JPS6362260B2 - - Google Patents
Info
- Publication number
- JPS6362260B2 JPS6362260B2 JP57101744A JP10174482A JPS6362260B2 JP S6362260 B2 JPS6362260 B2 JP S6362260B2 JP 57101744 A JP57101744 A JP 57101744A JP 10174482 A JP10174482 A JP 10174482A JP S6362260 B2 JPS6362260 B2 JP S6362260B2
- Authority
- JP
- Japan
- Prior art keywords
- separator
- magnetic powder
- matrix
- container
- granulator
- 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
Links
- 239000006247 magnetic powder Substances 0.000 claims description 19
- 239000002245 particle Substances 0.000 claims description 13
- 239000011159 matrix material Substances 0.000 claims description 9
- 239000008187 granular material Substances 0.000 claims description 7
- 230000005389 magnetism Effects 0.000 claims description 5
- 239000000696 magnetic material Substances 0.000 claims description 3
- 239000005300 metallic glass Substances 0.000 claims description 2
- 238000005469 granulation Methods 0.000 description 7
- 230000003179 granulation Effects 0.000 description 7
- 239000012530 fluid Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000002826 coolant Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION 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
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/025—High gradient magnetic separators
- B03C1/031—Component parts; Auxiliary operations
- B03C1/032—Matrix cleaning systems
Description
【発明の詳細な説明】
本発明は、流体中に懸濁する微細な粉粒体例え
ば原子炉一次二次系冷却材中に懸濁する微細な磁
性粉粒体をいつたん造粒して、ある程度の粒径と
した後除去することにより高い除去率を得ること
のできる磁性粉粒体の分離装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention is a method of granulating fine powder particles suspended in a fluid, for example, fine magnetic powder particles suspended in a primary and secondary system coolant of a nuclear reactor. The present invention relates to a separating device for magnetic powder and granules that can obtain a high removal rate by removing the particles after reducing the particle size to a certain degree.
原子炉一次二次系冷却材中等で生成される磁性
粉粒体を分離器で除去する場合、該生成物の粒径
が3μ以下になると除去が困難となり、能率が著
しく低下する。すなわち、分離器がサイクロンセ
パレータや交番磁界型分離器の場合は除去率が低
下し、フイルターの場合にはフイルターの目が細
かいため目詰りを起こして圧損を大きくすると共
にフイルター交換の頻度を多くして能率の低下を
招来する。そこで、これら問題点を解決するため
に、磁性粉粒体を造粒してある程度の粒度とした
うえ除去することが考えられており、例えば特開
昭53−24676号公報や特開昭51−21267号公報に示
すものがある。 When removing magnetic powder produced in the primary and secondary coolant of a nuclear reactor using a separator, if the particle size of the product becomes 3 μm or less, removal becomes difficult and efficiency drops significantly. In other words, if the separator is a cyclone separator or an alternating magnetic field type separator, the removal rate will be lower, and if the separator is a cyclone separator or an alternating magnetic field type separator, the filter may become clogged due to its fine mesh, increasing pressure loss and increasing the frequency of filter replacement. This leads to a decrease in efficiency. Therefore, in order to solve these problems, it has been considered to granulate magnetic powder to a certain degree of particle size and then remove it. There is one shown in Publication No. 21267.
しかるに、上記公報に示すものはただ単に磁気
を加えて造粒するようにしているだけであるた
め、磁性粉粒体を含む流体が高速であつたり或い
は磁性粉粒体の濃度が低い場合には、造粒が困難
であり、従つて良好な除去効率を得ることはでき
ず、又処理量も多くできないので能率も悪い、等
の問題があつた。 However, since the method disclosed in the above publication simply applies magnetism to granulate, if the fluid containing the magnetic powder is at high speed or the concentration of the magnetic powder is low, However, since granulation is difficult, good removal efficiency cannot be obtained, and the throughput cannot be increased, resulting in poor efficiency.
本発明の目的は、磁性粉粒体の除去を高い除去
効率でしかも能率良く行い得るようにすることを
目的としてなしたもので、粒径の小さい磁性粉粒
体を磁気により造粒し得るよう容器内部に多孔性
の非晶質金属磁性材料を細線状にしたマトリツク
スを収納すると共に振動子及び振動板を収納し容
器外周に磁気発生手段を配設した造粒器と、造粒
した磁性粉粒体を除去する分離器とを設けたこと
を特徴とするものである。 An object of the present invention is to remove magnetic powder and granules with high removal efficiency and efficiency. A granulator that houses a matrix of porous amorphous metal magnetic material in the form of fine wires inside a container, houses a vibrator and a diaphragm, and has magnetism generating means arranged around the outer periphery of the container, and granulated magnetic powder. The present invention is characterized by being equipped with a separator for removing particles.
以下、本発明の実施例を図面を参照しつつ説明
する。 Embodiments of the present invention will be described below with reference to the drawings.
