JP2005144390A - Method and apparatus for separating magnetic or non-magnetic material, and waste material melting treatment facilities - Google Patents

Method and apparatus for separating magnetic or non-magnetic material, and waste material melting treatment facilities Download PDF

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JP2005144390A
JP2005144390A JP2003388518A JP2003388518A JP2005144390A JP 2005144390 A JP2005144390 A JP 2005144390A JP 2003388518 A JP2003388518 A JP 2003388518A JP 2003388518 A JP2003388518 A JP 2003388518A JP 2005144390 A JP2005144390 A JP 2005144390A
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magnetic
magnetic material
drum
mixture
separator
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JP2005144390A5 (en
JP4939729B2 (en
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Yoshitomo Okabe
由知 岡部
Akira Kurata
顕 倉田
Yasutaka Yamada
康登 山田
Shinya Takenaka
伸也 竹中
Yasuyuki Aida
泰之 合田
Masami Kashima
正実 香島
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Ebara Corp
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Ebara Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for separating a magnetic or a non-magnetic material capable of efficiently separating the magnetic and the non-magnetic materials even if a mixture of the magnetic and the non-magnetic materials is in a wet state by solving the problem that a separating efficiency is extremely deteriorated when the mixture of metal which is the magnetic material in the wet state and slag which is the non-magnetic material is separated by a conventional drum type magnetic separator, an apparatus, and waste material melting treatment facilities. <P>SOLUTION: In the method and the apparatus for separating the magnetic or the non-magnetic material provided with the drum type magnetic separator 10, and separating the magnetic and the non-magnetic materials from the mixture 20 of a molten, granulated and solidified magnetic material supplied to the drum type magnetic separator 10 and the non-magnetic material, a peripheral speed of a rotary drum 12 on the drum type magnetic separator is changed in response to a feed speed of the mixture 20, pressurized air is sprayed to the surface of the drum surface 12, and the pressurized air 21 is sprayed to the drum surface 12 from a lower direction in a tangential direction from an air nozzle 22. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、都市ごみ焼却工場や産業廃棄物焼却工場における溶融炉から排出される溶融物を水砕固化した水砕スラグから磁性物を分離する磁性・非磁性物分離方法、磁性・非磁性物分離装置及び該磁性・非磁性物分離装置を備えた廃棄物溶融処理設備に関するものである。   The present invention relates to a magnetic / non-magnetic material separation method, a magnetic / non-magnetic material, and a magnetic / non-magnetic material separation method that separates magnetic material from granulated slag obtained by granulating and solidifying molten material discharged from a melting furnace in a municipal waste incineration plant or industrial waste incineration plant The present invention relates to a waste melting treatment facility equipped with a separation device and the magnetic / non-magnetic material separation device.

都市ごみ焼却工場や産業廃棄物焼却工場における溶融炉から発生するメタルとスラグは、ドラム型磁選機の上部からメタルとスラグの混合物を供給して、磁性物であるメタルをドラム表面に磁力で捕捉させて回収することにより、磁性物であるメタルと非磁性物であるスラグを分離していた。   Metal and slag generated from melting furnaces in municipal waste incineration plants and industrial waste incineration plants supply a mixture of metal and slag from the top of the drum type magnetic separator, and capture the magnetic metal on the drum surface by magnetic force. By collecting them, the magnetic metal and the non-magnetic slag were separated.

都市ごみ又は都市ごみ焼却灰を溶融処理した場合、溶融物として、磁性物であるメタルと非磁性物であるスラグが混合した状態で溶融炉の出口(出滓口)より排出される。このように混合状態の溶融物は、通常、溶融炉の下方部に位置した水砕水槽に落下し、水砕された後、水砕水槽内の溶融物分離コンベアで排出され、更にドラム型磁選機でメタルとスラグが分離され、スラグは土木資材(骨材等)、溶融メタルは金属資源としてリサイクルされている。   When municipal waste or municipal waste incineration ash is melt-processed, the molten metal is discharged from the outlet (unloading port) of the melting furnace in a state where the magnetic metal and the non-magnetic slag are mixed. In this way, the melt in a mixed state usually falls to a granulated water tank located in the lower part of the melting furnace, and after water granulation, is discharged by a melt separation conveyor in the water granulated water tank, and is further drum-type magnetically separated. Metal and slag are separated by the machine, slag is recycled as civil engineering materials (aggregates, etc.), and molten metal is recycled as metal resources.

しかし、溶融物分離コンベアより排出された溶融物は濡れ状態であるため(含水率約10%)、磁選機のドラム表面に水膜を形成する。そしてこの水の表面張力によりドラム表面にスラグが付着した状態を保持するため、ドラム表面の磁束密度が低下するという問題が起る。また、更にドラム表面に付着した非磁性物であるスラグが磁性物として回収されるため、磁選機での分離効率は極めて悪かった。   However, since the melt discharged from the melt separation conveyor is in a wet state (water content of about 10%), a water film is formed on the drum surface of the magnetic separator. And since the state in which the slag adhered to the drum surface is maintained by the surface tension of the water, there arises a problem that the magnetic flux density on the drum surface is lowered. Further, since the slag, which is a non-magnetic material adhering to the drum surface, is recovered as a magnetic material, the separation efficiency in the magnetic separator was extremely poor.

図1は従来のドラム型磁選機の概略構成を示す図である。図1(a)は側断面図、図1(b)は内部正面図である。図示するように、ドラム型磁選機100はケーシング101内に回転する回転ドラム102が配設され、該回転ドラム102の下方に仕切板103が配設され、該仕切板103で区分されたケーシング101の一方(図では右側)が磁性物排出シュート104、他方(図では左側)が非磁性物排出シュート105となっている。回転ドラム102の内部に断面扇形状の磁石106がその円弧部の外周面が回転ドラム102の内周面に接近して配設固定されている。また、ケーシング101の頂部にはメタルとスラグの混合物が投入される投入ホッパー107が設けられている。   FIG. 1 is a diagram showing a schematic configuration of a conventional drum type magnetic separator. 1A is a side sectional view, and FIG. 1B is an internal front view. As shown in the figure, the drum type magnetic separator 100 has a rotating drum 102 disposed in a casing 101, a partition plate 103 disposed below the rotating drum 102, and the casing 101 partitioned by the partition plate 103. One (right side in the figure) is a magnetic substance discharge chute 104, and the other (left side in the figure) is a non-magnetic substance discharge chute 105. Inside the rotating drum 102, a magnet 106 having a fan-shaped cross section is disposed and fixed with the outer peripheral surface of the arc portion approaching the inner peripheral surface of the rotating drum 102. A charging hopper 107 into which a mixture of metal and slag is charged is provided at the top of the casing 101.

上記構成のドラム型磁選機において、投入ホッパー107に投入されたメタルとスラグの混合物110は回転している回転ドラム102の上部(この部分の回転ドラム102の内部には磁石106が位置していない)に落下する。磁性物であるメタル108の一部は落下の衝撃により、飛散し、一部は磁石106の磁力により回転ドラム102の表面に吸引され、磁石106の磁力が作用しない位置まで移動し、ここで回転ドラム102の表面から離脱し、磁性物排出シュート104に落下する。また、非磁性物であるスラグ109は非磁性物排出シュート105に落下する。   In the drum type magnetic separator having the above-described configuration, the metal and slag mixture 110 charged into the charging hopper 107 is above the rotating drum 102 (the magnet 106 is not located inside this rotating drum 102). ). A part of the metal 108 that is a magnetic material is scattered by the impact of dropping, and a part of the metal 108 is attracted to the surface of the rotating drum 102 by the magnetic force of the magnet 106 and moves to a position where the magnetic force of the magnet 106 does not act, and rotates here. It separates from the surface of the drum 102 and falls onto the magnetic material discharge chute 104. Further, the slag 109 which is a non-magnetic material falls on the non-magnetic material discharge chute 105.

