Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0353363B2 - - Google Patents
[go: Go Back, main page]

JPH0353363B2 - - Google Patents

Info

Publication number
JPH0353363B2
JPH0353363B2 JP19865982A JP19865982A JPH0353363B2 JP H0353363 B2 JPH0353363 B2 JP H0353363B2 JP 19865982 A JP19865982 A JP 19865982A JP 19865982 A JP19865982 A JP 19865982A JP H0353363 B2 JPH0353363 B2 JP H0353363B2
Authority
JP
Japan
Prior art keywords
molten metal
container
induction coil
desulfurization
temperature
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.)
Expired
Application number
JP19865982A
Other languages
Japanese (ja)
Other versions
JPS5989704A (en
Inventor
Shigeyuki Shigihara
Masahiro Tadokoro
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)

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として、
または溶湯と添加物とを電磁的に撹拌することに
より溶湯の成分調整を行なう装置として用いて好
適な電磁誘導撹拌装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides an electromagnetic desulfurization device that effectively obtains a desulfurization effect while preventing a drop in the temperature of the molten metal to be desulfurized.
The present invention also relates to an electromagnetic induction stirring device suitable for use as a device for adjusting the composition of a molten metal by electromagnetically stirring the molten metal and additives.

例えば鋳鉄工場において溶湯を得る手段として
キユ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つて溶
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。
For example, cupolas are widely used in iron casting factories as a means of obtaining molten metal. On the other hand, 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、上記キユーポラを使つて生
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。このため、キユーポラによつて生成する溶湯
を用いる球状黒鉛鋳鉄の製造においては球状化剤
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
ため撹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
器内の溶湯を撹拌する方法であり、その2はガス
インジエクシヨン法と称され、耐火性管を溶湯内
に浸漬して、この管を通じてキヤリヤーガスとし
てN2ガスを粉末カーバイトと共に吹き込み、撹
拌と反応を得る方法である。
Although the production volume of this spheroidal graphite cast iron is increasing more and more, the molten metal produced using the above-mentioned Cupora contains a high concentration of sulfur derived from coke as a fuel, so the addition of a spheroidizing agent The progress of graphite spheroidization is insufficient and it cannot be put to practical use. For this reason, in the production of spheroidal graphite cast iron using molten metal produced by cupola, it is common to provide a desulfurization step before adding the spheroidizing agent. 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. 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 along with powdered carbide through the tube to obtain stirring and reaction. It is.

ところで、これらの2つの方法を実際の脱硫工
程に導入するとき、温度低下ということが重要な
弊害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、「キユーポラ出湯時1550℃→ポーラスプ
ラグ式脱硫装置内の温度1450℃→脱硫剤添加後の
出湯時1400℃→鋳造」となつている。
By the way, when these two methods are introduced into an actual desulfurization process, temperature reduction is seen as an important problem. Typical examples of the porous plug method are as follows. In other words, "1550°C when tapping the cupola → Temperature inside the porous plug desulfurization equipment 1450°C → 1400°C when tapping after adding the desulfurizing agent → 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℃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の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。この問題が基でキユーポラを容解設備とする
(通常経費の点から殆んどのキユーポラが用いら
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、比較的小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。
However, if the cast product is a small or thin item, the temperature during casting must be 1400°C to 1430°C, and the temperature during casting after adding a desulfurizing agent to the mold, and during the sequential casting time in multiple molds. Considering the temperature drop, it can be seen that the above temperature conditions are not practical. Because of this problem, when producing spheroidal graphite cast iron using a cupola as melting equipment (usually a cupola is 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 trench type induction furnace, but it is difficult to introduce it in relatively small-scale production plants because of its high expense ratio.

この発明の目的は溶湯に対し、脱硫剤ほかの添
加物の均一分布をはかるための撹拌力と昇温能力
を合せ持つ電磁的手段を備えた電磁誘導撹拌装置
を提供することにある。
An object of the present invention is to provide an electromagnetic induction stirring device equipped with electromagnetic means that has both stirring power and temperature raising ability for uniformly distributing additives such as a desulfurizing agent in molten metal.

