JPH1147896A - Immersion nozzle for continuous casting - Google Patents

Immersion nozzle for continuous casting

Info

Publication number
JPH1147896A
JPH1147896A JP20359597A JP20359597A JPH1147896A JP H1147896 A JPH1147896 A JP H1147896A JP 20359597 A JP20359597 A JP 20359597A JP 20359597 A JP20359597 A JP 20359597A JP H1147896 A JPH1147896 A JP H1147896A
Authority
JP
Japan
Prior art keywords
nozzle
spiral
spirals
section
present
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP20359597A
Other languages
Japanese (ja)
Other versions
JP3673372B2 (en
Inventor
Hideo Mori
秀夫 森
Kenzo Ayada
研三 綾田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kobe Steel Ltd
Original Assignee
Kobe Steel Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP20359597A priority Critical patent/JP3673372B2/en
Publication of JPH1147896A publication Critical patent/JPH1147896A/en
Application granted granted Critical
Publication of JP3673372B2 publication Critical patent/JP3673372B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Continuous Casting (AREA)
  • Casting Support Devices, Ladles, And Melt Control Thereby (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent the channeling in a mold, to reduce the inclusion in a nozzle and to prevent the clogging of a nozzle by arranging a spiral projection on the inner wall of the nozzle to circularly stir molten steel in the nozzle. SOLUTION: Double spirals A, B are arranged in the nozzle between a tundish and a mold. Number of spirals are desirable to be two or three. The starting point and end point of the spiral are a factor largely affected to the prevention of drift and the reduction of inclusion, etc. Then, related to the starting point of the spiral, it is desirable to control to the position having mutually 170-190 deg. angle in the same height in the case of being the double spirals and to the position having mutually 110-130 deg. angle at the same height in the case of being triple spirals. Further, related to the end point of the spiral, it is desirable to set to the position having at least 100 mm from the upper end of inner diameter part in a nozzle spouting hole. As the other, it is desirable to control the descending angle of the spiral to 20-70 deg. and the height in the spiral cross section to 5-25% to the nozzle inner diameter and the length of the bottom surface in the spiral cross section to 10-30 mm.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、例えば取鍋からタ
ンディッシュ、タンディッシュからモールドへ溶鋼を注
入する際に用いられる連続鋳造用浸漬ノズルに関するも
のである。本発明の連続鋳造用浸漬ノズルは、鋼の連続
鋳造において、鋳型内の偏流や鋳造中のノズル閉塞を防
止し得ると共に、溶鋼中の介在物も効率良く分離できる
点で非常に有用である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a continuous casting immersion nozzle used for injecting molten steel from a ladle to a tundish or from a tundish to a mold. INDUSTRIAL APPLICABILITY The immersion nozzle for continuous casting of the present invention is very useful in continuous casting of steel because it can prevent drift in the mold and blockage of the nozzle during casting and can efficiently separate inclusions in molten steel.

【0002】[0002]

【従来の技術】連続鋳造法においては、鋳造中、浸漬ノ
ズル内での閉塞を如何にして防止し得るかが重要課題の
一つになっている。ノズル内で閉塞が生じると、所望の
溶鋼吐出量が確保できず、実操業に支障をもたらすのみ
ならず、生成した閉塞物が鋳型内に残留し、鋳片の品質
を悪化させる要因にもなるからである。
2. Description of the Related Art In the continuous casting method, one of the important issues is how to prevent clogging in an immersion nozzle during casting. If clogging occurs in the nozzle, the desired molten steel discharge rate cannot be secured, not only hindering the actual operation, but also the generated clogging remains in the mold, which is a factor of deteriorating the quality of the slab. Because.

【0003】上述したノズル内閉塞防止に関しては、ノ
ズル内で旋回攪拌させることが有効であるという観点に
基づき、ノズル形状を制御した様々な態様が提案されて
いる。
[0003] Regarding the above-described prevention of nozzle blockage, various modes in which the nozzle shape is controlled have been proposed from the viewpoint that it is effective to swirl and stir in the nozzle.

【0004】例えば特開昭57−130745には、内
壁に螺旋状の溝または突起を設けた連続鋳造用ノズルが
開示されており、具体的には、2孔ノズル長手方向の上
端から吐出孔の上部まで、螺旋状の溝を施したものが図
示されている。また特開平2−41747には、内壁に
1本以上の螺旋状の段差を設け、入口側より出口側にか
けて溶融金属流路の断面積が漸次縮小した部分を有する
連続鋳造用ノズルが開示されている。
For example, Japanese Patent Application Laid-Open No. 57-130745 discloses a continuous casting nozzle provided with a spiral groove or projection on the inner wall. Specifically, a two-hole nozzle has a discharge hole from its upper end in the longitudinal direction. A spiral groove is shown up to the top. JP-A-2-41747 discloses a continuous casting nozzle in which one or more spiral steps are provided on an inner wall, and a cross-sectional area of a molten metal flow path is gradually reduced from an inlet side to an outlet side. I have.

