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JPS6044964B2 - Method for collecting particles captured by magnetic separator - Google Patents
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JPS6044964B2 - Method for collecting particles captured by magnetic separator - Google Patents

Method for collecting particles captured by magnetic separator

Info

Publication number
JPS6044964B2
JPS6044964B2 JP15112478A JP15112478A JPS6044964B2 JP S6044964 B2 JPS6044964 B2 JP S6044964B2 JP 15112478 A JP15112478 A JP 15112478A JP 15112478 A JP15112478 A JP 15112478A JP S6044964 B2 JPS6044964 B2 JP S6044964B2
Authority
JP
Japan
Prior art keywords
magnetic
particles
captured
magnetic separator
casing
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
JP15112478A
Other languages
Japanese (ja)
Other versions
JPS5579020A (en
Inventor
義弘 小澤
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP15112478A priority Critical patent/JPS6044964B2/en
Publication of JPS5579020A publication Critical patent/JPS5579020A/en
Publication of JPS6044964B2 publication Critical patent/JPS6044964B2/en
Expired 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
    • B03C1/031Component parts; Auxiliary operations
    • B03C1/032Matrix cleaning systems

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)

Description

【発明の詳細な説明】 本発明は、磁気分離機、さらに詳細には、磁性細線か
らなる充填物を縦形ケーシング内に充填配置して磁界を
印加しケーシング内を下方より上方に通過する流体中の
磁性粒子を分離する磁気分離機、における捕捉粒子回収
方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a magnetic separator, and more particularly, to a magnetic separator, a filler made of magnetic thin wires is placed in a vertical casing, and a magnetic field is applied to the fluid passing through the casing from the bottom to the top. The present invention relates to a method for collecting captured particles in a magnetic separator that separates magnetic particles.

磁気分離機は、低品位の鉄鉱石の品位上昇や窯業原料
からの鉄分除去に利用されてきた。
Magnetic separators have been used to upgrade low-grade iron ore and remove iron from ceramic raw materials.

最近、高勾配磁気分離法が開発されてからは、常磁性粒
子も磁気的に捕捉できるようになり、工場廃水からの重
金属の除去や、原子炉の一次冷却水中の放射性鉄分除去
にも応用されるようになつた。 高勾配磁気分離機では
、磁性細線を磁界中に充填し、大きな磁界勾配を発生さ
せる。磁性粒子の磁性細線上への捕捉が進むと、磁性細
線の実効半径が太くなつて捕捉率が低下すること及び磁
性粒子による流路が閉塞されることによつて圧力損失が
増大する。そこで、一たん、捕捉操作を中止し、かつ磁
界発生用の電磁コイルヘの通電を停止した後、逆洗水を
流すことによつて、磁性粒子を磁性細線上から離脱させ
回収する操作が採られる。この方法では、例えば製鉄所
排水の除鉄回収や、工場廃水からの重金属の除去のよう
に、磁性粒子を離脱させた後の逆洗水操作や濃縮操作等
が容易な場合は、多少逆洗水が多くなつてもそれほど問
題にはならない。しかし、放射性廃液や原子炉の冷却水
を処理する場合には、できる限り逆洗水の量を少なくす
ることが、高放射性廃液の処理操作上望ましい。通常の
逆洗水操作で捕捉粒子を離脱させるためには、高圧水に
よつて十分に大きな流速で通水する必要があり、結果的
に高放射性廃液の量が多くなつてしまう。 本発明の目
的は、磁気分離機の磁性細線上に捕捉された磁性粒子を
、できるだけ少量の処理水で離脱させ回収する捕捉粒子
回収方法を提供するにある。
Recently, with the development of high-gradient magnetic separation methods, it has become possible to magnetically capture paramagnetic particles, which has been applied to the removal of heavy metals from industrial wastewater and the removal of radioactive iron from primary cooling water of nuclear reactors. I started to do that. In high-gradient magnetic separators, magnetic wires are filled in a magnetic field to generate a large magnetic field gradient. As the capture of magnetic particles onto the magnetic wire progresses, the effective radius of the magnetic wire becomes thicker, the capture rate decreases, and the flow path is blocked by the magnetic particles, resulting in an increase in pressure loss. Therefore, after temporarily stopping the capture operation and stopping the power supply to the electromagnetic coil for generating the magnetic field, an operation is adopted in which the magnetic particles are separated from the magnetic wire and collected by flowing backwash water. . With this method, if it is easy to perform backwash water operation or concentration operation after removing magnetic particles, such as when recovering iron from steelworks wastewater or removing heavy metals from factory wastewater, it is possible to use some backwashing. Even if there is a lot of water, it won't be much of a problem. However, when treating radioactive waste liquid or nuclear reactor cooling water, it is desirable to reduce the amount of backwash water as much as possible from the viewpoint of processing highly radioactive waste liquid. In order to remove trapped particles using normal backwash water operations, it is necessary to use high-pressure water to flow at a sufficiently high flow rate, resulting in an increase in the amount of highly radioactive waste liquid. An object of the present invention is to provide a method for collecting captured particles in which magnetic particles captured on magnetic fine wires of a magnetic separator are separated and recovered using as little treated water as possible.

