JPS6273591A - Melted material agitator in furnace - Google Patents

Melted material agitator in furnace

Info

Publication number
JPS6273591A
JPS6273591A JP21410685A JP21410685A JPS6273591A JP S6273591 A JPS6273591 A JP S6273591A JP 21410685 A JP21410685 A JP 21410685A JP 21410685 A JP21410685 A JP 21410685A JP S6273591 A JPS6273591 A JP S6273591A
Authority
JP
Japan
Prior art keywords
molten metal
furnace
melting
stirring device
inductor
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
JP21410685A
Other languages
Japanese (ja)
Other versions
JPH0570915B2 (en
Inventor
和昭 谷田
金丸 政雄
美蔦 芳宏
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.)
Kobe Steel Ltd
Rozai Kogyo Kaisha Ltd
Original Assignee
Kobe Steel Ltd
Rozai Kogyo Kaisha Ltd
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 Kobe Steel Ltd, Rozai Kogyo Kaisha Ltd filed Critical Kobe Steel Ltd
Priority to JP21410685A priority Critical patent/JPS6273591A/en
Publication of JPS6273591A publication Critical patent/JPS6273591A/en
Publication of JPH0570915B2 publication Critical patent/JPH0570915B2/ja
Granted legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、炉床下に設置され非接触状態で炉内溶湯の攪
拌を行うための炉内溶湯攪拌装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to an in-furnace molten metal stirring device that is installed under the hearth and stirs molten metal in the furnace in a non-contact manner.

〔従来技術〕[Prior art]

従来、非接触式の炉内溶湯撹拌装置には、移動磁界を利
用して炉内溶湯を撹拌し移動させるようにした電磁溶湯
撹拌装置が開発されている。しかしながら、この種の撹
拌装置は主として溶湯の均熱及び均質を目的とし、溶湯
表面を微動させる程度の小容量のものであり、また溶湯
移動の起点位置も一定に限定されている。そのため、溶
湯と溶は残りの残塊とが渾然一体となって炉内に存在す
る溶解の溶は落ち後半時において、溶解の促進並びに精
錬及び除滓の合理化を図るには不適当であり、次のよう
な不都合を招来する。
Conventionally, as a non-contact type molten metal stirring device, an electromagnetic molten metal stirring device that uses a moving magnetic field to stir and move the molten metal in a furnace has been developed. However, this type of stirring device is mainly intended to uniformly heat and homogenize the molten metal, and has a small capacity that allows the surface of the molten metal to move slightly, and the starting point of movement of the molten metal is also limited to a fixed position. Therefore, the molten metal and the remaining lumps are mixed together and the molten metal existing in the furnace falls during the latter half of the period, which is inappropriate for promoting melting and streamlining refining and slag removal. This causes the following inconveniences.

(1) 溶解後半時点での積極的な溶湯移動が困難なた
め、この時点での残塊浸漬並びに低温溶解の促進ができ
ない。− (2) 溶湯は静止またはこれに近い状態にあるため、
精錬時においては精錬用ランスを渦中に浸漬し、バブリ
ングのみによる精錬しかできないので、作業が煩雑にな
り、また精錬効果を充分に得るためには長時間の精錬作
業と大量の精錬剤を要する。
(1) Since it is difficult to actively move the molten metal in the latter half of melting, it is impossible to immerse the remaining mass at this point and promote low-temperature melting. - (2) Since the molten metal is at rest or in a state close to this,
During refining, a refining lance is immersed in a vortex and refining can only be done by bubbling, which makes the work complicated and requires long refining work and a large amount of refining agent to obtain the full refining effect.

(3) また、溶湯表面に浮遊する溶滓の除去時に於い
ては、浮上滓が炉内全体に拡散した状態にあることに起
因して、炉側壁に設けられた大開口部から運搬車に搭載
された除滓治具又は専用除滓(撹拌を含む)機にて溶滓
を炉外へ排出するときの作業が非常に煩雑で且つ困難を
極め、甚だ非能率的であって長時間を要している。
(3) Furthermore, when removing molten slag floating on the surface of the molten metal, due to the floating slag being spread throughout the furnace, The work of discharging slag from the furnace using the on-board slag removal jig or dedicated slag removal (including stirring) machine is extremely complicated and difficult, and is extremely inefficient and takes a long time. I need it.

