JPS59139910A - Magnetic separation method - Google Patents

Magnetic separation method

Info

Publication number
JPS59139910A
JPS59139910A JP1254383A JP1254383A JPS59139910A JP S59139910 A JPS59139910 A JP S59139910A JP 1254383 A JP1254383 A JP 1254383A JP 1254383 A JP1254383 A JP 1254383A JP S59139910 A JPS59139910 A JP S59139910A
Authority
JP
Japan
Prior art keywords
magnetic
flocculant
magnetic separation
raw water
suspended substance
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.)
Granted
Application number
JP1254383A
Other languages
Japanese (ja)
Other versions
JPH0346182B2 (en
Inventor
Junichi Yano
純一 矢野
Noboru Ando
昇 安藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP1254383A priority Critical patent/JPS59139910A/en
Publication of JPS59139910A publication Critical patent/JPS59139910A/en
Publication of JPH0346182B2 publication Critical patent/JPH0346182B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C1/00Magnetic separation
    • B03C1/005Pretreatment specially adapted for magnetic separation
    • B03C1/01Pretreatment specially adapted for magnetic separation by addition of magnetic adjuvants

Abstract

PURPOSE:To efficiently and sufficiently separate and remove a non-magnetic suspended substance, in performing magnetic separation by adding a magnetic material and a flocculant in a liquid containing a non-magnetic suspended substance, by adding a magnetic material uniformly dispersed by ultrasonic waves. CONSTITUTION:Raw water containing a non-magnetic suspended substance is sent to an arranged pipe by a pump 14 while a dispersion 71 having magnetite powder particles uniformly dispersed therein by an ultrasonic oscillator 61 and a dilute solution 42 of a flocculant subjected to stirring treatment by a blade type stirrer 23 are added on the way of the arranged pipe by pumps 15, 16. In the next step, this liquid mixture is treated with an electromagnetic filter 52 to obtain treating water.

Description

【発明の詳細な説明】 本発明は磁気分離処理方法、更に詳しくは、液中の非磁
性懸濁物質を磁性体及び凝集剤等の存在下、共凝集して
磁性フロックとなした後にこれを磁気分肉11処理する
に当たり、超音波で均一分散せしめた磁性体を用いるこ
とによって、液中から該非磁性懸濁物質を効率的に且つ
充分に分離除去することかできる磁気分離処理方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a magnetic separation treatment method, more specifically, a method for coagulating non-magnetic suspended matter in a liquid into a magnetic floc in the presence of a magnetic substance, a coagulant, etc. The present invention relates to a magnetic separation treatment method in which non-magnetic suspended matter can be efficiently and sufficiently separated and removed from a liquid by using a magnetic substance uniformly dispersed by ultrasonic waves in the magnetic separation process.

都市下水、産業排水、各種の製造工程廃液更にはこれら
の活性汚泥処理水等の液中には有機系又は無機系の非磁
性懸濁物質(以下、これを単にSSと略記する)が混在
していることが多い○これらはそのit環境へ放出する
と公害源となるため何らかの手段で処理される必要があ
る。
Organic or inorganic non-magnetic suspended substances (hereinafter simply abbreviated as SS) are mixed in urban sewage, industrial wastewater, waste liquids from various manufacturing processes, and activated sludge treated water. ○If these are released into the IT environment, they become a source of pollution, so they need to be disposed of by some means.

近年、かかるSSを含む液(以下、これを単に原水と略
記する)を処理するに磁気分離処理が行われている。こ
の場合の磁気分離処理は、原水中のSSを適尭な磁性体
及び凝集剤等の存在下に共凝集して磁気分離処理し得る
形態の磁性フロックとなし、しかる後にこれを磁気分離
するもので、代表的には例えば、磁気分離装置として電
磁フィルタか、また磁性体として強磁性体であるマグネ
タイトの粉粒が各々用いられている。
In recent years, magnetic separation processing has been used to treat liquids containing such SS (hereinafter simply referred to as raw water). In this case, the magnetic separation treatment involves co-agglomerating the SS in the raw water in the presence of an appropriate magnetic substance, coagulant, etc. to form magnetic flocs that can be subjected to magnetic separation treatment, and then magnetically separating the SS. Typically, for example, an electromagnetic filter is used as the magnetic separation device, and powder particles of magnetite, which is a ferromagnetic material, are used as the magnetic material.

