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JPS6241773B2 - - Google Patents
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JPS6241773B2 - - Google Patents

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Publication number
JPS6241773B2
JPS6241773B2 JP59103860A JP10386084A JPS6241773B2 JP S6241773 B2 JPS6241773 B2 JP S6241773B2 JP 59103860 A JP59103860 A JP 59103860A JP 10386084 A JP10386084 A JP 10386084A JP S6241773 B2 JPS6241773 B2 JP S6241773B2
Authority
JP
Japan
Prior art keywords
matrix
magnetic
nozzle
separation device
magnetic separation
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
JP59103860A
Other languages
Japanese (ja)
Other versions
JPS60248211A (en
Inventor
Soichiro Sakata
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 JP59103860A priority Critical patent/JPS60248211A/en
Publication of JPS60248211A publication Critical patent/JPS60248211A/en
Publication of JPS6241773B2 publication Critical patent/JPS6241773B2/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
    • B03C1/031Component parts; Auxiliary operations
    • B03C1/032Matrix cleaning systems
    • 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
    • B03C1/029High gradient magnetic separators with circulating matrix or matrix elements
    • B03C1/03High gradient magnetic separators with circulating matrix or matrix elements rotating, e.g. of the carousel type

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明は磁気分離装置のマトリクスの閉塞の原
因となる残留磁着物を、圧力水を噴射して効果的
に除去する磁気分離装置に関する。 〔従来技術〕 従来、大量スラリー処理用に実用化されている
移動式磁気分離装置には、第1図に示す回転運動
式の分離装置と第2図に示す往復運動式の分離装
置との2つの種類がある。いずれも磁気回路(ヨ
ーク)11の対向磁極12の間隙部分に、強磁性
金属ウールの充てん構造あるいは強磁性金属の金
網やエキスパンドメタルやパンチングメタン等を
積層した構造を有するマトリクス13を収納した
容器14を配置したものである。第1図の回転運
動式では容器14は円周方向15に回転運動し、
第2図の往復運動式では容器14は水平方向26
に往復運動する。一方、給液口17から磁界空間
中のマトリクス13に原液18が重力フイードさ
れ、原液18中の磁性体粒子19が除去された
後、非磁性体粒子24を含む処理液25となつて
処理水トラフ20に流入する。マトリクス13に
捕捉された磁性体粒子19は、磁界空間外に設け
た洗浄ノズル21から鉛直下方に噴射される圧力
水22によつて洗い出され、その洗浄済液16は
洗浄済液トラフ23に流入する。圧力水22で洗
い出せない残留磁着物はマトリクス13の内部に
堆積するが、その堆積によりマトリクス13に閉
塞を生じた場合には直ちに原液18の流入を止め
て運転を停止し、マトリクス13を容器14から
外部に取り出し、新規マトリクスと交換して運転
を再開していた。 〔従来技術の問題点〕 このように従来の移動式磁気分離装置において
は、磁界空間外に設けた洗浄ノズルから鉛直下方
に噴射される圧力水をマトリクスの上面に吹き付
けて、前記マトリクスの内部に磁着した磁性体粒
子の除去が行なわれるが、前記圧力水は前記マト
リクスの内部を透過する際、著しい圧力損失を生
じるために、前記マトリクスの下方においては前
記圧力水の洗浄力は非常に弱くなる。このため、
前記マトリクスの上面付近に磁着した磁性体粒子
は、前記圧力水の強い洗浄力で前記マトリクスか
らはずされるが、前記マトリクスの下方において
は、前記圧力水の洗浄力が弱まるため、残留磁化
の作用で磁着した磁性体粒子は除去されにくいと
いう欠点があつた。次にマトリクスの洗浄の問題
点を第3図〜第5図のマトリクスを例にとつて説
明する。第3図は強磁性金属でつくられたエキス
パンドメタル27を、磁界の印加方向29と直交
し原液および洗浄水の流入方向28と平行に積層
した構造のマトリクスである。第4図にその平面
図、第5図に断面図を示す。第4図、第5図にお
いて、洗浄水の流入方向28と向かい合う側30
に磁着した磁性体粒子は洗浄除去されやすいが、
洗浄水の流入方向28に向き合わない側31に磁
着した磁性体粒子は前記洗浄水の流れがよどむい
わゆる死水域の範囲に存るために洗浄除去されに
くい。 この結果、前記洗浄水によつて除去されずに前
記マトリクスの内部に残存した前記磁性体粒子に
よる閉塞現象が度々発生し、前記マトリクスに流
入する原液があふれたり、前記原液中の磁性体粒
子の捕集効率が低下するという現象が生じ、マト
リクスの交換頻度が非常に多くなるという磁気分
離装置上の大きな問題が生じていたのである。 〔発明の目的〕 本発明の目的は、このような従来の欠点を除去
せしめて、マトリクスに対して原液流入側と原液
流出側の2方向から圧力水を噴射して洗浄を行な
い、マトリクスの閉塞の原因となる残存磁着物を
効果的に除去できる磁気分離装置を提供すること
にある。 〔発明の構成〕 本発明は強磁性金属でつくられたマトリクスと
前記マトリクスに磁界を加えるべく配置された磁
石装置と前記磁石装置の磁界空間の内外にわたつ
て連続的かつ反復的に前記マトリクスを往復運動
または回転運動せしめる機構と、前記磁界空間外
にて前記マトリクスを洗浄するノズルを備えた磁
気分離装置において、前記ノズルを前記マトリク
スに対して、原液流入側と原液流出側とにそれぞ
れマトリクスに向けて設置したことを特徴とする
磁気分離装置である。 〔実施例〕 以下、本発明の実施例について図面を参照して
詳細に説明する。 第6図は、本発明を回転運動式の磁気分離装置
に適用した場合の実施例である。第1図に示した
従来の回転運動式の磁気分離装置はマトリクス1
3の上方に洗浄ノズル21を設置したものであつ
たが、本発明ではマトリクス13を鉛直下方側か
ら洗浄可能な逆洗ノズル32をさらに設けたもの
である。マトリクス13に磁着した磁性体粒子1
9は、マトリクスの直下から上方へ向けて噴出す
る圧力水33によつてその大部分が除去され、そ
の直後に鉛直上方から下方へ噴出する圧力水22
によつて完全に除去される。第6図では、容器1
4の移動方向15に沿つて逆洗ノズル32と洗浄
ノズル21を順次配置したが、逆の順に、つまり
容器14の移動方向15に沿つて洗浄ノズル21
と逆洗ノズル32の順に配置しても、マトリクス
13に磁着した磁性体粒子19の洗浄除去効果は
同様に期待できる。 第7図と第8図は、往復運動式の磁気分離装置
に本発明を適用した実施例である。第7図は平面
図、第8図は第7図の−断面図をそれぞ
れ示す。容器14はモータ34とチエーン35と
を組合せて駆動するようになつている。第2図に
示した従来の往復運動式の磁気分離装置ではマト
リクス13の真上に洗浄ノズル21を備えている
が、本発明ではさらにマトリクス13を鉛直下方
から洗浄可能な逆洗ノズル32を付加したもので
ある。マトリクス13に磁着した磁性体粒子は、
鉛直下方から上方へ向けて逆洗ノズル32より噴
出させた圧力水33によつてその大部分が除去さ
れ、その直後に鉛直上方から下方へ向けて洗浄ノ
ズル21より噴出させた圧力水22によつて完全
に除去される。第7図では、磁極12から離れる
逆洗ノズル32と洗浄ノズル21を配置したが、
逆の順に、つまり磁極から離れる順に洗浄ノズル
21と逆洗ノズル32を配置しても、マトリクス
13に磁着した磁性体粒子19の洗浄除去効果は
同期に期待できる。 〔発明の効果〕 本発明装置(第7図に示すもの)と従来の磁気
分離装置(第2図に示したもの)との処理能力に
ついて以下の実験を行つた。まず原液としてブラ
ウン管ガラス製造ラインから排出される研摩スラ
リーを第1表の条件で処理した。この処理は、ス
ラリーからの除鉄を図り、スラリー中のスラツジ
のガラス原料化を目的とするものである。マトリ
クスは、第3図に示すように原液の流れ方向28
に沿う過長さが180mmの網目形状をもつエキス
パンドメタル板を45枚積層したものを用い、全体
の層の厚みを90mmとした。また洗浄水量は、本発
明装置と従来の磁気分離装置に対し共に0.5ton/
hrとした。
