JPH0440103B2 - - Google Patents
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- JPH0440103B2 JPH0440103B2 JP17181588A JP17181588A JPH0440103B2 JP H0440103 B2 JPH0440103 B2 JP H0440103B2 JP 17181588 A JP17181588 A JP 17181588A JP 17181588 A JP17181588 A JP 17181588A JP H0440103 B2 JPH0440103 B2 JP H0440103B2
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Description
産業上の利用分野
本発明は鋼の連続鋳造に関するものである。
従来の技術
鋼の連続鋳造時には、鋳型内に湯面保護剤が添
加される。この湯面保護剤の役割りは、鋳型内
に添加することにより溶鋼表面を被覆保温し、溶
鋼面の凝固防止及び酸化防止を行うこと。溶鋼
中より浮上してくる非金属介在物を吸収して鋳片
を清浄化せしめ、製品の介在物性欠陥を防止する
こと。鋳型と凝固シエル間に均一に流入潤滑す
ることにより鋳型の冷却を均一化して、鋳片の表
面割れおよび拘束性ブレークアウトを防止するこ
とである。
以上の特性を確保するために、湯面保護剤は、
SiO2、Al2O3、CaO、Fe2O3、MgO等の酸化物を
母材とし、その他に物性調整剤としてアルカリ金
属及びアルカリ土類金属の酸化物、炭酸塩又は弗
化物更には、溶融速度調整剤としての炭素分を含
有している。炭素分としては、コークス、カーボ
ンブラツク、天然黒鉛、人造黒鉛、石炭等の粉末
又は顆粒が使用されている。
一般的な湯面保護剤の成分としては、SiO220
〜45wt%、CaO20〜45wt%、Al2O30.5〜10wt
%、MgO1〜20wt%、Na2O1〜20wt%、F-2〜
20wt%、C10wt%以下で構成されており必要に
応じLiO2やB2O3その他の金属酸化物、金属弗化
物、金属炭酸塩も使用されている。分析上弗化物
は、酸化物とF-に、炭酸塩は、酸化物とCとし
て表記されている。また物性としては、1300℃の
粘度で0.5〜15poise、融点で800〜1200℃のもの
が使用されている。
一方近年省エネルギーや省資源、歩留や原単位
の向上によるコストダウンの要請が一段と高まる
傾向にある。そのため高速連続鋳造化さらには、
高速連続鋳造で製造された高温の鋳片を冷却−再
加熱することなく直接圧延工程に送り込む直送圧
延(CC−DR)が積極的に採用されるようになつ
ている。
該直送圧延を実施するためには、高速連続鋳造
により製造される鋳片の欠陥(表面割れ、凝固過
程の溶鋼への湯面保護剤の捲き込みによる鋳片の
パウダー性欠陥等)を皆無にするか、直送圧延を
実施しても問題のない程度に極めて少なくし、鋳
片の欠陥に起因する製品の欠陥を防止しなければ
ならない。
しかしながら従来の鋳造速度で使用していた湯
面保護剤をそのまま高速連続鋳造に使用すると、
湯面保護剤の消費量が減少し、そのため鋳型−鋳
片間の潤滑不良を起こし、拘束性ブレークアウト
が発生し易くなる。その防止策として従来は、高
速鋳造化に伴い、湯面保護剤の粘度を1300℃で
0.5〜1.5poiseへの低粘度化することにより、湯面
保護剤の消費量を増加させて、潤滑性を保持させ
ていた。(特開昭61−150752号公報)。
発明が解決しようとする課題
しかしながら湯面保護剤を低粘度化すると、拘
束性ブレークアウトの防止効果はあるが、高速化
による鋳型内への激しい注入流により、溶融した
湯面保護剤が溶鋼流に巻き込まれて、鋳片のパウ
ダー性欠陥が大巾に上昇し、これにより製品の欠
陥が激増するため、高速鋳造化、さらには直送圧
延を実施する上で新たに大きな問題となつてい
る。
また中、低速鋳造においても、ブリキ材、自動
車用鋼板材(Ti−Sulc鋼)等の品質要求厳格材
では製品の品位を更に向上させるために、湯面保
護剤の捲き込みによる鋳片のパウダー性欠陥を皆
無にする必要がある。
本発明は、高速鋳造時において拘束性ブレーク
アウトの発生を完全に防止すると同時に、上記従
来技術における課題である湯面保護剤の捲き込み
による鋳片のパウダー性欠陥の増加を抑止して、
直送圧延を可能にするとともに、中、低速鋳造あ
るいは高速鋳造においてさえもパウダー性欠陥の
無い鋳片を得ることにより、更に品位の高い製品
を得ることが出来る新しい連続鋳造法を提供する
ものである。
課題を解決するための手段
本発明者等は、前述の鋳造時の欠点を解決する
ため、各種実験検討を重ねた結果特定鋳造条件下
において極めて高粘度域に優れた領域が存在する
ことを知見し得た。本発明はこれ等の知見に基づ
きなされたものでありその特徴とするところは、
鋳型の長片テーパー〔(鋳型の上端開口厚−鋳型
の下端開口厚)/鋳型の長片の高さ×100%〕を
0.1%以下の条件でスラブを連続鋳造するに際し
て、CaO、SiO2、Al2O3を主成分とし、CaO/
SiO2(重量%比)が0.5〜1.6の範囲で、アルカリ
金属およびアルカリ土類金属および他金属の酸化
物、炭酸塩、弗化物の1種以上と更に溶融速度調
整剤として炭素分を含有し、1250℃における表面
張力が290dyne/cm以上、ブレークポイントが
1000℃以下で、かつ1300℃における粘度η
(poise)が鋳造速度V(m/min)との関係式
6.0<ηV
の範囲を満足する湯面保護剤(パウダー)を使用
して、スラブを鋳造することを特徴とする鋼の連
続鋳造法である。
即ち本発明は新たに表面張力、ブレークポイン
トを物性値として導入した湯面保護剤の粘度を鋳
造速度に対し、前記範囲を特定するとともに、鋳
型の長片テーパーを0.1%以下の領域で鋳造する
ことにより1.5m/min以下の低中速の鋳造はも
とより、1.5m/min以上の高速鋳造においても
鋳型−鋳片間に十分に流入潤滑して拘束性ブレー
クアウトを防止し、かつ直送圧延が可能な極めて
鋳片欠陥の少ない鋳片を製造でき、かつ高級鋼に
おいては介在物の少い連続鋳造法を提供するもの
である。
作 用
前述の如く、湯面保護剤を用いた連続鋳造法で
は、鋳型内溶鋼流によつて湯面保護剤溶融層が溶
鋼中へ捲き込まれて凝固し介在物として鋳片に残
り品質を低下させることを防止し、併せて鋳型内
壁面との円滑な潤滑能を維持せしめることであ
る。
この捲き込みを防止し、しかも潤滑性を確保す
るため、種々検討を実施した。まず捲き込みの防
止に関しては、その発生原因が鋳造時の溶鋼流入
にもとづく溶鋼表面の乱れであるため湯面保護剤
の新たな物性として、表面張力に注目し、市販品
の表面張力を測定した。表面張力の測定は、第1
2図に示す白金円筒引上げ法(Dipping
Cylinder method)により測定した。
先ず600℃マツフル炉中で1時間の脱炭処理し
た湯面保護剤約60grを黒鉛ルツボに入れ1400℃
マツフル炉中で10分間溶融処理する。この溶融試
