JP2000204421A - Gas-stirring of molten metal - Google Patents

Gas-stirring of molten metal

Info

Publication number
JP2000204421A
JP2000204421A JP361099A JP361099A JP2000204421A JP 2000204421 A JP2000204421 A JP 2000204421A JP 361099 A JP361099 A JP 361099A JP 361099 A JP361099 A JP 361099A JP 2000204421 A JP2000204421 A JP 2000204421A
Authority
JP
Japan
Prior art keywords
ladle
stirring
molten metal
immersion tube
immersion
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
JP361099A
Other languages
Japanese (ja)
Other versions
JP4009029B2 (en
Inventor
Kazuhiro Matsuzawa
和宏 松澤
Naochika Imamura
尚近 今村
Shigenori Yakura
重範 矢倉
Tsukasa Kashiwabara
司 柏原
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP00361099A priority Critical patent/JP4009029B2/en
Publication of JP2000204421A publication Critical patent/JP2000204421A/en
Application granted granted Critical
Publication of JP4009029B2 publication Critical patent/JP4009029B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)
  • Treatment Of Steel In Its Molten State (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for shortening uniform mixing time by effectively stirring the whole molten metal in a ladle more than the conventional method, in the case of stirring the whole molten metal with gas for stirring by dipping an immersion tube for charging an adjusting material for adjusting a component in the molten metal under atmospheric pressure. SOLUTION: In a ladle refining by dipping the immersion tube for charging the adjusting material for adjusting the component into the molten metal and blowing and stirring the gas into the molten metal from the lower part, the diameter (d) of the immersion tube satisfies an inequality I and the position of a gas blowing nozzle for stirring is made to the center part of the immersion tube, and further, an eccentric quantity X of the center in the diameter direction of the immersion tube to the center in the diameter direction of the ladle satisfies an inequality II. The inequality I: 1.2.2h.tan(θ/2)<=d<=2.0.2h.tan(θ/2). The inequality II: d/2<=X<=D/2-h.tan(θ/2), wherein, h: blowing depth of the gas for stirring from the lower end of the immersion tube, θ: widening angle of rising gas bubbles and D: diameter of the ladle.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、溶融金属の取鍋精
錬における溶融金属のガス攪拌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 agitating molten metal gas in ladle refining of molten metal.

【0002】[0002]

【従来の技術】溶融金属の成分調整方法として、取鍋に
収容された溶融金属に浸漬管を浸漬し、浸漬管の下方か
ら攪拌用ガスを吹込みつつ、浸漬管内上方から成分調整
用物質を溶融金属内に投入する取鍋精錬法が存在する。
溶融金属が溶鋼の場合には、例えば特開平7−1131
14号公報に開示される方式が提案されている。
2. Description of the Related Art As a method for adjusting the composition of a molten metal, an immersion tube is immersed in a molten metal stored in a ladle, and a stirring gas is blown from below the immersion tube while a substance for adjusting the component is injected from above the immersion tube. There is a ladle refining method for pouring into molten metal.
When the molten metal is molten steel, for example, Japanese Unexamined Patent Publication No.
A method disclosed in Japanese Patent Publication No. 14 has been proposed.

【0003】この方法は、図2(a)に示すように浸漬
管4下方から攪拌用ガス6を吹込むことで形成するプル
ーム(上昇する気泡領域)の広がりを考慮し、浸漬管4
径方向中心と取鍋1径方向中心を一致させると共に攪拌
用ガス6吹込み位置を取鍋1径方向中心に対して下記
(3)式に示す範囲Yだけ偏芯させるものである。 h・tan(θ/2)≦Y≦d/2−h・tan(θ/2) ・(3) 但し、 d:浸漬管径
In this method, as shown in FIG. 2A, the expansion of a plume (bubble bubble region) formed by blowing a stirring gas 6 from below the dip tube 4 is taken into consideration.
The center of the ladle 1 and the center of the ladle 1 are made to coincide with each other, and the blowing position of the stirring gas 6 is eccentric with respect to the center of the ladle 1 by the range Y shown in the following formula (3). h · tan (θ / 2) ≦ Y ≦ d / 2−h · tan (θ / 2) (3) where d: diameter of immersion tube