[Industrial Application Field] The present invention relates to a magnetic separation device that effectively removes residual magnetic substances that cause blockage of the matrix of the magnetic separation device by jetting pressurized water. [Prior Art] Conventionally, there are two types of mobile magnetic separators that have been put into practical use for processing large amounts of slurry: a rotary motion separator shown in FIG. 1 and a reciprocating motion separator shown in FIG. There are two types. In each case, a container 14 containing a matrix 13 having a structure filled with ferromagnetic metal wool or a structure laminated with ferromagnetic metal wire mesh, expanded metal, punched methane, etc. is placed in the gap between opposing magnetic poles 12 of a magnetic circuit (yoke) 11. is arranged. In the rotary motion type shown in FIG. 1, the container 14 rotates in the circumferential direction 15,
In the reciprocating type shown in FIG. 2, the container 14 is moved in the horizontal direction 26.
make a reciprocating motion. On the other hand, the stock solution 18 is gravity-fed from the liquid supply port 17 to the matrix 13 in the magnetic field space, and after the magnetic particles 19 in the stock solution 18 are removed, the processing solution 25 containing non-magnetic particles 24 is converted into treated water. It flows into the trough 20. The magnetic particles 19 captured in the matrix 13 are washed out by pressure water 22 sprayed vertically downward from a washing nozzle 21 provided outside the magnetic field space, and the washed liquid 16 is transferred to a washed liquid trough 23. Inflow. Residual magnetized matter that cannot be washed out with the pressure water 22 accumulates inside the matrix 13, but if the accumulation causes a blockage in the matrix 13, the flow of the raw solution 18 is immediately stopped, the operation is stopped, and the matrix 13 is placed in a container. The matrix was removed from No. 14, replaced with a new matrix, and operation resumed. [Problems with the prior art] As described above, in the conventional mobile magnetic separation device, pressurized water is sprayed vertically downward from the cleaning nozzle provided outside the magnetic field space onto the top surface of the matrix, and the interior of the matrix is The magnetized magnetic particles are removed, but when the pressure water passes through the matrix, a significant pressure loss occurs, so the cleaning power of the pressure water is very weak below the matrix. Become. For this reason,
Magnetic particles magnetized near the top surface of the matrix are removed from the matrix by the strong cleaning power of the pressure water, but below the matrix, the cleaning power of the pressure water is weakened, so that residual magnetization is reduced. The drawback was that magnetic particles that were magnetized by the action were difficult to remove. Next, problems with matrix cleaning will be explained using the matrices shown in FIGS. 3 to 5 as examples. FIG. 3 shows a matrix in which expanded metals 27 made of ferromagnetic metal are laminated in a direction perpendicular to the direction 29 of applying a magnetic field and parallel to the direction 28 of inflow of the stock solution and cleaning water. FIG. 4 shows a plan view thereof, and FIG. 5 shows a sectional view thereof. In FIGS. 4 and 5, the side 30 facing the washing water inflow direction 28
Magnetic particles that are magnetized are easily washed away, but
The magnetic particles magnetized on the side 31 that does not face the washing water inflow direction 28 are difficult to be washed away because they exist in a so-called dead zone where the flow of the washing water stagnates. As a result, blockage phenomena due to the magnetic particles remaining inside the matrix without being removed by the washing water often occur, and the stock solution flowing into the matrix overflows, or the magnetic particles in the stock solution This caused a phenomenon in which the collection efficiency decreased and the matrix had to be replaced very frequently, which was a major problem in magnetic separation devices. [Object of the Invention] The object of the present invention is to eliminate such conventional drawbacks, and to clean the matrix by jetting pressure water from two directions, the