JP2006070308A - Method for melting solid-iron source in molten iron carrier - Google Patents

Method for melting solid-iron source in molten iron carrier Download PDF

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JP2006070308A
JP2006070308A JP2004253183A JP2004253183A JP2006070308A JP 2006070308 A JP2006070308 A JP 2006070308A JP 2004253183 A JP2004253183 A JP 2004253183A JP 2004253183 A JP2004253183 A JP 2004253183A JP 2006070308 A JP2006070308 A JP 2006070308A
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metal
hot metal
iron source
desulfurization
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JP4442369B2 (en
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Tomoyuki Ueno
智之 上野
Yuki Nabeshima
祐樹 鍋島
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JFE Steel Corp
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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
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for melting solid-iron source in a molten iron carrier by which even in the case of beforehand laying dephosphorized bare metal and/or desulfurized bare metal recovered at the slag-off time after dephosphorization and/or desulfurization of the molten iron, there is no possibility of phreatic explosion. <P>SOLUTION: A technique with which the solid iron source is beforehand laid into the molten iron carrying vessel, the molten iron from a blast furnace is received and this solid iron source is melted by using the sensible heat and stirring force, is improved. In this method, as the solid-iron source, the dephosphorized bare metal and/or the desulfurized bare metal which are agglomerated and solidified at the size of 200-1,500mm and recovered in the high temperature state of 100-600°C are used in the slag generated with the dephosphorization and/or the desulfurization of the molten during leaving the slag in the yard. In this time, it is preferable to beforehand lay the dephosphorized bare metal and/or the desulfurized bare metal into the molten iron carrier by using a heat-resistant hydraulic-type heavy machine. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、溶銑搬送容器での固体鉄源の溶解方法に係わり、特に、溶銑の取鍋脱硫後の排滓時に回収される脱硫地金を固体鉄源として再利用する技術に関する。   The present invention relates to a method for melting a solid iron source in a hot metal transfer container, and more particularly to a technique for reusing desulfurized metal recovered at the time of discharge after hot metal ladle desulfurization as a solid iron source.

従来より、高炉を有する製鉄所では、鉄スクラップ、型銑等の固体鉄源(一般には、冷鉄源と称され、常温のものを用いることが多い)を製鋼原料の一部として溶銑搬送容器(例えば、混銑車等)内へ前置きしてから高炉で溶製した溶銑を装入することが行われている(特許文献1参照)。この技術は、転炉へ製鋼原料としての溶銑を払い出した後の空の溶銑搬送容器から大気中へ放散される熱を、積極的に有効利用するために開発されたものである。また、溶銑払い出し後の熱間状態の混銑車に、小径の湿潤固体鉄源を投入し、該混銑車を複数回傾転して前記固体鉄源を加熱乾燥した後、溶銑を受銑する技術も開示されている(特許文献2参照)。これは、粒鉄、ダスト等の小径の固体鉄源が、単位重量あたりの表面積が大きく、水分含有量が高いため、熱間の混銑車内でも水分が蒸発せずに残留し、受銑時に水蒸気爆発するのを防止する技術として開発されたものである。従って、これらの技術は、高炉溶銑以外の固体鉄源を製鋼原料として利用するので、高炉からの溶銑の供給量が不足する場合には、いずれも有効な技術である。     Conventionally, in steelworks having a blast furnace, a solid iron source (generally called a cold iron source, which is often used at room temperature) such as iron scrap and mold iron is used as a part of the steelmaking raw material. It has been carried out (for example, Patent Document 1) that a hot metal melted in a blast furnace after being placed in the interior (for example, a kneading vehicle or the like) is used. This technology has been developed to actively utilize the heat dissipated into the atmosphere from an empty hot metal transfer container after the hot metal as a steelmaking raw material has been delivered to the converter. In addition, a technology for putting a small-diameter wet solid iron source into a hot kneaded car after the hot metal is discharged, tilting the kneaded car a plurality of times, heating and drying the solid iron source, and then receiving the hot metal Is also disclosed (see Patent Document 2). This is because small solid iron sources, such as granular iron and dust, have a large surface area per unit weight and a high moisture content, so that moisture remains without being evaporated even in a hot kneading vehicle. It was developed as a technology to prevent explosion. Therefore, since these techniques use a solid iron source other than the blast furnace hot metal as a steelmaking raw material, both are effective techniques when the amount of hot metal supplied from the blast furnace is insufficient.

