JP4456491B2 - Porous immersion nozzle and continuous casting method using the same - Google Patents

Porous immersion nozzle and continuous casting method using the same Download PDF

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JP4456491B2
JP4456491B2 JP2005013067A JP2005013067A JP4456491B2 JP 4456491 B2 JP4456491 B2 JP 4456491B2 JP 2005013067 A JP2005013067 A JP 2005013067A JP 2005013067 A JP2005013067 A JP 2005013067A JP 4456491 B2 JP4456491 B2 JP 4456491B2
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JP2006198655A (en
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雅弘 谷
新一 福永
和久 田中
昌文 瀬々
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Nippon Steel Corp
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Description

本発明は、連続鋳造において溶鋼を鋳型に注入するための多孔浸漬ノズル及びこれを用いた連続鋳造方法に関し、詳しくは鋳型内の溶鋼の流れを緩慢にし、かつ均一な流れを形成して気泡や介在物による欠陥を防止して高速鋳造を可能にする多孔浸漬ノズル及びこれを用いた連続鋳造方法に関する。 The present invention relates to a multi-hole nozzle for injecting molten steel into a mold in continuous casting and a continuous casting method using the same, and more specifically, the flow of molten steel in the mold is slowed down and a uniform flow is formed to form bubbles and The present invention relates to a multi-hole immersion nozzle that enables high-speed casting by preventing defects due to inclusions and a continuous casting method using the same.

従来、連続鋳造においては、タンディッシュから浸漬ノズルを介して鋳型内に溶鋼を注湯し、鋳型による一次冷却で健全な凝固殻を形成し、引き続いて鋳型の下方に配置された支持セグメントに付設した冷却ノズルからの散水による二次冷却により凝固を促進して鋳片を製造している。しかしながら、鋳片の品質は、鋳型内で形成される初期の凝固殻の良否、及び鋳型内の下方に侵入する気泡や介在物の有無によって大きく左右される。すなわち、鋳型内においては、浸漬ノズルの左右対となる吐出口からの溶鋼の吐出流は、鋳型の短辺側に衝突して鋳型内壁に沿って上昇する上向き流と鋳型内壁に沿って下降する下向き流に分流するが、吐出口に介在物等が付着すると上向き流及び下向き流において左右のバランスが乱れたり局部的に強い吐出流が生じたりして流れが大きく変動し、凝固殻の生成不良や、気泡及び介在物が起因する欠陥発生の要因となる。従って、この吐出流の偏流を抑制する方法、及び発生した偏流を減衰させて安定した流れにする方法が鋭意検討されているのが現状であり、更に、吐出流を制御する方法あるいは吐出流の制御が可能な各種の浸漬ノズルの提案が行なわれている。 Conventionally, in continuous casting, molten steel is poured into the mold from the tundish through the immersion nozzle, and a solid solidified shell is formed by the primary cooling by the mold, and subsequently attached to the support segment located below the mold. The slab is manufactured by promoting solidification by secondary cooling by water spraying from the cooling nozzle. However, the quality of the slab depends greatly on the quality of the initial solidified shell formed in the mold and the presence or absence of bubbles and inclusions that enter the lower part of the mold. That is, in the mold, the discharge flow of the molten steel from the left and right discharge ports of the immersion nozzle collides with the short side of the mold and rises along the mold inner wall and descends along the mold inner wall. However, when inclusions adhere to the discharge port, the left and right balance is disturbed in the upward and downward flows, and a strong discharge flow is generated locally, resulting in large fluctuations in the flow and poor formation of solidified shells. Moreover, it becomes a factor of the defect generation | occurrence | production resulting from a bubble and an inclusion. Therefore, the present state is intensively studied a method for suppressing the uneven flow of the discharge flow and a method for attenuating the generated uneven flow to obtain a stable flow. Various types of immersion nozzles that can be controlled have been proposed.

例えば、特許文献1には、筒状体からなる第1のノズル部と、この第1のノズル部に連設する中空の矩形状からなる第2のノズル部を有し、第2のノズル部の下方を開放して吐出口にすると共に、第2のノズル部の内部を通過する溶鋼流に直交する抵抗部材を複数配置した浸漬ノズル及びその浸漬ノズルを用いた連続鋳造方法が提案されている。
特許文献2には、下端部を閉塞した筒体(ノズル本体)の対向する側壁に一対の溶鋼の吐出口を設け、各吐出口の外側に吐出口を囲む空間部を有する滞留室を配置し、吐出口と対向する滞留室の壁に複数の小吐出口を設けて、溶鋼をノズル本体の下部及び滞留室で撹拌混合して微小介在物の合体と集合を促進して鋳型内における介在物の浮上性を良好にする浸漬ノズルが提案されている。
For example, Patent Document 1 includes a first nozzle portion made of a cylindrical body, and a second nozzle portion made of a hollow rectangle connected to the first nozzle portion. An immersion nozzle in which a plurality of resistance members orthogonal to the molten steel flow passing through the inside of the second nozzle portion are arranged and a continuous casting method using the immersion nozzle have been proposed. .
In Patent Document 2, a pair of molten steel discharge ports are provided on opposite side walls of a cylindrical body (nozzle body) whose lower end portion is closed, and a retention chamber having a space portion surrounding the discharge port is disposed outside each discharge port. In addition, a plurality of small discharge ports are provided on the wall of the retention chamber facing the discharge port, and the molten steel is stirred and mixed in the lower portion of the nozzle body and the retention chamber to promote coalescence and assembly of the fine inclusions. There has been proposed an immersion nozzle that improves the floatability of the nozzle.

特許文献3には、浸漬ノズルの左右の側壁に上下一対の吐出口をそれぞれ設け、上下の吐出口間の距離をD、モールド長さをL、スループットをY、モールド上端からメニスカスに至るまでの距離をZとして、D<L−Z−64Y−370とすることで、スループットを高めてもモールドパウダー等を巻き込むことなく品質の高い鋳片を得ることができる高速連続鋳造用浸漬ノズルが開示されている。
特許文献4には、浸漬ノズルの構造を簡素化して鋳片の気泡、介在物、及びパウダー巻き込み等の品質欠陥要因を解消するため、浸漬ノズルの吐出口を上下2段に設け、吐出口の角度を鋳型の長辺側長さ、鋳型の短辺側長さ、及び吐出口からの吐出流が鋳型の長辺側壁と衝突するまでに移動する距離をそれぞれ特定の範囲に規定することによって、浸漬ノズルからの吐出流の減衰と溶鋼の吐出流を鋳型の長辺側壁に衝突させることが提案されている。
In Patent Document 3, a pair of upper and lower discharge ports are provided on the left and right side walls of the immersion nozzle, the distance between the upper and lower discharge ports is D, the mold length is L, the throughput is Y, and the upper end of the mold to the meniscus. Disclosed is a high-speed continuous casting immersion nozzle that can obtain a high-quality slab without entraining mold powder or the like even when the throughput is increased by setting the distance to Z and D <LZ-64Y-370. ing.
In Patent Document 4, in order to simplify the structure of the immersion nozzle and eliminate quality defect factors such as slab bubbles, inclusions, and powder entrainment, the immersion nozzle discharge ports are provided in two upper and lower stages. By defining the angle within a specific range, the long side length of the mold, the short side length of the mold, and the distance that the discharge flow from the discharge port moves until it collides with the long side wall of the mold, respectively. It has been proposed that the discharge flow attenuation from the immersion nozzle and the discharge flow of molten steel collide with the long side wall of the mold.

特開昭60−130456号公報JP-A-60-130456 実開昭60−71462号公報Japanese Utility Model Publication No. 60-71462 特開平2−187240号公報Japanese Patent Laid-Open No. 2-187240 特開平2−295654号公報JP-A-2-295654

しかしながら、特許文献1の発明では、吐出流の方向を浸漬ノズルの下方側に向かうようにしているため、上向き流によるパウダーの巻込みや湯面変動に起因した表面欠陥等を阻止できるが、下向きの溶鋼流を抵抗部材で減衰することが困難であり、強い下向き流が形成され、気泡や介在物が鋳片の深部に侵入して内部欠陥の要因となる。更に、上向き流が弱くなるため、鋳型内で形成される初期の凝固殻の内表面の溶鋼の流れによる洗浄効果が減少し、凝固殻の内表面に気泡や介在物が捕捉され、鋳片の表面欠陥の要因になるという問題がある。
特許文献2の発明では、浸漬ノズルの下部に流下した溶鋼流を滞留室内でその落下エネルギーを安定して減衰することができず、空間部を介して小吐出口に流れる溶鋼流に偏流が生じ、小吐出口から鋳型内への吐出流にも偏流が形成され、局部的に強い流れが発生する。その結果、溶鋼の下向き流や上向き流に起因した表面欠陥、及び気泡や介在物が鋳片の深部に侵入して発生する内部欠陥が発生する。更に、小吐出口に介在物の付着が生じて溶鋼の偏流が加速されたり、ノズルの構造が複雑になり耐火物のコストが高くなる等の問題がある。
However, in the invention of Patent Document 1, since the direction of the discharge flow is directed to the lower side of the submerged nozzle, it is possible to prevent surface defects and the like due to powder entrainment due to upward flow or fluctuation of the molten metal surface, but downward It is difficult to attenuate the molten steel flow with the resistance member, and a strong downward flow is formed. Bubbles and inclusions penetrate into the deep part of the slab and cause internal defects. Furthermore, since the upward flow becomes weak, the cleaning effect of the inner surface of the initial solidified shell formed in the mold due to the flow of molten steel is reduced, and bubbles and inclusions are trapped on the inner surface of the solidified shell, There is a problem of causing surface defects.
In the invention of Patent Document 2, the drop energy of the molten steel flow flowing down to the lower part of the immersion nozzle cannot be stably attenuated in the stay chamber, and a drift occurs in the molten steel flow flowing to the small discharge port through the space portion. Also, uneven flow is formed in the discharge flow from the small discharge port into the mold, and a strong flow is generated locally. As a result, surface defects caused by the downward flow and upward flow of the molten steel, and internal defects generated by bubbles and inclusions entering the deep part of the slab are generated. Furthermore, there is a problem that inclusions are attached to the small discharge ports to accelerate the drift of the molten steel, the nozzle structure is complicated, and the cost of the refractory is increased.

特許文献3の発明では、上下方向の2段の吐出口の間隔が狭い場合は、吐出口から出た溶鋼流が合流し、溶鋼を2孔から分散させて吐出させた効果がなくなる。一方、2段の吐出口の間隔が広い場合は、溶鋼の高さ方向の圧力差によって上下の吐出口を通過する流量バランスが崩れるという問題が生じる。
特許文献4の発明では、特許文献3の発明における問題点に加えて、鋳型内壁で成長しつつある凝固殻の内で長辺側の凝固殻に溶鋼の吐出流が直接当たるため、長辺側に形成される凝固殻の厚みのバラツキに起因する欠陥の発生、及び鋳型の長辺側壁に衝突した溶鋼流が短辺側壁に強い流れとなって再度衝突するため、短辺側壁における下向き流が大きくなり、気泡や介在物が鋳片の深部に侵入することを十分に回避できないという問題が生じる。
In the invention of Patent Document 3, when the interval between the two-stage discharge ports in the vertical direction is narrow, the molten steel flow coming out of the discharge ports merges and the effect of discharging the molten steel from the two holes is lost. On the other hand, when the interval between the two-stage discharge ports is wide, there arises a problem that the flow rate balance passing through the upper and lower discharge ports is lost due to the pressure difference in the height direction of the molten steel.
In the invention of Patent Document 4, in addition to the problems in the invention of Patent Document 3, since the discharge flow of the molten steel directly hits the solidified shell on the long side in the solidified shell growing on the inner wall of the mold, the long side The occurrence of defects due to the variation in the thickness of the solidified shell formed on the surface, and the molten steel flow that collided with the long side wall of the mold collided again with a strong flow on the short side wall, so the downward flow on the short side wall A problem arises in that air bubbles and inclusions cannot sufficiently be prevented from penetrating into the deep part of the slab.

本発明はかかる事情に鑑みてなされたもので、鋳型内の溶鋼の流れを緩慢にし、かつ均一な流れを形成して、気泡や介在物による欠陥を防止して高速鋳造を可能にする多孔浸漬ノズル及びこれを用いた連続鋳造方法を提供することを目的とする。 The present invention has been made in view of such circumstances, and a porous dipping that makes high-speed casting possible by slowing the flow of molten steel in the mold and forming a uniform flow to prevent defects due to bubbles and inclusions. An object is to provide a nozzle and a continuous casting method using the nozzle.

