されている。
A magnetic separator 100 is connected to the raw water storage tank 5 by a water pipe 2B and is driven by a motor 10
1, a medicine adjusting device 7 connected to the water pipe 2B by a conduit 8, a second magnetic separation unit 110 connected to the water tank 13 by a water pipe 13, and a second magnetic separation unit. Part 110
A first magnetic separation unit 21 connected to a water outlet side of the water treatment system by a water guide pipe 20 having a valve 19 interposed therebetween; a valve 19 and a first magnetic separation unit 2
And a third magnetic separation unit 120 connected to the water guide pipe 20 by a cleaning liquid outlet pipe 26 with a valve 27 interposed therebetween. The water pipe 22 and the air pipe 31 are:
The first magnetic separation unit 21 is connected to the treated water discharge side.

【0016】第1磁気分離部21は、磁場発生用第1磁
石と、その磁場内に配置され磁性細線を充填した高勾配
磁気フィルタを含んで形成され、被処理水がこの高勾配
磁気フィルタを通って流れるように構成されている。第
1磁気分離部21は、その高勾配磁気フィルタの逆洗処
理が可能なようにしてある。
The first magnetic separation section 21 is formed to include a first magnet for generating a magnetic field and a high gradient magnetic filter arranged in the magnetic field and filled with a magnetic fine wire, and the water to be treated is formed by the high gradient magnetic filter. It is configured to flow through. The first magnetic separation unit 21 is configured to enable backwashing of the high gradient magnetic filter.

【0017】第2磁気分離部110は、表面に永久磁石
円盤16Aが多数埋め込まれ回転軸をほぼ水平にして支
持された回転円盤15Aと、この回転円盤15Aを内装
し被処理水が流過する回転式磁気分離槽14Aと、回転
円盤15Aの表面吸着物(磁性凝集体)を削ぎ落すへら
17Aと、へら17Aで削ぎ落されたものが落下する位
置に配置されたスラッジ槽18Aと、を含んで構成され
ている。前記導水管13及び20は、回転式磁気分離槽
14Aに接続されている。また、回転円盤15Aは、そ
の下半部が回転式磁気分離槽14Aの水中にあり回転軸
が水面上に出るように配置され、かつへら17Aは、回
転円盤15Aに吸着した磁性凝集体を水面上で削ぎ落す
位置に配置されている。回転円盤15Aは、図示されて
いない駆動手段に依り所定の方向に連続的に回転され
る。
The second magnetic separation section 110 has a rotating disk 15A supported by a large number of permanent magnet disks 16A embedded on the surface and having a rotating axis substantially horizontal, and the rotating disk 15A is installed therein and water to be treated flows through the rotating disk 15A. It includes a rotary magnetic separation tank 14A, a spatula 17A for scraping off surface adsorbed matter (magnetic aggregates) of the rotating disk 15A, and a sludge tank 18A arranged at a position where the material scraped off by the spatula 17A falls. It is composed of The water pipes 13 and 20 are connected to a rotary magnetic separation tank 14A. The rotating disk 15A is disposed so that the lower half thereof is in the water of the rotary magnetic separation tank 14A and the rotation axis is above the water surface, and the spatula 17A disposes the magnetic aggregate adsorbed to the rotating disk 15A on the water surface. It is located at the position where it is scraped off. The rotating disk 15A is continuously rotated in a predetermined direction by driving means (not shown).