本発明の特徴は、捕捉粒子の離脱条件を種々検討した
結果、磁性細線上に捕捉された粒子は、電磁石への通電
を停止して数10cm/ s以上の流速で通水しないと
離脱させることは難カルいが、磁性細線充填部に強制的
に気泡を導入すると容易に磁性粒子から捕捉粒子を離脱
させることができることが判明したことに着眼して、磁
性細線充填物の下方より気体を導入することて充填物表
面からその捕捉粒子を離脱させる工程と、この工程終了
後に磁性細線充填物の上方より下方に逆洗水を流して離
脱された磁性粒子を回収する工程とからなる捕捉粒子回
収方法を採用することにある。
The feature of the present invention is that, as a result of various studies on the release conditions for captured particles, it was found that particles captured on magnetic thin wires are released only when electricity to the electromagnet is stopped and water is not passed at a flow rate of several tens of cm/s or more. Although it is difficult to do so, we discovered that by forcibly introducing air bubbles into the magnetic fine wire filling part, the trapped particles can be easily separated from the magnetic particles, and we introduced gas from below the magnetic fine wire filling. Captured particle recovery consists of a step of detaching the captured particles from the surface of the packing, and a step of flowing backwash water from above to below the magnetic fine wire packing to recover the detached magnetic particles. It consists in adopting a method.

以下図面により本発明を説明する。The present invention will be explained below with reference to the drawings.

第1図は本発明の回収方法を採用する磁気分離機を原子
炉一次冷却水の浄化に適用する場合の全体構成配置図で
あり、1は原子炉、2はこの原子炉の発生熱を駆動源と
するタービン、3は復水器、4は一次冷却水浄化系、5
はイオン交換塔、6は磁気分離機、7は磁気分離機6で
使用する逆洗水が流入する逆洗水入口、8は逆洗水出口
をそれぞれ示す。
Figure 1 is an overall configuration layout diagram when a magnetic separator that adopts the recovery method of the present invention is applied to purify nuclear reactor primary cooling water, where 1 is a nuclear reactor and 2 is a drive for the heat generated by this reactor. 3 is a condenser, 4 is a primary cooling water purification system, 5 is
6 indicates an ion exchange column, 6 indicates a magnetic separator, 7 indicates a backwash water inlet into which backwash water used in the magnetic separator 6 flows, and 8 indicates a backwash water outlet.

磁気分離機6の詳細を説明するための図面が第2図であ
る。
FIG. 2 is a drawing for explaining details of the magnetic separator 6.

