JP2012006771A - Wet classification equipment for steel slag - Google Patents

Wet classification equipment for steel slag Download PDF

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JP2012006771A
JP2012006771A JP2010141681A JP2010141681A JP2012006771A JP 2012006771 A JP2012006771 A JP 2012006771A JP 2010141681 A JP2010141681 A JP 2010141681A JP 2010141681 A JP2010141681 A JP 2010141681A JP 2012006771 A JP2012006771 A JP 2012006771A
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slag
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steel slag
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JP5321845B2 (en
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Kohei Yoneda
耕平 米田
Masatoshi Otsuka
正俊 大塚
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Nippon Steel Corp
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Sumitomo Metal Industries Ltd
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    • 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
    • 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
    • Y02W30/52Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly

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  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
  • Furnace Details (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide equipment which when steel slag is crushed and sized, efficiently removes and classifies fine powder sticking to a steel slag surface.SOLUTION: Wet classification equipment for steel slag includes wet sieves 14, 16 for classifying crushed and sized steel slag and a wet cyclone 18 for centrifugally separating particles having a smaller particle size and a smaller specific gravity than undersize particles through the wet sieves 14, 16 from the sieved particles. Since fine powder sticking to a steel slag surface is efficiently classified with the wet sieves and the wet cyclone, it is not necessary to carry out sieving again. Iron-containing steel slag can be subjected to efficient classification and separation into slag and iron.

Description

本発明は、高炉スラグ、製鋼スラグ等の鉄鋼スラグを湿式で分級する設備に関するもので、特に高炉スラグのうちの徐冷スラグ及び製鋼スラグのうちの脱硫スラグの有効利用が図れる湿式分級設備に関するものである。   TECHNICAL FIELD The present invention relates to an equipment for classifying steel slag such as blast furnace slag and steelmaking slag in a wet manner, and particularly to a wet classification equipment capable of effectively utilizing slow-cooled slag in blast furnace slag and desulfurization slag in steelmaking slag. It is.

製鉄所で発生する鉄鋼スラグの中で、高炉スラグ及び製鋼スラグの処理について、以下に説明する。   Processing of blast furnace slag and steelmaking slag among steel slag generated at steelworks will be described below.

高炉スラグは、高炉から出滓された溶融状態のスラグを、大量の水で急冷した水砕スラグと、徐冷した徐冷スラグに分類される。このうち、水砕スラグは、セメント原料等として有効利用され、一方、徐令スラグは、スラグ特有の潜在水硬性により強固な塊状の徐冷スラグが形成され、道路用路盤材等として有効利用されている。また、徐冷スラグは、天然石と同等の性質を持つことから、コンクリート用骨材等としても有効利用される。   The blast furnace slag is classified into a granulated slag rapidly cooled with a large amount of water and a gradually cooled slow slag discharged from the blast furnace. Of these, granulated slag is effectively used as a raw material for cement, while gradual slag is effectively used as roadbed material for roads, etc. due to the formation of strong massive slow-cooled slag due to the inherent hydraulic properties of slag. ing. Moreover, since slow cooling slag has the property equivalent to a natural stone, it is effectively used also as an aggregate for concrete.

一方、製鋼スラグは、高炉から出銑された溶銑を脱珪、脱硫、脱燐、脱炭等の予備処理を行った際に発生する脱硫スラグ、脱燐スラグ、脱炭スラグ等に分類される。これらの製鋼スラグは、路盤材等として有効利用される。また、CaO及びSiO2が多く含まれているので、製鉄所内でも再利用されている。 On the other hand, steelmaking slag is classified into desulfurization slag, dephosphorization slag, decarburization slag, etc. generated when pre-treatment such as desiliconization, desulfurization, dephosphorization, decarburization is performed on the hot metal discharged from the blast furnace. . These steelmaking slags are effectively used as roadbed materials. In addition, since it contains a lot of CaO and SiO 2, it is also reused in the steelworks.

