JP2001048605A - Treatment of steelmaking slag for cement - Google Patents

Treatment of steelmaking slag for cement

Info

Publication number
JP2001048605A
JP2001048605A JP21546899A JP21546899A JP2001048605A JP 2001048605 A JP2001048605 A JP 2001048605A JP 21546899 A JP21546899 A JP 21546899A JP 21546899 A JP21546899 A JP 21546899A JP 2001048605 A JP2001048605 A JP 2001048605A
Authority
JP
Japan
Prior art keywords
slag
granular iron
cement
dephosphorization
steelmaking
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.)
Granted
Application number
JP21546899A
Other languages
Japanese (ja)
Other versions
JP4219057B2 (en
Inventor
Ikuo Fujii
郁男 藤井
Masayoshi Yokoo
正義 横尾
Yasuhiro Yamazawa
靖弘 山澤
Masato Kajiyama
正人 梶山
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.)
Navitas Co Ltd
Nippon Steel Corp
Original Assignee
Navitas Co Ltd
Nippon Steel Corp
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 Navitas Co Ltd, Nippon Steel Corp filed Critical Navitas Co Ltd
Priority to JP21546899A priority Critical patent/JP4219057B2/en
Publication of JP2001048605A publication Critical patent/JP2001048605A/en
Application granted granted Critical
Publication of JP4219057B2 publication Critical patent/JP4219057B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B18/00Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
    • C04B18/04Waste materials; Refuse
    • C04B18/14Waste materials; Refuse from metallurgical processes
    • C04B18/141Slags
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B7/00Hydraulic cements
    • C04B7/14Cements containing slag
    • C04B7/147Metallurgical slag
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2100/00Handling of exhaust gases produced during the manufacture of iron or steel
    • C21B2100/40Gas purification of exhaust gases to be recirculated or used in other metallurgical processes
    • C21B2100/42Sulphur removal
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/022Methods of cooling or quenching molten slag
    • C21B2400/024Methods of cooling or quenching molten slag with the direct use of steam or liquid coolants, e.g. water
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/10Production of cement, e.g. improving or optimising the production methods; Cement grinding
    • 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
    • Y02W30/91Use of waste materials as fillers for mortars or concrete

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Civil Engineering (AREA)
  • Manufacture Of Iron (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a treatment process for steelmaking slag used for cement, which enables effective utilization of free CaO, reduction in water content of dephosphorization/desulfurization slag, accordingly, enhancement of efficiency of separation/removal of granular iron, inhibition of dephosphorization/ desulfurization slag from being deposited or accumulated in a crushing stage or magnetic separation treatment stage. SOLUTION: This treatment process comprises: conveying and discharging slag 10 formed in dephosphorization/desulfurization stages of a steelmaking process, to a treatment yard 13; spraying water on the slag 10 to cool the slag; crushing large lumps of the slag 10 to remove metal; thereafter, once stacking up the crushed slag 10 to reduce the water content of the slag to <=10 wt.% by the heat of reaction of CaO in the slag 10; then further crushing the resulting slag 10; and separating and removing granular iron from this slag 10.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、製鋼の脱燐、脱流
工程で発生するスラグから鉄や鋼等の金属を除去してセ
メントの原料に用いるセメント用製鋼スラグの処理方法
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating steelmaking slag for cement used as a raw material for cement by removing metals such as iron and steel from slag generated in a dephosphorization and deflow process of steelmaking.

【0002】[0002]