【0005】しかしながら、上記ノズルの場合はいずれ
も、螺旋に沿って旋回した溶鋼は、2つの吐出孔から均
一に排出されず、いずれか一方の吐出孔から優先的に排
出されてしまう為、鋳型内に偏流が生じてパウダーの巻
込みが発生したり、凝固が不均一になる等の悪影響を招
く恐れがある。
However, in any of the above nozzles, the molten steel swirled along the spiral is not uniformly discharged from the two discharge holes, but is preferentially discharged from one of the discharge holes. There is a risk of causing an adverse effect such as the occurrence of a drift in the powder, the entrainment of the powder, and the uneven solidification.

【0006】また、特開平7−303949には、浸漬
ノズル上端に中間ノズルを設けて溶鋼を旋回攪拌する方
法が開示されている。具体的には、溶湯を旋回させる旋
回力付与手段として、中間ノズルや浸漬ノズルにフィン
を設ける等し、更に、浸漬ノズル内に静磁界を印加する
ことにより溶湯の噴出流を制御している。しかしながら
該方法によれば、浸漬ノズル上部の中間ノズルで旋回攪
拌している為、その下方に位置する浸漬ノズルの吐出孔
まで旋回を持続させることは困難であり、所望の旋回攪
拌効果が充分得られない。また、溶鋼が高流速で排出さ
れる中間ノズル内に旋回力付与手段を設けている為、た
とえ、耐火物等で特殊な形状にしたとしても、連続鋳造
中、その形状を維持することは非常に困難である。
Japanese Patent Application Laid-Open No. 7-303949 discloses a method in which an intermediate nozzle is provided at the upper end of an immersion nozzle to swirl and agitate molten steel. Specifically, fins are provided in the intermediate nozzle and the immersion nozzle as a turning force applying means for turning the molten metal, and the jet flow of the molten metal is controlled by applying a static magnetic field in the immersion nozzle. However, according to this method, since the swirling is performed by the intermediate nozzle at the upper part of the immersion nozzle, it is difficult to continue the swirling to the discharge hole of the immersion nozzle located thereunder, and the desired swirling and stirring effect is sufficiently obtained. I can't. In addition, since the swirl force applying means is provided in the intermediate nozzle from which molten steel is discharged at a high flow rate, it is extremely difficult to maintain the shape during continuous casting even if the shape is specially made of a refractory or the like. Difficult.

【0007】更に特開平8−215809には、螺旋溝
の形状を特定した連続鋳造用ノズルが開示されている。
具体的には、複数条からなる所定の螺旋溝を形成させる
ことにより、ノズル内の溶鋼流を旋回させ、ジャイロ効
果によって溶鋼流の偏流を防止すると共に、該螺旋溝内
に溶鋼中の介在物を優先的に吸着させ、介在物の除去効
果を高めようとするものである。しかしながら、螺旋溝
に沿って溶鋼が流れることを期待するのは困難であり、
たとえ旋回が得られたとしても、該螺旋溝は吐出孔直上
まで設けられている為、2孔の吐出孔の一から優先して
排出され、鋳型内に偏流が生じ、パウダーが巻込まれた
り、凝固が不均一になる等の弊害を招く恐れがある。
Further, Japanese Patent Application Laid-Open No. Hei 8-215809 discloses a continuous casting nozzle in which the shape of a spiral groove is specified.
Specifically, by forming a predetermined spiral groove composed of a plurality of strips, the molten steel flow in the nozzle is swirled, the drift of the molten steel flow is prevented by the gyro effect, and inclusions in the molten steel in the spiral groove are formed. Is preferentially adsorbed to increase the effect of removing inclusions. However, it is difficult to expect molten steel to flow along the spiral groove,
Even if swirling is obtained, the spiral groove is provided immediately above the discharge hole, so that the discharge is preferentially discharged from one of the two discharge holes, a drift occurs in the mold, and the powder is caught, There is a possibility that adverse effects such as uneven coagulation may be caused.

【0008】[0008]

【発明が解決しようとする課題】本発明は上記事情に着
目してなされたものであって、その目的は、ノズル内の
溶鋼を旋回攪拌させると共に鋳型内の偏流を防止し得、
しかもノズル内の介在物を低減し、ノズル内の閉塞も防
止可能な連続鋳造用浸漬ノズルを提供することにある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and an object thereof is to swirl and agitate molten steel in a nozzle and prevent drift in a mold.
Moreover, it is an object of the present invention to provide a continuous casting immersion nozzle capable of reducing inclusions in the nozzle and preventing clogging in the nozzle.

