JPH0748632A - Method for removing impurity from scrap iron - Google Patents

Method for removing impurity from scrap iron

Info

Publication number
JPH0748632A
JPH0748632A JP15600893A JP15600893A JPH0748632A JP H0748632 A JPH0748632 A JP H0748632A JP 15600893 A JP15600893 A JP 15600893A JP 15600893 A JP15600893 A JP 15600893A JP H0748632 A JPH0748632 A JP H0748632A
Authority
JP
Japan
Prior art keywords
scraps
steel
iron
electric furnace
impurities
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.)
Pending
Application number
JP15600893A
Other languages
Japanese (ja)
Inventor
Masayoshi Mizuguchi
政義 水口
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.)
KOBAYASHI HEINOSUKE
Original Assignee
KOBAYASHI HEINOSUKE
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 KOBAYASHI HEINOSUKE filed Critical KOBAYASHI HEINOSUKE
Priority to JP15600893A priority Critical patent/JPH0748632A/en
Publication of JPH0748632A publication Critical patent/JPH0748632A/en
Pending 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

PURPOSE:To stably remove the impurities (Zn, Sn, Cu, etc.) contained in iron scraps at the time of making steel from the scraps. CONSTITUTION:Iron scraps are melted in an electric furnace or converter to make steel. In this case, the scraps are preheated at 550-1300 deg.C before being melted to previously remove the platings (e.g. Zn and Sn) depositing on the scraps or the impurities contained in the scraps. Consequently, since the nonferrous metals such as Zn and Sn depositing on the scraps are previously removed before melting, a steel having extremely low contents of Zn, Sn, etc., after melting is stably obtained.

Description

【発明の詳細な説明】Detailed Description of the Invention

【産業上の利用分野】本発明はスクラップを原料とする
鋼の製造方法において、不純物の少ない鋼の製造方法に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steel manufacturing method using scrap as a raw material and having a small amount of impurities.

【従来の技術】モータリゼーション化に相まって、わが
国の自動車の国内販売量は約800万台に達している。
逆にいうと、毎年ほぼ同じ台数の車が廃車され、スクラ
ップ化されているといえよう。以前は冷延鋼板に塗装を
施しただけの車が多く、スクラップ化され電気炉で溶解
して鋼製品を造っても、特に問題はなかった。しかしな
がら、最近の車は耐蝕性を向上させる為にZn,Sn等
のメッキを施した表面処理鋼板を使用したものが増大し
てきた。これらがスクラップ化され、電気炉で溶解され
ると、Zn,Sn等の不純物が鋼中に残留する。これら
の不純物は粒界に偏析し、熱間割れの原因となる為に、
表面処理鋼板等をスクラップ原料とした電気炉鋼では、
コンクリートバー等の低品位の鋼製品しか作られてなか
った。一方、表面処理鋼板のスクラップが今後ますます
増大すること、また電気炉鋼で転炉鋼と同程度の品位の
鋼製品をつくる社会的要求もあり、スクラップを溶解し
た溶鋼から、Zn,Sn等の不純物を除去する方法を確
立することが社会的に重要な課題である。これまで、Z
n,Sn等の不純物を除去する方法として、例えば、真
空蒸発除去,Arプラズマ蒸発等が試みられているが、
工業的にはまだ確立されているとはいい難い。
2. Description of the Related Art Due to motorization, domestic sales of automobiles in Japan have reached about 8 million.
Conversely, it can be said that almost the same number of cars are scrapped and scrapped every year. In the past, many cars were simply painted cold-rolled steel sheets, and there was no particular problem even if they were scrapped and melted in an electric furnace to make steel products. However, in recent years, an increasing number of cars use a surface-treated steel plate plated with Zn, Sn or the like in order to improve the corrosion resistance. When these are scrapped and melted in an electric furnace, impurities such as Zn and Sn remain in the steel. Since these impurities segregate at the grain boundaries and cause hot cracking,
In electric furnace steel made from scrap steel such as surface treated steel,
Only low-grade steel products such as concrete bars were made. On the other hand, there is an increasing demand for scraps of surface-treated steel sheets in the future, and there is also a social demand to produce steel products of the same quality as converter steel using electric furnace steel. From molten steel that melts scrap to Zn, Sn, etc. It is a socially important issue to establish a method for removing the impurities. So far, Z
As a method for removing impurities such as n and Sn, vacuum evaporation removal, Ar plasma evaporation, and the like have been tried.
It is hard to say that it is still established industrially.