【0018】第3磁気分離部120は、表面に永久磁石
円盤16Bが多数埋め込まれ回転軸をほぼ水平にして支
持された回転円盤15Bと、この回転円盤15Bを内装
し逆洗水が一時貯溜される逆洗処理水槽14Bと、回転
円盤15Bの表面吸着物を削ぎ落すへら17Bと、へら
17Bで削ぎ落されたものが落下する位置に配置された
スラッジ槽18Bと、逆洗処理水槽14Bに接続された
導水管28と、を含んで構成されている。前記導水管2
6は、逆洗処理水槽14Bに接続されている。また、回
転円盤15Bは、その下半部が逆洗処理水槽14Bの水
中にあり回転軸が水面上に出るように配置され、かつへ
ら17Bは、回転円盤15Bに吸着した磁性凝集体を水
面上で削ぎ落す位置に配置されている。回転円盤15B
は、図示されていない回転駆動手段に依り所定の方向に
連続的に回転されるようになっている。
The third magnetic separating section 120 has a rotating disk 15B supported by a large number of permanent magnet disks 16B embedded on the surface and having a rotating shaft substantially horizontal, and the rotating disk 15B is installed therein and temporarily stores backwash water. To the backwashing water tank 14B, a spatula 17B for scraping off the surface adsorbed material of the rotating disk 15B, a sludge tank 18B arranged at a position where the material scraped off by the spatula 17B falls, and a backwashing water tank 14B. And a water guide pipe 28 that is formed. The water pipe 2
Reference numeral 6 is connected to the backwash water tank 14B. The rotating disk 15B is disposed such that the lower half thereof is in the water of the backwashing treatment tank 14B and the rotating shaft is above the water surface, and the spatula 17B disposes the magnetic aggregate adsorbed to the rotating disk 15B on the water surface. It is located at the position where it is shaved off. Rotating disk 15B
Are continuously rotated in a predetermined direction by rotation driving means (not shown).

【0019】次に上記構成の装置の動作を説明する。磁
性凝集体は具体的に以下の方法で作られる。水処理する
被処理水は、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の硫酸バン土やポリ塩化ア
ルミニュウムを加えて撹拌され、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
コロイド状で磁性を有した磁性凝集体となる。
Next, the operation of the apparatus having the above configuration will be described. The magnetic aggregate is specifically produced by the following method. The water to be treated for water treatment is added as a pretreatment to the magnetic separation step, for example, by adding a magnetic powder such as triiron tetroxide and bansulfate or polyaluminum chloride as an aggregating agent, and stirring the mixture. Algae, fungi, and microorganisms are combined with the magnetic powder by the flocculant to form colloidal magnetic aggregates.

【0020】貯水池1の被処理水の原水は導水管2を経
てポンプ4で吸い上げられ、大きなゴミを取るためのフ
ィルタ3を通して原水貯槽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で撹拌機11により撹拌され、磁性凝集体
を含む前処理水12となる。前処理水12は導水管13
を通り、回転式磁気分離槽14Aに流入する。回転式磁
気分離槽14A内では、回転円盤15Aがその下半部を
水面下にして連続的に回転している。回転円盤15Aの
表面には磁性物体、例えば永久磁石円盤16Aが多数埋
め込まれており、流入した前処理水12中の磁性粉を多
く含む磁性凝集体、主に大型の磁性凝集体は永久磁石円
盤16A表面に吸着、捕捉される。そして、捕捉された
磁性凝集体は、回転する回転円盤15Aの回転に伴って
液面上に移動し、再び液面下に沈む前に、へら17Aで
磁石面からはぎ取られスラッジ槽18A内に蓄えられ
る。前処理水12は、回転式磁気分離槽14Aの一端か
ら流入し、他端から導水管20に流出するが、回転式磁
気分離槽14A内の流れ方向は、回転円盤15Aの回転
と逆向きにして、回転円盤15Aの永久磁石円盤16A
が被処理水に対して相対的に移動するようにしてある。
The raw water to be treated in the reservoir 1 is sucked up by a pump 4 through a water pipe 2 and temporarily stored in a raw water storage tank 5 through a filter 3 for removing large dust. To the raw water 6, a magnetic powder of triiron tetroxide and a coagulant such as polyaluminum chloride are added from a chemical preparation device 7 through a conduit 8, and the mixture is stirred by a stirrer 11 in a stirring tank 9, and the pretreatment including the magnetic aggregates Water 12 Pretreatment water 12 is a water pipe 13
And flows into the rotary magnetic separation tank 14A. In the rotary magnetic separation tank 14A, the rotating disk 15A is continuously rotating with its lower half below the water surface. A large number of magnetic objects, for example, permanent magnet disks 16A are embedded on the surface of the rotating disk 15A, and a magnetic aggregate containing a large amount of magnetic powder in the inflowed pretreatment water 12, mainly a large magnetic aggregate, is a permanent magnet disk. Adsorbed and captured on 16A surface. Then, the captured magnetic aggregates move on the liquid surface with the rotation of the rotating rotating disk 15A, and are separated from the magnet surface by the spatula 17A and settled in the sludge tank 18A before sinking below the liquid surface again. It is stored. The pretreatment water 12 flows in from one end of the rotary magnetic separation tank 14A and flows out from the other end to the water guide tube 20, but the flow direction in the rotary magnetic separation tank 14A is set to be opposite to the rotation of the rotary disk 15A. And the permanent magnet disk 16A of the rotating disk 15A
Move relatively to the water to be treated.

