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JPH06240332A - Method for refining molten metal and bottom blowing tuyere for refining molten metal - Google Patents

Method for refining molten metal and bottom blowing tuyere for refining molten metal

Info

Publication number
JPH06240332A
JPH06240332A JP2829493A JP2829493A JPH06240332A JP H06240332 A JPH06240332 A JP H06240332A JP 2829493 A JP2829493 A JP 2829493A JP 2829493 A JP2829493 A JP 2829493A JP H06240332 A JPH06240332 A JP H06240332A
Authority
JP
Japan
Prior art keywords
molten metal
gas
refining
tuyere
bubbles
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.)
Withdrawn
Application number
JP2829493A
Other languages
Japanese (ja)
Inventor
Mitsutaka Matsuo
充高 松尾
Masataka Yano
正孝 矢野
Yuji Ogawa
雄司 小川
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 JP2829493A priority Critical patent/JPH06240332A/en
Publication of JPH06240332A publication Critical patent/JPH06240332A/en
Withdrawn legal-status Critical Current

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Abstract

(57)【要約】 【目的】 ガスと溶融金属間の界面で生じる反応を利用
して溶融金属の精錬を行う際に、反応速度を増大させて
精錬時間を短縮し、生産性を向上し得る金属の精錬方法
およびそのための底吹き羽口を提供する。 【構成】 溶融金属精錬容器において底吹きガスによる
攪拌を行いながら溶融金属を精錬する際に、ガス出口形
状が円環状で、円環の内径Rと円環の半径方向の幅rと
の比R/rが10以上である底吹き羽口により底吹きガ
ス攪拌を行うことを特徴とする。 【効果】 本発明によれば発生気泡が微細化され、ガス
−メタル間の反応界面積が増大し、かつ気泡の滞留時間
も増加するため、溶融金属の精錬を短時間で行うことが
できる。
(57) [Summary] [Purpose] When refining molten metal by utilizing the reaction occurring at the interface between gas and molten metal, the reaction rate can be increased to shorten refining time and improve productivity. Provided is a metal refining method and a bottom-blown tuyere therefor. When a molten metal is refined in a molten metal refining vessel while stirring with a bottom-blown gas, the shape of the gas outlet is annular and the ratio R of the inner diameter R of the annular ring and the radial width r of the annular ring is R. It is characterized in that the bottom-blowing gas is agitated by a bottom-blowing tuyere where / r is 10 or more. [Effects] According to the present invention, generated bubbles are miniaturized, the reaction interface area between the gas and the metal is increased, and the residence time of the bubbles is also increased, so that refining of molten metal can be performed in a short time.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は溶融金属の精錬方法及び
そのための底吹き羽口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 refining molten metal and a bottom blowing tuyere therefor.

【0002】[0002]

【従来の技術】溶融金属を気液反応を利用して精錬する
場合、例えば低炭素域における溶鋼の脱炭処理を行うよ
うな場合には、溶鋼中の炭素は溶鋼中の酸素と結びつ
き、COガスとなって気液界面から抜けていく。このよ
うな気液界面における反応を利用した精錬においては、
容器の底からガスを吹き込むなどして気液界面積を増大
させることで反応を促進し、処理時間を短縮することが
可能となる。
2. Description of the Related Art When refining molten metal by utilizing a gas-liquid reaction, for example, when decarburizing molten steel in a low carbon region, carbon in molten steel is combined with oxygen in molten steel and CO It becomes a gas and escapes from the gas-liquid interface. In refining utilizing the reaction at such a gas-liquid interface,
By blowing gas from the bottom of the container to increase the gas-liquid interface area, the reaction can be promoted and the processing time can be shortened.

【0003】従来、溶鋼にガスを吹き込む方法は、例え
ば特開平2−217412号公報あるいは特開平3−6
1316号公報に示されるように減圧・真空槽内の溶鋼
に不活性ガスを吹き込む方法が公知であり、脱炭速度の
向上にはそれなりの効果が期待できる。その時、ガスは
多孔質のプラグや円管ノズルから吹き込まれる。吹き込
みガス流量が等しい場合、吹き込まれた気泡径が小さけ
れば小さいほど気液反応界面積が増大し、精錬反応時間
が短縮できる。
Conventionally, a method of blowing gas into molten steel has been disclosed in, for example, Japanese Patent Laid-Open No. 2-217412 or Japanese Patent Laid-Open No. 3-6.
As disclosed in Japanese Patent No. 1316, a method is known in which an inert gas is blown into the molten steel in a decompression / vacuum tank, and a certain effect can be expected in improving the decarburization rate. At that time, the gas is blown from a porous plug or a circular tube nozzle. When the blowing gas flow rates are the same, the smaller the bubble diameter that is blown, the larger the gas-liquid reaction interfacial area and the shorter the refining reaction time.