【従来の技術】従来、製鋼工程では、溶銑の燐や硫黄等
の不純物の除去、溶銑あるいは屑鉄等の脱炭や不純物の
除去を行うため、生石灰や酸化鉄等の副材料を用いて精
錬を行う必要があり、その結果、多量のスラグが発生す
る。このスラグは、製鋼の工程によって、溶銑の脱燐、
脱流等によって発生するいわゆる溶銑予備処理スラグ
(脱燐、脱流スラグ)と、転炉等の精錬から発生するス
ラグ(転炉スラグ)とに分けられる。この内、転炉スラ
グは、その主成分が高炉スラグと類似しており、金属
(粒鉄)等の不純物を除去し、エージング処理が施さ
れ、路盤材や土壌改良材、セメントクリンカー等に使用
され、リサイクル化が積極的に図られている。また、脱
燐、脱流スラグは、風化、膨張性が著しく、埋め立て等
に廃棄処分されていたが、近年、資源のリサイクル化が
積極的に推進されている。この代表的な方法として、特
開平7−223857号公報には、転炉スラグあるいは
脱燐、脱流スラグに、石炭灰、シルト、高炉スラグの1
種又は2種以上を1〜30重量%配合して蒸気あるいは
温水で処理することにより、スラグ粒子の遊離CaOを
石炭灰、シルト等に含有する可溶性シリカによって水の
存在で反応させ、不可溶性のCaO・SiO2 ・H2
ゲルを生成させて、風化、膨張性を抑制し、路盤材等に
使用することが記載されている。しかし、脱燐、脱流ス
ラグの用途を拡大して、付加価値の高いセメント原料等
への資源リサイクル化を図るには、脱燐、脱流スラグ中
に含まれる金属(粒鉄)や塩素イオン等が支障となる。
この対策として、例えば、特開平8−198647号公
報には、脱燐、脱流工程で発生したスラグを塩素の少な
い淡水により冷却し、破砕と磁選処理を複数回行うこと
により、塩素と粒鉄の少ない脱燐、脱流スラグを得て、
セメント原料に用いることが記載されている。
2. Description of the Related Art Conventionally, in the steelmaking process, in order to remove impurities such as phosphorus and sulfur from hot metal, decarburize hot metal and scrap iron, and remove impurities, refining is performed using auxiliary materials such as quicklime and iron oxide. Must be performed, resulting in a large amount of slag. This slag is dephosphorized from hot metal,
It is divided into so-called hot metal pretreatment slag (dephosphorization, degassing slag) generated by degassing or the like, and slag (converter slag) generated from refining of a converter or the like. Among them, converter slag is similar to blast furnace slag in its main component, and is subjected to aging treatment to remove impurities such as metal (granular iron) and used as roadbed material, soil improvement material, cement clinker, etc. And recycling is being actively promoted. In addition, dephosphorization and degassing slag are remarkably weathered and expanded, and have been disposed of in landfills. In recent years, recycling of resources has been actively promoted. As a typical method, Japanese Unexamined Patent Publication (Kokai) No. 7-223857 discloses that one of coal ash, silt, and blast furnace slag is added to converter slag, dephosphorization, and outflow slag.
By mixing 1 to 30% by weight of a seed or two or more kinds and treating with steam or warm water, free CaO of slag particles is reacted in the presence of water with soluble silica contained in coal ash, silt, etc. CaO ・ SiO 2・ H 2 O
It describes that a gel is formed, weathering and swelling are suppressed, and the gel is used for roadbed materials and the like. However, in order to expand the use of dephosphorization and dewatering slag and to recycle resources into high value-added cement raw materials, it is necessary to use metals (granular iron) and chlorine ions contained in dephosphorization and dewatering slag. And so on.
As a countermeasure, for example, Japanese Patent Application Laid-Open No. 8-198647 discloses that slag generated in a dephosphorization and deflow process is cooled with fresh water containing little chlorine, and crushing and magnetic separation are performed a plurality of times to obtain chlorine and granular iron. Dephosphorization and degassing slag with less
It is described to be used as a cement raw material.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、特開平
8−198647号公報に記載された方法では、脱燐、
脱流スラグの塩素の濃度は低減できるが、遊離CaOと
細かい粒鉄が多く存在するので、スラグ中の水分が高い
場合に、破砕と磁選処理により粒鉄の除去を行っても、
遊離CaOの反応による生成物等が粒鉄の表面に付着し
たり、この非磁性の付着物により磁選機への吸着が阻害
され、選別(磁選)効率の低下等を生じ、十分にスラグ
中の粒鉄の含有量を低減できない。また、破砕工程や磁
選工程の処理を行った際に、脱燐、脱流スラグの付着性
が高くなり、シュート等の供給装置、ベルトコンベア等
の搬送装置等への付着、堆積等を生じ、その除去や補修
等に手間がかかる上、処理の停止等が発生して、安定し
た操業に支障を招く等の問題がある。
However, in the method described in Japanese Patent Application Laid-Open No. 8-198647, dephosphorization,
Although the concentration of chlorine in the effluent slag can be reduced, since there are many free CaO and fine granular iron, if the moisture in the slag is high, even if the granular iron is removed by crushing and magnetic separation,
The products and the like due to the reaction of free CaO adhere to the surface of the granular iron, and the adsorption of the nonmagnetic adherence to the magnetic separator causes a decrease in the sorting (magnetic separation) efficiency and the like. The content of granular iron cannot be reduced. In addition, when the crushing step or the magnetic separation step is performed, the dephosphorization and the adhesion of the outflow slag are increased, and the adhesion to a feeding device such as a chute, a transfer device such as a belt conveyor, and the like are caused. Removal and repair are troublesome, and there are problems such as stoppage of processing and the like, which hinders stable operation.

