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JPS5940508B2 - Separation method for suspended particles - Google Patents
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JPS5940508B2 - Separation method for suspended particles - Google Patents

Separation method for suspended particles

Info

Publication number
JPS5940508B2
JPS5940508B2 JP49070417A JP7041774A JPS5940508B2 JP S5940508 B2 JPS5940508 B2 JP S5940508B2 JP 49070417 A JP49070417 A JP 49070417A JP 7041774 A JP7041774 A JP 7041774A JP S5940508 B2 JPS5940508 B2 JP S5940508B2
Authority
JP
Japan
Prior art keywords
particles
suspension
ferromagnetic
fine particles
paramagnetic
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
Application number
JP49070417A
Other languages
Japanese (ja)
Other versions
JPS5164A (en
Inventor
俊郎 辻
克 金森
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.)
NEC Corp
Original Assignee
Nippon Electric 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 Nippon Electric Co Ltd filed Critical Nippon Electric Co Ltd
Priority to JP49070417A priority Critical patent/JPS5940508B2/en
Publication of JPS5164A publication Critical patent/JPS5164A/en
Publication of JPS5940508B2 publication Critical patent/JPS5940508B2/en
Expired legal-status Critical Current

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  • Water Treatment By Electricity Or Magnetism (AREA)

Description

【発明の詳細な説明】 本発明は強磁性微粒子または常磁性微粒子の分散された
懸濁液から微粒子を分離する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for separating microparticles from a dispersed suspension of ferromagnetic or paramagnetic microparticles.

従来、前記の微粒子を分離するためには、プレコート濾
過法、遠心分離法が主として用いられ、最近さらに直径
10μ程度のスチールウールを用い超伝導マグネットに
よる磁気分離法が提案されているが、これらの方法には
次のような欠点がある。
Conventionally, precoat filtration methods and centrifugation methods have been mainly used to separate the above-mentioned fine particles, and recently a magnetic separation method using superconducting magnets using steel wool with a diameter of about 10 μm has been proposed. The method has the following drawbacks:

まず濾過法については、懸濁液を大量に処理しようとす
る場合には大型の装置または長時間を要する。
First, regarding the filtration method, if a large amount of suspension is to be processed, large equipment or a long time is required.

微粒子の粒径が数+λ程度である場合には、これを濾別
する適当な濾材が無く濾過を行なうことができない。
When the particle size of the fine particles is approximately several +λ, filtration cannot be carried out because there is no suitable filter material to filter the fine particles.

さらに濾過中に濾材の目詰りが生じ保守がやっかいであ
る。
Furthermore, the filter medium becomes clogged during filtration, making maintenance difficult.

遠心分離法については、濾材を用いる脱水型では濾過法
と同様に粒径が数+λ程度になると適当な濾材が無く、
濾材の目詰まりが生じ保守がやっかいであるなどの欠点
がある。
Regarding the centrifugal separation method, in the dehydration type that uses a filter material, as with the filtration method, when the particle size becomes about several + λ, there is no suitable filter material.
There are drawbacks such as clogging of the filter media and troublesome maintenance.

一方デカンタ−型遠心分離法では、十分な分離を行なお
うとする時に処理速度が小さくなり、粒径が数+λ程度
になれば処理速度は著るしく小さくなる。
On the other hand, in the decanter type centrifugal separation method, the processing speed becomes low when sufficient separation is attempted, and the processing speed becomes significantly low when the particle size becomes approximately several +λ.

従って大量の懸濁液の処理に不適である。Therefore, it is unsuitable for processing large amounts of suspension.

第3番目のスチールウールを用いる磁気分離法について
は、やはり粒径が数+λ程度の微粒子は分離が困難であ
る。
Regarding the third magnetic separation method using steel wool, it is still difficult to separate fine particles with a particle size of several +λ.

本発明の目的は、粒径数+λ程度の強磁性または常磁性
の微粒子を連続的に分離除去することである。
An object of the present invention is to continuously separate and remove ferromagnetic or paramagnetic fine particles having a particle size of about +λ.

本発明の主な利用の対象はリン、イオウなどの水中の有
害物質の除去のために、補集剤として、強磁性、常磁性
の微粒子を水中に分散させ懸濁液とし、有害物質を微粒
子に吸着させる方法および水中の有害金属を微粒子内に
包含させる方法によって除去を行なう際、分散された微
粒子を液外に分離するプロセスである。
The main application of the present invention is to remove harmful substances in water such as phosphorus and sulfur by dispersing ferromagnetic and paramagnetic fine particles in water as a scavenger to form a suspension. This is a process in which the dispersed fine particles are separated from the liquid when removal is carried out by a method of adsorbing harmful metals in water or a method of incorporating harmful metals into fine particles.