さらに、最近は、溶銑予備処理の普及に伴い、上記した固体鉄源とは別種のものが多量に発生している。例えば、高炉の溶銑樋、傾注樋で行われる脱珪処理、処理容器に混銑車を利用する脱珪、脱燐、脱硫処理、取鍋を利用する脱硫処理を行うと、必然的にヤードへの排滓が行われ、その冷却時に地金(例えば、脱珪地金、脱燐地金、脱硫地金等)が回収されるからである。そして、これら地金を製鉄原料として再使用できれば、前記した高炉からの溶銑の供給量が不足する場合に非常に役立つことになるため、それら地金を混銑車に前置きしてから受銑、溶解し、得られた溶銑を再度脱燐、脱硫する技術も公開されている(特許文献3参照)。加えて、溶銑予備処理の脱硫には、処理容器として混銑車を用いるものと、取鍋を用いるものの2種類があるが、混銑車又は適当な溶銑運搬容器内で炉外脱硫した後の脱硫滓中に含まれる脱硫地金を、該脱硫滓から粗分離し、受銑前の混銑車又は適当な溶銑運搬鍋に投入して受銑及び炉外脱硫等を行わせることを特徴とする脱硫地金の再利用方法も提案されている(特許文献4参照)。なお、混銑車での溶銑脱硫処理は、精錬剤にソーダ灰若しくは石灰系フラックスを用い、溶銑に浸漬したランスを介してキャリアガスと共に吹き込むことで行われ、溶銑運搬鍋(以下、取鍋という)での脱硫は、精錬剤に石灰系フラックスをを用い、インペラを溶銑に浸漬して機械的に撹拌することで行われる。   Furthermore, recently, with the widespread use of hot metal pretreatment, a large amount of materials different from the above-mentioned solid iron source has been generated. For example, desiliconization treatment using blast furnace hot metal, decanting iron, desiliconization using a kneading vehicle, dephosphorization, desulfurization treatment, and desulfurization treatment using a ladle are inevitable. This is because waste metal is removed and bullion (for example, desiliconized bullion, dephosphorized bullion, desulfurized bullion, etc.) is recovered during cooling. And if these bullion can be reused as a raw material for iron making, it will be very useful when the amount of hot metal supplied from the blast furnace is insufficient. In addition, a technique for dephosphorizing and desulfurizing the obtained hot metal again has been disclosed (see Patent Document 3). In addition, there are two types of desulfurization for hot metal pretreatment: using a kneading vehicle as a processing vessel and using a ladle. Desulfurization after desulfurization outside the furnace in a kneading vehicle or a suitable hot metal carrying vessel. A desulfurization site characterized in that the desulfurization metal contained therein is roughly separated from the desulfurization slag and is put into a kneading car or a suitable hot metal transport pan before receiving to perform the slag and external desulfurization. A method for reusing gold has also been proposed (see Patent Document 4). The hot metal desulfurization treatment in the kneading car is performed by using soda ash or lime-based flux as the refining agent and blowing it with the carrier gas through the lance immersed in the hot metal. Desulfurization is performed by using a lime-based flux as a refining agent, immersing the impeller in hot metal, and mechanically stirring.