投入ホッパー107に投入されたメタルとスラグの混合物は溶融炉から排出された後、水砕されているから濡れ状態(含水率約10%)にあるから、上記のようにドラム型磁選機100の回転ドラム102の表面に水膜を形成する。そしてこの水膜の表面張力により回転ドラム102の表面にスラグが付着した状態となるので、表面の磁束密度が低下し、更に本来、非磁性物であるスラグ109が磁性物であるメタル108が排出される磁性物排出シュート104に落下し、磁性物として回収されるため。ドラム型磁選機100での分離効率は極めて悪くなる。
特開平8−187485号公報
Since the mixture of metal and slag charged into the charging hopper 107 is discharged from the melting furnace and then water-crushed, it is in a wet state (water content of about 10%). A water film is formed on the surface of the rotating drum 102. Since the surface tension of the water film causes slag to adhere to the surface of the rotating drum 102, the magnetic flux density on the surface decreases, and the slag 109, which is originally non-magnetic, is discharged from the metal 108, which is magnetic. The magnetic material is dropped on the magnetic material discharge chute 104 and collected as a magnetic material. The separation efficiency in the drum type magnetic separator 100 is extremely deteriorated.
JP-A-8-187485

本発明は、上記のように従来のドラム型磁選機で濡れ状態の磁性物であるメタルと非磁性物であるスラグの混合物を分離した場合、分離効率は極めて悪くなるという問題を解決し、濡れ状態にある磁性物と非磁性物の混合物であっても磁性物と非磁性物を効率良く分離できる磁性・非磁性物分離方法、磁性・非磁性物分離装置及び該磁性・非磁性物分離装置を備えた廃棄物溶融処理設備を提供することを目的とする。   As described above, the present invention solves the problem that the separation efficiency becomes extremely poor when a mixture of a metal that is a wet magnetic substance and a slag that is a non-magnetic substance is separated by a conventional drum type magnetic separator. Magnetic / non-magnetic material separation method, magnetic / non-magnetic material separation device, and magnetic / non-magnetic material separation device capable of efficiently separating magnetic material and non-magnetic material even in the state of a mixture of magnetic material and non-magnetic material It aims at providing the waste melting processing equipment provided with.

上記課題を解決するため請求項1に記載の発明は、ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離方法において、混合物の供給速度に応じてドラム型磁選機のドラムの周速を変化させ、磁性物と非磁性物を分離することを特徴とする。   In order to solve the above-mentioned problem, the invention described in claim 1 is provided with a drum type magnetic separator, and a magnetic substance is obtained from a mixture of melted and crushed magnetic material and nonmagnetic material supplied to the drum type magnetic separator. In the magnetic / non-magnetic material separation method for separating non-magnetic materials, the peripheral speed of the drum of the drum type magnetic separator is changed according to the supply speed of the mixture to separate the magnetic material and the non-magnetic material.

請求項2に記載の発明は、ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離方法において、ドラム型磁選機のドラム表面に圧力空気を吹き付け、磁性物と非磁性物を分離することを特徴とする。   The invention according to claim 2 includes a drum type magnetic separator, and separates the magnetic substance and the nonmagnetic substance from the mixture of the melted and crushed and solidified magnetic substance and the nonmagnetic substance supplied to the drum type magnetic separator. In the magnetic / non-magnetic material separating method, the air is blown onto the drum surface of the drum type magnetic separator to separate the magnetic material and the non-magnetic material.

請求項3に記載の発明は、ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離方法において、ドラム型磁選機のドラム表面に圧力空気を該ドラム下方から接線方向に吹き付け、磁性物と非磁性物を分離することを特徴とする。   The invention according to claim 3 includes a drum type magnetic separator, and separates the magnetic substance and the nonmagnetic substance from the mixture of the melted and ground granulated magnetic substance and the nonmagnetic substance supplied to the drum type magnetic separator. In the magnetic / non-magnetic material separation method, the magnetic material and the non-magnetic material are separated by blowing pressure air tangentially from below the drum to the drum surface of the drum type magnetic separator.

請求項4に記載の発明は、ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離方法において、混合物の供給速度に応じてドラム型磁選機のドラムの周速を変化させること、該ドラム表面に圧力空気を吹き付けること、該ドラム表面に下方から接線方向に圧力空気を吹き付けることのいずれか二つ以上を組合せ磁性物と非磁性物を分離することを特徴とする。   The invention according to claim 4 includes a drum type magnetic separator, and separates the magnetic substance and the nonmagnetic substance from a mixture of the melted and crushed magnetic substance and the nonmagnetic substance supplied to the drum type magnetic separator. In the magnetic / non-magnetic separation method, the drum peripheral speed of the drum type magnetic separator is changed according to the supply speed of the mixture, the pressure air is blown onto the drum surface, and the pressure is tangentially applied to the drum surface from below. Any two or more of blowing air are combined to separate the magnetic material and the non-magnetic material.

請求項5に記載の発明は、ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離装置において、混合物の供給速度を検出する速度検出手段と、ドラム型磁選機のドラムの周速を制御する制御手段を設け、制御手段は速度検出手段で検出した混合物の供給速度に応じて、ドラムの周速を変化させ、磁性物と非磁性物を分離することを特徴とする。   The invention according to claim 5 includes a drum type magnetic separator, and separates the magnetic substance and the nonmagnetic substance from the mixture of the melted and ground granulated magnetic substance and the nonmagnetic substance supplied to the drum type magnetic separator. In the magnetic / non-magnetic substance separating apparatus, a speed detecting means for detecting the supply speed of the mixture and a control means for controlling the peripheral speed of the drum of the drum type magnetic separator are provided, and the control means supplies the mixture detected by the speed detecting means. According to the speed, the peripheral speed of the drum is changed to separate the magnetic material and the non-magnetic material.

請求項6に記載の発明は、ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離装置において、ドラム型磁選機のドラム表面に圧力空気を吹き付ける圧力空気吹付手段を設け、該ドラム表面に圧力空気を吹き付け、磁性物と非磁性物を分離することを特徴とする。   The invention according to claim 6 includes a drum type magnetic separator, and separates the magnetic substance and the nonmagnetic substance from the mixture of the melted and crushed magnetic substance and the nonmagnetic substance supplied to the drum type magnetic separator. In the magnetic / non-magnetic material separation device, there is provided pressure air blowing means for blowing pressure air onto the drum surface of the drum type magnetic separator, and the magnetic material and non-magnetic material are separated by blowing the pressure air onto the drum surface. To do.

請求項7に記載の発明は、ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離装置において、ドラム型磁選機のドラム表面に該ドラム下方から接線方向に圧力空気を吹き付ける圧力空気吹付手段を設け、該ドラム表面に圧力空気を吹き付け、磁性物と非磁性物を分離することを特徴とする。   The invention described in claim 7 includes a drum type magnetic separator, and separates the magnetic substance and the nonmagnetic substance from the mixture of the melted and crushed magnetic substance and the nonmagnetic substance supplied to the drum type magnetic separator. In the magnetic / non-magnetic material separation device, there is provided pressure air blowing means for blowing pressure air tangentially from below the drum on the drum surface of the drum-type magnetic separator, and the magnetic material and non-magnetic material are blown to the drum surface. It is characterized by separating.

