JPH06220550A - Treatment of iron scrap containing zn in cupolar - Google Patents
Treatment of iron scrap containing zn in cupolarInfo
- Publication number
- JPH06220550A JPH06220550A JP1214993A JP1214993A JPH06220550A JP H06220550 A JPH06220550 A JP H06220550A JP 1214993 A JP1214993 A JP 1214993A JP 1214993 A JP1214993 A JP 1214993A JP H06220550 A JPH06220550 A JP H06220550A
- Authority
- JP
- Japan
- Prior art keywords
- scrap
- cupola
- iron
- iron scrap
- furnace
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、Znを含んだ鉄スクラッ
プをキュポラにて溶解する際の、スクラップ中のZnの優
先除去方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for preferentially removing Zn in scrap when melting iron scrap containing Zn in a cupola.
【0002】[0002]
【従来の技術】一般にキュポラにてZnを含んだスクラッ
プを溶解する際に、Znの沸点が 907℃であるが故に、キ
ュポラ炉の下層部(1500℃程度)において気化したZnが
上層部( 300〜500 ℃程度)で再び凝集し、キュポラ内
部にZnが蓄積してしまう現象が生じ、短期間でキュポラ
の操業を停止し、この蓄積したZnを炉冷後除去してい
た。2. Description of the Related Art Generally, when a scrap containing Zn is melted in a cupola, since the boiling point of Zn is 907 ° C., the vaporized Zn in the lower part of the cupola furnace (about 1500 ° C.) is At around 500 ℃), the agglomeration occurred again and Zn accumulated inside the cupola. The cupola operation was stopped in a short period of time, and the accumulated Zn was removed after cooling the furnace.
【0003】従来Znを含んだ鉄スクラップを鉄源として
利用する場合、以上の問題点を解決するために特開昭57
−85916 号公報に示されるように、スクラップを溶解す
る前処理として該スクラップをロータリーキルンに装入
してガスバーナーでZnの沸点付近の温度に加熱して、Zn
を蒸発させて分離除去する方法、またさらにこのスクラ
ップの加熱に溶解炉の排ガスを利用する方法が特公昭63
−50406 号公報に提案されている。Conventionally, in order to solve the above-mentioned problems when utilizing iron scrap containing Zn as an iron source, JP-A-57-57
-85916, as a pretreatment for melting scrap, the scrap is charged into a rotary kiln and heated by a gas burner to a temperature near the boiling point of Zn.
There is a method of vaporizing and separating and removing, and a method of utilizing the exhaust gas of the melting furnace for heating this scrap.
It is proposed in -50406 publication.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、従来の
方法ではスクラップからZnを除去するために、溶解炉の
系外において前処理を行うため、処理後のスクラップを
溶解炉へ投入するまでの間の温度降下、酸化のために、
熱ロス、歩留り低下が生じる。また、特公昭63−50406
号公報のように、溶解炉の排ガスを利用する場合でも、
例えば煙道にスクラップを保持しておく複雑な設備が必
要となる。また、この場合にはキュポラからの排ガス温
度は常に一定なので、一定温度での加熱しかできずスク
ラップ予熱温度をコントロールするためには、別途加熱
装置(ガスバーナー、誘導コイルなど)が必要となり、
更に設備が複雑化してしまうことになる。However, in the conventional method, the pretreatment is performed outside the melting furnace in order to remove Zn from the scrap, so that the scrap after the treatment is charged into the melting furnace. Due to temperature drop and oxidation,
Heat loss and yield decrease occur. In addition, Japanese Examined Japanese Patent Publication Sho 63-50406
Even when using the exhaust gas from the melting furnace,
For example, complex equipment is needed to hold the scrap in the flue. Also, in this case, since the exhaust gas temperature from the cupola is always constant, only heating at a constant temperature is possible, and a separate heating device (gas burner, induction coil, etc.) is required to control the scrap preheating temperature,
Furthermore, the equipment becomes more complicated.
【0005】本発明は、キュポラでZnを含む鉄スクラッ
プを溶解するに際して、簡単な装置を附設するだけでZn
を除去し、かつ歩留りよく鉄スクラップを溶解するキュ
ポラでのZnを含む鉄スクラップの処理方法を提案するこ
とを目的とするものである。According to the present invention, when the iron scrap containing Zn is melted in the cupola, only a simple device is attached to the Zn scrap.