本発明に係る多孔浸漬ノズルは、溶鋼が上から下に通過する筒状のノズル本体と、該ノズル本体の下端に連設して設けられ、鋳型内に浸漬される吐出部とを有する浸漬ノズルにおいて、
前記吐出部の流路の平均断面積は前記ノズル本体の下部流路の断面積より小さく、該ノズル本体の下部流路の内平均寸法Dと前記吐出部の流路の最小内寸法dとの比d/Dが0.2以上0.8未満、かつ前記吐出部の流路の上端の内寸法は前記ノズル本体の下部流路の内寸法より小さく、しかも、前記吐出部の流路の内寸法は上端から下端まで一定であり、
前記鋳型の短辺側を指向する前記吐出部の側壁には上下に少なくとも2以上の吐出口が設けられ、前記鋳型内の溶鋼のメニスカスから前記吐出口のうち最上部の吐出口の外側上端までの距離Lと、前記吐出部の上端から前記最上部の吐出口の内側上端までの距離xの間に、0.1d<x<5dかつ1.5D<L−x≦20Dの関係が成立し、下側に設けられた前記吐出口の断面積は上側に設けられた前記吐出口の断面積よりも小さく、前記各吐出口の軸心の傾斜角度が水平に対して上向き10°から下向き45°の範囲に設定されている
ここで、流路の平均断面積とは流路の上流側から下流側に沿って流路の横断面積が変化する場合における横断面積の平均値を指し、流路の最小内寸法dとは流路の横断面積が最小となる位置における内寸法の最小値を指す。また、下部流路の内平均寸法Dとは、下部流路の横断面における最大内寸法と最小内寸法の平均値を指す。更に、吐出部の流路の内寸法とは吐出部の流路の断面積に等しい円の直径を指し、ノズル本体の下部流路の内寸法とはノズル本体の下部流路の断面積に等しい円の直径を指し、吐出口の内寸法とは吐出口の断面積に等しい円の直径を指す。
The porous immersion nozzle according to the present invention includes a cylindrical nozzle body through which molten steel passes from top to bottom, and a discharge nozzle that is provided continuously with the lower end of the nozzle body and is immersed in a mold. In
The average cross-sectional area of the flow path of the discharge section is smaller than the cross-sectional area of the lower flow path of the nozzle body, and the inner average dimension D of the lower flow path of the nozzle body and the minimum internal dimension d of the flow path of the discharge section The ratio d / D is 0.2 or more and less than 0.8 and the inner dimension of the upper end of the flow path of the discharge part is smaller than the inner dimension of the lower flow path of the nozzle body, and the inner dimension of the flow path of the discharge part The dimensions are constant from top to bottom ,
At least two or more discharge ports are provided in the upper and lower sides on the side wall of the discharge portion directed to the short side of the mold, from the meniscus of the molten steel in the mold to the outer upper end of the uppermost discharge port among the discharge ports The relationship of 0.1d <x <5d and 1.5D <L−x ≦ 20D is established between the distance L and the distance x from the upper end of the discharge unit to the inner upper end of the uppermost discharge port. The cross-sectional area of the discharge port provided on the lower side is smaller than the cross-sectional area of the discharge port provided on the upper side, and the inclination angle of the axis of each discharge port is 10 ° upward to 45 ° downward with respect to the horizontal. It is set in the range of ° .
Here, the average cross-sectional area of the flow path refers to the average value of the cross-sectional areas when the cross-sectional area of the flow path changes from the upstream side to the downstream side of the flow path. The minimum value of the internal dimension at the position where the cross-sectional area of the road is minimum. The inner average dimension D of the lower channel refers to the average value of the maximum inner dimension and the minimum inner dimension in the cross section of the lower channel. Furthermore, the inner dimension of the flow path of the discharge part refers to the diameter of a circle equal to the cross-sectional area of the flow path of the discharge part, and the inner dimension of the lower flow path of the nozzle body is equal to the cross-sectional area of the lower flow path of the nozzle body. This refers to the diameter of the circle, and the inner dimension of the discharge port refers to the diameter of the circle equal to the cross-sectional area of the discharge port.

本発明に係る連続鋳造方法は、溶鋼が上から下に通過する筒状のノズル本体と、該ノズル本体の下端に連設して設けられ、鋳型内に浸漬される吐出部とを有し、前記吐出部の流路の平均断面積は前記ノズル本体の下部流路の断面積より小さく、該ノズル本体の下部流路の内平均寸法Dと該吐出部の流路の最小内寸法dとの比d/Dが0.2以上0.8未満、かつ前記吐出部の流路の上端の内寸法は前記ノズル本体の下部流路の内寸法より小さく、しかも、前記吐出部の流路の内寸法は上端から下端まで一定であり、前記鋳型の短辺側を指向する前記吐出部の側壁には上下に少なくとも2以上の吐出口が設けられ、下側に設けられた前記吐出口の断面積は上側に設けられた前記吐出口の断面積よりも小さな多孔浸漬ノズルを介して、前記鋳型内に溶鋼を注湯し、溶鋼を凝固させながら0.6m/min以上の鋳造速度で前記鋳型から引き抜く連続鋳造方法であって、
前記吐出部の上端から前記吐出口のうち最上部の吐出口の内側上端までの距離xを0.1d<x<5d、前記鋳型内の溶鋼のメニスカスから前記最上部の吐出口の外側上端までの距離Lを1.5D<L−x≦20Dとすると共に、前記各吐出口の軸心の傾斜角度を水平状態に対して上向き10°から下向き45°の範囲に設定し、前記吐出部を前記鋳型内の溶鋼のメニスカス位置から150〜350mmの範囲で該鋳型中の溶鋼に浸漬させ、アルゴンガスの吹き込み量を0.2〜20ノルマルリットル/分にする
The continuous casting method according to the present invention has a cylindrical nozzle body through which molten steel passes from top to bottom, a discharge part that is provided continuously to the lower end of the nozzle body, and is immersed in a mold, The average cross-sectional area of the flow path of the discharge section is smaller than the cross-sectional area of the lower flow path of the nozzle body, and the inner average dimension D of the lower flow path of the nozzle body and the minimum internal dimension d of the flow path of the discharge section The ratio d / D is 0.2 or more and less than 0.8 and the inner dimension of the upper end of the flow path of the discharge part is smaller than the inner dimension of the lower flow path of the nozzle body, and the inner dimension of the flow path of the discharge part The dimension is constant from the upper end to the lower end , and at least two or more discharge ports are provided in the upper and lower sides on the side wall of the discharge unit directed to the short side of the mold, and the cross-sectional area of the discharge port provided on the lower side via a small porous immersion nozzle than the cross-sectional area of the discharge port provided on the upper side, said mold The molten steel pouring, a continuous casting method withdrawn from the mold while solidifying the molten steel at 0.6 m / min or more casting speed,
The distance x from the upper end of the discharge unit to the inner upper end of the uppermost discharge port among the discharge ports is 0.1d <x <5d, from the meniscus of the molten steel in the mold to the outer upper end of the uppermost discharge port The distance L is set to 1.5D <L−x ≦ 20D, the inclination angle of the axis of each discharge port is set in a range of 10 ° upward to 45 ° downward with respect to the horizontal state, and the discharge unit is The molten steel is immersed in the molten steel in the mold within a range of 150 to 350 mm from the meniscus position of the molten steel in the mold, and the amount of argon gas blown is 0.2 to 20 normal liters / minute .

本発明に係る多孔浸漬ノズル及びこれを用いた連続鋳造方法においては、鋳型内に浸漬される吐出部からの溶鋼の吐出流を緩慢、かつ均一な流れにでき、形成される溶鋼の下向き流を弱く、しかも、偏流のない均一な流れにできる。これにより、下向き流の減衰と均一化によって鋳片深部へ侵入する気泡や介在物を減少させることができ、鋳片の欠陥を防止できる。
特に、本発明に係る多孔浸漬ノズルでは、鋳型内の溶鋼のメニスカスから最上部の吐出口の外側上端までの距離Lと、吐出部の上端から最上部の吐出口の内側上端までの距離xの間に、0.1d<x<5dかつ1.5D<L−x≦20Dの関係が成立、側壁の上下に少なくとも2以上の吐出口を設けて下側に設けられた吐出口の断面積を上側に設けられた吐出口の断面積よりも小さくしているので、鋳型内で極端な上向きの吐出流の発生を抑制でき、湯面の変動を回避してパウダーの巻き込みなどの欠陥の発生を防止し、湯面近傍への熱供給を適正にして安定した鋳造が可能になる。そして、鋳片の凝固殻の内側面のウォッシング効果が積極的に発現して、凝固殻に捕捉される気泡や介在物を速やかに浮上させて、表層部の欠陥を減少することができる。更に、吐出流を緩慢にできるので、高速鋳造が可能になり、鋳造の生産性を向上できる。従って、気泡や介在物による欠陥を防止した高品質の鋳片を効率的、かつ経済的に製造できる。
In the porous immersion nozzle and the continuous casting method using the same according to the present invention, the discharge flow of the molten steel from the discharge portion immersed in the mold can be made slow and uniform, and the downward flow of the molten steel to be formed can be reduced. A weak and uniform flow with no drift can be achieved. Thereby, the bubble and inclusion which penetrate | invade into a slab deep part can be reduced by attenuation | damping and equalization of a downward flow, and the defect of a slab can be prevented.
In particular, the porous immersion nozzle according to the present invention, the distance L from the meniscus of the molten steel in the mold to the outer upper end of the top of the discharge port, from the upper end of the discharge portion of the distance x to the inner upper end of the uppermost discharge port during the cross-sectional area of 0.1d <x <5d and 1.5D <L-x ≦ 20D relationship is satisfied, a discharge port provided on the lower side provided with at least two discharge ports at the top and bottom of the side wall the since smaller comb than the cross-sectional area of the discharge port provided on the upper side, can in suppressing the occurrence of extreme upward discharge flow in the mold, to avoid fluctuations in the molten metal surface defects, such as entrainment of powder Occurrence is prevented, and stable casting can be performed by appropriately supplying heat to the vicinity of the molten metal surface. And the washing effect of the inner surface of the solidified shell of the slab is positively expressed, and bubbles and inclusions trapped in the solidified shell can be promptly floated to reduce defects in the surface layer portion. Furthermore, since the discharge flow can be made slow, high-speed casting becomes possible, and casting productivity can be improved. Therefore, it is possible to efficiently and economically manufacture a high quality slab in which defects due to bubbles and inclusions are prevented.

また、吐出部の横断面の外形が矩形である場合では、各吐出口からの吐出量のばらつきを小さくすることができ、均一な流れを形成することが可能になる。各吐出口に溶鋼の流れを誘導可能なひさし部が設けられている場合では、ひさし部により吐出口から吐出する溶鋼の拡散を抑制して均一な流れにすることができ、気泡や介在物による欠陥を防止した高品質の鋳片を効率的、かつ経済的に安定して製造することが可能になる。ノズル本体の下部を除く部分に流路断面積が縮小する絞り部が設けられている場合では、ノズル本体内に落下する溶鋼の落下エネルギーを絞り部で吸収して従来発生していた吐出流の偏流を抑制でき、良好な品質を備えた鋳片を製造することが可能になる。ノズル本体の下部を除く部分に溶鋼を通過させる複数の貫通孔を備えた整流部材が設けられている場合では、ノズル本体内に落下する溶鋼の落下エネルギーを整流部材で吸収し、しかも整流部材の各貫通孔によって整流部材を通過する溶鋼の落下流を均一化でき、従来発生していた吐出流の偏流を更に抑制することが可能になると共に、良好な品質を備えた鋳片を製造することが可能になる。
そして、少なくとも吐出部の流路及び吐出口の周囲がそれぞれカルシアを含有する耐火物及びドロマイトクリンカーを含有する耐火物のいずれか一方又は双方で構成されている場合では、アルミナ系の介在物が耐火物に付着しても介在物と耐火物中のカルシアが反応して界面に低融点化合物を形成するので、介在物が溶鋼によって下流側へ流され従来のようなアルミナ系介在物による小孔の孔詰まりを防止することが可能になる。その結果、吐出量のばらつきを減少させて製造する鋳片の品質を向上できる。
Further, when the outer shape of the cross section of the discharge portion is rectangular, the variation in the discharge amount from each discharge port can be reduced, and a uniform flow can be formed. In the case where each discharge port is provided with an eaves portion capable of guiding the flow of molten steel, the eaves portion can suppress the diffusion of the molten steel discharged from the discharge port and can make a uniform flow. It becomes possible to produce a high-quality slab in which defects are prevented efficiently and economically stably. In the case where a throttle part that reduces the cross-sectional area of the flow path is provided in the part other than the lower part of the nozzle body, the energy of the molten steel falling into the nozzle body is absorbed by the throttle part and the discharge flow that has been generated in the past is absorbed. It is possible to suppress drift and manufacture a slab having good quality. In the case where a rectifying member having a plurality of through-holes through which molten steel passes is provided in a portion other than the lower part of the nozzle body, the rectifying member absorbs the falling energy of the molten steel falling into the nozzle body, and the rectifying member The flow of molten steel passing through the flow straightening member can be made uniform by each through hole, and it is possible to further suppress the uneven flow of the discharge flow that has been generated in the past, and to produce a slab having good quality Is possible.
In the case where at least the flow path of the discharge section and the periphery of the discharge port are each composed of one or both of a refractory containing calcia and a refractory containing dolomite clinker, the alumina inclusions are refractory. Even if it adheres to the object, the inclusion and calcia in the refractory react to form a low melting point compound at the interface. It becomes possible to prevent clogging of holes. As a result, it is possible to improve the quality of the slab manufactured by reducing the variation in the discharge amount.

