JPS6187809A - Treatment of molten metal - Google Patents
Treatment of molten metalInfo
- Publication number
- JPS6187809A JPS6187809A JP20079784A JP20079784A JPS6187809A JP S6187809 A JPS6187809 A JP S6187809A JP 20079784 A JP20079784 A JP 20079784A JP 20079784 A JP20079784 A JP 20079784A JP S6187809 A JPS6187809 A JP S6187809A
- Authority
- JP
- Japan
- Prior art keywords
- molten metal
- gas
- blowing
- blown
- vessel
- 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.)
- Pending
Links
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- Treatment Of Steel In Its Molten State (AREA)
- Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は金属溶湯の処理方法に関し、殊に溶銑や溶鋼を
ガスインジェクション法或は(ガス+粉体)インジェク
ション法等によって処理する場合に適用されるガスの吹
込制御方法に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for treating molten metal, and is particularly applicable to treating molten pig iron or molten steel by a gas injection method or (gas + powder) injection method. This invention relates to a gas blowing control method.
溶銑の脱珪、脱硫、脱燐等を行なう場合、脱珪剤、脱硫
剤、脱燐剤等を溶銑と十分接触させて処理効率を向上さ
せる目的で溶銑をガスバブリング法によって撹拌したり
、或は脱珪剤等をキャリヤガスと共に溶銑内へ吹込むこ
とがある。また精輝処理後の溶鋼温度を高めて以後の溶
鋼取扱いを円滑にする目的で、溶鋼中に粉炭と酸素を吹
込む方法も知られている。第1図はこの様な場合のガス
吹込状況を示す概略縦断面図であり、開放容器(取鍋等
)l内の金属溶湯Mに吹込みランス2を突込み、該ラン
ス2の先端部に設けたノズルから金属溶渇へf内へガス
Gを吹込む。吹込まれたガスGは金属溶湯M中を上昇し
て湯面りから大気中へ逸散して行くが、該ガスGの上昇
流によって局面は局部的にかなり隆起する。この隆起高
さHはガスの吹込み速度やランス2の浸漬深さ或は金属
溶湯Mの密度等によって変わるが、該隆起部の頂点が開
放容器1の開口上端ライン1hよりも上方になる様なこ
とがあると金属溶湯λ1が容器1り)へあふれる恐れが
生じてくる1、そこで従来は該隆起部の頂点が開口上端
ライン1hよりも上方に来ることがない様に、湯面りと
開口上端ライン1hの間に特定長さ以上の間隔(フリー
ボード)ができる様、容器lへの溶湯装入量を調整して
いる。When performing desiliconization, desulfurization, dephosphorization, etc. of hot metal, the hot metal is stirred by a gas bubbling method or In some cases, a desiliconizing agent or the like is blown into the hot metal together with a carrier gas. Also known is a method in which powdered coal and oxygen are injected into molten steel for the purpose of increasing the temperature of the molten steel after polishing treatment to facilitate subsequent handling of the molten steel. FIG. 1 is a schematic vertical cross-sectional view showing the gas blowing situation in such a case, in which a blowing lance 2 is plunged into the molten metal M in an open container (such as a ladle), and a blowing lance 2 is installed at the tip of the lance 2. Gas G is blown from the nozzle into the metal melt into f. The injected gas G rises in the molten metal M and dissipates from the surface of the metal into the atmosphere, but the upward flow of the gas G causes the surface to locally rise significantly. The height H of this protrusion varies depending on the gas blowing speed, the immersion depth of the lance 2, the density of the molten metal M, etc., but the peak of the protrusion should be above the opening top line 1h of the open container 1. If this happens, there is a risk that the molten metal λ1 will overflow into the container (1). Therefore, in the past, the surface of the molten metal was adjusted so that the top of the protrusion did not come above the opening upper line 1h. The amount of molten metal charged into the container l is adjusted so that there is a gap (free board) of a certain length or more between the opening upper end lines 1h.
ところで場面の前記隆起高さは前述の如くガスの吹込み
速度やランスの浸漬深さ等によって相当変わってくるが
、これまではこの隆起高さを正確に予測することができ
ず、経験的な「感」を頼りに前記フリーボードを調整し
ていた為、時としては局面の隆起高さが前記フリーボー
ドを上回り湯こぼれの危険に曝らされることがあった。By the way, as mentioned above, the height of the bulge in the scene varies considerably depending on the gas injection speed, the immersion depth of the lance, etc., but until now it has not been possible to accurately predict the bulge height, and empirical Since the free board was adjusted based on "feel", the height of the protrusion of the curve sometimes exceeded the free board, exposing the player to the risk of hot water spilling.