請求項8に記載の発明は、ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離装置において、混合物の供給速度を検出し、該検出した混合物の供給速度に応じてドラム型磁選機のドラムの回転速度を制御する制御手段と、該ドラム表面に圧力空気を吹き付ける圧力空気吹付手段と、該ドラム表面に該ドラム下方から接線方向に圧力空気を吹き付ける圧力空気吹付手段のいずれか二つ以上を組合せ、磁性物と非磁性物を分離することを特徴とする。   The invention according to claim 8 includes a drum type magnetic separator, and separates the magnetic substance and the nonmagnetic substance from the mixture of the melted and crushed magnetic substance and the nonmagnetic substance supplied to the drum type magnetic separator. In the magnetic / non-magnetic substance separation device, a control means for detecting the supply speed of the mixture and controlling the rotation speed of the drum of the drum type magnetic separator according to the detected supply speed of the mixture, and pressure air on the drum surface Two or more of the pressure air spraying means for spraying and the pressure air spraying means for spraying the pressure air tangentially from below the drum to the drum surface are combined to separate the magnetic material and the non-magnetic material.

請求項9に記載の発明は、請求項5又は8に記載の磁性・非磁性物分離装置において、混合物の供給速度を検出する速度検出手段は、監視カメラの画像処理信号、又は温度計の検出出力、サーモカメラの検出出力のいずれか一つ、又は二つ以上の組合せから混合物の供給速度を検出することを特徴とする。   According to a ninth aspect of the present invention, in the magnetic / nonmagnetic substance separating apparatus according to the fifth or eighth aspect, the speed detection means for detecting the supply speed of the mixture is an image processing signal of a surveillance camera or a detection of a thermometer. The supply speed of the mixture is detected from any one of the output, the detection output of the thermo camera, or a combination of two or more.

請求項10に記載の発明は、請求項9に記載の磁性・非磁性物分離装置において、監視カメラ、温度計、サーモカメラは溶融状態の混合物が排出される排出口、溶融状態の混合物を水砕する水砕シュート部に設けたことを特徴とする。   According to a tenth aspect of the present invention, in the magnetic / nonmagnetic substance separating apparatus according to the ninth aspect, the monitoring camera, the thermometer, and the thermocamera have a discharge port from which the molten mixture is discharged, and the molten mixture is water. It was provided in the water granulation chute part to crush.

請求項11に記載の発明は、廃棄物を溶融する溶融炉、該溶融炉から排出される溶融物を水砕固化した水砕スラグを製造するスラグ製造装置、該スラグ製造装置から排出された水砕スラグを磁性物と非磁性物に分離する磁性・非磁性物分離装置を備えた廃棄物溶融処理設備において、磁性・非磁性物分離装置に、請求項5乃至10のいずれか1項に記載の磁性・非磁性物分離装置を用いることを特徴とする。   The invention described in claim 11 is a melting furnace for melting waste, a slag manufacturing apparatus for manufacturing a granulated slag obtained by granulating and solidifying a melt discharged from the melting furnace, and water discharged from the slag manufacturing apparatus. 11. The waste melting treatment facility equipped with a magnetic / non-magnetic material separation device that separates the crushed slag into a magnetic material and a non-magnetic material, and the magnetic / non-magnetic material separation device according to claim 5. The magnetic / non-magnetic material separating apparatus is used.

請求項1又は5に記載の発明によれば、磁性物と非磁性物の混合物の供給速度に応じてドラム型磁選機のドラムの周速を変化させることにより、分離された磁性物への非磁性物の混入率を小さくできる。   According to the first or fifth aspect of the present invention, the peripheral speed of the drum of the drum type magnetic separator is changed according to the supply speed of the mixture of the magnetic material and the non-magnetic material, so that the non-magnetic material is separated. The mixing rate of magnetic substances can be reduced.

請求項2又は6に記載の発明によれば、ドラム型磁選機のドラム表面に圧力空気を吹き付け、該ドラム表面に付着した非磁性物を吹き飛ばすので、分離された磁性物への非磁性物の混入率を小さくできる。   According to the second or sixth aspect of the invention, since the compressed air is blown onto the drum surface of the drum type magnetic separator and the nonmagnetic material adhering to the drum surface is blown off, the nonmagnetic material is separated from the separated magnetic material. The mixing rate can be reduced.

請求項3又は7に記載の発明によれば、圧力空気をドラム表面に接線方向から吹きつけるので、ドラム表面に付着した非磁性物をより効果的に吹き飛ばすことができ、分離された磁性物への非磁性物の混入率を小さくできる。   According to the invention described in claim 3 or 7, since the pressure air is blown against the drum surface from the tangential direction, the non-magnetic material attached to the drum surface can be blown off more effectively, and the separated magnetic material can be blown. The mixing rate of non-magnetic materials can be reduced.

請求項4又は8に記載の発明によれば、混合物の供給速度に応じてドラム型磁選機のドラムの周速を変化させること、該ドラム表面に圧力空気を吹き付けること、該ドラム表面に下方から接線方向に圧力空気を吹き付けることのいずれか二つ以上を組合せ磁性物と非磁性物を分離するので、分離された磁性物への非磁性物の混入率を更に小さくできる。   According to the invention described in claim 4 or 8, the peripheral speed of the drum of the drum type magnetic separator is changed according to the supply speed of the mixture, the pressurized air is blown onto the drum surface, and the drum surface is viewed from below. Since the magnetic material and the nonmagnetic material are separated by combining any two or more of blowing the pressure air in the tangential direction, the mixing ratio of the nonmagnetic material to the separated magnetic material can be further reduced.

請求項11に記載の発明によれば、廃棄物溶融処理設備のスラグ製造装置から排出された水砕スラグを磁性物と非磁性物に分離する磁性・非磁性物分離装置に請求項5乃至10のいずれか1項に記載の磁性・非磁性物分離装置を用いるので、廃棄物から磁性物を高効率で回収できる廃棄物溶融処理設備を提供できる。
According to the eleventh aspect of the present invention, there is provided a magnetic / nonmagnetic separation apparatus for separating the granulated slag discharged from the slag production apparatus of the waste melting treatment facility into a magnetic substance and a nonmagnetic substance. Since the magnetic / non-magnetic material separation apparatus according to any one of the above is used, it is possible to provide a waste melting treatment facility capable of recovering magnetic material from waste with high efficiency.