ところで、前記高炉スラグのうち、徐冷スラグAは、例えば図3(a)に示すように、破砕整粒プラント1で処理して、粒径が40mm未満20mm以上、20mm未満5.0mm以上、5.0mm未満のものに選別している。そして、粒径が5.0mm未満の粉体は、破砕整粒プラント1の系外の篩2で、粒径が5.0mm未満2.5mm以上と2.5mm未満に篩分けしている。また、図3(b)に示すように、破砕整粒プラントの操業を変更し、破砕を繰り返して27mm未満に整粒する場合もある。   By the way, among the blast furnace slag, as shown in FIG. 3A, for example, the slow-cooled slag A is processed in the crushing and sizing plant 1, and the particle size is less than 40 mm, 20 mm or more, less than 20 mm, 5.0 mm or more, Sorted to less than 5.0mm. And the powder with a particle size of less than 5.0 mm is sieved by a sieve 2 outside the system of the crushing and sizing plant 1 into a particle size of less than 5.0 mm and 2.5 mm or more and less than 2.5 mm. Moreover, as shown in FIG.3 (b), operation of a crushing and sizing plant may be changed, and crushing may be repeated and it may be sized to less than 27 mm.

なお、前記のうち、図3(a)で説明した、粒径が40mm未満20mm以上のものはロックウール(断熱材)原料、粒径が20mm未満5.0mm以上のものはコンクリート用粗骨材として、粒径が5.0mm未満2.5mm以上のものはコンクリートブロック用骨材、粒径が2.5mm未満のものはセメント用原料として再利用している。また、図3(b)で説明した、粒径が27mm未満のものは路盤材として再利用している。以後、コンクリート用粗骨材、コンクリートブロック用骨材、セメント用原料を総称してコンクリート用骨材という。   Of the above, the rock wool (heat insulating material) material having a particle size of less than 40 mm and 20 mm or more, as described in FIG. 3A, and the coarse particle material for concrete having a particle size of less than 20 mm and 5.0 mm or more are used. As a result, the aggregates having a particle size of less than 5.0 mm and 2.5 mm or more are reused as aggregates for concrete blocks, and those having a particle size of less than 2.5 mm are reused as raw materials for cement. Moreover, the thing with a particle size of less than 27 mm demonstrated in FIG.3 (b) is reused as a roadbed material. Hereinafter, the concrete aggregate, concrete block aggregate, and cement raw material are collectively referred to as concrete aggregate.

しかしながら、このうち、特に粒径が20mm未満5.0mm以上のものは、屋内或は屋外で山積み保管している際にスラグ表面に付着している微粉が振動やスラグ同士の接触等により粒度・比重・組成等に偏りを生じ、スラグの粒度分布が変化して規定粒度分布から外れ、コンクリート用粗骨材としての品質が低下する。従って、再度、篩を実施して前記微粉を除去するようにしているが、従来、採用している乾式篩では表面に付着した微粉を効果的に除去することは難い。   However, among these, especially those with a particle size of less than 20 mm and 5.0 mm or more, the fine powder adhering to the surface of the slag during indoor or outdoor storage is piled up due to vibration, contact between slags, etc. The specific gravity, composition, etc. are biased, the slag particle size distribution changes and deviates from the specified particle size distribution, and the quality of the coarse aggregate for concrete deteriorates. Therefore, the sieving is carried out again to remove the fine powder. However, it is difficult to effectively remove the fine powder adhering to the surface with the conventional dry sieve.

また、前記製鋼スラグのうち、溶銑予備処理として実施される脱硫工程で発生する脱硫スラグBには、鉄分が多く含まれる一方、微細な炭素粉が多く含まれているので、屋外で保管した場合に粉塵飛散等の環境汚染の懸念がある。   In addition, among the steelmaking slag, the desulfurization slag B generated in the desulfurization process performed as the hot metal pretreatment includes a large amount of iron and a large amount of fine carbon powder. In addition, there are concerns about environmental pollution such as dust scattering.

従って、図4に示すように、脱硫スラグBに注水イして冷却ロ、屋内攪拌ハした後、水ピット3へ排滓ニし、外気に晒して自然乾燥(以下、風乾と称す。)ホした後、図3に示す破砕整粒プラント1で篩処理している。篩処理後は、磁選機等で脱硫スラグから鉄分を選別し、スラグは製鉄所内で再利用、鉄分は鉄原料として再利用している。また、選別された鉄分は不純物が少なく、かつ粒径サイズの揃った粒鉄であるため、高品質な鉄原料として販売できる。   Therefore, as shown in FIG. 4, water is poured into the desulfurized slag B, cooled, and stirred indoors, then drained into the water pit 3, exposed to the outside air, and naturally dried (hereinafter referred to as air drying). Then, sieving is performed in the crushing and sizing plant 1 shown in FIG. After sieving, iron is separated from desulfurized slag using a magnetic separator, etc., and the slag is reused in the steelworks and the iron is reused as an iron raw material. Moreover, since the selected iron content is granular iron with few impurities and uniform particle size, it can be sold as a high-quality iron raw material.