更に、本発明に係る多孔浸漬ノズルを用いた連続鋳造方法では、多孔浸漬ノズルの各吐出口の軸心の傾斜角度を水平状態に対して上向き10°から下向き45°の範囲に設定し、吐出部を鋳型内の溶鋼のメニスカス位置から150〜350mmの範囲で鋳型中の溶鋼に浸漬させ、アルゴンガスの吹き込み量を0.2〜20ノルマルリットル/分にするので、吐出口から吐出する溶鋼の上向き流及び下向き流の速度を抑制することができ、上向き流に起因する湯面変動やパウダー巻き込みによる欠陥、下向き流に起因する気泡や介在物の鋳片深部への侵入を抑制することができ、高品質の鋳片を製造することが可能になる。しかも、溶鋼の吐出流の偏流が無いので、広い範囲の吐出部角度での鋳造が可能になり、同時に浸漬深さをメニスカス位置から150〜350mmの範囲にして、安定した高速鋳造が可能になり、生産性を高めることができる。
また、溶鋼中にカルシウムが添加されている場合では、生成すアルミナ系介在物を低融点化することができ、吐出口の詰まりを抑制して、安定した鋳造を行うことが可能になる。
Furthermore, in the continuous casting method using a porous immersion nozzle according to the present invention, set in the range of downward 45 ° from upward 10 ° inclination angle of the axis of each outlet of the porous immersion nozzle with respect to the horizontal state, the discharge parts was immersed in molten steel in the mold in the range of 150~350mm from the meniscus position of the molten steel in the mold, so that the blowing amount of the argon gas to 0.2 to 20 normal liters / minute, the molten steel to be discharged from the discharge port It is possible to suppress the speed of upward and downward flows, and to suppress defects caused by fluctuations in the molten metal surface and powder entrainment due to upward flows, and penetration of bubbles and inclusions due to downward flow into the slab. It becomes possible to manufacture high quality slabs. Moreover, since there is no drift in the discharge flow of molten steel, casting at a wide range of discharge part angles is possible, and at the same time, the immersion depth is set within the range of 150 to 350 mm from the meniscus position, enabling stable high-speed casting. , Can increase productivity.
Further, when calcium is added to the molten steel, it is possible to lower the melting point of the generated alumina inclusions, and it is possible to perform stable casting while suppressing clogging of the discharge port.

続いて、添付した図面を参照しつつ、本発明を具体化した実施の形態につき説明し、本発明の理解に供する。
ここに、図1は本発明の第1の実施の形態に係る多孔浸漬ノズルの側断面図、図2は同多孔浸漬ノズルを用いた連続鋳造方法の説明図、図3(A)は同多孔浸漬ノズルの使用状態を示す側断面図、(B)は(A)のP−P矢視断面図、図4(A)は従来例に係る浸漬ノズルの使用状態を示す側断面図、(B)は(A)のQ−Q矢視断面図、図5は本発明の第2の実施の形態に係る多孔浸漬ノズルの側断面図、図6は本発明の第3の実施の形態に係る多孔浸漬ノズルの側断面図、図7は本発明の第4の実施の形態に係る多孔浸漬ノズルの側断面図、図8は本発明の第5の実施の形態に係る多孔浸漬ノズルの側断面図である。
Next, embodiments of the present invention will be described with reference to the accompanying drawings for understanding of the present invention.
1 is a side sectional view of the porous immersion nozzle according to the first embodiment of the present invention, FIG. 2 is an explanatory view of a continuous casting method using the porous immersion nozzle, and FIG. FIG. 4B is a side sectional view showing the usage state of the immersion nozzle, FIG. 4B is a sectional view taken along the line PP of FIG. 4A, and FIG. 4A is a side sectional view showing the usage state of the immersion nozzle according to the conventional example. ) Is a cross-sectional view taken along the line Q-Q of (A), FIG. 5 is a side cross-sectional view of a porous immersion nozzle according to the second embodiment of the present invention, and FIG. 6 is according to the third embodiment of the present invention. 7 is a sectional side view of a porous immersion nozzle according to a fourth embodiment of the present invention, and FIG. 8 is a sectional side view of a porous immersion nozzle according to a fifth embodiment of the present invention. FIG.

図1、図2に示すように、本発明の第1の実施の形態に係る多孔浸漬ノズル10は、溶鋼19が上から下に通過する筒状のノズル本体11と、ノズル本体11の下端に連設して設けられ、鋳型22内に浸漬される吐出部12とを有している。ここで、吐出部12の流路13の断面積は、ノズル本体11の下部流路14の断面積に比較して小さくなっている。そして、下部流路14の内径(内平均寸法)Dと、吐出部12の流路13の内径(最小内寸法)dとの比d/Dが0.8未満である。従って、下部流路14と吐出部12の流路13との接続部には段差が発生している。 As shown in FIGS. 1 and 2, the porous immersion nozzle 10 according to the first embodiment of the present invention has a cylindrical nozzle body 11 through which molten steel 19 passes from the top to the bottom, and a lower end of the nozzle body 11. It has the discharge part 12 provided in a row and immersed in the mold 22. Here, the cross-sectional area of the flow path 13 of the discharge unit 12 is smaller than the cross-sectional area of the lower flow path 14 of the nozzle body 11. The ratio d / D between the inner diameter (inner average dimension) D of the lower flow path 14 and the inner diameter (minimum inner dimension) d of the flow path 13 of the discharge unit 12 is less than 0.8. Accordingly, a step is generated at the connection portion between the lower flow path 14 and the flow path 13 of the discharge section 12.

また、吐出部12の横断面の外形は矩形で、鋳型22の短辺側を指向する吐出部12の各側壁15、16にはそれぞれ上下に、例えば、2個の吐出口17、18が設けられている。更に、下側に設けられた吐出口18の内寸法は上側に設けられた吐出口17の内寸法よりも小さく形成されており、吐出口18の断面積は吐出口17の断面積よりも小さくなっている。更に、各吐出口17、18の軸心の傾斜角度α、βが、それぞれ水平に対して上向き10°から下向き45°以内に設定されている(図1では、各吐出口17、18の軸心の傾斜角度α、βが、それぞれ水平に対して上向きに形成されている場合を示している)。なお、吐出部12の流路13の内寸法は上端から下端まで一定である。 Further, the outer shape of the cross section of the discharge unit 12 is rectangular, and for example, two discharge ports 17 and 18 are provided on the respective side walls 15 and 16 of the discharge unit 12 directed to the short side of the mold 22 in the vertical direction. It has been. Furthermore, the inner dimension of the discharge port 18 provided on the lower side is formed smaller than the inner dimension of the discharge port 17 provided on the upper side, and the cross-sectional area of the discharge port 18 is smaller than the cross-sectional area of the discharge port 17. It has become. Further, the inclination angles α and β of the axial centers of the discharge ports 17 and 18 are set within 10 ° upward and 45 ° downward with respect to the horizontal (in FIG. 1, the axes of the discharge ports 17 and 18 are set). The case where the inclination angles α and β of the heart are formed upward with respect to the horizontal is shown). In addition, the internal dimension of the flow path 13 of the discharge part 12 is constant from the upper end to the lower end.

このような構成とすることにより、溶鋼19をノズル本体11から吐出部12に供給する際、下部流路14と吐出部12の流路13との接続部に存在する段差により溶鋼流が絞られて、吐出部12による圧損を溶鋼19に付与することができ、溶鋼19の高さ方向の圧力差によって上下の吐出口17、18を通過する流量バランスが崩れるのを抑制することができ、各吐出口17、18から吐出する吐出流の緩慢化及び均一化を図って溶鋼19を鋳型22内に吐出できる。
なお、下部流路14の内径Dと、吐出部12の流路13の内径dとの比d/Dが0.8以上になると、ノズル本体11の下部流路14を通過する溶鋼19の下降流が吐出部12内の溶鋼19に直接作用して、各吐出口17、18から吐出する吐出流の緩慢化及び均一化を図ることが困難になる。また、d/Dの下限値は0.2、好ましくは0.4である。d/Dが0.2未満では、吐出部12による圧損が大きくなり過ぎて所定の溶鋼流量を確保することが困難になる。
With such a configuration, when the molten steel 19 is supplied from the nozzle body 11 to the discharge portion 12, the molten steel flow is restricted by the step existing at the connection portion between the lower flow path 14 and the flow path 13 of the discharge section 12. Thus, the pressure loss due to the discharge part 12 can be applied to the molten steel 19, and the flow rate balance passing through the upper and lower discharge ports 17 and 18 can be prevented from being broken by the pressure difference in the height direction of the molten steel 19, The molten steel 19 can be discharged into the mold 22 by slowing and equalizing the discharge flow discharged from the discharge ports 17 and 18.
When the ratio d / D between the inner diameter D of the lower flow path 14 and the inner diameter d of the flow path 13 of the discharge unit 12 becomes 0.8 or more, the molten steel 19 passing through the lower flow path 14 of the nozzle body 11 descends. It becomes difficult for the flow to act directly on the molten steel 19 in the discharge section 12 to slow down and make uniform the discharge flow discharged from the discharge ports 17 and 18. The lower limit of d / D is 0.2, preferably 0.4. When d / D is less than 0.2, the pressure loss due to the discharge section 12 becomes too large, and it becomes difficult to ensure a predetermined molten steel flow rate.

ここで、吐出部12の上端から上側の吐出口17の内側上端までの距離xが、流路13の最小内径(内径)dに対して0.1d<x<5dを満たすように形成されている。そして、鋳型22内の溶鋼19のメニスカスから上側の吐出口17の外側上端までの距離Lを、1.5D<L−xの関係が満たされるようにすることで、溶鋼19をノズル本体11から吐出部12に供給する際、吐出部12による圧損を溶鋼19に確実に付与することができ、溶鋼19の高さ方向の圧力差によって上下の吐出口17、18を通過する流量バランスが崩れるのを抑制することができ、各吐出口17、18から吐出する吐出流の緩慢化及び均一化を図って溶鋼19を鋳型22内に吐出できる。 Here, the distance x from the upper end of the discharge part 12 to the inner upper end of the upper discharge port 17 is formed so as to satisfy 0.1d <x <5d with respect to the minimum inner diameter (inner diameter) d of the flow path 13. Yes. The distance L from the meniscus of the molten steel 19 in the mold 22 to the outer upper end of the upper discharge port 17 is made to satisfy the relationship of 1.5D <Lx, so that the molten steel 19 is removed from the nozzle body 11. When supplying to the discharge part 12, the pressure loss by the discharge part 12 can be reliably given to the molten steel 19, and the flow rate balance which passes the upper and lower discharge ports 17 and 18 by the pressure difference of the height direction of the molten steel 19 collapses. Therefore, the molten steel 19 can be discharged into the mold 22 by slowing and equalizing the discharge flow discharged from the discharge ports 17 and 18.