料を白金ルツボ3に入れ1250℃に保持し、Ar置
換した測定装置(第12図)の電気炉2に挿入し
た。
温度安定後上部天秤1と連結した白金円筒4を
溶融中に浸漬し、天秤をバランスさせる。次い
で、白金円筒4より、液面を低下させバランスが
平衝になるまで分銅を加える。白金円筒が液面か
ら離れるまでこの操作をくり返し離れる瞬間の最
大重量を記録する。
この測定を6回行い、最大値、最小値を除いた
平均値をとりWmax(g)とする。計算式は、
σ=g・Wman/4πR×V
で表わされる。ここでσは表面張力(dyne/
cm)、gは重力の加速度(980cm/sec2)、Wmax
は白金円筒に及ぼす最大の引き(gr)、Rはシリ
ンダーの半径(cm)、Vは補正係数であり、使用
シリンダー、融体液の密度により決まるものであ
る。
調査した従来品の表面張力の測定結果は240〜
290dyne/cmであつた。また、従来品の粘度は、
1300℃で0.6〜3.0poiseであり、粘度と表面張力の
間には、相関は認められなかつた。
次ぎに表面張力の水準を変更して鋳造試験を実
施し、鋳片の品質との関係を調査した。その結果
を第2図に示す。鋳造条件としては、スラブサイ
ズ1500×250mm、溶融成分C:0.04、Si:0.02、
Mn:0.24、P:0.02、S:0.01、Al:0.05(%)、
TD温度1560℃、鋳造速度1.5m/min、湯面保護
剤(主成分CaO:39.0%、Al2O3:2.0%、CaO:
36.0%、Na2O:14.0%、F-:6.0%)の粘度1300
℃1.6poiseで統一した。
第2図から明らかなように表面張力が高い程、
在物欠陥が減少する傾向がみられるが、表面張力
290dyne/cmを境として大巾な介在物の減少が見
られる。これは、鋳造条件による湯面の乱れ度に
対し、表面張力が高いということは溶融した湯面
保護剤の表面結合力が強いことを示しており、溶
鋼との接触で混合しにくく、まき込まれにくくな
り、結果として連続鋳造下においては、
290dyne/cm以上であれば捲き込み臨界条件外で
あることを新らたに見い出した。
しかしながら介在物欠陥の低減ははかれたが皆
無にする条件はみつからなかつた。そこで、潤滑
性(B.O発生率)を犠性にした設計に変更し、粘
度を1300℃で3.2poiseとし、再度前記操業条件に
て1.5m/minの鋳造試験を実施した。その結果
を第3図に示す。
第3図から明らかなように、粘性を高くするこ
とにより介在物の発生率は低減するが、表面張力
を290dyne/cm以上にすることにより鋳片の介在
物欠陥を皆無にできることが新たに判明した。し
かしながら粘性を上げたことにより、潤滑性は低
下し拘束性B.Oの発生率指数は高く、いずれも1
(第2図では、0.1)であり、十分な潤滑性を保証
するには致らなかつた。
そこで本発明者らは、この潤滑性を保証する手
段の調査・研究を実施した結果次の知見を得た。
すなわち、消費原単位と最も密接な関係を有する
物性は粘度であるといわれており、鋳造速度を上
昇させるに伴ない、湯面保護剤の粘度を低下させ
ることが従来の知見であつた。一般に粘度は、
1300℃での測定値が採用されているが、これは、
メニスカス直下の流入フイルムの平均温度が約
1300℃であるとのことと、測定値が比較的安定し
て得られるからである。
本発明者等は、ローター回転法により脱炭後の
各種湯面保護剤200grを1400℃、10分間溶融し、
1300℃に保持した後粘度測定を実施し、その後20
℃づつ温度を降下させて、各温度で保持後に粘度
測定を行つて1ogη−1/T(ηは粘度poise、T
は絶対温度〓を示す)グラフを作成した。
この測定時、温度降下により、試料中に結晶が
晶出し、ニユートン液体でなくなり、測定不能に
なつた温度から10℃高い温度をブレークポイント
と定義した。第4図にその測定例を示す。第4図
から明らかなように1300℃の粘度が同一であつて
も、ブレークポイントが大巾に異なる湯面保護剤
があることがわかつた。
そこでブレークポイントを変更したサンプルを
試作し、実機鋳造試験を実施し、ブレークアウト
発生率(以下B.O発生率という。)に及ぼす影響
を調査した。鋼種、鋳造速度は今までと同一にし
粘度は1300℃で3.2poiseとした。第5図に結果を
示す。
第5図から明らかなようにB.O発生率とブレー
クポイントに大きな相関がみられ、ブレークポイ
ントを低下させることにより、B.O発生率を低下
させることが可能であることを得、かつそのブレ
ークポイント温度を1000℃以下にすることによ
り、B.O発生率は皆無となることを新たに見い出
した。
これは第6図bのごとく、従来の湯面保護剤7
は、メニスカス部のみでの液体潤滑8でありその
他の下位部では、固体状態9になつており、1300
℃の粘性のみがパウダーの原単位つまり潤滑性を
支配していた。
また第6図aのごとく本発明湯面保護剤10の
ブレークポイントが1000℃以下ということは、一
般にモールド下端の鋳片表面は1000℃といわれて
おり、このため、モールド下端においても溶融し
た湯面保護剤は液体として存在し、モールド全面
(モールド内鋳片表面全面)において液体潤滑1
1となつており従来と異なり理想の潤滑状態を示
す。
この結果拘束性ブレークアウトの発生率が皆無
になつた。
更に鋳型のある特性条件、つまり長辺の鋳型テ
ーパーを規制することにより、鋳型内壁面と凝固
シエル表面間の全面が湯面保護剤の液体潤滑する
と共に、テーパーが小さければ、同じブレークポ
イント及び表面張力であつても高粘度の湯面保護
が使用可能となり良好な鋳片が得られた。
この知見に基づいてテストを行つた。つまり鋳
型長片テーパーを種々に変動させ最適原単位
(Kg/Ton Steel)と品質、操業性を調査した。
このときの湯面保護剤の特性及び操業条件は今ま
でと同一である。第7図に結果を示す。
第7図から明らかなように、長片の鋳型テーパ
ーと湯面保護剤の原単位とは大きな関係が見い出
され、その関係は、長片のテーパー0.1%を境に
明らかな差があることを見い出した。
この理由は、0.1%より大であると鋳型内にて、
鋳片のバルジングが大となり、流入が阻害される
が、0.1%以下であれば、下端への鋳型の開きが
大であり、流れ込み量が急激に大きくなる。
同様に0.1%より大の条件で低粘土を使用する
と、原単位は正常値となるが、前述のごとく鋳片
への巻き込み量が大で品質が劣化する。又高粘度
を使用すると、品質は良好であるが原単位が少な
くなり、鋳造トラブル(鋳型損耗量大による表面
疵)が大となる。
ブレークアウト発生率が皆無で、かつ鋳片品質
も良好であるとしても湯面保護剤の原単位が多い
と、鋳片鋳造のコストがアツプすると共に、スラ
グフイルムの鋳片への付着量が多くなり、鋳片の
圧延時に剥離が悪く圧延疵が増大する。また原単
位が少なくなると、鋳型の内面の損耗量が大とな
り、結果として表面疵発生が大となるか又は、鋳
型の手入れ率が非常に高くなる。つまり最適の原
単位が存在する。
これ等の関係を第8(操業条件は第7図と同
