JPS6261641B2 - - Google Patents

Info

Publication number
JPS6261641B2
JPS6261641B2 JP6597778A JP6597778A JPS6261641B2 JP S6261641 B2 JPS6261641 B2 JP S6261641B2 JP 6597778 A JP6597778 A JP 6597778A JP 6597778 A JP6597778 A JP 6597778A JP S6261641 B2 JPS6261641 B2 JP S6261641B2
Authority
JP
Japan
Prior art keywords
magnetic
sieve
metal
magnetic separator
passed
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
JP6597778A
Other languages
Japanese (ja)
Other versions
JPS54157380A (en
Inventor
Yoshio Watabe
Takeo Taniguchi
Shigenobu Matsumoto
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.)
Nippon Jiryoku Senko Co Ltd
Original Assignee
Nippon Jiryoku Senko 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 Jiryoku Senko Co Ltd filed Critical Nippon Jiryoku Senko Co Ltd
Priority to JP6597778A priority Critical patent/JPS54157380A/en
Publication of JPS54157380A publication Critical patent/JPS54157380A/en
Publication of JPS6261641B2 publication Critical patent/JPS6261641B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies

Description

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

本発明は、製鉄所における高炉,製鋼炉(主と
して転炉)から生じるスラグから高品位の地金を
回収するとともに、その他即ち地金を除いた残留
物を利用用途にあつたサイズにするスラグの処理
方法に関するものである。 従来これらの各種スラグ類は、これらを埋立に
用いたり、大塊地金を手選で回収する等して、残
りの大半の部分はまだ地金が相当残存するままの
状態で廃棄されていた。 本願出願人は、先にこれらのスラグ類から地金
を回収する方法として、該スラグをロツドミルに
よる破砕と磁選を繰返すことにより、地金を回収
する方法を開発し、実施して来たが、破砕を繰返
されるスラグがある程度(約10mm)以下に細かく
なると、ロツドミル若しくはボールミルによる破
砕では、スラグ中にある地金とその他の物との分
離が、ある限度以上には達し難いこと、更に破砕
を行うにしても磁選を行うにしてもサイズ別に行
う方が効率が良いと共に地金を分別回収した残留
物をその後路盤材、土質改良資材又はセメント副
原料等に利用する場合に有効であるということを
見い出した。下記の第1表にスラグの用途とその
規格、需要動向の概要を示す。
The present invention aims to recover high-grade ingots from slag produced from blast furnaces and steelmaking furnaces (mainly converters) in steel plants, and to convert the remaining material other than ingots into sizes suitable for the intended use. This relates to a processing method. In the past, these various types of slag were used for landfill, or large chunks of bullion were collected by hand, and most of the remaining portion was disposed of with a considerable amount of bullion still remaining. . The applicant of the present application has previously developed and implemented a method for recovering bullion from these slags by repeatedly crushing the slag with a rod mill and magnetic separation. When slag that has been repeatedly crushed becomes finer than a certain level (approximately 10 mm), it is difficult to separate the metal in the slag from other materials beyond a certain limit when crushing with a rod mill or ball mill. Whether it is magnetic separation or magnetic separation, it is more efficient to separate the metal by size, and it is also effective when the residue after separately recovering the metal is used as roadbed material, soil improvement material, or cement auxiliary raw material. I found out. Table 1 below outlines the uses of slag, its standards, and demand trends.