本発明はこうした問題を解消しようとするものであり、
ガス吹込み時の諸条件から湯面隆起高さを算出し、該隆
起高さが前記フリーボードを上回ることのない様に制御
できる方式を確立しようとするものである。The present invention aims to solve these problems,
The objective is to establish a method that calculates the height of the rise of the hot water surface from various conditions during gas injection and controls the rise height so that it does not exceed the freeboard.
本発明は、開放容器内の金属溶湯にガスを吹込んで処理
する方法において、容器の開口上端縁から局面までの深
さく即ち前記フリーボード:y)が下記CI)及びCI
Dの関係式を満足する様に金属溶湯装入量、吹込みガス
流量、吹込みガス温度及び湯面から見たガス吹込み深さ
を調整するところに要旨がある。The present invention provides a method for treating molten metal in an open container by blowing gas into it, in which the depth from the upper edge of the opening of the container to the curved surface, that is, the freeboard: y) shown below is CI) and CI
The key point is to adjust the amount of molten metal charged, the flow rate of blown gas, the blown gas temperature, and the depth of gas blown as seen from the molten metal surface so as to satisfy the relational expression D.
y≧as、9tx;0°692 ・・・(T’l)
Q :ガス流量(l!/分)
T、:溶湯温度(・K)
Ml:溶湯装入量(トン)
ρI!:溶島密度(y/ cm3)
Z :局面から見たガス吹込み汗さくcm)T8:吹込
みガス温度(・K)
〔作用〕
本発明者等が拙々研究を行なったところによると、金属
溶湯の湯面隆起高さは、吹込ガスめ流量、溶湯温度、溶
湯装入量、溶湯密度、湯面から見たガス吹込み深さ及び
吹込みガス温度を基に前記〔■〕式によって求めること
のできる撹拌動力値(:)と密接な関係を有しており、
この値が一定レベル以下となる様にガス吹込みの諸条件
及び処理容器の容量等を調整してやれば、湯面の隆起高
さを前記フリーボード以下に確実に抑制し得ることが確
認された。即ち第2因は、溶鋼及び溶銑を対象とする多
数のガス吹込み実酷により得た結采から、撹拌動力値(
:)と場面隆起高さく口)の関係を整理してグラフ化し
たものであり、両者の間には図示した如く一定の相関々
係がありその関係は下記[111)式の通りとなる。y≧as, 9tx; 0°692...(T'l)
Q: Gas flow rate (l!/min) T: Molten metal temperature (・K) Ml: Molten metal charging amount (tons) ρI! : Density of melted island (y/cm3) Z: Gas blowing temperature from the surface (cm) T8: Blowing gas temperature (・K) [Effect] According to the research carried out by the present inventors, The height of the molten metal surface elevation is determined by the formula [■] above, based on the blown gas flow rate, molten metal temperature, molten metal charge amount, molten metal density, gas injection depth as seen from the molten metal surface, and blown gas temperature. It has a close relationship with the stirring power value (:) that can be determined.
It has been confirmed that by adjusting the gas injection conditions and the capacity of the processing container so that this value is below a certain level, it is possible to reliably suppress the height of the rise of the hot water surface to below the above-mentioned freeboard. In other words, the second factor is that the stirring power value (
:) and the height of the scene elevation) are arranged and graphed, and there is a certain correlation between the two as shown in the figure, and the relationship is as shown in the following equation [111].
H=38.91Xε ・・・ClIDここで溶
湯のあふれ出しを防止する為には、前記フリーボード(
2)が場面隆起高さく)I)以上となる様に調整する必
要があるから、この要件を加えると下記〔■〕式、即ち
前記〔13式が導かれる。H=38.91Xε...ClIDHere, in order to prevent the molten metal from overflowing, the free board (
Since it is necessary to adjust so that 2) is equal to or higher than the scene elevation height (I), adding this requirement leads to the following formula [■], that is, the above-mentioned formula 13.