様)、9,10図に示す。これ等により最適原単
位は0.20〜0.6Kg/Ton Steelであることを見い出
した。
次に最適粘度範囲を求めるため、表面張力を
1250℃で290dyne/cm以上、ブレークポイントを
1000℃以下の範囲で粘度を変化させた湯面保護剤
を試作し、鋳型の長片テーパーを0.1%以下とし、
種々の鋳造速度の組合せで実機鋳造し、鋳片品質
をチエツクした。
その結果を第1図に示す。○印は、総合評価で
合格のもの(本発明実施例)、×印は不合格のもの
(比較品)を示す。第1図から鋳造速度に対し、
適正粘度範囲が存在する。ここで本発明において
用いた鋳型の長片テーパーとは、第13図のごと
く
上端開口厚B−下端開口厚C/長片の高さA×100
%
と定義したものである。
湯面保護剤中の炭素は、添加時に、溶鋼温度に
より加熱燃焼しながら湯面保護剤の溶融速度を調
整するものであり、その含有量の大小により溶融
速度を左右する。つまり、含有量が多いと、溶融
速度は遅くなり、鋳造操業に適した含有量が必要
である。すなわち鋳造速度Vに対し、1300℃の粘
度ηを、
6.0<ηV
の範囲で設計すること、好ましくは、ηVは20以
下が望ましい。これはあまり高過ぎると、原単位
が低下するおそれがあるからである。
更に第11図に示すごとく、第2図の高表面張
力による在物による鋳片欠陥指数(湯面保護剤の
まき込み)低下のみならず、一般の表面張力でも
低ブレークポイント化することにより鋳片内の介
在物による欠陥指数が低下し、第11図に示すよ
うに、高表面張力、低ブレークポイント化するこ
とにより、この組合せで著るしい効果を見いだす
ことができた。
このように、表面張力が高く(290dyne/cm以
上)かつ低ブレークポイント(1000℃以下)にす
ることにより著るしく在物の発生を低減すること
ができた。これ等の条件にて鋳造欠陥のない良鋳
片を製造できることを見い出したのである。
以上の結果により本発明の範囲限定理由をまと
めると次の如くとなる。
使用する湯面保護剤の成分系は一般に使用され
ている湯面保護剤の組成でよく、特許請求の範囲
である表面張力290dyne/cm以上、ブレークポイ
ント1000℃以下の物性で、CaO/SiO2(wt%比)
のみ0.5〜1.6に限定する。それは、CaO/SiO2<
0.5の場合は、物性特に粘度を調整するため多量
のフラツクス成分(Na2O、Li2O、F-等)を必要
とするため、浸漬ノズル溶損量が大きくなり、か
つコスト高となり実用的でなく、またCaO/
SiO2>1.6の場合は、鋳型内での変性(Al2O3介在
物吸収、鋼中のAlによる溶融した湯面保護剤中
のSiO2の還元)により流入潤滑時にガラス性が
なくなつて、再結晶を起こす。
ブレークポイントが1000℃以下ということは、
低温でもガラス性を保持することを意味し、イオ
ン結晶的には、SiO2の連結は、塊状の集団では
なく、直線的な構造として結晶を起しにくくした
ものである。結晶が発生すると鋳片の抜熱が不均
一となり、表面欠陥の発生や潤滑不良によるブレ
ークアウトが発生し易くなるのでCaO/SiO2=
0.5〜1.6の範囲とした。
表面張力を1250℃で290dyne/cm以上とする理
由は、前述のごとく290dyne/cm以下であると湯
面保護剤の溶融層が溶鋼流に捲き込まれ易くな
り、介在物欠陥の原因となるため表面張力は1250
℃で290dyne/cm以上にする必要がある。
ブレークポイント1000℃以下の理由は前述の如
く比較的高粘度でB.O発生率を皆無とすることが
可能であり、1000℃以上では、前述のごとくモー
ルド内にて固体の湯面保護剤が存在し、鋳型と鋳
片の間隙において潤滑不良を起こし、ブレークア
ウトが発生し易くなるので1000℃以下にする必要
がある。
1300℃の粘度ηを鋳造速度Vに対し
6.0<ηV
に限定する理由は、ηV≦6では、長片テーパー
0.1%以下の条件で鋳造速度に対し、粘度が低す
ぎて鋳型内のスラグフイルムの液体が自由に流下
し、結果として原単位が多すぎて、それに伴う欠
陥すなわち圧延疵及び問題点(コストアツプ)が
発生し易くなるためであり、鋳型テーパーが0.1
以上では、原単位の低下にともなう表面疵の発生
が大となる。ηV>6.0においてテーパーが0.1以上
では上記同様表面疵が激増する。
この理由は前述したごとく、湯面保護剤の特
性、ブレークポイント1000℃以下及び表面張力
290dyne/cm以上の場合、鋳型内で液体潤滑とな
り、品質が良好な鋳片を得ることができるが、更
に鋳型テーパーを規制することにより、高粘度域
の湯面保護剤の使用が可能となり、湯面保護剤の
まき込みがなく極めて良好な鋳片が得られる。こ
れ等の理由により、鋳型長片テーパーを0.1%以
下にて、1300℃の粘度ηは鋳造速度Vに対し、
6.0<ηV
の範囲にする必要がある。
ブレークポイント又は表面張力の若干の変動に
ついてはNa2O、Li2O、F-、B2O3、AlF3、
Na3AlF6、MgF2等により調整行いえるものであ
る。スラブ巾については、600mm以下では、長片
長さが短かく比較的均一なシエルを形成し易く、
表面欠陥は発生しにくく600mm以上になると不均
一になり表面欠陥が発生し易いので、本発明によ
り操業の場合、鋳造巾を600mm以上とすることが
好ましい。
実施例
第1表に湯面保護剤の成分、物性を示す。この
湯面保護剤を使用して、スラブ連鋳機にて鋳造を
実施した。鋳造条件はモールドサイズ250×1600
mm、鋳造速度は1.0〜2.0m/minについて実施し
た。その時の鋳造結果を第2表に表示した。な
お、ブレークアウト発生指数:(発生回数/1000
チヤージ)、鋳片欠陥指数:(発生量/鋳片m2×
100)である。
A,B,C,D,E,Fは本発明実施例であ
り、B.O発生率指数は0、鋳片品質、鋳造操業性
共に良好な結果を示した。
G,H,J,Kは比較品(従来品)である。G
はブレークポイントは本発明範囲にあるが、表面
張力及び、ηVが本発明範囲外にあるもので、B.
O発生率は少かつたが、鋳片に介在物欠陥が発生
した。Hは表面張力は、本発明範囲内にあるがブ
レークポイント及びηVが範囲外にある例で、B.
O発生率が高く、かつ鋳片の表面割れが発生し
た。
Jはブレークポイント、表面張力は本発明範囲
にあるがηVが低すぎる例であり、B.O発生率は
少いが介在物欠陥及び表面割れが発生した。Kは
従来品(ブレークポイントが高く、表面張力が低
く、本発明外でかつηVが低すぎるため)であり、
B.Oが発生し鋳片に湯面保護剤の捲き込み疵が多
発した。
A′,C′は新たに得られた鋳型テーパーの条件
を入れたものであり、本発明操業外である鋳型テ
ーパー0.11%で操業した結果原単位が少なく、鋳
型の損耗量も多くかつ鋳造量にしたがい表面品位
の劣化が認められた。またD′はDと同じパウダ
ーを用いたが、更に高速鋳造を行つた結果で総合
評価において、充分満足するものであつた。K,
K′は共に、本発明範囲外のものであり、操業条
件である鋳型テーパーを0.11%と0.05%で鋳造を
行つた結果であり、総合評価では共に満足するも