〔発明の目的〕[Purpose of the invention]

本発明は、上記従来の問題点を考慮してなされたもので
あって、溶湯を積極的に移動可能かつその移動方向を可
変とし、またその移動起点位置及び移動方向を適切に選
択できる構成とし、炉内残塊の溶解促進によってメタル
ロスの低減及び省エネルギ化を実現すると共に、精錬及
び除滓を容易にしてその合理化をなし得る炉内溶湯撹拌
装置の提供を目的とするものである。
The present invention has been made in consideration of the above conventional problems, and has a configuration in which the molten metal can be actively moved, the direction of movement thereof is variable, and the starting point position and direction of movement can be appropriately selected. The object of the present invention is to provide an in-furnace molten metal stirring device that can reduce metal loss and save energy by promoting the melting of residual lumps in the furnace, and can facilitate and rationalize refining and slag removal.

〔発明の構成〕[Structure of the invention]

本発明の炉内溶湯撹拌装置は、炉床下に設置される電磁
溶湯撹拌装置であって、上記電磁溶湯撹拌装置に設けら
れている誘導子が、磁界移動方向の転換が自在で溶湯移
動能力を有し、かつ水平移動と回動と昇降移動とが自在
となるように設けて、炉内溶湯の移動起点及び移動方向
を各溶解工程の段階に応じて適正に選択j7得るように
構成したことを特徴とするものである。
The in-furnace molten metal stirring device of the present invention is an electromagnetic molten metal stirring device installed under the hearth, and the inductor provided in the electromagnetic molten metal stirring device can freely change the direction of magnetic field movement and improve the molten metal movement ability. and is arranged so that it can be moved horizontally, rotated, and moved up and down freely, so that the starting point and direction of movement of the molten metal in the furnace can be appropriately selected according to the stage of each melting process. It is characterized by:

〔実施例〕〔Example〕

本発明の一実施例を第1図乃至第3図に基づいて説明す
れば、以下の通りである。
An embodiment of the present invention will be described below based on FIGS. 1 to 3.

第1図は、本実施例の炉内溶湯撹拌装置の概要を示すと
共に、溶解溶は落ち後半時における炉内状況を示してい
る。アルミニウム溶解炉本体の下部は、円筒形状を成す
側部炉壁1と皿形状から成る底部炉床2により形成され
、上記炉床2の端縁上に設けられた炉傾動芯5を中心と
して、その位置に対向する上記炉床2の対向端縁部に作
用端が下から結合されている傾動シリンダー6によって
、溶解炉本体が傾動自在となるように構成されている。
FIG. 1 shows an overview of the in-furnace molten metal agitation device of this embodiment, and also shows the situation in the furnace in the second half of the period when the molten metal has subsided. The lower part of the aluminum melting furnace body is formed by a side furnace wall 1 having a cylindrical shape and a bottom hearth 2 having a dish shape. The melting furnace main body is configured to be tiltable by a tilting cylinder 6 whose working end is connected from below to the opposing edge of the hearth 2 facing that position.

側部炉壁1の下端部には、炉内部の溶滓を除去するため
の除滓口3及び溶湯取出しのための出湯口4が設けられ
ている。炉内底部には炉内溶湯8が溜められ、溶湯8の
表面には、溶解後半の状況を呈するように溶は落ち前の
残塊9が露出しかつ溶滓10が浮遊している。
At the lower end of the side furnace wall 1, a slag removal port 3 for removing molten slag inside the furnace and a tapping port 4 for taking out molten metal are provided. Molten metal 8 is stored at the bottom of the furnace, and on the surface of the molten metal 8, residual lumps 9 are exposed before the melt falls off, and slag 10 is floating, as if in the latter half of melting.