【0004】本発明はかかる事情に鑑みてなされたもの
で、遊離CaOを有効に活用し、脱燐、脱流スラグの水
分を低減して、粒鉄の選別除去の効率を高め、破砕工程
や磁選処理工程での脱燐、脱流スラグの付着や堆積を抑
制するセメント用製鋼スラグの処理方法を提供すること
を目的とする。
The present invention has been made in view of the above circumstances, and effectively utilizes free CaO to reduce the water content of dephosphorization and degassed slag to increase the efficiency of sorting and removing granular iron. It is an object of the present invention to provide a method for treating steelmaking slag for cement, which suppresses the adhesion and deposition of dephosphorization and outflow slag in a magnetic separation process.

【0005】[0005]

【課題を解決するための手段】前記目的に沿う本発明の
セメント用製鋼スラグの処理方法は、製鋼の脱燐、脱流
工程で発生するスラグを搬送して、処理ヤードに排出
し、該スラグに散水して冷却してから、前記スラグの大
きい塊を破砕し、地金を除去した後、前記スラグを一旦
積み付けて、該スラグに含有されたCaOの反応熱によ
り水分を10重量%以下にしてから前記スラグを破砕
し、該スラグに含まれる粒鉄を選別して除去する。この
方法により、遊離CaOの反応熱を有効に活用して、脱
燐、脱流スラグ(以下スラグと言う)の水分を所定の値
に低減でき、遊離CaOの反応生成物等の粒鉄への付着
を抑制し、粒鉄の選別除去の効率を高め、破砕工程や磁
選処理工程でのスラグの付着や堆積を防止することがで
きる。
According to the present invention, there is provided a method for treating steelmaking slag for cement according to the present invention, wherein the slag generated in the dephosphorization and deflow processes of steelmaking is conveyed, discharged to a treatment yard, and discharged. After cooling and crushing the large slag lump and removing the ingot, the slag is temporarily stacked and the water content is reduced to 10% by weight or less due to the heat of reaction of CaO contained in the slag. Then, the slag is crushed, and the granular iron contained in the slag is sorted out and removed. By this method, the heat of reaction of free CaO can be effectively utilized to reduce the water content of dephosphorization and degassed slag (hereinafter referred to as slag) to a predetermined value. Adhesion can be suppressed, the efficiency of sorting and removing granular iron can be increased, and adhesion and accumulation of slag in the crushing step and the magnetic separation processing step can be prevented.

【0006】ここで、前記スラグは屋内に積み付けるこ
とができる。これにより、遊離CaOの含有率の高いス
ラグの水和反応による熱を利用してスラグを乾燥するの
で、スラグの水分を所定値に安定して低減でき、粒鉄の
除去効率をより向上することができ、資源としての活用
価値を高めることができる。
Here, the slag can be stacked indoors. Thereby, since the slag is dried by using the heat generated by the hydration reaction of the slag having a high content of free CaO, the water content of the slag can be stably reduced to a predetermined value, and the efficiency of removing granular iron is further improved. And increase the value of utilization as a resource.

【0007】更に、前記粒鉄の選別除去を磁選機で行う
ことが好ましい。これにより、スラグ中の粒鉄の除去を
確実に行なうことができ、セメントクリンカー等の原料
に使用する際に、混入した粒鉄による破砕機の磨耗の抑
制と、セメント中に含まれる粒鉄の腐食によるセメント
の膨張等を防止してセメントの品質を向上することがで
きる。
Further, it is preferable that the sorting and removal of the granular iron is performed by a magnetic separator. Thereby, it is possible to reliably remove the granular iron in the slag, and when using it as a raw material such as cement clinker, to suppress wear of the crusher due to the mixed granular iron, and to reduce the granular iron contained in the cement. The quality of the cement can be improved by preventing the expansion and the like of the cement due to corrosion.

【0008】[0008]

