JPS58130217A - Ladle refining method - Google Patents
Ladle refining methodInfo
- Publication number
- JPS58130217A JPS58130217A JP1018182A JP1018182A JPS58130217A JP S58130217 A JPS58130217 A JP S58130217A JP 1018182 A JP1018182 A JP 1018182A JP 1018182 A JP1018182 A JP 1018182A JP S58130217 A JPS58130217 A JP S58130217A
- Authority
- JP
- Japan
- Prior art keywords
- ladle
- molten metal
- liquid
- atmosphere
- gas
- 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.)
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Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/04—Removing impurities by adding a treating agent
- C21C7/072—Treatment with gases
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Treatment Of Steel In Its Molten State (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は、取鍋内で溶融金属に対する合金添加、不純
物除去、攪拌などの処l1t−行う取鍋精錬法の改曳K
llするものである。DETAILED DESCRIPTION OF THE INVENTION The present invention is an improved ladle refining method in which alloying, impurity removal, stirring, etc. are performed on molten metal in a ladle.
It is something that I will do.
近年、溶鋼等o111融金属の高品質化、生産性向上、
安定操業などの目的で、溶融金属に対する取鍋精錬処理
を行うのが一般化して1ている。この取鎗精錬処理とし
ては、合金添加、脱酸中脱硫などの不純物除去、ポーラ
スプラグによる不活性ガスの底吹き中浸漬ランスによる
不活性ガスの上吹きなどによる溶融金属の攪拌等がある
が、このような処理を安定してかつ効果的に行うには、
取鍋内管非酸化性雰囲気に維持する必要がある。In recent years, the quality of O111 molten metal such as molten steel has improved, productivity has improved,
For the purpose of stable operation, it has become common to perform ladle refining treatment on molten metal. This hammer refining process includes alloy addition, removal of impurities such as desulfurization during deoxidation, stirring of molten metal by bottom blowing of inert gas with a porous plug, and top blowing of inert gas with an immersion lance. To perform such processing stably and effectively,
It is necessary to maintain a non-oxidizing atmosphere inside the ladle.
取鍋内を非酸化性雰囲気に維持する方法としては、従来
、取鍋に1lItかぶせ、その中にN、ガスヤArガス
などの不活性ガスを送p込む方法や、取鍋内の溶融金属
を被覆しているスラグ層が処理のためのガス攪拌で破ら
れてi鉄溶融金属が露出した部分に向けて不活性ガスを
噴射してシールする方法(%金昭56−43373号公
報)などがある。Conventional methods for maintaining the inside of the ladle in a non-oxidizing atmosphere include covering the ladle with 1 liter of gas and pumping an inert gas such as N, gas or Ar gas into the ladle, or removing the molten metal in the ladle. There is a method of sealing by injecting inert gas toward the exposed part of the molten iron metal when the covering slag layer is broken by gas agitation for treatment (Kin-Sho No. 56-43373). be.
しかしながら、このような従来の方法では、取鍋内の雰
囲気中は大気との比重差が小さくかつ乱流状態であるた
め、不活性ガス管導入し九場合に溶融金属表面が非酸化
性状11(0,(1vot噂)となるのに長時間t−要
するだけでなく、不活性ガスの流量が少なすぎると良好
な非酸化性状態が得られず、流速が大きすぎると外気の
巻き込みを生じ中すい九め、不活性ガスの送り込み条件
に制約を有し、加えて上蓋と取鍋の四層性が悪い場合に
は非酸化性雰囲気がζわれてしオリなどの欠点を有して
い九〇
この発明は、上述した従来の欠点に着目してなされ念も
ので、取鍋内における非酸化性雰囲気を短時間のうちに
安定して形成することがでキ、嵐好な非酸化性雰囲気の
−とでの溶融金属に対する処理がa]能であり、従来の
ような上蓋中スラグなどを必らずしも使用する必要がな
い取鍋精錬法を提供することを目的としている。However, in such conventional methods, the difference in specific gravity between the ladle and the atmosphere is small and the atmosphere is turbulent, so when an inert gas pipe is introduced, the surface of the molten metal becomes non-oxidized ( Not only does it take a long time to reach 0, (1vot rumor), but if the flow rate of inert gas is too low, a good non-oxidizing state cannot be obtained, and if the flow rate is too high, outside air may be entrained. Finally, there are restrictions on the conditions for feeding the inert gas, and in addition, if the four-layer structure of the top cover and ladle is poor, the non-oxidizing atmosphere may be eroded. This invention was made by focusing on the above-mentioned drawbacks of the conventional technology. It is an object of the present invention to provide a ladle refining method in which molten metal can be treated with a] and which does not necessarily require the use of slag in the upper lid as in the conventional method.
