JPS5989704A - Electromagnetic desulfurizer - Google Patents

Electromagnetic desulfurizer

Info

Publication number
JPS5989704A
JPS5989704A JP19865982A JP19865982A JPS5989704A JP S5989704 A JPS5989704 A JP S5989704A JP 19865982 A JP19865982 A JP 19865982A JP 19865982 A JP19865982 A JP 19865982A JP S5989704 A JPS5989704 A JP S5989704A
Authority
JP
Japan
Prior art keywords
molten metal
vessel
induction coil
container
coil
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
JP19865982A
Other languages
Japanese (ja)
Other versions
JPH0353363B2 (en
Inventor
Shigeyuki Shigihara
鴫原 重之
Masahiro Tadokoro
昌宏 田所
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.)
Shinko Electric Co Ltd
Original Assignee
Shinko Electric Co 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 Shinko Electric Co Ltd filed Critical Shinko Electric Co Ltd
Priority to JP19865982A priority Critical patent/JPS5989704A/en
Publication of JPS5989704A publication Critical patent/JPS5989704A/en
Publication of JPH0353363B2 publication Critical patent/JPH0353363B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C1/00Refining of pig-iron; Cast iron
    • C21C1/02Dephosphorising or desulfurising

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
  • Crucibles And Fluidized-Bed Furnaces (AREA)
  • Furnace Details (AREA)

Abstract

PURPOSE:To provide a titled device which stirs and heats a molten metal and desulfurizes effectively said metal by providing a vessel for molten metal consisting of a refractory material in a cylindrical induction coil, and communicating the lower part of the vessel and a charging port positioned at the same level as the upper part of the vessel. CONSTITUTION:An induction coil 1 formed by winding a water cooling pipe into a cylindrical shape is supported together with an iron core 5 by annular supports 2, 3, and a vessel 4a for molten metal consisting of a refractory material is provided in the coil 1. A communication pipe 4b of a refractory material which communicates the bottom of said vessel and a charging port 4c positioned at the same level as the vessel 4a is provided, whereby a furnace body 4 is constituted. The molten metal R supplied, via an inflow spout 6 for the molten metal, from a cupola, (not shown in figure), is added with a desulfurizing agent from an addition pipe 7 for the desulfurizing agent in the vessel 4a; at the same time, stirring flow is induced therein in an arrow direction by the coil 1 and the molten metal is heated, whereby the molten metal is effectively desulfurized. The desulfurized metal overflows from the port 4c into a casting mold (not shown in figure) according to the supply rate of the molten metal from the cupola.

Description

【発明の詳細な説明】 この発明は、被脱硫溶湯の温度低下を防止しつつ効果的
に脱硫作用を得る電磁脱硫装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an electromagnetic desulfurization device that effectively obtains a desulfurization effect while preventing a drop in the temperature of a molten metal to be desulfurized.

鋳鉄工場において溶湯を得る手段としてキューポラが広
く採用されている。一方、高品質の鋳鉄を得るために、
鋳型への注湯に先だって溶湯中に球状化剤を添加し、球
状黒鉛鋳鉄を得ることが考えられている。
Cupolas are widely used in iron foundries as a means of obtaining molten metal. Meanwhile, in order to obtain high quality cast iron,
It has been considered to add a spheroidizing agent to the molten metal before pouring it into a mold to obtain spheroidal graphite cast iron.

そして、この球状黒鉛鋳鉄はますますその生産量が増加
しているが、上記キューポラを使って生成した溶湯は燃
料としてのコークスに由来する硫黄を高濃度に含有する
ため、球状化剤の添加による黒鉛球状化の進行が不充分
で実用に供し得ない。
The production volume of this spheroidal graphite cast iron is increasing, but since the molten metal produced using the cupola contains a high concentration of sulfur derived from coke as a fuel, it is necessary to add a spheroidizing agent. The progress of graphite spheroidization is insufficient and it cannot be put to practical use.

