JPH10192731A - Magnetic separator - Google Patents
Magnetic separatorInfo
- Publication number
- JPH10192731A JPH10192731A JP9005240A JP524097A JPH10192731A JP H10192731 A JPH10192731 A JP H10192731A JP 9005240 A JP9005240 A JP 9005240A JP 524097 A JP524097 A JP 524097A JP H10192731 A JPH10192731 A JP H10192731A
- Authority
- JP
- Japan
- Prior art keywords
- magnetic
- aggregate
- magnetic powder
- separated
- sludge
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
- C02F1/488—Treatment of water, waste water, or sewage with magnetic or electric fields for separation of magnetic materials, e.g. magnetic flocculation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、浄化装置に関し、
特に磁気分離により高速に分離したスラッジ中の磁性粉
の分離、脱水等を行う浄化装置の構造に関する。TECHNICAL FIELD The present invention relates to a purification device,
In particular, the present invention relates to a structure of a purification device for separating and dewatering magnetic powder in sludge separated at high speed by magnetic separation.
【0002】[0002]
【従来の技術】従来の磁気分離装置としては、例えば、
高勾配電磁フィルタに外部から印加する磁場発生装置と
しては、直流電源による電磁石を用いる。この構造は化
学工学、第45巻、第4号(1981年)第235頁か
ら239頁に記載されている。2. Description of the Related Art As a conventional magnetic separation device, for example,
As a magnetic field generator for externally applying a high gradient electromagnetic filter, an electromagnet using a DC power supply is used. This structure is described in Chemical Engineering, Vol. 45, No. 4, (1981), pp. 235-239.
【0003】また、磁気分離部洗浄スラッジの磁性粉回
収および脱水方法について、遠心分離方法による脱水工
程が特開昭60ー244390号公報に開示されてい
る。本公知例では、磁性凝集体から磁性粉を除去した後
に脱水処理を行う運転方法が記載されている。[0003] As for a method of collecting and dewatering magnetic powder from a washing sludge of a magnetic separation part, a dewatering step by a centrifugal separation method is disclosed in Japanese Patent Application Laid-Open No. 60-244390. In this known example, an operation method of performing a dehydration treatment after removing magnetic powder from a magnetic aggregate is described.
【0004】また、磁性凝集体からの磁性粉の他の回収
方法については、特開昭60−61979号公報に開示
されているが、本公知例では磁性凝集体を燃焼し、凝集
体内の藻類等の有機物を燃焼分解させるものである。Another method for recovering magnetic powder from magnetic aggregates is disclosed in Japanese Patent Application Laid-Open No. 60-61979, but in this known example, the magnetic aggregates are burned and the alga in the aggregates is burned. And the like to decompose and decompose organic substances.
【0005】[0005]
【発明が解決しようとする課題】ところで、特開昭60
−244390号公報では、磁性凝集体から磁性粉を除
去する方法として、洗浄スラッジを高磁場中に通すのみ
で、磁性粉が磁性凝集体から磁気力のみで剥離して捕集
分離できるとしている。しかし、実際その運転方法を再
現実施したが磁性凝集体から磁性粉のみが剥離する結果
が得られず、大部分の磁性粉が凝集体とともに磁場中か
ら流出した。これは、実施した凝集過程で、磁性凝集体
の強度を増すために高分子剤を添加したことも1つの要
因であるが、高磁場中に通すのみでは磁性凝集体中の磁
性粉を磁気力で吸引すると磁性粉周りの被除去物、凝集
剤、高分子剤も吸引され、磁性粉を選択的に剥離分離す
ることはできない。The problem to be solved by the present invention is disclosed in
Japanese Patent No. 244390 discloses that as a method of removing magnetic powder from a magnetic aggregate, the magnetic powder can be separated and collected from the magnetic aggregate only by a magnetic force only by passing the cleaning sludge through a high magnetic field. However, in practice, the operation method was reproduced, but no result was obtained in which only the magnetic powder was separated from the magnetic aggregate, and most of the magnetic powder flowed out of the magnetic field together with the aggregate. This is partly due to the fact that a polymer agent was added to increase the strength of the magnetic aggregate during the aggregating process, but the magnetic powder in the magnetic agglomerate was only magnetically driven by passing through a high magnetic field. When the suction is performed, the removal object, the coagulant, and the polymer agent around the magnetic powder are also sucked, and the magnetic powder cannot be selectively separated and separated.
【0006】また、特開昭60−61979号公報の方
法では、磁性粉に炭化物等が付着結合し、回収磁性粉の
純度が低下すると共に,有機物を堆肥化して有効利用す
ることが出来ない等の問題がある。Further, in the method disclosed in Japanese Patent Application Laid-Open No. 60-61979, carbides and the like adhere to and bind to the magnetic powder, thereby lowering the purity of the recovered magnetic powder and making it impossible to effectively use organic substances by composting. There is a problem.