この発明は、取鍋内で溶融金属に対して合金添加、脱酸
や脱硫などの不純物除去、攪拌などの処理を行う取鍋精
錬法において、前記取鍋内の溶融金属表面に液体状不活
性物質を供給し、当諌溶融金I4表面で前記液体状不活
性物質の気化ならびに上昇気fILを生じさせて非酸化
性雰囲気の迅速な形成ならびKm#を実現しうるように
したことtI!Ii黴としている。In a ladle refining method in which alloy addition to molten metal, removal of impurities such as deoxidation and desulfurization, and stirring are performed on molten metal in a ladle, the surface of the molten metal in the ladle is coated with a liquid inert material. The material was supplied to cause the vaporization of the liquid inert substance and the rising air fIL on the surface of the molten gold I4, so that the rapid formation of a non-oxidizing atmosphere and Km# could be realized. Ii mold.
この発明が適用される取鍋精錬法は、いわゆる取鍋を使
用した精錬法であり、具体的には、取鍋内の溶融金属管
アーク加熱するための電極管備えたもの、取鍋内の溶融
金属を攪拌する九めの装置、例えば、電磁誘導攪拌装置
、取鍋上部や取鍋底部からの攪拌ガス供給装置、機械的
な攪拌装置などを単独であるいは併用して備えたもの、
線材や粉末として合金成分あるいはスラグ成分を添加す
る九めの添加装置を備えたもの、減圧下で精錬を行うた
めに減圧(真空)装置(タンク)t−備えたものなどが
ある。The ladle refining method to which this invention is applied is a refining method that uses a so-called ladle. Specifically, it includes a ladle equipped with an electrode tube for arc heating the molten metal tube in the ladle, and a ladle refining method that uses a ladle. Ninth device for stirring molten metal, such as an electromagnetic induction stirring device, a stirring gas supply device from the top of the ladle or the bottom of the ladle, a mechanical stirring device, etc. alone or in combination;
There are those equipped with a ninth addition device for adding alloy components or slag components in the form of wire or powder, and those equipped with a vacuum device (tank) for refining under reduced pressure.
また、液体状不活性物質としては、液体窒素中漬体アル
ゴンなどを使用するのが簡便でかつ有効である。Furthermore, as the liquid inert substance, it is convenient and effective to use argon soaked in liquid nitrogen.
上記し九取鍋精錬法において、前記取鍋内の溶融金属表
面に液体窒嵩や液体アルゴン等の液体状不活性物質を供
給すると、供給した液体状不活性物質は比重差から直接
溶融金属表面上に落下する。In the nine ladle refining method described above, when a liquid inert substance such as liquid nitrogen or liquid argon is supplied to the surface of the molten metal in the ladle, the supplied liquid inert substance is directly applied to the surface of the molten metal due to the difference in specific gravity. fall on top.
この液体状不活性物質は落下と同時に瞬間的に気化し、
溶融金属表面上で不活性気体層を形成すると同時に、溶
融金属表面を蒸発源とする如く上昇気流を形成する。し
念がって、取鍋内は迅速に非酸化性雰囲気に置換される
と共に、連続し皮下活性ガスの上昇気流によって外部か
ら取鍋内への大気の浸入をことごとく防ぐことができ、
取鍋内の非酸化性雰囲気ta好に維持することができる
。This liquid inert substance instantly vaporizes as it falls,
At the same time, an inert gas layer is formed on the surface of the molten metal, and at the same time, an upward air current is formed so that the surface of the molten metal becomes an evaporation source. With this in mind, the inside of the ladle can be quickly replaced with a non-oxidizing atmosphere, and the continuous updraft of subcutaneous active gas can completely prevent atmospheric air from entering the ladle from the outside.
A good non-oxidizing atmosphere within the ladle can be maintained.
実残例 1 ここでは第1図に示す取鍋精錬装置を使用して行つ九。Actual example 1 Here, the ladle refining apparatus shown in FIG. 1 is used.
第1図に示す装置は、取鍋本体1に上蓋2をかぶせ、取
鍋本体1内に溶融金属6會収容すると共に、取鍋本体1
の底部にポーラスプラグ4を取付け、ポーラスプラグ4
および攪拌用ガス供給15を介して溶融金属6中に攪拌
用ガス6の送給を可能にし、さらに上蓋2に液体状不活
性物質供給管7t−取付け、溶融金属6の表面への液体
状不活性物質8の送り込みを可能にしている。なお、9
はスラグである。The apparatus shown in FIG.