のではなかつた。
INDUSTRIAL APPLICATION FIELD OF THE INVENTION The present invention relates to continuous casting of steel. BACKGROUND TECHNOLOGY During continuous casting of steel, a molten metal level protectant is added to the mold. The role of this molten metal surface protectant is to coat the surface of molten steel and keep it warm by adding it to the mold, and to prevent solidification and oxidation of the molten steel surface. To clean slabs by absorbing non-metallic inclusions floating up from molten steel, and to prevent defects caused by inclusions in products. Uniform inflow lubrication between the mold and the solidifying shell ensures uniform cooling of the mold, thereby preventing surface cracking and restraint breakout of the slab. In order to ensure the above properties, the hot water surface protectant is
The base material is oxides such as SiO 2 , Al 2 O 3 , CaO, Fe 2 O 3 , MgO, etc. In addition, oxides, carbonates, or fluorides of alkali metals and alkaline earth metals are used as physical property modifiers. Contains carbon as a melting rate regulator. As the carbon component, powders or granules of coke, carbon black, natural graphite, artificial graphite, coal, etc. are used. The ingredients of common hot water surface protectants include SiO 2 20
~45wt%, CaO20~45wt%, Al2O3 0.5 ~10wt
%, MgO1~20wt%, Na2O1~20wt%, F - 2 ~
It is composed of 20wt% or less and C10wt% or less, and LiO 2 , B 2 O 3 and other metal oxides, metal fluorides, and metal carbonates are also used as necessary. Analytically, fluorides are expressed as oxides and F - , and carbonates are expressed as oxides and C. In terms of physical properties, it has a viscosity of 0.5 to 15 poise at 1300°C and a melting point of 800 to 1200°C. On the other hand, in recent years there has been an increasing demand for cost reduction through energy conservation, resource conservation, and improvements in yield and unit consumption. Therefore, high-speed continuous casting and furthermore,
Direct feed rolling (CC-DR), in which high-temperature slabs produced by high-speed continuous casting are sent directly to the rolling process without cooling and reheating, is increasingly being adopted. In order to carry out this direct rolling, it is necessary to completely eliminate defects in the slabs manufactured by high-speed continuous casting (surface cracks, powdery defects in the slabs due to the inclusion of surface protection agent into the molten steel during the solidification process, etc.). Or, it must be extremely small to the extent that there is no problem even if direct rolling is performed, and product defects caused by defects in the slab must be prevented. However, if the surface protection agent used at conventional casting speeds is used as is for high-speed continuous casting,
The consumption of the surface protective agent decreases, which causes poor lubrication between the mold and the slab, making it more likely that a restraining breakout will occur. As a preventive measure, the viscosity of the surface protectant was lowered to 1300℃ due to high-speed casting.