なお、xが0.1d以下の場合、溶鋼が吐出口17に到るまでに通過する流路13内の距離が短かいため、溶鋼流動が不安定になり吐出口17、18から吐出する吐出流を緩慢化かつ均一にできない。また、xが5d以上の場合、溶鋼中の圧損が回復して、吐出口17、18から吐出する吐出流を緩慢化かつ均一にできない。更に、L−xが1.5D以下の場合、ノズル本体11内の溶鋼の影響を受けて吐出流を緩慢化かつ均一化できない。一方、L−xの上限値については規定していないが、多孔浸漬ノズル10の浸漬深さと鋳型22内部への浸漬方法を考慮すると、20D以下にすることが好ましい。
更に、各吐出口17、18の軸心の傾斜角度α、βを水平に対して上向き10°から下向き45°の範囲に設定することにより、各吐出口17、18から吐出する溶鋼19の上向き流及び下向き流の速度を調整することができ、上向き流に起因する湯面変動やパウダー巻き込みによる欠陥、下向き流に起因する気泡や介在物の鋳片深部への侵入を抑制することができる。
In addition, when x is 0.1 d or less, since the distance in the flow path 13 through which the molten steel reaches the discharge port 17 is short, the molten steel flow becomes unstable and the discharge discharged from the discharge ports 17 and 18 The flow cannot be slowed and made uniform. Moreover, when x is 5d or more, the pressure loss in molten steel recovers, and the discharge flow discharged from the discharge ports 17 and 18 cannot be made slow and uniform. Furthermore, when Lx is 1.5 D or less, the discharge flow cannot be slowed down and made uniform under the influence of the molten steel in the nozzle body 11. On the other hand, although the upper limit value of Lx is not defined, in consideration of the immersion depth of the porous immersion nozzle 10 and the method of immersion in the mold 22, it is preferably 20 D or less.
Further, by setting the inclination angles α and β of the axial centers of the discharge ports 17 and 18 in the range of 10 ° upward to 45 ° downward with respect to the horizontal, the upward direction of the molten steel 19 discharged from the discharge ports 17 and 18 is increased. The velocity of the flow and the downward flow can be adjusted, and defects caused by fluctuations in the molten metal surface caused by the upward flow and powder entrainment, and intrusion of bubbles and inclusions due to the downward flow into the slab can be suppressed.

吐出部12の流路13及び吐出口17、18の周囲は、それぞれドロマイトクリンカーを含有する耐火物で構成されており、流路13の終端部には、例えば、アルミナ黒鉛質耐火物で構成された底部20がジルコニア系のモルタルを介して設けられている。ここで、ドロマイトクリンカーを含有する耐火物とは、例えば、CaO成分の含有量W1 とMgO成分の含有量W2 との質量比W1 /W2 が0.46〜3.0であって、しかもMgO成分が30〜70質量%含まれたものである。なお、この耐火物中には、炭素成分が1質量%以下含有されている。また、CaO成分及びMgO成分を除いた残部成分の含有量W3 に対するCaO成分の含有量W1 の質量比W1 /W3 が2〜30で、特に、残部成分中のSiO2 及びFe23 の各含有率が、それぞれ3質量%以下、更には1質量%以下になるように調整されている。
また、ノズル本体11は、従来から使用されている浸漬ノズル用の耐火物、例えばアルミナ黒鉛質耐火物を用いて形成することができる。なお、アルミナ黒鉛質耐火物とドロマイトとは反応するため、ノズル本体11と吐出部12とはジルコニア系のモルタルを介して接続されている。また、ノズル本体11をジルコニア黒鉛質耐火物で構成することも可能で、この場合は吐出部12をノズル本体11に直接接続できる。
The periphery of the flow path 13 and the discharge ports 17 and 18 of the discharge section 12 is made of a refractory containing dolomite clinker, and the end of the flow path 13 is made of, for example, an alumina graphite refractory. The bottom 20 is provided through zirconia mortar. Here, the refractory material containing dolomite clinker, for example, the weight ratio W 1 / W 2 between the content W 2 content W 1 and MgO components of CaO component is a 0.46 to 3.0 And 30 to 70 mass% of MgO components are contained. In addition, in this refractory material, 1 mass% or less of carbon components are contained. Further, the mass ratio W 1 / W 3 of the content W 1 of the CaO component to the content W 3 of the remaining component excluding the CaO component and the MgO component is 2 to 30, in particular, SiO 2 and Fe 2 in the remaining component. Each content of O 3 is adjusted to be 3% by mass or less, and further 1% by mass or less.
The nozzle body 11 can be formed using a conventionally used refractory material for an immersion nozzle, such as an alumina graphite refractory material. Since the alumina graphite refractory and dolomite react, the nozzle body 11 and the discharge part 12 are connected via a zirconia mortar. In addition, the nozzle body 11 can be made of zirconia graphite refractory. In this case, the discharge part 12 can be directly connected to the nozzle body 11.

続いて、本発明の第1の実施の形態に係る多孔浸漬ノズル10を用いた連続鋳造方法について説明する。
図2に示すように、溶鋼19をタンディッシュ21に入れ、更にタンディッシュ21の下方に設けた多孔浸漬ノズル10を介して鋳型22に注湯した。なお、鋳型22は、横断面の外形及び内形が共に矩形であり、例えば、内形の寸法は250mm×1000〜1800mmである。そして、鋳型22による冷却と支持セグメント23に設けた図示しない冷却水ノズルからの散水による冷却によって、凝固殻(凝固シェル)24を生成させ、凝固殻24の成長を促進しながら、軽圧下セグメント25の複数の図示しない押圧ロールによって圧下を行い、ピンチロール26により0.6m/min以上の鋳造速度で鋳型22から引き抜き、鋳片27を鋳造する。
ここで、鋳造速度を0.6m/min以上にすることにより、鋳片の表層や内部に欠陥のない鋳片を製造できるが、生産性をより高め、鋳片を高温度で加熱炉等の後工程に供給して熱エネルギーを有効に活用するためには、鋳造速度を0.8m/min以上にすることが好ましく、更には1m/min以上にすることが好ましい。一方、鋳造速度の上限値については規定していないが、溶鋼の凝固を行なう連続鋳造設備の冷却能力を考慮すれば、例えば、3m/min以下の鋳造速度で鋳造するのがよい。
Then, the continuous casting method using the porous immersion nozzle 10 which concerns on the 1st Embodiment of this invention is demonstrated.
As shown in FIG. 2, molten steel 19 was put in a tundish 21 and further poured into a mold 22 through a porous immersion nozzle 10 provided below the tundish 21. Note that the outer shape and the inner shape of the mold 22 are both rectangular, and for example, the inner shape has a dimension of 250 mm × 1000 to 1800 mm. Then, a solidified shell (solidified shell) 24 is generated by cooling by the mold 22 and cooling by sprinkling water from a cooling water nozzle (not shown) provided in the support segment 23, and while promoting the growth of the solidified shell 24, the lightly pressed segment 25 A plurality of pressing rolls (not shown) are used for reduction, and the pinch roll 26 is pulled out from the mold 22 at a casting speed of 0.6 m / min or more to cast a cast piece 27.
Here, by setting the casting speed to 0.6 m / min or more, it is possible to produce a slab having no defects in the surface layer or inside of the slab, but the productivity is further improved, and the slab is heated at a high temperature such as a heating furnace. In order to use the thermal energy effectively by supplying it to the subsequent process, the casting speed is preferably 0.8 m / min or more, and more preferably 1 m / min or more. On the other hand, although the upper limit value of the casting speed is not defined, it is preferable to cast at a casting speed of 3 m / min or less, for example, considering the cooling capacity of a continuous casting facility for solidifying molten steel.

多孔浸漬ノズル10は、図3(A)、(B)に示すように、鋳型22の短辺側に、吐出口17、18が設けられた側壁15、16が対向するように鋳型22内に浸漬されている。また、多孔浸漬ノズル10は、上側の吐出口17の上端部が、例えば鋳型22内の溶鋼19のメニスカス(湯面)位置から150〜350mmの範囲の深さで、鋳型22中の溶鋼19に浸漬するように配置し固定されている。更に、多孔浸漬ノズル10中に、アルゴンガスを吹き込む場合は、アルゴンガス量を、例えば0.2〜20ノルマルリットル/分に調整する。なお、アルゴンガスをタンディッシュ21に設けられた上ノズル、スライディングノズル(SN)プレート、及び多孔浸漬ノズル10に設けたスリットを介してそれぞれ吹き込むようにする場合、その総量が0.2〜20ノルマルリットル/分となるように調整する。 As shown in FIGS. 3A and 3B, the porous immersion nozzle 10 is placed in the mold 22 so that the side walls 15 and 16 provided with the discharge ports 17 and 18 face the short side of the mold 22. Soaked. Further, the upper end of the upper discharge port 17 has a depth in the range of 150 to 350 mm from the meniscus (molten metal surface) position of the molten steel 19 in the mold 22, for example, to the molten steel 19 in the mold 22. It is arranged and fixed so as to be immersed. Furthermore, when argon gas is blown into the porous immersion nozzle 10, the amount of argon gas is adjusted to, for example, 0.2 to 20 normal liters / minute. When argon gas is blown through the upper nozzle provided in the tundish 21, the sliding nozzle (SN) plate, and the slit provided in the porous immersion nozzle 10, the total amount is 0.2 to 20 normal. Adjust to 1 / min.

ここで、各吐出口17、18から鋳型22内へ溶鋼19を吐出させた場合、溶鋼19中のAlから生成したAl23 は、各吐出口17、18の内側面である稼動面28に付着するが、付着したAl23 がドロマイトクリンカー内のCaOと反応して低融点のAl23 −CaO系液相が形成される。ここで、CaO成分の含有量W1 とMgO成分の含有量W2 との質量比W1 /W2 が0.46〜3.0であって、しかもMgO成分が30〜70質量%含有されるようにしているため、過剰なAl23 −CaO系液相の形成が抑えられる。また、ドロマイトクリンカーの結晶粒子の粒界にSiO2 及びFe23 が存在することで、ドロマイトクリンカーの消化を抑えると共に、ドロマイトクリンカー内のCaOと反応して低融点の化合物を形成し、CaOの移動を活発化させてCaOの反応性を向上させることができる。更に、Al23 −CaO系液相の形成に伴って稼動面28の内部に形成されるMgOリッチな層により、稼動面側の耐食性を向上できる。 Here, when the molten steel 19 is discharged from the discharge ports 17 and 18 into the mold 22, the Al 2 O 3 generated from Al in the molten steel 19 is the working surface 28 that is the inner surface of the discharge ports 17 and 18. However, the attached Al 2 O 3 reacts with CaO in the dolomite clinker to form an Al 2 O 3 —CaO-based liquid phase having a low melting point. Here, a weight ratio W 1 / W 2 between the content W 2 content W 1 and MgO components of CaO component from 0.46 to 3.0, moreover MgO component is contained 30 to 70 wt% Therefore, the formation of an excessive Al 2 O 3 —CaO-based liquid phase can be suppressed. In addition, the presence of SiO 2 and Fe 2 O 3 at the grain boundaries of the dolomite clinker crystal particles suppresses the digestion of the dolomite clinker and reacts with CaO in the dolomite clinker to form a low-melting compound. It is possible to improve the reactivity of CaO by activating the movement of. Furthermore, the corrosion resistance on the operating surface side can be improved by the MgO-rich layer formed inside the operating surface 28 along with the formation of the Al 2 O 3 —CaO-based liquid phase.