【0009】[0009]

【課題を解決するための手段】上記目的を達成し得た本
発明の連続鋳造用浸漬ノズルとは、内壁に螺旋状突起を
設けたところに要旨を有する。偏流防止等の観点からす
れば、螺旋の数は2個または3個であることが好まし
い。螺旋の起点や終点も、偏流防止や介在物の低減化等
に大きな影響を及ぼす因子であり、螺旋の起点について
は、2重螺旋の場合は、同一の高さで互いに170〜1
90゜の位置に、3重螺旋の場合は、同一の高さで互い
に110〜130゜の位置に制御することが好ましく、
また、螺旋の終点については、ノズル吐出孔の内径部上
端より少なくとも100mmの位置に設定することが好
ましい。その他、螺旋の下降角度を20〜70゜に制御
したり、螺旋断面の高さをノズル内径に対し5〜25
%,螺旋断面の底面長さを10〜30mmに制御するこ
とは、より優れた特性を得る為の好ましい態様である。
The immersion nozzle for continuous casting of the present invention, which has achieved the above object, has a gist in that a spiral projection is provided on the inner wall. From the viewpoint of preventing drift, the number of spirals is preferably two or three. The starting point and the end point of the helix are also factors that greatly affect the prevention of drift and the reduction of inclusions. In the case of a double helix, the starting point of the helix is 170 to 1 at the same height.
In the case of a triple helix at a position of 90 °, it is preferable to control the positions at 110 to 130 ° with each other at the same height,
The end point of the spiral is preferably set at a position at least 100 mm from the upper end of the inner diameter of the nozzle discharge hole. In addition, the descending angle of the spiral is controlled to 20-70 °, and the height of the spiral cross section is 5-25
%, Controlling the length of the bottom surface of the spiral cross section to 10 to 30 mm is a preferable embodiment for obtaining more excellent characteristics.

【0010】[0010]

【発明の実施の形態】図1は、タンディッシュとモール
ド間のノズルに2重螺旋A,Bを施した本発明の概略説
明図であり、ノズルの内壁に、螺旋状の突起をノズル長
手方向の上端から吐出孔の所定部まで施したものであ
る。この構成をより明らかにする為に、紙面に平行な面
で半割にしたときの奥側の螺旋状態を示す図を図2
(a)に、手前側の螺旋状態を示す図を図2(b)に夫
々示す。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a schematic explanatory view of the present invention in which a double spiral A and B are provided on a nozzle between a tundish and a mold. A spiral projection is provided on the inner wall of the nozzle in the longitudinal direction of the nozzle. From the upper end to a predetermined portion of the discharge hole. In order to clarify this configuration, FIG. 2 is a diagram illustrating a spiral state on the back side when the plane is halved in a plane parallel to the paper surface.
FIGS. 2A and 2B show the spiral state on the near side in FIG.

【0011】上述した様に、本発明のノズルは、内壁に
螺旋状突起を設けた点に最大の特徴を有する。従来の螺
旋状ノズルは、せいぜい、螺旋状の溝や段差を設けた程
度のものしか開示されておらず、これでは、浸漬ノズル
の閉塞を有効に防止することができないことが分かっ
た。例えば、特開平8−215809は螺旋溝内に介在
物を優先的に吸着させようとするものであり、これにに
より微細介在物の除去効率は向上するかもしれないが、
ノズル内の閉塞を有効に防止することはできない。ま
た、特開平57−130745は、実質的に螺旋状の溝
を設けたノズルを開示するものであり、螺旋状突起につ
いては一言記載されている程度で、螺旋状の突起を溝と
同一レベルにしか認識していない。これに対して本発明
は、螺旋状突起に限定して鋭意検討を重ねたものであ
り、その結果、後記する実施例に示す如く、溝ではなく
突起を設けることにより、格段に優れたノズル閉塞防止
効果が得られ、介在物の不良欠陥も著しく減少できるこ
とを見出し、本発明を完成したのである。
As described above, the nozzle of the present invention is most characterized in that a spiral projection is provided on the inner wall. At most, conventional spiral nozzles only disclose spiral grooves or steps, and it has been found that this cannot effectively prevent the immersion nozzle from being blocked. For example, Japanese Patent Application Laid-Open No. Hei 8-215809 attempts to preferentially adsorb inclusions in a spiral groove, which may improve the efficiency of removing fine inclusions.
Blockage in the nozzle cannot be effectively prevented. Japanese Patent Application Laid-Open No. 57-130745 discloses a nozzle provided with a substantially spiral groove. The spiral protrusion is described in a word, and the spiral protrusion is formed at the same level as the groove. I only recognize it. On the other hand, the present invention has been intensively studied by limiting the present invention to a spiral projection. As a result, as shown in an embodiment described later, by providing a projection instead of a groove, a significantly excellent nozzle blockage is achieved. The present inventors have found that the prevention effect can be obtained and the defect defect of the inclusion can be significantly reduced, and the present invention has been completed.