An object of the present invention is to propose a method for treating iron scrap containing Zn in a cupola that removes iron and dissolves iron scrap with good yield.
【0006】[0006]
【課題を解決するための手段】本発明は、鉄スクラップ
をキュポラにて溶解するに際して、装入され堆積してい
るスクラップの上部を誘導加熱により、Znの沸点以上の
温度に加熱し、スクラップに含まれるZnを気化させて分
離排出することを特徴とするキュポラでのZnを含む鉄ス
クラップの処理方法である。According to the present invention, when melting iron scrap with a cupola, the upper part of the scrap that has been charged and deposited is heated to a temperature not lower than the boiling point of Zn by induction heating to produce scrap. A method for treating iron scrap containing Zn in a cupola, characterized in that the contained Zn is vaporized and separated and discharged.
【0007】[0007]
【作用】本発明では、キュポラ内に装入されたスクラッ
プ上部を誘導加熱によりZnの沸点以上の温度に加熱する
のでキュポラ下部からの熱風と相まってZnが気化分離さ
れ、Zn蒸気の一部は酸化され、集塵装置等で除去され
る。従って、キュポラ内に装入されたスクラップは、上
面部においてZnが気化して上方へ排出された後に、溶解
されるため、キュポラでのZnの蓄積を防ぐことが可能と
なる。In the present invention, the upper part of the scrap charged in the cupola is heated to a temperature higher than the boiling point of Zn by induction heating, so that Zn is vaporized and separated together with the hot air from the lower part of the cupola, and a part of Zn vapor is oxidized. And removed by a dust collector or the like. Therefore, since the scrap charged in the cupola is melted after Zn is vaporized and discharged upward in the upper surface portion, it is possible to prevent accumulation of Zn in the cupola.
【0008】さらに、炉内で直接処理されるために、炉
外での処理に比べて温度降下、酸化がなく、熱ロス、歩
留り低下も生じない。Znを含んだスクラップとは、例え
ば亜鉛めっき鋼板くず、Zn合金が付着したくずなどであ
る。ここでいうスクラップ上部とは、キュポラ内に装入
され増積したスクラップの上方向にさらされた表面部を
含んだ部位のことである。Further, since the treatment is carried out directly in the furnace, there is no temperature drop or oxidation, and no heat loss or yield reduction, as compared with the treatment outside the furnace. The scrap containing Zn is, for example, scrap of galvanized steel plate, scrap to which a Zn alloy is attached, and the like. The scrap upper portion as referred to herein is a portion including a surface portion of the scrap loaded and accumulated in the cupola and exposed upward.
【0009】本発明における誘導コイルの設置位置は、
上記の装入スクラップ上面部において、最も強い誘導加
熱がなされる位置にするのが、最も効果的である。誘導
コイルに供給する交流電流周波数は、特に指定はなく一
般に50Hz以上ならよいが、装入スクラップのサイズが大
きい場合には低周波を、サイズが小さい場合には高周波
を選択する方がよく、スクラップの大きさに応じて、周
波数を最適に選択して加熱すれば効率が良い。The installation position of the induction coil in the present invention is
It is most effective to set the position where the strongest induction heating is performed on the upper surface of the charging scrap. The frequency of the alternating current supplied to the induction coil is generally 50Hz or more without any particular specification.However, if the size of the scrap to be charged is large, it is better to select the low frequency and if the size is small, it is better to select the high frequency. It is efficient if the frequency is optimally selected and heated according to the size of.
【0010】本発明法によれば、Znのみでなく、低沸点
のPb、Cd等を含むものでも同一原理で分離除去すること
ができる。また、本発明によれば、加熱は誘導コイルを
用いるため、電流のON/OFFあるいは強度調整によ
り、加熱/非加熱を自由に制御でき、誘導コイルの設置
位置を変更することにより、加熱位置も自由に設定でき
る。According to the method of the present invention, not only Zn but also those containing low boiling point Pb, Cd, etc. can be separated and removed by the same principle. Further, according to the present invention, since the induction coil is used for heating, heating / non-heating can be freely controlled by turning the current ON / OFF or adjusting the intensity, and the heating position can be changed by changing the installation position of the induction coil. It can be set freely.