これにより、図3に示すように、鋳型22内に形成される各吐出口17、18からの溶鋼19の吐出流を緩慢、かつ均一な流れにでき、形成される溶鋼19の下向き流を弱く、しかも、偏流のない均一な流れにできる。また、極端に偏流した上向きの吐出流の発生を抑制できるので、湯面の変動を回避してパウダーの巻き込みなどの欠陥の発生を防止し、湯面近傍への熱供給を適正にして、安定した鋳造が可能になる。
一方、図4(A)、(B)に示すように、溶鋼19を鋳型22の短辺側に向けて吐出する1対の吐出口30、31を有底の筒状のノズル本体29の下部に設けた従来の浸漬ノズル32を使用した場合、各吐出口30、31から吐出する溶鋼19の流れが凝固殻の内面に衝突し、反転する上向き流及び下向き流が発生する。これにより、上向き流による湯面の変動やパウダー巻き込みが生じ、また強い下向き流に随伴する気泡や介在物が鋳片の深部に侵入するため、鋳片内部の気泡や介在物に起因する欠陥を防止できず、鋳片の品質低下を招いたり、鋳片を安定に製造できない問題が発生する。
以上のことから、第1の実施の形態に係る多孔浸漬ノズル10を使用することで、アルミナ系介在物による各吐出口17、18の孔詰まりを防止し、各吐出口17、18からの溶鋼19の吐出流の偏流を抑制し、更には防止して、高品質の鋳片27を製造できる。また、溶鋼19中にカルシウム(Ca)を添加して、例えば、カルシウム濃度を5〜50ppmにすることにより、前記した効果をより顕著に発現することができる。
Thereby, as shown in FIG. 3, the discharge flow of the molten steel 19 from each discharge port 17 and 18 formed in the casting_mold | template 22 can be made into a slow and uniform flow, and the downward flow of the molten steel 19 formed is weakened. Moreover, the flow can be made uniform without drift. In addition, it is possible to suppress the occurrence of extremely uneven upward discharge flow, avoiding fluctuations in the molten metal surface, preventing the occurrence of defects such as powder entrainment, and making the heat supply close to the molten metal surface stable. Casting becomes possible.
On the other hand, as shown in FIGS. 4 (A) and 4 (B), a pair of discharge ports 30 and 31 for discharging the molten steel 19 toward the short side of the mold 22 are provided at the bottom of the bottomed cylindrical nozzle body 29. When the conventional immersion nozzle 32 provided in is used, the flow of the molten steel 19 discharged from the discharge ports 30 and 31 collides with the inner surface of the solidified shell, and an upward flow and a downward flow that are reversed are generated. This causes fluctuations in the molten metal surface and powder entrainment due to the upward flow, and bubbles and inclusions accompanying the strong downward flow penetrate into the deep part of the slab, so that defects caused by bubbles and inclusions inside the slab are eliminated. There are problems that cannot be prevented and that the quality of the slab is reduced or that the slab cannot be manufactured stably.
From the above, by using the porous immersion nozzle 10 according to the first embodiment, the clogging of the discharge ports 17 and 18 due to the alumina inclusions is prevented, and the molten steel from the discharge ports 17 and 18 is prevented. High quality cast slab 27 can be manufactured by suppressing and further preventing the uneven flow of 19 discharge flows. Moreover, by adding calcium (Ca) to the molten steel 19 and setting the calcium concentration to 5 to 50 ppm, for example, the effects described above can be expressed more remarkably.

図5に示すように、本発明の第2の実施の形態に係る多孔浸漬ノズル33は、本発明の第1の実施の形態に係る多孔浸漬ノズル10と比較して、下部流路14と吐出部34の流路35の接続部において下部流路14の内径と吐出部34の流路35の内径が実質的に同一で、吐出部34の流路35の内径が吐出部34の上端から下端に向けて徐々に減少していることが特徴となっている。このため、同一の構成部材には同一の符号を付して詳細な説明は省略する。
このような構成とすることにより、溶鋼19をノズル本体11から吐出部34に供給する際、下部流路14から吐出部34の流路35内に侵入した溶鋼19は流路35の側壁に接触することにより溶鋼流の流れが妨げられ、吐出部34による圧損を溶鋼19に付与することができ、溶鋼19の高さ方向の圧力差によって上下の吐出口17、18を通過する流量バランスが崩れるのを抑制することができ、各吐出口17、18から吐出する吐出流の緩慢化及び均一化を図って溶鋼19を鋳型22内に吐出できる。なお、第2の実施の形態に係る多孔浸漬ノズル33を用いた連続鋳造方法は、第1の実施の形態に係る多孔浸漬ノズル10を用いた連続鋳造方法と同一に行なうことができるので、説明は省略する。
As shown in FIG. 5, the porous immersion nozzle 33 according to the second embodiment of the present invention has a lower flow path 14 and a discharge rate compared to the porous immersion nozzle 10 according to the first embodiment of the present invention. The inner diameter of the lower flow path 14 and the inner diameter of the flow path 35 of the discharge section 34 are substantially the same at the connection portion of the flow path 35 of the section 34, and the inner diameter of the flow path 35 of the discharge section 34 is lower than the upper end of the discharge section 34. It is characterized by a gradual decrease toward For this reason, the same code | symbol is attached | subjected to the same structural member and detailed description is abbreviate | omitted.
With this configuration, when the molten steel 19 is supplied from the nozzle body 11 to the discharge part 34, the molten steel 19 that has entered the flow path 35 of the discharge part 34 from the lower flow path 14 contacts the side wall of the flow path 35. By doing so, the flow of the molten steel flow is hindered, and pressure loss due to the discharge part 34 can be imparted to the molten steel 19, and the flow rate balance passing through the upper and lower discharge ports 17, 18 is disrupted by the pressure difference in the height direction of the molten steel 19. Therefore, the molten steel 19 can be discharged into the mold 22 by slowing and equalizing the discharge flow discharged from the discharge ports 17 and 18. The continuous casting method using the porous immersion nozzle 33 according to the second embodiment can be performed in the same manner as the continuous casting method using the porous immersion nozzle 10 according to the first embodiment. Is omitted.

図6に示すように、本発明の第3の実施の形態に係る多孔浸漬ノズル36は、本発明の第1の実施の形態に係る多孔浸漬ノズル10と比較して、ノズル本体37の内部に存在する溶鋼19の湯面位置39(二次メニスカス位置)より、例えば、50〜300mm上方のノズル本体37の内周部に、その内径Sがノズル本体37の内径Dよりも小さな絞り部40(例えば、D/2≦S<D)が設けられていることが特徴となっている。このため、同一の構成部材には同一の符号を付して詳細な説明は省略する。
これにより、落下する溶鋼19を絞り部40の段差部分に衝突させ、溶鋼19の落下エネルギーを減衰することができ、吐出部12による圧損を溶鋼19に付与することができ、溶鋼19の下部流路38の高さ方向における圧力差によって上下の吐出口17、18を通過する流量バランスが崩れるのを抑制することができ、各吐出口17、18から吐出する吐出流の緩慢化及び均一化を図って溶鋼19を鋳型22内に吐出できる。なお、第3の実施の形態に係る多孔浸漬ノズル36を用いた連続鋳造方法は、第1の実施の形態に係る多孔浸漬ノズル10を用いた連続鋳造方法と同一に行なうことができるので、説明は省略する。
As shown in FIG. 6, the porous immersion nozzle 36 according to the third embodiment of the present invention is provided inside the nozzle body 37 as compared with the porous immersion nozzle 10 according to the first embodiment of the present invention. From the molten metal surface position 39 (secondary meniscus position) of the molten steel 19, for example, on the inner peripheral portion of the nozzle body 37 50 to 300 mm above, the throttle portion 40 (with an inner diameter S smaller than the inner diameter D of the nozzle body 37). For example, D / 2 ≦ S <D) is provided. For this reason, the same code | symbol is attached | subjected to the same structural member and detailed description is abbreviate | omitted.
As a result, the falling molten steel 19 can collide with the stepped portion of the throttle portion 40, the falling energy of the molten steel 19 can be attenuated, the pressure loss due to the discharge portion 12 can be imparted to the molten steel 19, and the lower flow of the molten steel 19 It is possible to prevent the flow rate balance passing through the upper and lower discharge ports 17 and 18 from being lost due to the pressure difference in the height direction of the passage 38, and to slow down and equalize the discharge flow discharged from the discharge ports 17 and 18. As a result, the molten steel 19 can be discharged into the mold 22. The continuous casting method using the porous immersion nozzle 36 according to the third embodiment can be performed in the same manner as the continuous casting method using the porous immersion nozzle 10 according to the first embodiment. Is omitted.

図7に示すように、本発明の第4の実施の形態に係る多孔浸漬ノズル41は、本発明の第1の実施の形態に係る多孔浸漬ノズル10と比較して、ノズル本体42の内部に存在する溶鋼19の湯面位置44(二次メニスカス位置)より、例えば、50〜300mm上方のノズル本体42の内周部に、整流部材45が設けられていることが特徴となっている。このため、同一の構成部材には同一の符号を付して詳細な説明は省略する。
ここで、整流部材45には複数(例えば、4以上)の貫通孔46が形成されている。そして、整流部材45は、ノズル本体42の内周側に、例えば、5〜10mmの幅で突出させて形成した掛止部47の上面に、その下面を当接させて配置されている。なお、各貫通孔46の内側面が溶鋼19との接触面48となるので、整流部材45を、ドロマイトクリンカーを含有する耐火物で構成することが好ましい。この場合、少なくともノズル本体42の内面側で整流部材45と直接接触する部分には、ジルコニア系のモルタルを使用する。
As shown in FIG. 7, the porous immersion nozzle 41 according to the fourth embodiment of the present invention is provided inside the nozzle body 42 as compared with the porous immersion nozzle 10 according to the first embodiment of the present invention. For example, a rectifying member 45 is provided on the inner peripheral portion of the nozzle body 42 50 to 300 mm above the surface level 44 (secondary meniscus position) of the molten steel 19 present. For this reason, the same code | symbol is attached | subjected to the same structural member and detailed description is abbreviate | omitted.
Here, a plurality of (for example, four or more) through holes 46 are formed in the rectifying member 45. And the rectification | straightening member 45 is arrange | positioned by making the lower surface contact | abut on the inner peripheral side of the nozzle main body 42 with the upper surface of the latching | locking part 47 formed by protruding with the width | variety of 5-10 mm, for example. In addition, since the inner side surface of each through-hole 46 becomes the contact surface 48 with the molten steel 19, it is preferable to comprise the rectification | straightening member 45 with the refractory material containing a dolomite clinker. In this case, zirconia-based mortar is used at least in a portion in direct contact with the rectifying member 45 on the inner surface side of the nozzle body 42.

このような構成とすることにより、多孔浸漬ノズル41内に落下してきた溶鋼19を、多孔浸漬ノズル41内の溶鋼19の湯面に直接衝突させることなく、整流部材45で溶鋼19の落下エネルギーを一旦減衰した後、各貫通孔46で分散させて下部流路43へ均一な流れとして供給できるので、多孔浸漬ノズル41内の湯面位置44の変動を抑制できる。これにより、吐出部12による圧損を溶鋼19に付与することができ、溶鋼19の下部流路43の高さ方向における圧力差によって上下の吐出口17、18を通過する流量バランスが崩れるのを抑制することができ、各吐出口17、18から吐出する吐出流の緩慢化及び均一化を図って溶鋼19を鋳型22内に吐出できる。なお、第4の実施の形態に係る多孔浸漬ノズル41を用いた連続鋳造方法は、第1の実施の形態に係る多孔浸漬ノズル10を用いた連続鋳造方法と同一に行なうことができるので、説明は省略する。 With such a configuration, the molten steel 19 that has fallen into the porous immersion nozzle 41 does not directly collide with the molten metal surface of the molten steel 19 within the porous immersion nozzle 41, and the dropping energy of the molten steel 19 is increased by the rectifying member 45. Since it once attenuate | damps, it can disperse | distribute by each through-hole 46, and since it can supply to the lower flow path 43 as a uniform flow, the fluctuation | variation of the hot_water | molten_metal surface position 44 in the porous immersion nozzle 41 can be suppressed. Thereby, the pressure loss by the discharge part 12 can be given to the molten steel 19, and it is suppressed that the flow volume balance which passes the upper and lower discharge outlets 17 and 18 by the pressure difference in the height direction of the lower flow path 43 of the molten steel 19 is destroyed. The molten steel 19 can be discharged into the mold 22 by slowing down and uniforming the discharge flow discharged from the discharge ports 17 and 18. The continuous casting method using the porous immersion nozzle 41 according to the fourth embodiment can be performed in the same manner as the continuous casting method using the porous immersion nozzle 10 according to the first embodiment. Is omitted.