【0012】本発明の基本構成は上記の通りであるが、
更に、螺旋の数や起点、終点を適切に制御することが推
奨される。従来のノズルでは、ノズル内の旋回攪拌効果
をできるだけ高めるべく螺旋を広範囲に設けていたが、
本発明者らの検討によれば、浸漬ノズルの上端から吐出
孔直上までノズルを設けると、むしろ鋳型内の偏流を助
長してしまうことが分かった。そこで、鋳型内の偏流を
防止したうえで適切な旋回攪拌効果を確保し、しかもノ
ズルの閉塞防止も可能なノズルの形状について更に検討
を重ねた結果、螺旋の形状を、従来の溝ではなく突起に
限定すると共に、螺旋の数、起点および終点を下記の如
く特定すれば良いことを見出したのである。
The basic structure of the present invention is as described above.
Furthermore, it is recommended that the number of spirals, the starting point, and the end point be appropriately controlled. In conventional nozzles, spirals were provided over a wide area to maximize the effect of swirling and stirring in the nozzles.
According to the study of the present inventors, it has been found that providing the nozzle from the upper end of the immersion nozzle to immediately above the discharge hole rather promotes the drift in the mold. Therefore, as a result of further study on the shape of the nozzle which can prevent the nozzle from clogging while securing the appropriate swirling and stirring effect while preventing the drift in the mold, the spiral shape was changed to a projection instead of the conventional groove. And found that the number of spirals, the starting point, and the ending point should be specified as follows.

【0013】尚、以下の説明では、図3〜8を用いなが
ら各要件の設定理由について詳述する。これらの図は、
240mm×1230mmのスラブ連鋳機にて[C]=
0.05%の鋼種を用い、1.6m/分の鋳造速度で鋳
造した場合において、螺旋条件を種々変化させたときの
結果を示すものである。尚、浸漬ノズルの内径は80m
mφ、全長は670mmである。
In the following description, the reasons for setting each requirement will be described in detail with reference to FIGS. These figures are
[C] = with continuous slab caster of 240mm × 1230mm
This shows the results obtained when the spiral conditions were variously changed in a case where the casting was performed at a casting speed of 1.6 m / min using a steel type of 0.05%. The inner diameter of the immersion nozzle is 80m
mφ, the total length is 670 mm.

【0014】螺旋の数:2または3 図3(a)に、螺旋の数と偏流度の関係を示す。数以外
の螺旋条件は、螺旋の下降角度45゜,螺旋断面の高さ
10mm(内径に対し12.5%),螺旋断面底面の長
さ20mm,螺旋の有する設置範囲は、始点を、螺旋の
数が2個の場合は同一高さで互いに180℃,3個の場
合は同一高さで互いに120℃とし、終点は、吐出孔上
端より120mmとした。また、偏流度は、図3(b)
に示す如く、吐出孔両端の狭面における溶鋼の湯面盛上
がり高さの比(H2 /H1 )で表され、偏流度が1と
は、両端の湯面高さが同一、即ち偏流が発生しないこと
を意味する。
Number of spirals: 2 or 3 FIG. 3A shows the relationship between the number of spirals and the degree of drift. The helix conditions other than the numbers are as follows: the descent angle of the helix is 45 °, the height of the helix cross section is 10 mm (12.5% of the inner diameter), the length of the helix cross section bottom is 20 mm, the installation range of the helix is the starting point, When the number is two, the temperature is 180 ° C. at the same height, and when the number is two, the temperature is 120 ° C. at the same height. When the number is three, the end point is 120 mm from the upper end of the discharge hole. In addition, the degree of drift is shown in FIG.
As shown in the figure, the ratio of the height of the molten steel surface rising (H 2 / H 1 ) on the narrow surfaces at both ends of the discharge hole is expressed as “H 2 / H 1”. Means not to occur.

【0015】図3(a)より、螺旋の数が1個では、螺
旋を全く設けない場合に比べて偏流度は悪くなった。こ
れは、螺旋出口側方向に溶鋼が優先的に流出する為であ
る。これに対し、螺旋の数を2個以上にすると偏流は発
生しなくなった。この様に偏流防止の観点のみに基づけ
ば、螺旋の数を2個以上にすることが推奨されるが、4
個以上形成させたとしても、ノズルの製作が困難にな
り、費用が高くつくだけで経済的に無駄であるので、本
発明では2個または3個とした。
From FIG. 3 (a), when the number of spirals is one, the degree of drift is worse than when no spiral is provided. This is because molten steel flows out preferentially in the direction of the spiral outlet. On the other hand, when the number of spirals was set to two or more, drift did not occur. Thus, based only on the viewpoint of preventing drifting, it is recommended that the number of spirals be two or more.
Even if more than two nozzles are formed, it is difficult to manufacture the nozzles and the cost is high, which is wasteful economically. Therefore, in the present invention, two or three nozzles are used.