高勾配磁気分離機11は、縦形のケーシング12の内部
に磁性細線で形成される充填物14を配置しておいてケ
ーシング外部に設けたコイル13により磁性細線充填物
14に磁界を印加することで構成される。原子炉の一次
冷却水の浄化系プロセス流れから、ケーシング12の下
方位置に設けたバルブ20を介して、放射性の酸化鉄を
含む冷却水をケーシング12内に導入する。一次冷却水
中に含まれるFe3O4やFe2O3の粒子の大部分は
磁性細線充填物14の磁性細線上に捕捉される。捕捉さ
れなかつた粒子を含む一次冷却水は、ケーシング12の
上方位置に設けたバルブ21を介して浄化系プロセス流
れに戻される。捕捉操作が進むと、磁性細線上に2重に
も3重にも粒子が捕捉されるため、磁性細線充填物14
での粒子捕捉効率は低下する。また、流路の一部が閉塞
することになるので圧力損失が上昇する。圧力損失等を
測定して高勾配磁気分離機11の捕捉可能限界を検知し
た後、前記のバルブ20及び21を閉じて、磁気分離機
をプロセス流れから分離する。次にバルブ22を開いて
気体導入管16にアルゴンあるいは窒素ガスを送り、気
体吹出ノズル17から放出する。
The high gradient magnetic separator 11 is constructed by arranging a filler 14 made of magnetic thin wire inside a vertical casing 12 and applying a magnetic field to the magnetic thin wire filler 14 using a coil 13 provided outside the casing. configured. Cooling water containing radioactive iron oxide is introduced into the casing 12 from the purification system process flow of the reactor primary cooling water through a valve 20 located below the casing 12 . Most of the particles of Fe3O4 and Fe2O3 contained in the primary cooling water are captured on the magnetic wires of the magnetic wire packing 14. The primary cooling water containing uncaptured particles is returned to the purification system process stream via a valve 21 located above the casing 12. As the trapping operation progresses, the particles are captured double or triple on the magnetic fine wire, so the magnetic fine wire packing 14
The particle capture efficiency will be reduced. Moreover, since a part of the flow path is blocked, pressure loss increases. After determining the capture limit of the high gradient magnetic separator 11 by measuring pressure drop, etc., the valves 20 and 21 are closed to separate the magnetic separator from the process stream. Next, the valve 22 is opened to send argon or nitrogen gas to the gas introduction pipe 16 and discharged from the gas blowing nozzle 17.

このとき気体の吹出圧力は数Kg/Cdあれば十分であ
る。放出された気体は整流板15を通つて磁性細線充填
物14の下部から上部へ気泡となつて上昇する。気泡は
ケーシング12内に残留する一次冷却水と混合し、一部
の一次冷却水は磁性細線充填物14内を気泡にともなつ
て上昇するが自重で直ちに落下する。以上の気泡の上昇
、及び一次冷却水の落下等により、磁性細線上に捕捉さ
れている粒子は容易に磁性細線から引離される。このと
きコイル13への通電を止めておく。さらに、バルブ2
3は上気の気体吹出操″作中は開いておき、バルブ23
から排出される気体を例えば放射性ガス処理施設(図示
せず)で処理する。気泡による磁性細線からの捕捉粒子
の離脱操作が終了した後、バルブ22及び23を閉じ、
バルブ24を開いて逆洗水導入管18を経由して逆洗水
を導入し、ケーシング12内に滞留している放射性粒子
を洗い出し、バルブ25を介して系外に排出する。
At this time, a gas blowing pressure of several kg/Cd is sufficient. The released gas passes through the baffle plate 15 and rises from the bottom to the top of the magnetic fine wire packing 14 in the form of bubbles. The air bubbles mix with the primary cooling water remaining in the casing 12, and some of the primary cooling water rises inside the magnetic fine wire packing 14 along with the air bubbles, but immediately falls down due to its own weight. Due to the rise of the bubbles and the falling of the primary cooling water, the particles captured on the magnetic wire are easily separated from the magnetic wire. At this time, power to the coil 13 is stopped. Furthermore, valve 2
Valve 23 is kept open during the upper air blowing operation.
For example, the gas discharged from the reactor is treated in a radioactive gas processing facility (not shown). After the separation of the captured particles from the magnetic wire by the bubbles is completed, the valves 22 and 23 are closed,
The valve 24 is opened and backwash water is introduced via the backwash water introduction pipe 18 to wash out the radioactive particles staying in the casing 12 and discharged to the outside of the system via the valve 25.