ところで、これら溶銑予備処理で回収される地金は、ヤードでスラグを水冷しているため、水分を多量に内包し、混銑車に前置きしてから受銑すると、水蒸気爆発を引き起こすので、自ずと使用量が制限されるという問題がある。前記脱燐地金及び脱硫地金も例外でなく、水分が約13質量%、化合水約8質量%にもなることがある。そのため、混銑車等に前置きすると、必ず突沸や水蒸気爆発の問題が懸念される。そのため、従来は転炉へ直接投入するようにしている。   By the way, the bullion collected in the hot metal pretreatment is slag water cooled in the yard. There is a problem that the amount is limited. The dephosphorized metal and desulfurized metal are no exception, and the water content may be about 13% by mass and the combined water may be about 8% by mass. For this reason, there is a concern about problems such as bumping and steam explosion when placed in front of a chaotic vehicle or the like. For this reason, conventionally, the direct input to the converter is made.

しかしながら、該脱燐地金及び/又は脱硫地金を転炉に投入すると、それが燐(P),硫黄(S)含有量が多いため、転炉装入前の溶銑脱硫処理における脱硫剤原単位が大幅に増加する、あるいは転炉での脱燐剤原単位が増加するという別の問題が生じ、脱硫、脱燐処理や熱経済の見地から溶銑搬送容器での前置きが望ましい。ところが、前記特許文献3には、この問題についての記載が一切見られない。また、対策として、前置き後に混銑車を傾転して予め水分を蒸発除去するという特許文献2の技術を応用することも考えられるが、それでは前置き時間が著しく長くなってしまい、効率良く高生産性を維持したい製鋼工程に支障を与えることになる。さらには、特許文献4には、「脱硫滓より地金を粗分離して回収方法として、マグネットロールを利用するのが最も容易且つ確実」及び「それに先立って脱硫滓の破砕及び整粒をしておくのが好ましい」との記載はあるが、それ以上の具体的な技術は記載されていない。恐らくその実施例に「25〜150mmの大きさに破砕整粒した」旨の記載があることから、そこでは破砕整粒に際して予め水冷されていると予想される。
特開昭54−142116号公報 特開平5−239523号公報 特開平8−193210号公報 特開昭55−94413号公報
However, when the dephosphorized metal and / or desulfurized metal is put into the converter, it contains a large amount of phosphorus (P) and sulfur (S), so the desulfurizing agent raw material in the hot metal desulfurization treatment before charging the converter Another problem that the unit greatly increases or the basic unit of dephosphorization agent in the converter arises, and it is desirable to place it in a hot metal transfer container from the viewpoint of desulfurization, dephosphorization treatment and thermal economy. However, Patent Document 3 does not show any description about this problem. Also, as a countermeasure, it is conceivable to apply the technique of Patent Document 2 in which the chaotic wheel is tilted after the pre-placement to evaporate and remove the water in advance, but this leads to a significant increase in the pre-place time, and efficient and high productivity. This will interfere with the steelmaking process that is desired to maintain the same. Furthermore, Patent Document 4 states that “It is easiest and most reliable to use a magnet roll as a method for roughly separating and recovering the metal from the desulfurization slag” and “prior to smashing and sizing the desulfurization slag. Although there is a description that “it is preferable”, no more specific technique is described. Presumably, there is a description in the example that “crushed and sized to a size of 25 to 150 mm”. Therefore, it is expected that the crushed and sized particles are cooled with water in advance.
JP 54-142116 A JP-A-5-239523 JP-A-8-193210 JP-A-55-94413

本発明は、かかる事情に鑑み、溶銑の脱燐及び/又は脱硫後の排滓時に回収される脱燐地金及び/又は脱硫地金を前置きしても、水蒸気爆発の恐れがない溶銑搬送容器での固体鉄源の溶解方法を提供することを目的としている。   In view of such circumstances, the present invention provides a hot metal transport container that does not cause a steam explosion even if a dephosphorized metal and / or desulfurized metal recovered at the time of dephosphorization and / or desulfurization after desulfurization is placed in advance. The object is to provide a method for dissolving solid iron sources at the same time.