By lowering the viscosity to 0.5 to 1.5 poise, the consumption of hot water surface protectant was increased and lubricity was maintained. (Japanese Patent Application Laid-open No. 150752/1983). Problems to be Solved by the Invention However, although reducing the viscosity of the molten metal surface protective agent has the effect of preventing restrictive breakout, the molten surface protective agent may flow into the molten steel due to the intense injection flow into the mold due to increased speed. As a result, the number of powder defects in the slab increases dramatically, which dramatically increases the number of defects in the product, creating a new major problem in implementing high-speed casting and direct rolling. In addition, even in medium and low speed casting, in order to further improve the quality of materials with strict quality requirements such as tinplate materials and steel plate materials for automobiles (Ti-Sulc steel), it is necessary to powder the slab by rolling in a surface protectant. We need to eliminate all sexual defects. The present invention completely prevents the occurrence of restraint breakout during high-speed casting, and at the same time suppresses the increase in powdery defects in slabs due to rolling in of the surface protectant, which is a problem in the above-mentioned conventional technology.
The present invention provides a new continuous casting method that not only enables direct rolling but also produces slabs with no powdery defects even during medium, low-speed or high-speed casting, thereby making it possible to obtain products of even higher quality. . Means for Solving the Problems In order to solve the above-mentioned drawbacks during casting, the inventors of the present invention have conducted various experiments and studies, and have discovered that under specific casting conditions there is an excellent region of extremely high viscosity. I was able to do it. The present invention was made based on these findings, and its characteristics are as follows:
Mold long piece taper [(mold top opening thickness - mold bottom opening thickness)/mold long piece height x 100%]
When continuously casting slabs under conditions of 0.1% or less, CaO, SiO 2 and Al 2 O 3 are the main components, and CaO/
SiO 2 (wt% ratio) is in the range of 0.5 to 1.6, and contains one or more oxides, carbonates, and fluorides of alkali metals, alkaline earth metals, and other metals, and carbon as a melting rate regulator. , surface tension at 1250℃ is 290dyne/cm or more, break point is
Viscosity η below 1000℃ and at 1300℃
A continuous steel casting method characterized by casting a slab using a surface protectant (powder) that satisfies the relationship between (poise) and casting speed V (m/min): 6.0<ηV It is. That is, the present invention newly introduces surface tension and break point as physical property values, specifies the range of the viscosity of the molten metal surface protective agent with respect to the casting speed, and casts the long piece taper of the mold in the range of 0.1% or less. This allows sufficient inflow lubrication between the mold and the slab to prevent restrictive breakout, not only in low-medium speed casting of 1.5 m/min or less, but also in high-speed casting of 1.5 m/min or more, and prevents restrictive breakout. The present invention provides a continuous casting method that can produce slabs with extremely few slab defects and, in the case of high-grade steel, has few inclusions. Function As mentioned above, in the continuous casting method using a surface protection agent, the molten layer of the surface protection agent is drawn into the molten steel by the molten steel flow in the mold, solidifies, and remains in the slab as inclusions, which impairs quality. The purpose is to prevent the deterioration of the lubricity and maintain smooth lubrication ability with the inner wall surface of the mold. Various studies were conducted to prevent this rolling and to ensure lubricity. First, regarding the prevention of entrainment, since the cause of entrainment is the disturbance of the molten steel surface due to the inflow of molten steel during casting, we focused on surface tension as a new physical property of the molten metal surface protectant, and measured the surface tension of commercially available products. . The measurement of surface tension is the first
Figure 2 shows the platinum cylindrical drawing method (Dipping).
Cylinder method). First, about 60g of a hot water surface protectant that had been decarburized for 1 hour in a Matsufuru furnace at 600°C was placed in a graphite crucible and heated to 1400°C.
Melt in a Matsufuru furnace for 10 minutes. This molten sample was placed in a platinum crucible 3, maintained at 1250° C., and inserted into an electric furnace 2 of a measuring device (FIG. 12) that was replaced with Ar. After the temperature stabilizes, the platinum cylinder 4 connected to the upper balance 1 is immersed in the melt and the balance is balanced. Next, weights are added from the platinum cylinder 4 to lower the liquid level until the balance reaches equilibrium. Repeat this operation until the platinum cylinder leaves the liquid surface, and record the maximum weight at the moment it leaves. This measurement is performed six times, and the average value excluding the maximum and minimum values is taken as Wmax (g). The calculation formula is expressed as σ=g·Wman/4πR×V. Here, σ is the surface tension (dyne/
cm), g is the acceleration of gravity (980cm/sec 2 ), Wmax
is the maximum pull (gr) exerted on the platinum cylinder, R is the radius of the cylinder (cm), and V is a correction coefficient, which is determined by the cylinder used and the density of the melt. The surface tension measurement results of the conventional products investigated were 240~
It was 290dyne/cm. In addition, the viscosity of the conventional product is
It was 0.6 to 3.0 poise at 1300°C, and no correlation was observed between viscosity and surface tension. Next, a casting test was conducted with different surface tension levels, and the relationship with the quality of the slab was investigated. The results are shown in FIG. The casting conditions were: slab size 1500 x 250 mm, melt composition C: 0.04, Si: 0.02,
Mn: 0.24, P: 0.02, S: 0.01, Al: 0.05 (%),
TD temperature 1560℃, casting speed 1.5 m/min, hot water surface protection agent (main components CaO: 39.0%, Al 2 O 3 : 2.0%, CaO:
36.0%, Na2O : 14.0%, F- : 6.0%) viscosity 1300
Standardized at ℃1.6poise. As is clear from Figure 2, the higher the surface tension, the
Although there is a tendency for inclusion defects to decrease, surface tension
A large decrease in inclusions can be seen at 290 dyne/cm. This means that the higher surface tension means that the surface binding force of the molten metal surface protective agent is stronger than the degree of turbulence of the molten metal surface caused by the casting conditions. As a result, under continuous casting,
We have newly discovered that if it is 290 dyne/cm or more, it is outside the critical condition for entrainment. However, although efforts have been made to reduce inclusion defects, conditions for eliminating them entirely have not been found. Therefore, the design was changed to one that sacrificed lubricity (BO generation rate), the viscosity was set to 3.2 poise at 1300°C, and a casting test was conducted again at 1.5 m/min under the above operating conditions. The results are shown in FIG. As is clear from Figure 3, it has been newly discovered that increasing the viscosity reduces the incidence of inclusions, but increasing the surface tension to 290 dyne/cm or higher can completely eliminate inclusion defects in slabs. did. However, by increasing the viscosity, the lubricity decreased and the rate of occurrence of restrictive BO increased, both of which were 1
(0.1 in Figure 2), which did not guarantee sufficient lubricity. Accordingly, the present inventors conducted research and investigation into means for ensuring this lubricity, and as a result, obtained the following knowledge.