【0007】ところで、近年、水処理装置の浄化処理量
の運転コスト低減化、磁気分離効率の向上が求められて
おり、その1つの方法は、磁性凝集体の強度を強くして
なおかつ磁気分離部磁気吸引力の増加すなわち磁場強度
を高め、磁性凝集体の捕捉力を強くして浄化の高速化で
あり、洗浄水と磁性凝集体が混合した分離スラッジから
の磁性粉の回収再利用、磁性粉分離後のスラッジの脱水
率の向上である。[0007] In recent years, there has been a demand for a reduction in the operating cost of the purification treatment amount of the water treatment apparatus and an improvement in the magnetic separation efficiency. One of the methods is to increase the strength of the magnetic aggregate and to increase the magnetic separation unit. Increased magnetic attraction force, that is, increased magnetic field strength, strengthened the capture power of magnetic aggregates, and speeded up purification.Recovered and reused magnetic powder from separation sludge mixed with washing water and magnetic aggregates, magnetic powder This is an improvement in the dewatering rate of the sludge after separation.
【0008】本発明の目的は、分離スラッジの磁性粉回
収効率を向上した、脱水処理効率を向上した浄化装置の
構造を提供することにある。An object of the present invention is to provide a structure of a purifying apparatus in which the efficiency of recovering magnetic powder from separated sludge is improved and the efficiency of dewatering treatment is improved.
【0009】[0009]
【課題を解決するための手段】上記目的は、磁気分離部
で磁気分離した磁性凝集体を磁気分離部から逆洗にて洗
浄した分離スラッジを、機械的せん断力を付加するとと
もに磁気分離部を有する装置に通して、大半の磁性粉を
回収し、その後再度残留スラッジに高分子剤付加したの
ち再フロック処理等を行ってまたは残留スラッジを直接
脱水用遠心分離機を通して磁性粉回収後の残留スラッジ
を脱水する。SUMMARY OF THE INVENTION It is an object of the present invention to provide a method for separating magnetically aggregated magnetically separated agglomerates from a magnetic separation unit by backwashing the separated sludge, applying mechanical shearing force to the magnetic separation units, and forming a magnetic separation unit. Most of the magnetic powder is recovered by passing through a device having the same, and then a polymer agent is added to the residual sludge again, and then the floc treatment is performed again, or the residual sludge is directly recovered from the magnetic powder through a centrifuge for dehydration. To dehydrate.
【0010】また、遠心分離機の後流側に乾燥、破砕、
磁性粉分離機を配置することにより、残りの磁性粉を回
収して磁性粉を放棄することなく再使用する。Also, drying, crushing,
By disposing a magnetic powder separator, the remaining magnetic powder is collected and reused without discarding the magnetic powder.
【0011】逆洗による分離スラッジを高速回転翼やへ
ら等で磁性凝集体に機械的に強いせん断力を与え、強度
の高い凝集体と磁性粉を分離することにより、磁性粉の
みを磁気分離手段で回収できる。また、遠心分離機の後
流側に乾燥、破砕手段を配置することにより、磁性粉は
乾燥した凝集体と分離でき、その後磁気分離手段で回収
することにより磁性粉をほぼ100%回収し磁性粉を放
棄することなく、再利用できる。The separation sludge by backwashing is mechanically applied to the magnetic aggregate by a high-speed rotor or a spatula to separate the magnetic powder from the high-strength aggregate by magnetically separating only the magnetic powder. Can be recovered. In addition, by disposing the drying and crushing means on the downstream side of the centrifugal separator, the magnetic powder can be separated from the dried aggregates. Can be reused without giving up.
【0012】更には、脱水処理した磁性凝集体を乾燥、
破砕して解体することにより、燃焼後に分離する場合に
比べ純度の高い磁性粉を分離回収でき、磁性粉以外の分
離物例えば、藻類を炭化せずに分離回収出来るので、分
離物を容易に堆肥化できる。Furthermore, the dehydrated magnetic aggregate is dried,
By crushing and dismantling, it is possible to separate and collect magnetic powder with a higher purity than when separating after burning, and to separate and collect segregates other than magnetic powder, such as algae, without carbonizing them. Can be
【0013】[0013]
【発明の実施の形態】まず、図4を用いて磁気分離装置
の基本的な処理フローを説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First, a basic processing flow of a magnetic separation apparatus will be described with reference to FIG.