発明者は、上記目的を達成するため、溶銑の脱燐及び/又は脱硫後の排滓時における地金の回収方法について鋭意研究を重ね、その成果を本発明に具現化した。   In order to achieve the above-mentioned object, the inventor has conducted earnest research on a method for recovering a bare metal at the time of dephosphorization of hot metal and / or waste after desulfurization, and has realized the results in the present invention.

すなわち、本発明は、溶銑搬送容器に固体鉄源を前置きし、高炉からの溶銑を受銑して、その顕熱及び撹拌力を用いて該固体鉄源を溶解するに際して、前記固体鉄源として、溶銑の脱燐及び/又は脱硫で生じたスラグをヤード放置中に、該スラグ内にサイズが200〜1500mmで凝集、固化し、100〜600℃の高温状態で回収された脱燐地金及び/又は脱硫地金とすることを特徴とする溶銑搬送容器での固体鉄源の溶解方法である。この場合、前記脱燐地金及び/又は脱硫地金を、前記溶銑搬送容器内に耐熱式油圧重機を用いて前置きしたり、あるいは前記溶銑搬送容器が混銑車であることが好ましい。   That is, in the present invention, the solid iron source is placed in advance in the hot metal transfer container, the hot iron from the blast furnace is received, and when the solid iron source is melted using the sensible heat and stirring force, the solid iron source is used as the solid iron source. The slag produced by dephosphorization and / or desulfurization of the hot metal was allowed to agglomerate and solidify in the slag at a size of 200 to 1500 mm while being left in the yard, and the dephosphorized metal recovered at a high temperature of 100 to 600 ° C. It is a melting method of the solid iron source in the hot metal transport container characterized by using desulfurized metal. In this case, it is preferable that the dephosphorized metal and / or the desulfurized metal is placed in advance in the hot metal transport container using a heat-resistant hydraulic heavy machine, or the hot metal transport container is a kneading vehicle.

本発明によれば、溶銑脱硫後の排滓時に回収される脱硫地金を溶銑搬送容器に前置きした際に水蒸気爆発が起きる恐れが解消される。従来、あまり利用されていなかった脱硫地金が固体鉄源として有効に再利用できるようになる。   According to the present invention, the risk of a steam explosion when the desulfurized metal recovered at the time of discharge after hot metal desulfurization is placed in the hot metal transfer container is eliminated. Conventionally, desulfurized metal that has not been used much can be effectively reused as a solid iron source.

以下、発明をなすに至った経緯をまじえ、本発明の最良の実施形態を説明する。   Hereinafter, the best embodiment of the present invention will be described based on the background of the invention.

脱硫地金等を溶銑搬送容器に前置きし、受銑した際に突沸、水蒸気爆発を起こすのは、溶銑予備処理容器(混銑車、取鍋等)からヤードへ排滓したスラグを水冷して、その内部で凝集、固化した地金をグリズリ等で分級するという従来の地金回収方法に問題があると考えた。つまり、かかる方法で回収した地金は、水分を内胞するばかりでなく、凝集が十分進行しないうちに固化を開始するのでサイズが小さく、比表面積が大きい。そのため、CaOが水和反応を起こし易いからである。   When desulfurized metal is put in front of the hot metal transport container and received, bumping and steam explosion are caused by cooling the slag discharged from the hot metal pretreatment container (mixing wheel, ladle, etc.) to the yard, We thought that there was a problem with the conventional bullion collection method of classifying the bullion that was agglomerated and solidified with grizzly etc. In other words, the bullion recovered by such a method not only encapsulates moisture but also starts to solidify before the agglomeration sufficiently proceeds, so the size is small and the specific surface area is large. Therefore, CaO tends to cause a hydration reaction.

そこで、発明者は、溶銑搬送容器へ前置きするまで100℃以上の高温を維持した地金であれば、突沸等の危険は回避できると考えた。そして、そのようにするには、少なくとも400℃以上の熱間で地金を回収する必要があった。   Therefore, the inventor considered that the risk of bumping or the like can be avoided if the metal is kept at a high temperature of 100 ° C. or higher until it is placed in the hot metal transfer container. And in order to do so, it was necessary to collect ingots at a temperature of at least 400 ° C. or higher.