ところが、このような場合にお゛ける従来の磁気分離処
理は一般に、羽根式攪拌機等で機械的に攪拌して得た磁
性体粉粒の攪拌混合液を原水に投入し、凝集剤を加え、
該原水中のSSを磁性体粉粒とともに共凝集して磁性フ
ロックとなし、しかる後にこれを磁気分離装置へ供する
方法であるが、実際上、かかる従来法によると処理水中
に依然として無視できない程度のSSが浮遊していて、
特にSSの除去か質的及び量的に極めて高度に要求され
る今日においてはなお充分といえず、磁気分離処理によ
るSSのより効率的なそしてより充分な分離除去が望寸
れているのである。
However, conventional magnetic separation treatment in such cases generally involves adding a stirred mixture of magnetic powder particles obtained by mechanically stirring with a blade stirrer to raw water, adding a flocculant,
This method involves co-agglomerating the SS in the raw water with magnetic powder particles to form magnetic flocs, which are then sent to a magnetic separator, but in practice, according to this conventional method, there is still a non-negligible amount of particles in the treated water. SS is floating,
Particularly in today's world, where removal of SS is extremely demanding both qualitatively and quantitatively, it is still not sufficient, and there is a high demand for more efficient and sufficient separation and removal of SS by magnetic separation treatment. .

本発明は、叙上の如き観点において、原水中のSSを効
率的に且つ充分に分離除去することができる磁気分離処
理方法を提供するものである。
In view of the above, the present invention provides a magnetic separation treatment method that can efficiently and sufficiently separate and remove SS in raw water.

以下、磁気分離装置として電磁フィルタを、壕/こ磁性
体としてマクネタイト粉粒を各々例にとり、図面に基つ
いて従来法と比較しつつ本発明の構成を詳細に説明する
Hereinafter, the structure of the present invention will be explained in detail by using an electromagnetic filter as a magnetic separation device and macnetite powder as an example of the groove/magnetic material, while comparing with a conventional method based on the drawings.

第1図は従来法の処理手順を例示する概略系統図である
。原水をポンプ11で送液する配管途中において、羽根
式攪拌機セ機21によるマグネタイト粉粒の攪拌混合液
31及び羽根式攪拌機22に」=る凝集剤の希釈溶解液
41が各々ポンプ12.13て加えられ、次いて電磁フ
ィルタ51に供されて、処理水が得られている。電磁フ
ィルタ51ては、凝集剤により共凝集したSSとマグネ
タイト粉粒との磁性フロックが捕捉蓄積され、これらは
例えば−、時間の連続処理後に常法の逆洗で系夕1へ排
出される。
FIG. 1 is a schematic system diagram illustrating the processing procedure of the conventional method. In the middle of the piping through which raw water is sent by the pump 11, a mixed liquid 31 of magnetite particles stirred by the blade-type stirrer 21 and a diluted solution 41 of the coagulant are pumped to the blade-type stirrer 22, respectively. The treated water is then supplied to an electromagnetic filter 51 to obtain treated water. The electromagnetic filter 51 captures and accumulates magnetic flocs of SS and magnetite powder coagulated by the coagulant, and these are discharged to the system 1 by conventional backwashing after continuous treatment for, for example, several hours.

かかる従来法には、図面で例示する場合の他に、別途、
原水とマクネタイト粉粒との混合槽や、凝集剤による共
凝集槽等を設けたり、また原水にマグネタイト粉粒と凝
集剤とを同時に加える場合等もあるが、いずれの方法で
も実際に磁気分離処理すると、処理水中に依然として無
視できない程度のSSが浮遊してくるのである。
In addition to the examples shown in the drawings, such conventional methods include
In some cases, a mixing tank for raw water and macnetite powder particles, a co-flocculation tank using a flocculant, etc. are installed, or magnetite powder particles and a flocculant are added to raw water at the same time, but either method actually requires magnetic separation treatment. As a result, a non-negligible amount of SS still floats in the treated water.