That is, it is said that the physical property most closely related to the unit consumption is viscosity, and it has been conventional knowledge that as the casting speed increases, the viscosity of the surface protectant decreases. Generally, the viscosity is
The measured value at 1300℃ is used, which is
The average temperature of the inflow film just below the meniscus is approximately
This is because the temperature is 1300°C and the measured values can be obtained relatively stably. The present inventors melted 200g of various hot water surface protectants after decarburization at 1400℃ for 10 minutes using a rotor rotation method.
Viscosity measurement was carried out after holding at 1300℃, and then 20
The temperature was lowered by ℃ and the viscosity was measured after holding at each temperature to obtain 1ogη-1/T (η is the viscosity poise, T
I created a graph (indicating the absolute temperature). During this measurement, crystals crystallized in the sample due to temperature drop, and the sample ceased to be a Newtonian liquid, and the breakpoint was defined as a temperature 10°C higher than the temperature at which measurement became impossible. Figure 4 shows an example of the measurement. As is clear from Figure 4, it was found that there are hot water surface protective agents that have vastly different break points even if the viscosity at 1300°C is the same. Therefore, we prototyped a sample with a different breakpoint, conducted an actual casting test, and investigated the effect on the breakout occurrence rate (hereinafter referred to as BO occurrence rate). The steel type and casting speed were the same as before, and the viscosity was 3.2 poise at 1300℃. The results are shown in Figure 5. As is clear from Figure 5, there is a large correlation between the BO incidence rate and the breakpoint, and it is possible to reduce the BO incidence rate by lowering the breakpoint, and the breakpoint temperature can be reduced. We have newly discovered that by keeping the temperature below 1000°C, the BO incidence can be completely eliminated. As shown in Figure 6b, this is the conventional hot water surface protection agent 7.
is liquid lubrication 8 only in the meniscus part, and the other lower parts are in a solid state 9, and 1300
Only the viscosity in °C controlled the basic unit of powder, that is, the lubricity. Furthermore, as shown in Figure 6a, the fact that the break point of the molten metal level protectant 10 of the present invention is 1000°C or lower means that the surface of the slab at the lower end of the mold is generally said to be at 1000°C, and for this reason, molten water is also present at the lower end of the mold. The surface protective agent exists as a liquid, and the entire surface of the mold (the entire surface of the cast piece in the mold) has liquid lubrication.
1, indicating an ideal lubrication condition unlike the conventional one. As a result, the incidence of restrictive breakouts was completely eliminated. Furthermore, by regulating a certain characteristic condition of the mold, that is, the mold taper on the long side, the entire surface between the mold inner wall surface and the surface of the solidified shell is lubricated by the liquid level protectant, and if the taper is small, the break point and surface are the same. Even under tension, high-viscosity molten metal surface protection could be used and good slabs were obtained. Based on this knowledge, we conducted a test. In other words, we varied the mold long piece taper and investigated the optimum unit consumption (Kg/Ton Steel), quality, and operability.
At this time, the characteristics of the hot water surface protective agent and the operating conditions were the same as before. The results are shown in Figure 7. As is clear from Figure 7, a large relationship was found between the mold taper of the long piece and the basic unit of the hot water surface protective agent, and this relationship showed that there was a clear difference at the taper of the long piece of 0.1%. I found it. The reason for this is that if it is greater than 0.1%, in the mold,
The bulging of the slab becomes large and the inflow is inhibited, but if it is less than 0.1%, the opening of the mold toward the lower end is large and the amount of inflow increases rapidly. Similarly, if low clay is used under conditions of greater than 0.1%, the basic unit will be at a normal value, but as mentioned above, the amount of entrainment in the slab will be large and the quality will deteriorate. Furthermore, when a high viscosity is used, the quality is good, but the unit consumption is low and casting troubles (surface flaws due to large amount of mold wear) become serious. Even if there is no breakout rate and the quality of the slab is good, if the consumption of surface protection agent is high, the cost of casting the slab will increase and the amount of slag film attached to the slab will increase. This results in poor peeling during rolling of the slab and increases in rolling defects. Furthermore, when the unit consumption decreases, the amount of wear on the inner surface of the mold increases, resulting in increased surface flaws or a very high mold maintenance rate. In other words, an optimal basic unit exists. These relationships are shown in Figures 8 (operating conditions are the same as in Figure 7), 9 and 10. Based on these results, it was found that the optimum basic unit was 0.20 to 0.6Kg/Ton Steel. Next, to find the optimal viscosity range, the surface tension is
290dyne/cm or more at 1250℃, breakpoint
We prototyped a hot water surface protective agent with a viscosity that varied within the range of 1000℃ or less, and set the long piece taper of the mold to 0.1% or less.
The slab quality was checked by casting on an actual machine using various combinations of casting speeds. The results are shown in FIG. The mark ○ indicates a product that passed the overall evaluation (example of the present invention), and the mark x indicates a product that failed the test (comparison product). From Figure 1, for casting speed,
There is an appropriate viscosity range. Here, the long piece taper of the mold used in the present invention is as shown in Fig. 13: Upper end opening thickness B - lower end opening thickness C/long piece height A x 100
It is defined as %. Carbon in the hot water level protectant adjusts the melting rate of the hot water level protectant while being heated and burned depending on the molten steel temperature when added, and the melting rate is influenced by the amount of carbon contained therein. In other words, if the content is high, the melting rate will be slow, and a content suitable for casting operations is required. That is, for the casting speed V, the viscosity η at 1300° C. is designed to be in the range of 6.0<ηV, preferably ηV is 20 or less. This is because if it is too high, the basic unit may decrease. Furthermore, as shown in Fig. 11, not only does the high surface tension in Fig. 2 reduce the slab defect index (incorporation of surface protection agent) due to inclusions, but also the general surface tension lowers the break point. The defect index due to inclusions within the piece was reduced, and as shown in FIG. 11, a remarkable effect could be found with this combination by creating a high surface tension and a low break point. In this way, by making the surface tension high (290 dyne/cm or more) and the break point low (1000°C or less), we were able to significantly reduce the occurrence of inclusions. It was discovered that under these conditions, good slabs without casting defects could be produced. Based on the above results, the reasons for limiting the scope of the present invention can be summarized as follows. The component system of the hot water surface protectant used may be the composition of a commonly used hot water surface protectant, and has the physical properties of a surface tension of 290 dyne/cm or more and a break point of 1000°C or less as claimed in the claims, CaO/SiO 2 (wt% ratio)
Only 0.5 to 1.6. It is CaO/SiO 2 <
In the case of 0.5, a large amount of flux components (Na 2 O, Li 2 O, F -, etc.) are required to adjust the physical properties, especially the viscosity, which increases the amount of erosion of the immersion nozzle and increases the cost, making it impractical. But also CaO/
If SiO 2 > 1.6, glassy properties are lost during inflow lubrication due to denaturation within the mold (absorption of Al 2 O 3 inclusions, reduction of SiO 2 in the molten metal surface protectant by Al in the steel). , causing recrystallization. The break point is below 1000℃.