以下、本発明の実施の形態例を図面に基づいて説明する。図2は本発明に係る磁性・非磁性物分離装置のドラム型磁選機の構成例を示す図である。図2(a)は側断面図、図2(b)は内部正面図である。図示するように、ドラム型磁選機10はケーシング11内に回転する回転ドラム12が配設され、該回転ドラム12の下方に仕切板13が配設され、該仕切板13で区分されたケーシング11の一方(図では右側)が磁性物排出シュート14、他方(図では左側)が非磁性物排出シュート15となっている。回転ドラム12の内部に断面扇形状の磁石16がその円弧部の外周面が回転ドラム12の内周面に接近して配設固定されている。また、ケーシング11の頂部には溶融水砕固化されたメタルとスラグの混合物20が投入される投入ホッパー17が設けられている。また、回転ドラム12の下方には圧力空気21を噴出するエアノズル22を設け、該エアノズル22から圧力空気21を非磁性物排出シュート15側の上方で且つ回転ドラム12の表面の接線方向に噴出するようになっている。   Embodiments of the present invention will be described below with reference to the drawings. FIG. 2 is a diagram showing a configuration example of a drum type magnetic separator of the magnetic / nonmagnetic substance separating apparatus according to the present invention. 2A is a side sectional view, and FIG. 2B is an internal front view. As shown in the figure, the drum type magnetic separator 10 has a rotating drum 12 disposed in a casing 11, a partition plate 13 disposed below the rotating drum 12, and the casing 11 partitioned by the partition plate 13. One (right side in the figure) is a magnetic substance discharge chute 14, and the other (left side in the figure) is a non-magnetic substance discharge chute 15. Inside the rotary drum 12, a magnet 16 having a fan-shaped cross section is disposed and fixed with the outer peripheral surface of the arc portion approaching the inner peripheral surface of the rotary drum 12. In addition, a charging hopper 17 into which a mixture 20 of molten and crushed metal and slag is charged is provided at the top of the casing 11. Further, an air nozzle 22 for ejecting the pressure air 21 is provided below the rotating drum 12, and the pressure air 21 is ejected from the air nozzle 22 above the non-magnetic material discharge chute 15 side and in the tangential direction of the surface of the rotating drum 12. It is like that.

また、回転ドラム12は図3に示すように、モータ23で回転駆動されるようになっており、該モータ23はモータ駆動装置24で駆動されるようになっている。また、モータ駆動装置24には制御装置25から制御信号Sが入力され、モータ駆動装置24は該制御信号Sに基づいてモータ23を指令された回転速度で駆動するようになっている。また、制御装置25にはドラム型磁選機10に供給される溶融水砕固化されたメタルとスラグの混合物20の供給速度を検出するための各種センサ26−1〜26−nが接続されており、制御装置25は該センサ26−1〜26−nからの出力により混合物20の供給速度を演算して求め、この供給速度に応じて回転ドラム12の周速を変化させることができるようになっている。   Further, as shown in FIG. 3, the rotary drum 12 is driven to rotate by a motor 23, and the motor 23 is driven by a motor driving device 24. In addition, a control signal S is input to the motor drive device 24 from the control device 25, and the motor drive device 24 drives the motor 23 at the commanded rotation speed based on the control signal S. The control device 25 is connected to various sensors 26-1 to 26-n for detecting the supply speed of the melted and crushed metal and slag mixture 20 supplied to the drum type magnetic separator 10. The control device 25 calculates and obtains the supply speed of the mixture 20 based on the outputs from the sensors 26-1 to 26-n, and can change the peripheral speed of the rotary drum 12 in accordance with the supply speed. ing.

上記構成のドラム型磁選機において、投入ホッパー17に投入されたメタルとスラグの混合物20は回転している回転ドラム12の上部に落下する。混合物20は上記のように濡れ状態(含水率約10%)にあるから、回転ドラム12の表面に水膜を形成し、水の表面張力により回転ドラム12の表面にスラグ19が付着した状態となると共に、メタル18は磁石16の磁力により回転ドラム12の表面に吸引される。回転ドラム12の表面には上記のようにその接線方向にエアノズル22から圧力空気21が吹き付けられているから、付着したスラグが吹き飛ばされて回転ドラム12の表面から離脱し、非磁性物排出シュート15に落下する。また、磁性物であるメタル18は磁石16の磁力が作用しない位置で回転ドラム12の表面から離脱し、磁性物排出シュート14に落下する。   In the drum type magnetic separator having the above-described configuration, the metal and slag mixture 20 charged into the charging hopper 17 falls onto the rotating rotary drum 12. Since the mixture 20 is in a wet state (water content of about 10%) as described above, a water film is formed on the surface of the rotating drum 12, and the slag 19 is attached to the surface of the rotating drum 12 due to the surface tension of water. At the same time, the metal 18 is attracted to the surface of the rotating drum 12 by the magnetic force of the magnet 16. Since the pressure air 21 is blown from the air nozzle 22 to the surface of the rotating drum 12 in the tangential direction as described above, the adhering slag is blown off and separated from the surface of the rotating drum 12, and the non-magnetic substance discharge chute 15 is discharged. Fall into. Further, the metal 18 which is a magnetic material is detached from the surface of the rotating drum 12 at a position where the magnetic force of the magnet 16 does not act, and falls onto the magnetic material discharge chute 14.

上記のように、回転ドラム12の表面に付着したスラグ19はエアノズル22から噴出された圧力空気21により吹き飛ばされるから、磁性物排出シュート14に落下するメタル18にはスラグ19の混入率は極めて小さくなる。また、回転ドラム12の表面に付着したスラグ19が除去されることにより、回転ドラム12の表面の磁石16による磁気吸引力が低下することなく、磁性物であるメタル18は確実に回転ドラム12の表面に吸引され、磁力が作用しない位置で離脱するから、混合物20からのメタル18の分離率が向上する。また、回転ドラム12の周速は上記のように混合物20の供給速度に応じて変化させるようになっているから、後に実験結果で示すように分離されたメタル18のスラグ混入率を低減させることができる。   As described above, since the slag 19 adhering to the surface of the rotating drum 12 is blown away by the pressure air 21 ejected from the air nozzle 22, the mixing rate of the slag 19 is extremely small in the metal 18 falling on the magnetic substance discharge chute 14. Become. Further, by removing the slag 19 adhering to the surface of the rotary drum 12, the magnetic attraction force by the magnet 16 on the surface of the rotary drum 12 does not decrease, and the metal 18 that is a magnetic material is reliably attached to the rotary drum 12. Since it is attracted to the surface and separated at a position where no magnetic force acts, the separation rate of the metal 18 from the mixture 20 is improved. Further, since the peripheral speed of the rotating drum 12 is changed according to the supply speed of the mixture 20 as described above, the slag mixing rate of the separated metal 18 is reduced as shown in the experimental results later. Can do.

図4は本発明に係る磁性・非磁性物分離装置を使用する廃棄物溶融処理設備の全体構成例を示す図である。図示するように廃棄物溶融処理設備は、溶融炉30、スラグ分離コンベア40、スラグヤード50を具備する。溶融炉30はプラズマトーチ31を具備し、焼却灰投入口32から投入された焼却灰33をプラズマトーチ31から発せられるプラズマアーク34の高温で溶融し、出滓口35から溶融した磁性物であるメタルと非磁性物であるスラグの混合物37を排出するようになっている。焼却灰33の溶融に伴って発生するガスは排ガス39となってガス出口36から排出される。   FIG. 4 is a diagram showing an example of the overall configuration of a waste melting treatment facility using the magnetic / non-magnetic material separating apparatus according to the present invention. As shown in the figure, the waste melting treatment facility includes a melting furnace 30, a slag separation conveyor 40, and a slag yard 50. The melting furnace 30 includes a plasma torch 31, and is a magnetic material in which the incineration ash 33 charged from the incineration ash charging port 32 is melted at a high temperature of the plasma arc 34 emitted from the plasma torch 31 and melted from the tap hole 35. A mixture 37 of slag, which is a metal and a non-magnetic material, is discharged. The gas generated as the incineration ash 33 melts becomes exhaust gas 39 and is discharged from the gas outlet 36.