【発明の実施の形態】続いて、添付した図面を参照しつ
つ、本発明を具体化した実施の形態につき説明し、本発
明の理解に供する。図1は本発明の一実施の形態に係る
セメント用製鋼スラグの処理方法の処理工程の説明図、
図2は原鉱スラグの含水率と製品スラグ中の粒鉄の含有
量の関係を表すグラフ、図3は乾燥日数と原鉱スラグの
含水率の関係を表すグラフである。図1に示すように、
本発明の一実施の形態に係るセメント用製鋼スラグの処
理方法について具体的に説明する。まず、図示しない予
備処理炉により精鋼の脱燐や脱硫処理を行って、溶銑中
の不純物を除去し、生成したスラグ10を予備処理炉か
ら排滓台車11に載置した排滓鍋12に排出する。排滓
台車11により搬送される排滓鍋12内のスラグ10
は、殆ど溶融(一部凝固している状態)している。この
排滓台車11を処理ヤード13に搬送し、排滓台車11
に載置した排滓鍋12を傾けて、スラグ10を処理ヤー
ド13に流し扇形に広げ、同時に、散水して、散水によ
る強制冷却と空冷によって、スラグ10を完全に凝固さ
せ、表面温度を30〜60℃程度にする。凝固したスラ
グ10は、ショベル等で踏み割りを行なって大きい塊を
破砕し、混入した大きい地金をリフマグ等で吸着して除
去し、更に、スラグ10を80mm以下に破砕して原鉱
となるスラグ10を作る。そして、水分を11〜15重
量%含んだスラグ10は、セルフローダーやトラック等
で搬送され、屋内エージング処理場14に、2〜5mの
高さに積み付けられる。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, embodiments of the present invention will be described with reference to the accompanying drawings to provide an understanding of the present invention. FIG. 1 is an explanatory diagram of processing steps of a method for processing steelmaking slag for cement according to one embodiment of the present invention,
FIG. 2 is a graph showing the relationship between the water content of raw ore slag and the content of granular iron in the product slag, and FIG. 3 is a graph showing the relationship between the number of drying days and the water content of raw ore slag. As shown in FIG.
A method for treating steelmaking slag for cement according to an embodiment of the present invention will be specifically described. First, dephosphorization or desulfurization treatment of refined steel is performed by a pretreatment furnace (not shown) to remove impurities in the hot metal, and the generated slag 10 is discharged from the pretreatment furnace to a waste pan 12 placed on a waste truck 11. I do. Slag 10 in waste pan 12 conveyed by waste trolley 11
Is almost molten (partly solidified). The waste trolley 11 is transported to the processing yard 13 and the waste trolley 11
The slag 10 is tilted, and the slag 10 is poured into the treatment yard 13 and spread in a fan shape. At the same time, the slag 10 is completely solidified by water cooling, forced cooling and air cooling, and the surface temperature is reduced to 30. 6060 ° C. The solidified slag 10 is broken by a shovel or the like to break up a large lump, the mixed large metal is absorbed and removed by a rif mag or the like, and further, the slag 10 is crushed to 80 mm or less to become an ore. Make slag 10. The slag 10 containing 11 to 15% by weight of water is conveyed by a self-loader or a truck, and is loaded on the indoor aging treatment plant 14 at a height of 2 to 5 m.

【0009】この状態で7〜10日間のエージング処理
を行う。この積み付けられたスラグ10は、CaOが4
0〜60重量%、SiO2 が5〜20重量%、Al2
3 が4〜15重量%、酸化第二鉄が10〜25重量%を
主体とし、この内CaOは、SiO2 やAl23 等と
未結合の遊離CaOを5〜10重量%含んでいる。遊離
CaOは、スラグ10の水分と水和反応を起こして発熱
し、積み付けたスラグ10にじっくりと熱を伝え、スラ
グ10を乾燥し、スラグ10の水分を10重量%以下に
することができる。しかも、遊離CaOの自熱により乾
燥するので、水和反応で生成したCa(OH)2 等の粘
着性が抑制され、粒鉄に付着するのを防止できる。そし
て、磁選を効率良く行うことができ、スラグ10中の粒
鉄を大幅に減少することができる。特に、スラグの水分
は、低くなる程に粒鉄の選別の効率を安定して高めるこ
とができる。しかし、3重量%以下になると発塵を生じ
て作業環境が悪化するので、3〜8重量%にするとより
好ましい結果が得られる。
In this state, aging treatment is performed for 7 to 10 days. The stacked slag 10 has a CaO of 4
0-60wt%, SiO 2 is 5 to 20 wt%, Al 2 O
3 is 4 to 15 wt%, mainly composed of 10 to 25 wt% ferric oxide, the inner CaO contains free CaO unbound and the like SiO 2 and Al 2 O 3 5 to 10 wt% . The free CaO causes a hydration reaction with the water of the slag 10 to generate heat, conducts heat to the stacked slag 10 slowly and dries the slag 10, and can reduce the water content of the slag 10 to 10% by weight or less. . Moreover, since the free CaO is dried by self-heating, the adhesiveness of Ca (OH) 2 and the like generated by the hydration reaction is suppressed, and it is possible to prevent the Ca (OH) 2 from adhering to the granular iron. And magnetic separation can be performed efficiently, and the granular iron in the slag 10 can be reduced significantly. In particular, as the water content of the slag becomes lower, the efficiency of sorting of granular iron can be stably increased. However, when the content is less than 3% by weight, dust is generated and the working environment deteriorates. Therefore, when the content is 3 to 8% by weight, more preferable results are obtained.