Attach the porous plug 4 to the bottom of the
The stirring gas 6 can be fed into the molten metal 6 through the stirring gas supply 15, and a liquid inert substance supply pipe 7t is attached to the upper lid 2, so that the liquid inert substance is not applied to the surface of the molten metal 6. This allows the active substance 8 to be delivered. In addition, 9
is a slag.
ここで使用し九溶融金属6は、表に示す化学成分のアル
ミキルド低合金鋼である。The molten metal 6 used here is aluminum killed low alloy steel having the chemical composition shown in the table.
次に、前記破鍋(容量15 Ton )内に入れた上記
成分の溶融金属6に対し、攪拌用ガス送給管5より攪拌
用ガス6としてアルゴンガスを0.3Nm”/minの
流量で送シ込んで第2図に示す攪拌のエネルギ密度二以
上の攪拌力を付与して攪拌を行うと共に、攪拌によって
溶融金属6がスラグ9の間から露出し九部分を中心にし
て、前記溶融金属60表向に、液体状不活性物質供給管
7よp液体状不活性物質8として筐体窒1It−気体換
算で1.ON11l”/minの流量で供給する。この
結果、液体窒素は溶融金属60表面で気化すると共に1
矢印人方向く上昇気5t′t−生じ、取鍋本体1と上蓋
2との間および上蓋2と液体状不活性物質供給管7との
間から抜ける。Next, argon gas was fed as the stirring gas 6 from the stirring gas supply pipe 5 at a flow rate of 0.3 Nm''/min to the molten metal 6 of the above components placed in the broken pot (capacity 15 ton). The molten metal 6 is exposed from between the slag 9 and the molten metal 6 On the surface, the liquid inert material supply pipe 7 supplies the liquid inert material 8 to the housing nitrogen at a flow rate of 1.ON11 l''/min in terms of gas. As a result, liquid nitrogen vaporizes on the surface of the molten metal 60 and
Rising air 5t't- is generated in the direction of the arrow and escapes from between the ladle body 1 and the upper lid 2 and between the upper lid 2 and the liquid inert substance supply pipe 7.
このような攪拌処理において、第1図の取鍋の×点部分
における攻鍋内雰囲気中00.@度変化および溶融金属
3中の全酸素濃度変化をそれぞれ処理開始から調べたと
ころ、第3図および第4図に示す結果となった。In such a stirring process, 0.00. When the temperature change and the total oxygen concentration change in the molten metal 3 were investigated from the start of the treatment, the results are shown in FIGS. 3 and 4.
第3図は取鍋内の第1図x点の0□渋度変化を示すもの
で、本実施例による場合には溶融金s!sの表面に液体
窒素を供給しているため、その比重差によってきわめて
迅速KJI鍋内を雰囲気置換でき九ことが明らかである
。これに対して、溶融金属るのlI!画に同量(1,0
島” / wim )の気体窒素を供給した場合には、
雰囲気との比重差が小さい友め、雰囲気置換に要する時
間がかなり長くなっていることが明らかである。ま友、
第4図は溶鋼中全酸素濃度を示すもので、液体窒素を溶
融金属6の表面に供給した場合の方が溶融金属3の精錬
効果が明らかに促進されていることがわかる。Figure 3 shows the change in astringency of 0□ at point x in Figure 1 in the ladle, and in the case of this example, molten gold s! It is clear that because liquid nitrogen is supplied to the surface of the KJI pot, the atmosphere inside the KJI pot can be replaced very quickly due to the difference in specific gravity. On the other hand, the molten metal lI! The same amount (1,0
When gaseous nitrogen is supplied from the island (wim),
It is clear that the time required to replace the atmosphere is considerably longer when the difference in specific gravity with the atmosphere is small. Mayu,
FIG. 4 shows the total oxygen concentration in the molten steel, and it can be seen that the refining effect of the molten metal 3 is clearly promoted when liquid nitrogen is supplied to the surface of the molten metal 6.
実施例 2
この実施例では、第6図に示すように、溶融金属5をア
ーク加熱するための電極(三本)11t−備えた職鍋精
錬炉を例にとっている。なお、第5図に示す符号は第1
図の符号と同一機能部分において同一である。Embodiment 2 In this embodiment, as shown in FIG. 6, a pot refining furnace equipped with three electrodes 11t for arc heating the molten metal 5 is taken as an example. Note that the symbols shown in FIG.