【0014】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、この原水6に、薬剤調整装置7から四
酸酸化鉄の磁性粉とポリ塩化アルミニュウム等の凝集剤
を導管8を通じて加え、撹絆槽9でモータ10で回転す
る撹絆機11で撹絆し、磁性フロックを含む前処理水1
2を製造する。前処理水12は弁13を通じ導水管14
を通り磁気分離容器15内に流入する。The raw water in the reservoir 1 is passed through a filter 3 for removing large debris from the water pipe 2 and is pumped by a pump 4 into a raw water storage tank 5.
Is added to the raw water 6, and a magnetic powder of iron tetroxide and a coagulant such as polyaluminum chloride are added to the raw water 6 through a conduit 8, and a stirring machine 11 rotated by a motor 10 in a stirring tank 9. Pretreated water 1 containing magnetic floc
2 is manufactured. The pretreated water 12 is supplied through a valve 13 to a water pipe 14.
And flows into the magnetic separation container 15.
【0015】空心コイル16に直流電源装置17から直
流電源を流す。直流電流に比例した磁場が、円筒状の磁
気分離容器15内に発生し、磁場は通水用の多孔磁極1
8によって均一化され、鉄製のヨーク19で囲み、磁力
線の通路としてその漏洩の防止する。均一化された磁場
によって、高勾配磁気フィルタ20の磁性細線充填物を
磁化する。磁気分離容器15内の磁場は、磁化された磁
性細線充填物のために乱れを生じ、局部的に磁束の疎密
ができ、高磁場勾配となる部分が多数発生する。磁性フ
ロックを含んだ前処理水12を下方から上向流で送水す
ると、原水中の磁性フロックは充填物の磁性細線表面
に、大きな磁力で捕捉され、浄化された原水は処理水と
して弁21、導水管22を通り処理水槽23に一旦蓄え
られ、導水管24を通じて貯水池1に戻される。A DC power is supplied from the DC power supply 17 to the air-core coil 16. A magnetic field proportional to the direct current is generated in the cylindrical magnetic separation vessel 15, and the magnetic field is generated by the porous magnetic pole 1 for water flow.
8 and is surrounded by an iron yoke 19 to prevent leakage as a magnetic field line passage. The magnetic wire filling of the high gradient magnetic filter 20 is magnetized by the homogenized magnetic field. The magnetic field in the magnetic separation container 15 is disturbed by the magnetized magnetic fine wire filling, and the magnetic flux can be locally densified and dense, and many portions having a high magnetic field gradient are generated. When the pre-treated water 12 containing the magnetic flocs is supplied in an upward flow from below, the magnetic flocs in the raw water are captured by the magnetic fine wire surface of the filler with a large magnetic force, and the purified raw water is treated as the treated water by the valve 21, The water is temporarily stored in the treated water tank 23 through the water pipe 22, and returned to the reservoir 1 through the water pipe 24.
【0016】磁性フロックが一定量高勾配磁気フィルタ
20に捕捉された後、磁気分離の性能を回復させるため
に、フィルタの逆洗が行われる。逆洗は、先ず弁13を
閉じ前処理水12の送水を止める。次に、直流電源を切
り、磁場を無くした後高勾配磁気フィルタ20の上部か
ら弁21を通じて処理水を所定の量逆流させ弁25を開
く。また、この時、空気タンク26から弁27、導管2
8を通じて空気を供給しエヤーバブリングを行いながら
磁性細線表面に付着した磁性フロックを洗浄除去し、洗
浄水を逆洗処理水槽29に蓄える。この洗浄水は別途逆
洗処理水槽29から運び出され、埋め立て地等に廃棄さ
れたり、焼却される。After a certain amount of magnetic flocs have been captured by the high gradient magnetic filter 20, a backwash of the filter is performed to restore the performance of the magnetic separation. In the backwash, first, the valve 13 is closed, and the supply of the pretreated water 12 is stopped. Next, the DC power supply is turned off, the magnetic field is removed, and after a predetermined amount of treated water flows backward from the upper part of the high gradient magnetic filter 20 through the valve 21, the valve 25 is opened. At this time, the valve 27 and the conduit 2 are connected from the air tank 26.
Air is supplied through 8 to carry out air bubbling to wash and remove magnetic flocks adhering to the surface of the magnetic fine wire, and to store washing water in a back washing water tank 29. This washing water is separately carried out from the backwashing water tank 29, and is discarded or incinerated in a landfill.