【0004】この方法は、成分調整と共に浸漬管内を減
圧状態にして溶融金属内脱ガス反応を促進させる減圧精
錬反応には有効である。即ち図2(a)に示すように浸
漬管4内を減圧した場合には浸漬管4内の溶融金属2上
面が浸漬管4外に比べ上昇するため、この際に浸漬管4
内の溶融金属2に上昇流が発生し、さらに浸漬管4下方
からの吹込み攪拌ガス6との相乗効果により浸漬管4内
では一層大きな溶融金属2上昇流の発生と共に、浸漬管
4外への流出する溶融金属2攪拌流7が発生するためで
ある。また、減圧精錬装置では脱ガス反応を効率よく行
うため、浸漬管4内の溶融金属2上面の反応面積を大き
くしなければならず、取鍋径dに対する浸漬管径Dを大
きくする必要がある。しかしながら、脱ガス反応効果の
少ない常圧下での精錬装置への従来方法の適用は成分調
整用物質の攪拌が十分にできない。
[0004] This method is effective for a vacuum refining reaction in which the degassing reaction in the molten metal is promoted by reducing the pressure inside the immersion tube while adjusting the components. That is, when the inside of the immersion tube 4 is depressurized as shown in FIG. 2A, the upper surface of the molten metal 2 in the immersion tube 4 rises as compared with the outside of the immersion tube 4.
An upward flow is generated in the molten metal 2 inside the immersion tube 4, and a larger upward flow of the molten metal 2 is generated in the immersion tube 4 by the synergistic effect with the blowing stirring gas 6 from below the immersion tube 4, and the molten metal 2 flows out of the immersion tube 4. This is because the agitated flow 7 of the molten metal 2 that flows out is generated. Further, in the vacuum refining apparatus, in order to efficiently perform the degassing reaction, the reaction area of the upper surface of the molten metal 2 in the immersion pipe 4 must be increased, and the immersion pipe diameter D with respect to the ladle diameter d needs to be increased. . However, when the conventional method is applied to a refining apparatus under normal pressure where the degassing reaction effect is small, stirring of the component adjusting substance cannot be sufficiently performed.

【0005】即ち、浸漬管内を常圧状態下で、前記特開
平7−113114号公報に示されているように、浸漬
管径dの取鍋径Dに対する比率を高めた場合(前記特開
平7−113114号公報の実施例では浸漬管4断面積
に対する浸漬管4内の溶融金属2上面の攪拌プルーム面
積の比率を0.03程度に小さくにした場合)は、図2
(b)に示すように、攪拌用ガス6によって生成した上
昇流は溶融金属2上面から浸漬管内壁に向かって流動す
るものの、浸漬管径が大きいため浸漬管内壁に衝突する
までに減速してしまい、その結果衝突後の下降流も更に
減速するため、取鍋内溶融金属2全体を攪拌させる流動
が得られなくなってしまう。以上のように、本方法を常
圧状態下で適用した場合には、取鍋内溶融金属2全体を
均一に混合させるのに時間を要する問題があった。
That is, when the ratio of the diameter d of the immersion tube to the diameter D of the ladle is increased while the inside of the immersion tube is under normal pressure as described in Japanese Patent Application Laid-Open No. In the example of JP-A-113114, when the ratio of the area of the stirring plume on the upper surface of the molten metal 2 in the immersion tube 4 to the cross-sectional area of the immersion tube 4 is reduced to about 0.03), FIG.
As shown in (b), although the upward flow generated by the stirring gas 6 flows from the upper surface of the molten metal 2 toward the inner wall of the immersion tube, it decelerates before colliding with the inner wall of the immersion tube due to the large diameter of the immersion tube. As a result, the descending flow after the collision is further decelerated, so that a flow for stirring the entire molten metal 2 in the ladle cannot be obtained. As described above, when the present method is applied under normal pressure, there is a problem that it takes time to uniformly mix the entire molten metal 2 in the ladle.

【0006】[0006]

【発明が解決しようとする課題】本発明の目的は、常圧
下にて溶融金属の成分調整用物質を投入する為の浸漬管
を浸漬し、攪拌用ガスによる溶融金属の攪拌を行うに当
たり、取鍋内溶融金属全体を効果的に攪拌を生じさせ、
均一混合時間を短縮する方法を提供することである。
SUMMARY OF THE INVENTION An object of the present invention is to immerse a dip tube into which a substance for adjusting the composition of a molten metal is introduced under normal pressure and stir the molten metal with a stirring gas. Effectively agitating the entire molten metal in the pot,
It is an object of the present invention to provide a method for shortening the uniform mixing time.