図8に示すように、本発明の第5の実施の形態に係る多孔浸漬ノズル49は、本発明の第1の実施の形態に係る多孔浸漬ノズル10と比較して、吐出部50に設けられた各吐出口51、52の上部には、各吐出口51、52から吐出した溶鋼19の流れを誘導する平板状のひさし部53、54がそれぞれ設けられていることが特徴となっている。このため、同一の構成部材には同一の符号を付して詳細な説明は省略する。
ここで、ひさし部53、54の傾斜角度γ、δは、水平状態に対して上向き10°から下向き35°の範囲に設定し、上側の吐出口51の上端部が、例えば、鋳型22内の溶鋼19のメニスカス位置から150〜350mmの範囲の深さで、鋳型22中の溶鋼19に浸漬させ、アルゴンガスの吹き込み量を0.2〜20ノルマルリットル/分にする。このように、ひさし部53、54の傾斜角度γ、δ、及び鋳型22内の溶鋼19への多孔浸漬ノズル49の浸漬深さ、及びアルゴンガスの吹き込み量を規定することで、各吐出口51、52から吐出する溶鋼19の上向き流及び下向き流の速度を抑制することができ、上向き流に起因する湯面変動やパウダー巻き込みによる欠陥、下向き流に起因する気泡や介在物の鋳片27深部への侵入を抑制することができる。
As shown in FIG. 8, the porous immersion nozzle 49 according to the fifth embodiment of the present invention is provided in the discharge unit 50 as compared with the porous immersion nozzle 10 according to the first embodiment of the present invention. Further, the upper portions of the discharge ports 51 and 52 are characterized by flat plate eaves portions 53 and 54 for guiding the flow of the molten steel 19 discharged from the discharge ports 51 and 52, respectively. For this reason, the same code | symbol is attached | subjected to the same structural member and detailed description is abbreviate | omitted.
Here, the inclination angles γ and δ of the eaves portions 53 and 54 are set in a range of 10 ° upward to 35 ° downward with respect to the horizontal state, and the upper end portion of the upper discharge port 51 is, for example, in the mold 22. The molten steel 19 is immersed in the molten steel 19 in the mold 22 at a depth in the range of 150 to 350 mm from the meniscus position of the molten steel 19 so that the blowing amount of argon gas is 0.2 to 20 normal liters / minute. As described above, by defining the inclination angles γ and δ of the eaves portions 53 and 54, the immersion depth of the porous immersion nozzle 49 into the molten steel 19 in the mold 22, and the amount of argon gas blown in, the discharge ports 51 are provided. , 52 can suppress the speed of the upward and downward flows of the molten steel 19, and defects due to fluctuations in the molten metal surface and powder entrainment due to the upward flow, bubbles and inclusion slabs 27 due to the downward flow Can be prevented from entering.

ここで、ひさし部53、54の傾斜角度が水平位置に対して上向き10度を超える場合、上向き流による湯面の変動やパウダーの巻き込みを生じる。一方、ひさし部53、54の傾斜角度が水平位置に対して下向き35度を超える場合、下向き流が強くなり、この下向き流に随伴する介在物や気泡が鋳片27の深部に侵入し、鋳片27の内部欠陥の要因になり、高品質の鋳片を製造できない。以上のことから、高品質の鋳片27を製造するためには、ひさし部53、54の傾斜角度を、水平位置に対して上向き5°から下向き20°の範囲とすることが好ましく、更に好ましくは水平位置に対して上向き5°から下向き15°の範囲とすることがよい。なお、第5の実施の形態に係る多孔浸漬ノズル49を用いた連続鋳造方法は、第1の実施の形態に係る多孔浸漬ノズル10を用いた連続鋳造方法と同一に行なうことができるので、説明は省略する。 Here, when the inclination angle of the eaves parts 53 and 54 exceeds 10 degrees upward with respect to the horizontal position, fluctuation of the molten metal surface or entrainment of powder occurs due to the upward flow. On the other hand, when the inclination angle of the eaves portions 53 and 54 exceeds 35 degrees downward with respect to the horizontal position, the downward flow becomes strong, and inclusions and bubbles accompanying the downward flow penetrate into the deep part of the slab 27, and the casting It becomes a factor of the internal defect of the piece 27, and a high quality cast piece cannot be manufactured. From the above, in order to manufacture a high quality slab 27, it is preferable that the inclination angle of the eaves portions 53, 54 is in the range of 5 ° upward to 20 ° downward with respect to the horizontal position, and more preferably Is preferably in the range of 5 ° upward to 15 ° downward with respect to the horizontal position. The continuous casting method using the porous immersion nozzle 49 according to the fifth embodiment can be performed in the same manner as the continuous casting method using the porous immersion nozzle 10 according to the first embodiment. Is omitted.

次に、本発明の作用効果を確認するために行った試験例について説明する。
ここで、図9は試験例1における多孔浸漬ノズルのd/Dを変化させた場合における製造した鋳片の不具合発生指数の変化を示す説明図、図10は試験例2における多孔浸漬ノズルのx/dを変化させた場合における製造した鋳片の不具合発生指数の変化を示す説明図、図11は試験例3における多孔浸漬ノズルで(L−x)/Dを変化させた場合における製造した鋳片の不具合発生指数の変化を示す説明図、、図12は試験例4における鋳造速度と製造した鋳片の不具合発生指数との関係を示す説明図である。
[試験例1]
第1の実施の形態に係る多孔浸漬ノズル10において、下部流路14の内径Dと吐出部12の流路13の内径dとの比d/D(0を超え1.2未満の範囲)、吐出部12の流路13の内径dと吐出部12の上端から上側の吐出口17の内側上端までの距離xとの比x/d(0.1以上かつ5未満の範囲)、各吐出口17、18の傾斜角度α、β(上向き10°から下向き35°の範囲)、上側の吐出口17の断面積(内寸法)と下側の吐出口18の断面積(内寸法)との比(吐出口断面積比)、多孔浸漬ノズル10の浸漬深さ(150〜350mmの範囲)、アルゴンガスの吹き込み量(0.2〜20NL/minの範囲)、及び鋳造速度(0.6〜1.8m/minの範囲)をそれぞれ変化させながら、鋳片27を製造した。なお、L−x=2.5Dとした。そして、得られた鋳片27の不具合(不良品)発生指数とd/Dとの関係を調べた。その試験条件を表1、表2に、試験結果を図9に示す。ここで、鋳片27の不具合発生指数とは、所定期間内に製造した鋳片27に対する不具合の発生割合を示しており、1に近づくほど不具合が多く発生していることを示している。
Next, test examples performed for confirming the effects of the present invention will be described.
Here, FIG. 9 is an explanatory view showing a change in the defect occurrence index of the manufactured slab when the d / D of the porous immersion nozzle in Test Example 1 is changed, and FIG. 10 is an x of the porous immersion nozzle in Test Example 2. FIG. 11 is an explanatory diagram showing a change in a defect occurrence index of a manufactured slab when / d is changed, and FIG. 11 is a manufactured casting when (Lx) / D is changed by a porous immersion nozzle in Test Example 3. FIG. 12 is an explanatory diagram showing a change in a defect occurrence index of a piece, and FIG. 12 is an explanatory diagram showing a relationship between a casting speed in Test Example 4 and a defect occurrence index of a manufactured slab.
[Test Example 1]
In the porous immersion nozzle 10 according to the first embodiment, the ratio d / D of the inner diameter D of the lower flow path 14 and the inner diameter d of the flow path 13 of the discharge unit 12 (range of more than 0 and less than 1.2), Ratio x / d (range of 0.1 or more and less than 5) between the inner diameter d of the flow path 13 of the discharge unit 12 and the distance x from the upper end of the discharge unit 12 to the inner upper end of the upper discharge port 17, each discharge port 17, 18 inclination angles α, β (range of 10 ° upward to 35 ° downward), ratio of cross-sectional area (internal dimension) of upper discharge port 17 to cross-sectional area (internal dimension) of lower discharge port 18 (Discharge port cross-sectional area ratio), immersion depth of porous immersion nozzle 10 (range of 150 to 350 mm), amount of argon gas blown (range of 0.2 to 20 NL / min), and casting speed (0.6 to 1) The slab 27 was manufactured while changing the range of .8 m / min. Note that L−x = 2.5D. Then, the relationship between the defect (defective product) occurrence index of the obtained slab 27 and d / D was examined. The test conditions are shown in Tables 1 and 2, and the test results are shown in FIG. Here, the defect occurrence index of the slab 27 indicates the occurrence ratio of defects to the slab 27 manufactured within a predetermined period, and indicates that more defects are generated as the value approaches 1.

Figure 0004456491
Figure 0004456491

Figure 0004456491
Figure 0004456491

図9に示すように、多孔浸漬ノズル10のd/Dが0.2以上で0.8未満であれば、比x/d、各吐出口17、18の断面積(内寸法)の比、傾斜角度α、β、多孔浸漬ノズル10の浸漬深さ、及びアルゴンガスの吹き込み量の各条件を変化させても、不具合発生指数は0.2前後となっており、高品質の鋳片27を製造できることを確認できた。一方、d/Dが0.8以上又は0.2未満になると不具合発生指数は増加し、特にd/Dが0.8以上では不具合発生指数の増加が顕著となった。以上のことから、多孔浸漬ノズル10のd/Dは0.2以上で0.8未満にするのがよいことが確認できた。 As shown in FIG. 9, if the d / D of the porous immersion nozzle 10 is 0.2 or more and less than 0.8, the ratio x / d, the ratio of the cross-sectional areas (internal dimensions) of the discharge ports 17 and 18, Even when the inclination angles α, β, the immersion depth of the porous immersion nozzle 10 and the amount of argon gas blowing are changed, the defect occurrence index is around 0.2, and the high-quality slab 27 is obtained. It was confirmed that it could be manufactured. On the other hand, when d / D is 0.8 or more or less than 0.2, the failure index increases, and particularly when d / D is 0.8 or more, the increase in failure index becomes significant. From the above, it was confirmed that the d / D of the porous immersion nozzle 10 should be 0.2 or more and less than 0.8.

[試験例2]
第1の実施の形態に係る多孔浸漬ノズル10において、吐出部12の流路13の内径dと吐出部12の上端から上側の吐出口17の内側上端までの距離xとの比x/d(0を超え8未満の範囲)、下部流路14の内径Dと吐出部12の流路13の内径dとの比d/D(0.2以上で0.8未満の範囲)、各吐出口17、18の傾斜角度α、β(上向き10°から下向き35°の範囲)、上側の吐出口17の断面積(内寸法)と下側の吐出口18の断面積(内寸法)との比(吐出口断面積比)、多孔浸漬ノズル10の浸漬深さ(150〜350mmの範囲)、アルゴンガスの吹き込み量(0.2〜20NL/minの範囲)、及び鋳造速度(0.6〜1.8m/minの範囲)をそれぞれ変化させながら、鋳片27を製造した。そして、得られた鋳片27の不具合発生指数とx/dとの関係を調べた。その試験条件を表3、表4に、試験結果を図10に示す。なお、L−x=2.5Dとした。
[Test Example 2]
In the porous immersion nozzle 10 according to the first embodiment, the ratio x / d of the inner diameter d of the flow path 13 of the discharge unit 12 and the distance x from the upper end of the discharge unit 12 to the inner upper end of the upper discharge port 17 ( A range of more than 0 and less than 8), the ratio d / D (in the range of 0.2 to less than 0.8) of the inner diameter D of the lower flow path 14 and the inner diameter d of the flow path 13 of the discharge section 12, each discharge port 17, 18 inclination angles α, β (range of 10 ° upward to 35 ° downward), ratio of cross-sectional area (internal dimension) of upper discharge port 17 to cross-sectional area (internal dimension) of lower discharge port 18 (Discharge port cross-sectional area ratio), immersion depth of porous immersion nozzle 10 (range of 150 to 350 mm), amount of argon gas blown (range of 0.2 to 20 NL / min), and casting speed (0.6 to 1) The slab 27 was manufactured while changing the range of .8 m / min. Then, the relationship between the failure occurrence index of the obtained slab 27 and x / d was examined. The test conditions are shown in Tables 3 and 4, and the test results are shown in FIG. Note that L−x = 2.5D.

Figure 0004456491
Figure 0004456491

Figure 0004456491
Figure 0004456491

図10に示すように、多孔浸漬ノズル10のx/dが0.1を超え、かつ5未満であれば、下部流路14の内径Dと吐出部12の流路13の内径dとの比d/D、各吐出口17、18の断面積(内寸法)の比、傾斜角度α、β、多孔浸漬ノズル10の浸漬深さ、及びアルゴンガスの吹き込み量の各条件を変化させても、不具合発生指数は0.2前後となっており、高品質の鋳片27を製造できることを確認できた。
一方、d/Dが5以上又は0.1未満になると不具合発生指数の増加が顕著となった。以上のことから、多孔浸漬ノズル10のx/dは0.1を超えかつ5未満にするのがよいことが確認できた。
As shown in FIG. 10, if x / d of the porous immersion nozzle 10 exceeds 0.1 and is less than 5, the ratio between the inner diameter D of the lower flow path 14 and the inner diameter d of the flow path 13 of the discharge unit 12 Even if the respective conditions of d / D, the ratio of the cross-sectional areas (internal dimensions) of the discharge ports 17 and 18, the inclination angles α and β, the immersion depth of the porous immersion nozzle 10, and the blowing amount of argon gas are changed, The defect occurrence index was around 0.2, and it was confirmed that a high quality slab 27 could be manufactured.
On the other hand, when d / D is 5 or more or less than 0.1, the increase in the defect occurrence index becomes remarkable. From the above, it was confirmed that x / d of the porous immersion nozzle 10 should be more than 0.1 and less than 5.