【0010】図2は、原鉱スラグの水分が変化した場合
の製品スラグ中の粒鉄の残存率を調査した結果である。
スラグの乾燥後の水分が10重量%を超えると、製品ス
ラグ中の粒鉄の残存率が上限値10%を超える場合が発
生し、セメントの品質を安定して満足することができな
いことが判る。これは、粒鉄の表面にスラグやCa(O
H)2 粉等が付着し、磁選の効率が低下するからであ
る。従って、スラグ中の水分を低くし、例えば、磁選を
一回行う(図中の○)場合で、スラグ水分7重量%以下
であれば製品スラグ中の粒鉄の残存率を10%以下にす
ることができる。また、磁選を二回行う(図中の●)場
合で、スラグ水分が10重量%以下であれば製品スラグ
中の粒鉄の残存率を10%以下にすることができる。し
かし、スラグの水分が3重量%より低くなると、破砕や
粒鉄の磁選の効率を高めることはできるが、極端に発塵
が激しくなり、集塵装置の増強や作業環境の悪化を招
く。また、図3は、スラグを乾燥させるため、積み付け
を屋外と屋内の場合について調査したものであり、従来
の屋外乾燥(図中の○)では、天候の影響を受けたり、
スラグの水分過多により遊離CaOを活用した乾燥を行
うことができないため、スラグ中のスラグ水分が領域A
で示すようにバラツキが大きくなり10重量%を超えて
しまう場合がある。これに対し、本実施の形態である屋
内乾燥(図中の●)では、スラグの水分を10重量%以
下に短期間に安定して低減することができる。これは、
スラグに付着や浸透した水分を遊離CaOと反応した熱
により蒸発させて乾燥するため、天候等の外乱を防止す
ると共に、遊離CaOの反応熱により蒸発する付着水や
浸透水の量を調整して、水分を低減することができるか
らである。図1に示すように、エージング処理されたス
ラグ10は、ショベルカー15により切り出され、ベル
トコンベア等の搬送手段を介して、クラッシャー等の破
砕機16に供給され、25mm以下のサイズに破砕され
る。この破砕されたスラグ10は、ベルトコンベア等の
搬送手段の途中に配置した磁選機17により、スラグ1
0に含まれる25mm以下の粒鉄が選別除去され、粒鉄
の含有量が10重量%以下に低減される。そして、粒鉄
を除去した後のスラグ10は、セメントクリンカーの原
料として製品積み付け場18に貯蔵され、必要に応じて
ダンプカー等により後工程に搬送される。
FIG. 2 shows the result of investigation on the residual ratio of granular iron in product slag when the water content of raw ore slag changes.
If the moisture content of the slag after drying exceeds 10% by weight, the residual ratio of the iron granules in the product slag may exceed the upper limit of 10%, which indicates that the quality of the cement cannot be stably satisfied. . This is because slag or Ca (O
H) 2 powder or the like adheres, and the efficiency of magnetic separation decreases. Therefore, when the water content in the slag is reduced and, for example, magnetic separation is performed once (○ in the figure), if the slag water content is 7% by weight or less, the residual ratio of granular iron in the product slag is 10% or less. be able to. In addition, when the magnetic separation is performed twice (● in the figure) and the slag moisture is 10% by weight or less, the residual ratio of the granular iron in the product slag can be 10% or less. However, if the water content of the slag is lower than 3% by weight, the efficiency of crushing and magnetic separation of granular iron can be increased, but the generation of dust becomes extremely violent, which leads to an increase in the size of the dust collector and a deterioration in the working environment. In addition, FIG. 3 shows the results of an investigation of the case where the slag is dried outdoors and indoors in order to dry the slag.
Since drying using free CaO cannot be performed due to excessive moisture in the slag, the slag moisture in the slag is reduced to the area A.
In some cases, the variation becomes large and exceeds 10% by weight. In contrast, in the indoor drying according to the present embodiment (● in the figure), the water content of the slag can be stably reduced to 10% by weight or less in a short period of time. this is,
Since the water adhering or penetrating into the slag is evaporated and dried by the heat reacted with the free CaO, it is possible to prevent disturbances such as weather and adjust the amount of the adhering water or the permeated water evaporated by the heat of reaction of the free CaO. This is because moisture can be reduced. As shown in FIG. 1, the aged slag 10 is cut out by a shovel car 15, supplied to a crusher 16 such as a crusher via a conveyor such as a belt conveyor, and crushed to a size of 25 mm or less. . The crushed slag 10 is separated from the slag 1 by a magnetic separator 17 disposed in the middle of a conveying means such as a belt conveyor.
The iron particles having a particle size of 25 mm or less contained in the particle No. 0 are selectively removed, and the content of the iron particles is reduced to 10% by weight or less. Then, the slag 10 from which the granular iron has been removed is stored in the product storage site 18 as a raw material for cement clinker, and is transported to a subsequent process by a dump truck or the like as necessary.