【0021】大型の磁性凝集体が除去された前処理水1
2は弁19を通じ導水管20を通り、第1磁気分離部2
1の高勾配磁気フィルタに流入し、残りの磁性凝集体が
高勾配磁気フィルタで捕捉される。磁性凝集体が除去さ
れて浄化された原水は、処理水として、導水管22、弁
23を通って処理水槽24に一旦蓄えられ、送水手段を
なす導水管25を通じて貯水池1に戻される。
Pretreated water 1 from which large magnetic aggregates have been removed
2 passes through the water pipe 20 through the valve 19 and the first magnetic separation unit 2
One high gradient magnetic filter flows, and the remaining magnetic aggregates are captured by the high gradient magnetic filter. The raw water from which the magnetic aggregates have been removed and purified is temporarily stored as treated water in a treated water tank 24 through a water guide pipe 22 and a valve 23, and is returned to the reservoir 1 through a water guide pipe 25 serving as water supply means.

【0022】第1磁気分離部21の高勾配磁気フィルタ
は、磁性凝集体が吸着されるにつれて磁気分離性能が低
下していく。このため、磁性凝集体が一定量、高勾配磁
気フィルタに捕捉された後(あるいは、一定時間浄化運
転を行なった後、もしくは高勾配磁気フィルタ前後の差
圧が所定値を超えたら)、高勾配磁気フィルタの磁気分
離の性能を回復させるために、フィルタを洗浄する逆洗
が行われる。右側の磁気分離部は逆洗過程を示してい
る。逆洗は、先ず弁19を閉じて弁27を開き、磁場発
生用第1磁石を消磁する。次いで、弁23を通じて処理
水槽24の処理水を洗浄水として高勾配磁気フィルタに
所定の量逆流させ、高勾配磁気フィルタに捕捉されてい
た磁性凝集体を洗浄水とともに洗浄液出口配管26を経
て流出させ、洗浄水(逆洗水ともいう)を逆洗処理水槽
14Bに蓄える。この洗浄時、空気タンク29から弁3
0、空気管31を通じて空気を第1磁気分離部に供給し
エヤーバブリングを行い、よりよくフィルタから磁性凝
集体を除去する。
The magnetic separation performance of the high gradient magnetic filter of the first magnetic separation section 21 decreases as the magnetic aggregates are adsorbed. For this reason, after a certain amount of the magnetic aggregates are captured by the high gradient magnetic filter (or after performing the purifying operation for a certain period of time, or when the differential pressure before and after the high gradient magnetic filter exceeds a predetermined value), the high gradient In order to restore the performance of the magnetic separation of the magnetic filter, a backwash for cleaning the filter is performed. The magnetic separation section on the right shows the backwash process. In the backwash, first, the valve 19 is closed and the valve 27 is opened to demagnetize the first magnet for generating a magnetic field. Next, a predetermined amount of the treated water in the treated water tank 24 flows back through the valve 23 through the high gradient magnetic filter as cleaning water, and the magnetic aggregates captured by the high gradient magnetic filter are discharged together with the cleaning water through the cleaning liquid outlet pipe 26. Then, the washing water (also called backwashing water) is stored in the backwashing treatment water tank 14B. During this cleaning, the valve 3 is removed from the air tank 29.
0. Air is supplied to the first magnetic separation unit through the air pipe 31 to perform air bubbling, thereby removing magnetic aggregates from the filter better.