【0017】この後、弁25、弁27を閉じ、再び空心
コイル16に直流電源装置17から直流電源を流し、弁
27を開いて磁気分離を再開する。本発明では、この逆
洗処理水槽に蓄えられた洗浄水から磁性粉のみを効率よ
く回収するようにしたものでその処理フローを図1を用
いて説明する。Thereafter, the valves 25 and 27 are closed, DC power is supplied from the DC power supply 17 to the air-core coil 16 again, and the valve 27 is opened to restart magnetic separation. In the present invention, only the magnetic powder is efficiently recovered from the washing water stored in the backwashing water tank, and the processing flow will be described with reference to FIG.
【0018】図1は本発明の一実施例の磁気分離装置の
処理フローを示したものである。FIG. 1 shows a processing flow of a magnetic separator according to one embodiment of the present invention.
【0019】被浄化水源例えば貯水池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、この原水に、薬剤調
整装置7から四三酸化鉄等の磁性粉とポリ塩化アルミニ
ュウム、硫化鉄等の凝集剤および凝集体のせん断強度を
増すために高分子ポリマ等の凝集強化剤等を加え、撹絆
槽9で撹絆し、磁性凝集体を含む前処理水を製造する。
前処理水は磁気分離器30で磁性凝集体を分離捕捉し、
浄化された原水は処理水槽23aに貯蔵され、その後、
ポンプ23bにより貯水池1に戻される。A source of water to be purified, for example, raw water from a reservoir 1 is temporarily stored in a raw water storage tank 5 by a pump 4 through a filter 3 for removing large debris from a water pipe 2, and the raw water is supplied from a chemical adjusting device 7 to ferric oxide or the like. Magnetic powder, a coagulant such as polyaluminum chloride, iron sulfide and the like, and a cohesion enhancer such as a polymer polymer for increasing the shear strength of the agglomerate. Produce pretreatment water.
The pretreatment water separates and captures magnetic aggregates in the magnetic separator 30,
The purified raw water is stored in the treated water tank 23a, and thereafter,
The water is returned to the reservoir 1 by the pump 23b.
【0020】磁気分離器30で捕捉された磁性凝集体
は、所定の周期で逆洗され磁性凝集体を含むその洗浄水
は逆洗処理水槽29に貯蔵される。磁気分離器30は複
数個例えば2個の磁気分離部30a、30bで構成され、
片方が逆洗時にもう片方は浄化運転を行い磁気分離器3
0では連続的に浄化運転を行う。The magnetic aggregate captured by the magnetic separator 30 is backwashed at a predetermined cycle, and the washing water containing the magnetic aggregate is stored in the backwash water tank 29. The magnetic separator 30 includes a plurality of, for example, two magnetic separating units 30a and 30b,
When one is backwashed, the other performs a cleaning operation and performs magnetic separation 3
At 0, the purifying operation is continuously performed.
【0021】逆洗処理水槽29内の洗浄水は磁性粉回収
装置31に導かれる。すなわち磁性凝集体に高速回転翼
や、平板とへらを組み合わせ平板上で相対的に回転する
へら等で磁性凝集体に機械的にせん断力を与える攪拌装
置31aに導かれ、磁性凝集体の高分子剤の結合力を断
ち切り磁性凝集体を細かく分解する。その後、永久磁石
等を配置した回転円盤で構成した磁性粉回収用磁気分離
装置31b部で磁性粉を分離回収し、回収した磁性粉は
薬剤調整装置7に戻し再利用する。また、磁性粉回収装
置は磁石を埋め込んだ平板と、へらに相対速度を与え、
攪拌装置31a、磁性粉回収用磁気分離装置31bを一
体で構成し、磁性凝集体を平板上に磁気力で保持しなが
ら、ゴム等の弾性の材料で作られたへらで磁性凝集体を
破壊しながら磁性粉のみを平板上に停留、分離し回転円
板上の一個所で磁性粉を掻き取り板で掻き取り再利用す
る構造でもよい。The washing water in the backwashing water tank 29 is led to a magnetic powder recovery unit 31. That is, the magnetic aggregate is guided to a stirrer 31a that mechanically applies a shearing force to the magnetic aggregate by a high-speed rotating blade or a spatula that combines a flat plate and a spatula and relatively rotates on the flat plate. It breaks the binding force of the agent and breaks down the magnetic aggregates. Thereafter, the magnetic powder is separated and collected by a magnetic powder collecting magnetic separation device 31b formed of a rotating disk on which permanent magnets and the like are arranged, and the collected magnetic powder is returned to the medicine adjusting device 7 for reuse. Also, the magnetic powder recovery device gives relative speed to the flat plate with the magnet embedded and the spatula,
The stirrer 31a and the magnetic separation device 31b for collecting magnetic powder are integrally formed, and the magnetic aggregate is destroyed by a spatula made of an elastic material such as rubber while holding the magnetic aggregate on a flat plate by magnetic force. Alternatively, the magnetic powder alone may be retained and separated on a flat plate, and the magnetic powder may be scraped off at a single point on the rotating disk by a scraping plate and reused.