【0011】[0011]

【実施例】次に、本発明に係るセメント用製鋼スラグの
処理方法の実施例について説明する。製鋼工程で脱燐、
脱硫処理を行い、その際に発生した主組成が、CaO4
0〜60重量%、SiO2 5〜20重量%、Al23
4〜15重量%、酸化第二鉄10〜25重量%であり、
前記CaOの一部が遊離CaOであるスラグを処理ヤー
ドに流して、散水による冷却とショベルカーによる踏み
割りを行ってから大きい地金を除去し、破砕してサイズ
を80mm以下にし、処理ヤードでの散水を調整して水
分を12重量%にした。このスラグを長さ32m、幅3
4mの建屋内に、最大5mの高さになるように積み付
け、7日間置いて遊離CaOの水和反応によって生じる
熱により乾燥を行ない、スラグの水分を7重量%にし
た。更に、この乾燥後に、破砕機により25mm以下に
破砕し、磁選機を用いて粒鉄を吸着して除去し、粒鉄の
含有量を10重量%以下にしたスラグを製造した。その
結果、スラグの水分が低く、しかも、安定しているた
め、破砕や磁選のトラブルが無く、磁選機による粒鉄の
除去効率が良好であった。そして、このスラグをセメン
トクリンカーの原料に用いて製造した場合セメントの品
質も良好であった。
Next, an embodiment of a method for treating steelmaking slag for cement according to the present invention will be described. Dephosphorization in steel making process,
Desulfurization treatment is performed, and the main composition generated at that time is CaO4
0-60wt%, SiO 2 5 to 20 wt%, Al 2 O 3
4 to 15% by weight, 10 to 25% by weight of ferric oxide,
The slag in which a part of the CaO is free CaO is flowed to a processing yard, and after cooling by watering and sloping with a shovel car, a large ingot is removed and crushed to a size of 80 mm or less. Was adjusted to a water content of 12% by weight. This slag is 32m long and 3 width wide.
The slag was piled up in a 4 m building to a height of 5 m at maximum and left for 7 days to be dried by the heat generated by the hydration reaction of free CaO to reduce the water content of the slag to 7% by weight. Further, after drying, the slag was crushed to 25 mm or less by a crusher, and granular iron was adsorbed and removed using a magnetic separator to produce a slag having a content of granular iron of 10% by weight or less. As a result, the water content of the slag was low and stable, so that there was no trouble in crushing or magnetic separation, and the efficiency of removing granular iron by the magnetic separator was good. When this slag was used as a raw material for cement clinker, the quality of cement was good.

【0012】これに対し、比較例として、前記のスラグ
と同じ条件で、水分を13重量%にしたスラグを屋外に
積み付けし、天候の影響等を受けて水分が13重量%に
なったスラグを破砕機により25mm以下に破砕してか
ら磁選機を用いて粒鉄を吸着して除去した。その結果、
破砕機や磁選機、搬送のベルトコンベア等にスラグ等の
付着や堆積が見られ、磁選機の粒鉄の除去の効率も悪
く、粒鉄の含有量が15重量%と悪く、破砕や磁選のト
ラブルが発生し、セメントクリンカーの原料としての品
質も悪くなった。
On the other hand, as a comparative example, a slag having a water content of 13% by weight was stacked outdoors under the same conditions as the slag described above, and the slag having a water content of 13% by weight under the influence of weather or the like was obtained. Was crushed to 25 mm or less by a crusher, and iron particles were adsorbed and removed using a magnetic separator. as a result,
Adhesion or accumulation of slag etc. is seen on the crusher, magnetic separator, conveyor belt conveyor, etc., the efficiency of removal of granular iron by the magnetic separator is poor, and the content of granular iron is as poor as 15% by weight. A trouble occurred and the quality of the raw material for cement clinker deteriorated.