まず、発明者は、ヤードに放置した脱燐及び/又は脱硫スラグをロングリーチ・ショベルで掻き揚げ、グリズリ(鋼鉄棒を一定間隔で配列した格子)にかけて、凝固した地金を熱いまま回収することを試みた。その結果、水冷を行わないため、鉄分の凝集が促進し、直径300mm×長さ1000mmと大型の地金を合計で1.5トン回収することに成功した。該地金の放射温度計で測定した温度は平均400℃であった。   First, the inventor scrapes the dephosphorized and / or desulfurized slag left in the yard with a long reach shovel and applies it to grizzly (grid with steel rods arranged at regular intervals) to collect the solidified metal in a hot state. Tried. As a result, since water cooling was not performed, the aggregation of iron was promoted, and a total of 1.5 tons of a large metal having a diameter of 300 mm and a length of 1000 mm was successfully recovered. The average temperature of the bare metal measured with a radiation thermometer was 400 ° C.

しかしながら、この方法では、グリズリにかける際の発塵が激しく、環境問題上、実施を認めるわけにはいかない。   However, with this method, dust generation is severe when it is applied to the grizzly, and implementation cannot be accepted due to environmental problems.

次に、脱燐及び/又は脱硫スラグはヤードに山積みしたままで、図1に示すように、その脱燐及び/又は脱硫スラグ1の山中より地金2だけを掴み出すことを試みた。そのためには、耐熱仕様の重機3が必要であるが、先端部「アイアンクロー型」油圧式重機の各部品を耐熱材で保護して利用することにした。   Next, while the dephosphorization and / or desulfurization slag was piled up in the yard, as shown in FIG. 1, an attempt was made to grasp only the metal 2 from the mountain of the dephosphorization and / or desulfurization slag 1. For this purpose, a heat-resistant heavy machine 3 is required. However, it was decided to protect and use each part of the tip "iron claw type" hydraulic heavy machine with a heat-resistant material.

その結果、5分間の作業で直径300mm以上×長さ500mmの取鍋脱硫地金を4トン程度回収でき、しかも発塵は肉眼で観察できないほど少なく、工程的に実施しても作業環境に問題がないと判断できた。従って、長時間の熱間使用に耐える耐熱仕様の重機3及び搬送車両(ダンプ等)があれば、この方法の実施で回収した地金を前置きに利用できると考え、このことを本発明の重要要件としたのである。   As a result, about 4 tons of ladle desulfurization metal with a diameter of 300 mm or more x length of 500 mm can be recovered in 5 minutes, and dust generation is so small that it cannot be observed with the naked eye. I was able to judge that there was no. Therefore, if there is a heat-resistant heavy machine 3 that can withstand long-term hot use and a transporting vehicle (such as a dump truck), it is considered that the bullion collected by the implementation of this method can be used in advance, which is important for the present invention. It was a requirement.

本発明では、脱燐地金及び/又は脱硫地金のサイズを200mm〜1500mmとするが、200mm以下では、比表面積が大きくなり、水分の吸収等が起き易くなるのを防止するためであり、1500mm超えでは、混銑車等への前置きが困難になるからである。なお、当然のことながら、混銑車等への前置きに用いる油圧式重機も耐熱仕様であることが好ましい。また、地金の温度を100〜600℃としたのは、100℃未満では吸水が発生する可能性があるため、600℃超えでは重機の耐熱温度を超過してしまうからである。   In the present invention, the size of the dephosphorized metal and / or desulfurized metal is set to 200 mm to 1500 mm. However, if it is 200 mm or less, the specific surface area is increased to prevent moisture absorption and the like from occurring easily. This is because when it exceeds 1500 mm, it is difficult to place the vehicle in front of a chaotic vehicle or the like. As a matter of course, it is preferable that the hydraulic heavy machine used in front of the chaotic vehicle or the like is also heat resistant. The reason why the temperature of the bare metal is set to 100 to 600 ° C. is that water absorption may occur when the temperature is lower than 100 ° C., and the heat resistance temperature of heavy machinery is exceeded when the temperature exceeds 600 ° C.