このため、キューポラによって生成する溶湯を用いる球
状黒鉛鋳鉄の製造においては球状他剤添加前に脱硫工程
を設けるのが一般的である。この脱硫は、脱硫剤を溶湯
中に添加し、反応促進のため攪拌を行う必要があり、従
来技術においてはいくつかの方法がある。その1はポー
ラスプラグ法と称され、容器の底部に設けたポーラスプ
ラグを通して溶湯との反応をみないN2ガスを溶湯容器
底より吹上げ、N2ガス気泡の上昇力により容器内の溶
湯を攪拌する方法であり、その2はガスインジェクショ
ン法と称され、耐火性管を溶湯内に浸漬して、この管を
通じてキャリヤーガスとしてN2ガスを粉末カーバイト
と共に吹き込み、攪拌と反応を得る方法である。
For this reason, in the production of spheroidal graphite cast iron using molten metal produced in a cupola, it is common to provide a desulfurization step before adding the spheroidal additive. This desulfurization requires adding a desulfurizing agent to the molten metal and stirring to promote the reaction, and there are several methods available in the prior art. The first method is called the porous plug method, in which N2 gas that does not react with the molten metal is blown up from the bottom of the molten metal container through a porous plug installed at the bottom of the container, and the molten metal in the container is stirred by the upward force of the N2 gas bubbles. The second method is called the gas injection method, in which a refractory tube is immersed in the molten metal, and N2 gas is injected as a carrier gas together with powdered carbide through the tube to obtain stirring and reaction.

ところで、これらの2つの方法を実際の脱硫工弊背とし
て問題視される。今ポーラスプラグ法における代表的な
例を示すと、次の通りである。すなわち、[キューボラ
出湯時り550℃→ポーラスプラグ式脱硫装置内の温度
1450 ’C→脱硫剤添加後の” 出湯時1400 
’c→鋳造」となっている。
By the way, these two methods are considered problematic as they are the backbone of the actual desulfurization process. Typical examples of the porous plug method are as follows. In other words, [550°C at the time of tapping the Cubola → Temperature inside the porous plug desulfurization equipment 1450'C → 1400°C at the time of tapping after adding the desulfurizing agent.
'c→casting'.

しかるに、鋳造による製品が、小物ないし薄状物などで
は鋳造時の温度は1400℃〜1430 ′Cを要し、
脱硫剤添加後の鋳型までの運搬、複数個の鋳型への順次
の鋳造時間中d温度低下を考慮すると、上記の温度状況
では実用に耐えないことが判る。
However, if the product is a small or thin product, the casting temperature will be 1400°C to 1430'C.
Considering the temperature drop during transport to the mold after addition of the desulfurizing agent and during sequential casting into a plurality of molds, it can be seen that the above temperature conditions are not practical.

この問題が基でキューボラを容解設備とする(通常経費
の点から殆んどこのキューボラが用いられる)球状黒鉛
鋳鉄の生産に際して脱硫処理後の溶湯の昇温手段を備え
ることが普通である。この手段として一般的に溝型誘導
炉が用いられる傾向にあるが、比較的少規模の生産工場
ではその経費比率が大となり導入が困難である。
Because of this problem, when producing spheroidal graphite cast iron using a cubera as melting equipment (which is usually used in most cases from the point of view of cost), it is common to provide means for raising the temperature of the molten metal after desulfurization treatment. As a means for this purpose, there is a general tendency to use a channel induction furnace, but it is difficult to introduce it in relatively small-scale production plants because of its large expense ratio.

この発明の目的は脱硫剤の均一分布をはかるための攪拌
力と昇温能力を合せ持つ電磁的手段を備えた電磁脱硫装
置を提供することにある。
An object of the present invention is to provide an electromagnetic desulfurization apparatus equipped with electromagnetic means that has both stirring power and temperature raising ability for uniformly distributing the desulfurization agent.

以下、図示する実施例について具体的に説明する。第1
図はこの発明に係る脱硫装置の断面図、第2図は溶湯及
び脱硫剤の添加手段を除いた平面図である。各図におい
て、1は誘導コイルで、水冷パイプを円筒状に巻回して
形成され、その上下に配置される円還状の支持体2.3
にはさまれ、図示しないボルトで支持さnているものと
する。
The illustrated embodiment will be specifically described below. 1st
The figure is a sectional view of the desulfurization apparatus according to the present invention, and FIG. 2 is a plan view excluding the means for adding molten metal and desulfurization agent. In each figure, reference numeral 1 denotes an induction coil, which is formed by winding a water-cooled pipe into a cylindrical shape, and circular supports 2 and 3 arranged above and below the induction coil.
It is assumed that it is supported by bolts (not shown).