The same functional parts as the reference numerals in the figure are the same.
そこで、第5図に示す城鍋槽錬炉(容置15Ton)K
jrいて、電1i11による通電加熱時間中に、攪拌用
ガス供給管5からアルゴンガス6t30L/m1n(D
流量で送り込んで攪拌を行うと同時に、液体状不活性物
質供給管7より液体アルゴン8を気体換算1.0 Nt
n” / mlaの流量で供給して取鍋内雰囲気を置換
した。そして、置換の開始から第5図中X印の位置での
雰囲気中0.濃WILを測定し念ところ、第6図に示す
ように、きわめて短時間のうちにきわめて棗好な非酸化
性雰囲気を安定して得ることがで龜友。また、液体アル
ゴンの代りにアルゴンガスを同量供給した場合の同位置
における雰囲気中08濃ft同様に調べたと仁ろ、同じ
く第6図に示すように、雰囲気置換が緩慢で時間を要し
、加えて雰囲気中02濃度が不安定であるという好まし
くない結果となった。Therefore, a castle pot tank refining furnace (capacity 15 tons) K shown in Fig. 5 was used.
argon gas 6t30L/m1n (D
At the same time, liquid argon 8 was fed at a flow rate and stirred at a rate of 1.0 Nt in terms of gas from the liquid inert material supply pipe 7.
The atmosphere in the ladle was replaced by supplying at a flow rate of n"/mla.Then, from the start of replacement, the 0.0 concentration WIL in the atmosphere at the position of the X mark in Figure 5 was measured. As shown, it is possible to stably obtain an extremely favorable non-oxidizing atmosphere in a very short period of time.Also, when the same amount of argon gas is supplied instead of liquid argon, the atmosphere at the same position is When 08 concentration ft was investigated in the same manner, as shown in FIG. 6, the atmosphere replacement was slow and took time, and in addition, the 02 concentration in the atmosphere was unstable, which were unfavorable results.
実施例 3
この実施例では第7図に示すように、攪拌用ガス供給管
5の端部に上吹きランス14を堰付け、この上吹きラン
ス14t−上蓋2に貫通させて、上吹きランス14から
の攪拌用ガス6によって溶融金属6の攪拌を行うと共に
、液体状不活性物質供給管7の先端に、前記上吹きラン
ス14の囲りに配置した環状流体管17を取付けた構造
の取鍋を例にとっている。なお、第7図に示す符号は第
1図の符号と同一機能部分において同一である。Embodiment 3 In this embodiment, as shown in FIG. 7, a top blow lance 14 is attached to the end of the stirring gas supply pipe 5, and the top blow lance 14t is passed through the top cover 2. The ladle has a structure in which the molten metal 6 is stirred by the stirring gas 6 from the above, and an annular fluid pipe 17 arranged around the top blowing lance 14 is attached to the tip of the liquid inert material supply pipe 7. is taken as an example. Note that the symbols shown in FIG. 7 are the same as those in FIG. 1 for the same functional parts.
環状流体管17は、第8図および第9図に示すように、
液体状不活性物質8が気化した不活性ガスを分離排出す
るための気体ノズル21を上面側に有していると共に、
液体状不活性物質8を溶融金属60表面に向けて供給す
る液体ノズル22を下面側に有する構造をなしている。The annular fluid pipe 17, as shown in FIGS. 8 and 9,
The liquid inert substance 8 has a gas nozzle 21 on the upper surface side for separating and discharging the vaporized inert gas, and
It has a structure in which a liquid nozzle 22 for supplying liquid inert substance 8 toward the surface of molten metal 60 is provided on the lower surface side.
そこで、取鍋(容量15 Ton )内に入れた〆I表
に示す成分の溶融金属6に対し、攪拌用ガス過給管5を
経て上吹きランス14からアルゴンガスtioOA/m
1no流量で送り込んで効果的な攪拌エネルギ密度以上
の攪拌力を付与して攪拌管行うと共に、液体状不活性物
質供給管7より液体アルゴンt1.5b/mimの流量
で供給し、環状流体管17の上面側に設は友気体ノズル
21よりアルゴンガスを上吹きランス14の側面に向け
て第9図(&)の矢印方向に流すと同時に、環状流体管
17の下面側に設は友液体ノズル22より液体アルゴン
を溶融金属30表面に向けて供給し7’!、。Therefore, argon gas tioOA/m was added to the molten metal 6 having the components shown in Table I in a ladle (capacity 15 ton) from the top blowing lance 14 through the stirring gas supercharging pipe 5.