出滓口35から排出された混合物37はシュート38を通ってスラグ分離コンベア40の水砕水槽41内に落下する。該水砕水槽41に落下した混合物37は水砕水槽41内の水と接触し、水砕され、固化する。なお、混合物37をシュート38内で水と接触させ、水砕された混合物を水砕水槽41内に落下させる場合もある。水砕水槽41内で水砕固化した混合物20はコンベア42でドラム型磁選機10の投入ホッパー17に運ばれ投入される。ドラム型磁選機10では混合物20は、上記のように磁性物であるメタル18と非磁性物であるスラグ19に分離される。分離されたメタル18は磁性物排出シュート14から排出され、メタルバケット27に収容され、再利用される。また、分離されたスラグ19はスラグ搬送コンベア28によりスラグヤード50に運ばれる。   The mixture 37 discharged from the spout 35 passes through the chute 38 and falls into the granulated water tank 41 of the slag separation conveyor 40. The mixture 37 that has fallen into the granulated water tank 41 comes into contact with the water in the granulated water tank 41, and is ground and solidified. In some cases, the mixture 37 is brought into contact with water in the chute 38, and the crushed mixture is dropped into the crushed water tank 41. The mixture 20 crushed and solidified in the pulverized water tank 41 is conveyed to the input hopper 17 of the drum type magnetic separator 10 by the conveyor 42 and input. In the drum type magnetic separator 10, the mixture 20 is separated into the metal 18 which is a magnetic material and the slag 19 which is a non-magnetic material as described above. The separated metal 18 is discharged from the magnetic material discharge chute 14, accommodated in the metal bucket 27, and reused. The separated slag 19 is transported to the slag yard 50 by the slag transport conveyor 28.

ドラム型磁選機10に供給される水砕固化されたメタルとスラグの混合物20の供給速度(t/h)を検出するための各種センサ26−1〜26−n(図3参照)としては、例えば溶融炉30の出滓口35やシュート38の近傍に、出滓口35から排出される混合物37やシュート38内を落下する混合物37を監視する監視カメラを設け、制御装置25で該監視カメラからの画像信号を画像処理し、供給される混合物20の供給速度を検出する方法がある。また、監視カメラに替えてサーモカメラを設置し、制御装置25で該サーモカメラの出力信号を処理し、混合物20の供給速度を検出するようにしてもよい。また、出滓口35やシュート38の近傍に、1個又は複数個の温度計を設け、この温度計の出力信号を処理し、混合物20の供給速度を検出するようにしてもよい。また、スラグ分離コンベア40の水砕水槽41の1又は複数箇所に水温を測定する温度計を設け、該温度計の出力信号を処理し、混合物20の供給速度を検出するようにしてもよい。   As various sensors 26-1 to 26-n (see FIG. 3) for detecting the supply speed (t / h) of the mixture 20 of the granulated and solidified metal and slag 20 supplied to the drum type magnetic separator 10. For example, a monitoring camera for monitoring the mixture 37 discharged from the spout 35 or the mixture 37 falling in the chute 38 is provided in the vicinity of the spout 35 and chute 38 of the melting furnace 30, and the control device 25 uses the monitoring camera. There is a method of detecting the supply speed of the supplied mixture 20 by image processing the image signal from the image signal. Alternatively, a thermo camera may be installed in place of the monitoring camera, and the output signal of the thermo camera may be processed by the control device 25 to detect the supply speed of the mixture 20. Further, one or a plurality of thermometers may be provided in the vicinity of the spout 35 and the chute 38, and the output signal of the thermometer may be processed to detect the supply speed of the mixture 20. Further, a thermometer for measuring the water temperature may be provided at one or a plurality of locations of the granulated water tank 41 of the slag separation conveyor 40, and the output signal of the thermometer may be processed to detect the supply speed of the mixture 20.

図5は水砕水槽にて水砕冷却された混合物(メタル50%、スラグ50%)を供給速度0.5t/h、1.0t/h、2.0t/hの条件で、図2に示す構成のドラム型磁選機10に供給し、磁性物(メタル)と非磁性物(スラグ)を分離した場合の磁性物側(磁性物排出シュート14側)のスラグ混入率(%)を示す図である。この時の回転ドラム12の周速は50m/minに固定している。また、回転ドラム12の表面に下方に設置したエアノズル22から接線方向にエア(圧力空気)を吹き付けて付着したスラグを除去する場合と、エアを吹き付けない場合を示す。従来のように、エアを吹き付けない場合の磁性物側スラグ混入率が13%、18%、27%であるのに対して、エアを吹き付け、回転ドラム12の表面に付着したスラグを除去した場合の磁性物側スラグ混入率が1.6%、1.9%、2.0%となる。図から明らかなように、回転ドラム12の表面にエアを吹き付けた場合、即ち本発明によれば磁性物側スラグ混入率が大幅に改善されることがわかる。なお、このときのエア吹き付け量は、回転ドラム12の単位長当り(1〜5m3/min)/m吹き付け圧力は500〜1000kPaである。 FIG. 5 shows a mixture (50% metal, 50% slag) that has been subjected to water granulation cooling in a water granulation tank under the conditions of supply speeds of 0.5 t / h, 1.0 t / h, and 2.0 t / h. The figure which shows the slag mixing rate (%) by the side of the magnetic material (magnetic material discharge chute 14 side) at the time of supplying to the drum type magnetic separator 10 of the structure shown, and isolate | separating a magnetic material (metal) and a nonmagnetic material (slag) It is. The peripheral speed of the rotating drum 12 at this time is fixed at 50 m / min. Moreover, the case where the slag adhering by spraying air (pressure air) from the air nozzle 22 installed on the surface of the rotating drum 12 in the tangential direction is removed and the case where air is not blown are shown. When the magnetic material side slag mixing rate is 13%, 18%, and 27% when air is not blown as in the conventional case, when air is blown and the slag adhering to the surface of the rotating drum 12 is removed The magnetic material side slag mixing ratio is 1.6%, 1.9%, and 2.0%. As can be seen from the figure, when air is blown onto the surface of the rotating drum 12, that is, according to the present invention, the magnetic material side slag mixing rate is greatly improved. At this time, the air blowing amount is (1 to 5 m 3 / min) / m blowing pressure per unit length of the rotary drum 12 and is 500 to 1000 kPa.

図6は上記実施例1と同様の混合物(メタル50%、スラグ50%)を供給速度0.5t/h、1.0t/h、1.5t/hの条件で図2に示す構成のドラム型磁選機10に供給し、回転ドラム12のドラム周速を変化させて磁性物(メタル)と非磁性物(スラグ)を分離した場合の磁性物側(磁性物排出シュート14側)のスラグ混入率(%)を示す図である。曲線Aが1.5t/h、曲線Bが1.0t/h、曲線Cが0.5t/hをそれぞれ示す。図示するように、ドラム周速を50m/min〜200m/minに変化させることにより、混合物の供給速度0.5t/h、1.0t/h、1.5t/hのいずれの場合もスラグ混入率が改善される。   FIG. 6 shows a drum having the same composition as in Example 1 (50% metal, 50% slag) at a feed rate of 0.5 t / h, 1.0 t / h, and 1.5 t / h as shown in FIG. Slag mixing on the magnetic material side (magnetic material discharge chute 14 side) when the magnetic material (metal) and the non-magnetic material (slag) are separated by changing the drum peripheral speed of the rotary drum 12 It is a figure which shows a rate (%). Curve A is 1.5 t / h, curve B is 1.0 t / h, and curve C is 0.5 t / h. As shown in the figure, by changing the drum peripheral speed from 50 m / min to 200 m / min, slag is mixed at any of the mixture supply speeds of 0.5 t / h, 1.0 t / h, and 1.5 t / h. The rate is improved.