第1図中1は磁気により造粒を行う磁気造粒
器、2は該造粒器1の下流に設けられたサイクロ
ンセパレータ若しくはフイルター或は交番磁界型
分離器のごとき分離器である。 In FIG. 1, 1 is a magnetic granulator that performs granulation using magnetism, and 2 is a separator such as a cyclone separator, a filter, or an alternating magnetic field type separator provided downstream of the granulator 1.
造粒器1の詳細例を第2図により説明すると管
路3,4を接続した所要の容器5内に、底面に複
数の通水孔6を穿設せしめたキヤニスター7を収
納し、該キヤニスター7内に、上面に複数の通水
孔8を穿設せしめた振動板9を配設すると共に該
振動板9とキヤニスター7との間にマトリツクス
10を収納し、振動板9の上面に磁歪振動子若し
くは電歪振動子のごとき振動子11を取付け、容
器5の外周に電磁コイル12を配設し、容器5上
面の振動子11に高周波電流を送るケーブル挿通
面に、高温、高圧用の電線貫通部13を取付け
る。 A detailed example of the granulator 1 will be described with reference to FIG. 2. A canister 7 having a plurality of water passage holes 6 in the bottom is housed in a required container 5 to which pipes 3 and 4 are connected. A diaphragm 9 with a plurality of water holes 8 formed on its upper surface is disposed within the diaphragm 7, and a matrix 10 is housed between the diaphragm 9 and the canister 7. A vibrator 11 such as a oscillator or an electrostrictive vibrator is attached, an electromagnetic coil 12 is arranged around the outer periphery of the container 5, and a high-temperature, high-voltage electric wire is installed on the cable insertion surface that sends a high-frequency current to the vibrator 11 on the top surface of the container 5. Attach the penetration part 13.
前記マトリツクス10は多孔性の非晶質金属磁
性材料を細線状にしたもので薄いテープ状をして
おり、その配列は長手方向が流れに対して平行な
方向となるようにするのが好ましいがアトランダ
ムの配列であつてもよい。 The matrix 10 is made of porous amorphous metallic magnetic material in the form of thin wires, and is in the form of a thin tape, and is preferably arranged so that its longitudinal direction is parallel to the flow. It may be an at random arrangement.
次に、本発明の作用について説明する。 Next, the operation of the present invention will be explained.
造粒時には、管路3から磁性粉粒体の懸濁して
いる流体を容器5を供給し、マトリツクス10部
を通過させて管路4へ排出し、管路4よりライン
外へ排出する。磁性を帯びた磁性粉粒体は、電磁
コイル12による高勾配磁気に依りマトリツクス
10に付着し、付着した部分に他の生成物が付着
することにより造粒が行われる。 During granulation, a fluid in which magnetic powder particles are suspended is supplied from a pipe 3 to a container 5, passed through 10 parts of the matrix, discharged to a pipe 4, and discharged from the pipe 4 to the outside of the line. The magnetic powder particles are attached to the matrix 10 by the high gradient magnetism generated by the electromagnetic coil 12, and granulation is performed by adhering other products to the attached portions.
一定時間造粒を行つて磁性粉粒体の粒度が分離
器2の種類に対応した粒度になつたら管路3から
の流体の供給を行ないつつ電磁コイル12への通
電は止め、振動子11に10〜15KCの高周波又は
電歪電流を通電をすることで振動板9を介してマ
トリツクス10を振動させ、造粒された付着物を
マトリツクス10から離脱させ、離脱させた付着
物を管路3から供給された洗浄水と共に管路4よ
り分離器2へ送り、該分離器2で造粒されて粒度
の大きくなつた磁性粉粒体を分離する。分離器2
がサイクロンセパレータや交番磁界型分離器の場
合は粉粒体を3μ以上に造粒し、分離器2がフイ
ルターの場合は10〜20μ程度に造粒する。 After granulation is carried out for a certain period of time and the particle size of the magnetic powder becomes a particle size corresponding to the type of separator 2, the fluid is supplied from the conduit 3 while the electromagnetic coil 12 is turned off, and the vibrator 11 is turned off. By applying a high frequency or electrostrictive current of 10 to 15 KC, the matrix 10 is vibrated through the diaphragm 9, the granulated deposits are separated from the matrix 10, and the detached deposits are removed from the conduit 3. Together with the supplied washing water, it is sent to a separator 2 through a pipe line 4, and the separator 2 separates the magnetic powder which has been granulated and whose particle size has increased. Separator 2
When the separator 2 is a cyclone separator or an alternating magnetic field type separator, the powder is granulated to a size of 3μ or more, and when the separator 2 is a filter, it is granulated to a size of about 10 to 20μ.
なお、本発明において使用する分離器としては
電磁フイルター又はミルポアー等も使用できるこ
と、その他、本発明の要旨を逸脱しない範囲内で
種々変更を加え得ること、等は勿論である。 It goes without saying that an electromagnetic filter, a mille pore, etc. can be used as the separator used in the present invention, and that various other changes can be made without departing from the gist of the present invention.