【0022】図2に攪拌装置31aと磁性粉回収用磁気
分離装置31b部を示す。洗浄水は穴38から攪拌装置
31aに流入し、高速回転翼38で攪拌され、磁性凝集
体の高分子剤の結合力を断ち切り磁性凝集体を細かく分
解する。高速回転翼38はモータ39で駆動され、シャ
フト40は水密性を有した軸封部41で支持される。モ
ータ39は電源42に接続されている。FIG. 2 shows a stirring device 31a and a magnetic separation device 31b for collecting magnetic powder. The washing water flows into the stirrer 31a through the hole 38 and is stirred by the high-speed rotating blades 38 to break the binding force of the polymer of the magnetic aggregate to break down the magnetic aggregate finely. The high-speed rotor 38 is driven by a motor 39, and the shaft 40 is supported by a watertight shaft seal 41. The motor 39 is connected to a power supply 42.
【0023】攪拌された洗浄水は、磁性粉回収用磁気分
離装置31b部に流入する。洗浄水中の磁性粉は永久磁
石43をはめ込んだ回転円盤44の側を通過するとき、
永久磁石43の表面に吸引される。回転円盤44はモー
タ45で駆動され、シャフト46は水密性を有した軸封
部47で支持される。モータ45は電源48に接続され
ている。The stirred washing water flows into the magnetic separation device 31b for collecting magnetic powder. When the magnetic powder in the washing water passes by the side of the rotating disk 44 in which the permanent magnet 43 is fitted,
It is attracted to the surface of the permanent magnet 43. The rotating disk 44 is driven by a motor 45, and the shaft 46 is supported by a watertight shaft seal 47. The motor 45 is connected to a power supply 48.
【0024】永久磁石43の表面に吸引された磁性粉
は、回転円盤44の両サイドに配置した掻き取り用の樋
49で掻き取られ、掻き取られた磁性粉は出口50から
重力方向に流れ出口50から流出して回収され、再利用
される。磁性粉を取り除かれた洗浄水は出口51から流
出する。The magnetic powder attracted to the surface of the permanent magnet 43 is scraped by scraping gutters 49 arranged on both sides of the rotating disk 44, and the scraped magnetic powder flows from the outlet 50 in the direction of gravity. Outflow from the outlet 50 is collected and reused. The cleaning water from which the magnetic powder has been removed flows out of the outlet 51.
【0025】次に、磁性粉の他の回収装置の一実施例を
図3に示す。Next, one embodiment of another apparatus for collecting magnetic powder is shown in FIG.
【0026】攪拌装置31aと磁性粉回収用磁気分離装
置31b部は回収装置31abに一体化されており、洗
浄水は穴38から攪拌部に流入し、磁性凝集体は回転円
盤52にはめ込んだ永久磁石53の表面に吸引される。
回転円盤52に吸引された磁性凝集体は円盤と共に連れ
回り、硬質のゴム等で製作し回収装置31abに固定し
たヘラ54で強いせん断力を受け、高分子剤の結合力を
断ち切り磁性凝集体を細かく分解する。分解され磁性粉
のみは永久磁石53に吸引されて回転円盤52と共に連
れ回り、回転円盤44の両サイドに配置した掻き取り用
の樋49で掻き取られ、掻き取られた磁性粉は出口50
から重力方向に流れ出口50から流出して回収され、再
利用される。磁性粉を取り除かれた洗浄水は出口51か
ら流出する。ここで、ヘラ54は回転円盤52の円周回
転方向に複数段配置し磁性凝集体を複数回せん断力を与
えて、磁性粉の周りに付着した非磁性の凝集剤等をさら
に剥離し磁性粉の純度を上げるようにしても良い。The agitating device 31a and the magnetic separation device 31b for collecting magnetic powder are integrated into the collecting device 31ab. The washing water flows into the agitating section through the hole 38, and the magnetic aggregates are permanently inserted into the rotating disk 52. It is attracted to the surface of the magnet 53.
The magnetic aggregate sucked by the rotating disk 52 rotates together with the disk, receives a strong shearing force with a spatula 54 made of hard rubber or the like and fixed to the recovery device 31ab, cuts off the bonding force of the polymer agent, and removes the magnetic aggregate. Disintegrate finely. Only the magnetic powder that has been disassembled is attracted to the permanent magnet 53 and is entrained along with the rotating disk 52, and is scraped off by the scraping gutters 49 arranged on both sides of the rotating disk 44.