【0004】気泡径は吹き込みノズル径に依存するた
め、気泡を小さくするためにはノズル径を極力小さくす
る必要があるが、その場合ノズル1本当たりの吹き込み
流量が制限されるため、同じ流量を確保するためには多
数のノズルを必要とする。そのような底吹き羽口とし
て、細管を集合したCB羽口が知られているが、この場
合ノズル間の距離が短く、気泡が合体してしまい、小さ
な気泡は生成されない。気泡が合体しないようなノズル
間距離を確保するためには、1本の細管ノズルを有した
羽口を多数精錬容器に設置しなければならず、羽口れん
がや羽口スリーブれんが等のコストが増大する。また、
多孔質のプラグを用いた場合も、一つ一つの気孔は小さ
くてもやはり気孔間の距離が極めて小さく、また溶融金
属とプラグの濡れ性が悪いため、ガスはプラグ表面に広
がって気泡の合体が生じ、やはり小さな気泡は生成され
ない。
Since the bubble diameter depends on the blowing nozzle diameter, it is necessary to make the nozzle diameter as small as possible in order to make the bubbles small. In that case, however, the blowing flow rate per nozzle is limited, so that the same flow rate is maintained. A large number of nozzles are required to secure it. As such a bottom blowing tuyere, a CB tuyere in which thin tubes are gathered is known, but in this case, the distance between the nozzles is short and the air bubbles coalesce, so that small air bubbles are not generated. In order to secure a distance between nozzles that prevents bubbles from merging, a large number of tuyere with one thin tube nozzle must be installed in the refining container, and the cost of tuyere brick, tuyere sleeve brick, etc. Increase. Also,
Even when using a porous plug, even if each pore is small, the distance between the pores is still extremely small, and the wettability between the molten metal and the plug is poor, so the gas spreads on the plug surface and coalesces bubbles. And still small bubbles are not generated.

【0005】[0005]

【発明が解決しようとする課題】本発明は、ガスを吹き
込みながら溶融金属を精錬する際に、小さな気泡を生成
させることでガス−メタル界面積を増大させ、精錬反応
速度を促進し、処理時間を短縮する溶融金属の精錬方法
及びそのための底吹き羽口を提供することを目的とす
る。
DISCLOSURE OF THE INVENTION According to the present invention, when refining a molten metal while blowing gas, small bubbles are generated to increase the gas-metal interface area, accelerate the refining reaction rate, and increase the treatment time. It is an object of the present invention to provide a method for refining molten metal for shortening the temperature and a bottom-blown tuyere therefor.

【0006】[0006]

【課題を解決するための手段】本発明の要旨とするとこ
ろは下記のとおりである。 (1) 溶融金属精錬容器において底吹きガスによる攪
拌を行いながら溶融金属を精錬する際に、ガス出口形状
が円環状で、円環の内径Rと円環の半径方向の幅rとの
比R/rが10以上である底吹き羽口により底吹きガス
攪拌を行うことを特徴とする溶融金属の精錬方法。
The subject matter of the present invention is as follows. (1) When refining molten metal while stirring with a bottom-blown gas in a molten metal refining vessel, the gas outlet shape is annular, and the ratio R of the inner diameter R of the annular ring and the radial width r of the annular ring A method for refining molten metal, characterized in that bottom blowing gas stirring is performed by a bottom blowing tuyere having an / r of 10 or more.

【0007】(2) ガス出口形状が円環状で、円環の
内径Rと円環の半径方向の幅rとの比R/rが10以上
である溶融金属精錬用底吹き羽口。本発明の特徴とする
ところは、底吹き羽口のガス出口形状を円環状とし、か
つ円環の内径Rと円環の半径方向の幅rとの比R/rを
前記の如く規定することで、ノズル1本当たりのガス流
量を減少させることなく生成気泡径を小さくし、ガス−
メタル界面積を増大させ、気液界面で生じる反応を従来
よりも速やかに進ませることを可能とした点にある。
(2) A bottom blowing tuyere for molten metal refining in which the gas outlet shape is an annular shape and the ratio R / r of the inner diameter R of the annular ring and the radial width r of the annular ring is 10 or more. The feature of the present invention resides in that the gas outlet shape of the bottom blown tuyere is annular and the ratio R / r of the inner diameter R of the annular ring and the radial width r of the annular ring is defined as described above. Thus, the diameter of generated bubbles can be reduced without decreasing the gas flow rate per nozzle,
This is because the metal interfacial area is increased and the reaction occurring at the gas-liquid interface can be made to proceed faster than before.