しかしながら、硫黄の含有量が多い脱硫スラグを、水没後に風乾して表面が乾燥した状態で篩分けしただけでは、前記回収した鉄分に硫黄分の高い粉状のスラグが固着しているので、鉄源としての品質が低い。   However, desulfurized slag with a high sulfur content is air-dried after submerging and sifted in a state where the surface is dried, so that powdered slag with a high sulfur content is fixed to the recovered iron content. Low quality as a source.

そこで、例えば特許文献1では、冷却後に粉砕機で1〜5mmに粉砕整粒した製鋼スラグ粒に、混合機を使用して炭素含有回収粉粒と鉄分含有回収粉粒を添加混合し、高炉用焼結鉱原料の一部として使用することが記載されている。   Therefore, for example, in Patent Document 1, the steel-containing slag particles that have been crushed and sized to 1 to 5 mm with a pulverizer after cooling are added to and mixed with the carbon-containing recovered particles and the iron-containing recovered particles using a mixer. It is described that it is used as a part of a raw material for sintered ore.

また、特許文献1では、前記粉砕途中に磁選機で選別除去した製鋼スラグ中に含まれる鉄分を、篩で5mm以下に篩分けして鉄分含有回収粉粒とすると共に、5mmを超えるものは転炉鉄源、転炉冷却剤等の製鋼原料の一部に使用することも記載されている。   Moreover, in patent document 1, the iron content contained in the steelmaking slag screened and removed by the magnetic separator during the pulverization is sieved to 5 mm or less with a sieve to obtain iron-containing recovered particles, and those exceeding 5 mm are rolled. It is also described that it is used as a part of steelmaking raw materials such as a furnace iron source and a converter coolant.

しかしながら、脱硫スラグを対象とする場合、スラグと鉄分の分離が十分にできていないので、回収した鉄分を溶鋼中に投入すると鋼中の硫黄分が増加し、品質低下をもたらすことは、従来と変わりがない。   However, when desulfurized slag is the target, the slag and iron content are not sufficiently separated, so when the recovered iron content is put into the molten steel, the sulfur content in the steel increases, leading to a decrease in quality. There is no change.

特開2001−192741号公報JP 2001-192741 A

鉄鋼スラグを分級する際に、本発明が解決しようとする問題点は、以下の2点である。第1は、徐冷スラグをコンクリート用骨材として破砕整粒した際に表面に付着した微粉を効果的に除去するのが難いので、保管の際に微粉が偏析し、粒度分布が変化して規定粒度分布から外れ、コンクリート用骨材の品質が低下するという点である。また、第2は、脱硫スラグは、スラグ中の硫黄分が高いので、回収された鉄分の表面には硫黄分の高いスラグが固着し、鉄源としての品質が低いという点である。   The problems to be solved by the present invention when classifying steel slag are the following two points. The first is that it is difficult to effectively remove fine powder adhering to the surface when gradual slag is crushed and sized as concrete aggregate, so that the fine powder segregates during storage and the particle size distribution changes. It is out of the specified particle size distribution and the quality of the aggregate for concrete deteriorates. Second, since desulfurized slag has a high sulfur content in the slag, a high sulfur content slag adheres to the surface of the recovered iron and the quality as an iron source is low.

本発明は、高炉スラグ、製鋼スラグ等の鉄鋼スラグを分級して有効利用する際に、上述の従来技術が有する問題点を解消するものである。   The present invention solves the above-mentioned problems of the prior art when effectively classifying and effectively using steel slag such as blast furnace slag and steelmaking slag.