【0007】[0007]

【課題を解決するための手段】かかる目的達成の為の手
段について、本発明者は、詳細なる検討及び緻密な実験
等を繰り返し実施した結果、常圧下にて溶融金属の混合
・攪拌が主目的である精錬設備においては、浸漬管径を
最小限に抑えつつ、攪拌用ガス吹込み位置を適切に設定
することにより、上記の課題が解決可能であることを知
見し、本発明を完成させた。
The present inventor has repeatedly conducted detailed examinations and detailed experiments on the means for achieving the object, and as a result, the main object of the present invention is to mix and stir the molten metal under normal pressure. In the refining equipment, it was found that the above-mentioned problems could be solved by appropriately setting the stirring gas injection position while minimizing the immersion pipe diameter, and completed the present invention. .

【0008】ここに、本発明の要旨とするところは、図
1に示すように溶融金属を収容する取鍋中に浸漬管を浸
漬させて、浸漬管内に溶融金属の成分調整用物質を投入
しつつ取鍋下部の浸漬管下方に設置したノズルから攪拌
用ガスを吹込み溶融金属を攪拌しながら取鍋精錬を行う
に際して、浸漬管径dが下記(4)式の条件を満たし、
且つ、攪拌用ガス吹込み位置は浸漬管径方向中心とし、
更に、取鍋径方向中心に対する浸漬管径方向中心の偏芯
量Xが下記(5)式の条件を満たすことを特徴とする溶
融金属のガス攪拌方法である。 1.2・2h・tan(θ/2)≦d≦2.0・2h・tan(θ/2)(4) d/2≦X≦D/2−h・tan(θ/2) .(5) 但し、h:浸漬管下端から攪拌用ガス吹込み深さ θ:上昇気泡の広がり角 D:取鍋径
Here, the gist of the present invention is that, as shown in FIG. 1, a dip tube is immersed in a ladle containing molten metal, and a substance for adjusting a component of the molten metal is introduced into the dip tube. When performing ladle refining while stirring the molten metal by blowing a stirring gas from a nozzle installed below the dip tube below the ladle, the dip tube diameter d satisfies the condition of the following formula (4),
And the agitating gas injection position is at the center of the immersion pipe radial direction,
Further, there is provided a gas stirring method for molten metal, wherein an eccentric amount X of a center of a ladle in a radial direction with respect to a center of a ladle in a radial direction satisfies a condition of the following formula (5). 1.2.2htan (θ / 2) ≦ d ≦ 2.0.2.htan (θ / 2) (4) d / 2 ≦ X ≦ D / 2-htan (θ / 2). (5) where, h: depth of gas blowing for stirring from the lower end of immersion tube θ: spread angle of rising bubble D: ladle diameter

【0009】[0009]

【発明の実施の形態】次に、本発明の実施の形態につい
て詳細に説明する。尚、以下の例においては、図1を基
に溶融金属として溶鋼を例にとって説明する。図1に示
すように、取鍋1に収容された溶鋼2中に溶鋼に投入す
る成分調整用物質3を投入する為の浸漬管4を浸漬させ
て、取鍋1下部の浸漬管4下に攪拌用ガス吹込みノズル
5を設置して、攪拌用ガス6を吹込み溶鋼2を攪拌しな
がら常圧下にて取鍋精錬を行う。
Next, an embodiment of the present invention will be described in detail. In the following example, molten steel will be described as an example of molten metal based on FIG. As shown in FIG. 1, an immersion pipe 4 for introducing a substance 3 for component adjustment to be introduced into molten steel is immersed in molten steel 2 accommodated in a ladle 1, and is immersed in a lower part of the ladle 1 under the immersion pipe 4. A stirring gas injection nozzle 5 is installed, and a ladle refining is performed under normal pressure while blowing the stirring gas 6 and stirring the molten steel 2.