This means that it maintains glassiness even at low temperatures, and in terms of ionic crystals, SiO 2 connections form a linear structure rather than a lumpy group, making it difficult to form crystals. When crystals occur, heat removal from the slab becomes uneven, making it easier for breakouts to occur due to surface defects and poor lubrication, so CaO/SiO 2 =
The range was 0.5 to 1.6. The reason why the surface tension is set to 290 dyne/cm or more at 1250℃ is because, as mentioned above, if it is 290 dyne/cm or less, the molten layer of the molten metal surface protectant will be easily engulfed by the molten steel flow, causing inclusion defects. Surface tension is 1250
The temperature must be 290dyne/cm or higher at ℃. The reason why the breakpoint is below 1000℃ is that the viscosity is relatively high and the BO generation rate can be completely eliminated as mentioned above, and above 1000℃, there is a solid surface protectant in the mold as mentioned above. It is necessary to keep the temperature below 1000℃, as this will cause poor lubrication in the gap between the mold and the slab, making breakouts more likely to occur. The reason why the viscosity η at 1300℃ is limited to 6.0<ηV with respect to the casting speed V is that when ηV≦6, the long piece taper
Under the condition of 0.1% or less, the viscosity is too low for the casting speed, and the liquid of the slag film in the mold flows freely, resulting in too high a unit consumption, resulting in defects, such as rolling scratches, and problems (increased costs). This is because mold taper is 0.1.
In this case, the occurrence of surface defects increases as the basic unit decreases. When ηV>6.0 and the taper is 0.1 or more, surface flaws increase dramatically as described above. The reason for this is, as mentioned above, the characteristics of the hot water surface protectant, the break point of 1000℃ or less, and the surface tension.
When it is 290 dyne/cm or more, liquid lubrication occurs within the mold and slabs of good quality can be obtained, but by further regulating the mold taper, it is possible to use a surface protectant with a high viscosity. Very good slabs can be obtained without mixing in the surface protection agent. For these reasons, it is necessary to set the mold long piece taper to 0.1% or less, and the viscosity η at 1300°C to be in the range of 6.0<ηV with respect to the casting speed V. Na 2 O, Li 2 O, F − , B 2 O 3 , AlF 3 , for break points or slight variations in surface tension.
It can be adjusted with Na 3 AlF 6 , MgF 2 , etc. Regarding the slab width, if it is 600 mm or less, the length of the long pieces is short and it is easy to form a relatively uniform shell.
Surface defects are difficult to occur, and if the width is 600 mm or more, it becomes non-uniform and surface defects are likely to occur. Therefore, when operating according to the present invention, it is preferable that the casting width is 600 mm or more. Examples Table 1 shows the components and physical properties of the hot water surface protectant. Using this hot water surface protective agent, casting was carried out using a continuous slab caster. Casting conditions are mold size 250 x 1600
mm, and the casting speed was 1.0 to 2.0 m/min. The casting results at that time are shown in Table 2. In addition, breakout occurrence index: (number of occurrences/1000
charge), slab defect index: (amount of occurrence / slab m 2 ×
100). Examples A, B, C, D, E, and F are examples of the present invention, and the BO generation rate index was 0, and both slab quality and casting operability showed good results. G, H, J, and K are comparative products (conventional products). G
The breakpoint is within the scope of the present invention, but the surface tension and ηV are outside the scope of the present invention, and B.
Although the O generation rate was low, inclusion defects occurred in the slab. H is an example in which the surface tension is within the range of the present invention, but the break point and ηV are outside the range, and B.
The O generation rate was high, and surface cracking of the slab occurred. J is a break point, the surface tension is within the range of the present invention, but ηV is too low, and although the BO generation rate is low, inclusion defects and surface cracks occur. K is a conventional product (because the break point is high, the surface tension is low, it is outside the scope of the present invention, and ηV is too low),
BO occurred and there were many cracks caused by the molten metal surface protection agent being rolled into the slab. A′ and C′ include the newly obtained mold taper conditions, and as a result of operating with a mold taper of 0.11%, which is outside the operation of the present invention, the basic unit was small, the amount of mold wear was large, and the casting amount was Deterioration of surface quality was observed. In addition, D' used the same powder as D, but was cast at a higher speed, and the results were fully satisfactory in the overall evaluation. K,
Both K' were outside the scope of the present invention, and were the results of casting under operating conditions of mold taper of 0.11% and 0.05%, and both were not satisfactory in the overall evaluation.
【表】【table】
【表】【table】
【表】
発明の効果
本発明は鋼の連続鋳造技術の進歩に伴い高品質
化、高速化、無手入れ化が指向される中で従来の
技術ではなし得なかつた無手入れ鋳片の製造を可
能にするものである。[Table] Effects of the Invention The present invention enables the production of maintenance-free slabs, which was not possible with conventional technology, as continuous steel casting technology advances and the trend is toward higher quality, faster speeds, and maintenance-free casting. It is meant to be.