アルミニウム溶解炉本体の下方には、その底部炉床2の
下面に対して非接触状態となるように電磁溶湯撹拌装置
7が設置されている。この電磁溶湯撹拌装置7の上面は
、上記炉床2と一定間隔をおいて近接して対面し得るよ
うな凹面形状を有し、同撹拌装置7には第2図に示した
ような方形から成る誘導子(磁界発生装置)7aが設け
られている。そして、電磁溶湯撹拌装置7は前記溶解炉
の炉床2に対して、昇降移動、回動、及び走行レール1
2による水平移動がそれぞれ自在となるように構成され
、且つ上記誘導子7aを炉床2下の任意の位置に設定し
得るようになされている。上記誘導子7aは、磁界の移
動方向の転換が自在であって移動磁界を発生し、また正
逆転が可能であって上記移動磁界を利用して炉内の溶湯
8を正逆可変に移動させ得る能力を具備している。
An electromagnetic molten metal stirring device 7 is installed below the aluminum melting furnace main body so as to be in a non-contact state with the lower surface of the bottom hearth 2. The upper surface of this electromagnetic molten metal stirring device 7 has a concave shape so that it can face the hearth 2 closely at a certain distance. An inductor (magnetic field generating device) 7a is provided. The electromagnetic molten metal stirring device 7 moves up and down, rotates, and moves on the running rail 1 with respect to the hearth 2 of the melting furnace.
2 can be moved freely horizontally, and the inductor 7a can be set at any position below the hearth 2. The inductor 7a is capable of changing the moving direction of the magnetic field and generates a moving magnetic field, and is also capable of forward and reverse movement, and uses the moving magnetic field to move the molten metal 8 in the furnace in variable forward and reverse directions. have the ability to obtain

以上の構成に於いて、本発明に係るが内湾湯撹拌装置の
操作手順を、各工程順に説明すれば、以下の通りである
In the above configuration, the operating procedure of the inner bay hot water stirring device according to the present invention will be explained in the order of each step as follows.

[1] 炉内残塊9の溶解促進工程 炉原料溶解後半時には前記のごとく炉内溶湯8の表面上
に溶は落ち前の残塊9が浮遊した状態にある。この残塊
9の溶解を促進するため、電磁溶湯撹拌装置7を走行レ
ール12上で水平移動させ、第2図のD位置に示すよう
に誘導子7aを炉壁1側に接近して設置し、磁界の移動
方向を正逆転させる。
[1] Step of promoting dissolution of the remaining lumps 9 in the furnace During the latter half of the melting of the raw materials in the furnace, the remaining lumps 9, which have not yet melted, are floating on the surface of the molten metal 8 in the furnace, as described above. In order to promote the melting of this residual mass 9, the electromagnetic molten metal stirring device 7 is moved horizontally on the running rail 12, and the inductor 7a is installed close to the furnace wall 1 side as shown at position D in FIG. , reverse the direction of movement of the magnetic field.

[2] 溶湯による炉内残塊9の浸漬溶解工程次に、電
磁溶湯撹拌装置7を、誘導子7aの中心が炉床2の中心
と合致するように移動させ、第2図のB位置・A位置又
はC位置に示すように、誘導子7aを炉中心と除滓口3
を結ぶ方向(B位置)、又はこの方向に対し左右回り各
々45度をなすいずれかの方向(A位置またはC位置)
に位置を設定し、誘導子7aにより磁界移動の正逆転を
数回繰り返す。
[2] Process of immersing and melting the remaining lump 9 in the furnace with molten metal Next, move the electromagnetic molten metal stirring device 7 so that the center of the inductor 7a matches the center of the hearth 2, and move the electromagnetic molten metal stirring device 7 to position B in FIG. As shown at position A or position C, the inductor 7a is connected to the center of the furnace and the slag removal port 3.
(Position B), or any direction that makes 45 degrees to the left and right to this direction (Position A or C)
, and repeat the forward and reverse movement of the magnetic field several times using the inductor 7a.