・0.692
y≧H−=−38,91Xε ・・・(ff’)即
ち所定の精錬効果を得る為に必要な諸条件が予め決めら
れている場合は、これらの条件から(II)式により撹
拌動力値を算出し、この値を前記〔19式に当てはめる
ことによって場面隆起高さく6)を算出し、該隆起高さ
αつ以上のフリーボード(y)が得られる様に処理容器
の容器又は溶湯装入量を決めればよく、一方処理容器の
容器が既に決められている場合は、溶湯装入量によって
決まるフリーボードωに応じてガス吹込み条件(吹込み
ガス流量、吹込みガス温度及びランスの局面下吹き込み
深さ等)を調整し、場面隆起高さ卸がフリーボードυ)
以下となる様に調整することにより、潟こぼれの危険を
なくすことができる。・0.692 y≧H-=-38,91Xε ...(ff') In other words, if the various conditions necessary to obtain the specified refining effect are determined in advance, formula (II) can be calculated from these conditions. Calculate the stirring power value, apply this value to the equation 19 above to calculate the scene elevation height 6), and adjust the processing vessel so that a free board (y) with the elevation height α or more is obtained. All you need to do is decide on the container or amount of molten metal to be charged.On the other hand, if the container for the processing container has already been determined, the gas injection conditions (injection gas flow rate, injection gas Adjust the temperature and the blowing depth of the lance, etc.), and set the height of the raised surface freeboard υ)
The risk of lagoon spillage can be eliminated by making the following adjustments.
第3.4図は、ガス吹込み条件のうち容易にコントロー
ルすることのできる吹込みガス流量(Q及びガス吹込口
の湯面から見た深さく即ち吹込みランスの浸漬深さ:Z
)が撹拌動力値に)に及ぼす影響を示したものであり、
他のガス吹込条件は下記第1表の通りとした。Figure 3.4 shows the gas blowing conditions that can be easily controlled: the blowing gas flow rate (Q) and the depth of the gas blowing port as seen from the hot water surface, i.e. the immersion depth of the blowing lance: Z.
) shows the influence of ) on the stirring power value.
Other gas injection conditions were as shown in Table 1 below.
第1表
、濃口 1928 ’ 7.2 、 298第3
.4図からも明らかな様に、吹込みガスの流会及びラン
ス浸漬深さと総撹拌動力値の間には一定の相関々係があ
るので、処理容器の容量及び溶湯装入nによって決まる
フリーボード0)に応じて上記ガス流nやランス浸漬深
さを変更して総撹拌動力値を調節することにより、潟面
隆起高さく6)がフリーボード(y)を上回ることがな
い様にコントロールすることができる。一方処理効率上
の要請から匝拌動力値が決められている場合は、該動力
値から必然的に決まってくる潟面隆起高さく6)に応じ
て、該隆起高さく9)を上回るフリーボードが得られる
様に処理容器の容量或は溶湯装入量を調整することによ
り、湯こぼれの危険を無くすことができる。Table 1, Koikuchi 1928' 7.2, 298 No. 3
.. As is clear from Figure 4, there is a certain correlation between the flow of the blown gas, the immersion depth of the lance, and the total stirring power value, so the free board is determined by the capacity of the processing vessel and the molten metal charging n. By adjusting the total stirring power value by changing the gas flow n and the lance immersion depth according to 0), the lagoon surface elevation height 6) is controlled so that it does not exceed the freeboard (y). be able to. On the other hand, if the stirring power value is determined from the requirements for processing efficiency, the free board that exceeds the lagoon height 9) according to the lagoon elevation height 6) that is inevitably determined from the power value. By adjusting the capacity of the processing container or the amount of molten metal charged so as to obtain the following, the risk of hot water spilling can be eliminated.
尚ガス吹込みランスのノズル径は撹拌動力値に無関係で
あるので、該ノズル径は主に「ノズルの閉塞防止」とい
う観点から決めればよい。即ちノズルの閉塞は、ノズル
内へ溶湯が侵入し凝固することによって発生するもので
、このノズル閉塞を防止する為には、浸漬ランスのノズ
ル囲口面にがかる溶湯の静圧よりも高い圧力でガスを吹
込めばよい。従って前述の様にして吹込みガスの流量が
決まれば、この流量と処理溶湯の密度及びランス浸漬深
さ等に応じて、ノズル開口面にかかる溶湯の静圧を上回
るガス吹込み圧が得られる様にノズルの開口面債を調整
すれば、溶湯侵入によるノズルの閉塞小数も防止するこ
とができる。向上記ではランスを用いてガスを吹込む場
合について説明したが、容器底部に設けた底吹きノズル
からガスを吹込む場合についても同様に適用することが
できる。Since the nozzle diameter of the gas blowing lance has no relation to the stirring power value, the nozzle diameter may be determined mainly from the viewpoint of "prevention of nozzle clogging." In other words, nozzle blockage occurs when the molten metal enters the nozzle and solidifies. In order to prevent this nozzle blockage, a pressure higher than the static pressure of the molten metal applied to the nozzle surrounding surface of the immersion lance is applied. Just blow in some gas. Therefore, if the flow rate of the blown gas is determined as described above, depending on this flow rate, the density of the molten metal to be treated, the immersion depth of the lance, etc., a gas blown pressure that exceeds the static pressure of the molten metal applied to the nozzle opening surface can be obtained. By adjusting the opening surface of the nozzle in this way, it is possible to prevent the nozzle from becoming clogged due to intrusion of molten metal. In the above description, the case where the gas is blown using a lance has been described, but the same can be applied to the case where the gas is blown from a bottom blowing nozzle provided at the bottom of the container.