本発明者らは、この原因を追究すると、従来法では原水
中に投入するマグネタイト粉粒が一様な均一分散状態に
なく、マクネタイト粉粒相互間で凝集していて、マグネ
タイト粉粒の一つ一つが原水中のSSを吸着するような
状態になっていないため、該SS―、磁性フロックを形
成することなく凝集剤により単なるフロックの状態で電
磁フィルタに供給されるか、又は磁性フロックを形成し
たとしても、SSとマグネタイト粉粒との緊密度か弱い
磁性フロックのitで電磁フィルタに供給され、このよ
うなフロックのSSが電磁フィルタに捕捉されることな
く処理水中に同伴されてし捷うことが判った。
When the present inventors investigated the cause of this problem, they found that in the conventional method, the magnetite powder particles added to the raw water were not uniformly dispersed, and that some of the magnetite powder particles were agglomerated between each other. Since the SS is not in a state where it can adsorb SS in the raw water, the SS is either supplied to the electromagnetic filter in the form of flocs by the flocculant without forming magnetic flocs, or it forms magnetic flocs. Even if the SS and magnetite powder particles are not close together, the magnetic flocs may be supplied to the electromagnetic filter, and the SS of such flocs may not be captured by the electromagnetic filter and may be entrained in the treated water and shuffled. It turns out.

そこで本発明者らは、このような問題を解消するへく更
に鋭意イυ[究した結果、原水中に投入するマグネタイ
ト粉粒を予め超音波て液中分散さぜると、該マグイ・タ
イト粉粒ばあたかもその一つ一つがバラバラになった均
一分散状態となり、しかもその表面に付着していること
の多い塵埃等が同時に除去された活性状態となって、こ
のような状態のマグネタイト粉粒を原水に投入ずれは、
原水中のSSがマグネタイト粉粒のあたかも一つ一つに
効率的且つ緊密強固に吸着され、これらが凝集剤によっ
て磁性フロックを形成し、かかる磁性フロックか電磁フ
ィルタに確実に捕捉されることを見出し、本発明を完成
するに至った。
Therefore, the inventors of the present invention have made further efforts to solve this problem.As a result of their research, they found that if the magnetite powder to be added to raw water is dispersed in the liquid using ultrasonic waves, the magnetite particles Magnetite powder particles are in a uniformly dispersed state in which each particle is broken up into pieces, and at the same time, the dust, etc. that often adhere to the surface of the powder particles are removed, and the particles are in an activated state. The difference between adding the water to the raw water is
It was discovered that SS in raw water is efficiently, tightly and strongly adsorbed to each magnetite powder particle, and that these particles form magnetic flocs using a flocculant, and these magnetic flocs are reliably captured by an electromagnetic filter. , we have completed the present invention.

第2図と第3図とは本発明の各別の一実施例を示す(政
略系統図である。第2図の場合、原水をポンプ14て送
液する配管途中において、超音波発振器61によるマグ
イ・タイト粉粒の均一分散液71及び羽根式攪拌機23
による凝集剤の希釈溶解液42か各々ポンプ1.5.1
6で加えられ、次いで電磁フィルタ52に供されて、処
理水が得られている。第3図の」場合、原水をポンプ1
7て送液する配管途中において、羽根式攪拌機24によ
るマグネタイト粉粒の攪拌混合液32を超音波発振器6
2を備える分散容器8J内にて前述の如き均一分散液7
2としたもの及O・羽根式攪拌機25による凝集剤の希
釈溶解液43か各々ポンプ18.19で加えられ、次い
で電磁フィルタ53に供されて、処理水が得られている
2 and 3 show different embodiments of the present invention (political system diagrams. In the case of FIG. 2, an ultrasonic oscillator 61 Uniform dispersion of Maguitite powder 71 and blade stirrer 23
Dilute solution of flocculant by pump 42 or pump 1.5.1 respectively
6 and then subjected to an electromagnetic filter 52 to obtain treated water. In the case shown in Figure 3, the raw water is pumped 1
7, the stirred mixture 32 of magnetite powder particles is stirred by an ultrasonic oscillator 6 by a blade-type stirrer 24 in the middle of the pipe to which the liquid is sent.
A uniform dispersion liquid 7 as described above is prepared in a dispersion container 8J provided with
2 and a diluted solution 43 of the flocculant produced by the O/impeller stirrer 25 are added by pumps 18 and 19, respectively, and then passed through the electromagnetic filter 53 to obtain treated water.