【発明が解決しようとする課題】本発明は、Zn,Sn
等のメッキを施した表面処理鋼板をスクラップ原料とす
る電気炉または転炉製鋼法において、鋼の熱間割れの原
因となるZn,Snの不純物の少ない鋼を工業的に安価
につくることを目的とする。
DISCLOSURE OF THE INVENTION The present invention is based on Zn, Sn
In an electric furnace or converter steelmaking method using a surface-treated steel sheet plated with steel, etc. as a scrap material, it is an object to industrially produce a steel containing a small amount of impurities such as Zn and Sn that cause hot cracking of the steel. And

【課題を解決するための手段】本発明の要旨とするとこ
ろは、下記のとおりである。鉄屑(スクラップ)を電気
炉または、転炉で溶解して鋼をつくるにあたり、溶解に
供する前にスクラップを550℃以上、1300℃以下
で予備加熱することにより、スクラップに付着している
メッキ物(例えば、Zn,Sn等)または、混在してい
る不純物等を事前に除去することを特徴とする鋼の製造
方法。以下に、本発明について詳細に説明する。本発明
者は、表面処理鋼板を含む鉄屑を電気炉で溶解した後、
溶鋼中のZn,Snを分離するのは容易でないこと、ま
たメッキ鋼板のZn,Sn等の融点が鉄のそれに比べは
るかに低いことに着目し、電気炉装入前に非酸化性雰囲
気下で、これらのメッキ物の融点以上、例えば550℃
以上に加熱して、メッキ物を溶解〜溶出させることによ
り、不純物が転炉鋼並の溶鋼を電気炉鋼で得た。事前の
加熱温度は、該鉄屑にメッキされた非鉄金属の融点以上
の温度であれば良いが、通常1300℃を越えると、非
酸化性雰囲気下といえども酸化が急速に増大するため
に、加熱温度を1300℃以下とした。図1に表面処理
鋼板を含む鉄屑をAr雰囲気下で予備加熱した時の加熱
温度と、溶鋼中のZn,Snのトータル残存量との関係
を示すが、550℃より溶鋼中の不純物の減少が認めら
れ、800℃では0.02%以下となった。また、これ
らの方法は、Cu等の非鉄金属を含む鉄屑にも有効であ
った。Cuを含む場合は、銅の融点である1085℃以
上で鉄屑を電気炉装入前に予熱することにより、Cuの
濃度を0.2%以下にすることができた。 上記で述べ
たZn,Sn,Cuを予熱により溶解〜溶出させるにあ
たり、減圧下で処理することにより、不純物の除去がよ
り効果的にできる。 雰囲気条件としては、非酸化性雰
囲気が望ましいが、Zn,Sn等のメッキ付着物に対し
ては、酸化性雰囲気下でも、550℃以上加熱すること
により、メッキ物が該鉄屑から剥離するために、これら
の非鉄金属をある程度除去することが可能である。 ま
た、鉄屑を電気炉で溶解前に550℃以上に予熱するこ
とにより、プラスティック、ゴム等の混入物も溶融〜溶
出するために、非金属を含んだ鉄屑の処理についても有
効である。これらの予備加熱は電気溶解炉とは別に設け
てもよいし、電気溶解炉を兼用しても良い。また、転炉
でスクラップを多量に使用する際にも同様に有効であ
る。 実施例 1.表面処理鋼板を含む鉄屑をシュレッダーに
かけ小片化した後、予熱炉に入れ、Arガスを密封した
後、誘導加熱により800℃で加熱し、該鉄屑にメッキ
した非鉄金属を溶融〜溶出させた。 次に、鉄屑を電気
炉に移し、炭材を入れ酸素を40Nm/ton吹き込
みながら、アークで80分溶解した。次に、電気炉から
溶鋼を精錬炉に入れ、鍋底から溶鋼攪拌用のArを50
Nm/ton投入しながら合金を鍋上に設置したホッ
パーから溶鋼中に投入し、溶鋼を還元すると同時に溶鋼
温度を調節した。次に、精錬した溶鋼をタンディッシュ
に注入し、3m/minで引き抜きながら鋳造すること
により、125mm厚のスラブを得た。得られたスラブ
の一部を切り出し、不純物の濃度を調査した。その結果
を第1表に示す。 実施例 2 表面処理鋼板銅線を含む鉄屑をシュレッダーにかけ小片
化した後、真空加熱ができる予熱炉に入れ、炉内を最初
にArで置換した後、1キロパスカルに減圧し、誘導加
熱により1100℃で加熱した。 該鉄屑中の非鉄金属
分を溶融させた後、金属蒸気として気化させた。 気化
した蒸気はダクト途中で冷却させ、金属として回収し
た。 次に、鉄屑を電気炉に移し、炭材を入れ、酸素を
40Nm/ton吹き込みながら、アークで80分溶
解した。 次に、電気炉から溶鋼を精錬炉に入れ、鍋底
から溶鋼攪拌用のArを50Nm/ton投入しなが
ら、合金を鍋上に設置したホッパーから溶鋼中に投入
し、溶鋼を還元すると同時に溶鋼温度を調整した。精錬
した溶鋼をタンディッシュに注入し、3m/minで引
き抜きながら、125mm厚のスラブを得た。 得られ
たスラブの一部を切り出し、不純物の濃度を調査した。
その結果を第2表に示す。 実施例 3.表面処理鋼板を含む鉄屑をシュレッダーに
かけ小片化した後、予熱炉に入れガスバーナーで700
℃で予備加熱し、該鉄屑にメッキした非鉄金属を該鉄屑
より剥離させた。次に、鉄屑を電気炉に移し、炭材を入
れ酸素を40/ton吹き込みながら、アークで80分
溶解した。次に、電気炉から溶鋼を精錬炉に入れ、鍋底
から溶鋼攪拌用のArを50m/ton投入しなが
ら、合金を鍋上に設置したホッパーから溶鋼中に投入
し、溶鋼を還元すると同時に溶鋼温度をした。次に、精
錬した溶鋼をタンディッシュに注入し、3m/minで
引き抜きら鋳造することにより、125mm厚のスラブ
を得た。 得られたスラブの一部り出し、不純物の濃度
を調査した。その結果を第3表に示す。
The gist of the present invention is as follows. When iron scraps (scraps) are melted in an electric furnace or converter to produce steel, the scraps are preheated at 550 ° C or higher and 1300 ° C or lower before being subjected to melting, so that the plated products adhered to the scraps (For example, Zn, Sn, etc.) or mixed impurities are removed in advance. The present invention will be described in detail below. The present inventor, after melting iron scraps including the surface-treated steel plate in an electric furnace,
Paying attention to the fact that it is not easy to separate Zn and Sn in molten steel, and that the melting points of Zn, Sn, etc. of the plated steel sheet are much lower than that of iron, in a non-oxidizing atmosphere before charging in an electric furnace. , Above the melting point of these plated products, eg 550 ° C
By heating to the above temperature to dissolve and elute the plated product, molten steel with impurities equivalent to converter steel was obtained in electric furnace steel. The heating temperature in advance may be a temperature equal to or higher than the melting point of the non-ferrous metal plated on the iron scrap, but if it exceeds 1300 ° C., the oxidation rapidly increases even in a non-oxidizing atmosphere. The heating temperature was 1300 ° C. or lower. Fig. 1 shows the relationship between the heating temperature when iron scrap including surface-treated steel sheet is preheated in Ar atmosphere and the total residual amount of Zn and Sn in molten steel. Was observed, and it was 0.02% or less at 800 ° C. Moreover, these methods were also effective for iron scraps containing non-ferrous metals such as Cu. In the case of containing Cu, the Cu concentration could be reduced to 0.2% or less by preheating the iron scraps before charging the