本発明は、無機および有機の物質を吸着または含有した
強磁性微粒子または常磁性微粒子を懸濁液から分離除去
するにあたり、前記懸濁液に強磁性体粒子を分散させ、
磁場内に導き、該強磁性体粒子に微粒子を磁気的に付着
させた後、該強磁性体粒子と共に液外に除くことを特徴
とする微粒子の分離方法である。
In the present invention, when separating and removing ferromagnetic particles or paramagnetic particles adsorbing or containing inorganic and organic substances from a suspension, ferromagnetic particles are dispersed in the suspension,
This method of separating fine particles is characterized in that the fine particles are introduced into a magnetic field, the fine particles are magnetically attached to the ferromagnetic particles, and then the fine particles are removed from the liquid together with the ferromagnetic particles.

さらに詳しく述べれば、粒径数+λ程度の強磁性または
常磁性微粒子はこのまま、従来法による磁気分離によっ
て分離することは不可能であるが、懸濁液にあらかじめ
、粒径数百λ〜数千人の強磁性体粒子を添加した後、磁
場内に導けば、強磁性体粒子の磁化は飽和し、粒子付近
にはその粒子のMs(飽和磁化)程度の磁場ができ、そ
の磁場のおよぶ範囲は、その粒径程度であるから、極め
て大きい磁場勾配が得られ、前記微粒子は強磁性体粒子
に吸引付着される。
To be more specific, it is impossible to separate ferromagnetic or paramagnetic particles with particle diameters of several + λ as they are by magnetic separation using conventional methods, but particles with particle sizes of several hundred λ to several thousand λ are added to a suspension in advance. If human ferromagnetic particles are added and introduced into a magnetic field, the magnetization of the ferromagnetic particles will be saturated, and a magnetic field of about the Ms (saturation magnetization) of the particles will be created near the particles, and the range of that magnetic field will be Since the particle size is about that size, an extremely large magnetic field gradient is obtained, and the fine particles are attracted and adhered to the ferromagnetic particles.

微粒子を付着した強磁性体粒子は引き続き、他の方法に
よる分離装置によって集められ、系外に除かれる。
The ferromagnetic particles with fine particles attached thereto are subsequently collected by another separation device and removed from the system.

この段階での分離には、遠心分離法や、沈降法、あるい
はスチールウールなどによる磁気分離法などが利用でき
る。
For separation at this stage, centrifugation, sedimentation, magnetic separation using steel wool, etc. can be used.

懸濁液に対し、強磁性体粒子を加え、付着させる点が本
発明の主要な点であり、この方法と類似の方法であると
ころの、磁場内に強磁性粒子を詰めたフィルター状のも
の、板、膜、繊維上に強磁性体粒子を埋め込んだものを
設け、この中を懸濁液を通過させる方法は本発明の範囲
に含まれる。
The main point of the present invention is to add ferromagnetic particles to a suspension and make them adhere to the suspension, and a similar method to this method is a filter-like filter filled with ferromagnetic particles in a magnetic field. The scope of the present invention includes a method in which a plate, membrane, or fiber in which ferromagnetic particles are embedded is provided and a suspension is passed through the plate, membrane, or fiber.

以下実施例により本発明を具体的に説明する。The present invention will be specifically explained below using Examples.

実施例 1 平均粒径50人のδ−Fe00H(フェリ磁性)粒子を
水に濃度0.19/13で分散させた懸濁液を図に示さ
れる磁気的分離装置を用いて分離を行なった。
Example 1 A suspension of δ-Fe00H (ferrimagnetic) particles having an average particle size of 50 particles dispersed in water at a concentration of 0.19/13 was separated using the magnetic separation device shown in the figure.

図中の1は20000eの磁場を発生させることのでき
る空芯コイル、2は懸濁液を流すパイプ、3はスチール
ウールを示す。
In the figure, 1 is an air-core coil capable of generating a magnetic field of 20,000 e, 2 is a pipe through which the suspension flows, and 3 is steel wool.

懸濁液をそのまま、この分離装置に流したところ、流出
液中の懸濁物の濃度は0.099/13であった。
When the suspension was directly passed through this separation device, the concentration of the suspension in the effluent was 0.099/13.

一方懸濁液に、平均粒径0.1μのマグネタイト粒子を
濃度1 g/lで加え、同様な磁気分離を行なったとこ
ろ、流出液中の懸濁物の濃度は0.02g/lとなった
On the other hand, when magnetite particles with an average particle size of 0.1μ were added to the suspension at a concentration of 1 g/l and similar magnetic separation was performed, the concentration of the suspended matter in the effluent was 0.02 g/l. Ta.

実施例 2 水銀を1oppmfiむ水に第1鉄イオンFe2+と、
第2鉄イオンFe3+をl:2の比になるように加え、
さらにアルカリを加え常温で攪拌し、マグネタイトの微
粒子を得た。
Example 2 Ferrous ion Fe2+ in water containing 1 oppmfi of mercury,
Add ferric ion Fe3+ in a ratio of l:2,
Furthermore, an alkali was added and the mixture was stirred at room temperature to obtain fine particles of magnetite.