すなわち、本発明の鉄鋼スラグの湿式分級設備は、微粉が偏析して保管中にコンクリート用骨材の粒度分布が変化することがなく、また、回収された鉄分の表面に硫黄分の高い脱硫スラグが固着しないようにするために、
破砕整粒或いは注水処理した鉄鋼スラグを所定の粒径に篩分けする湿式篩と、この湿式篩の篩下から、前記篩分けしたものよりも粒径が小さく比重の小さいものを遠心分離する湿式サイクロンを有することを最も主要な特徴としている。
That is, the steel slag wet classification equipment of the present invention does not change the particle size distribution of the aggregate for concrete during storage due to segregation of fine powder, and the sulfur content of the desulfurized slag is high on the recovered iron surface. To prevent the sticking
Wet sieve for sieving steel slag that has been crushed and squeezed or treated with water into a predetermined particle size, and a wet type for centrifuging a material having a particle size smaller than the sieved material and having a smaller specific gravity from the sieve under the wet sieve Having a cyclone is the main feature.

本発明の鉄鋼スラグの湿式分級設備は、湿式篩で鉄鋼スラグを所定の粒径に篩分けするので、高炉徐冷スラグの場合は、破砕整粒したコンクリート用骨材の表面に付着した微粉の除去が可能になって、再度篩分けする必要がない。また、脱硫スラグの場合は、粒鉄が多く含まれているため、湿式篩で脱硫スラグを篩分ける事により、精度良く鉄分とスラグを分離する事ができる。また、脱硫スラグから回収した鉄分の表面に硫黄分の高い粉状スラグが付着するのを抑制できて、鉄分の回収率が向上するのと共に高品質の鉄源として有効利用が図れるようになる。   The steel slag wet classification equipment of the present invention screens steel slag into a predetermined particle size with a wet sieve, so in the case of blast furnace slow-cooled slag, fine powder adhering to the surface of the crushed and sized concrete aggregate Removal is possible and there is no need to screen again. In addition, since desulfurized slag contains a large amount of granular iron, it is possible to accurately separate iron and slag by sieving the desulfurized slag with a wet sieve. Moreover, it can suppress that powdery slag with a high sulfur content adheres to the surface of the iron content collect | recovered from desulfurization slag, and the effective utilization as a high quality iron source comes to be achieved while improving the recovery rate of iron content.

本発明の鉄鋼スラグの湿式分級設備において、鉄鋼スラグが破砕整粒した高炉徐冷スラグの場合は、湿式篩の上流に磁選機を設けて、湿式篩に投入する前の高炉徐冷スラグ中の地金を選別することが望ましい。   In the steel slag wet classification equipment of the present invention, in the case of a blast furnace slow-cooled slag in which the steel slag is crushed and sized, a magnetic separator is provided upstream of the wet sieve, It is desirable to sort out bullion.

また、本発明の鉄鋼スラグの湿式分級設備において、鉄鋼スラグが注水処理した脱硫スラグの場合は、前述した様に湿式篩で脱硫スラグを篩分ける事により、精度良く鉄分とスラグを分離する事ができるが、磁選機を使用しても良い。   Moreover, in the steel slag wet classification equipment of the present invention, in the case of desulfurized slag in which the steel slag is injected, it is possible to separate the iron and slag accurately by sieving the desulfurized slag with a wet sieve as described above. Yes, a magnetic separator may be used.

本発明では、湿式篩で鉄鋼スラグを所定の粒径に篩分けするので、高炉徐冷スラグの場合、コンクリート用粗骨材の表面に付着した微粉の除去が可能になる。従って、長時間山積みして保管した場合も、規定の粒度分布範囲から外れることがない。   In the present invention, since the steel slag is sieved to a predetermined particle size by a wet sieve, fine powder adhering to the surface of the coarse aggregate for concrete can be removed in the case of a blast furnace slow-cooled slag. Therefore, even when stored for a long period of time, it does not deviate from the specified particle size distribution range.

また、同様の理由により、脱硫スラグの場合、水没後、風乾することなく湿式篩で処理するため、回収した鉄分の表面に硫黄分の高いスラグが付着するのを抑制できて、脱硫スラグと鉄分を効率良く分離回収できる。また、湿式処理のため、微細な炭素粉等の飛散も抑えることができる。   For the same reason, in the case of desulfurization slag, since it is treated with a wet sieve without being air-dried after submersion, it is possible to suppress the adhesion of high sulfur content slag to the surface of the recovered iron content. Can be separated and recovered efficiently. In addition, because of wet processing, scattering of fine carbon powder and the like can be suppressed.