electric furnace at 1085 ° C. or higher, which is the melting point of copper. When the Zn, Sn, and Cu described above are dissolved and eluted by preheating, the impurities can be more effectively removed by treating under reduced pressure. As the atmospheric condition, a non-oxidizing atmosphere is desirable, but for a plated deposit such as Zn or Sn, the plated product is separated from the iron scrap by heating at 550 ° C. or more even in an oxidizing atmosphere. In addition, it is possible to remove these non-ferrous metals to some extent. Further, by preheating iron scraps to 550 ° C. or more before melting in an electric furnace, the contaminants such as plastics and rubber are also melted or eluted, so that it is also effective for the treatment of iron scraps containing non-metals. These preheating may be provided separately from the electric melting furnace, or may be combined with the electric melting furnace. It is also effective when a large amount of scrap is used in the converter. Example 1. Iron scraps including the surface-treated steel plate were shredded into small pieces, placed in a preheating furnace, sealed with Ar gas, and then heated at 800 ° C. by induction heating to melt to elute the nonferrous metal plated on the iron scraps. . Next, the iron scraps were transferred to an electric furnace, and a carbonaceous material was charged therein, and oxygen was melted for 80 minutes while being blown with 40 Nm 3 / ton of oxygen. Next, the molten steel is put into the refining furnace from the electric furnace, and Ar for stirring the molten steel is put in from the bottom of the pan.
While charging Nm 3 / ton, the alloy was charged into the molten steel from a hopper installed on a pan to reduce the molten steel and at the same time control the temperature of the molten steel. Next, the slab having a thickness of 125 mm was obtained by injecting the refined molten steel into a tundish and casting it while drawing it at 3 m / min. A part of the obtained slab was cut out and the concentration of impurities was investigated. The results are shown in Table 1. Example 2 Iron scraps containing a surface-treated steel sheet copper wire were shredded into small pieces, put into a preheating furnace capable of vacuum heating, the inside of the furnace was first replaced with Ar, and then depressurized to 1 kPa, by induction heating. Heated at 1100 ° C. The non-ferrous metal component in the iron scrap was melted and then vaporized as metal vapor. The vaporized vapor was cooled in the middle of the duct and recovered as metal. Next, the iron scrap was transferred to an electric furnace, charged with carbonaceous material, and melted by an arc for 80 minutes while blowing oxygen at 40 Nm 3 / ton. Next, the molten steel is put into the refining furnace from the electric furnace, and Ar for stirring the molten steel is introduced from the bottom of the pan at 50 Nm 3 / ton, while the alloy is put into the molten steel from the hopper installed on the pan to reduce the molten steel and at the same time. The temperature was adjusted. The slab having a thickness of 125 mm was obtained by pouring the refined molten steel into a tundish and drawing it out at 3 m / min. A part of the obtained slab was cut out and the concentration of impurities was investigated.
The results are shown in Table 2. Example 3. Iron scraps including surface-treated steel plates are shredded into small pieces, then put into a preheating furnace and 700 with a gas burner.
Preheating was performed at 0 ° C., and the non-ferrous metal plated on the iron scrap was separated from the iron scrap. Next, the iron scraps were transferred to an electric furnace, and a carbonaceous material was put therein, and oxygen was blown at 40 / ton, and was melted by an arc for 80 minutes. Next, the molten steel is put into the refining furnace from the electric furnace, while Ar for stirring the molten steel at 50 m 3 / ton is introduced from the bottom of the pot, the alloy is introduced into the molten steel from the hopper installed on the pot to simultaneously reduce the molten steel. Temperature. Next, the slab with a thickness of 125 mm was obtained by injecting the refined molten steel into a tundish, drawing it out at 3 m / min, and casting. A part of the obtained slab was extracted and the concentration of impurities was investigated. The results are shown in Table 3.