From the outlet 50 in the direction of gravity to be collected and reused. The cleaning water from which the magnetic powder has been removed flows out of the outlet 51. Here, the spatula 54 is arranged in a plurality of stages in the circumferential direction of rotation of the rotating disk 52, and applies a shearing force to the magnetic agglomerate a plurality of times to further peel off the non-magnetic aggregating agent and the like adhered around the magnetic powder. May be increased.
【0027】磁性粉を分離除去された洗浄水のスラッジ
は、薬剤調整装置31dで比重が1よりも大きな粒子、
例えば、砂の微粒子や消石灰微粒子と例えばポリ塩化ア
ルミニュウム、ポリ鉄等の凝集剤や高分子ポリマ等を再
投入し、混合槽31cで再凝集させ磁性粉の量が少なく
なった凝集体の密度を大きくし、遠心分離機31eで凝
集体を効率よく分離、脱水する。遠心分離機31eでス
ラッジを分離された水は貯水池1に戻すか、ポンプ4の
吸引側に戻す。The sludge of the washing water from which the magnetic powder has been separated and removed is a particle having a specific gravity larger than 1 in the chemical preparation device 31d,
For example, sand fine particles or slaked lime fine particles and a flocculant such as polyaluminum chloride and polyiron, a polymer polymer, and the like are re-charged, and the density of the flocculated material in which the amount of the magnetic powder is reduced by reaggregating in the mixing tank 31c is reduced. Then, the aggregate is efficiently separated and dehydrated by the centrifugal separator 31e. The water from which the sludge has been separated by the centrifugal separator 31e is returned to the reservoir 1 or to the suction side of the pump 4.
【0028】更には、脱水処理した凝集体を乾燥、破砕
して残りの磁性粉をさらに回収する事により、燃焼後に
分離する場合に比べ純度の高い磁性粉を分離回収でき、
磁性粉以外の分離物、例えば、藻類を炭化せずに分離回
収出来るので、分離物を容易に堆肥化できる。これによ
り、磁性粉のほぼ100%を回収し磁性粉を放棄するこ
となく、再利用できる。遠心分離機31eで、凝集体と
洗浄用水を分離し、更に磁性凝集体内に含まれた水分を
分離し、凝集体の含水量を大幅に低減し、その容積を大
幅に減少させる。磁気分離部で分離濃縮された凝集体
は、小容量のスラッジタンク32に貯蔵できる。Further, by drying and crushing the dehydrated aggregate, and further recovering the remaining magnetic powder, magnetic powder having a higher purity can be separated and recovered as compared with the case of separating after burning.
Separates other than magnetic powder, for example, algae can be separated and collected without carbonizing, so that the isolates can be easily composted. Thereby, almost 100% of the magnetic powder can be recovered and reused without discarding the magnetic powder. The centrifugal separator 31e separates the aggregate from the washing water, further separates the water contained in the magnetic aggregate, greatly reduces the water content of the aggregate, and significantly reduces its volume. The aggregate separated and concentrated in the magnetic separation unit can be stored in a small-capacity sludge tank 32.
【0029】スラッジタンク32内の凝集体は、例えば
油を燃料とする集塵機能を有した乾燥炉33のバーナー
で更に乾燥脱水され、加熱ガスは例えば活性炭等を充填
した脱臭器34を通り大気に放出される。粉砕機35で
微粒子に粉砕された後、炭化物等が付着していない残り
の磁性粉が、例えば永久磁石等の磁場を利用した磁性粉
分離器36で回収され、磁気分離用薬剤として再利用さ
れる。また、磁性粉を除去した後の分離物は堆肥処理槽
37で堆肥化され、肥料として利用される。The agglomerates in the sludge tank 32 are further dried and dehydrated by, for example, a burner of a drying furnace 33 having a dust collecting function using oil as a fuel, and the heated gas passes through a deodorizer 34 filled with, for example, activated carbon and the like to the atmosphere. Released. After being pulverized into fine particles by the pulverizer 35, the remaining magnetic powder to which no carbide or the like adheres is collected by a magnetic powder separator 36 using a magnetic field such as a permanent magnet, and is reused as a magnetic separation agent. You. The separated material from which the magnetic powder has been removed is composted in the composting tank 37 and used as fertilizer.