【0023】逆洗処理水槽14Bに内装された回転円盤
15Bには、磁性物体、例えば永久磁石円盤16Bが多
数埋め込まれており、洗浄水中の磁性粉を含む磁性凝集
体、主に小型の磁性凝集体の集合体は永久磁石円盤16
B表面に捕捉される。そして、永久磁石円盤16B表面
に捕捉された磁性凝集体は、回転円盤15Bの回転に伴
って液面上に移動し、再び水面下に沈む前に、へら17
Bで磁石面からはぎ取られスラッジ槽18B内に蓄えら
れる。磁性凝集体を分離した洗浄水は導水管28を通
り、水源に戻されるか洗浄用水として使用される。第2
磁気分離部110の磁気分離においては、前処理水12
は、回転式磁気分離槽14A内で一定方向の流れをなし
ているが、第3磁気分離部120での磁気分離において
は、洗浄水は、逆洗処理水槽14Bに貯溜され、静止し
ていて流れていない。
A large number of magnetic objects, for example, permanent magnet disks 16B, are embedded in a rotating disk 15B provided in the backwashing treatment tank 14B, and a magnetic aggregate containing magnetic powder in the washing water, mainly a small magnetic disk, is provided. The aggregate of the aggregate is a permanent magnet disk 16
Captured on the B surface. The magnetic agglomerates captured on the surface of the permanent magnet disk 16B move on the liquid surface with the rotation of the rotating disk 15B.
At B, it is stripped off from the magnet surface and stored in the sludge tank 18B. The washing water from which the magnetic aggregate has been separated passes through the water pipe 28 and is returned to the water source or used as washing water. Second
In the magnetic separation of the magnetic separation unit 110, the pretreated water 12
Flows in a fixed direction in the rotary magnetic separation tank 14A. However, in the magnetic separation in the third magnetic separation unit 120, the washing water is stored in the backwash treatment water tank 14B and is stationary. Not flowing.

【0024】このスラッジ槽18A、18B内の磁性凝
集体は、それぞれの槽から運び出され、脱水処理を行っ
た後、磁性粉を回収したり、埋め立て地等に廃棄された
り、焼却される。
The magnetic agglomerates in the sludge tanks 18A and 18B are carried out of the respective tanks and subjected to a dehydration treatment, after which magnetic powder is collected, discarded in a landfill, or incinerated.

【0025】逆洗後、弁27、弁30を閉じ、弁19を
開けて前処理水を磁気分離部21に満たし浄化運転が再
開される。同時に、逆洗処理水槽14Bに貯溜された洗
浄水の磁気分離が、第1磁気分離部、第2磁気分離部を
用いた浄化運転に平行して実行される。
After the backwash, the valves 27 and 30 are closed, and the valve 19 is opened to fill the magnetic separation section 21 with the pretreated water and the purification operation is resumed. At the same time, the magnetic separation of the wash water stored in the backwash water tank 14B is performed in parallel with the purification operation using the first magnetic separation unit and the second magnetic separation unit.

【0026】このように本実施例によれば、前処理水1
2中の磁性凝集体の大半は大型の磁性凝集体であり、そ
のほとんどは磁石回転方式の第2磁気分離部で連続的に
捕捉され連続的に除去される。したがって、高勾配磁気
フィルタに堆積する磁性凝集体の量は半分以下に低減で
き、逆洗周期も2倍以上に長くなる。このようにして、
本実施例では、逆洗周期をできるだけ長くして、かつ逆
洗時の洗浄水からの磁性凝集体の磁気分離と浄化運転を
平行してできるので、浄化処理量を増加できる。また、
逆洗水に含まれる磁性凝集体は、それぞれの磁性凝集体
が結合し大型化しているので、回転円盤15Bによる磁
気分離の効率も向上し、分離工程の高速化が可能とな
る。
As described above, according to the present embodiment, the pretreated water 1
Most of the magnetic aggregates in 2 are large magnetic aggregates, and most of them are continuously captured and continuously removed by the second magnetic separation unit of the magnet rotation type. Therefore, the amount of magnetic aggregates deposited on the high gradient magnetic filter can be reduced to half or less, and the backwashing cycle becomes twice or longer. In this way,
In the present embodiment, the backwashing cycle is made as long as possible, and the magnetic separation of the magnetic aggregates from the washing water during the backwashing and the purification operation can be performed in parallel, so that the purification treatment amount can be increased. Also,
Since the magnetic aggregates contained in the backwash water are combined with each other to increase in size, the efficiency of magnetic separation by the rotating disk 15B is also improved, and the speed of the separation process can be increased.