【表】 以上の様な目的を達成するために研究開発した
のが本願であり、その要旨とするところは、次の
各工程より成る製鉄所より発生するスラグ処理方
法。 第1工程:粗砕後大塊地金を除したスラグを25〜
120mm目の所要段数の篩にかけてサイ
ズ別に分け、各サイズ群毎に各別に磁
選機にかけて磁性物を回収し、各磁選
機に於ける非磁着物はその後破砕機に
よる破砕を行い各一段小サイズ群を磁
選する磁選機へまわし地金を回収する
という操作を最終非磁着物が約25mm以
下となるまで繰返す。 第工程:第1工程で得られる磁着物の中約25mm
未満のものは約15mm目の篩で篩別し、
篩下物は更に磁選機にかけて磁性物を
分離し、該15mm未満の磁着物は乾燥後
1〜3mm目の篩にかけて篩別する。 第工程:第工程の非磁着物と、第工程の非
磁着物とをセメント副原料や路盤材に
適したサイズ毎に分別する。 第工程:第工程で得られる磁着物中約15mm以
上のものと、第工程で得られる磁着
物とをロツドミルにかけて磨砕後約10
mm目の篩にかけて篩上物は磁選機にか
けて地金を回収し篩下物は更に1〜3
mm目の篩にかける。 第工程:第工程に於ける1〜3mm目の篩の篩
上物は高速度で被投射体もしくは篩上
物同士を投射衝突せしめる操作を所要
回数行うことにより、地金とその他の
部分との分離を図り地金は回収し該そ
の他の部分は、第工程に於ける1〜
3mm目の篩の篩下物及び第工程に於
ける1〜3mm目の篩の篩下物と共に磁
選機にかけて磁選別を行い地金を回収
する。 である。 以下本願方法の一実施例を図面に示すフローシ
ートを参酌しながら詳述すれば、原料1となるス
ラグは先ずグリズリーのような篩別機2により大
塊地金を回収した後、25mmと100mmの2段の篩に
かけて、100mm以上は直ちに磁選機3にかけ、地
金を回収しその時の非磁着物は油圧装置付きジヨ
ークラツシヤー4にかけて破砕と同時に地金と地
金以外のものとの単体分離を行う。 ジヨークラツシヤー4のセツト間隔より大きな
地金が混入している場合は、噛込み現象が起ると
同時に油圧装置に連動したダンパーが応動して、
大塊地金を系外へ回収する。 30〜100mmサイズのものは先の非磁着物と共に
磁選機5で磁選、次いでコーン破砕機6で破砕を
行い、最初の25mm目の篩の篩下物と混合して磁選
機7で磁選を行う。この場合下限を25mm目の篩と
したのはスラグから地金を回収した残りのものを
有効に活用するのに、その大きさが25mm位が適し
ているので、25mmとしたのであるが、地金を回収
するという目的の為だけならば、もつと小さい方
が望ましいが、効率的には低下する。 この様にして磁選機7で磁選された磁着物は15
mm目の篩8で篩別し篩上物を回収し篩下物は該磁
着物中に再度磁選機9にかけて巻込まれている非
磁性物を除去し該磁着物自体の品位を向上する。 なお、この場合の非磁着物は篩10で用途別に
分ける。 次いで15mm未満の磁着物中には水分が約5〜7
%含まれているので乾燥機11により乾燥して水
分を約2%以下に減少せしめた後1〜3mm目の篩
12で篩別して篩上物は前工程で得られた15mm以
上の磁着物の方へまわし、篩下物は磁選機13に
より磁選別して地金を回収する。一方篩12より
まわされて来た磁着物と15mm以上の磁着物とはロ
ツドミル14により破砕及び地金とその他の部分
との単体分離を行つた後10mm目の篩15で篩別し
篩上物は磁選機16にかけて地金を回収し、篩下
物は更に2mm目の篩17にかけて篩別し、この場
合の篩上物は篩上物同士あるいは該篩上物を壁等
に高速で投射せしめる装置18により、地金とそ
の他の部分とを分離せしめる操作を4回繰返し、
単体分離を行い地金を回収し、その他の部分は磁
選機13によつて磁選し地金を回収する。 以上の工程で処理した場合のスラグ及び地金、
その他の部分の量的割合等を第2図に示すフロー
シート中に重量%をもつて表現する。 本願発明方法によれば、スラグ中の有価成分た
る地金は高品位で回収が行えると共に、その残の
残留物もセメント副原料や路盤材として有効に活
用できるし、工程が一環して乾式で行われる為に
設備費が安価であると共に管理が容易に行えると
いう効果がある。
[Table] This application has been researched and developed to achieve the above objectives, and its gist is a method for treating slag generated from steel works, which consists of the following steps. 1st process: 25~
Sort by size by passing through a sieve with the required number of 120 mm stages, and collect the magnetic materials by passing each size group through a magnetic separator separately.The non-magnetic materials in each magnetic separator are then crushed by a crusher to separate them into smaller size groups. The process of sending the metal to a magnetic separator to collect the metal is repeated until the final non-magnetized material is approximately 25 mm or less. 1st process: Approximately 25mm inside the magnetic material obtained in the 1st process
Those with a diameter of less than
The sieved material is further passed through a magnetic separator to separate magnetic materials, and the magnetic material less than 15 mm is dried and then sieved through a 1 to 3 mm sieve. 1st step: The non-magnetic material of the 1st step and the non-magnetic material of the 1st step are separated into sizes suitable for cement auxiliary raw materials and roadbed materials. 1st step: The magnetic material obtained in the 1st step with a diameter of about 15 mm or more and the magnetic material obtained in the 1st step are ground by a rod mill for about 10 min.
The material on the sieve is passed through a mm-th sieve, and the material on the sieve is passed through a magnetic separator to recover the metal, and the material on the sieve is further 1 to 3
Pass through a mm sieve. 1st step: In the 1st step, the material on the sieve of 1 to 3 mm sieves is separated from the base metal and other parts by performing an operation of projecting objects or objects on the sieve at high speed and colliding them a required number of times. The metal is separated and the other parts are collected in steps 1 to 1 in the first process.