【0010】攪拌用ガス6は溶鋼2内部を上昇しなが
ら、徐々に広がる。この広がり角をθとし、浸漬管4下
端から攪拌用ガス吹込みノズル5の吹込み点までの深さ
をhとしたとき、浸漬管4下端付近に到達した攪拌ガス
6のプルームは、半径h・tan(θ/2)の広がりを
もつ。即ち、攪拌用ガス6が浸漬管4外へ流出しない為
には、浸漬管4径dは2h・tan(θ/2)以上必要
であり、下記(6)式を満足させる必要がある。 2h・tan(θ/2)≦d .(6)
The stirring gas 6 gradually spreads while rising inside the molten steel 2. When the divergence angle is θ and the depth from the lower end of the immersion pipe 4 to the blowing point of the stirring gas injection nozzle 5 is h, the plume of the stirring gas 6 reaching the lower end of the immersion pipe 4 has a radius h.・ It has a spread of tan (θ / 2). That is, in order for the stirring gas 6 not to flow out of the immersion tube 4, the diameter d of the immersion tube 4 needs to be 2 h · tan (θ / 2) or more, and it is necessary to satisfy the following expression (6). 2h · tan (θ / 2) ≦ d. (6)

【0011】この場合、攪拌用ガス6によって浸漬管4
に流入した溶鋼2が、直ちに浸漬管4から流出し、取鍋
1内部に下降する溶鋼流7を効果的に生成させるために
は、浸漬管4径dと浸漬管4下端の高さ位置へ到達した
攪拌ガス6のプルーム径とが理想的には同じ値にするべ
きであり、従って、上記(6)式は下記(7)式とな
る。 d=2h・tan(θ/2) .(7)
In this case, the immersion tube 4 is stirred by the stirring gas 6.
In order for the molten steel 2 flowing into the ladle 1 to immediately flow out of the dipping tube 4 and effectively generate the molten steel flow 7 descending into the ladle 1, the dipping tube 4 has a diameter d and a height position at the lower end of the dipping tube 4. Ideally, the plume diameter of the reached stirring gas 6 should be the same value. Therefore, the above equation (6) becomes the following equation (7). d = 2h · tan (θ / 2). (7)

【0012】更に、前述のようにプルームを完全に浸漬
管4内に収容しつつ、浸漬管4径を最小とするために
は、幾何学的な位置関係の検討から浸漬管4径方向中心
部直下に攪拌用ガス6吹込み点を設けることが必要とな
る。
Further, as described above, in order to minimize the diameter of the immersion pipe 4 while completely accommodating the plume in the immersion pipe 4, it is necessary to consider the geometrical positional relationship and to examine the center of the immersion pipe 4 in the radial direction. It is necessary to provide a stirring gas 6 injection point immediately below.

【0013】しかしながら溶鋼流7や攪拌用ガス6流
量,圧力及びノズル状態の不安定性によりプルーム径及
びプルーム生成位置の変動は避けられない為、結果とし
て、見掛けのプルーム径が拡大し、浸漬管4内にプルー
ムを完全に収容可能とする浸漬管4径dを適宜選択する
必要がある。そこで、浸漬管4径dを変化させ、取鍋1
内の溶鋼2に成分調整物質を投入開始から、取鍋1内の
溶鋼2に完全に混合するまでの時間τ(以下均一混合時
間と称す)を調査した結果、均一混合時間を短くするた
めには(8)式の範囲とする必要があることが判った。 1.2・2h・tan(θ/2)≦d≦2.0・2h・tan(θ/2)(8)
However, fluctuations in plume diameter and plume generation position are unavoidable due to instability in the flow rate, pressure, and nozzle state of the molten steel flow 7 and the stirring gas 6, and as a result, the apparent plume diameter increases and the immersion pipe 4 It is necessary to appropriately select the diameter d of the immersion tube 4 that can completely accommodate the plume therein. Therefore, the diameter d of the immersion tube 4 is changed and the ladle 1
Investigation of the time τ (hereinafter referred to as “homogeneous mixing time”) from the start of the addition of the component adjusting material to the molten steel 2 in the ladle to the complete mixing into the molten steel 2 in the ladle 1, revealed that in order to shorten the uniform mixing time, Has to be in the range of the expression (8). 1.2.2 h · tan (θ / 2) ≦ d ≦ 2.0 · 2h · tan (θ / 2) (8)