図7は上記実施例1と同様の混合物(メタル50%、スラグ50%)を供給速度0.5t/h、1.0t/h、1.5t/hの条件で図2に示す構成のドラム型磁選機10に供給し、回転ドラム12の周速を変化させて磁性物(メタル)と非磁性物(スラグ)を分離した場合の磁性物側(磁性物排出シュート14側)のスラグ混入率(%)を示す図である。ここでは、回転ドラム12の表面に下方に設置したエアノズル22から接線方向に空気を吹き付けて付着したスラグを除去している。曲線Aが1.5t/h、曲線Bが1.0t/h、曲線Cが0.5t/hをそれぞれ示す。図示するように、回転ドラム12の表面に接線方向に空気を吹き付けて付着スラグを除去し、回転ドラム12の周速を速くすることにより、磁性物側のスラグ混入率が大幅に改善されることがわかる。   FIG. 7 shows a drum having the same composition as in Example 1 (50% metal, 50% slag) at a feed rate of 0.5 t / h, 1.0 t / h, and 1.5 t / h as shown in FIG. Slag mixing rate on the magnetic material side (magnetic material discharge chute 14 side) when the magnetic material (metal) and the non-magnetic material (slag) are separated by supplying to the magnetic separator 10 and changing the peripheral speed of the rotary drum 12 It is a figure which shows (%). Here, slag adhered by blowing air in a tangential direction from the air nozzle 22 disposed below the surface of the rotary drum 12 is removed. Curve A is 1.5 t / h, curve B is 1.0 t / h, and curve C is 0.5 t / h. As shown in the figure, the slag mixing rate on the magnetic material side is greatly improved by blowing the air tangentially to the surface of the rotating drum 12 to remove the adhered slag and increasing the peripheral speed of the rotating drum 12. I understand.

図8は混合物として、(1)メタル25%、スラグ75%、(2)メタル50%、スラグ50%、(3)メタル75%、スラグ25%の3種類の混合物を供給速度1.0t/hで図2に示す構成のドラム型磁選機10に供給し、磁性物側のスラグ混入率を1.0%以下にするための回転ドラム12の周速を求めた。(1)の場合は周速125m/min、(2)の場合は周速80m/min、(3)の場合は周速50m/minで、磁性物側のスラグ混入率が1.0%以下になる。これにより、メタルの含有率に応じてドラム型磁選機10の回転ドラム12の周速を変化させることにより磁性物側のスラグ混入率を低減させることができることがわかる。   FIG. 8 shows a mixture of (1) 25% metal, 75% slag, (2) 50% metal, 50% slag, and (3) 75% metal, 25% slag. 2 was supplied to the drum type magnetic separator 10 having the configuration shown in FIG. 2, and the peripheral speed of the rotating drum 12 for obtaining the slag mixing ratio on the magnetic material side to 1.0% or less was obtained. In the case of (1), the peripheral speed is 125 m / min. In the case of (2), the peripheral speed is 80 m / min. In the case of (3), the peripheral speed is 50 m / min. become. Thereby, it turns out that the slag mixing rate by the side of a magnetic material can be reduced by changing the peripheral speed of the rotating drum 12 of the drum type magnetic separator 10 according to the metal content.

図9は図4に示すような構成の廃棄物溶融処理設備において、出滓口35の近傍に監視カメラを設置し、該監視カメラで溶融炉30の炉体を傾動させ炉体内に滞留している溶融物が出滓口35から排出される状態を撮影し、図3の制御装置25で該監視カメラからの画像信号を画像処理し、溶融物の排出速度を検出し、その排出速度に応じて、図3のドラム型磁選機10の回転ドラム12の周速を変化させた場合と、変化させない場合で磁性物(メタル)と非磁性物(スラグ)を分離させた場合の磁性物側のスラグ混入率を示す図である。図示するように、従来のように回転ドラム12の周速を100m/minで一定にした場合、磁性物側のスラグ混入率が26%であるのに対し、本発明のように回転ドラム12の周速を50m/min〜100m/minの範囲で可変した場合、磁性物側のスラグ混入率が3.3%と大幅に改善できる。   FIG. 9 shows a waste melting treatment facility configured as shown in FIG. 4. A monitoring camera is installed in the vicinity of the spout 35, and the furnace body of the melting furnace 30 is tilted by the monitoring camera and stays in the furnace body. The state in which the molten material is discharged from the spout 35 is photographed, and the image signal from the monitoring camera is image-processed by the control device 25 in FIG. 3, the discharge speed of the melt is detected, and according to the discharge speed Thus, when the peripheral speed of the rotating drum 12 of the drum type magnetic separator 10 in FIG. 3 is changed and when the peripheral speed is not changed, the magnetic material (metal) and the non-magnetic material (slag) are separated on the magnetic material side. It is a figure which shows a slag mixing rate. As shown in the figure, when the peripheral speed of the rotating drum 12 is constant at 100 m / min as in the prior art, the slag mixing rate on the magnetic material side is 26%, whereas the rotating drum 12 of the rotating drum 12 as in the present invention. When the peripheral speed is varied in the range of 50 m / min to 100 m / min, the slag mixing rate on the magnetic material side can be greatly improved to 3.3%.

以上本発明の実施形態を説明したが、本発明は上記実施形態に限定されるものではなく、特許請求の範囲、及び明細書と図面に記載された技術的思想の範囲内において種々の変形が可能である。例えば、図2に示すドラム型磁選機10ではドラム下方に設置したエアノズルから、回転ドラム12の表面に接線方向に圧力空気21を噴出したが、回転ドラム12の表面に付着した非磁性物であるスラグを効果的に除去できるのであれば、接線方向に限定されるものではない。また、混合物の供給速度に応じて回転ドラム周速を変えること、回転ドラム表面に圧力空気を吹き付けること、回転ドラム表面に下方から接線方向に圧力空気を吹き付けることの二つ以上を組合せて、本発明に係る磁性・非磁性物分離方法及び装置を構成してもよい。   Although the embodiments of the present invention have been described above, the present invention is not limited to the above-described embodiments, and various modifications can be made within the scope of the technical idea described in the claims and the specification and drawings. Is possible. For example, in the drum type magnetic separator 10 shown in FIG. 2, the pressure air 21 is ejected tangentially to the surface of the rotating drum 12 from the air nozzle installed below the drum, but is a non-magnetic material attached to the surface of the rotating drum 12. The tangential direction is not limited as long as the slag can be effectively removed. Also, the combination of two or more of changing the peripheral speed of the rotating drum according to the supply speed of the mixture, spraying the pressure air on the surface of the rotating drum, and blowing the pressure air tangentially from below on the surface of the rotating drum, You may comprise the magnetic and nonmagnetic substance separation method and apparatus which concern on invention.