undiluted solution inflow side and the undiluted solution outflow side, to eliminate matrix occlusion. An object of the present invention is to provide a magnetic separation device that can effectively remove residual magnetic substances that cause . [Structure of the Invention] The present invention includes a matrix made of ferromagnetic metal, a magnet device arranged to apply a magnetic field to the matrix, and a magnet device that continuously and repeatedly applies the matrix inside and outside the magnetic field space of the magnet device. In a magnetic separation device comprising a mechanism for causing reciprocating or rotational movement, and a nozzle for cleaning the matrix outside the magnetic field space, the nozzle is arranged on an undiluted solution inflow side and an undiluted solution outflow side with respect to the matrix, respectively. This is a magnetic separation device characterized by being installed toward the [Example] Hereinafter, an example of the present invention will be described in detail with reference to the drawings. FIG. 6 shows an embodiment in which the present invention is applied to a rotary motion type magnetic separation device. The conventional rotary motion type magnetic separation device shown in Fig. 1 is a matrix 1
However, in the present invention, a backwash nozzle 32 that can wash the matrix 13 from the vertically downward side is further provided. Magnetic particles 1 magnetically attached to matrix 13
Most of the water 9 is removed by the pressure water 33 that is ejected upward from directly below the matrix, and immediately after that, the pressure water 22 is ejected downward from the vertically upward direction.
completely removed by In Figure 6, container 1
4, the backwash nozzle 32 and the cleaning nozzle 21 are arranged sequentially along the moving direction 15 of the container 14, but the cleaning nozzle 21 is arranged in the reverse order, that is, along the moving direction 15 of the container
Even if the backwash nozzle 32 is arranged in this order, the same effect of washing and removing the magnetic particles 19 magnetically attached to the matrix 13 can be expected. FIGS. 7 and 8 show an embodiment in which the present invention is applied to a reciprocating type magnetic separation device. FIG. 7 is a plan view, and FIG. 8 is a cross-sectional view taken from FIG. 7. The container 14 is driven by a combination of a motor 34 and a chain 35. The conventional reciprocating magnetic separator shown in FIG. 2 is equipped with a cleaning nozzle 21 directly above the matrix 13, but in the present invention, a backwashing nozzle 32 that can clean the matrix 13 from vertically below is added. This is what I did. The magnetic particles magnetically attached to the matrix 13 are
Most of it is removed by the pressure water 33 jetted from the vertically downward direction upwards from the backwashing nozzle 32, and immediately after that, the pressure water 22 jetted vertically downwardly from the cleaning nozzle 21 removes the water. completely removed. In FIG. 7, the backwash nozzle 32 and the cleaning nozzle 21 are placed away from the magnetic pole 12, but
Even if the cleaning nozzle 21 and the backwashing nozzle 32 are arranged in the reverse order, that is, in the order away from the magnetic pole, the cleaning and removal effect of the magnetic particles 19 magnetically attached to the matrix 13 can be expected to be synchronous. [Effects of the Invention] The following experiments were conducted regarding the throughput of the apparatus of the present invention (as shown in FIG. 7) and the conventional magnetic separation apparatus (as shown in FIG. 2). First, a polishing slurry discharged from a cathode ray tube glass manufacturing line as a stock solution was treated under the conditions shown in Table 1. The purpose of this treatment is to remove iron from the slurry and convert the sludge in the slurry into a raw material for glass. The matrix is arranged in the flow direction 28 of the stock solution as shown in FIG.
A stack of 45 expanded metal plates with a mesh shape with an overlength of 180 mm along the length was used, and the total layer thickness was 90 mm. In addition, the amount of washing water is 0.5ton/for both the present invention device and the conventional magnetic separation device.
hr.