【0013】以上、本発明の実施の形態を説明したが、
本発明は、上記した形態に限定されるものでなく、要旨
を逸脱しない条件の変更等は全て本発明の適用範囲であ
る。例えば、処理ヤードで散水して凝固したスラグをシ
ョベルカーによる踏み割りを行って後に、破砕機にかけ
て篩分けしたものを積み付けてエージング処理を行うこ
ともできる。更に、屋内に積み付けた際に、遊離CaO
の反応熱による乾燥を行った後のスラグ含有水分が10
重量%以下になるように、予め散水して、例えば水分を
11〜12重量%に調整することもできる。
The embodiments of the present invention have been described above.
The present invention is not limited to the above-described embodiment, and all changes in conditions that do not depart from the gist are within the scope of the present invention. For example, it is also possible to perform aging treatment by sieving a slag solidified by sprinkling water in a processing yard with a shovel car and then sieving the slag through a crusher. Furthermore, when loaded indoors, free CaO
Slag-containing water after drying by the heat of reaction
It is also possible to adjust the water content to 11 to 12% by weight, for example, by spraying water in advance so that the amount is equal to or less than the weight%.

【0014】[0014]

【発明の効果】請求項1〜3記載のセメント用製鋼スラ
グの処理方法は、製鋼の脱燐、脱流工程で発生するスラ
グを搬送して、処理ヤードにスラグを排出し、スラグに
散水して冷却してから、スラグの大きい塊を破砕し地金
を除去した後、スラグを一旦積み付けて、スラグに含有
したCaOの反応熱により水分を10重量%以下にして
からスラグを破砕し、スラグに含まれる粒鉄を選別して
除去するので、遊離CaOの反応熱を利用してスラグの
水分を安定して所定の値に低減して、破砕工程や磁選処
理工程でのスラグの付着や堆積を抑制し、粒鉄に付着物
するスラグを少なくして粒鉄の選別効率を良好にでき、
セメントクリンカーの原料への資源のリサイクル化を可
能にできる。しかも、破砕、選別等の生産ライン等の生
産性が向上し、補修や付着物除去等の作業をなくすこと
ができる。
According to the method for treating steelmaking slag for cement according to claims 1 to 3, the slag generated in the dephosphorization and deflow processes of steelmaking is conveyed, the slag is discharged to a treatment yard, and water is sprinkled on the slag. After cooling and crushing a large lump of slag and removing the ingot, the slag is once stacked, and the slag is crushed after the moisture is reduced to 10% by weight or less by the reaction heat of CaO contained in the slag, Since the granular iron contained in the slag is sorted and removed, the water of the slag is stably reduced to a predetermined value by using the reaction heat of free CaO, and the adhesion of the slag in the crushing process and the magnetic separation process is reduced. Suppression of sedimentation, reduction of slag adhering to granular iron, and good selection efficiency of granular iron,
Resources can be recycled as raw materials for cement clinker. In addition, productivity of a production line such as crushing and sorting can be improved, and operations such as repair and removal of attached matter can be eliminated.

【0015】特に、請求項2記載のセメント用製鋼スラ
グの処理方法は、スラグを屋内に積み付けるので、遊離
CaOの水和反応熱を用いてスラグを乾燥し、水分を安
定して低減でき、破砕や選別の効率を高くすることがで
きる。しかも、風化や膨張性の高いスラグをセメントク
リンカー等にリサイクルし、資源の再利用が達成でき
る。
In particular, in the method for treating steelmaking slag for cement according to claim 2, since the slag is loaded indoors, the slag can be dried using the heat of hydration reaction of free CaO, and the water content can be reduced stably. The efficiency of crushing and sorting can be increased. Moreover, slag having high weathering and expansion properties can be recycled to cement clinker or the like, and resources can be reused.

【0016】請求項3記載のセメント用製鋼スラグの処
理方法は、粒鉄の選別除去を磁選機で行うので、スラグ
中の粒鉄の除去を確実に行なうことができ、破砕機の磨
耗を防止し、セメントの膨張や亀裂の発生等のトラブル
を回避し、セメントクリンカー等の品質を向上すること
ができる。
In the method for treating steelmaking slag for cement according to the third aspect, since the granular iron is selectively removed by the magnetic separator, the granular iron in the slag can be reliably removed, and the crusher is prevented from being worn. However, it is possible to avoid problems such as expansion of the cement and generation of cracks, and to improve the quality of the cement clinker and the like.

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

【図1】本発明の一実施の形態に係るセメント用製鋼ス
ラグの処理方法の処理工程の説明図である。
FIG. 1 is an explanatory diagram of processing steps of a method for processing steelmaking slag for cement according to one embodiment of the present invention.