鉄鋼スラグが高炉徐冷スラグの場合における本発明の湿式分級設備の一例を説明する図である。It is a figure explaining an example of the wet classification equipment of this invention in case the steel slag is a blast furnace slow cooling slag. 鉄鋼スラグが脱硫スラグの場合における本発明の湿式分級設備の一例を説明する図である。It is a figure explaining an example of the wet classification equipment of this invention in case the steel slag is desulfurization slag. 従来の高炉徐冷スラグの分級設備の一例を説明する図で、(a)は粒径が40mm未満20mm以上、20mm未満5.0mm以上、5.0mm未満のものに選別する場合、(b)は破砕を繰り返して27mm未満に整粒する場合である。It is a figure explaining an example of the classification equipment of the conventional blast furnace slow cooling slag, (a), when classifying into a thing with a particle size of less than 40 mm 20 mm or more, less than 20 mm 5.0 mm or more, and less than 5.0 mm, (b) Is a case where pulverization is repeated and the particle size is reduced to less than 27 mm. 従来の脱硫スラグの分級設備の一例を説明する図である。It is a figure explaining an example of the classification equipment of the conventional desulfurization slag.

本発明は、高炉徐冷スラグでは、破砕整粒プラントで破砕したスラグに付着した微粉を効率的に除去し、山積み保管中に粒度分布が変化せず、また、脱硫スラグでは、回収された鉄分の表面に硫黄分の高い脱硫スラグが固着しないようにするという目的を、湿式篩で鉄鋼スラグを所定の粒径に篩分けすることによって実現した。   In the blast furnace slow-cooled slag, the fine powder adhering to the slag crushed in the pulverization and sizing plant is efficiently removed, and the particle size distribution does not change during the pile storage. The purpose of preventing desulfurization slag having a high sulfur content from adhering to the surface of the steel was achieved by sieving the steel slag into a predetermined particle size with a wet sieve.

以下、本発明の鉄鋼スラグの湿式分級設備について説明する。
先ず、本発明の高炉徐冷スラグの湿式分級設備の一例を、図1を用いて説明する。
Hereinafter, the steel slag wet classification equipment of the present invention will be described.
First, an example of wet classification equipment for blast furnace slow cooling slag of the present invention will be described with reference to FIG.

Aは高炉から出滓された溶融状態のスラグを徐冷し塊状になった徐冷スラグであり、破砕整粒プラント1で、粒径が例えば40mm未満20mm以上、20mm未満となるように処理される。このうち粒径が40mm未満20mm以上のものはロックウール(断熱材)の材料として再利用される。一方、粒径が20mm未満のものは、本発明では、受入ホッパー11からベルトコンベア12を介して磁選機13に送り、鉄分を含む磁着物Aaとそれ以外に選別する。   A is a slow-cooled slag obtained by gradually cooling the molten slag discharged from the blast furnace into a lump, and is processed in the crushing and sizing plant 1 so that the particle size is, for example, less than 40 mm and less than 20 mm and less than 20 mm. The Of these, those having a particle size of less than 40 mm and 20 mm or more are reused as a material for rock wool (heat insulating material). On the other hand, in the present invention, those having a particle size of less than 20 mm are sent from the receiving hopper 11 to the magnetic separator 13 via the belt conveyor 12 and sorted into the magnetically-adhered material Aa containing iron and the others.

なお、路盤材の材料として再利用すべく、破砕整粒プラントの操業を変更し、破砕を繰り返して27mm未満に整粒しても良いことは従来と同じである。   In addition, it is the same as before that the operation of the crushing and sizing plant may be changed and the crushing may be repeated to reduce the particle size to less than 27 mm in order to be reused as the material for the roadbed material.

前記磁選機13で磁着物Aaを除去したものはベルトコンベア12で一次分離湿式篩14に送り、ここで水wを散布して、粒径が例えば20mm未満15mm以上、15mm未満5.0mm以上、5.0mm未満2.5mm以上の3つに篩分ける。これら篩分けされたものは、いずれもコンクリート用骨材として再利用される。   What the magnetic deposit Aa has been removed by the magnetic separator 13 is sent to the primary separation wet sieve 14 by the belt conveyor 12, where water w is dispersed, and the particle size is, for example, less than 20 mm, 15 mm or more, less than 15 mm, 5.0 mm or more, Sift into 3 pieces of less than 5.0mm and 2.5mm or more. All of these sieved materials are reused as aggregates for concrete.

