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JPS6236730B2 - - Google Patents
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JPS6236730B2 - - Google Patents

Info

Publication number
JPS6236730B2
JPS6236730B2 JP1936979A JP1936979A JPS6236730B2 JP S6236730 B2 JPS6236730 B2 JP S6236730B2 JP 1936979 A JP1936979 A JP 1936979A JP 1936979 A JP1936979 A JP 1936979A JP S6236730 B2 JPS6236730 B2 JP S6236730B2
Authority
JP
Japan
Prior art keywords
magnetic
particles
liquid
magnetic field
filter
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
JP1936979A
Other languages
Japanese (ja)
Other versions
JPS55111813A (en
Inventor
Yoshihiro Kenmoku
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 JP1936979A priority Critical patent/JPS55111813A/en
Publication of JPS55111813A publication Critical patent/JPS55111813A/en
Publication of JPS6236730B2 publication Critical patent/JPS6236730B2/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
    • B03C1/02Magnetic separation acting directly on the substance being separated
    • B03C1/025High gradient magnetic separators

Landscapes

  • Filtering Materials (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Description

【発明の詳細な説明】 本発明は液体あるいは気体などの流体中に分散
浮遊している磁性体粒子を捕集する磁気分離機に
関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a magnetic separator that collects magnetic particles dispersed and suspended in a fluid such as a liquid or gas.

従来液体中、気体中あるいは配管蒸気中などに
分散浮遊している磁性粒子を捕集するためのフイ
ルターとしては濾布や小さい穴径の金属網、ある
いは細線、細かい穴径の焼結金属など、いずれも
穴径が非常に小さい構造を有するフイルターによ
り磁性体粒子を機械的に除去しているのが大部分
である。しかし、かかる機械的な方法で微細な磁
性体粒子を除去するには、当然濾布や金属網、焼
結金属などの穴径を極端に小さくする必要があり
又細線を用いる場合には細線を極めて密に充填す
る必要がある。このようなフイルター構造では短
時間でフイルターの目詰まりを生じ、従つてフイ
ルターの洗篠や交換の頻度が多く、かつフイルタ
ーを洗篠するにしてもフイルターの目が細かすぎ
て洗篠が不十分であつたり、又困難な場合も多く
従つてフイルターを一度使用する毎に廃棄する場
合もあり非常に不経済である。さらにフイルター
の目が細かすぎるために流体の圧力損失が大きく
なり使用不可能な場合も多い。このような機械的
なフイルターの他に、たとえば磁気的な力を利用
して磁性粒子を捕集するフイルターの構造も従来
からいろいろ採用されており、例えば永久磁石を
内蔵したドラム式の分離機や、ステンレススチー
ルの細線を密に充填した構造のフイルターに電磁
石を用いて磁界を印加する構造のものなどがあ
る。ドラム式の場合は内蔵された永久磁石等によ
つてドラムの外周面付近に生ずる磁界と磁界勾配
を利用するタイプであるが磁界勾配も磁界も小さ
く、従つて微細な磁性体粒子を効果的に捕集する
ことが難かしく流体の流速が非常に小さい場合に
は多少の捕集効果はあるが気体中や配管中などの
磁性体粒子の捕集のためには適用できない。ま
た、ステンレススチールなどの細線を密に充填し
たフイルターの構造は最近各方面で注目されてい
るが、ほとんどが電磁石を利用したものであり、
電力の消費が大きく装置も大きくなる欠点があ
る。処理量を多くするためにフイルターの構造を
大きくする場合には電磁石の両極の間隔を広くす
る必要があり、広くした状態で大きな磁界を得る
ためには増々消費電力が大きくなり不経済であ
る。他方永久磁石を用いる場合でも両磁極面が接
近した場合ならその間に置いたステンレススチー
ルが磁化して磁性粒子を捕集できる場合もある
が、発生磁界が小さく捕集能力は電磁石による場
合より劣る。まして両磁極面の間隔を大きくする
につれて磁極の中間部分の磁界は著しく小さくな
り、磁性粒子の効果的な分離は困難となる。
Conventional filters for collecting magnetic particles dispersed and suspended in liquids, gases, or pipe steam include filter cloth, metal nets with small holes, thin wires, sintered metals with small holes, etc. In most cases, magnetic particles are mechanically removed using a filter having a structure with very small hole diameters. However, in order to remove minute magnetic particles using such mechanical methods, it is necessary to make the hole diameter of the filter cloth, metal mesh, sintered metal, etc. extremely small, and when using a thin wire, the diameter of the hole must be made extremely small. It is necessary to pack extremely densely. With this type of filter structure, the filter becomes clogged in a short period of time, so the filter has to be washed or replaced frequently, and even if the filter is washed, the mesh is too fine and the washing is insufficient. It is often difficult to do so, and the filter may have to be discarded after each use, which is very uneconomical. Furthermore, because the filter is too fine, the pressure loss of the fluid becomes large, and it is often impossible to use the filter. In addition to such mechanical filters, various filter structures have been used to collect magnetic particles using magnetic force, such as drum-type separators with built-in permanent magnets, and filters that collect magnetic particles using magnetic force. There are filters that use electromagnets to apply a magnetic field to a filter that is densely packed with thin stainless steel wires. The drum type uses the magnetic field and magnetic field gradient generated near the outer circumferential surface of the drum by built-in permanent magnets, etc., but the magnetic field gradient and magnetic field are small, so it is effective for capturing fine magnetic particles. Although it has some collection effect when it is difficult to collect and the flow velocity of the fluid is very low, it cannot be applied to collect magnetic particles in gases or pipes. In addition, the structure of filters densely packed with fine wires such as stainless steel has recently been attracting attention in various fields, but most of them utilize electromagnets.
The drawback is that power consumption is large and the device is also large. When increasing the size of the filter structure in order to increase the throughput, it is necessary to widen the spacing between the two poles of the electromagnet, and in order to obtain a large magnetic field with the spacing widened, power consumption increases, which is uneconomical. On the other hand, even when using a permanent magnet, if the two magnetic pole faces are close to each other, the stainless steel placed between them may become magnetized and be able to collect magnetic particles, but the generated magnetic field is small and the collection ability is inferior to that using an electromagnet. Furthermore, as the distance between the two magnetic pole faces increases, the magnetic field in the middle portion of the magnetic poles becomes significantly smaller, making it difficult to effectively separate the magnetic particles.