以上の操作において、捕捉した粒子を離脱させるための
逆洗水はほとんど必要とせず、洗い出しに必要とするの
みで、逆洗水量を従来の方法に比べて極端に少なくする
ことが可能となる。以上説明したように、本発明によれ
ば、磁気分離機の磁性細線上に捕捉された磁性粒子を極
く少量の処理水で回収できるようになる。
In the above operation, almost no backwash water is required to remove the captured particles, and only necessary for washing out, making it possible to significantly reduce the amount of backwash water compared to conventional methods. As explained above, according to the present invention, magnetic particles captured on the magnetic wire of a magnetic separator can be recovered with a very small amount of treated water.

なお、前記実施例では原子炉の一次冷却水の処理につい
てのみ説明したが、本発明方法は放射性廃液中の磁性粒
子の除去に適用できる以外に、一般の液体中の不純物除
去などで、廃液の容積を少なくする必要がある場合にも
有効である。
In the above embodiment, only the treatment of primary cooling water of a nuclear reactor was explained, but the method of the present invention can be applied not only to the removal of magnetic particles from radioactive waste liquid, but also to the removal of impurities from general liquid waste. It is also effective when it is necessary to reduce the volume.

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

第1図は磁気分離機を原子炉一次冷却水の浄化に適用す
る場合の全体配置図、第2図は本発明の一実施例説明図
である。 12・・・・・・ケーシング、13・・・・コイル、1
4・・・・・磁性細線充填物、15・・・・・・整流板
、16・・・・・・気体導入管、17・・・・・・気体
吹出ノズル、18・・・・・・逆洗水導入管、20〜2
5・・・・・・バルブ。
FIG. 1 is an overall layout diagram when a magnetic separator is applied to purify primary cooling water of a nuclear reactor, and FIG. 2 is an explanatory diagram of an embodiment of the present invention. 12...Casing, 13...Coil, 1
4... Magnetic thin wire filling, 15... Current plate, 16... Gas introduction tube, 17... Gas blowing nozzle, 18... Backwash water introduction pipe, 20-2
5...Valve.

Claims (1)

【特許請求の範囲】[Claims] 1 磁性細線からなる充填物を縦形ケーシング内に充填
配置して磁界を印加しケーシング内を下方より上方に通
過する流体中の磁性粒子を分離する磁気分離機において
、上記充填物に捕捉された磁性粒子を上記充填物の下方
より気体を導入することで上記充填物の表面から離脱さ
せる工程と、この工程終了後に上記充填物の上方より下
方に逆洗水を流して上記離脱された磁性粒子を回収する
工程とを含むことを特徴とする磁気分離機の捕捉粒子回
収方法。
1. In a magnetic separator that separates magnetic particles in a fluid that passes through the casing from the bottom to the top by filling and arranging a filler made of magnetic fine wires in a vertical casing and applying a magnetic field, the magnetic particles captured by the filler are The particles are separated from the surface of the packing by introducing gas from below the packing, and after this step, backwash water is flowed downward from above the packing to remove the separated magnetic particles. 1. A method for collecting captured particles in a magnetic separator, comprising the step of collecting.
JP15112478A 1978-12-08 1978-12-08 Method for collecting particles captured by magnetic separator Expired JPS6044964B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15112478A JPS6044964B2 (en) 1978-12-08 1978-12-08 Method for collecting particles captured by magnetic separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15112478A JPS6044964B2 (en) 1978-12-08 1978-12-08 Method for collecting particles captured by magnetic separator

Publications (2)

Publication Number Publication Date
JPS5579020A JPS5579020A (en) 1980-06-14
JPS6044964B2 true JPS6044964B2 (en) 1985-10-07

Family

ID=15511881

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15112478A Expired JPS6044964B2 (en) 1978-12-08 1978-12-08 Method for collecting particles captured by magnetic separator

Country Status (1)

Country Link
JP (1) JPS6044964B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55149616A (en) * 1979-05-11 1980-11-21 Toshiba Corp Cleaning of magnetic filter
JPS58114750A (en) * 1981-12-28 1983-07-08 Nec Corp Recovering device of magnetic material
MX2007009601A (en) * 2007-07-31 2009-01-30 Yuri Nahmad Molinari try><pc

Also Published As

Publication number Publication date
JPS5579020A (en) 1980-06-14

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