At the same time, liquid argon is supplied at a flow rate of 1.5 b/min from the liquid inert material supply pipe 7 to provide a stirring force higher than the effective stirring energy density to the annular fluid pipe 17. A friendly liquid nozzle 21 installed on the upper side causes argon gas to flow toward the side of the top blowing lance 14 in the direction of the arrow in FIG. 22, liquid argon is supplied toward the surface of the molten metal 30, and 7'! ,.
このように攪拌用ガス6を上吹きランス14から供給し
て溶融金属δの攪拌を行うようK t、、九堆絹に対し
ても、上記溶融金属60表面に液体状不活性物質8t−
供給すること罠よって、取鍋内1118気全迅速に非酸
化性雰囲気に置換することができると同時に、上記非酸
化性雰囲気を良好Kf41に持できることが確認され友
。In order to stir the molten metal δ by supplying the stirring gas 6 from the top blowing lance 14 in this way, 8 tons of liquid inert material is added to the surface of the molten metal 60.
It was confirmed that by using the supply trap, all 1118 air in the ladle can be quickly replaced with a non-oxidizing atmosphere, and at the same time, the non-oxidizing atmosphere can be maintained at a good Kf41.
なお、上配し九各実施例においては、溶融金属3の攪拌
手段として、ポーラスプラグ4あるいは上吹きランス1
4から送給される不活性ガス6を用いた場合を示してい
るが、そのほか、攪拌手段として、電磁誘導攪拌装置や
プロペラ等の機械的な攪拌装置など1*独であるいはこ
れらt併用して備えた取鍋精錬装置に対しても適用する
ことができ、さらには溶融金属6の攪拌処理だけでなく
、合金添加処理、あるいは脱酸や脱硫などの不純物除去
処理等の際にもこの発WAtl−適用することができる
。In addition, in each embodiment of the upper arrangement, a porous plug 4 or an upper blowing lance 1 is used as a stirring means for the molten metal 3.
The case is shown in which the inert gas 6 supplied from 4 is used, but other stirring means include mechanical stirring devices such as electromagnetic induction stirring devices and propellers 1* alone or in combination. It can also be applied to ladle refining equipment equipped with a ladle refining equipment, and furthermore, this WAtl can be used not only for stirring the molten metal 6, but also for alloy addition processing, or impurity removal processing such as deoxidation and desulfurization. - Can be applied.
以上説明してきたように、この発明によれば、取鍋内で
溶融金属の処理を行う取@稽錬法において、前記取鍋内
の溶融金属表面に液体状不活性物質を供給し、尚該溶融
金属表面で前記液体状不活性物質の気化ならびに上昇気
流を生じさせるようにしたから、取鍋内における非酸化
性雰囲気を極めて短時間のうちにかつ非常に安定して形
成することができ、良好な非酸化性雰囲気のもとての溶
融金属に対する合金添加、不純物除去、攪拌等の処理が
可能であり、従来のように上蓋やスラグなどを必らずし
も使用する必要がなく、また雰囲気置換の九めに長時間
にわたる操業準備操作を行う必要もないなどの数々の著
大なる効果を有する。As explained above, according to the present invention, in the ladle method in which molten metal is treated in a ladle, a liquid inert substance is supplied to the surface of the molten metal in the ladle, and the molten metal is Since the liquid inert substance is vaporized and an upward air current is generated on the surface, a non-oxidizing atmosphere can be formed in the ladle in a very short time and in a very stable manner, resulting in a good ladle. It is possible to add alloys, remove impurities, stir, etc. to molten metal in a non-oxidizing atmosphere, and there is no need to use a top lid or slag as in the past, and it is also possible to replace the atmosphere. Ninth, it has many significant effects, such as eliminating the need for long hours of operation preparation operations.