【0014】次に、取鍋1径方向中心に対する攪拌用ガ
ス吹込みノズル5位置(=浸漬管4径方向中心)の配置
方法について述べる。本発明では、前述の浸漬管4内の
混合をも含めた取鍋1内全体の攪拌を効率良く行うた
め、浸漬管4径方向中心、即ち攪拌ガス吹込みノズル5
位置が取鍋1中心に対し偏芯量Xで配置する必要があ
る。これは図3に示すように、攪拌ガス用吹込みノズル
5位置を偏芯させた場合は、取鍋1側壁によって浸漬管
4から流出する溶鋼流7が取鍋1側壁方向へ分散し難く
なり、その結果、取鍋1内全体の一方向環状流が生じ易
くなるためである。しかし、図4に示すように偏芯量X
を大きくし過ぎると、攪拌ガス6のプルームが取鍋1の
側壁に接し、プルームを浸漬管4にて確実に覆うことが
出来なくなる。以上の結果から、取鍋1径方向中心に対
する攪拌ガス吹込みノズル5位置の偏芯量Xは、下記
(9)式の範囲にする必要がある。 d/2≦X≦D/2−h・tan(θ/2) .(9) 但し、上記(8)式の浸漬管4径dの値によって、上記
(9)式の範囲内の偏芯量Xであっても浸漬管4が取鍋
1壁に接触する場合は、浸漬管4が接触しないようなX
の値とする。
Next, a method of arranging the position of the stirring gas injection nozzle 5 with respect to the center of the ladle 1 in the radial direction (= the center of the dip tube 4 in the radial direction) will be described. In the present invention, in order to efficiently stir the entire ladle 1 including the above-described mixing in the immersion tube 4, the center of the immersion tube 4 in the radial direction, that is, the stirring gas injection nozzle 5
The position needs to be arranged with the eccentric amount X with respect to the center of the ladle 1. This is because, as shown in FIG. 3, when the position of the stirring gas injection nozzle 5 is decentered, the molten steel flow 7 flowing out of the immersion pipe 4 by the ladle 1 side wall becomes difficult to be dispersed toward the ladle 1 side wall. As a result, the one-way annular flow in the entire ladle 1 is likely to occur. However, as shown in FIG.
Is too large, the plume of the stirring gas 6 comes into contact with the side wall of the ladle 1, and the plume cannot be reliably covered with the immersion pipe 4. From the above results, the eccentric amount X at the position of the stirring gas injection nozzle 5 with respect to the center of the ladle 1 in the radial direction needs to be within the range of the following equation (9). d / 2 ≦ X ≦ D / 2−h · tan (θ / 2). (9) However, depending on the value of the diameter d of the immersion tube 4 in the above formula (8), when the immersion tube 4 comes into contact with the wall of the ladle 1 even if the eccentric amount X is within the range of the above formula (9). X such that the immersion tube 4 does not contact
Value.

【0015】以上説明したように、浸漬管4径と攪拌ガ
ス吹込みノズル5位置を一致させ、浸漬管4径d、浸漬
管4径d及び取鍋1径D方向中心に対する攪拌用ガス吹
込みノズル5位置(=浸漬管4径方向中心)の偏芯量X
を適正にすることにより、取鍋1内の溶鋼2を効率的に
混合・攪拌をすることができる。尚、図5に示すような
攪拌用ガス吹込みノズル5としてランスを用いた際も、
吹込み深さが小さくなる為、ポーラスプラグを用いて攪
拌用ガスを取鍋1の底から吹込んだ際に比較して攪拌・
混合効果は減じられるものの、本発明の効果は同等に得
られる。
As described above, the diameter of the immersion pipe 4 and the position of the stirring gas injection nozzle 5 are made to coincide with each other, and the stirring gas is injected into the center of the immersion pipe 4 d, the immersion pipe 4 d and the ladle 1 in the direction D. Eccentricity X at nozzle 5 position (= radial center of immersion tube 4)
By appropriately setting, the molten steel 2 in the ladle 1 can be efficiently mixed and stirred. When a lance is used as the stirring gas injection nozzle 5 as shown in FIG.
Since the blowing depth is small, the stirring gas is stirred and compared with the case where the stirring gas is blown from the bottom of the ladle 1 using a porous plug.
Although the mixing effect is reduced, the effect of the present invention can be obtained equally.