The material under the 3 mm sieve and the material under the sieve from the 1 to 3 mm sieves in the first step are passed through a magnetic separator to perform magnetic separation and recover the metal. It is. An embodiment of the method of the present application will be described in detail below with reference to the flow sheet shown in the drawings. The slag that becomes the raw material 1 is first collected by a sieve 2 like a Grizzly, and then 25 mm and 100 mm 100 mm or more is immediately passed through a magnetic separator 3 to recover the bullion, and the non-magnetic material is passed through a geocrusher 4 equipped with a hydraulic device to crush and simultaneously separate the bullion and other materials into single pieces. Perform separation. If there is metal mixed in that is larger than the set interval of the jaw crusher 4, the jamming phenomenon occurs and at the same time a damper linked to the hydraulic system responds.
Collect large bullion out of the system. 30 to 100 mm size items are magnetically separated together with the non-magnetic material in magnetic separator 5, then crushed in cone crusher 6, mixed with the under-sieve material of the first 25 mm sieve, and magnetically separated in magnetic separator 7. . In this case, the lower limit was set as 25 mm because a size of about 25 mm is suitable for effectively utilizing the remaining metal recovered from the slag. If it is only for the purpose of collecting gold, it is better to have a smaller size, but it will be less efficient. The number of magnetic substances magnetically separated in this way by the magnetic separator 7 is 15.
The material is sieved through a mm-th sieve 8 to recover the upper material, and the material under the sieve is passed through the magnetic separator 9 again to remove non-magnetic substances entangled in the magnetic material and improve the quality of the magnetic material itself. In this case, the non-magnetic substances are separated by use using a sieve 10. Next, moisture content in magnetic objects less than 15 mm is approximately 5 to 7 mm.
%, so it is dried in a dryer 11 to reduce the water content to about 2% or less, and then sieved with a 1 to 3 mm sieve 12.The sieved material is the magnetic material of 15 mm or more obtained in the previous step. The unsifted material is magnetically separated by a magnetic separator 13 to recover the metal. On the other hand, the magnetic material passed through the sieve 12 and the magnetic material larger than 15 mm are crushed by a rod mill 14 and separated from the base metal and other parts, and then sieved by a 10 mm sieve 15 to remove the sieved material. The ingots are recovered by passing through a magnetic separator 16, and the unsifted material is further sieved through a 2 mm sieve 17, and in this case, the sieved materials are projected onto each other or the sieved materials at high speed onto a wall, etc. Using the device 18, the operation of separating the bullion from the other parts is repeated four times,
Individual parts are separated to recover the metal, and other parts are magnetically separated by a magnetic separator 13 to recover the metal. Slag and metal when processed through the above process,
The quantitative proportions of other parts are expressed in weight percentages in the flow sheet shown in FIG. According to the method of the present invention, ingots, which are valuable components in slag, can be recovered in high quality, and the remaining residue can be effectively used as a cement auxiliary raw material or roadbed material, and the entire process is a dry process. Since this method is carried out, equipment costs are low and management is easy.