【0027】本発明になる第2の実施例を図2に示す。
本実施例が図1に示す実施例と異なる点は、回転式磁気
分離槽14を含む第2磁気分離部110を浄化運転時の
弁19の後流側、逆洗時の弁27の上流側に配置し、前
記第1の実施例における第3磁気分離部120の機能を
も第2磁気分離部110に行なわせた点にある。また、
本実施例では、弁27の下流側に第3磁気分離部120
に代えて処理水槽32を置き、処理水槽32を弁33を
介装した導水管34により第1磁気分離部21の出側の
導水管22に接続してある。
FIG. 2 shows a second embodiment according to the present invention.
This embodiment is different from the embodiment shown in FIG. 1 in that the second magnetic separation unit 110 including the rotary magnetic separation tank 14 is provided on the downstream side of the valve 19 during the cleaning operation and on the upstream side of the valve 27 during the backwash. And the function of the third magnetic separation unit 120 in the first embodiment is also performed by the second magnetic separation unit 110. Also,
In this embodiment, the third magnetic separation unit 120 is provided downstream of the valve 27.
Instead, a treated water tank 32 is placed, and the treated water tank 32 is connected to the outlet water pipe 22 of the first magnetic separation unit 21 by a water pipe 34 with a valve 33 interposed.

【0028】本実施例によれば、回転式磁気分離槽の設
置数が低減でき、装置の小型化が図られるとともに、逆
洗時の洗浄水の水量は浄化運転時に比べ十分小さく、す
なわち流速が遅く、かつ、フィルタに堆積した小型の磁
性凝集体は長時間高磁場内のフィルタに停留している
為、それぞれの磁性凝集体が結合し大型化し、逆洗時に
洗浄水中の磁性凝集体群を回転式磁気分離槽14で高い
確率で捕捉できる。したがって、逆洗水は磁性凝集体を
除去され、弁27を通り処理水槽32にいったん蓄えら
れ、貯水池1に戻されるか、または弁33、導水管34
を通じて逆洗用の水として使用される。なお、第1磁気
分離部21、第2磁気分離部110、処理水槽32、弁
19,27,33およびそれらを接続する導水管を含ん
で構成される分離逆洗ユニット35はモジュール化した
方が便利である。
According to the present embodiment, the number of rotary magnetic separation tanks can be reduced, the size of the apparatus can be reduced, and the amount of washing water during backwashing is sufficiently smaller than that during the purification operation. Since the small magnetic aggregates deposited on the filter are slow and stay in the filter in the high magnetic field for a long time, the respective magnetic aggregates are combined and become large, and the magnetic aggregates in the washing water are removed at the time of back washing. It can be captured with high probability in the rotary magnetic separation tank 14. Thus, the backwash water is freed of magnetic aggregates and stored once in the treatment tank 32 via the valve 27 and returned to the reservoir 1 or alternatively, the valve 33, the water pipe 34
Used as backwash water. The separation and backwashing unit 35 including the first magnetic separation unit 21, the second magnetic separation unit 110, the treatment water tank 32, the valves 19, 27, 33, and the water conduit connecting them should be modularized. It is convenient.

【0029】本発明になる第3の実施例を図3に示す。
本図が図2と異なる点は、分離逆洗ユニット35を複数
列、例えば35A、35Bの2個を並列に配置し、片方
例えば、分離逆洗ユニット35Aで浄化運転中は弁33
Aを開き、弁36Aを閉じる。このとき分離逆洗ユニッ
ト35Bは逆洗運転中で、弁33Bを閉じ、弁36Bを
開いている。本実施例によれば、分離逆洗ユニット35
A、35Bを切り替えて運転することにより浄化運転を
連続的に行うことができる効果がある。
FIG. 3 shows a third embodiment according to the present invention.
This drawing is different from FIG. 2 in that the separation backwashing unit 35 is arranged in a plurality of rows, for example, two units of 35A and 35B are arranged in parallel, and one of the separation backwashing units 35A is a valve 33 during the purification operation.
Open A and close valve 36A. At this time, the separation backwash unit 35B is performing the backwash operation, the valve 33B is closed, and the valve 36B is open. According to the present embodiment, the separation backwash unit 35
By switching between A and 35B for operation, there is an effect that the purification operation can be continuously performed.