4は炉体で、炉材をかためて形成しており、コイルで囲
まれる領域において溶湯容器4aを形成し、この容器4
aと誘導コイル1とでいわゆるるつぼ形誘導炉を構成し
ている。4bは連通管で、例えば処理溶湯と同一種類の
素材からなるパイプにて形成しておき、溶湯での溶解を
基に形成される。そして、この連通管4bは上記容器4
aの底面部より注湯口4cに連らなる。ところで、この
注湯口4eの出湯レベルは溶湯容器4a中に供給される
溶湯レベルが誘導コイル1の上方端になったときに適合
させるものとする。5は鉄心で、垂直方向を向けて誘導
コイル1の周囲に適当間隔に配置される。6は溶湯流入
樋で、図示しなしAキューボラより生成の溶湯を上記脱
硫装置の溶湯容器4aに供給する。7は脱硫剤添加管で
、溶湯容器4aに単位時間に供給される溶湯Rの量シこ
応じて適当量の脱硫剤を溶湯容器中に切出す。
Reference numeral 4 denotes a furnace body, which is formed by hardening the furnace material, and forms a molten metal container 4a in the area surrounded by the coil.
a and the induction coil 1 constitute a so-called crucible-shaped induction furnace. Reference numeral 4b denotes a communicating pipe, which is formed, for example, from a pipe made of the same type of material as the molten metal to be treated, and is formed based on melting with the molten metal. This communication pipe 4b is connected to the container 4.
The bottom part of a is connected to the pouring spout 4c. Incidentally, the level of the melt coming out of the pouring port 4e is adjusted when the level of the molten metal supplied into the molten metal container 4a reaches the upper end of the induction coil 1. Reference numeral 5 denotes iron cores, which are arranged at appropriate intervals around the induction coil 1, facing vertically. A molten metal inlet trough 6 supplies the molten metal produced from a not-shown A cubera to the molten metal container 4a of the desulfurization apparatus. Reference numeral 7 denotes a desulfurizing agent addition pipe, which cuts out an appropriate amount of desulfurizing agent into the molten metal container according to the amount of molten metal R supplied to the molten metal container 4a per unit time.

上記構成において、まずキューボラ(図示せず)より得
られる鋳鉄溶湯Rが溶湯流入樋6を通じて炉体4中に形
成されている溶湯容器4aへの注入過程で徐々に溶湯レ
ベルが上昇してし1く。そしてこの容器4a内の溶湯レ
ベルの上昇と同時;こ連溶湯レベルの上昇は停止し、溶
湯流入樋から流入した等量の溶湯が注湯口4Cより図示
しなし1鋳型などに供給されていく。
In the above configuration, first, the molten metal R obtained from the cubera (not shown) is poured into the molten metal container 4a formed in the furnace body 4 through the molten metal inlet trough 6, and the molten metal level gradually rises. Ku. Simultaneously with the rise in the molten metal level in the container 4a, the continuous rise in the molten metal level stops, and an equal amount of molten metal flowing from the molten metal inflow gutter is supplied to a mold (not shown) from the pouring port 4C.

一方、上記溶湯流入樋6から溶湯容器4a+ご流入され
る溶湯は容器4a内1こおし)て脱硫剤添力l管7より
脱硫剤の添加を受は脱硫作用を交番する。
On the other hand, the molten metal flowing into the molten metal container 4a from the molten metal inlet trough 6 is poured into the container 4a, and a desulfurizing agent is added from the desulfurizing agent addition pipe 7, thereby alternating the desulfurization action.

この際の動作をより具体約1こ説明すると、まず、誘導
フィル1に単相交流電圧を111 jJDすること番こ
よって当該誘導コイル1の各部垂直方向の断面を囲むよ
うに交番磁束が発生し、この磁束が容器4a内に蓄積さ
nる溶湯R中を貫通し、この溶湯中を通過する磁束によ
り渦電流が発生する。この渦電流は容器内においての温
度低下を補償するのみならず昇温作用を担う。この昇温
作用と同時に上記溶湯容器4A中を通過する磁束によっ
て溶湯中には誘導コイル1中を流れる電流とは反対方向
の電流が束状に流れる。これらの束状の電流は同方向で
あるため、溶湯Rに反発力が生じ、ひいては溶湯Rは周
縁より中心部に移行する作用が生じ、誘導コイルlへの
供給電圧の位相反転時において電流の流れの方向が反転
することに絞られる作用を伴って添加された脱硫剤の均
一の分布を促し脱硫作用を促進する。このようにして脱
硫作用を終えた溶湯は連続的に注湯口4Cより流出する
。上記誘導コイル1をとり巻く磁束は外部におし)では
鉄心5に集中し、図示しないt枠(鉄製)の誘導加熱を
防止するが、外枠の材質ないしその配置を考慮すれば必
ずしも設けることを要しない。
To explain the operation in more detail, first, a single-phase AC voltage of 111 jJD is applied to the induction coil 1. As a result, an alternating magnetic flux is generated surrounding the vertical cross section of each part of the induction coil 1. This magnetic flux passes through the molten metal R accumulated in the container 4a, and an eddy current is generated by the magnetic flux passing through the molten metal. This eddy current not only compensates for the temperature drop within the container, but also serves to raise the temperature. Simultaneously with this temperature raising action, a current flows in the molten metal in a bundle in the opposite direction to the current flowing through the induction coil 1 due to the magnetic flux passing through the molten metal container 4A. Since these bundled currents are in the same direction, a repulsive force is generated in the molten metal R, which causes the molten metal R to move from the periphery to the center, and when the phase of the voltage supplied to the induction coil l is reversed, the current The reversal of the flow direction has a constricting effect, which promotes uniform distribution of the added desulfurizing agent and promotes the desulfurizing action. The molten metal that has completed the desulfurization action in this manner continuously flows out from the pouring port 4C. When the magnetic flux surrounding the induction coil 1 is placed outside), it concentrates on the iron core 5 and prevents induction heating of the T-frame (made of iron), not shown. does not require