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

第1図は本願方法の一実施例のフローシート、
第2図は同量的割合を示す説明図、第3図は同配
置図。 図中、1:原料、2:篩別機、3:磁選機、
4:ジヨークラツシヤー、5:磁選機、6:コー
ン破砕機、7:磁選機、8:15mm目の篩、9:磁
選機、10:篩、11:乾燥機、12:1〜3mm
目の篩、13:磁選機、14:ロツドミル、1
5:10mm目の篩、16:磁選機、17:2mm目の
篩、18:投射装置。
FIG. 1 is a flow sheet of an example of the method of the present invention.
FIG. 2 is an explanatory diagram showing the same quantitative ratio, and FIG. 3 is an illustration of the same arrangement. In the figure, 1: raw material, 2: sieving machine, 3: magnetic separator,
4: Diyo crusher, 5: Magnetic separator, 6: Corn crusher, 7: Magnetic separator, 8: 15 mm sieve, 9: Magnetic separator, 10: Sieve, 11: Dryer, 12: 1-3 mm
Eye sieve, 13: Magnetic separator, 14: Rod mill, 1
5: 10mm sieve, 16: Magnetic separator, 17: 2mm sieve, 18: Projection device.

Claims (1)

【特許請求の範囲】 1 次の各工程より成る製鉄所より発生するスラ
グ処理方法。 第1工程:粗砕後大塊地金を除したスラグを25〜
120mm目の所要段数の篩にかけてサイ
ズ別に分け、各サイズ群毎に各別に磁
選機にかけて磁性物を回収し、各磁選
機に於ける非磁着物はその後砕砕機に
よる破砕を行い、各一段小サイズ群を
磁選する磁選機へまわし地金を回収す
るという操作を最終非磁着物が約25mm
以下となるまで繰返す。 第工程:第1工程で得られる磁着物の中約25mm
未満のものは約15mm目の篩で篩別し、
篩下物は更に磁選機にかけて磁着物を
分離し、該15mm未満の磁着物は乾燥後
1〜3mm目の篩にかけて篩別する。 第工程:第工程の非磁着物と、第工程の非
磁着物とをセメント副原料路盤材に適
したサイズ毎に分別する。 第工程:第工程で得られる磁着物中約15mm以
上のものと、第工程で得られる磁着
物とをロツドミルにかけて磨砕後約10
mm目の篩にかけ篩上物は磁選機にかけ
て地金を回収し、篩下物は更に1〜3
mm目の篩にかける。 第工程:第工程に於ける1〜3mm目の篩の篩
上物は高速度で被投射体もしくは篩上
物同士を投射衝突せしめる操作を所要
回数行うことにより、地金とその他の
部分との分離を図り地金は回収し、該
その他の部分は第工程に於ける1〜
3mm目の篩の篩下物及び第工程に於
ける1〜3mm目の篩の篩下物と共に磁
選機にかけて磁選別を行い地金を回収
する。
[Claims] 1. A method for treating slag generated from a steelworks, which comprises the following steps: 1st process: 25~
Sort by size by passing through a sieve with the required number of 120 mm stages, and collect the magnetic materials by passing each size group through a magnetic separator separately.The non-magnetic materials in each magnetic separator are then crushed by a crusher, and each size is one step smaller. The final non-magnetic material is about 25mm after the operation of sending the group to a magnetic separator to collect the metal.
Repeat until below. 1st process: Approximately 25mm inside the magnetic material obtained in the 1st process
Those with a diameter of less than
The sieved material is further passed through a magnetic separator to separate the magnetic substances, and the magnetic substances smaller than 15 mm are dried and then sieved through a 1 to 3 mm sieve. 1st step: The non-magnetic material of the 1st step and the non-magnetic material of the 1st step are separated into sizes suitable for cement sub-raw material roadbed material. 1st step: The magnetic material obtained in the 1st step with a diameter of about 15 mm or more and the magnetic material obtained in the 1st step are ground by a rod mill for about 10 min.
The material on the sieve is passed through a mm-th sieve, and the material on the sieve is passed through a magnetic separator to recover the metal, and the material on the sieve is further 1 to 3
Pass through a mm sieve. 1st step: In the 1st step, the material on the sieve of 1 to 3 mm sieves is separated from the base metal and other parts by performing an operation of projecting objects or objects on the sieve at high speed and colliding them a required number of times. The metal is separated and the other parts are collected from steps 1 to 1 in the first process.
The material under the 3 mm sieve and the material under the sieve from the 1 to 3 mm sieves in the first step are passed through a magnetic separator to perform magnetic separation and recover the metal.
JP6597778A 1978-05-31 1978-05-31 Method of disposing slag formed from iron mill Granted JPS54157380A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6597778A JPS54157380A (en) 1978-05-31 1978-05-31 Method of disposing slag formed from iron mill

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6597778A JPS54157380A (en) 1978-05-31 1978-05-31 Method of disposing slag formed from iron mill

Publications (2)

Publication Number Publication Date
JPS54157380A JPS54157380A (en) 1979-12-12
JPS6261641B2 true JPS6261641B2 (en) 1987-12-22

Family

ID=13302563

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6597778A Granted JPS54157380A (en) 1978-05-31 1978-05-31 Method of disposing slag formed from iron mill

Country Status (1)

Country Link
JP (1) JPS54157380A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01164940U (en) * 1988-05-12 1989-11-17

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITMI20050539A1 (en) * 2005-04-01 2006-10-02 Techint Spa METHOD AND APPARATUS FOR THE RECOVERY OF REFRACTORY MATERIALS OF RESULTS AND SORRIES FROM SIVIERA AS PROCESS SCORES IN STEEL PRODUCTION IN EAF AND ITS RELATED DOSAGE FOR THE FORMATION OF PROCESS SCORIA
US9016477B2 (en) * 2012-03-19 2015-04-28 Mid-American Gunite, Inc. Method and system for processing slag material

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5317511A (en) * 1976-07-30 1978-02-17 Nippon Jiriyoku Senkou Kk Slag treatment

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5317511A (en) * 1976-07-30 1978-02-17 Nippon Jiriyoku Senkou Kk Slag treatment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01164940U (en) * 1988-05-12 1989-11-17

Also Published As

Publication number Publication date
JPS54157380A (en) 1979-12-12

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