本発明の目的は構造的に簡単でしかも永久磁石
でも十分に使用可能でかつ従来の機械的フイルタ
ー、例えば焼結金属フイルターにくらべ圧力損失
を生じにくく長時間連続使用でき、消費電力が小
さく、磁性粒子の捕集効率が極めて高い構造を有
する磁気分離機を提供することにある。
The purpose of the present invention is to have a simple structure, which can be sufficiently used even with permanent magnets, which causes less pressure loss than conventional mechanical filters such as sintered metal filters, which can be used continuously for long periods of time, which has low power consumption, and which has magnetic properties. An object of the present invention is to provide a magnetic separator having a structure with extremely high particle collection efficiency.

本発明よる磁気分離機は磁性体微粒子を含有す
る液体や気体が複数個の簡単な形状の邪魔板に衝
突しながら通過し次に強磁性体の網などを通過す
る構造で、この構造のエレメントに対し、このエ
レメントの外部から磁界を与えることにより磁気
分離機が構成されている。このエレメントは通常
非磁性体の容器に収容される。磁性体微粒子を含
む液体や気体がこのような構造の磁気分離機に入
ると磁界中に置かれた邪魔板に衝突しつつ粒子同
志の衝突を繰り返し、さらに加えて磁界中での衝
突は磁性体粒子の磁気凝集を進め、単に邪魔板の
みで磁界が作用しない場合より十倍以上粒子の凝
集が速く進む結果を得る。このような粒子が次に
ステンレススチール(SUS410)などの磁性体細
線網を通過する際には永久磁石よる低磁界でも磁
気的に簡単に捕集される。この構造では永久磁石
(磁界3000G位)を用いても電磁石による10000G
以上の磁界中に置かれた細線による捕集効率と同
程度の性能をもつ磁気分離が得られる。と同時に
強磁性体細線などの充填率が数%と低くできるの
で圧力損失を起しにくい。次に本発明を図面に基
づいて実施例で詳細に説明する。
The magnetic separator according to the present invention has a structure in which liquid or gas containing magnetic fine particles collides with a plurality of simply shaped baffle plates and then passes through a ferromagnetic net. On the other hand, a magnetic separator is constructed by applying a magnetic field from outside of this element. This element is usually housed in a non-magnetic container. When a liquid or gas containing magnetic fine particles enters a magnetic separator with such a structure, it collides with a baffle plate placed in a magnetic field and the particles repeatedly collide with each other. The magnetic aggregation of the particles is promoted, and the aggregation of the particles progresses ten times faster than when the magnetic field does not act only with a baffle plate. When these particles then pass through a fine wire network made of magnetic material such as stainless steel (SUS410), they are easily captured magnetically even in a low magnetic field from a permanent magnet. With this structure, even if a permanent magnet (magnetic field of about 3000G) is used, the electromagnet's 10000G
Magnetic separation with performance comparable to the collection efficiency achieved by the thin wire placed in the magnetic field described above can be obtained. At the same time, the filling rate of thin ferromagnetic wires can be as low as a few percent, so pressure loss is less likely to occur. Next, the present invention will be explained in detail by way of examples based on the drawings.