上記本発明装置における溶湯の湿度変化は次のような状
態とすることができる。すなわち、「キューボラ出湯時
り550℃−説硫装置内の温度1500’c→脱硫後の
出湯時湛度1450 ’(: →鋳造」である。
The humidity of the molten metal in the apparatus of the present invention may change as follows. That is, "550° C. at the time of tapping the Cubola - Temperature in the sulfurizing device 1500'c -> Fullness at the time of tapping after desulfurization 1450' (: → Casting").

つまり前記の湿度状態に比して通常、脱硫装置内の温度
を実質的に50°上昇させていることがわかる0 また、本発明に係る電磁脱硫装置の具体的概念をより明
確にするために、代表的な例で諸元を示すと キューボラ・・・・・・2on/Hr出湯時il&M 
度1550−C本脱硫装置・・・・・・溶湯量 400
kqコイル電力・・・・・・・・・100 KW溶湯滞
留時間 400/2000 X 60 = 12分間昇
湿温力・・・・・・・・・約50′Cとなる。
In other words, it can be seen that the temperature inside the desulfurization apparatus is normally substantially increased by 50° compared to the above-mentioned humidity condition.In addition, in order to clarify the specific concept of the electromagnetic desulfurization apparatus according to the present invention, To show the specifications using a typical example, Cubola... 2 on/Hr when hot water is tapped & M
degree 1550-C main desulfurization equipment...molten metal amount 400
kq coil power: 100 KW Molten metal residence time: 400/2000 x 60 = 12 minutes Humidity heating power: approximately 50'C.

なお、上記説明においては脱硫装置内の溶湯レベルが上
昇するまでに既に連通管に入っている溶湯湯量に比して
ごく僅かであるので殆んど影響なく必要に応じて最初注
湯口4Cから出湯する溶湯を排棄してもよい。また、加
熱、攪拌作用を担う容器4aよりの連通管4bの接続位
置は容器4aの底部としているが、炉体4の形態上、容
器4aの下方部側方としてもよい。但し、このときは誘
導コイル1の下方部の一部を下方にたわましてコイル1
の側方より連通管を連らねる必要も生じ得る。一方、連
通管の一部又は全部を誘導コイル1内に配置してもよい
。さらに誘導フィル1は円筒形に限らず筒状であればよ
い。
In addition, in the above explanation, by the time the molten metal level in the desulfurization equipment rises, the amount of molten metal already in the communication pipe is very small compared to the amount of molten metal that has already entered the communication pipe. The molten metal may be discarded. Further, although the connection position of the communication pipe 4b from the container 4a, which performs heating and stirring functions, is at the bottom of the container 4a, it may be connected to the lower side of the container 4a due to the shape of the furnace body 4. However, in this case, a part of the lower part of the induction coil 1 is bent downward, and the coil 1
It may also be necessary to connect communication pipes from the sides. On the other hand, part or all of the communication tube may be placed inside the induction coil 1. Further, the guide filter 1 is not limited to a cylindrical shape, and may be any shape as long as it is cylindrical.