[3] 自動精錬工程 上記の浸漬溶解工程によって炉内溶湯8が所定の温度に
達すると、自動精錬工程は次の要領で実施される。
[3] Automatic refining process When the molten metal 8 in the furnace reaches a predetermined temperature through the above-described immersion melting process, the automatic refining process is carried out as follows.

電磁溶湯撹拌装置7は炉床2の中心位置で回動し、誘導
子7aが第2図に示したC位置ニ設定すれ、磁界移動の
正逆転が数回繰り返される。この磁界移動の正逆転と共
に、炉内溶湯8中に精錬用ランス11・11を装入し、
精錬剤を炉内へ自動供給する。上記精錬用ランス11は
その先端が前記誘導子7aの一端付近に位置するように
配置される。
The electromagnetic molten metal stirring device 7 rotates at the center of the hearth 2, the inductor 7a is set at the C position shown in FIG. 2, and the forward and reverse movement of the magnetic field is repeated several times. Along with the forward and reverse movement of the magnetic field, the refining lances 11 and 11 are charged into the molten metal 8 in the furnace,
Automatically supplies refining agent into the furnace. The refining lance 11 is arranged so that its tip is located near one end of the inductor 7a.

[4] 除滓工程 上記自動精錬工程後は、電磁溶湯撹拌装置7を回動させ
、その誘導子7aは、炉内溶湯8の表面上に浮遊し散在
する溶滓10を除滓口3付近に集合させ得るような位置
すなわち第2図に示したB位置に設定するか、或いは上
記溶滓10を炉中央付近に集合させ得るような位置すな
わち第2図に示したD位置に設定して、磁界の移動方向
を正逆転させる。
[4] Slag removal process After the above automatic refining process, the electromagnetic molten metal stirring device 7 is rotated, and its inductor 7a removes the slag 10 floating and scattered on the surface of the molten metal 8 in the furnace near the slag removal port 3. Either the molten slag 10 is set at a position where the slag 10 can be collected near the center of the furnace, that is, position B shown in FIG. , reverse the direction of movement of the magnetic field.

尚、上記各工程で行われる誘導子7aのセット替は、パ
ターンによるプリセット、又は遠隔操作(ワンタンチ)
により行うことができ、またその位置及び動作は監視テ
レビで確認することが可能である。
The setting of the inductor 7a performed in each of the above steps can be changed by presetting by pattern or by remote control (one-touch).
The location and operation can be confirmed on surveillance television.

次に5、上記各工程における炉内溶湯8及び溶滓lOの
状況を第3図に基づいて説明する。
Next, 5, the state of the molten metal 8 and molten slag lO in the furnace in each of the above steps will be explained based on FIG.