【0030】また、磁気分離器30を構成する空心コイ
ルを超電導コイルにすることにより、コイル発生磁場が
大きくなり、かつコイルを小型、軽量化できる。発生磁
場が大きくなることにより、高勾配磁気フィルタ20に
捕捉する磁性凝集体の吸着力が大きくなり、前処理水を
高速で流しても、磁性凝集体を捕捉できることになり、
処理速度を大きくして、高速浄化が可能となる。更に
は、コイルの消費電力が大幅に低減され、給電設備が小
型、軽量化される。この超電導コイルは液体ヘリウムや
液体窒素冷媒で冷却されても、機械式、電子式の冷凍機
で冷却されても、同様な効果が生じる。Further, by using a superconducting coil as the air-core coil constituting the magnetic separator 30, the coil-generated magnetic field can be increased, and the coil can be reduced in size and weight. By increasing the generated magnetic field, the adsorptive power of the magnetic aggregate to be captured by the high gradient magnetic filter 20 increases, and the magnetic aggregate can be captured even when the pretreated water flows at a high speed.
By increasing the processing speed, high-speed purification becomes possible. Furthermore, the power consumption of the coil is greatly reduced, and the power supply equipment is reduced in size and weight. The same effect is obtained whether the superconducting coil is cooled by a liquid helium or liquid nitrogen refrigerant or by a mechanical or electronic refrigerator.
【0031】このように本実施例によれば、逆洗による
分離スラッジを高速回転翼やへら等で磁性凝集体に機械
的にせん断力を与え、凝集体と磁性粉を分離することに
より、磁性粉のみを磁気分離手段で高効率で回収でき
る。また、遠心分離機の後流側に乾燥、破砕手段を配置
することにより、磁性粉は乾燥した凝集体と分離でき、
その後、磁気分離手段で回収することにより磁性粉をほ
ぼ100%回収し磁性粉を放棄することなく、再利用で
きる。As described above, according to the present embodiment, the separation sludge by the backwash is mechanically applied to the magnetic aggregate by a high-speed rotating blade or a spatula to separate the aggregate from the magnetic powder, thereby obtaining the magnetic powder. Only the powder can be recovered with high efficiency by the magnetic separation means. Also, by placing the drying and crushing means on the downstream side of the centrifuge, the magnetic powder can be separated from the dried aggregates,
Thereafter, the magnetic powder is recovered by the magnetic separation means, whereby the magnetic powder can be recovered almost 100%, and can be reused without discarding the magnetic powder.
【0032】また、本実施例では逆洗による分離スラッ
ジに水酸化ナトリウム等の化学薬品を加えることなくス
ラッジを分解できるので、逆洗水のpHを元に戻す中和
行程は必要ない。In this embodiment, since the sludge can be decomposed without adding a chemical such as sodium hydroxide to the sludge separated by the backwash, a neutralization step for returning the pH of the backwash water to the original state is not necessary.
【0033】以上、本発明による構成機器を全て地上に
配置しても、またスラッジタンクまでを第1の移動体、
残りの構成要素を第2の移動体叉は地上に配置しても、
更には、スラッジタンクまでを地下に、残りを地上側に
配置しても、同様な効果を生じる。As described above, even if all of the components according to the present invention are arranged on the ground, the first mobile unit up to the sludge tank,
Even if the remaining components are placed on the second mobile or on the ground,
Further, the same effect can be obtained even if the sludge tank is disposed underground and the rest is disposed above ground.
【0034】[0034]
【発明の効果】本発明によれば、逆洗による分離スラッ
ジを高速回転翼やへら等で磁性凝集体に機械的にせん断
力を与え、凝集体と磁性粉を分離することにより、磁性
粉のみを磁気分離手段で高効率で回収できる。According to the present invention, the separation sludge by backwashing is mechanically applied to the magnetic aggregate by a high-speed rotary blade or a spatula to separate the aggregate from the magnetic powder. Can be recovered with high efficiency by magnetic separation means.
【図1】 本発明の一実施例の磁気分離装置のフローを
説明する図。FIG. 1 is a diagram illustrating a flow of a magnetic separation device according to an embodiment of the present invention.
【図2】 本発明の一実施例の磁気分離装置の磁性粉回
収部の構造を説明する図。FIG. 2 is a view for explaining the structure of a magnetic powder recovery unit of the magnetic separation device according to one embodiment of the present invention.
【図3】 本発明の他の実施例の磁気分離装置の磁性粉
回収部の構造を説明する図。FIG. 3 is a view for explaining the structure of a magnetic powder recovery unit of a magnetic separation device according to another embodiment of the present invention.
【図4】 磁気分離装置の運転操作の基本フローを説明
する図。FIG. 4 is a diagram illustrating a basic flow of an operation operation of the magnetic separation device.
15…磁気分離容器、20a,20b…高勾配磁気フィル
タ、31…磁性粉回収装置、31a…攪拌装置、31b
…磁性粉回収用磁気分離装置、38…高速回転翼、44
…回転円盤、49…掻き取り用の樋、54…ヘラ。15: magnetic separation container, 20a, 20b: high gradient magnetic filter, 31: magnetic powder recovery device, 31a: stirring device, 31b
... Magnetic separator for collecting magnetic powder, 38 ... High-speed rotor, 44
... a rotating disk, 49 ... a gutter for scraping, 54 ... a spatula.