【0016】[0016]

【実施例】取鍋径D=4770mm,浸漬管下端から攪
拌用ガス吹込みノズルとしての取鍋底に設置したポーラ
スプラグまでの深さh=2500mmとして340tの
アルミキルド溶鋼を用い、取鍋径方向中心に対する攪拌
ガス吹込みノズル位置の偏芯量X、取鍋径方向中心に対
する浸漬管径方向中心の偏芯量Y、さらに浸漬管径dを
変化させてそれぞれの均一混合時間を調査した結果を表
1に示す。尚、本実施に当たっては、攪拌ガスとしてポ
ーラスプラグから上昇気泡の広がり角θ=20°、流量
=500NL/hrのArの吹込みを行った。
[Example] Ladle diameter D = 4770 mm, depth h from the lower end of the immersion pipe to the porous plug installed at the bottom of the ladle as a stirring gas injection nozzle, h = 2500 mm, and 340 t of aluminum killed molten steel was used. Table 1 shows the results of the investigation of the uniform mixing time by varying the eccentric amount X of the stirring gas injection nozzle position, the eccentric amount Y of the immersion pipe radial center with respect to the ladle radial center, and the immersion pipe diameter d. It is shown in FIG. In the present embodiment, Ar was blown from the porous plug as a stirring gas at a spread angle θ of the rising bubbles of 20 ° and a flow rate of 500 NL / hr.

【0017】[0017]

【表1】 [Table 1]

【0018】実施例1及び2は取鍋径方向中心に対する
攪拌ガス吹込みノズル位置の偏芯量Xと浸漬管径dを適
正範囲にし、取鍋径方向中心に対する浸漬管径方向中心
の偏芯量Yを偏芯量Xと一致(X=Y)させた例であ
る。従来例1は取鍋径方向中心と浸漬管径方向中心を一
致(X=0)させた例である。比較例1〜3は偏芯量
X、Y、浸漬管径dを本発明の範囲外にした例である。
表1より、偏芯量X、Y、浸漬管径dを適正範囲にする
ことにより均一混合時間を短縮することが可能となっ
た。
In Examples 1 and 2, the eccentricity X of the stirring gas injection nozzle position with respect to the center of the ladle in the radial direction and the immersion pipe diameter d are set to appropriate ranges, and the eccentricity of the center of the immersion pipe in the radial direction with respect to the center of the ladle is considered. This is an example in which the amount Y is made coincident with the eccentric amount X (X = Y). Conventional example 1 is an example in which the center in the ladle radial direction and the center in the dip tube radial direction are matched (X = 0). Comparative Examples 1 to 3 are examples in which the eccentric amounts X and Y and the immersion tube diameter d are out of the range of the present invention.
From Table 1, it was possible to shorten the uniform mixing time by setting the eccentric amounts X and Y and the immersion tube diameter d in appropriate ranges.

【0019】[0019]

【発明の効果】本発明により、溶融金属を収容する取鍋
中に常圧下で溶融金属の成分調整用物を投入する為の浸
漬管を浸漬させ、その浸漬管下から攪拌用ガス浸漬管内
に流入するように吹込み、溶融金属を攪拌しながら行う
取鍋精錬において、取鍋内の良好な攪拌を実現し、均一
混合時間の短縮により攪拌用ガスの使用量を大幅に削減
することが可能となり、大きな経済効果を享受する事を
可能とした。
According to the present invention, an immersion pipe for charging a molten metal component adjusting substance is immersed in a ladle for accommodating the molten metal under normal pressure, and the immersion pipe is placed under the immersion pipe into a stirring gas immersion pipe. In ladle refining, in which the molten metal is blown in while stirring and the molten metal is stirred, good stirring in the ladle is realized, and the amount of stirring gas used can be significantly reduced by shortening the uniform mixing time. It has become possible to enjoy a great economic effect.

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

【図1】本発明の概念図FIG. 1 is a conceptual diagram of the present invention.

【図2】従来技術における減圧下と常圧下の差異を示す
概念図
FIG. 2 is a conceptual diagram showing the difference between reduced pressure and normal pressure in the prior art.

【図3】取鍋と浸漬管の相対位置と溶融金属流の模式図FIG. 3 is a schematic view of a relative position of a ladle and a dip tube and a flow of a molten metal.

【図4】プルーム、浸漬管、取鍋の相対位置関係Fig. 4 Relative positional relationship between plume, dip tube and ladle

【図5】攪拌用ガス吹込みノズルにランスを用いた際の
概念図
FIG. 5 is a conceptual diagram when a lance is used for a gas injection nozzle for stirring.