一般に、製鋼工場では、高炉からの溶銑を傾注樋を用いて脱珪処理し、溶銑搬送容器としての混銑車に受け入れ、脱燐処理してから転炉へ装入し、酸素吹錬で溶鋼を溶製する。その際、必要に応じ、取鍋を処理容器として、その中に保持した溶銑に脱硫剤を投入すると共に、インペラ等で機械的に撹拌する脱硫処理が行われる。本発明は、この脱燐及び/又は脱硫処理で生じたスラグに伴われている鉄分を、脱燐地金及び/又は脱硫地金として製鋼原料に再利用するものである。   Generally, in a steelmaking factory, hot metal from a blast furnace is desiliconized using a tilting iron, received in a kneading car as a hot metal transport container, dephosphorized, charged into a converter, and molten steel is supplied by oxygen blowing. Melt. At that time, if necessary, the ladle is used as a processing vessel, and a desulfurization process is performed in which a desulfurizing agent is introduced into the hot metal held therein and mechanically stirred with an impeller or the like. In the present invention, the iron content accompanying the slag generated by the dephosphorization and / or desulfurization treatment is reused as a dephosphorization metal and / or desulfurization metal for a steelmaking raw material.

ヤードに排滓された脱燐及び/又は脱硫スラグを山積みし、まだ該スラグの表面温度が800〜600℃のうちに、底部に凝集、固化している脱燐地金及び/又は脱硫地金を重機で掴み出した。使用した重機は、油圧ホースを耐熱材で覆い、さらにステンレス鋼帯を巻きつけ、油圧シリンダに鋼板カバーを施した油圧式重機である。これにより、5分間の掴みだし作業が実施可能であり、回収した脱燐地金及び/又は脱硫地金の温度は平均400℃であった。この地金を荷台に高炉滓を敷き詰めて断熱保護したダンプカーで運び、空の混銑車に耐熱重機を利用して前置き装入し、高炉からの溶銑を受銑し、その顕熱及び撹拌力で前置きした脱燐地金及び/又は脱硫地金を溶解した。この溶解に際して、まったく溶銑の突沸、水蒸気爆発等は起きなかった。ここで、受け入れた溶銑の重量は300トンであり、前置きした脱燐地金及び/又は脱硫地金の重量は3トンである。   Dephosphorization metal and / or desulfurization metal which piles up dephosphorization and / or desulfurization slag discharged to the yard and is still agglomerated and solidified at the bottom while the surface temperature of the slag is 800-600 ° C. Was grabbed with heavy machinery. The heavy machinery used is a hydraulic heavy machinery in which a hydraulic hose is covered with a heat-resistant material, a stainless steel strip is wound around, and a hydraulic cylinder is covered with a steel plate cover. As a result, the picking work for 5 minutes can be carried out, and the temperature of the recovered dephosphorized metal and / or desulfurized metal was 400 ° C. on average. This bullion is transported by a dump truck with a blast furnace laid on the carrier and insulated, and is placed in front of the empty kneading car using a heat-resistant heavy machine, receiving hot metal from the blast furnace, and using its sensible heat and stirring power. The pre-removed dephosphorized metal and / or desulfurized metal was dissolved. Upon melting, no hot metal bumping, steam explosion, etc. occurred. Here, the weight of the hot metal received is 300 tons, and the weight of the pre-dephosphorized metal and / or desulfurized metal is 3 tons.