本発明は以上の様に構成されるが、要はガス吹込みによ
って生じる潟面隆起高さを吹込み条件に応じて理論的且
つ正確に予知することができる他、吹込み条件を変える
ことによって揚面隆起高さを調整することができ、ひい
ては処理容器のフリーボードを超えない様に処理条件を
コントロールすることができるので、湯面隆起に起因す
るのとぼれ串故を無くすことができる。The present invention is constructed as described above, but the point is that the height of the lagoon surface elevation caused by gas injection can be predicted theoretically and accurately according to the injection conditions, and also by changing the injection conditions. Since the height of the raised surface can be adjusted and the processing conditions can be controlled so that it does not exceed the freeboard of the processing vessel, it is possible to eliminate spillage caused by the raised surface of the hot water.
第1図は、金属溶湯のガス吹込み処理状況を示す概略断
面図、第2図は撹拌島力値と溶渇隆起高さの関係を示す
グラフ、第3.4図はガス流量及びランス突込み深さが
総撹拌動力値に与える影響を示すグラフである。
l・・・処理容器、 2・・・ランス、SL・・
溶面。
出 願人 株式会社神戸製41所
代理人弁理士植木久、1<云ヒ\
第3図
ガス流量(Nm /Hr )
第4図
タンス突込み深さく朋)
手糸完7市正書 (自発)
昭和60年8月38
1、事件の表示
昭和59年特許願第200797号
2、発明の名称
金属溶湯の処理方法
3、補正をする者
事件との関係 特許出願人
神戸市中央区脇浜町−丁目3番18号
(J19)株式会社 神戸製鋼所
代表者 牧 冬 彦
4、代理人〒530
大阪市北区堂島2丁目3番7号
シンコービル
明細書の「特許請求の範囲」、「発明の詳細な説明」及
び「図面の簡単な説明」の各欄並特許請求の範囲
(1)「特許請求の範囲」を別紙の通り訂正します。
(2)明細書第4頁第15行
誤: X (I n (1+O,0O09138正:
×(見n (1+0.0O09BB(3)同第4頁最下
行
誤: 溶湯装入量
正: 溶湯重量
(4)同第5頁第7行
誤: 溶湯装入量
正: 溶湯装入量(重量)
(5)同第9頁第15行
誤: ランス突込み深さ
正: ガス吹込み深さ
く6)図面中、第3図及び第4図を添付の第3図及び第
4図と差し待えます。
開放容器内の金属溶湯にガスを吹込んで処理するに当た
り、容器の開口上端縁から静止湯面までの距fffl(
y)が下記関係式を満足する様に金属溶湯装入−祉、吹
込みガス流量、吹込みガス温度及び湯面から見たガス吹
込み深さを調整することを特徴とする金属溶湯の処理方
法。
y≧38.91 X ;0692
Q :ガス流量CfL1分)
1文:溶湯温度(0K)
M文:溶湯重量(トン)
ρ!l:溶湯密度(g/cm3)
Z :@面からみたガス吹込み深さくcm )Tg:吹
込みガス温度(0K)
Oto 20 30 40 50 60
70 80ガヌ流ユ(Nm”/Hr )Figure 1 is a schematic cross-sectional view showing the gas injection treatment status of molten metal, Figure 2 is a graph showing the relationship between the stirring island force value and the height of the molten bulge, and Figure 3.4 is the gas flow rate and lance thrust. It is a graph showing the influence that depth has on the total stirring power value. l...processing container, 2...lance, SL...