実施例 1 第1図において非磁性体の容器1の入口部2か
ら磁性体粒子、実験ではマグネタイト(平均粒子
径約0.3μm)微粒子を含む液体が流入(液の流
れは線3で示す)することにより液体は液体の流
れとほぼ垂直な面を有する複数個の邪魔板4に衝
突し、流れが乱れ、同時に含有磁性体粒子同志が
衝突し凝集すると同時に、外部から磁石5(永久
磁石バリウムフエライト使用)により磁界として
約3000Gが印加されているので磁性体粒子同志は
さらに凝集が著しく進む。次に流れにそつて強磁
性体細線(ステンレススチールSUS4100.1mmφ)
網(充填率約5%)の固定層6を通過し、出口7
から流れ8として出ていく。この構造の磁気分離
機を用い、分散したマグネタイト(Fe3O4)粒子
(平均粒子径約0.3μm―含有マグネタイト量250
mg/)を含有する液体を50/Hrの流量で通過
させた。結果は0.5mg/のマグネタイトが流出し
た。この実施例で使用した原液と同じ性状の液を
0.1mmφステンレススチール(SUS410)を約5%
充填し電磁石で11000G(ガウス)の磁界を印加
した磁気分離機に50/Hrの液量で液を流したと
きの通過液中の流出マグネタイトは約0.65mg/
であり、本実施例の構造では同等の捕集効率を
3000G(ガウス)の低磁界で実現できた。また平
均穴径約10μmの焼結金属と比較して、本実施例
の磁気分離機は130時間、焼結金属フイルターは
15分で圧力損失を生じ液量が急激に減少した。
Example 1 In FIG. 1, a liquid containing magnetic particles (in the experiment, fine particles of magnetite (average particle diameter approximately 0.3 μm) flows in from the inlet 2 of a non-magnetic container 1 (the flow of the liquid is indicated by line 3). As a result, the liquid collides with a plurality of baffle plates 4 having surfaces almost perpendicular to the flow of the liquid, the flow is disturbed, and at the same time, the contained magnetic particles collide with each other and coagulate. Since a magnetic field of approximately 3000 G is applied (using the magnetic field), the magnetic particles significantly agglomerate together. Next, along the flow, ferromagnetic thin wire (stainless steel SUS4100.1mmφ)
It passes through a fixed bed 6 of a mesh (filling rate about 5%) and exits at an exit 7.
It exits as flow 8. Using a magnetic separator with this structure, dispersed magnetite (Fe 3 O 4 ) particles (average particle diameter approximately 0.3 μm - amount of magnetite contained 250
mg/) was passed through at a flow rate of 50/Hr. As a result, 0.5mg/magnetite leaked out. A liquid with the same properties as the stock solution used in this example was used.
Approximately 5% of 0.1mmφ stainless steel (SUS410)
When the liquid is poured at a flow rate of 50/Hr through a magnetic separator filled with a magnetic field of 11000G (Gauss) using an electromagnet, the amount of magnetite flowing out in the passing liquid is approximately 0.65mg/Hr.
Therefore, the structure of this example can achieve the same collection efficiency.
This was achieved using a magnetic field as low as 3000G (Gauss). Also, compared to sintered metal with an average hole diameter of about 10 μm, the magnetic separator of this example lasted 130 hours, and the sintered metal filter
After 15 minutes, a pressure loss occurred and the liquid volume decreased rapidly.