【0008】[0008]

【作用】本発明の作用を図1、2、3に従って説明す
る。図1は羽口の形状を示した図、図2はその羽口を用
いて溶鋼の低炭素域での脱炭を実施した例の説明図、図
3は図2A部の拡大図である。図1のように、羽口れん
が1内部に円筒状のノズル2を用いることにより、ガス
の出口形状を円環状とする。この羽口を図2のように溶
融金属5の精錬容器4の底部に設置して、Arガスを吹
き込むと、気泡3は図3に示すようにノズル出口の円環
の幅に規定されて溶融金属中に吹き込まれる。従って、
同一ノズル出口の面積を持つ単管ノズルに比べ、同一ガ
ス量では発生する気泡は非常に小さくなる。ただし、円
環の内径Rと円環の半径方向の幅rとの比R/rが10
未満になると、図4に示すように気泡は円環出口直上で
合体し、気泡の微細化の効果は減少する。溶融金属中に
吹き込まれたAr気泡の表面で溶鋼中の炭素と酸素が反
応し、COガスとなって脱炭反応が進行するが、Ar気
泡が小さいほど反応界面積が増大する。また気泡が小さ
いほど気泡の浮上速度も小さくなるため、気泡の溶鋼滞
留時間も増加する。以上2つの理由から、吹き込みガス
流量が等しい場合は、気泡が小さいほどトータルの脱炭
反応速度が増大する。
The operation of the present invention will be described with reference to FIGS. FIG. 1 is a diagram showing the shape of tuyere, FIG. 2 is an explanatory view of an example of decarburization of molten steel in the low carbon region using the tuyere, and FIG. 3 is an enlarged view of a portion of FIG. 2A. As shown in FIG. 1, by using a cylindrical nozzle 2 inside a tuyere brick 1, the shape of the gas outlet is annular. When this tuyere is installed at the bottom of the refining vessel 4 for the molten metal 5 as shown in FIG. 2 and Ar gas is blown into it, the bubbles 3 are melted by being defined by the width of the ring at the nozzle outlet as shown in FIG. It is blown into metal. Therefore,
Compared to a single pipe nozzle having the same nozzle outlet area, the bubbles generated at the same gas amount are much smaller. However, the ratio R / r of the inner diameter R of the annulus and the radial width r of the annulus is 10
When it is less than the above, the bubbles coalesce immediately above the annular exit, as shown in FIG. 4, and the effect of making the bubbles finer decreases. Carbon and oxygen in the molten steel react with each other on the surface of the Ar bubbles blown into the molten metal to form CO gas and the decarburization reaction proceeds, but the reaction interface area increases as the Ar bubbles become smaller. Further, as the bubbles are smaller, the floating speed of the bubbles is also reduced, so that the molten steel residence time of the bubbles is increased. For the above two reasons, the total decarburization reaction rate increases as the bubbles become smaller when the blowing gas flow rates are the same.

【0009】以上の理由により、従来よりも短い処理時
間で、ガス−メタル間の界面で生じる反応を利用した溶
融金属の精錬を行うことが可能となる。
For the above reasons, it becomes possible to carry out the refining of the molten metal by utilizing the reaction occurring at the interface between the gas and the metal in a shorter processing time than before.

【0010】[0010]

【実施例】内径1.1mの底吹き攪拌機能を有する円筒
型の精錬容器を用いて、低炭素溶鋼の脱炭実験を行っ
た。羽口のノズル環状部は、円環の内径30mm、円環
の半径方向の幅1mmとした。実験は、C濃度を290
〜310ppmに調整した溶鋼を用いて行った。溶鋼重
量は6t、Arガス吹き込み量は150Nl/min、
精錬時間は10分間とした。精錬開始後、2分おきに金
属サンプルを採取してC分析を行った。図5に、本実験
中の溶鋼中のC濃度の経時変化を示す。比較として、ノ
ズル出口断面積がほぼ等しい内径8mmの円管ノズルを
有する羽口を使用した場合のC濃度の経時変化を併せて
図5に示す。本発明による精錬方法の場合の方が、一定
のC濃度に到達する時間が短いことが確認できた。
EXAMPLE A decarburization experiment of low carbon molten steel was conducted using a cylindrical refining vessel having an inner diameter of 1.1 m and having a bottom blowing stirring function. The nozzle annular part of the tuyere had an inner diameter of 30 mm and a radial width of 1 mm. In the experiment, the C concentration was 290
It carried out using the molten steel adjusted to -310 ppm. Molten steel weight is 6 t, Ar gas blowing amount is 150 Nl / min,
The refining time was 10 minutes. After the start of refining, a metal sample was taken every 2 minutes and C analysis was performed. FIG. 5 shows the change with time of the C concentration in the molten steel during this experiment. As a comparison, FIG. 5 also shows changes over time in the C concentration when a tuyere having a circular tube nozzle with an inner diameter of 8 mm having substantially the same nozzle outlet cross-sectional area is used. It was confirmed that the refining method according to the present invention took less time to reach a certain C concentration.