【図2】原鉱スラグの含水率と製品スラグ中の粒鉄の含
有量の関係を表すグラフである。
FIG. 2 is a graph showing the relationship between the water content of raw ore slag and the content of granular iron in product slag.

【図3】乾燥日数と原鉱スラグの含水率の関係を表すグ
ラフである。
FIG. 3 is a graph showing the relationship between the number of drying days and the water content of raw ore slag.

【符号の説明】[Explanation of symbols]

10:スラグ、11:排滓台車、12:排滓鍋、13:
処理ヤード、14:屋内エージング処理場、15:ショ
ベルカー、16:破砕機、17:磁選機、18:製品積
み付け場
10: slag, 11: waste truck, 12: waste pan, 13:
Processing yard, 14: indoor aging treatment plant, 15: excavator, 16: crusher, 17: magnetic separator, 18: product loading site

───────────────────────────────────────────────────── フロントページの続き (72)発明者 横尾 正義 福岡県北九州市戸畑区飛幡町1番1号 新 日本製鐵株式会社八幡製鐵所内 (72)発明者 山澤 靖弘 福岡県北九州市八幡東区川淵町9の27 太 平工業株式会社八幡支店内 (72)発明者 梶山 正人 福岡県北九州市八幡東区川淵町9の27 太 平工業株式会社八幡支店内 Fターム(参考) 4G012 JD01 JD02 JE04 JE06 4K012 AB02 AB08  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Masayoshi Yokoo 1-1, Hibata-cho, Tobata-ku, Kitakyushu-shi, Fukuoka New Nippon Steel Corporation Yawata Works (72) Inventor Yasuhiro Yamazawa Yawata-Higashi-ku, Kitakyushu-shi, Fukuoka 27 in Kawabuchicho 9 Yatai Branch, Taihei Kogyo Co., Ltd. (72) Inventor Masato Kajiyama Inside 27 Yatai Branch, Taihei Kogyo Co., Ltd. 9-9 Kawabuchicho, Yawatahigashi-ku, Kitakyushu-shi, Fukuoka F-term (reference) 4G012 JD01 JD02 JE04 JE06 4K012 AB02 AB08

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 製鋼の脱燐、脱流工程で発生するスラグ
を搬送して、処理ヤードに排出し、該スラグに散水して
冷却してから、前記スラグの大きい塊を破砕し地金を除
去した後、前記スラグを一旦積み付けて、該スラグに含
有されたCaOの反応熱により水分を10重量%以下に
してから前記スラグを破砕し、該スラグに含まれる粒鉄
を選別して除去することを特徴とするセメント用製鋼ス
ラグの処理方法。
Claims 1. A slag generated in a dephosphorization and deflow process of steelmaking is conveyed, discharged to a treatment yard, sprinkled on the slag and cooled, and then a large lump of the slag is crushed to remove the metal. After the removal, the slag is temporarily piled up, the moisture is reduced to 10% by weight or less by the reaction heat of CaO contained in the slag, and then the slag is crushed, and the granular iron contained in the slag is selectively removed. A method for treating steelmaking slag for cement, comprising:
【請求項2】 請求項1記載のセメント用製鋼スラグの
処理方法において、前記スラグを屋内に積み付けるセメ
ント用製鋼スラグの処理方法。
2. The method for treating steelmaking slag for cement according to claim 1, wherein said slag is loaded indoors.
【請求項3】 請求項1又は2記載のセメント用製鋼ス
ラグの処理方法において、前記粒鉄の選別を磁選機で行
うセメント用製鋼スラグの処理方法。
3. The method for treating steel slag for cement according to claim 1 or 2, wherein the separation of the granular iron is performed by a magnetic separator.
JP21546899A 1999-07-29 1999-07-29 Method for processing steelmaking slag for cement Expired - Fee Related JP4219057B2 (en)

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JP2008247665A (en) * 2007-03-30 2008-10-16 Iwate Industrial Research Center Method of producing iron-and-steel slag fertilizer
WO2010131658A1 (en) * 2009-05-12 2010-11-18 国立大学法人新潟大学 Device for recovering heat of molten slag
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JP2008247665A (en) * 2007-03-30 2008-10-16 Iwate Industrial Research Center Method of producing iron-and-steel slag fertilizer
KR101079503B1 (en) 2008-11-27 2011-11-03 주식회사 포스코 Recovering method for slag which is not magnetically recovered, high specific gravity materials manufactured from the same and manufacturing method for the high specific gravity materials
KR101049088B1 (en) * 2008-12-19 2011-07-15 재단법인 포항산업과학연구원 Cement admixture using molten iron preliminary slag and its manufacturing method
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