【0016】螺旋の終点:浸漬ノズル吐出孔の内径部
上端から少なくとも100mm以上 図4(a)は、浸漬ノズル吐出孔の内径部上端からの距
離[図(b)中のs]と偏流度の関係を示すグラフであ
る。実験条件は、螺旋の数を2,下降角度を45゜,螺
旋の始点は、同一高さで互いに180゜としたこと以外
は前記図3の場合と同様にした。
The end point of the spiral: at least 100 mm or more from the upper end of the inner diameter of the immersion nozzle discharge hole. FIG. 4A shows the distance [s in FIG. It is a graph which shows a relationship. The experimental conditions were the same as in FIG. 3 except that the number of spirals was 2, the descending angle was 45 °, and the starting points of the spirals were 180 ° with each other at the same height.

【0017】図4より、吐出孔直上まで(即ち、s=
0)螺旋を設けると、偏流が発生し易くなることが分か
る。従って、偏流の発生を有効に防止する為には、螺旋
の終点を、浸漬ノズル吐出孔の内径部上端から少なくと
も100mm以上に設定することが推奨される。好まし
くは110mm以上、より好ましくは120mm以上で
ある。尚、その上限は特に限定されないが、ノズル吐出
孔と湯面レベルの位置を考慮すれば、200mm以下
(より好ましくは150mm以下)にすることが推奨さ
れる。
As shown in FIG. 4, up to the position just above the discharge hole (ie, s =
0) It can be seen that when the spiral is provided, the drift easily occurs. Therefore, in order to effectively prevent the occurrence of drift, it is recommended that the end point of the spiral be set to at least 100 mm or more from the upper end of the inner diameter of the immersion nozzle discharge hole. It is preferably at least 110 mm, more preferably at least 120 mm. Although the upper limit is not particularly limited, it is recommended that the upper limit be 200 mm or less (more preferably 150 mm or less) in consideration of the position of the nozzle discharge hole and the level of the molten metal.

【0018】尚、螺旋の始点については、2重螺旋の場
合は、同一の高さで互いに170〜190゜の位置に、
また3重螺旋の場合は、同一の高さで互いに110〜1
30゜の位置に設定することが推奨される。なかでも、
ノズルの軸心を中心に、螺旋を同一の高さで対称(即
ち、2重螺旋の場合は180゜、3重螺旋の場合は12
0゜)に設置したものは、溶鋼の偏流を一層有効に防止
できるので最も推奨される態様であるが、これに限定さ
れず、夫々、±10゜の範囲であれば許容レベルとして
本発明の範囲内に包含され得る。従って、2重螺旋の場
合は、最小で170゜,最大で190゜の位置に設置可
能であり、一方、3重螺旋の場合は、最小で110゜、
最大で130゜の位置に設置可能である。
In the case of a double helix, the starting point of the helix is at the same height and 170 to 190 ° from each other.
In the case of a triple helix, 110 to 1 at the same height
It is recommended to set the position at 30 °. Above all,
The spiral is symmetrical at the same height about the axis of the nozzle (ie, 180 ° for a double spiral, 12 ° for a triple spiral).
0 °) is the most recommended mode because it can more effectively prevent the drift of the molten steel, but is not limited to this, and each is within the range of ± 10 ° as an allowable level of the present invention. May be included within the scope. Therefore, in the case of a double helix, it can be installed at a minimum of 170 ° and a maximum of 190 °, while in the case of a triple helix, it can be installed at a minimum of 110 °,
It can be installed at a maximum of 130 °.

【0019】以上の要件を特定することにより、より優
れた効果を得ることができるが、更に、一層の向上を目
指して、螺旋の形状を以下の様に制御することが推奨さ
れる。
By specifying the above requirements, a better effect can be obtained. However, it is recommended to control the shape of the spiral as follows for further improvement.