Claims (3)
記磁気吸着手段で原水中に磁性物質と凝集剤を加え被除
去物質を含む磁性凝集体を形成し磁気的に吸着除去する
磁気分離装置において、 前記磁気吸着手段を複数備え、磁性凝集体を形成する第
1の磁気吸着手段と、前記磁性凝集体に機械的にせん断
力を加えて前記磁性凝集体から磁性物質を剥離させるせ
ん断力付加手段と、剥離された磁性物質を回収する第2
の磁気吸着手段と、前記第2の磁気吸着手段で磁性物質
を取り除かれたの残りの凝集体を脱水濃縮する脱水手段
とを備えたことを特徴とする磁気分離装置。1. A magnetic separation device comprising: a separation unit having a magnetic adsorbing means therein, wherein a magnetic substance and a coagulant are added to raw water to form a magnetic aggregate containing a substance to be removed and magnetically adsorbed and removed by the magnetic adsorption means An apparatus, comprising: a plurality of the magnetic attraction means; a first magnetic attraction means for forming a magnetic aggregate; and a shear force for mechanically applying a shear force to the magnetic aggregate to separate a magnetic substance from the magnetic aggregate. Second means for recovering the separated magnetic substance
And a dehydrating means for dehydrating and concentrating the remaining aggregates from which the magnetic substance has been removed by the second magnetic adsorbing means.
が、回転翼を有した攪拌装置であることを特徴とする磁
気分離装置。2. A magnetic separation apparatus according to claim 1, wherein said shearing force applying means is a stirrer having rotating blades.
加手段および前記第2の磁気吸着手段が、前記第2の磁
気吸着手段を内蔵した平板とこれに接触し、相対速度を
有する攪拌用回転翼および磁性粉回収用回転翼を有した
一体型装置であることを特徴とする磁気分離装置。3. A stirrer according to claim 1, wherein said shear force applying means and said second magnetic attraction means come into contact with a flat plate containing said second magnetic attraction means and have a relative speed. A magnetic separation device which is an integrated device having a rotor and a rotor for collecting magnetic powder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9005240A JPH10192731A (en) | 1997-01-16 | 1997-01-16 | Magnetic separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9005240A JPH10192731A (en) | 1997-01-16 | 1997-01-16 | Magnetic separator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10192731A true JPH10192731A (en) | 1998-07-28 |
Family
ID=11605685
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9005240A Pending JPH10192731A (en) | 1997-01-16 | 1997-01-16 | Magnetic separator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10192731A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100970689B1 (en) * | 2010-01-15 | 2010-07-15 | (주)에코원테크놀로지 | Waste water treatment process using the electromagnet powder |
JP2011121033A (en) * | 2009-12-14 | 2011-06-23 | Hitachi Plant Technologies Ltd | Magnetic separation apparatus and magnetic separation method, wastewater treatment apparatus, and wastewater treatment method |
CN110844982A (en) * | 2019-11-05 | 2020-02-28 | 北京航天斯达科技有限公司 | Flat plate type magnetic seed separation and recovery equipment and method |
CN113751194A (en) * | 2021-09-24 | 2021-12-07 | 井冈山大学 | Device for extracting magnetic biochar from soil |
CN118204194A (en) * | 2024-05-22 | 2024-06-18 | 山东安和磁电科技有限公司 | Permanent magnet wet magnetic separator |
-
1997
- 1997-01-16 JP JP9005240A patent/JPH10192731A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011121033A (en) * | 2009-12-14 | 2011-06-23 | Hitachi Plant Technologies Ltd | Magnetic separation apparatus and magnetic separation method, wastewater treatment apparatus, and wastewater treatment method |
KR100970689B1 (en) * | 2010-01-15 | 2010-07-15 | (주)에코원테크놀로지 | Waste water treatment process using the electromagnet powder |
CN110844982A (en) * | 2019-11-05 | 2020-02-28 | 北京航天斯达科技有限公司 | Flat plate type magnetic seed separation and recovery equipment and method |
CN113751194A (en) * | 2021-09-24 | 2021-12-07 | 井冈山大学 | Device for extracting magnetic biochar from soil |
CN113751194B (en) * | 2021-09-24 | 2024-01-26 | 井冈山大学 | Device for extracting magnetic biochar from soil |
CN118204194A (en) * | 2024-05-22 | 2024-06-18 | 山东安和磁电科技有限公司 | Permanent magnet wet magnetic separator |
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