【符号の説明】[Explanation of symbols]

1.取鍋 2.溶鋼(溶融金属) 3.溶鋼に投入する成分調整用物質 4.浸漬管 5.攪拌用ガス吹込みノズル 6.攪拌用ガス 7.溶鋼流(溶融金属流) d:浸漬管径 h:浸漬管下端から攪拌用ガス吹込み高さ θ:上昇気泡の広がり角 D:取鍋径 X:取鍋径方向中心に対する攪拌用ガス吹込み位置の偏
芯量 Y:取鍋径方向中心に対する浸漬管径方向中心の偏芯量 τ:均一混合時
1. Ladle 2. 2. Molten steel (molten metal) 3. Substances for adjusting components to be added to molten steel Immersion tube 5. 5. Gas blowing nozzle for stirring Stirring gas 7. Molten steel flow (molten metal flow) d: diameter of immersion pipe h: height of gas injection for stirring from lower end of immersion pipe θ: spread angle of rising bubble D: ladle diameter X: gas injection for ladle diameter center Eccentricity of position Y: Eccentricity of immersion tube radial center with respect to ladle radial center τ: At uniform mixing

フロントページの続き (72)発明者 矢倉 重範 大分県大分市大字西ノ洲1番地 新日本製 鐵株式会社大分製鐵所内 (72)発明者 柏原 司 大分県大分市大字西ノ洲1番地 新日本製 鐵株式会社大分製鐵所内 Fターム(参考) 4K001 AA10 BA04 GA18 GB05 4K013 BA16 CA02 CA21 CC04 Continued on the front page (72) Inventor Shigenori Yakura 1 Nishinosu, Oji, Oita, Oita Prefecture Inside Nippon Steel Corporation Oita Works (72) Inventor Tsukasa Kashihara 1 Nishinosu, Oita, Oita, Oita Prefecture Nippon Steel Corporation Oita Works F term (reference) 4K001 AA10 BA04 GA18 GB05 4K013 BA16 CA02 CA21 CC04

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 溶融金属を収容する取鍋中に常圧下で溶
融金属の成分調整用物質を投入する為の浸漬管を浸漬さ
せ、その浸漬管下方から攪拌用ガスを浸漬管内に流入す
るように吹込み、該金属を攪拌しながら取鍋精錬を行う
に際して、浸漬管径dが下記(1)式の条件を満たし、
且つ、前記攪拌用ガス吹込みノズルの位置を前記浸漬管
の中心部下方とし、更に、取鍋径方向中心に対しての浸
漬管径方向中心の偏芯量Xが下記(2)式の条件を満た
すことを特徴とする溶融金属のガス攪拌方法。 1.2・2h・tan(θ/2)≦d≦2.0・2h・tan(θ/2)(1) d/2≦X≦D/2−h・tan(θ/2) .(2) 但し、h:浸漬管下端から攪拌用ガス吹込み深さ θ:上昇気泡の広がり角 D:取鍋径
An immersion tube for charging a molten metal component adjusting substance is immersed in a ladle for accommodating a molten metal under normal pressure so that a stirring gas flows from below the immersion tube into the immersion tube. When performing ladle refining while stirring the metal, the immersion pipe diameter d satisfies the condition of the following formula (1),
The position of the stirring gas injection nozzle is located below the center of the immersion tube, and the eccentric amount X of the center of the immersion tube in the radial direction with respect to the center of the ladle in the radial direction is defined by the following equation (2). A gas stirring method for molten metal, characterized by satisfying the following. 1.2.2htan (.theta. / 2) .ltoreq.d.2.0.2.htan (.theta. / 2) (1) d / 2.ltoreq.X.ltoreq.D / 2-htan (.theta. / 2). (2) Here, h: Depth of gas blowing for stirring from the lower end of immersion tube θ: Spread angle of rising bubble D: Ladle diameter
JP00361099A 1999-01-11 1999-01-11 Gas stirring method for molten metal Expired - Fee Related JP4009029B2 (en)

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Application Number Priority Date Filing Date Title
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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104988343A (en) * 2015-08-12 2015-10-21 北京科技大学 Device and method for preparing light alloy semi-solid slurry through air-cooling multi-tube stirring
CN111172354A (en) * 2020-02-28 2020-05-19 鞍钢股份有限公司 Microbubble molten steel purification device and purification method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104988343A (en) * 2015-08-12 2015-10-21 北京科技大学 Device and method for preparing light alloy semi-solid slurry through air-cooling multi-tube stirring
CN111172354A (en) * 2020-02-28 2020-05-19 鞍钢股份有限公司 Microbubble molten steel purification device and purification method
CN111172354B (en) * 2020-02-28 2021-11-12 鞍钢股份有限公司 Microbubble molten steel purification device and purification method

Also Published As

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