【表】【table】

【表】 装置の仕様と処理条件を第1表に示す。本発明
装置と従来装置とによるマトリクスの単位体積当
たりの残存磁着物の堆積量および鉄粉粒子の捕集
効率の長期間ランニングにおける経時変化を第2
表に示す。 第2表によれば、本発明と従来の移動式磁気分
離装置を使用して第1表の条件でガラス研摩スラ
リーを処理した場合、本発明は40日間の連続運転
に対してもマトリクスの残存磁着物の堆積はほと
んどなく、鉄粉粒子の捕集効率の低下は全く生じ
なかつたのに対して、従来の磁気分離装置では、
マトリクスは残存磁着物の堆積によつて徐々に閉
塞を起こし、40日後には原液がマトリクスからあ
ふれ出し、新規マトリクスと交換する必要が生じ
た。また前記従来の磁気分離装置では、マトリク
スが除々に閉塞を起こすとともに鉄粉粒子の捕集
効率も徐々に低下した。 以上、詳細に述べた通り、本発明によれば、マ
トリクスの閉塞の原因になる残存磁着物の堆積を
ほぼ完全に防止し、前記閉塞に伴う鉄粉粒子の捕
集効率の低下を招くことがなく、したがつて、長
期間のランニングが可能であり、マトリクスの交
換頻度も大幅に減少できる効果を有するものであ
る。
[Table] Table 1 shows the equipment specifications and processing conditions. The second graph shows the changes over time in the amount of residual magnetic material deposited per unit volume of the matrix and the collection efficiency of iron powder particles in the device of the present invention and the conventional device during long-term running.
Shown in the table. According to Table 2, when glass abrasive slurry is processed using the present invention and the conventional mobile magnetic separator under the conditions shown in Table 1, the present invention shows that the matrix remains even after 40 days of continuous operation. There was almost no accumulation of magnetic substances, and there was no decrease in the collection efficiency of iron powder particles, whereas with conventional magnetic separation equipment,
The matrix gradually became clogged due to the accumulation of residual magnetic material, and after 40 days, the stock solution overflowed from the matrix and it became necessary to replace it with a new matrix. Furthermore, in the conventional magnetic separation device, the matrix gradually became clogged and the efficiency of collecting iron powder particles gradually decreased. As described in detail above, according to the present invention, it is possible to almost completely prevent the accumulation of residual magnetic particles that cause matrix clogging, and to prevent the reduction in iron powder particle collection efficiency caused by the clogging. Therefore, it is possible to run for a long period of time, and the frequency of replacing the matrix can be significantly reduced.