そして、受銑後の混銑車は、図2に示したように、通常の脱燐処理、及び脱硫処理を経て製鋼工場に搬送され、転炉へ払い出した。この転炉への払い出しに際しては、未溶解物はまったく観察されず、本発明により、脱燐地金及び/又は脱硫地金が製鋼原料に有効利用できることが明らかである。   Then, as shown in FIG. 2, the kneaded vehicle after receiving was transported to a steelmaking factory through a normal dephosphorization process and a desulfurization process, and discharged to a converter. At the time of paying out to the converter, no undissolved material is observed, and it is clear that dephosphorized metal and / or desulfurized metal can be effectively used as a steelmaking raw material according to the present invention.

ヤードに山積みした脱燐及び/又は脱硫スラグから、熱間で地金を回収する方法を説明する模式図である。It is a schematic diagram explaining the method of collect | recovering hot metal from the dephosphorization and / or desulfurization slag piled up in the yard. 本発明に係る溶銑搬送容器での固体鉄源の溶解方法を説明する流れ図である。It is a flowchart explaining the melt | dissolution method of the solid iron source in the hot metal conveyance container which concerns on this invention.

符号の説明Explanation of symbols

1 脱燐及び/又は脱硫スラグ
2 地金
3 耐熱仕様の重機
1 Dephosphorization and / or desulfurization slag 2 Metal 3 Heat resistant heavy machinery

Claims (3)

溶銑搬送容器に固体鉄源を前置きし、高炉からの溶銑を受銑して、その顕熱及び撹拌力を用いて該固体鉄源を溶解するに際して、
前記固体鉄源として、溶銑の脱燐及び/又は脱硫で生じたスラグをヤード放置中に、該スラグ内にサイズが200〜1500mmで凝集、固化し、100〜600℃の高温状態で回収された脱燐地金及び/又は脱硫地金とすることを特徴とする溶銑搬送容器での固体鉄源の溶解方法。
When the solid iron source is placed in the hot metal transfer container in advance, the hot metal from the blast furnace is received, and when the solid iron source is melted using the sensible heat and stirring force,
As the solid iron source, slag produced by dephosphorization and / or desulfurization of hot metal was allowed to stand in the yard, and was aggregated and solidified at a size of 200 to 1500 mm in the slag and recovered at a high temperature of 100 to 600 ° C. A method for dissolving a solid iron source in a hot metal transfer container, characterized by using dephosphorized metal and / or desulfurized metal.
前記脱燐地金及び/又は脱硫地金を、前記溶銑搬送容器内に耐熱式油圧重機を用いて前置きすることを特徴とする請求項1記載の溶銑搬送容器での固体鉄源の溶解方法。   2. The method for melting a solid iron source in a hot metal transport container according to claim 1, wherein the dephosphorized metal and / or desulfurized metal is placed in advance in the hot metal transport container using a heat-resistant hydraulic heavy machine. 前記溶銑搬送容器が混銑車であることを特徴とする請求項1又は2記載の溶銑搬送容器での固体鉄源の溶解方法。

The method for melting a solid iron source in a hot metal transport container according to claim 1 or 2, wherein the hot metal transport container is a kneading vehicle.

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007031800A (en) * 2005-07-28 2007-02-08 Jfe Steel Kk Method for desulfurizing molten iron
JP2008081796A (en) * 2006-09-28 2008-04-10 Jfe Steel Kk METHOD FOR RECOVERING METAL FROM CaO-BASED DESULPHURIZED-SLAG
KR101489378B1 (en) 2013-06-12 2015-02-03 주식회사 포스코 Method for treating raw material

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007031800A (en) * 2005-07-28 2007-02-08 Jfe Steel Kk Method for desulfurizing molten iron
JP4687307B2 (en) * 2005-07-28 2011-05-25 Jfeスチール株式会社 Hot metal desulfurization method
JP2008081796A (en) * 2006-09-28 2008-04-10 Jfe Steel Kk METHOD FOR RECOVERING METAL FROM CaO-BASED DESULPHURIZED-SLAG
KR101489378B1 (en) 2013-06-12 2015-02-03 주식회사 포스코 Method for treating raw material

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