[1] 炉内残塊9の溶解促進工程 一般に、非鉄金属の溶解の場合、例えばA1及びA1合
金の溶解を一例にとると、/lの黒度は0.2 程度で
あって鉄(0,8程度)に比べると低く、火陥などの輻
射エネルギーを吸収し難い。更に、溶湯8と残塊9の混
在する溶解後半時においては、炉内残塊9の表面は高温
に熱せられて酸化が促進されるので、その溶解は一層困
難な状況にある。本実施例における溶解促進工程では、
第3図り、に示したように、残塊9の周囲の溶湯8が炉
壁1に沿って旋回移動または衝突移動させられるので、
上記溶湯8の侵食作用によって残塊9の外周部は削り落
とされ、これにより残塊9表面の酸化は阻止される。ま
た、上記炉内溶湯8の旋回又は衝突移動によって、溶湯
8表面には造波現象が生じ、かかる造波現象は、溶湯表
面温度を溶湯8が静止状態にある場合に比し低下(一般
的に静止状態では800℃以上に対し本実施例では76
5℃以下)させると共に、平均伝熱面積を静止状態に比
べ大きくすることができる。この表面温度の低下と伝熱
面積の増大は、 Q=U−A・ΔT−H という熱伝達の一般式で表される。ここで、Q:金属の
受伝熱量(Kcal) 、U :平均熱伝熱係数(Kc
al/ rd ・h −”C) 、A :被加熱物の平
均伝熱面積(耐)、ΔT:雰囲気と被加熱物との平均温
度差(’C)、H:溶解時間(h)である。上記の熱伝
達の一般式において、本実施例ではA及びΔTが大きく
なるので、金属溶解の被加熱物への熱伝達量は増大する
ことになる。以上の溶湯8による侵食作用及び溶湯表面
の造波現象によって、炉内残塊9の溶解は、溶湯が静止
状態にある場合に比べ著しく促進させることになる。
[1] Process of promoting melting of the remaining ingot 9 , 8), and it is difficult to absorb radiant energy such as fire damage. Furthermore, in the latter half of the melting period when the molten metal 8 and the residual mass 9 coexist, the surface of the residual mass 9 in the furnace is heated to a high temperature and oxidation is promoted, making the melting even more difficult. In the dissolution promotion step in this example,
As shown in the third diagram, the molten metal 8 around the remaining lump 9 is moved in a swirling manner or collides with the furnace wall 1, so that
The outer periphery of the remaining lump 9 is scraped off by the erosive action of the molten metal 8, thereby preventing the surface of the remaining lump 9 from being oxidized. Further, due to the swirling or collision movement of the molten metal 8 in the furnace, a wave-forming phenomenon occurs on the surface of the molten metal 8, and this wave-forming phenomenon lowers the surface temperature of the molten metal compared to when the molten metal 8 is in a stationary state (general In this example, the temperature is 76°C, whereas in a static state it is 800°C or higher.
5° C. or lower), and the average heat transfer area can be made larger than in a static state. This decrease in surface temperature and increase in heat transfer area is expressed by the general formula for heat transfer: Q=U−A·ΔT−H. Here, Q: amount of heat transferred by metal (Kcal), U: average heat transfer coefficient (Kc
al/rd・h−”C), A: Average heat transfer area (resistance) of the object to be heated, ΔT: Average temperature difference between the atmosphere and the object to be heated ('C), H: Melting time (h) In the above general formula for heat transfer, in this example, A and ΔT become large, so the amount of heat transferred to the object to be heated during metal melting increases.Erosion effect by the molten metal 8 and the molten metal surface Due to the wave-forming phenomenon, the melting of the lump 9 remaining in the furnace is significantly accelerated compared to when the molten metal is in a stationary state.

[2] 溶湯による炉内残塊9の浸漬溶解工程この工程
では、第2図に示す誘導子7aの位置A−B又はCに各
々対応して、炉内溶湯8は第3図に示すA、・B+又は
C8の状態に流動して、炉内中央付近に浮遊する残塊9
に衝突する。これによって残塊9の崩壊(所謂山くずし
)は完全になされて溶湯による浸漬溶解が可能となる。
[2] Immersion melting process of the in-furnace residual lump 9 with molten metal In this step, the in-furnace molten metal 8 is immersed in the position A-B or C shown in FIG. 3, respectively, of the inductor 7a shown in FIG. , - Residue mass 9 floating near the center of the furnace, flowing to a B+ or C8 state
collide with As a result, the remaining lump 9 is completely collapsed (so-called crumbling), and it becomes possible to melt it by immersion in the molten metal.

[3] 自動精錬工程 この工程では、第3図のC2に示すような炉内溶湯8の
積極的な可変移動がなされるので、従来例のように溶湯
が微動又は静止状態の下で精錬剤の投入が行われる場合
に比し、精錬剤を自動供給するだけで精錬剤の効果的な
撹拌がなされることになる。
[3] Automatic refining process In this process, the molten metal 8 in the furnace is actively moved in a variable manner as shown in C2 in FIG. Compared to the case where the refining agent is added, the refining agent can be effectively stirred simply by automatically supplying the refining agent.