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

第1図は従来の回転運動式磁気分離装置の斜視
図、第2図は往復運動式磁気分離装置の斜視図、
第3図はエキスパンドメタルを積層した構造のマ
トリクスの斜視図、第4図はエキスパンドメタル
の網目形状を示す平面図、第5図は第4図の−
線断面図、第6図は本発明の第1の実施例を示
す斜視図、第7図は本発明の第2の実施例を示す
正面図、第8図は第7図の−線断面図で
ある。 11……ヨーク、12……対向磁極、13……
マトリクス、14……容器、15……回転運動方
向、16……洗浄済液、17……給液トラフ、1
8……原液、19……磁性体粒子、20……処理
済液トラフ、21……洗浄ノズル、22……圧力
水、23……洗浄済液トラフ、24……非磁性体
粒子、25……処理済液、26……往復運動方
向、27……エキスパンドメタル、28……原液
および洗浄水の流入方向、29……磁界の印加方
向、30……洗浄水の流入方向28と向かい合う
側、31……洗浄水の流入方向28に向き合わな
い側、32……逆洗ノズル、33……圧力水、3
4……モータ、35……チエーン。
FIG. 1 is a perspective view of a conventional rotary motion magnetic separator, FIG. 2 is a perspective view of a reciprocating motion magnetic separator,
Fig. 3 is a perspective view of a matrix with a structure in which expanded metals are laminated, Fig. 4 is a plan view showing the mesh shape of the expanded metal, and Fig. 5 is the − of Fig. 4.
6 is a perspective view showing the first embodiment of the present invention, FIG. 7 is a front view showing the second embodiment of the present invention, and FIG. 8 is a sectional view taken along the line -- of FIG. 7. It is. 11... Yoke, 12... Opposing magnetic pole, 13...
Matrix, 14... Container, 15... Rotational movement direction, 16... Washed liquid, 17... Liquid supply trough, 1
8... Raw solution, 19... Magnetic particles, 20... Treated liquid trough, 21... Washing nozzle, 22... Pressure water, 23... Washed liquid trough, 24... Non-magnetic particles, 25... ... Treated liquid, 26 ... Direction of reciprocating movement, 27 ... Expanded metal, 28 ... Inflow direction of raw solution and washing water, 29 ... Direction of magnetic field application, 30 ... Side opposite to washing water inflow direction 28, 31... Side not facing the washing water inflow direction 28, 32... Backwash nozzle, 33... Pressure water, 3
4...Motor, 35...Chain.

Claims (1)

【特許請求の範囲】[Claims] 1 強磁性金属でつくられたマトリクスと、前記
マトリクスに磁界を加えるべく配置された磁石装
置と、前記磁石装置の磁界空間の内外にわたつて
連続的かつ反復的に前記マトリクスを往復運動ま
たは回転運動せしめる機構と、前記磁界空間外に
て前記マトリクスを洗浄するノズルとを備えた磁
気分離装置において、前記ノズルを前記マトリク
スに対して、原液流入側と原液流出側とにそれぞ
れマトリクスに向けて設置したことを特徴とする
磁気分離装置。
1 A matrix made of ferromagnetic metal, a magnet device arranged to apply a magnetic field to the matrix, and a continuous and repetitive reciprocating or rotational movement of the matrix inside and outside the magnetic field space of the magnet device. In the magnetic separation device, the nozzles are installed on an undiluted solution inflow side and an undiluted solution outflow side facing the matrix, respectively, with respect to the matrix. A magnetic separation device characterized by:
JP59103860A 1984-05-23 1984-05-23 Magnetic separation device Granted JPS60248211A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59103860A JPS60248211A (en) 1984-05-23 1984-05-23 Magnetic separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59103860A JPS60248211A (en) 1984-05-23 1984-05-23 Magnetic separation device

Publications (2)

Publication Number Publication Date
JPS60248211A JPS60248211A (en) 1985-12-07
JPS6241773B2 true JPS6241773B2 (en) 1987-09-04

Family

ID=14365199

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59103860A Granted JPS60248211A (en) 1984-05-23 1984-05-23 Magnetic separation device

Country Status (1)

Country Link
JP (1) JPS60248211A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0474545A (en) * 1990-07-17 1992-03-09 Kenzo Takahashi Magnetic sorter of dry high grade inductive magnetic drum type
FR2862633B1 (en) * 2003-11-21 2006-06-09 Promaiga DEVICE FOR DISCHARGING SLUDGE PRESENT IN A CIRCUIT, IN PARTICULAR HEATING

Also Published As

Publication number Publication date
JPS60248211A (en) 1985-12-07

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