以上述べたように、この発明に係る電磁脱硫装置は筒形
誘導フィルとその内部に構成される耐火材で形成さnる
溶湯容器を備え、この容器の下方部より外部注湯口へ連
通する耐火性連通管を有し、上記外部注湯口は容器上部
と同一レベル関係にあ)す、上記溶湯容器より連続的流
れとして鋳鉄溶湯と脱硫剤を同時に受け、上記連通路よ
りオーバーフローする脱硫処理された溶湯を得るように
構成したものである。このような構成に基づいて、電磁
誘導による攪拌力と昇温力の両方を脱硫作用に効果的に
結びつけることができ、とりわけ脱硫装置での温度低下
に伴う弊害を別途昇温装置を設けることなく除去できる
実利は大である。また、脱硫装置に取入れられた溶湯量
は連通管の穴寸法の大小に関係なく、同量の出湯が得ら
れ、出湯量のフントロールはキューボラの出湯量の制御
でなされる。さらに受湯と出湯との落差が小さいので、
既設の工場プロセス中にm単に導入することができる。
As described above, the electromagnetic desulfurization apparatus according to the present invention includes a cylindrical induction filter and a molten metal container formed of a refractory material inside the cylindrical induction filter, and a fireproof molten metal container that communicates with an external pouring port from the lower part of the container. The external pouring port is located at the same level as the upper part of the container, and the molten cast iron and desulfurization agent are simultaneously received as a continuous flow from the molten metal container, and the desulfurized metal overflows from the communication path. It is configured to obtain molten metal. Based on this configuration, it is possible to effectively combine both the stirring power and the temperature raising power generated by electromagnetic induction with the desulfurization effect, and in particular, it is possible to eliminate the adverse effects associated with the temperature drop in the desulfurization equipment without installing a separate temperature raising device. The practical benefit of removing it is huge. Furthermore, the same amount of molten metal introduced into the desulfurization device is obtained regardless of the size of the hole in the communication pipe, and the amount of molten metal discharged is controlled by controlling the amount of molten metal discharged from the cubera. Furthermore, since the difference in head between the receiving hot water and the hot water coming out is small,
It can be simply introduced into existing factory processes.

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

第1図は断面図、第2図は一部を省略した平面図である
。 1・・・・・・・・・誘導フィル  4・・・・・・・
・・炉体4EL・・・・・・溶湯容器   4b・・・
・・・連通管4c・・・・・・注湯口    6・・・
・・・・・・溶湯流入樋7 ・・・・・・脱硫剤添加管 出願人 神鋼電機株式会社 代理人 弁理士 斎藤春弥
FIG. 1 is a sectional view, and FIG. 2 is a partially omitted plan view. 1...Induction fill 4...
... Furnace body 4EL ... Molten metal container 4b ...
...Communication pipe 4c...Pouring port 6...
...Molten metal inflow gutter 7 ...Desulfurizing agent addition pipe Applicant Shinko Electric Co., Ltd. Agent Patent attorney Haruya Saito

Claims (1)

【特許請求の範囲】[Claims] 1、筒形誘導コイルで囲まれ6る空間に耐火拐にて溶湯
容器を形成し、上記溶湯容器のほぼ誘導コイルの上端部
に対応するレベルの誘導コイルの外部における適所に注
湯口と、上記溶湯容器の下方部より上記注湯口に連らな
る連通管とを設け、上記溶湯容器への被脱硫溶湯及び脱
流剤の各供給手段を備えたことを特徴とする電磁脱硫装
置。
1. A molten metal container is formed using fireproof insulation in a space surrounded by a cylindrical induction coil, and a molten metal pouring port is provided at an appropriate location outside the induction coil at a level corresponding to the upper end of the induction coil in the molten metal container, and An electromagnetic desulfurization apparatus characterized in that a communication pipe connected from a lower part of the molten metal container to the pouring port is provided, and means for supplying molten metal to be desulfurized and a deflow agent to the molten metal container are provided.
JP19865982A 1982-11-11 1982-11-11 Electromagnetic desulfurizer Granted JPS5989704A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19865982A JPS5989704A (en) 1982-11-11 1982-11-11 Electromagnetic desulfurizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19865982A JPS5989704A (en) 1982-11-11 1982-11-11 Electromagnetic desulfurizer

Publications (2)

Publication Number Publication Date
JPS5989704A true JPS5989704A (en) 1984-05-24
JPH0353363B2 JPH0353363B2 (en) 1991-08-14

Family

ID=16394902

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19865982A Granted JPS5989704A (en) 1982-11-11 1982-11-11 Electromagnetic desulfurizer

Country Status (1)

Country Link
JP (1) JPS5989704A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2648538C2 (en) * 2013-12-06 2018-03-26 Дзе Йокогама Раббер Ко., Лтд. Pneumatic tire

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2648538C2 (en) * 2013-12-06 2018-03-26 Дзе Йокогама Раббер Ко., Лтд. Pneumatic tire
US10766317B2 (en) 2013-12-06 2020-09-08 The Yokohama Rubber Co., Ltd. Pneumatic tire

Also Published As

Publication number Publication date
JPH0353363B2 (en) 1991-08-14

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