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れているものとする。
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4a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4a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の上方端になつ
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、図示しないキユ
ーポ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の量に応じて
適当量の脱硫剤を溶湯容器中に切出す。
The illustrated embodiment will be specifically described below. FIG. 1 is a sectional view of a desulfurization device according to the present invention;
FIG. 2 is a plan view excluding the means for adding molten metal and desulfurizing agent. In each figure, 1 is an induction coil, which is formed by winding a water-cooled pipe into a cylindrical shape, and is sandwiched between circular supports 2 and 3 placed above and below the induction coil.
It is assumed that it is supported by bolts not shown.
Reference numeral 4 denotes a furnace body, which is formed by solidifying furnace materials, and forms a molten metal container 4a in an area surrounded by the coil, and this container 4a and the induction coil 1 constitute a so-called crucible-shaped induction furnace. 4b is a communicating pipe,
For example, it is formed 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. The communication pipe 4b is connected to the pouring spout 4c from the bottom of the container 4a. By the way, 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 molten metal produced from a cupola (not shown) 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、まずキユーポラ(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いく。そ
してこの容器4a内の溶湯レベルの上昇と同時に
連通管4b内の溶湯レベルも上昇し、注湯口4c
から溶湯が供給を開始する時点以後、容器4a内
の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より図示しない鋳
型などに供給されていく。
In the above configuration, first, the molten metal R obtained from a cupola (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 level of the molten metal gradually rises. At the same time as the molten metal level in the container 4a rises, the molten metal level in the communication pipe 4b also rises, and the molten metal level in the pouring port 4c rises.
After the point in time when molten metal starts to be supplied, the level of molten metal in the container 4a stops rising, and an equal amount of molten metal that has flowed from the molten metal inflow trough is supplied from the pouring port 4c to a mold (not shown) or the like.

一方、上記溶湯流入樋6から溶湯容器4aに流
入される溶湯は容器4a内において脱硫剤添加管
7より脱硫剤の添加を受け脱硫作用を受ける。こ
の際の動作をより具体的に説明すると、まず、誘
導コイル1に単相交流電圧を印加することによつ
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
に蓄積される溶湯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つて溶湯中には
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1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得
て図示の矢印方向の溶湯流が得られ、撹拌作用が
得られる。この容器4a内の溶湯Rの撹拌作用に
伴つ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いては鉄
心5に集中し、図示しない外枠(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。
On the other hand, the molten metal flowing into the molten metal container 4a from the molten metal inlet trough 6 receives a desulfurizing agent from the desulfurizing agent addition pipe 7 in the container 4a and undergoes a desulfurizing action. To explain the operation in more detail, first, by applying a single-phase AC voltage to the induction coil 1, an alternating magnetic flux is generated surrounding the vertical cross section of each part of the induction coil 1. The 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 on 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 1 is reversed, the current By reversing the flow direction, a constricting action is obtained, and a molten metal flow in the direction of the arrow shown in the figure is obtained, and a stirring action is obtained. As the molten metal R in the container 4a is stirred, the added desulfurizing agent is uniformly distributed and the desulfurizing action is promoted. The molten metal that has completed the desulfurization action in this manner continuously flows out from the pouring port 4c. The magnetic flux surrounding the induction coil 1 is concentrated on the iron core 5 externally to prevent induction heating of the outer frame (made of iron), not shown, but this is not necessarily required if the material of the outer frame and its arrangement are taken into consideration. .

上記本発明装置における溶湯の温度変化は次の
ような状態とすることができる。すなわち、「キ
ユーポラ出湯時1550℃→脱硫装置内の温度1500℃
→脱硫後の出湯時温度1450℃→鋳造」である。
The temperature change of the molten metal in the apparatus of the present invention can be as follows. In other words, the temperature inside the desulfurization equipment is 1500°C.
→ Temperature at tapping after desulfurization: 1450℃ → Casting.”

つまり前記の温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。
In other words, it can be seen that the temperature inside the desulfurization apparatus is normally increased by substantially 50° compared to the above temperature state.

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 キユーポラ……2on/Hr出湯時温度1550℃ 本脱硫装置……溶湯量 400Kg コイル電力……100KW 溶湯滞留時間400/2000×60=12分間 昇温能力……約50℃ となる。
In addition, in order to clarify the specific concept of the electromagnetic desulfurization equipment according to the present invention, the specifications are shown using a typical example: Kupora... 2 on/Hr Temperature during tapping 1550℃ This desulfurization equipment... Molten metal amount 400Kg Coil power...100KW Molten metal residence time 400/2000 x 60 = 12 minutes Temperature rising capacity...approximately 50℃.

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つている溶
湯は脱硫作用を受けていないか、この分は全体の
溶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、撹拌作用を担う
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。さらに誘導コイル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 molten metal that has already entered the communication pipe has not been subjected to the desulfurization action, or this amount is very small compared to the total amount of molten metal. The molten metal initially discharged from the pouring port 4c may be discarded as necessary with almost no effect. In addition, the connecting position of the communication pipe 4b from the container 4a which is responsible for heating and stirring is the container 4a.
However, due to the shape of the furnace body 4, the bottom of the container 4a
It may also be placed on the lower side of the . However, in this case, it may be necessary to bend a portion of the lower part of the induction coil 1 downward and connect a communication pipe from the side of the coil 1. On the other hand, a part or all of the communication pipe is connected to the induction coil 1
It may be placed inside. Furthermore, the induction coil 1 is not limited to a cylindrical shape, and may be any shape as long as it is cylindrical.