【0011】以下、本発明を実施例に基づいてより詳し
く説明する。The present invention will be described below in more detail based on examples.
【0012】[0012]
【実施例】図1はキュポラを模式的に示したものであ
り、溶解能力は3ton /hrである。炉本体2内の原料ス
クラップ1は、適時原料投入孔3より投入される。誘導
コイル4には、交流電源5が配線6を介して接続されて
いる。この高周波電源5は、1000Hz、500kw の規模のも
のである。EXAMPLE FIG. 1 schematically shows a cupola having a dissolving capacity of 3 ton / hr. The raw material scrap 1 in the furnace body 2 is charged from the raw material charging hole 3 at appropriate times. An AC power supply 5 is connected to the induction coil 4 via a wire 6. The high frequency power source 5 is of a scale of 1000 Hz and 500 kw.
【0013】本発明を実施するために亜鉛めっき鋼板く
ずを上記キュポラを用いて溶解し、その際に誘導コイル
には、200kw の電力を連続的に投入した。また、従来技
術と比較するために、同じく上記のキュポラを用いて誘
導コイルによる加熱を行わず亜鉛めっき鋼板くずを溶解
した。2週間の連続操業後、操業を停止し、炉内を調べ
たところ、比較例の場合には図1の8に示す羽口の上方
の炉壁内面に亜鉛および亜鉛濃度の高い塊状の付着物が
認められたが、誘導加熱を実施した別のキャンペーンで
は、2週間の連続操業でも、この塊状の付着物は認めら
れなかった。In order to carry out the present invention, galvanized steel scraps were melted using the cupola, and at that time, 200 kw of electric power was continuously supplied to the induction coil. In addition, in order to compare with the prior art, the above-mentioned cupola was also used to melt the galvanized steel scrap without heating by the induction coil. After continuous operation for 2 weeks, the operation was stopped and the inside of the furnace was examined. As a result, in the case of the comparative example, zinc and lumpy deposits with a high zinc concentration were formed on the inner surface of the furnace wall above the tuyere shown in FIG. However, in another campaign in which induction heating was carried out, even in the continuous operation for 2 weeks, these lump-shaped deposits were not observed.
【0014】本発明のように誘導加熱によりキュポラ内
に装入されたスクラップ上部におけるZnの除去を実施で
きない従来方法では、Znを含んだスクラップを溶解する
際に、キュポラ内にZnが蓄積するため、操業を中断し
て、蓄積したZnを除去する作業が必要となるか、あるい
は、Znを含んだスクラップの使用を避けるしかなかっ
た。In the conventional method in which the removal of Zn in the upper portion of the scrap charged into the cupola by induction heating cannot be carried out as in the present invention, Zn is accumulated in the cupola when the scrap containing Zn is melted. However, the operation must be stopped to remove the accumulated Zn, or the use of scrap containing Zn must be avoided.
【0015】もう一つの比較例として、炉外にてZn除去
の前処理を行う方法を示す。すなわち亜鉛メッキ鋼板く
ずをロータリーキルンに供給し、ガスバーナーによって
約1000℃まで加熱してZnを蒸発分離させた後に、従来型
キュポラにて溶解操業する方法である。この方法によっ
て得られた溶湯の歩留りと、先に示した本発明の実施例
における歩留りを比較して図2に示す。As another comparative example, a method of performing a pretreatment for removing Zn outside the furnace will be shown. That is, this is a method in which galvanized steel scrap is supplied to a rotary kiln, heated to about 1000 ° C. by a gas burner to evaporate and separate Zn, and then melted and operated in a conventional cupola. The yield of the molten metal obtained by this method is compared with the yield in the above-mentioned embodiment of the present invention, and shown in FIG.