【0030】なお、以上の本発明の実施例では、磁性物
体に永久磁石を使用した場合について述べたが、本磁性
物体が、電流を供給されて磁場を発生する常電導コイル
や超電導コイル、常電導コイルや超電導コイル等の外部
磁石の磁場により磁化される金属体であっても、同様な
効果が生じる。また、外部磁石が高勾配磁気分離器21
を構成する磁石であっても同様な効果が生じる。また、
本装置は船上、車上、地下等にも設置可能である。
In the above embodiment of the present invention, a case where a permanent magnet is used as a magnetic object has been described. However, the present magnetic object is supplied with a current to generate a magnetic field. The same effect is obtained even with a metal body magnetized by the magnetic field of an external magnet such as a conductive coil or a superconductive coil. The external magnet is a high gradient magnetic separator 21.
A similar effect is produced by the magnet constituting the above. Also,
This device can be installed on a ship, on a car, underground, and the like.

【0031】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(被除去物質)とは、先
に述べた固形浮遊物、藻類、菌類に限らず、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,金属イオン等を含むものである。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 above-mentioned raw water is water containing impurities such as rivers, dams, lakes and marshes, seawater, reservoirs, industrial wastewater, sewage, rainwater, and the like. Not only solid suspended solids, algae and fungi described above, but also objects such as organic matter, inorganic matter and microorganisms, metallic matter, non-metallic matter, soil, radioactive material, metal ions and the like. In particular, after adding divalent iron ions such as ferrous sulfate and alkali to raw water containing heavy metal ions to co-precipitate heavy metal ions with the precipitate of ferrous hydroxide, oxidize with air to precipitate the ferrite. Become The heavy metal can be magnetically separated by the ferrite formation. In this case, if the purpose is to separate only heavy metal ions, no coagulant is required. Therefore, in this case, ferrous sulfate, an alkali solution, and air may be injected into the raw water as a pretreatment, and the raw water may be treated in the stirring tank, and then the pretreatment water may be guided to the magnetic separation unit.

【0032】[0032]

【発明の効果】本発明によれば、単位時間に高勾配磁気
フィルタに堆積する磁性凝集体の量を低減できるので、
逆洗周期を長くでき、磁気分離装置の時間当りの平均浄
化処理量を増加することができる。
According to the present invention, the amount of magnetic aggregates deposited on a high gradient magnetic filter per unit time can be reduced.
The backwash cycle can be lengthened, and the average purification processing amount per time of the magnetic separation device can be increased.

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

【図1】本発明の第1の実施例の磁気分離装置の要部構
成を示す系統図である。
FIG. 1 is a system diagram showing a main configuration of a magnetic separation device according to a first embodiment of the present invention.

【図2】本発明の第2の実施例の磁気分離装置の要部構
成を示す系統図である。
FIG. 2 is a system diagram showing a main configuration of a magnetic separator according to a second embodiment of the present invention.

【図3】本発明の第3の実施例の磁気分離装置の要部構
成を示す系統図である。
FIG. 3 is a system diagram showing a main configuration of a magnetic separation device according to a third embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 貯水池 2,2A,2
B 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 導水管 14、14
A、 回転式磁気分離槽 14B 逆洗処理水槽 15,15
A,15B 回転円盤 16,16A、16B 永久磁石円盤、 17,17
A、17B へら 18,18A,18B スラッジ槽 19 弁 20 導水管 21 第1磁
気分離部 22 導水管 23 弁 24 処理水槽 25 導水管 26 洗浄液出口配管 27 弁 28 導水管 29 空気タ
ンク 30 弁 31 空気管 32 処理水槽 33,33
A,33B 弁 34 導水管 35,35A,35B 分離逆洗ユニット 36A,36B 弁 100 磁気
分離装置 110 第2磁気分離部 120 第3
磁気分離部
1 reservoir 2, 2A, 2
B water guide tube 3 filter 4 pump 5 raw water storage tank 6 raw water 7 chemical preparation device 8 conduit 9 stirring tank 10 motor 11 stirrer 12 pretreatment water 13 water guide pipe 14, 14
A, Rotary magnetic separation tank 14B Backwashing water tank 15,15
A, 15B Rotating disk 16, 16A, 16B Permanent magnet disk, 17, 17
A, 17B Spatula 18, 18A, 18B Sludge tank 19 Valve 20 Water pipe 21 First magnetic separation part 22 Water pipe 23 Valve 24 Treatment water tank 25 Water pipe 26 Cleaning liquid outlet pipe 27 Valve 28 Water pipe 29 Air tank 30 Valve 31 Air pipe 32 Treatment water tank 33, 33
A, 33B valve 34 water pipe 35, 35A, 35B separation backwashing unit 36A, 36B valve 100 magnetic separator 110 second magnetic separator 120 third
Magnetic separation unit