本発明の磁性粉粒体の分離装置によれば、
() 磁性粉粒体を含む流体が高速の場合や磁性
粉粒体の濃度が薄い場合でも造粒器で磁性粉粒
体を確実に造粒することができるうえ造粒され
た付着物の造粒器からの離脱を効率良く確実に
行うことができ、又造粒することにより生成物
1粒の重量を増すため、遠心力による効果及び
生成の水中における沈降速度が大きくなり、従
つて除去効率が非常に良好(造粒せずに除去す
る合の約4倍)になると共に処量を多くするこ
とができることにより能率も向上する。 According to the magnetic powder separation device of the present invention, () magnetic powder can be reliably produced in the granulator even when the fluid containing the magnetic powder is at high speed or when the concentration of the magnetic powder is low; In addition to being able to granulate, it is possible to efficiently and reliably remove the granulated deposits from the granulator, and since granulation increases the weight of each product grain, the effect of centrifugal force and The sedimentation rate of the product in water is increased, and therefore the removal efficiency is very good (approximately 4 times that of removal without granulation) and the efficiency is also improved due to the higher throughput.
() 分離器としてフイルターを使用した場合に
は、目詰りの度合いが少なくなり、フイルター
の交換頻度が少なくなるため作業能率が向上
し、又目詰りが少なければ圧損が減少するから
省エネルギーに貢献する。() When a filter is used as a separator, the degree of clogging is reduced, reducing the frequency of filter replacement, improving work efficiency, and less clogging reduces pressure loss, contributing to energy savings. .
() 分離器として交番磁界型分離器を使用した
場合には小型化可能である。() If an alternating magnetic field type separator is used as the separator, it can be made smaller.
() 装置全体が簡単な構造であるためイニシヤ
ルコストを削減できる。() Since the entire device has a simple structure, initial costs can be reduced.
等、種々の優れた効果を奏し得る。Various excellent effects can be achieved.
第1図は本発明の実施例の説明図、第2図は第
1図の実施例に使用する造粒器の説明図である。
図中1は磁気造粒器、2は分離器を示す。
FIG. 1 is an explanatory diagram of an embodiment of the present invention, and FIG. 2 is an explanatory diagram of a granulator used in the embodiment of FIG. In the figure, 1 indicates a magnetic granulator, and 2 indicates a separator.
Claims (1)
得るよう容器内部に多孔性の非晶質金属磁性材料
を細線状にしたマトリツクスを収納すると共に振
動子及び振動板を収納し容器外周に磁気発生手段
を配設した造粒器と、造粒した磁性粉粒体を除去
する分離器とを設けたことを特徴とする磁性粉粒
体の分離装置。1. In order to magnetically granulate magnetic powder with a small particle size, a matrix of porous amorphous metal magnetic material in the form of fine wires is housed inside the container, and a vibrator and a diaphragm are also housed, and the matrix is placed around the outer periphery of the container. 1. An apparatus for separating magnetic powder and granules, comprising: a granulator equipped with a magnetism generating means; and a separator for removing the granulated magnetic powder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57101744A JPS58219956A (en) | 1982-06-14 | 1982-06-14 | Apparatus for separating magnetic powdery particle |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57101744A JPS58219956A (en) | 1982-06-14 | 1982-06-14 | Apparatus for separating magnetic powdery particle |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58219956A JPS58219956A (en) | 1983-12-21 |
JPS6362260B2 true JPS6362260B2 (en) | 1988-12-01 |
Family
ID=14308750
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57101744A Granted JPS58219956A (en) | 1982-06-14 | 1982-06-14 | Apparatus for separating magnetic powdery particle |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58219956A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101912816B (en) * | 2010-08-16 | 2012-02-29 | 河南理工大学 | Electromagnetic separator used for experiment |
JP2015192936A (en) * | 2014-03-31 | 2015-11-05 | 国立大学法人秋田大学 | Magnetic granulator, filter device using the same and high gradient magnetic separation method |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5121267A (en) * | 1974-08-14 | 1976-02-20 | Mitsubishi Heavy Ind Ltd | |
JPS5324676A (en) * | 1976-08-20 | 1978-03-07 | Nippon Steel Corp | Method for separating pulverulent bodies containing magnetic substances |
-
1982
- 1982-06-14 JP JP57101744A patent/JPS58219956A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5121267A (en) * | 1974-08-14 | 1976-02-20 | Mitsubishi Heavy Ind Ltd | |
JPS5324676A (en) * | 1976-08-20 | 1978-03-07 | Nippon Steel Corp | Method for separating pulverulent bodies containing magnetic substances |
Also Published As
Publication number | Publication date |
---|---|
JPS58219956A (en) | 1983-12-21 |
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