Molten surface. Applicant: Hisashi Ueki, Patent Attorney, Kobe Seisaku Co., Ltd. 41, 1<Yuuhi\ Figure 3: Gas flow rate (Nm/Hr) Figure 4: Depth of drawer plunger) (Volunteer) August 38, 1985 1. Indication of the case 1988 Patent Application No. 200797 2. Name of the invention Method for processing molten metal 3. Person making the amendment Relationship to the case Patent applicant Wakihama-cho-chome, Chuo-ku, Kobe City No. 3-18 (J19) Kobe Steel, Ltd. Representative: Fuyuhiko Maki 4, Agent: Shinko Building, 2-3-7 Dojima, Kita-ku, Osaka 530 "Claims" and "Details of the Invention" The columns of ``Brief Description of Drawings'' and ``Brief Description of Drawings'' as well as Claims (1) ``Claims'' will be corrected as shown in the attached sheet. (2) Error in page 4, line 15 of specification: X (I n (1+O, 0O09138 correct:
×(Seen (1+0.0O09BB(3) Error in the bottom line of page 4 of the same page: Molten metal charge amount is correct: Molten metal weight (4) Error in line 7 of page 5 of the same page: Molten metal charge amount is correct: Molten metal charge amount ( Weight) (5) Wrong line 15 on page 9: Lance thrust depth correct: Gas injection depth 6) In the drawings, Figures 3 and 4 are interpolated with the attached Figures 3 and 4. When treating molten metal in an open container by blowing gas into it, the distance fffl (
Processing of molten metal characterized by adjusting the molten metal charging, the blown gas flow rate, the blown gas temperature, and the gas blown depth as seen from the molten metal surface so that y) satisfies the following relational expression. Method. y≧38.91 l: Molten metal density (g/cm3) Z: Gas injection depth cm as seen from @ surface) Tg: Blowing gas temperature (0K) Oto 20 30 40 50 60
70 80 Ganu style Yu (Nm”/Hr)
Claims (1)
り、容器の開口上端縁から静止湯面までの距離(y)が
下記関係式を満足する様に金属溶湯装入量、吹込みガス
流量、吹込みガス温度及び湯面から見たガス吹込み深さ
を調整することを特徴とする金属溶湯の処理方法。 y≧38.91×■^0^.^6^9^2 ■=(0.0062・Q・T_l)/M_l×{In(
1+0.000968・ρ_l・Z)+(1−T_g/
T_l)} Q:ガス流量(l/分) T_l:溶湯温度(°K) M_l:溶湯装入量(トン) ρ_l:溶湯密度(g/cm^3) Z:湯面からみたガス吹込口深さ(cm) T_g:吹込みガス温度(°K)[Scope of Claims] When treating the molten metal in an open container by blowing gas into it, the amount of molten metal charged is determined such that the distance (y) from the upper edge of the opening of the container to the static molten metal level satisfies the following relational expression: A method for treating molten metal, characterized by adjusting the flow rate of the blown gas, the temperature of the blown gas, and the depth of the gas blown as seen from the surface of the molten metal. y≧38.91×■^0^. ^6^9^2 ■=(0.0062・Q・T_l)/M_l×{In(
1+0.000968・ρ_l・Z)+(1−T_g/
T_l)} Q: Gas flow rate (l/min) T_l: Molten metal temperature (°K) M_l: Molten metal charge amount (tons) ρ_l: Molten metal density (g/cm^3) Z: Depth of gas inlet seen from the molten metal surface (cm) T_g: Blowing gas temperature (°K)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20079784A JPS6187809A (en) | 1984-09-26 | 1984-09-26 | Treatment of molten metal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20079784A JPS6187809A (en) | 1984-09-26 | 1984-09-26 | Treatment of molten metal |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6187809A true JPS6187809A (en) | 1986-05-06 |
Family
ID=16430347
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20079784A Pending JPS6187809A (en) | 1984-09-26 | 1984-09-26 | Treatment of molten metal |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6187809A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2021070455A1 (en) * | 2020-05-29 | 2021-04-15 | ダイヤモンドエンジニアリング株式会社 | Mechanical stirring-type desulfurization system |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56150119A (en) * | 1980-04-19 | 1981-11-20 | Nippon Kokan Kk <Nkk> | Stirring method in refining molten iron in vessel |
JPS5943806A (en) * | 1982-09-03 | 1984-03-12 | Nippon Steel Corp | Blowing method of gas |
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1984
- 1984-09-26 JP JP20079784A patent/JPS6187809A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56150119A (en) * | 1980-04-19 | 1981-11-20 | Nippon Kokan Kk <Nkk> | Stirring method in refining molten iron in vessel |
JPS5943806A (en) * | 1982-09-03 | 1984-03-12 | Nippon Steel Corp | Blowing method of gas |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2021070455A1 (en) * | 2020-05-29 | 2021-04-15 | ダイヤモンドエンジニアリング株式会社 | Mechanical stirring-type desulfurization system |
TWI747779B (en) * | 2020-05-29 | 2021-11-21 | 日商鑽石工程股份有限公司 | Mechanical agitated desulfurization system |
JP2021188097A (en) * | 2020-05-29 | 2021-12-13 | ダイヤモンドエンジニアリング株式会社 | Mechanical stirring desulfurization system |
CN114096686A (en) * | 2020-05-29 | 2022-02-25 | 钻石工程株式会社 | Mechanical stirring type desulfurization system |
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