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平2−218493(JP,A) 特開 昭55−132684(JP,A) 特開 昭55−61979(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01D 35/06 B03C 1/00 - 1/32 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-2-218493 (JP, A) JP-A-55-132684 (JP, A) JP-A-55-61979 (JP, A) (58) Field (Int.Cl. 7 , DB name) B01D 35/06 B03C 1/00-1/32

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 磁場発生用第1磁石の磁場内に磁性細線
を充填した高勾配磁気フィルタで被処理水中の磁性凝集
体を吸着捕捉する第1磁気分離部と、被処理水中を前記
被処理水と相対的に移動する第2磁性物体の磁場を利用
して被処理水中の磁性凝集体を吸着捕捉する第2磁気分
離部とを含んでなり、前記第2磁気分離部が、前記被処
理水の浄化運転時の流れ方向において前記第1磁気分離
部の上流側に配置され、かつ、該第2磁気分離部が吸着
捕捉された前記磁性凝集体を連続的に除去する除去手段
を備える磁気分離装置において、第2磁気分離部の被処
理水出側と第1磁気分離部の被処理水入り側を接続する
配管に、弁を介装した洗浄液出口配管を介して第3磁気
分離部が接続され、この第3磁気分離部は、前記洗浄液
出口配管を経て流入する逆洗水中を該逆洗水と相対的に
移動する第3磁性物体の磁場を利用して前記逆洗水中の
磁性凝集体を連続的に吸着捕捉するものであるととも
に、前記第3磁性物体に吸着捕捉された前記磁性凝集体
を連続的に除去する除去手段を備えてなることを特徴と
する磁気分離装置。
A first magnetic separation unit for adsorbing and capturing magnetic aggregates in the water to be treated by a high gradient magnetic filter in which a magnetic thin wire is filled in a magnetic field of a first magnet for generating a magnetic field; A second magnetic separation unit for adsorbing and capturing magnetic aggregates in the water to be treated using a magnetic field of a second magnetic object relatively moving with water, wherein the second magnetic separation unit comprises A magnetic device comprising: a removing unit disposed upstream of the first magnetic separation unit in a flow direction during a water purification operation, wherein the second magnetic separation unit continuously removes the magnetic aggregate adsorbed and captured. In the separation device, a third magnetic separation unit is connected to a pipe connecting a water discharge side of the second magnetic separation unit and a water inlet side of the first magnetic separation unit through a cleaning liquid outlet pipe provided with a valve. Connected to the third magnetic separation section, and flows in through the cleaning liquid outlet pipe. A magnetic field of a third magnetic object that moves relatively to the backwash water, and continuously adsorbs and captures magnetic aggregates in the backwash water, and the third magnetic object A magnetic separation device comprising a removing means for continuously removing the magnetic aggregate adsorbed and captured on the magnetic separation device.
【請求項2】 磁場発生用第1磁石の磁場内に磁性細線
を充填した高勾配磁気フィルタで被処理水中の磁性凝集
体を吸着捕捉する第1磁気分離部と、被処理水中を前記
被処理水と相対的に移動する第2磁性物体の磁場を利用
して被処理水中の磁性凝集体を吸着捕捉する第2磁気分
離部とを含んでなり、前記第2磁気分離部が、前記被処
理水の浄化運転時の流れ方向において前記第1磁気分離
部の上流側に配置され、かつ、該第2磁気分離部が吸着
捕捉された前記磁性凝集体を連続的に除去する除去手段
を備える磁気分離装置において、前記第2磁気分離部の
被処理水入り側に接続されて被処理水を供給する導水管
に弁が介装され、前記弁と前記第2磁気分離部の被処理
水入り側との間の導水管に、弁を介装した洗浄液出口配
管を介して前記第2磁気分離部を通過した逆洗水を収容
する処理水槽が接続され、この処理水槽はまた、前記第
1磁気分離部の被処理水出側に接続された導水管に、弁
を介して接続されていることを特徴とする磁気分離装
置。
2. A first magnetic separation unit for adsorbing and capturing magnetic agglomerates in water to be treated by a high gradient magnetic filter filled with a magnetic wire in a magnetic field of a first magnet for generating a magnetic field, and the water to be treated is treated in the water to be treated. A second magnetic separation unit for adsorbing and capturing magnetic aggregates in the water to be treated using a magnetic field of a second magnetic object relatively moving with water, wherein the second magnetic separation unit comprises A magnetic device comprising: a removing unit disposed upstream of the first magnetic separation unit in a flow direction during a water purification operation, wherein the second magnetic separation