第1図は鋳造速度と粘度、表面張力との鋳片品
質関係を示すグラフ、第2,3図は表面張力と鋳
片表面欠陥指数及びブレークアウト発生指数の関
係を示すグラフ、第4図は粘度及びブレークポイ
ントの測定例を示すグラフ、第5図はブレークポ
イントとブレークアウト発生指数の関係を示すグ
ラフ、第6図aは本発明鋳型内の潤滑モデルの説
明図であり、第6図bは、従来の鋳型内の潤滑モ
デルの説明図である。第7は、鋳型長片テーパー
と原単位の関係を示すグラフであり、第8図は、
原単位と鋳片のスラグ付着量及び圧延疵発生との
関係を示すグラフである。第9図は、鋳型長片テ
ーパーと鋳型内面損耗量との関係を示すグラフ、
第10図は、鋳造時間と鋳片表面疵発生との関係
を示すグラフ、第11図は、ブレークポイントと
鋳片欠陥指数の関係を示すグラフ、第12図は、
表面張力の測定装置概略図である。第13図は、
鋳型長片テーパーの定義の説明図である。
1…天秤、2…電気炉、3…白金ルツボ、4…
白金円筒、5…Pt−Pt・Ph熱電対、6…熱遮蔽
板、7,10…湯面保護剤、8,11…溶融部、
9…固体、12…鋳片、13…鋳型。
Figure 1 is a graph showing the relationship between casting speed, viscosity, and surface tension, and Figures 2 and 3 are graphs showing the relationship between surface tension, slab surface defect index, and breakout occurrence index, and Figure 4 is a graph showing the relationship between surface tension and slab surface defect index and breakout occurrence index. Graph showing an example of measurement of viscosity and break point, FIG. 5 is a graph showing the relationship between break point and breakout occurrence index, FIG. FIG. 1 is an explanatory diagram of a conventional lubrication model within a mold. The seventh is a graph showing the relationship between the mold long piece taper and the basic unit, and FIG.
It is a graph showing the relationship between the basic unit, the amount of slag adhering to a slab, and the occurrence of rolling defects. FIG. 9 is a graph showing the relationship between the mold long piece taper and the amount of mold inner wear;
Fig. 10 is a graph showing the relationship between casting time and slab surface flaw occurrence, Fig. 11 is a graph showing the relationship between break point and slab defect index, and Fig. 12 is a graph showing the relationship between casting time and slab surface flaw occurrence.
FIG. 1 is a schematic diagram of a surface tension measuring device. Figure 13 shows
FIG. 3 is an explanatory diagram of the definition of a mold long piece taper. 1... Balance, 2... Electric furnace, 3... Platinum crucible, 4...
Platinum cylinder, 5... Pt-Pt/Ph thermocouple, 6... heat shielding plate, 7, 10... hot water surface protective agent, 8, 11... melting part,
9...Solid, 12...Slab, 13...Mold.
Claims (1)
鋳型の下端開口厚)/鋳型の長片の高さ×100%〕
を0.1%以下の条件でスラブを連続鋳造するに際
して、CaO、SiO2、Al2O3を主成分とし、CaO/
SiO2(重量%比)が0.5〜1.6の範囲で、アルカリ
金属およびアルカリ土類金属および他金属の酸化
物、炭酸塩、弗化物の1種以上と更に溶融速度調
整剤として炭素分を含有し、1250℃における表面
張力が290dyne/cm以上、ブレークポイントが
1000℃以下で、かつ1300℃における粘度η
(poise)が鋳造速度V(m/min)との関係式 6.0<ηV の範囲を満足する湯面保護剤(パウダー)を使用
して、スラブを鋳造することを特徴とする鋼の連
続鋳造法。[Claims] 1 Long piece taper of the mold [(Mold upper end opening thickness -
Thickness of the lower end of the mold) / Height of the long piece of the mold x 100%]
When continuously casting slabs under conditions of 0.1% or less, CaO, SiO 2 and Al 2 O 3 are the main components, and CaO/
SiO 2 (wt% ratio) is in the range of 0.5 to 1.6, and contains one or more oxides, carbonates, and fluorides of alkali metals, alkaline earth metals, and other metals, and carbon as a melting rate regulator. , surface tension at 1250℃ is 290dyne/cm or more, break point is
Viscosity η below 1000℃ and at 1300℃
A continuous steel casting method characterized by casting a slab using a surface protectant (powder) that satisfies the relationship between (poise) and casting speed V (m/min): 6.0<ηV .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17181588A JPH0225254A (en) | 1988-07-12 | 1988-07-12 | Continuous casting method of steel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17181588A JPH0225254A (en) | 1988-07-12 | 1988-07-12 | Continuous casting method of steel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0225254A JPH0225254A (en) | 1990-01-26 |
| JPH0440103B2 true JPH0440103B2 (en) | 1992-07-01 |
Family
ID=15930246
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17181588A Granted JPH0225254A (en) | 1988-07-12 | 1988-07-12 | Continuous casting method of steel |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0225254A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2018144046A (en) * | 2017-03-01 | 2018-09-20 | 新日鐵住金株式会社 | Mold powder for continuous casting and method for continuous casting of steel |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2303825C (en) * | 1998-07-21 | 2007-01-09 | Shinagawa Refractories Co., Ltd. | Molding powder for continuous casting of thin-slab |
| AU764954B2 (en) * | 1998-12-08 | 2003-09-04 | Shinagawa Refractories Co., Ltd. | Molding powder for continuous casting of steel and method for continuous casting of steel |
| JP4513162B2 (en) * | 2000-04-03 | 2010-07-28 | Jfeスチール株式会社 | Powder for continuous casting of steel |
| JP3717049B2 (en) * | 2000-05-26 | 2005-11-16 | 品川白煉瓦株式会社 | Mold powder for continuous casting of steel and continuous casting method of steel |
| JP4265285B2 (en) * | 2003-05-29 | 2009-05-20 | Jfeスチール株式会社 | Mold powder for continuous casting of steel |
| JP5454131B2 (en) * | 2009-03-23 | 2014-03-26 | Jfeスチール株式会社 | Mold powder for continuous casting of steel and continuous casting method of steel |
| JP6871525B2 (en) * | 2020-06-12 | 2021-05-12 | 品川リフラクトリーズ株式会社 | Mold powder |
-
1988
- 1988-07-12 JP JP17181588A patent/JPH0225254A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2018144046A (en) * | 2017-03-01 | 2018-09-20 | 新日鐵住金株式会社 | Mold powder for continuous casting and method for continuous casting of steel |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0225254A (en) | 1990-01-26 |
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