一方、篩下の、粒径が2.5mm未満のものは、一次分級槽15を介して二次分離湿式篩16に送り、ここで、粒径が例えば2.5mm未満0.8mm以上のものと0.8mm未満のものに篩分ける。   On the other hand, those having a particle size of less than 2.5 mm under the sieve are sent to the secondary separation wet sieve 16 via the primary classification tank 15, where the particle size is, for example, less than 2.5 mm and 0.8 mm or more. And sieve to less than 0.8mm.

篩下の、粒径が0.8mm未満のものは、二次分級槽17を介して湿式サイクロン18に送り、ここで、粒径が0.8mm未満0.075mm以上のものと、0.075mm未満のものに遠心分離する。   Those having a particle size of less than 0.8 mm under the sieve are sent to the wet cyclone 18 via the secondary classification tank 17, where the particle size is less than 0.8 mm and 0.075 mm or more, and 0.075 mm. Centrifuge to less than.

粒径が0.8mm未満0.075mm以上のものは、再度、二次分離湿式篩16に送り、粒径が2.5mm未満0.8mm以上のものと合わされて篩分けられる。そして、粒径が2.5mm未満0.075mm以上のものは、コンクリート用細骨材の材料として再利用される。粒径が0.075mm未満のものは、スラリー槽19に送り、ここで凝集沈殿剤を加えて凝集して沈殿させ、圧搾フィルタープレス20で脱水ろ過する。この粒径が0.075mm未満のものは、セメント原料等として再利用される。   Those having a particle size of less than 0.8 mm and 0.075 mm or more are sent again to the secondary separation wet sieve 16 and sieved together with those having a particle size of less than 2.5 mm and 0.8 mm or more. And a thing with a particle size of less than 2.5 mm and 0.075 mm or more is reused as a material for fine aggregate for concrete. Those having a particle size of less than 0.075 mm are sent to a slurry tank 19 where a coagulating precipitant is added for aggregation and precipitation, followed by dehydration filtration with a compressed filter press 20. Those having a particle size of less than 0.075 mm are reused as cement raw materials.

上記構成の本発明の湿式分級設備では、破砕整粒プラント1で破砕整粒した徐冷スラグAは、一次分離湿式篩14により篩分けする際に微粉は水で除去される為、その表面には微粉が付着しておらず、再度、篩分けする必要がない。また、これら篩分けしたものを、長時間山積みして保管した場合も、規定の粒度分布範囲から外れることがない。   In the wet classification equipment of the present invention having the above-described configuration, the slow-cooled slag A crushed and sized in the pulverization and sizing plant 1 is finely removed with water when sieving with the primary separation wet sieve 14, so that Does not have fine powder attached and does not need to be sieved again. Moreover, even when these sieved products are stored in a pile for a long time, they do not deviate from the specified particle size distribution range.

徐冷スラグAに含まれる鉄分を選別する場合は、上記構成のように一次分離湿式篩14により篩分けする前に磁選機13を配置して選別することが望ましい。   When sorting the iron contained in the slowly cooled slag A, it is desirable to place and sort the magnetic separator 13 before sieving with the primary separation wet sieve 14 as in the above configuration.

次に、本発明の脱硫スラグの湿式分級設備の一例を、図2を用いて説明する。
Bは脱硫スラグであり、微細な炭素粉の飛散防止のため、注水イして冷却ロ、屋内攪拌ハした後、水ピット3へ排滓ニする。
Next, an example of the desulfurization slag wet classification equipment of the present invention will be described with reference to FIG.
B is desulfurization slag, and is injected into the water pit 3 after water injection, cooling, and indoor stirring to prevent the scattering of fine carbon powder.

本発明では、水ピット3内の脱硫スラグを振動フィーダ21に投入し、振動フィーダ21を介して湿式振動篩22に供給して散水しながら、30mm以上の地金Baと、30mm未満の篩下に篩分ける。   In the present invention, the desulfurized slag in the water pit 3 is put into the vibration feeder 21 and supplied to the wet vibration sieve 22 through the vibration feeder 21 to sprinkle water while sprinkling water. Sift into pieces.