【0020】螺旋の下降角度:20〜70゜ 図5(a)は、螺旋の下降角度と回転指数の関係を示す
グラフである。これは、浸漬ノズルを単孔とし、その直
下の回転状況(旋回攪拌)を水モデルにより評価したも
の[図中(b)の×が測定点]であり、図中の「回転指
数」は、螺旋の下降角度を20゜とした場合の回転速度
を基準に、その回転速度と各条件での回転速度の比で表
したものである。実験条件は、螺旋の数:2,螺旋の始
点は、同一高さで互いに180゜としたこと以外は図3
の場合と同様に設定した。
Spiral descending angle: 20-70 ° FIG. 5A is a graph showing the relationship between the spiral descending angle and the rotation index. This is a single hole in the immersion nozzle, and the rotation status (swirl stirring) immediately below the immersion nozzle was evaluated using a water model [x in FIG. 3 (b) is a measurement point]. The rotation speed is represented by a ratio of the rotation speed under each condition to the rotation speed when the descent angle of the spiral is set to 20 °. The experimental conditions were as follows: the number of spirals: 2, the starting points of the spirals were 180 ° from each other at the same height.
Was set in the same way as in the case of.

【0021】図5より、螺旋の下降角度が20〜70゜
では回転指数が1以上になり良好な結果が得られること
が分かる。より好ましい下限値は30゜であり、より好
ましい上限値は60゜である。
FIG. 5 shows that when the spiral descending angle is 20 to 70 °, the rotation index becomes 1 or more and good results are obtained. A more preferred lower limit is 30 ° and a more preferred upper limit is 60 °.

【0022】螺旋断面の高さ :内径に対して5〜2
5% 螺旋断面の底面長さ:10〜30mm 図6(a)は、良好な旋回攪拌(回転指数1.0以上)
を得る為の、螺旋断面の高さと断面の底面長さの関係を
示すグラフである。実験条件は、螺旋の数を2としたこ
と以外は図3の場合と同様に設定した。尚、本発明にお
ける「螺旋断面の底面長さ」と「螺旋断面の高さ」は、
夫々図中(b)のwとhに対応する。
Spiral section height: 5 to 2 with respect to inner diameter
5% Bottom length of spiral cross section: 10 to 30 mm Fig. 6 (a) shows good swirling agitation (rotation index 1.0 or more)
5 is a graph showing the relationship between the height of the spiral cross section and the length of the bottom surface of the cross section for obtaining the following formula. The experimental conditions were set in the same manner as in FIG. 3 except that the number of spirals was two. In the present invention, the “bottom length of the spiral cross section” and the “height of the spiral cross section” are:
These correspond to w and h in FIG.

【0023】図6より、良好な回転指数を得る為には、
螺旋断面の高さを4〜20mm(内径に対して5〜25
%),螺旋断面の底面長さを10〜30mmにすること
が推奨される。このうち螺旋断面の高さは、使用する浸
漬ノズルの内径に応じて決定され、従って本発明では、
螺旋断面の高さを内径に対して5〜25%に特定するこ
とが好ましい。より好ましい下限値は8mm(内径に対
して10%)であり、一方、より好ましい上限値は16
mm(内径に対して20%)である。また、螺旋断面の
底面長さの下限値(10mm)は、溶鋼の衝突力に耐え
るだけの強度を確保するという観点から特定されるもの
である。より好ましい螺旋断面の底面長さは20mmで
ある。螺旋断面の底面長さの上限はノズル内に設けられ
る螺旋の段数によって決まり、底面長さを大きくするに
つれ、螺旋の段数は減少する為、実用上の観点から30
mm程度で充分である。尚、螺旋断面の形状は、図示す
る如く台形形状のものに限定されず、楕円状、円状等、
種々の形状を適宜採用することができる。
FIG. 6 shows that in order to obtain a good rotation index,
The height of the spiral cross section is 4 to 20 mm (5 to 25 mm
%), It is recommended that the bottom length of the spiral cross section be 10 to 30 mm. Among them, the height of the spiral cross section is determined according to the inner diameter of the immersion nozzle used, and therefore, in the present invention,
It is preferable to specify the height of the spiral cross section to be 5 to 25% of the inner diameter. A more preferred lower limit is 8 mm (10% of the inner diameter), while a more preferred upper limit is 16 mm.
mm (20% of the inner diameter). Further, the lower limit (10 mm) of the bottom length of the spiral cross section is specified from the viewpoint of securing strength enough to withstand the collision force of molten steel. More preferably, the bottom length of the spiral cross section is 20 mm. The upper limit of the bottom length of the spiral cross section is determined by the number of spirals provided in the nozzle. As the length of the bottom increases, the number of spirals decreases.
mm is sufficient. The shape of the spiral cross section is not limited to a trapezoidal shape as shown in the figure, but may be elliptical, circular, etc.
Various shapes can be appropriately adopted.