【0011】また、ノズル出口の断面積を一定として、
R/rを5、10、15、30とした場合の、上記と同
一実験条件での10分後のC濃度を図6に示す。R/r
を10以上にすることにより、いずれも低いC濃度が得
られていることが確認できた。
Further, the cross-sectional area of the nozzle outlet is constant,
FIG. 6 shows the C concentration after 10 minutes under the same experimental conditions as above when R / r was set to 5, 10, 15, and 30. R / r
It was confirmed that by setting 10 to 10 or more, a low C concentration was obtained in each case.

【0012】[0012]

【発明の効果】本発明によって、ガス−メタル間の界面
で生じる反応を利用した精錬の時間を短くでき、生産性
を向上することができる。
According to the present invention, the refining time utilizing the reaction occurring at the gas-metal interface can be shortened and the productivity can be improved.

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

【図1】ノズル出口形状を円環状とした羽口の透視図で
ある。
FIG. 1 is a perspective view of a tuyere in which a nozzle outlet shape is annular.

【図2】底からArガスを吹き込んで溶鋼の脱炭を行う
精錬容器に本発明を適用した例の説明図である。
FIG. 2 is an explanatory view of an example in which the present invention is applied to a refining vessel for decarburizing molten steel by blowing Ar gas from the bottom.

【図3】図2のA部拡大説明図である。FIG. 3 is an enlarged explanatory view of a portion A of FIG.

【図4】R/rが10未満のノズルを用いてArガスを
吹き込んだ場合の気泡の挙動を示す図である。
FIG. 4 is a diagram showing the behavior of bubbles when Ar gas is blown in using a nozzle having an R / r of less than 10.

【図5】脱炭実験時の溶鋼中のC濃度変化を示すグラフ
である。
FIG. 5 is a graph showing changes in C concentration in molten steel during a decarburization experiment.

【図6】R/rが変化した時の、脱炭実験時の到達C濃
度を示す図である。
FIG. 6 is a diagram showing the ultimate C concentration during a decarburization experiment when R / r was changed.

【符号の説明】[Explanation of symbols]

1:羽口れんが 2:円環状ノズル 3:気泡 4:精錬容器 5:溶融金属 1: Tuyere brick 2: Annular nozzle 3: Bubbles 4: Refining vessel 5: Molten metal

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 溶融金属精錬容器において底吹きガスに
よる攪拌を行いながら溶融金属を精錬する際に、ガス出
口形状が円環状で、円環の内径Rと円環の半径方向の幅
rとの比R/rが10以上である底吹き羽口により底吹
きガス攪拌を行うことを特徴とする溶融金属の精錬方
法。
1. When refining a molten metal in a molten metal refining vessel while stirring with a bottom-blown gas, the gas outlet shape is annular, and the inner diameter R of the annular ring and the radial width r of the annular ring A method for refining molten metal, characterized in that bottom-blowing gas stirring is performed by a bottom-blowing tuyere having a ratio R / r of 10 or more.
【請求項2】 ガス出口形状が円環状で、円環の内径R
と円環の半径方向の幅rとの比R/rが10以上である
溶融金属精錬用底吹き羽口。
2. The gas outlet shape is an annular shape, and the inner diameter R of the annular shape.
Bottom blown tuyere for molten metal refining, wherein the ratio R / r between the radial width r of the ring and the radial width r is 10 or more.
JP2829493A 1993-02-17 1993-02-17 Method for refining molten metal and bottom blowing tuyere for refining molten metal Withdrawn JPH06240332A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2829493A JPH06240332A (en) 1993-02-17 1993-02-17 Method for refining molten metal and bottom blowing tuyere for refining molten metal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2829493A JPH06240332A (en) 1993-02-17 1993-02-17 Method for refining molten metal and bottom blowing tuyere for refining molten metal

Publications (1)

Publication Number Publication Date
JPH06240332A true JPH06240332A (en) 1994-08-30

Family

ID=12244605

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2829493A Withdrawn JPH06240332A (en) 1993-02-17 1993-02-17 Method for refining molten metal and bottom blowing tuyere for refining molten metal

Country Status (1)

Country Link
JP (1) JPH06240332A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006283066A (en) * 2005-03-31 2006-10-19 Jfe Steel Kk Gas-blowing tuyere
JP2011026709A (en) * 2010-09-28 2011-02-10 Jfe Steel Corp Gas-blowing tuyere

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006283066A (en) * 2005-03-31 2006-10-19 Jfe Steel Kk Gas-blowing tuyere
JP2011026709A (en) * 2010-09-28 2011-02-10 Jfe Steel Corp Gas-blowing tuyere

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