篩下の脱硫スラグは、混合槽23を介して一次分離湿式篩14に送り、ここで水を散布して表面に付着した粉状の脱硫スラグを除去した後、地金Bbと粉状のスラグに篩分ける。図2の例では、地金Bbは、例えば粒径が30mm未満15mm以上と15mm未満5mm以上と5.0mm未満2.5mm以上に篩分けている。   The desulfurized slag under the sieve is sent to the primary separation wet sieve 14 through the mixing tank 23, and after spraying water to remove the powdered desulfurized slag adhering to the surface, the base metal Bb and the powdered slag are removed. Sift into pieces. In the example of FIG. 2, the bare metal Bb is sieved to, for example, a particle size of less than 30 mm, 15 mm or more, less than 15 mm, 5 mm or more, and less than 5.0 mm, 2.5 mm or more.

以上の地金Ba、Bbは、表面に付着する粉状の脱硫スラグが少ないので、硫黄分が低くなって製鋼原料として有効利用することができる。   Since the above-mentioned bullion Ba and Bb have little powdery desulfurization slag adhering to the surface, the sulfur content becomes low and can be effectively used as a steelmaking raw material.

一方、篩下の、粒径が2.5mm未満の脱硫スラグBcは、一次分級槽15を介して二次分離湿式篩16に送り、ここで、粒径が例えば2.5mm未満0.8mm以上のものと0.8mm未満のものに篩分ける。   On the other hand, the desulfurized slag Bc having a particle size of less than 2.5 mm under the sieve is sent to the secondary separation wet sieve 16 through the primary classification tank 15, where the particle size is, for example, less than 2.5 mm and 0.8 mm or more. Sieving into one with less than 0.8mm.

篩下の、粒径が0.8mm未満のものは、二次分級槽17を介して湿式サイクロン18に送り、ここで、粒径が0.8〜0.075mmのものと、0.075mm未満のものに遠心分離する。   Those having a particle size of less than 0.8 mm under the sieve are sent to the wet cyclone 18 through the secondary classification tank 17, where the particle size is 0.8 to 0.075 mm and less than 0.075 mm. Centrifuge into one.

粒径が0.8mm未満0.075mm以上のものは、再度、二次分離湿式篩16に送り、粒径が2.5mm未満0.8mm以上のものと合わされて篩分けられる。そして、粒径が2.5mm未満0.075mm以上のものは砂状スラグとして回収され、製鉄原料として再利用される。粒径が0.075mm未満のものは、スラリー槽19に送り、ここで凝集沈殿剤を加えて凝集して沈殿させ、圧搾フィルタープレス20で脱水ろ過する。この粒径が0.075mm未満のものは、脱水ケーキを回収し、製鉄原料として再利用される。   Those having a particle size of less than 0.8 mm and 0.075 mm or more are sent again to the secondary separation wet sieve 16 and sieved together with those having a particle size of less than 2.5 mm and 0.8 mm or more. And a thing with a particle size of less than 2.5mm and 0.075mm or more is collect | recovered as sandy slag, and is reused as an iron-making raw material. Those having a particle size of less than 0.075 mm are sent to a slurry tank 19 where a coagulating precipitant is added for aggregation and precipitation, followed by dehydration filtration with a compressed filter press 20. When the particle size is less than 0.075 mm, the dehydrated cake is recovered and reused as an ironmaking raw material.

上記構成の本発明の湿式分級設備では、脱硫スラグBに含まれる地金は、磁選機を使用せず、湿式振動篩22、一次分離湿式篩14により脱硫スラグBと選別する。従って、地金Ba、Bbの表面には脱硫スラグの付着量が少なく、地金Ba、Bbの硫黄分が低くなって、製鋼原料として有効利用することが可能になる。   In the wet classification equipment of the present invention having the above-described configuration, the metal contained in the desulfurization slag B is separated from the desulfurization slag B by the wet vibrating sieve 22 and the primary separation wet sieve 14 without using a magnetic separator. Accordingly, the amount of desulfurized slag attached to the surface of the metal bars Ba and Bb is small, and the sulfur content of the metal bars Ba and Bb is reduced, so that it can be effectively used as a steelmaking raw material.

本発明は上記の例に限らず、各請求項に記載された技術的思想の範疇であれば、適宜実施の形態を変更しても良いことは言うまでもない。   The present invention is not limited to the above example, and it goes without saying that the embodiments may be changed as appropriate within the scope of the technical idea described in each claim.