従来のドラム型磁選機の構成を示す図で、図1(a)は側断面図、図1(b)は内部正面図である。It is a figure which shows the structure of the conventional drum type magnetic separator, Fig.1 (a) is a sectional side view, FIG.1 (b) is an internal front view. 本発明に係るドラム型磁選機の構成を示す図で、図2(a)は側断面図、図2(b)は内部正面図である。It is a figure which shows the structure of the drum type magnetic separator which concerns on this invention, Fig.2 (a) is a sectional side view, FIG.2 (b) is an internal front view. 本発明に係るドラム型磁選機の駆動制御部の構成例を示す図である。It is a figure which shows the structural example of the drive control part of the drum type magnetic separator which concerns on this invention. 本発明に係る磁性・非磁性物分離装置を使用する廃棄物溶融処理設備の全体構成例を示す図である。It is a figure which shows the example of whole structure of the waste-melting processing equipment which uses the magnetic / non-magnetic material separation apparatus which concerns on this invention. 本発明に係るドラム型磁選機と従来のドラム型磁選機の磁性物側スラグ混入率の比較例を示す図である(実施例1)。It is a figure which shows the comparative example of the magnetic material side slag mixing rate of the drum type magnetic separator which concerns on this invention, and the conventional drum type magnetic separator (Example 1). 本発明に係るドラム型磁選機における磁性物側スラグ混入率とドラム周速の関係を示す図である(実施例2)。(Example 2) which is a figure which shows the relationship between the magnetic material side slag mixing rate and drum peripheral speed in the drum type magnetic separator which concerns on this invention. 本発明に係るドラム型磁選機における磁性物側スラグ混入率とドラム周速の関係を示す図である(実施例3)。(Example 3) which is a figure which shows the relationship between the magnetic material side slag mixing rate and drum peripheral speed in the drum type magnetic separator which concerns on this invention. ドラム型磁選機における磁性物側スラグ混入率を所定の値にするための磁性物と非磁性物の混合割合とドラム周速の関係を示す図である(実施例4)。(Example 4) which is a figure which shows the relationship between the mixing ratio of the magnetic material and nonmagnetic material, and drum peripheral speed for making the magnetic material side slag mixing rate into a predetermined value in a drum type magnetic separator. ドラム型磁選機におけるドラム周速一定(従来技術)とドラム周速可変(本願発明)の場合の磁性物側スラグ混入率を示す図である(実施例5)。(Example 5) which is a figure which shows the magnetic material side slag mixing rate in the case of drum peripheral speed constant (prior art) and drum peripheral speed variable (this invention) in a drum type magnetic separator.

符号の説明Explanation of symbols

10 ドラム型磁選機
11 ケーシング
12 回転ドラム
13 仕切板
14 磁性物排出シュート
15 非磁性物排出シュート
16 磁石
17 投入ポッパー
18 メタル
19 スラグ
20 混合物
21 圧力空気
22 エアノズル
23 モータ
24 モータ駆動装置
25 制御装置
26 センサ
27 メタルバケット
28 スラグ搬送コンベア
30 溶融炉
31 プラズマトーチ
32 焼却灰投入口
33 焼却灰
34 プラズマアーク
35 出滓口
36 ガス出口
37 混合物
39 排ガス
40 スラグ分離コンベア
41 水砕水槽
42 コンベヤ
50 スラグヤード
DESCRIPTION OF SYMBOLS 10 Drum type magnetic separator 11 Casing 12 Rotating drum 13 Partition plate 14 Magnetic substance discharge chute 15 Nonmagnetic substance discharge chute 16 Magnet 17 Input popper 18 Metal 19 Slag 20 Mixture 21 Pressure air 22 Air nozzle 23 Motor 24 Motor drive device 25 Control device 26 Sensor 27 Metal bucket 28 Slag conveyor 30 Melting furnace 31 Plasma torch 32 Incineration ash inlet 33 Incineration ash 34 Plasma arc 35 Outlet 36 Gas outlet 37 Mixture 39 Exhaust gas 40 Slag separation conveyor 41 Granulated water tank 42 Conveyor 50 Slag yard

Claims (11)

ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離方法において、
前記混合物の供給速度に応じて前記ドラム型磁選機のドラムの周速を変化させ、磁性物と非磁性物を分離することを特徴とする磁性・非磁性物分離方法。
In a magnetic / non-magnetic material separation method comprising a drum-type magnetic separator, and separating a magnetic material and a non-magnetic material from a mixture of melted and ground magnetic material and non-magnetic material supplied to the drum-type magnetic separator,
A magnetic / non-magnetic material separation method characterized in that a magnetic material and a non-magnetic material are separated by changing a peripheral speed of the drum of the drum type magnetic separator according to a supply speed of the mixture.
ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離方法において、
前記ドラム型磁選機のドラム表面に圧力空気を吹き付け、磁性物と非磁性物を分離することを特徴とする磁性・非磁性物分離方法。
In a magnetic / non-magnetic material separation method comprising a drum-type magnetic separator, and separating a magnetic material and a non-magnetic material from a mixture of melted and ground magnetic material and non-magnetic material supplied to the drum-type magnetic separator,
A method for separating magnetic and non-magnetic materials, characterized in that pressurized air is blown onto the drum surface of the drum type magnetic separator to separate magnetic and non-magnetic materials.
ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離方法において、
前記ドラム型磁選機のドラム表面に圧力空気を該ドラム下方から接線方向に吹き付け、磁性物と非磁性物を分離することを特徴とする磁性・非磁性物分離方法。
In a magnetic / non-magnetic material separation method comprising a drum-type magnetic separator, and separating a magnetic material and a non-magnetic material from a mixture of melted and ground magnetic material and non-magnetic material supplied to the drum-type magnetic separator,
A magnetic / non-magnetic material separation method characterized in that pressure air is blown tangentially from below the drum surface of the drum type magnetic separator to separate a magnetic material and a non-magnetic material.
ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離方法において、
前記混合物の供給速度に応じてドラム型磁選機のドラムの周速を変化させること、該ドラム表面に圧力空気を吹き付けること、該ドラム表面に下方から接線方向に圧力空気を吹き付けることのいずれか二つ以上を組合せ磁性物と非磁性物を分離することを特徴とする磁性・非磁性物分離方法。
In a magnetic / non-magnetic material separation method comprising a drum-type magnetic separator, and separating a magnetic material and a non-magnetic material from a mixture of melted and ground magnetic material and non-magnetic material supplied to the drum-type magnetic separator,
Any one of changing the peripheral speed of the drum of the drum type magnetic separator according to the supply speed of the mixture, blowing the pressure air on the drum surface, and blowing the pressure air tangentially from below on the drum surface A magnetic / non-magnetic material separation method characterized by separating two or more magnetic materials and non-magnetic materials.
ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離装置において、
前記混合物の供給速度を検出する速度検出手段と、前記ドラム型磁選機のドラムの周速を制御する制御手段を設け、
前記制御手段は前記速度検出手段で検出した混合物の供給速度に応じて、ドラムの周速を変化させ、磁性物と非磁性物を分離することを特徴とする磁性・非磁性物分離装置。
In a magnetic / non-magnetic material separation apparatus comprising a drum-type magnetic separator and separating magnetic material and non-magnetic material from a mixture of melted and ground magnetic material and non-magnetic material supplied to the drum-type magnetic separator,
A speed detecting means for detecting the supply speed of the mixture, and a control means for controlling the peripheral speed of the drum of the drum type magnetic separator;
The magnetic / non-magnetic material separating apparatus characterized in that the control means changes the peripheral speed of the drum in accordance with the supply speed of the mixture detected by the speed detecting means to separate the magnetic material and the non-magnetic material.
ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離装置において、
前記ドラム型磁選機のドラム表面に圧力空気を吹き付ける圧力空気吹付手段を設け、該ドラム表面に圧力空気を吹き付け、磁性物と非磁性物を分離することを特徴とする磁性・非磁性物分離装置。
In a magnetic / non-magnetic material separation apparatus comprising a drum-type magnetic separator and separating magnetic material and non-magnetic material from a mixture of melted and ground magnetic material and non-magnetic material supplied to the drum-type magnetic separator,
A magnetic / non-magnetic material separating apparatus comprising pressure air blowing means for blowing pressure air onto a drum surface of the drum type magnetic separator, and blowing the pressure air onto the drum surface to separate a magnetic material and a non-magnetic material. .
ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離装置において、
前記ドラム型磁選機のドラム表面に該ドラム下方から接線方向に圧力空気を吹き付ける圧力空気吹付手段を設け、該ドラム表面に圧力空気を吹き付け、磁性物と非磁性物を分離することを特徴とする磁性・非磁性物分離装置。
In a magnetic / non-magnetic material separation apparatus comprising a drum-type magnetic separator and separating magnetic material and non-magnetic material from a mixture of melted and ground magnetic material and non-magnetic material supplied to the drum-type magnetic separator,
The drum type magnetic separator is provided with pressure air blowing means for blowing pressure air in a tangential direction from below the drum, and pressure air is blown to the drum surface to separate a magnetic material and a non-magnetic material. Magnetic / non-magnetic separation device.
ドラム型磁選機を具備し、該ドラム型磁選機に供給される溶融水砕固化された磁性物と非磁性物の混合物から磁性物と非磁性物を分離する磁性・非磁性物分離装置において、
前記混合物の供給速度を検出し、該検出した混合物の供給速度に応じて前記ドラム型磁選機のドラムの回転速度を制御する制御手段と、該ドラム表面に圧力空気を吹き付ける圧力空気吹付手段と、該ドラム表面に該ドラム下方から接線方向に圧力空気を吹き付ける圧力空気吹付手段のいずれか二つ以上を組合せ、磁性物と非磁性物を分離することを特徴とする磁性・非磁性物分離装置。
In a magnetic / non-magnetic material separation apparatus comprising a drum-type magnetic separator and separating magnetic material and non-magnetic material from a mixture of melted and ground magnetic material and non-magnetic material supplied to the drum-type magnetic separator,
Control means for detecting the supply speed of the mixture and controlling the rotation speed of the drum of the drum type magnetic separator according to the detected supply speed of the mixture; and pressure air spraying means for blowing pressure air onto the drum surface; A magnetic / non-magnetic substance separating apparatus characterized by combining any two or more of pressure air blowing means for blowing pressure air tangentially from below the drum surface to the drum surface to separate the magnetic substance and the non-magnetic substance.
請求項5又は8に記載の磁性・非磁性物分離装置において、
前記混合物の供給速度を検出する速度検出手段は、監視カメラの画像処理信号、又は温度計の検出出力、サーモカメラの検出出力のいずれか一つ、又は二つ以上の組合せから混合物の供給速度を検出することを特徴とする磁性・非磁性物分離装置。
The magnetic / non-magnetic material separating apparatus according to claim 5 or 8,
The speed detection means for detecting the supply speed of the mixture is configured to determine the supply speed of the mixture from one of the image processing signal of the monitoring camera, the detection output of the thermometer, the detection output of the thermo camera, or a combination of two or more. Magnetic and non-magnetic material separation device characterized by detecting.
請求項9に記載の磁性・非磁性物分離装置において、
前記監視カメラ、温度計、サーモカメラは溶融状態の混合物が排出される排出口、溶融状態の混合物を水砕する水砕シュート部に設けたことを特徴とする磁性・非磁性物分離装置。
The magnetic / non-magnetic material separating apparatus according to claim 9,
The magnetic / non-magnetic material separating apparatus according to claim 1, wherein the monitoring camera, the thermometer, and the thermo camera are provided in a discharge port through which the molten mixture is discharged, and in a water granulation chute unit that granulates the molten mixture.
廃棄物を溶融する溶融炉、該溶融炉から排出される溶融物を水砕固化した水砕スラグを製造するスラグ製造装置、該スラグ製造装置から排出された水砕スラグを磁性物と非磁性物に分離する磁性・非磁性物分離装置を備えた廃棄物溶融処理設備において、
前記磁性・非磁性物分離装置に、請求項5乃至10のいずれか1項に記載の磁性・非磁性物分離装置を用いることを特徴とする廃棄物溶融処理設備。
A melting furnace for melting waste, a slag manufacturing apparatus for manufacturing a granulated slag obtained by granulating and solidifying a melt discharged from the melting furnace, a granulated slag discharged from the slag manufacturing apparatus as a magnetic material and a non-magnetic material In a waste melting treatment facility equipped with a magnetic / non-magnetic material separation device
11. A waste melting treatment facility using the magnetic / nonmagnetic substance separation device according to any one of claims 5 to 10 as the magnetic / nonmagnetic substance separation apparatus.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102527508A (en) * 2011-12-14 2012-07-04 柳州市远健磁力设备制造有限责任公司 Method for recovering aluminum and iron from metal scraps produced by cutting by wet magnetic separation
WO2019054087A1 (en) * 2017-09-14 2019-03-21 日新製鋼株式会社 Steelmaking slag magnetic separation method and steelmaking slag magnetic separation apparatus
CN109847926A (en) * 2019-01-11 2019-06-07 孙树春 A kind of dry type wind magnetic separator and its application method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
MX2018015034A (en) * 2016-06-06 2019-03-06 Sintokogio Ltd Separator apparatus and shot processing apparatus.

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5038866A (en) * 1973-07-16 1975-04-10 Atomenergi Ab
JPH04131151A (en) * 1990-09-25 1992-05-01 Tohoku Electric Power Co Inc Removing device for iron piece in bulk material
JPH05123605A (en) * 1991-11-06 1993-05-21 Sumitomo Metal Ind Ltd Method for recovering ground metal contained in slag
JPH0985124A (en) * 1995-09-26 1997-03-31 Hitachi Zosen Corp Magnetic force separator
JPH11179334A (en) * 1997-12-19 1999-07-06 Nkk Corp Method and apparatus for collecting slag from melt of waste melting furnace
JP2003145123A (en) * 2001-11-14 2003-05-20 Kawasaki Heavy Ind Ltd Method for reforming slag and device therefor

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5038866A (en) * 1973-07-16 1975-04-10 Atomenergi Ab
JPH04131151A (en) * 1990-09-25 1992-05-01 Tohoku Electric Power Co Inc Removing device for iron piece in bulk material
JPH05123605A (en) * 1991-11-06 1993-05-21 Sumitomo Metal Ind Ltd Method for recovering ground metal contained in slag
JPH0985124A (en) * 1995-09-26 1997-03-31 Hitachi Zosen Corp Magnetic force separator
JPH11179334A (en) * 1997-12-19 1999-07-06 Nkk Corp Method and apparatus for collecting slag from melt of waste melting furnace
JP2003145123A (en) * 2001-11-14 2003-05-20 Kawasaki Heavy Ind Ltd Method for reforming slag and device therefor

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102527508A (en) * 2011-12-14 2012-07-04 柳州市远健磁力设备制造有限责任公司 Method for recovering aluminum and iron from metal scraps produced by cutting by wet magnetic separation
WO2019054087A1 (en) * 2017-09-14 2019-03-21 日新製鋼株式会社 Steelmaking slag magnetic separation method and steelmaking slag magnetic separation apparatus
CN109847926A (en) * 2019-01-11 2019-06-07 孙树春 A kind of dry type wind magnetic separator and its application method

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