図示した実施例はいずれも、マグネタイト粉粒を前述の
ことくあたかも一つ一つバラバラにし/こ活性状態の均
一分散液71.72として原水に力[1えており、電磁
フィルタ52.53で捕捉された磁性フロックの系外へ
の排出は従来法と同様逆洗による。
In all of the illustrated embodiments, the magnetite particles are broken up one by one as described above, and are applied to raw water as a homogeneous dispersion liquid 71,72 in an active state, and captured by an electromagnetic filter 52,53. The magnetic flocs are discharged from the system by backwashing as in the conventional method.

本発明において、マグネタイト粉粒は磁性体の、丑だ電
磁フィルタは磁気分離装置のそれぞれ代表例であり、既
によく知られている他の磁性体や磁気分離装置が使用さ
れ得る。そして凝集剤は、対象となる原水の性状に応じ
て適宜選択される1種又は2種以上のもので、通常アニ
オン系やノニオン系の高分子凝集剤等、例えばポリ塩化
アルミニウム、が使用され得る。
In the present invention, the magnetite powder particles are representative examples of a magnetic material, and the electromagnetic filter is representative examples of a magnetic separation device, and other well-known magnetic materials and magnetic separation devices may be used. The flocculant is one or more types selected as appropriate depending on the properties of the target raw water, and usually anionic or nonionic polymer flocculants, such as polyaluminum chloride, may be used. .

以上説明した本発明の効果をより具体的にするため、次
の第1表を例示する。表中、従来例は第1図に、実施例
1は第2図に、丑だ実施例2は第3図に、各々したかっ
て処理したものである○第1表 (米1:第2図において超音波発振器61を備えるタン
クの容量、従来例も同じ容量のタンクを使用した。米2
:第3図において超音波発振器62を備える分散容器8
1の容量0尚、処理水のSS濃度は繰り返しの連続処理
時における複数の71111定値の平均値。)第1表の
結果からも明らかなように、各実施例はいずれも、従来
例に比へて処理水中のSS濃度が著るしく低くなってお
り、使用したマグネタイト粉粒か超音波によって効率的
に且つ充分に機能していることか判る。
In order to make the effects of the present invention explained above more concrete, the following Table 1 is illustrated. In the table, the conventional example is shown in Figure 1, Example 1 is shown in Figure 2, and Ushida Example 2 is shown in Figure 3. The capacity of the tank equipped with the ultrasonic oscillator 61 was the same as that of the conventional example.
:Dispersion container 8 equipped with an ultrasonic oscillator 62 in FIG.
1 capacity: 0 Note that the SS concentration of the treated water is the average value of multiple 71111 constant values during repeated continuous treatments. ) As is clear from the results in Table 1, in each example, the SS concentration in the treated water was significantly lower than in the conventional example, and the efficiency was improved by the magnetite powder particles used and the ultrasonic waves. It can be seen that the system is functioning effectively and adequately.

本発明によると、磁気分離処理において原水中のSSを
より効率的且つ充分に分離除去することができ、従来法
において生しるマグネタイト粉粒のタンクや配管途中へ
のイ」着堆積現象もない。
According to the present invention, SS in raw water can be separated and removed more efficiently and sufficiently in the magnetic separation process, and there is no phenomenon in which magnetite particles are deposited in tanks or in the middle of piping, which occurs in conventional methods. .