第imlはこの発明の実施例1において使用し九取鍋精
錬装置の縦断面説明図% K 2図は溶融金属の均一混
合に必要な時間<1)とエネルギ密度(−)との関係の
一例を示すグラフ、第3図および第4図はそれぞれ第1
図の取鍋の×点部分における取鍋内雰囲気中の0.濃度
変化および溶融金属中の全酸素濃度変化をそれぞれ処理
開始から調べた結果を示すグラフ、第5図はこの発明の
実施例2において使用し友取鍋精錬装置の縦断面説明図
、第6図は第5図の取鍋内x印部分における雰囲気中O
8濃度変化を置換の開始から調べた結果を示すグラフ、
第7図はこの発明の実施例3において便用し九取鍋精錬
装置の縦断面説明図、第8図は第7図の環状流体管の平
面図、第9図(&)(b)は第8図の各々ムーA纏およ
びB−B線断面図である。
1・・・取鍋本体、6・・・溶融金属、5−・攪拌用ガ
ス供給管、6−・攪拌用ガス、7・・・液体状不活性物
質供給管、8・・・液体状不活性物質、A−・・上昇気
流の方向。
特許出願人 大同特殊鋼株式会社
代理人弁通士 小 塩 豊第1図
42N
工xルff!l ε(Wrl tt/ 丁@M )第3
しj
処理#l鱈fly帽◆問(會)
処a和tea、番吟閏(創
第5図
第6図
這」央開姥カ・ジの吟閏(介)No. iml is an explanatory longitudinal cross-sectional view of the nine-ladle refining device used in Example 1 of the present invention. Figure 2 is an example of the relationship between the time required for uniform mixing of molten metal (<1) and energy density (-). The graphs shown in Figures 3 and 4 are respectively
0.0 in the atmosphere inside the ladle at the x-point part of the ladle in the figure. Graphs showing the results of investigating concentration changes and total oxygen concentration changes in molten metal from the start of treatment, respectively. FIG. 5 is a vertical cross-sectional explanatory diagram of the ladle refining apparatus used in Example 2 of the present invention, and FIG. 6 is the O in the atmosphere at the x-marked part in the ladle in Figure 5.
8 Graph showing the results of examining concentration changes from the start of replacement,
Fig. 7 is a longitudinal cross-sectional explanatory view of a nine-ladle refining device conveniently used in Embodiment 3 of the present invention, Fig. 8 is a plan view of the annular fluid pipe of Fig. 7, and Fig. 9 (&) (b) is a FIG. 8 is a cross-sectional view taken along line A and B-B of FIG. 8, respectively. DESCRIPTION OF SYMBOLS 1... Ladle body, 6... Molten metal, 5-- Stirring gas supply pipe, 6-- Stirring gas, 7... Liquid inert substance supply pipe, 8... Liquid inert substance supply pipe. Active substance, A--direction of updraft. Patent Applicant: Daido Steel Co., Ltd. Agent: Yutaka Koshio No. 1 Fig. 42N Engineering x Le ff! l ε (Wrl tt/ Ding@M) 3rd
Shij Processing #l Cod fly hat
Claims (1)
て、前配取鍋内の溶融金属表面に液体状不活性物質を供
給し、蟲該溶融金属表面で前記液体状不活性物質の気化
表らびに上昇気流を生じさせることt一時機とする取鍋
精錬法。(1) In a ladle refining method in which molten metal is processed in a ladle, a liquid inert substance is supplied to the surface of the molten metal in the ladle, and the liquid inert substance is applied to the surface of the molten metal. A ladle refining method in which the vaporization and updraft are created at one time.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1018182A JPS58130217A (en) | 1982-01-27 | 1982-01-27 | Ladle refining method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1018182A JPS58130217A (en) | 1982-01-27 | 1982-01-27 | Ladle refining method |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58130217A true JPS58130217A (en) | 1983-08-03 |
Family
ID=11743114
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1018182A Pending JPS58130217A (en) | 1982-01-27 | 1982-01-27 | Ladle refining method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58130217A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2635789A1 (en) * | 1988-08-29 | 1990-03-02 | Air Liquide American | PROCESS FOR PRODUCING STEEL WITH LOW NITROGEN CONTENT IN POCKET OVEN |
US20130213184A1 (en) * | 2010-10-26 | 2013-08-22 | Anatoly Alexeevich Kuznetsov | Process For Making Low and Specified Hardenability Structural Steel |
-
1982
- 1982-01-27 JP JP1018182A patent/JPS58130217A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2635789A1 (en) * | 1988-08-29 | 1990-03-02 | Air Liquide American | PROCESS FOR PRODUCING STEEL WITH LOW NITROGEN CONTENT IN POCKET OVEN |
US20130213184A1 (en) * | 2010-10-26 | 2013-08-22 | Anatoly Alexeevich Kuznetsov | Process For Making Low and Specified Hardenability Structural Steel |
US9187793B2 (en) * | 2010-10-26 | 2015-11-17 | Anatoly Alexeevich Kuznetsov | Process for making low and specified hardenability structural steel |
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