なお、上述した用途に限らず例えばアルミニウ
ム溶湯にチタン地金等の合金素材を添加して合金
溶湯を製造する装置等、溶湯の成分調整を行なう
装置として使用することも無論可能である。
Note that it is of course possible to use the present invention not only for the above-mentioned applications but also as a device for adjusting the composition of molten metal, such as a device for producing a molten alloy by adding an alloy material such as titanium metal to molten aluminum.

以上述べたように、この発明に係る電磁脱硫装
置は筒形誘導コイルとその内部に構成される耐火
材で形成される溶湯容器を備え、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
にあり、上記溶湯容器より連続的流れとして溶湯
と脱硫剤ほかの添加剤を同時に受け、上記連通路
よりオーバーフローする脱硫処理あるいは添加剤
を与えられた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
による撹拌力と昇温力の両方を脱硫作用ないし添
加物の均一分布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、電磁誘導撹拌装置に取入れられ
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、出湯量のコントロールはキユ
ーポ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
中に簡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 coil and a molten metal container made of a refractory material inside the cylindrical induction coil. The external pouring port is on the same level as the upper part of the container, and receives molten metal, desulfurization agent, and other additives simultaneously from the molten metal container as a continuous flow, and desulfurization treatment or addition that overflows from the communication path. It is designed to obtain a molten metal that has been given a chemical agent. Based on this configuration, it is possible to effectively combine both the stirring power and the temperature raising power by electromagnetic induction with the desulfurization effect or the uniform distribution of additives, and in particular, it is possible to separately increase the adverse effects associated with the temperature drop in the desulfurization equipment. The practical advantage of being able to remove it without installing a heating device is great. In addition, the same amount of molten metal introduced into the electromagnetic induction stirring 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 cupola. Furthermore, since the head difference between the receiving and tapping hot water is small, it can be easily 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……誘導コイル、4……炉体、4a……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。
FIG. 1 is a sectional view, and FIG. 2 is a partially omitted plan view. 1... Induction coil, 4... Furnace body, 4a... Molten metal container, 4b... Communication pipe, 4c... Pouring port, 6...
Molten metal inflow gutter, 7... desulfurization agent addition pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 筒形誘導コイルで囲まれる空間に耐火材にて
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なる連通管とを設け、上記溶
湯容器への溶湯及び添加剤の各供給手段を備えた
ことを特徴とする電磁誘導撹拌装置。
1. A molten metal container is formed from a refractory material in a space surrounded by a cylindrical induction coil, and a molten metal pouring port is placed at an appropriate place outside the induction coil at a level corresponding to the upper end of the induction coil in the molten metal container, and An electromagnetic induction stirring device, characterized in that it is provided with a communication pipe connected to the pouring port from the lower part, and is provided with means for supplying molten metal and additives to the molten metal container.
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 JPS5989704A (en) 1984-05-24
JPH0353363B2 true 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)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015083726A1 (en) * 2013-12-06 2015-06-11 横浜ゴム株式会社 Pneumatic tire

Also Published As

Publication number Publication date
JPS5989704A (en) 1984-05-24

Similar Documents

Publication Publication Date Title
EP0434822A1 (en) Continuous casting of ingots
SU725571A1 (en) Device for metal refining with gaseous and powder-like reagents
JP2001040411A (en) Ladle for refining molten steel
JPH07331351A (en) Copper smelting equipment
US3971547A (en) Apparatus and method for refining metal
JPH0353363B2 (en)
KR100305497B1 (en) Holding furnace for oxygen-free copper continuous casting
EP0116221B1 (en) Apparatus for and method of desulfurizing and heating molten metal
US3700779A (en) Method of treatment of liquid steel under vacuum
KR20000060792A (en) Ladle for Aluminum Molten Metal
CN104451355A (en) High phosphorous cast iron inoculating treatment method device in vacuum induction furnace
US5845699A (en) Strip casting
JPS63149055A (en) Refining method for molten steel in tundish for continuous casting
US3961779A (en) Apparatus and method for refining a metal melt
US3819842A (en) Method and furnace for maintaining the temperature level of metal melts
KR20180040587A (en) Channel type induction furnace
JPH0126158B2 (en)
JPS60208083A (en) Electromagnetic desulfurizing device
KR101356909B1 (en) High clean molten steel refiner and high clean molten steel manufacturing method
RU2061057C1 (en) Equipment with electric heater for treatment of metal with gases
JPS6229885A (en) Continuous tapping type temperature elevating furnace
JPH0235004B2 (en)
JP2000301320A (en) How to eliminate porous clogging in ladle refining furnace
JPS5873711A (en) Desulfurizing device for molten cast iron
JPS62144865A (en) Casting method