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来法の処理手順を例示する概略系統図、第2
図と第3図とは本発明の各別の〜実施例を示す概略系統
図である。 11〜19   ポンプ、  21〜25・ 羽根式攪
拌機、31.32  攪拌混合液、41〜43  ・希
釈溶解液、51〜53   電磁フィルタ、 61.62  超音波発振器、 71.72  均一分散液、81  分散容器、特許出
願人   大同特殊鋼株式会社 代理人 弁理士 入 山 宏 正 第1図 第3図
Figure 1 is a schematic system diagram illustrating the processing procedure of the conventional method;
3 and 3 are schematic system diagrams showing different embodiments of the present invention. 11-19 Pump, 21-25・Blade type stirrer, 31.32 Stirring mixed liquid, 41-43・Diluted solution, 51-53 Electromagnetic filter, 61.62 Ultrasonic oscillator, 71.72 Uniform dispersion liquid, 81 Dispersion Container, Patent Applicant Daido Steel Co., Ltd. Agent Patent Attorney Hiroshi Iriyama Figure 1 Figure 3

Claims (1)

【特許請求の範囲】[Claims] 1 非磁性懸濁物質を含む液中に磁性体及び凝集剤等を
適宜に加えて該非磁性懸濁物質を磁性フロックとなした
後にこれを磁気分離処理するに蟲たり、超音波で均一分
散せし7めた磁性体を加えることを特徴とする磁気分肉
11理方法。
1. Add a magnetic substance, a flocculant, etc. to a liquid containing non-magnetic suspended matter as appropriate to make the non-magnetic suspended matter into a magnetic floc, and then perform magnetic separation treatment or uniformly disperse it using ultrasonic waves. 7. Magnetic separation method characterized by adding a magnetic substance.
JP1254383A 1983-01-27 1983-01-27 Magnetic separation method Granted JPS59139910A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1254383A JPS59139910A (en) 1983-01-27 1983-01-27 Magnetic separation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1254383A JPS59139910A (en) 1983-01-27 1983-01-27 Magnetic separation method

Publications (2)

Publication Number Publication Date
JPS59139910A true JPS59139910A (en) 1984-08-11
JPH0346182B2 JPH0346182B2 (en) 1991-07-15

Family

ID=11808246

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1254383A Granted JPS59139910A (en) 1983-01-27 1983-01-27 Magnetic separation method

Country Status (1)

Country Link
JP (1) JPS59139910A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62190466A (en) * 1985-12-20 1987-08-20 シンテツクス(ユ−・エス・エイ)インコ−ポレイテツド Method of separating particle
JPH0295594U (en) * 1988-07-27 1990-07-30
JPH0440248A (en) * 1990-06-01 1992-02-10 Fujita Corp Solid-liquid separating method
KR100918373B1 (en) 2008-12-01 2009-09-21 충남대학교산학협력단 Hybrid water treatment equipment and method using electromagnet and membrane
CN106391302A (en) * 2016-11-10 2017-02-15 江苏省冶金设计院有限公司 High-intensity magnetic disperse magnetic separation device and method for low-intensity magnetic separation tailings containing magnetic mica
CN110655290A (en) * 2019-09-26 2020-01-07 欧涛 Coal mine wastewater treatment method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62190466A (en) * 1985-12-20 1987-08-20 シンテツクス(ユ−・エス・エイ)インコ−ポレイテツド Method of separating particle
JPH0295594U (en) * 1988-07-27 1990-07-30
JPH0440248A (en) * 1990-06-01 1992-02-10 Fujita Corp Solid-liquid separating method
KR100918373B1 (en) 2008-12-01 2009-09-21 충남대학교산학협력단 Hybrid water treatment equipment and method using electromagnet and membrane
CN106391302A (en) * 2016-11-10 2017-02-15 江苏省冶金设计院有限公司 High-intensity magnetic disperse magnetic separation device and method for low-intensity magnetic separation tailings containing magnetic mica
CN110655290A (en) * 2019-09-26 2020-01-07 欧涛 Coal mine wastewater treatment method

Also Published As

Publication number Publication date
JPH0346182B2 (en) 1991-07-15

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