[試験例3]
第1の実施の形態に係る多孔浸漬ノズル10において、下部流路14の内径Dと吐出部12の流路13の内径dとの比d/D(0.2以上で0.8未満の範囲)、吐出部12の流路13の内径dと吐出部12の上端から上側の吐出口17の内側上端までの距離xとの比x/d(0.1を超え5未満の範囲)、鋳型22内の溶鋼19のメニスカスから上側の吐出口17の外側上端までの距離をLとして比(L−x)/D(0を超え3.5未満の範囲)、各吐出口17、18の傾斜角度α、β(上向き10°から下向き35°の範囲)、上側の吐出口17の断面積(内寸法)と下側の吐出口18の断面積(内寸法)との比、アルゴンガスの吹き込み量(0.2〜20NL/minの範囲)、及び鋳造速度(0.6〜1.8m/minの範囲)をそれぞれ変化させながら、鋳片27を製造した。そして、得られた鋳片27の不具合発生指数と(L−x)/Dとの関係を調べた。その試験条件を表5、表6に、試験結果を図11に示す。なお、x=Dとした。
[Test Example 3]
In the porous immersion nozzle 10 according to the first embodiment, the ratio d / D between the inner diameter D of the lower flow path 14 and the inner diameter d of the flow path 13 of the discharge part 12 (range of 0.2 or more and less than 0.8) ) Ratio x / d (range of more than 0.1 and less than 5) between the inner diameter d of the flow path 13 of the discharge part 12 and the distance x from the upper end of the discharge part 12 to the inner upper end of the upper discharge port 17, the mold The ratio from the meniscus of the molten steel 19 in 22 to the outer upper end of the upper discharge port 17 is L, and the ratio (L−x) / D (over 0 and less than 3.5), the inclination of the discharge ports 17 and 18. Angles α and β (range of 10 ° upward to 35 ° downward), ratio of the cross-sectional area (internal dimension) of the upper discharge port 17 to the cross-sectional area (internal dimension) of the lower discharge port 18, argon gas blowing Amount (range 0.2-20 NL / min) and casting speed (range 0.6-1.8 m / min) While changing to produce a slab 27. Then, the relationship between the failure index of the obtained slab 27 and (L−x) / D was examined. The test conditions are shown in Tables 5 and 6, and the test results are shown in FIG. Note that x = D.

Figure 0004456491
Figure 0004456491

Figure 0004456491
Figure 0004456491

図11に示すように、比(L−x)/Dが1.5を超えるように多孔浸漬ノズル10を鋳型22内に浸漬すれば、下部流路14の内径Dと吐出部12の流路13の内径dとの比d/D、吐出部12の流路13の内径dと吐出部12の上端から上側の吐出口17の内側上端までの距離xとの比x/d、各吐出口17、18の断面積(内寸法)の比、各吐出口17、18の傾斜角度α、β、及びアルゴンガスの吹き込み量の各条件を変化させても、不具合発生指数を0.2未満にすることができ、高品質の鋳片27を製造できることが確認できた。
一方、比(L−x)/Dが1.5以下になると不具合発生指数の増加が顕著となった。以上のことから、比(L−x)/Dが1.5を超えるように多孔浸漬ノズル10の浸漬深さを設定するのがよいことが確認できた。なお、比(L−x)/Dが3.5以上で20を超えない範囲でも、不具合発生指数は0.2未満となり、高品質の鋳片27を製造できることが確認できた。
As shown in FIG. 11, if the porous immersion nozzle 10 is immersed in the mold 22 so that the ratio (Lx) / D exceeds 1.5, the inner diameter D of the lower flow path 14 and the flow path of the discharge section 12 The ratio d / D of the inner diameter d of the discharge section 12, the ratio x / d of the inner diameter d of the flow path 13 of the discharge section 12 and the distance x from the upper end of the discharge section 12 to the inner upper end of the upper discharge opening 17, each discharge opening Even if each of the ratios of the cross-sectional areas (inner dimensions) 17 and 18, the inclination angles α and β of the discharge ports 17 and 18, and the amount of argon gas blown in is changed, the malfunction occurrence index is less than 0.2 It was confirmed that a high quality cast slab 27 could be manufactured.
On the other hand, when the ratio (L−x) / D is 1.5 or less, the increase in the defect occurrence index becomes remarkable. From the above, it was confirmed that the immersion depth of the porous immersion nozzle 10 should be set so that the ratio (Lx) / D exceeds 1.5. In addition, even if the ratio (Lx) / D is 3.5 or more and does not exceed 20, the defect occurrence index is less than 0.2, and it was confirmed that the high-quality slab 27 can be manufactured.

[試験例4]
第1の実施の形態に係る多孔浸漬ノズル10において、下部流路14の内径Dと吐出部12の流路13の内径dとの比d/D(0.2以上で0.8未満の範囲)、吐出部12の流路13の内径dと吐出部12の上端から上側の吐出口17の内側上端までの距離xとの比x/d(0.1以上かつ5未満の範囲)、各吐出口17、18の傾斜角度α、β(上向き10°から下向き35°の範囲)、上側の吐出口17の断面積(内寸法)と下側の吐出口18の断面積(内寸法)との比(吐出口断面積比)、多孔浸漬ノズル10の浸漬深さ(150〜350mmの範囲)、アルゴンガスの吹き込み量(0.2〜20NL/minの範囲)、及び鋳造速度(0.6〜1.8m/minの範囲)をそれぞれ変化させながら、鋳片27を製造した。そして、得られた鋳片27の不具合(不良品)発生指数と鋳造速度との関係を調べた。その試験条件を表7、表8に、試験結果を図12にを示す。
また、従来例に係る浸漬ノズル(d/D=1、x/d=0,吐出口の傾斜角度α=15°)において、浸漬ノズルの浸漬深さ、アルゴンガスの吹き込み量、及び鋳造速度をそれぞれ表9に示す条件に設定して、鋳片を製造した。そして、得られた鋳片の不具合(不良品)発生指数と鋳造速度との関係を調べた。その結果を図12に併せて示す。
[Test Example 4]
In the porous immersion nozzle 10 according to the first embodiment, the ratio d / D between the inner diameter D of the lower flow path 14 and the inner diameter d of the flow path 13 of the discharge part 12 (range of 0.2 or more and less than 0.8) ) Ratio x / d (range of 0.1 or more and less than 5) between the inner diameter d of the flow path 13 of the discharge unit 12 and the distance x from the upper end of the discharge unit 12 to the inner upper end of the upper discharge port 17; Inclination angles α and β of the discharge ports 17 and 18 (range of 10 ° upward to 35 ° downward), a cross-sectional area (internal dimension) of the upper discharge port 17 and a cross-sectional area (internal dimension) of the lower discharge port 18 Ratio (discharge port cross-sectional area ratio), immersion depth of porous immersion nozzle 10 (range of 150 to 350 mm), argon gas blowing rate (range of 0.2 to 20 NL / min), and casting speed (0.6 The cast slab 27 was manufactured while changing the range of ˜1.8 m / min. Then, the relationship between the defect (defective product) occurrence index of the obtained slab 27 and the casting speed was examined. The test conditions are shown in Tables 7 and 8, and the test results are shown in FIG.
Further, in the immersion nozzle according to the conventional example (d / D = 1, x / d = 0, discharge port inclination angle α = 15 °), the immersion depth of the immersion nozzle, the blowing amount of argon gas, and the casting speed are set as follows. The slab was manufactured by setting each to the conditions shown in Table 9. And the relationship between the defect (defective product) occurrence index of the obtained slab and the casting speed was examined. The results are also shown in FIG.

Figure 0004456491
Figure 0004456491

Figure 0004456491
Figure 0004456491

Figure 0004456491
Figure 0004456491

図12に示すように、鋳造速度が0.6〜1.8m/minであれば、下部流路14の内径Dと吐出部12の流路13の内径dとの比d/D、吐出部12の流路13の内径dと吐出部12の上端から上側の吐出口17の内側上端までの距離xとの比x/d、各吐出口17、18の断面積(内寸法)の比、各吐出口17、18の傾斜角度α、β、多孔浸漬ノズル10の浸漬深さ、及びアルゴンガスの吹き込み量の各条件を変化させても、不具合発生指数は0.2前後となっており、高品質の鋳片27を製造できることを確認できた。
一方、従来例に係る浸漬ノズルでは、図12に示すように、鋳造速度が低速になる程、すなわち、0.7m/分未満の速度の場合、鋳片にヘゲ、スリバ等が発生し、鋳片表層の品質を低下させる。また、鋳造速度が高速になる程、すなわち、1.5m/分を超える速度の場合、鋳片に、気泡、介在物等の起因による内部欠陥が発生する。従って、不具合発生指数が、実施例に係る多孔浸漬ノズルと比較して、大幅に高くなることが分かる。以上のことから、実施例に係る多孔浸漬ノズルを使用することで、鋳型内の溶鋼の流れを緩慢にし、かつ均一な流れを形成して、気泡や介在物による欠陥を防止して高速鋳造を可能にできる。
As shown in FIG. 12, when the casting speed is 0.6 to 1.8 m / min, the ratio d / D between the inner diameter D of the lower flow path 14 and the inner diameter d of the flow path 13 of the discharge section 12, the discharge section A ratio x / d between the inner diameter d of the 12 flow paths 13 and the distance x from the upper end of the discharge section 12 to the inner upper end of the upper discharge port 17, the ratio of the cross-sectional areas (internal dimensions) of the discharge ports 17 and 18, Even if each condition of the inclination angles α and β of the discharge ports 17 and 18, the immersion depth of the porous immersion nozzle 10, and the amount of argon gas blown is changed, the defect occurrence index is around 0.2, It was confirmed that a high-quality cast slab 27 could be manufactured.
On the other hand, in the immersion nozzle according to the conventional example, as shown in FIG. 12, as the casting speed becomes lower, that is, when the speed is less than 0.7 m / min, shave, sliver and the like occur in the slab, Reduce the quality of the slab surface. Further, as the casting speed increases, that is, when the speed exceeds 1.5 m / min, internal defects due to bubbles, inclusions, and the like occur in the slab. Therefore, it can be seen that the occurrence index is significantly higher than that of the porous immersion nozzle according to the example. From the above, by using the porous immersion nozzle according to the embodiment, the flow of the molten steel in the mold is slowed down and a uniform flow is formed, and defects due to bubbles and inclusions are prevented and high speed casting is performed. It can be made possible.

以上、本発明の実施の形態を説明したが、本発明は、この実施の形態に限定されるものではなく、発明の要旨を変更しない範囲での変更は可能であり、前記したそれぞれの実施の形態や変形例の一部又は全部を組み合わせて本発明の多孔浸漬ノズル及びこれを用いた連続鋳造方法を構成する場合も本発明の権利範囲に含まれる。
例えば、第5の実施の形態においては、各吐出口の上部のみにひさし部を設けたが、各吐出口の下部及び側部のいずれか一方又は双方、あるいは各吐出口を囲むようにひさし部を設けてもよい。更に、第3の実施の形態においても整流部材及びひさし部のいずれか一方又は双方を設けることもできる。また、第2の実施の形態においても、絞り部、整流部材、及びひさし部のいずれか1又は任意の2以上を設けることもできる。なお、吐出部の流路及び吐出口の周囲は、カルシアを含有する耐火物で構成してもよい。
As mentioned above, although embodiment of this invention was described, this invention is not limited to this embodiment, The change in the range which does not change the summary of invention is possible, Each above-mentioned embodiment is possible. The case where the porous immersion nozzle of the present invention and the continuous casting method using the same are combined with some or all of the forms and modifications are also included in the scope of the right of the present invention.
For example, in the fifth embodiment, the eaves part is provided only at the upper part of each discharge port, but the eaves part surrounds each discharge port, either or both of the lower part and the side part of each discharge port. May be provided. Furthermore, in the third embodiment, either one or both of the rectifying member and the eaves portion can be provided. Also in the second embodiment, any one or any two or more of the throttle part, the rectifying member, and the eaves part can be provided. In addition, you may comprise the periphery of the flow path and discharge outlet of a discharge part with the refractory containing a calcia.