【0024】以下実施例を挙げて本発明をさらに詳細に
説明するが、下記実施例は本発明を制限するものではな
く、前・後記の趣旨を逸脱しない範囲で変更実施するこ
とは全て本発明の技術的範囲に包含される。
Hereinafter, the present invention will be described in more detail with reference to Examples. However, the following Examples do not limit the present invention, and all changes and implementations without departing from the spirit of the present invention will be described. Within the technical scope of

【0025】[0025]

【実施例】【Example】

実施例1 本実施例では、螺旋突起の形成によるノズル閉塞防止効
果および介在物の付着防止効果を調べた。具体的には、
螺旋の数:2,螺旋の下降角度:45゜,螺旋断面の高
さ:10mm,底面長さ:20mm,螺旋の終点:吐出
孔上端より120mmの構成からなる本発明ノズルと、
螺旋を有しない比較例のノズルを用い、上記効果につい
て比較検討した。ノズルの閉塞防止効果は、ノズル内壁
に付着したアルミナ等の付着量を示す「ノズル閉塞指
数」を用いて評価した。また、介在物の付着防止効果
は、超音波探傷による欠陥個数の指数を示す「介在物不
良欠陥指数」を用いて評価した。
Example 1 In this example, the effect of preventing the nozzle from being blocked and the effect of preventing the inclusion of inclusions from being formed by the spiral projection were examined. In particular,
The number of spirals: 2, the descending angle of the spiral: 45 °, the height of the spiral cross section: 10 mm, the bottom length: 20 mm, the end point of the spiral: 120 mm from the upper end of the discharge hole, and the nozzle of the present invention.
Using the nozzle of the comparative example having no spiral, the above effects were compared and studied. The effect of preventing nozzle blockage was evaluated using a “nozzle blockage index,” which indicates the amount of alumina or the like deposited on the inner wall of the nozzle. The effect of preventing inclusions from inclusions was evaluated using an “inclusion defect index,” which indicates an index of the number of defects by ultrasonic flaw detection.

【0026】図7にノズル閉塞指数の結果を、図8に介
在物不良欠陥指数の結果を、夫々示す。これらの図から
明らかな様に、本発明ノズルを用いれば、ノズル内面に
介在物が付着し難くなる為、ノズル内の閉塞を有効に防
止することができる。これは、本発明ノズルが、ノズル
内で溶鋼を充分回転することができたことに基づくもの
と考えられる。尚、比重の小さい介在物は、旋回攪拌速
度を高めてノズル中央部に該介在物を集中させ、ノズル
詰まり防止の為ノズル内に吹き込まれている不活性ガス
に捕捉される頻度を増加させてやれば、介在物による弊
害を低減することができる。
FIG. 7 shows the result of the nozzle blockage index, and FIG. 8 shows the result of the inclusion defect index. As is apparent from these figures, the use of the nozzle of the present invention makes it difficult for inclusions to adhere to the inner surface of the nozzle, so that blockage in the nozzle can be effectively prevented. This is considered to be based on the fact that the nozzle of the present invention was able to sufficiently rotate molten steel in the nozzle. In addition, the inclusion having a small specific gravity increases the swirling speed and concentrates the inclusion at the center of the nozzle, and increases the frequency of being caught by the inert gas blown into the nozzle in order to prevent nozzle clogging. By doing so, adverse effects due to inclusions can be reduced.

【0027】実施例2 本実施例では、本発明を最も特徴付ける螺旋状突起形成
による効果について、螺旋状溝の場合と比較検討した。
具体的には、表1に示す如く、2重螺旋または3重螺旋
からなるノズルにおいて、溝か突起かの区別を設けたこ
と以外は同一形状にし、実施例1と同様にしてノズル閉
塞指数および介在物不良欠陥指数を調べた。その結果を
表1に併記する。
Embodiment 2 In this embodiment, the effect of the formation of the spiral projection which characterizes the present invention most was compared with the case of the spiral groove.
More specifically, as shown in Table 1, a nozzle formed of a double helix or a triple helix has the same shape except that a distinction between a groove and a projection is provided. The inclusion defect index was investigated. The results are also shown in Table 1.

【0028】[0028]

【表1】 [Table 1]

【0029】表1より明らかな様に、螺旋状突起を設け
たNo.1〜6(本発明例)は、2重螺旋、3重螺旋のい
ずれの態様であっても、ノズル閉塞指数0.2〜0.
3,介在物不良欠陥指数0.05〜0.1と極めて小さ
くなっているのに対し、本発明の要件を満足しないNo.
7〜12(比較例)はいずれも、上記評価基準が、最も
小さいもので2.5(ノズル閉塞指数),1.4(介在
物不良欠陥指数)と、本発明例に比べて非常に大きくな
った。この様に、従来の螺旋状溝ではなく螺旋状突起を
設けることにより、ノズルの閉塞や介在物の付着等によ
る欠陥を極めて有効に防止できることが分かる。
As is evident from Table 1, No. 1 to No. 6 having spiral projections (Examples of the present invention) have a nozzle blockage index of 0.1 in any of the double spiral and triple spiral modes. 2-0.
3, the inclusion defect defect index is extremely small, 0.05 to 0.1, but is not satisfied with the requirements of the present invention.
In all of 7 to 12 (Comparative Examples), the above evaluation criteria were the smallest, 2.5 (nozzle clogging index) and 1.4 (inclusion defect defect index), which were much larger than those of the present invention. became. Thus, it can be understood that the provision of the spiral projection instead of the conventional spiral groove can extremely effectively prevent defects due to nozzle blockage and inclusion of inclusions.