例えば、図1の例では、鉄鋼スラグを篩分ける湿式篩を一次分離湿式篩14と二次分離湿式篩16の2基設置しているが、湿式篩は1基でも良い。   For example, in the example of FIG. 1, two wet sieves for sieving steel slag, the primary separation wet sieve 14 and the secondary separation wet sieve 16, are installed, but one wet sieve may be used.

1 破砕整粒プラント
3 水ピット
13 磁選機
14 一次分離湿式篩
16 二次分離湿式篩
18 湿式サイクロン
22 湿式振動篩
A 徐冷スラグ
B 脱硫スラグ
1 Crushing and Sizing Plant 3 Water Pit 13 Magnetic Separator 14 Primary Separation Wet Sieve 16 Secondary Separation Wet Sieve 18 Wet Cyclone 22 Wet Vibrating Sieve A Slow Cooling Slag B Desulfurization Slag

Claims (3)

破砕整粒或いは注水処理した鉄鋼スラグを所定の粒径に篩分けする湿式篩と、
この湿式篩の篩下から、前記篩分けしたものよりも粒径が小さく比重の小さいものを遠心分離する湿式サイクロンを有することを特徴とする鉄鋼スラグの湿式分級設備。
A wet sieve that screens steel slag that has been crushed and sized or irrigated with water to a predetermined particle size;
A wet classifier for steel slag, characterized by having a wet cyclone for centrifuging a material having a particle size smaller than that of the sieved material and having a specific gravity smaller than that of the sieved product.
前記鉄鋼スラグが破砕整粒した高炉徐冷スラグであり、前記湿式篩の上流に、湿式篩に投入する前の高炉徐冷スラグ中の地金を選別して除去する磁選機を設けることを特徴とする請求項1に記載の鉄鋼スラグの湿式分級設備。   The steel slag is a blast furnace slow-cooled slag in which the steel slag is crushed and sized, and a magnetic separator is provided upstream of the wet sieve to select and remove the metal in the blast furnace slow-cooled slag before being put into the wet sieve. The steel slag wet classification equipment according to claim 1. 前記鉄鋼スラグが注水処理した脱硫スラグであり、前記湿式篩で地金とスラグを篩分けることを特徴とする請求項1に記載の鉄鋼スラグの湿式分級設備。   The steel slag wet classification equipment according to claim 1, wherein the steel slag is desulfurized slag subjected to water injection treatment, and the metal slag is separated with the wet sieve.
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* Cited by examiner, † Cited by third party
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JP2015160782A (en) * 2014-02-28 2015-09-07 Jfeスチール株式会社 Method of producing artificial stone material
CN105457748A (en) * 2016-01-11 2016-04-06 青岛双星环保设备有限公司 Updraught type magnetic separation device for scrap tire pyrolysis carbon black
JP2018090477A (en) * 2016-11-29 2018-06-14 Jfeスチール株式会社 Method for processing steel slag
CN108246491A (en) * 2018-01-25 2018-07-06 包头钢铁(集团)有限责任公司 The process of fine chrome mine is recycled in a kind of gravity tailings of high-carbon chrome iron for smelting wet slag
EP2931926B1 (en) * 2012-12-11 2018-11-21 LAB Geodur GmbH Method for recovering materials from slag
CN109092844A (en) * 2018-06-22 2018-12-28 南京芬钢环保科技有限公司 Steel slag multistage treatment method
CN111589576A (en) * 2020-06-20 2020-08-28 中冶节能环保有限责任公司 Steel slag crushing, grading, sorting and continuous processing device and method
CN111760850A (en) * 2020-06-30 2020-10-13 金燕 Multistage dust removal slag equipment of polishing of low-power consumption
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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004075454A (en) * 2002-08-16 2004-03-11 Tetsugen Corp Blast furnace granulated slag fine aggregate and method of preventing caking of blast furnace granulated slag
JP2010046569A (en) * 2008-08-19 2010-03-04 Shikyo Tei Post-treatment apparatus of slag and method therefor

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004075454A (en) * 2002-08-16 2004-03-11 Tetsugen Corp Blast furnace granulated slag fine aggregate and method of preventing caking of blast furnace granulated slag
JP2010046569A (en) * 2008-08-19 2010-03-04 Shikyo Tei Post-treatment apparatus of slag and method therefor

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