【0016】本発明の場合には鉄の歩留りが94%と高い
のに比べ比較例の場合には、ロータリーキルン内で酸化
された鉄の一部がキュポラに搬送・装入される時点でス
ケールとして分離され、キュポラに装入される全鉄(金
属鉄と酸化鉄の合計)量自体が低下しているため、鉄源
歩留りが85%と低くなっている。また、本発明では、Zn
を含んだスクラップを溶解する場合のみ誘導加熱を行
い、それ以外の場合は、誘導加熱は行わないので、電力
を溶解エネルギーの一部として利用しているのではな
く、電力コスト増加による非経済的な溶解にはならな
い。In the case of the present invention, the yield of iron is as high as 94%, whereas in the case of the comparative example, a part of iron oxidized in the rotary kiln is used as a scale at the time of being conveyed and charged into the cupola. The total iron content (total of metallic iron and iron oxide) that has been separated and charged into the cupola has decreased, resulting in a low iron source yield of 85%. Further, in the present invention, Zn
Induction heating is performed only when melting scrap containing smelting, and in other cases, induction heating is not performed.Therefore, electricity is not used as a part of melting energy, but uneconomical due to increased power costs. It does not dissolve easily.
【0017】[0017]
【発明の効果】本発明では、キュポラ内の装入スクラッ
プ上部から、誘導加熱によりZnを気化させて除去させる
ようにしたため、従来法においてZnを含んだスクラップ
を溶解した際に生じるキュポラ内におけるZnの蓄積をな
くすことができるようになった。故に炉内に蓄積したZn
を除去するために、操業を中断することなく、Znを含ん
だスクラップを使用した場合でも安定した操業を行うこ
とができるようになった。In the present invention, since Zn is vaporized and removed from the upper portion of the charging scrap in the cupola by induction heating, the Zn in the cupola generated when the scrap containing Zn is melted by the conventional method is dissolved. It has become possible to eliminate the accumulation of. Therefore Zn accumulated in the furnace
Therefore, stable operation can be performed even when scrap containing Zn is used for removing the above without interrupting the operation.
【0018】また、本発明ではZnが効率よく系外に排出
できるため、キュポラの排ガス処理系の一部にZn凝集設
備を設置することにより、ZnまたはZn酸化物の回収、再
利用が可能となり、Zn資源の有効利用ができるという利
点も有する。Further, in the present invention, since Zn can be efficiently discharged out of the system, it is possible to recover and reuse Zn or Zn oxide by installing a Zn coagulation facility in a part of the exhaust gas treatment system of cupola. , It also has an advantage that Zn resources can be effectively used.
【図1】本発明で用いるキュポラの概要を示す断面模式
図。FIG. 1 is a schematic sectional view showing an outline of a cupola used in the present invention.
【図2】本発明と比較例の溶湯歩留りを比較した図。FIG. 2 is a diagram comparing the molten metal yields of the present invention and a comparative example.
1 原料スクラップ 2 炉本体 3 原料投入孔 4 誘導コイル 5 高周波電源 6 配線 7 出湯孔 8 送風管 1 Raw Material Scrap 2 Furnace Main Body 3 Raw Material Input Hole 4 Induction Coil 5 High Frequency Power Supply 6 Wiring 7 Hot Water Hole 8 Blower Pipe
Claims (1)
際して、装入され堆積しているスクラップの上部を誘導
加熱により、Znの沸点以上の温度に加熱し、スクラップ
に含まれるZnを気化させて分離排出することを特徴とす
るキュポラでのZnを含む鉄スクラップの処理方法。1. When melting iron scrap in a cupola, the upper part of the charged and deposited scrap is heated to a temperature not lower than the boiling point of Zn by induction heating to vaporize and separate Zn contained in the scrap. A method of treating iron scrap containing Zn in a cupola, characterized by discharging.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1214993A JPH06220550A (en) | 1993-01-28 | 1993-01-28 | Treatment of iron scrap containing zn in cupolar |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1214993A JPH06220550A (en) | 1993-01-28 | 1993-01-28 | Treatment of iron scrap containing zn in cupolar |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06220550A true JPH06220550A (en) | 1994-08-09 |
Family
ID=11797433
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1214993A Pending JPH06220550A (en) | 1993-01-28 | 1993-01-28 | Treatment of iron scrap containing zn in cupolar |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06220550A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4701521B2 (en) * | 2001-03-14 | 2011-06-15 | 大同特殊鋼株式会社 | Cold crucible dissolution method |
-
1993
- 1993-01-28 JP JP1214993A patent/JPH06220550A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4701521B2 (en) * | 2001-03-14 | 2011-06-15 | 大同特殊鋼株式会社 | Cold crucible dissolution method |
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