[4] 除滓工程 本工程では、第2図で示した誘導子7aのB位置又はD
位置の設定により、それに対応して炉内溶湯8は第3図
のB、又はり、の状態の流動をなし、溶滓10は自動的
に除滓口3の周辺又は炉中各辺りの除滓最適位置に1箇
所に集められる。
[4] In this step of the slag removal process, the inductor 7a shown in FIG.
Depending on the position setting, the molten metal 8 in the furnace will flow in the state shown in FIG. The slag is collected in one place at the optimum position.

〔発明の効果〕〔Effect of the invention〕

本発明の炉内溶湯撹拌装置は、以上のように原料溶解後
半時における各工程に応じて炉床下の最も適切な位置に
誘導子を設置し、効果的な溶湯の流動状態が得られるよ
うに構成されているので、下記の諸効果を顕著に奏する
ものである。
As described above, the in-furnace molten metal stirring device of the present invention installs the inductor at the most appropriate position under the hearth according to each process in the latter half of raw material melting, so as to obtain an effective flow state of the molten metal. Because of this structure, the following effects can be achieved significantly.

[1] 金属溶解後半時点での積極的な溶湯可変移動に
よる残塊浸漬及び低温溶解の促進によって、省エネルギ
ー化(従来例に比し3%以上の低減)及び酸化抑制に伴
うメタルロスの低減(従来例に比し10%以上の低減)
が可能となった。
[1] By actively variable movement of the molten metal during the latter half of metal melting to promote immersion of residual lumps and low-temperature melting, energy savings (3% or more reduction compared to conventional methods) and reduction of metal loss due to oxidation suppression (conventional (10% or more reduction compared to the example)
became possible.

[2] 精錬時の積極的な溶湯移動による自動精錬の容
易化によって、精錬時間の短縮化、省力化、及び生産性
の向上が可能となった。60T/CHのAl溶解炉にお
いて、従来2本/炉のランスで20分/CH要していた
のが、無人操作(プリセット無人又は遠隔操作)にて1
0分/CH以内で完全精錬することができた。また精錬
剤撹拌の効率化により、精錬剤の使用量も従来の173
に節約することができた。
[2] Facilitation of automatic refining through active movement of molten metal during refining has made it possible to shorten refining time, save labor, and improve productivity. In a 60T/CH Al melting furnace, the conventional 2 lances/furnace lance required 20 minutes/CH, but with unmanned operation (preset unmanned or remote control)
Complete refining was possible within 0 minutes/CH. In addition, by improving the efficiency of stirring the refining agent, the amount of refining agent used has been reduced to 173% compared to the conventional one.
was able to save on.

[3] 除滓時における炉内溶滓の積極的な可変移動に
よる溶滓の一ケ所集中化によって、除滓時間の短縮化、
省力化、生産性の向上が可能となった。前記60T/C
HのAl溶解炉又は保持炉において、従来は3箇所/炉
の除滓L1から3人で40分/ CH要していたが、本
発明では1箇所/炉の閉口部から1人だけで20分lC
H以内で除滓することが可能となった。
[3] By concentrating the slag in one place through active variable movement of the slag in the furnace during slag removal, the slag removal time can be shortened.
It has become possible to save labor and improve productivity. Said 60T/C
In the H Al melting furnace or holding furnace, conventionally it took 40 minutes/CH by 3 people from 3 places/from the slag removal L1 of the furnace, but in the present invention it took 20 minutes/CH from 1 place/from the closing part of the furnace. min lC
It became possible to remove slag within H.

[4] 上記60T/CHのAl溶解炉において溶湯の
均熱均質化を5分以内で実現することが可能となった。
[4] In the above 60T/CH Al melting furnace, it became possible to achieve homogenization of the molten metal within 5 minutes.