実施例 2 実施例1と異なるところは邪魔板の角度と磁性
粒子を含有する液体が実施例1が容器の下部に対
し、実施例2は容器の上部である。第2図におい
て非磁性体の容器11の入口部12からマグネタ
イト微粒子(平均粒子約0.3μm)を含む液体が
流入(液の流れを線13で示した)することによ
り液体は液の流速を速くするような角度に配置さ
れた6対の邪魔板14を通過し、次第に粒子が衝
突して凝集し、さらに磁界(磁石15により発生
する)の影響で凝集が促進され大きなフロツクに
なる。このフロツクになつた磁性体粒子は流れと
共に強磁性体細径16(ステンレススチール
SUS410,0.1mφ細線)網を通過する際に磁気的
に捕集され、きれいな液が出口部17を経て流れ
18として出ていく。いまこの構造の磁気分離機
を用い、マグネタイト(Fe3O4)粒子(平均粒子
径約0.3μm―含有マグネタイト量250mg/)が
分散している液を50/Hrで流した。その結果
0.35mg/のマグネタイトの流出をとなつた。こ
の実施例2で使用した原液と同じ性状の液を0.1
mmφのステンレススチール(SUS410)を約5%
充填し電磁石で13000G(ガウス)の磁界を印加
した磁気分離機に50/Hrの液量で流したときの
通過液中の流出マグネタイトは約0.3mg/であ
り、本実施例の構造では永久磁石による永久磁石
による3000G(ガウス)低磁界で上記の通り0.35
mg/となり本構造の優れていることが明らかに
なつた。また平均穴径約10μmの焼結金属と比較
して、本実施例の磁気分離機は約182時間、焼結
金属フイルターでは約15分で圧力損失を生じ液量
が急激に減少した。
Example 2 The difference from Example 1 is that the angle of the baffle plate and the liquid containing magnetic particles are in the lower part of the container in Example 1, whereas in Example 2 it is in the upper part of the container. In FIG. 2, a liquid containing fine magnetite particles (average particle size of about 0.3 μm) flows in from the inlet 12 of a non-magnetic container 11 (the flow of the liquid is shown by a line 13), causing the liquid to increase its flow rate. After passing through six pairs of baffle plates 14 arranged at such an angle, the particles gradually collide and aggregate, and the aggregation is further promoted by the influence of the magnetic field (generated by the magnet 15) to form a large floc. The magnetic particles that have become flocs flow together with the ferromagnetic material with a small diameter of 16 (stainless steel).
When passing through the SUS410, 0.1 mφ fine wire) net, it is magnetically collected, and the clean liquid exits as a flow 18 through the outlet section 17. Now, using a magnetic separator with this structure, a liquid containing dispersed magnetite (Fe 3 O 4 ) particles (average particle diameter of approximately 0.3 μm - amount of magnetite contained: 250 mg/hr) was flowed at a rate of 50/hr. the result
The outflow of 0.35mg/magnetite resulted. A solution with the same properties as the stock solution used in this Example 2 was added at 0.1
About 5% of mmφ stainless steel (SUS410)
When the liquid is filled at a flow rate of 50/hr through a magnetic separator to which a magnetic field of 13,000 G (Gauss) is applied using an electromagnet, the amount of magnetite released in the passing liquid is approximately 0.3 mg/hr. 0.35 as above at 3000G (Gauss) low magnetic field with permanent magnet
mg/, making it clear that this structure is superior. Furthermore, compared to the sintered metal with an average hole diameter of about 10 μm, the magnetic separator of this example caused a pressure loss in about 182 hours, and the sintered metal filter caused a pressure loss in about 15 minutes, causing a rapid decrease in liquid volume.

実施例1および2に対し、約100mg/のマグネ
タイトを含む空気を流しても本磁気分離機が優れ
ていることが明らかであつた。また邪魔板の形状
大きさは液量、含有磁性体量などによりいかなる
形状でもよい。
Compared to Examples 1 and 2, it was clear that the present magnetic separator was superior even when air containing about 100 mg/magnetite was flowed. Further, the shape and size of the baffle plate may be any shape depending on the amount of liquid, the amount of magnetic material contained, etc.

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

第1図および第2図は共に本発明による磁気分
離機を示すそれぞれ断面図である。 1,11……非磁性体の容器、2,12……入
口部、3,13……流れ、4,14……邪魔板、
5,15……磁石、6,16……強磁性体細線
網、7,17……出口、8,18……出口からの
流れである。
1 and 2 are sectional views, respectively, showing a magnetic separator according to the present invention. 1, 11... Container of non-magnetic material, 2, 12... Inlet part, 3, 13... Flow, 4, 14... Baffle plate,
5, 15... magnet, 6, 16... ferromagnetic thin wire mesh, 7, 17... outlet, 8, 18... flow from the outlet.

Claims (1)

【特許請求の範囲】[Claims] 1 磁性体微粒子を含有する流体の流れ方向に、
上記流体の流路を乱す手段と磁性材料から成る吸
着部とを配したことを特徴とする磁気分離機。
1 In the flow direction of the fluid containing magnetic particles,
A magnetic separator comprising means for disturbing the flow path of the fluid and an adsorption section made of a magnetic material.
JP1936979A 1979-02-21 1979-02-21 Magnetic separator Granted JPS55111813A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1936979A JPS55111813A (en) 1979-02-21 1979-02-21 Magnetic separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1936979A JPS55111813A (en) 1979-02-21 1979-02-21 Magnetic separator

Publications (2)

Publication Number Publication Date
JPS55111813A JPS55111813A (en) 1980-08-28
JPS6236730B2 true JPS6236730B2 (en) 1987-08-08

Family

ID=11997421

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1936979A Granted JPS55111813A (en) 1979-02-21 1979-02-21 Magnetic separator

Country Status (1)

Country Link
JP (1) JPS55111813A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3039171C2 (en) * 1980-10-16 1985-11-28 Siemens AG, 1000 Berlin und 8000 München Device for separating magnetizable particles according to the principle of high-gradient magnetic separation technology

Also Published As

Publication number Publication date
JPS55111813A (en) 1980-08-28

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