本発明の第1の実施の形態に係る多孔浸漬ノズルの側断面図である。It is a sectional side view of the porous immersion nozzle which concerns on the 1st Embodiment of this invention. 同多孔浸漬ノズルを用いた連続鋳造方法の説明図である。It is explanatory drawing of the continuous casting method using the same porous immersion nozzle. (A)は同多孔浸漬ノズルの使用状態を示す側断面図、(B)は(A)のP−P矢視断面図である。(A) is side sectional drawing which shows the use condition of the same porous immersion nozzle, (B) is PP sectional view taken on the line of (A). (A)は従来例に係る浸漬ノズルの使用状態を示す側断面図、(B)は(A)のQ−Q矢視断面図である。(A) is a sectional side view showing the usage state of the immersion nozzle according to the conventional example, (B) is a sectional view taken along the line Q-Q of (A). 本発明の第2の実施の形態に係る多孔浸漬ノズルの側断面図である。It is a sectional side view of the porous immersion nozzle which concerns on the 2nd Embodiment of this invention. 本発明の第3の実施の形態に係る多孔浸漬ノズルの側断面図である。It is a sectional side view of the porous immersion nozzle which concerns on the 3rd Embodiment of this invention. 本発明の第4の実施の形態に係る多孔浸漬ノズルの側断面図である。It is a sectional side view of the porous immersion nozzle which concerns on the 4th Embodiment of this invention. 本発明の第5の実施の形態に係る多孔浸漬ノズルの側断面図である。It is a sectional side view of the porous immersion nozzle which concerns on the 5th Embodiment of this invention. 試験例1における多孔浸漬ノズルのd/Dを変化させた場合における製造した鋳片の不具合発生指数の変化を示す説明図である。It is explanatory drawing which shows the change of the malfunction occurrence index | exponent of the manufactured slab when changing d / D of the porous immersion nozzle in the test example 1. FIG. 試験例2における多孔浸漬ノズルのx/dを変化させた場合における製造した鋳片の不具合発生指数の変化を示す説明図である。It is explanatory drawing which shows the change of the malfunction occurrence index of the slab manufactured when x / d of the porous immersion nozzle in Test Example 2 is changed. 試験例3における多孔浸漬ノズルで(L−x)/Dを変化させた場合における製造した鋳片の不具合発生指数の変化を示す説明図である。It is explanatory drawing which shows the change of the malfunction occurrence index of the slab manufactured when (Lx) / D is changed with the porous immersion nozzle in Test Example 3. 試験例4における鋳造速度と製造した鋳片の不具合発生指数との関係を示す説明図である。It is explanatory drawing which shows the relationship between the casting speed in Test Example 4, and the malfunction occurrence index of the manufactured slab.

符号の説明Explanation of symbols

10:多孔浸漬ノズル、11:ノズル本体、12:吐出部、13:流路、14:下部流路、15、16:側壁、17、18:吐出口、19:溶鋼、20:底部、21:タンディッシュ、22:鋳型、23:支持セグメント、24:凝固殻、25:軽圧下セグメント、26:ピンチロール、27:鋳片、28:稼動面、29:ノズル本体、30、31:吐出口、32:浸漬ノズル、33:多孔浸漬ノズル、34:吐出部、35:流路、36:多孔浸漬ノズル、37:ノズル本体、38:下部流路、39:湯面位置、40:絞り部、41:多孔浸漬ノズル、42:ノズル本体、43:下部流路、44:湯面位置、45:整流部材、46:貫通孔、47:掛止部、48:接触面、49:多孔浸漬ノズル、50:吐出部、51、52:吐出口、53、54:ひさし部 DESCRIPTION OF SYMBOLS 10: Porous immersion nozzle, 11: Nozzle body, 12: Discharge part, 13: Flow path, 14: Lower flow path, 15, 16: Side wall, 17, 18: Discharge port, 19: Molten steel, 20: Bottom part, 21: Tundish, 22: mold, 23: support segment, 24: solidified shell, 25: lightly pressed segment, 26: pinch roll, 27: cast slab, 28: working surface, 29: nozzle body, 30, 31: discharge port, 32: immersion nozzle, 33: porous immersion nozzle, 34: discharge part, 35: flow path, 36: porous immersion nozzle, 37: nozzle body, 38: lower flow path, 39: hot water surface position, 40: throttle part, 41 : Porous immersion nozzle, 42: nozzle body, 43: lower flow path, 44: molten metal surface position , 45: flow regulating member, 46: through hole, 47: latching portion, 48: contact surface, 49: porous immersion nozzle, 50 : Discharge part, 51, 52: discharge port, 53, 4: eaves part

Claims (8)

溶鋼が上から下に通過する筒状のノズル本体と、該ノズル本体の下端に連設して設けられ、鋳型内に浸漬される吐出部とを有する浸漬ノズルにおいて、
前記吐出部の流路の平均断面積は前記ノズル本体の下部流路の断面積より小さく、該ノズル本体の下部流路の内平均寸法Dと前記吐出部の流路の最小内寸法dとの比d/Dが0.2以上0.8未満、かつ前記吐出部の流路の上端の内寸法は前記ノズル本体の下部流路の内寸法より小さく、しかも、前記吐出部の流路の内寸法は上端から下端まで一定であり、
前記鋳型の短辺側を指向する前記吐出部の側壁には上下に少なくとも2以上の吐出口が設けられ、前記鋳型内の溶鋼のメニスカスから前記吐出口のうち最上部の吐出口の外側上端までの距離Lと、前記吐出部の上端から前記最上部の吐出口の内側上端までの距離xの間に、0.1d<x<5dかつ1.5D<L−x≦20Dの関係が成立し、下側に設けられた前記吐出口の断面積は上側に設けられた前記吐出口の断面積よりも小さく、前記各吐出口の軸心の傾斜角度が水平に対して上向き10°から下向き45°の範囲に設定されていることを特徴とする多孔浸漬ノズル。
In a submerged nozzle having a tubular nozzle body through which molten steel passes from top to bottom, and a discharge part that is provided continuously to the lower end of the nozzle body and is immersed in a mold,
The average cross-sectional area of the flow path of the discharge section is smaller than the cross-sectional area of the lower flow path of the nozzle body, and the inner average dimension D of the lower flow path of the nozzle body and the minimum internal dimension d of the flow path of the discharge section The ratio d / D is 0.2 or more and less than 0.8 and the inner dimension of the upper end of the flow path of the discharge part is smaller than the inner dimension of the lower flow path of the nozzle body, and the inner dimension of the flow path of the discharge part The dimensions are constant from top to bottom ,
At least two or more discharge ports are provided in the upper and lower sides on the side wall of the discharge portion directed to the short side of the mold, from the meniscus of the molten steel in the mold to the outer upper end of the uppermost discharge port among the discharge ports The relationship of 0.1d <x <5d and 1.5D <L−x ≦ 20D is established between the distance L and the distance x from the upper end of the discharge unit to the inner upper end of the uppermost discharge port. The cross-sectional area of the discharge port provided on the lower side is smaller than the cross-sectional area of the discharge port provided on the upper side, and the inclination angle of the axis of each discharge port is 10 ° upward to 45 ° downward with respect to the horizontal. A multi-hole immersion nozzle characterized by being set in the range of ° .
請求項1記載の多孔浸漬ノズルにおいて、前記吐出部の横断面の外形が矩形であることを特徴とする多孔浸漬ノズル。 In the porous immersion nozzle according to claim 1 Symbol placement, porous immersion nozzle, wherein the outer shape of the cross section of the discharge section is rectangular. 請求項1又は2記載の多孔浸漬ノズルにおいて、前記各吐出口の少なくとも上部及び下部のいずれか一方又は双方には、前記各吐出口から吐出した溶鋼の流れを誘導可能なひさし部が設けられていることを特徴とする多孔浸漬ノズル。 3. The porous immersion nozzle according to claim 1, wherein at least one or both of the upper and lower portions of each discharge port is provided with an eaves portion capable of guiding a flow of molten steel discharged from each discharge port. A porous immersion nozzle characterized by having 請求項1〜のいずれか1項に記載の多孔浸漬ノズルにおいて、前記下部流路の上方には、流路断面積が縮小する絞り部が設けられていることを特徴とする多孔浸漬ノズル。 The porous immersion nozzle according to any one of claims 1 to 3 , wherein a throttle part for reducing a cross-sectional area of the flow path is provided above the lower flow path. 請求項1〜のいずれか1項に記載の多孔浸漬ノズルにおいて、前記下部流路の上方には、溶鋼を通過させる複数の貫通孔を備えた整流部材が設けられていることを特徴とする多孔浸漬ノズル。 The porous immersion nozzle according to any one of claims 1 to 4 , wherein a rectifying member having a plurality of through holes through which molten steel passes is provided above the lower flow path. Porous immersion nozzle. 請求項1〜のいずれか1項に記載の多孔浸漬ノズルにおいて、少なくとも前記吐出部の流路及び前記吐出口の周囲は、それぞれカルシアを含有する耐火物及びドロマイトクリンカーを含有する耐火物のいずれか一方又は双方で構成されていることを特徴とする多孔浸漬ノズル。 The porous immersion nozzle according to any one of claims 1 to 5 , wherein at least the flow path of the discharge unit and the periphery of the discharge port are any of a refractory containing calcia and a refractory containing dolomite clinker, respectively. A porous immersion nozzle characterized by comprising either or both. 溶鋼が上から下に通過する筒状のノズル本体と、該ノズル本体の下端に連設して設けられ、鋳型内に浸漬される吐出部とを有し、前記吐出部の流路の平均断面積は前記ノズル本体の下部流路の断面積より小さく、該ノズル本体の下部流路の内平均寸法Dと該吐出部の流路の最小内寸法dとの比d/Dが0.2以上0.8未満、かつ前記吐出部の流路の上端の内寸法は前記ノズル本体の下部流路の内寸法より小さく、しかも、前記吐出部の流路の内寸法は上端から下端まで一定であり、前記鋳型の短辺側を指向する前記吐出部の側壁には上下に少なくとも2以上の吐出口が設けられ、下側に設けられた前記吐出口の断面積は上側に設けられた前記吐出口の断面積よりも小さな多孔浸漬ノズルを介して、前記鋳型内に溶鋼を注湯し、溶鋼を凝固させながら0.6m/min以上の鋳造速度で前記鋳型から引き抜く連続鋳造方法であって、
前記吐出部の上端から前記吐出口のうち最上部の吐出口の内側上端までの距離xを0.1d<x<5d、前記鋳型内の溶鋼のメニスカスから前記最上部の吐出口の外側上端までの距離Lを1.5D<L−x≦20Dとすると共に、前記各吐出口の軸心の傾斜角度を水平状態に対して上向き10°から下向き45°の範囲に設定し、前記吐出部を前記鋳型内の溶鋼のメニスカス位置から150〜350mmの範囲で該鋳型中の溶鋼に浸漬させ、アルゴンガスの吹き込み量を0.2〜20ノルマルリットル/分にすることを特徴とする連続鋳造方法。
A cylindrical nozzle body through which molten steel passes from the top to the bottom, and a discharge part that is connected to the lower end of the nozzle body and is immersed in the mold. The area is smaller than the cross-sectional area of the lower flow path of the nozzle body, and the ratio d / D between the inner average dimension D of the lower flow path of the nozzle body and the minimum inner dimension d of the flow path of the discharge section is 0.2 or more. The inner dimension of the upper end of the flow path of the discharge unit is less than 0.8 and smaller than the inner dimension of the lower flow path of the nozzle body, and the inner dimension of the flow path of the discharge unit is constant from the upper end to the lower end . In addition, at least two or more discharge ports are provided in the upper and lower sides on the side wall of the discharge unit directed to the short side of the mold, and the discharge port provided on the lower side has the cross-sectional area provided on the upper side. through a small perforated immersion nozzle than the cross sectional area of, and pouring molten steel into said mold, of solidifying the molten steel While a continuous casting process withdrawn from the mold at a 0.6 m / min or more casting speed,
The distance x from the upper end of the discharge unit to the inner upper end of the uppermost discharge port among the discharge ports is 0.1d <x <5d, from the meniscus of the molten steel in the mold to the outer upper end of the uppermost discharge port The distance L is set to 1.5D <L−x ≦ 20D, the inclination angle of the axis of each discharge port is set in a range of 10 ° upward to 45 ° downward with respect to the horizontal state, and the discharge unit is A continuous casting method characterized by immersing the molten steel in the mold in a range of 150 to 350 mm from the meniscus position of the molten steel in the mold and setting the argon gas blowing rate to 0.2 to 20 normal liters / minute .
請求項7記載の連続鋳造方法において、溶鋼中にカルシウムが添加されていることを特徴とする連続鋳造方法。 In the continuous casting method according to claim 7 Symbol mounting, continuous casting method characterized by calcium in the molten steel are added.
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