unit continuously removes the magnetic aggregate adsorbed and captured. In the separation device, a valve is interposed in a water supply pipe connected to the second magnetic separation unit to supply the water to be treated and supplies the water to be treated, and the valve and the second magnetic separation unit are provided with the water to be treated. Through the washing liquid outlet pipe provided with a valve, A treated water tank containing the backwash water that has passed through the magnetic separation unit is connected, and the treated water tank is also connected via a valve to a water pipe connected to the treated water outlet side of the first magnetic separation unit. A magnetic separation device.
【請求項3】 被処理水を水源から汲みあげるポンプ手
段と、汲みあげられた被処理水を一時貯溜する原水貯槽
と、該原水貯槽に貯溜された被処理水に含まれる固形浮
遊物及び藻類、菌類からなる浮遊生物を磁性凝集体とし
て磁気分離する磁気分離装置と、該磁気分離装置に接続
して設けられ磁性凝集体が分離された処理水を一時貯溜
する処理水槽と、該処理水槽の処理水を前記水源に還流
させる送水手段と、を含んでなる水浄化装置において、
磁気分離装置が、請求項1または2に記載の装置である
ことを特徴とする磁気分離装置を備えた水浄化装置。
3. A pump means for pumping water to be treated from a water source, a raw water storage tank for temporarily storing the water to be pumped, solid suspended matter and algae contained in the water to be stored stored in the raw water storage tank. A magnetic separation device for magnetically separating suspended organisms composed of fungi as magnetic aggregates, a treatment water tank provided to be connected to the magnetic separation device and temporarily storing treated water from which the magnetic aggregates have been separated, and a treatment water tank. A water supply means for returning treated water to the water source,
A water purification device comprising a magnetic separation device, wherein the magnetic separation device is the device according to claim 1.
JP23958295A 1995-09-19 1995-09-19 Magnetic separation device and water treatment device with magnetic separation device Expired - Fee Related JP3334067B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP23958295A JP3334067B2 (en) 1995-09-19 1995-09-19 Magnetic separation device and water treatment device with magnetic separation device
DE19637711A DE19637711C2 (en) 1995-09-19 1996-09-16 Magnetic separator device and device for cleaning liquids
US08/715,324 US5944986A (en) 1995-09-19 1996-09-18 Liquid purification apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23958295A JP3334067B2 (en) 1995-09-19 1995-09-19 Magnetic separation device and water treatment device with magnetic separation device

Publications (2)

Publication Number Publication Date
JPH0975631A JPH0975631A (en) 1997-03-25
JP3334067B2 true JP3334067B2 (en) 2002-10-15

Family

ID=17046940

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23958295A Expired - Fee Related JP3334067B2 (en) 1995-09-19 1995-09-19 Magnetic separation device and water treatment device with magnetic separation device

Country Status (1)

Country Link
JP (1) JP3334067B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000254544A (en) * 1999-03-08 2000-09-19 Sumitomo Electric Ind Ltd Magnetic separation apparatus and method, and treatment of solid in raw water
JP5085052B2 (en) * 2005-06-08 2012-11-28 積水化学工業株式会社 Rainwater outflow control drainage channel structure
JP7235304B2 (en) * 2019-06-28 2023-03-08 有限会社アルファサービス Blue-green algae collection device
CN112209559A (en) * 2020-11-04 2021-01-12 中建环能科技股份有限公司 Wastewater treatment method, magnetic separation system and integrated magnetic separation device

Also Published As

Publication number Publication date
JPH0975631A (en) 1997-03-25

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