【発明の効果】本発明によれば、実施例に見られるよう
に、Zn,Sn,Cuの極めて少ない鋼が廃車等のスク
ラップから得られる。
According to the present invention, as can be seen from the examples, steel containing a very small amount of Zn, Sn and Cu can be obtained from scraps such as scrapped vehicles.

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

第1図は、鉄屑の予備加熱温度と電気溶解後の溶鋼中の
亜鉛,錫の濃度の関係を示す図。
FIG. 1 is a diagram showing the relationship between the preheating temperature of iron scrap and the concentrations of zinc and tin in molten steel after electromelting.

【手続補正書】[Procedure amendment]

【提出日】平成6年4月6日[Submission date] April 6, 1994

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】発明の名称[Name of item to be amended] Title of invention

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【発明の名称】 鉄屑からの不純物除去方法Method of removing impurities from iron scrap

Claims (1)

【特許請求の範囲】[Claims] 鉄屑(スクラップ)を電気炉または、転炉で溶解して鋼
をつくるにあたり、溶解に供する前にスクラップを55
0℃以上、1300℃以下で予備加熱することによりス
クラップに付着しているメッキ物(例えば、Zn,Sn
等)または、混在している不純物等を事前に除去するこ
とを特徴とする鋼の製造方法。
When melting iron scrap (scrap) in an electric furnace or a converter to make steel, 55
Plated material (eg Zn, Sn) attached to scrap by preheating at 0 ° C or higher and 1300 ° C or lower
Etc.) or mixed impurities are removed in advance.
JP15600893A 1993-05-20 1993-05-20 Method for removing impurity from scrap iron Pending JPH0748632A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15600893A JPH0748632A (en) 1993-05-20 1993-05-20 Method for removing impurity from scrap iron

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15600893A JPH0748632A (en) 1993-05-20 1993-05-20 Method for removing impurity from scrap iron

Publications (1)

Publication Number Publication Date
JPH0748632A true JPH0748632A (en) 1995-02-21

Family

ID=15618313

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15600893A Pending JPH0748632A (en) 1993-05-20 1993-05-20 Method for removing impurity from scrap iron

Country Status (1)

Country Link
JP (1) JPH0748632A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005118890A3 (en) * 2004-05-29 2006-04-27 Noel Warner Recovery of steel from contaminated scrap

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005118890A3 (en) * 2004-05-29 2006-04-27 Noel Warner Recovery of steel from contaminated scrap
GB2437374A (en) * 2004-05-29 2007-10-24 Noel Alfred Warner Recovery of steel from contaminated scrap
GB2437374B (en) * 2004-05-29 2010-03-24 Noel Alfred Warner Recovery of steel from contaminated scrap

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