反応後の液中の水銀の量は0.01ppnm下となり、
水銀はマグネタイトの結晶格子内に組み込まれ、含有さ
れている。
The amount of mercury in the solution after the reaction is less than 0.01 ppnm,
Mercury is incorporated and contained within the crystal lattice of magnetite.

生成したマグネタイト微粒子の平均粒径は100λ以下
であった。
The average particle diameter of the produced magnetite fine particles was 100λ or less.

マグネタイト微粒子の懸濁液を実施例1で用いた磁気的
分離装置を一相いて分離した。
A suspension of magnetite fine particles was separated using the magnetic separator used in Example 1 in one phase.

原懸濁液中のマグネタイトの量は500ppIllであ
り、一方分離操作後の流出液中のマグネタイト量は45
0p−であり、はとんど分離されていなかった。
The amount of magnetite in the original suspension was 500 ppIll, while the amount of magnetite in the effluent after the separation operation was 45 ppIll.
0p-, and was hardly separated.

原懸濁液に平均粒径0.1μのマグネタイト粒子を1g
/lの濃度で加えた後、磁気分離操作を行なったところ
流出液中のマグネタイトの総量は40ppmとなった。
Add 1g of magnetite particles with an average particle size of 0.1μ to the original suspension.
After adding the solution at a concentration of 1/l, a magnetic separation operation was performed, and the total amount of magnetite in the effluent was 40 ppm.

以上の実施例でも述べたように、本発明は液体中に懸濁
された強磁性および常磁性の微粒子を連続的に除去する
際、極めて有効である。
As described in the above examples, the present invention is extremely effective in continuously removing ferromagnetic and paramagnetic fine particles suspended in a liquid.

なお飽和磁化の小さい強磁性体粒子を用いる場合はより
低い磁場で飽和させることができる。
Note that when using ferromagnetic particles with low saturation magnetization, saturation can be achieved with a lower magnetic field.

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

図は本発明に用いる磁気的分離装置の一例を示し、図中
の1は空芯コイル、2は懸濁液を流すパイプ、3はスチ
ールウール、4は流量調製のための弁を示す。
The figure shows an example of a magnetic separation device used in the present invention, in which 1 is an air-core coil, 2 is a pipe through which a suspension flows, 3 is steel wool, and 4 is a valve for adjusting the flow rate.

Claims (1)

【特許請求の範囲】[Claims] 1 無機あるいは有機の物質を含有する液に強磁性体微
粒子または常磁性体微粒子を添加して上記物質を該微粒
子に吸着または含有せしめて懸濁液となす第一の段階と
、上記懸濁液に上記強磁性体微粒子または常磁性体微粒
子よりも粒径が大きい磁性体粒子を分散させる第二の段
階と、しかる後懸濁液を磁場内に導き、前記強磁性体粒
子に前記微粒子を磁気的に付着させた後、前記強磁性体
粒子と共に液外に除く段階とを有することを特徴とする
懸濁微粒子の分離方法。
1. A first step of adding ferromagnetic fine particles or paramagnetic fine particles to a liquid containing an inorganic or organic substance so that the substance is adsorbed or contained in the fine particles to form a suspension, and the above suspension. a second step of dispersing magnetic particles having a larger particle size than the ferromagnetic particles or paramagnetic particles; then, the suspension is introduced into a magnetic field, and the ferromagnetic particles are exposed to the magnetic particles; 1. A method for separating suspended fine particles, which comprises the step of removing the ferromagnetic particles from the liquid together with the ferromagnetic particles.
JP49070417A 1974-06-20 1974-06-20 Separation method for suspended particles Expired JPS5940508B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP49070417A JPS5940508B2 (en) 1974-06-20 1974-06-20 Separation method for suspended particles

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP49070417A JPS5940508B2 (en) 1974-06-20 1974-06-20 Separation method for suspended particles

Publications (2)

Publication Number Publication Date
JPS5164A JPS5164A (en) 1976-01-05
JPS5940508B2 true JPS5940508B2 (en) 1984-10-01

Family

ID=13430863

Family Applications (1)

Application Number Title Priority Date Filing Date
JP49070417A Expired JPS5940508B2 (en) 1974-06-20 1974-06-20 Separation method for suspended particles

Country Status (1)

Country Link
JP (1) JPS5940508B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3607320B2 (en) * 1994-09-02 2005-01-05 株式会社日立製作所 Method and apparatus for recovering solid phase in analysis using fine particles
JP6845538B2 (en) * 2016-11-22 2021-03-17 株式会社テッツコーポレーション Magnetite Ferromagnetic material Suspension fine particle removal equipment

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5017779B2 (en) * 1971-10-06 1975-06-24
JPS4920948A (en) * 1972-06-15 1974-02-23

Also Published As

Publication number Publication date
JPS5164A (en) 1976-01-05

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