【図面の簡単な説明】 第1図は本発明の一実施例を示す要部概略した構成図、
第2図は誘導子の設定位置を示す説明図、第3図は第2
図に対応する炉内溶湯の流動状況を示す説明図である。 1は炉壁、2は炉床、7は電磁溶湯撹拌装置、7aは誘
導子(移動磁界発生装置)である。
[BRIEF DESCRIPTION OF THE DRAWINGS] FIG. 1 is a schematic configuration diagram of main parts showing an embodiment of the present invention;
Figure 2 is an explanatory diagram showing the setting position of the inductor, and Figure 3 is an explanatory diagram showing the setting position of the inductor.
It is an explanatory view showing the flow situation of the molten metal in the furnace corresponding to the figure. 1 is a furnace wall, 2 is a hearth, 7 is an electromagnetic molten metal stirring device, and 7a is an inductor (moving magnetic field generator).

Claims (1)

【特許請求の範囲】[Claims] 1、炉床下に設置される電磁溶湯撹拌装置であって、上
記電磁溶湯撹拌装置に設けられている誘導子が、磁界移
動方向の転換が自在で溶湯移動能力を有し、かつ水平移
動と回動と昇降移動とがそれぞれ自在となるように設け
たことを特徴とする炉内溶湯撹拌装置。
1. An electromagnetic molten metal stirring device installed under the hearth, in which the inductor installed in the electromagnetic molten metal stirring device has the ability to freely change the direction of magnetic field movement and move the molten metal, and is capable of horizontal movement and rotation. An in-furnace molten metal stirring device characterized in that it is provided so that it can freely move and move up and down.
JP21410685A 1985-09-27 1985-09-27 Melted material agitator in furnace Granted JPS6273591A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21410685A JPS6273591A (en) 1985-09-27 1985-09-27 Melted material agitator in furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21410685A JPS6273591A (en) 1985-09-27 1985-09-27 Melted material agitator in furnace

Publications (2)

Publication Number Publication Date
JPS6273591A true JPS6273591A (en) 1987-04-04
JPH0570915B2 JPH0570915B2 (en) 1993-10-06

Family

ID=16650330

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21410685A Granted JPS6273591A (en) 1985-09-27 1985-09-27 Melted material agitator in furnace

Country Status (1)

Country Link
JP (1) JPS6273591A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991009508A1 (en) * 1989-12-14 1991-06-27 Mitsubishi Denki Kabushiki Kaisha Cooker
JP2016022528A (en) * 2014-07-24 2016-02-08 大亜真空株式会社 Metal melting method
US20190390908A1 (en) * 2017-02-10 2019-12-26 Abb Schweiz Ag Furnace Assembly For A Metal-Making Process
IT201900016790A1 (en) * 2019-09-19 2021-03-19 Danieli Off Mecc METHOD OF STIRRING LIQUID METAL IN AN ELECTRIC ARC OVEN

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991009508A1 (en) * 1989-12-14 1991-06-27 Mitsubishi Denki Kabushiki Kaisha Cooker
EP0458977A1 (en) * 1989-12-14 1991-12-04 Mitsubishi Denki Kabushiki Kaisha Cooker
JP2016022528A (en) * 2014-07-24 2016-02-08 大亜真空株式会社 Metal melting method
US20190390908A1 (en) * 2017-02-10 2019-12-26 Abb Schweiz Ag Furnace Assembly For A Metal-Making Process
JP2020505579A (en) * 2017-02-10 2020-02-20 アーベーベー・シュバイツ・アーゲー Furnace assembly for metal manufacturing process
US10921060B2 (en) * 2017-02-10 2021-02-16 Abb Schweiz Ag Furnace assembly for a metal-making process
US11543182B2 (en) 2017-02-10 2023-01-03 Abb Schweiz Ag Furnace assembly for a metal-making process
IT201900016790A1 (en) * 2019-09-19 2021-03-19 Danieli Off Mecc METHOD OF STIRRING LIQUID METAL IN AN ELECTRIC ARC OVEN
WO2021053701A1 (en) * 2019-09-19 2021-03-25 Danieli & C. Officine Meccaniche S.P.A. Method of stirring liquid metal in an electric arc furnace
CN114729781A (en) * 2019-09-19 2022-07-08 达涅利机械设备股份公司 Method for stirring liquid metal in electric arc furnace

Also Published As

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