【0030】実施例3 本実施例では、本発明で規定する種々の好ましい要件が
上記評価指数に及ぼす影響について調べた。具体的に
は、表2に示す如く、螺旋状突起を設けた各種ノズルの
形状を種々変化させ、実施例1と同様にしてノズル閉塞
指数および介在物不良欠陥指数を調べた。その結果を表
2に併記する。
Example 3 In this example, the effects of various desirable requirements defined in the present invention on the evaluation index were examined. Specifically, as shown in Table 2, the shapes of various nozzles provided with spiral projections were variously changed, and the nozzle blockage index and the inclusion defect index were examined in the same manner as in Example 1. The results are also shown in Table 2.

【0031】[0031]

【表2】 [Table 2]

【0032】まず、No.1,2は、夫々螺旋の数を1個
または4個にした例であるが、螺旋の数が2個または3
個である本発明例(表1のNo.1〜6)に比べて、上記
評価指数が大きくなっている。
First, Nos. 1 and 2 are examples in which the number of spirals is one or four, respectively, but the number of spirals is two or three.
The evaluation index is larger than that of the present invention examples (Nos. 1 to 6 in Table 1).

【0033】また、No.3〜6/No.7〜10は、螺旋
の始点/終点が本発明の好ましい要件を満足しない例で
あるが、本発明要件を満足する例(例えば表1のNo.
1,2,6等)に比べて上記評価指数が大きくなり、所
望の効果が得られない。
Nos. 3 to 6 / Nos. 7 to 10 are examples in which the starting point / ending point of the helix does not satisfy the preferred requirements of the present invention, but examples satisfying the requirements of the present invention (for example, No. 1 in Table 1). .
1, 2, 6, etc.), the evaluation index becomes large, and the desired effect cannot be obtained.

【0034】No.11〜14は、螺旋の下降角度が好ま
しくない例、No.15〜18は、螺旋断面の形状が好ま
しくない例であるが、本発明の好ましい要件を満足する
例(例えば表1のNo.2等)に比べて、ノズル閉塞効果
や介在物不良の低減効果に乏しい。
Nos. 11 to 14 are examples in which the descending angle of the spiral is not preferable, and Nos. 15 to 18 are examples in which the shape of the spiral cross section is not preferable. No. 1 of No. 2) and the like, the effect of blocking nozzles and the effect of reducing inclusion failure are poor.

【0035】[0035]

【発明の効果】本発明は上記の様に構成されているの
で、ノズル内の溶鋼を旋回攪拌させると共に鋳型内の偏
流を防止し得、しかもノズル内の介在物を低減し、ノズ
ル内の閉塞も防止可能な連続鋳造用浸漬ノズルを提供す
ることができる。
Since the present invention is configured as described above, the molten steel in the nozzle can be swirled and agitated, and the drift in the mold can be prevented. In addition, the inclusion in the nozzle can be reduced, and the nozzle can be blocked. Thus, it is possible to provide a continuous casting immersion nozzle capable of preventing the occurrence of the problem.

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

【図1】本発明の基本構成を示す断面図である。FIG. 1 is a sectional view showing a basic configuration of the present invention.

【図2】図1における螺旋の構成を示す為の断面図であ
る。
FIG. 2 is a sectional view showing a configuration of a spiral in FIG. 1;

【図3】螺旋の数と偏流度の関係を示すグラフである。FIG. 3 is a graph showing the relationship between the number of spirals and the degree of drift.

【図4】浸漬ノズル吐出孔の内径部上端からの距離と偏
流度の関係を示すグラフである。
FIG. 4 is a graph showing the relationship between the distance from the upper end of the inner diameter portion of the immersion nozzle discharge hole and the degree of drift.

【図5】螺旋の下降角度と回転指数の関係を示すグラフ
である。
FIG. 5 is a graph showing a relationship between a descending angle of a spiral and a rotation index.

【図6】螺旋断面の高さと断面の底面長さの関係を示す
グラフである。
FIG. 6 is a graph showing the relationship between the height of the spiral cross section and the bottom length of the cross section.

【図7】実施例1におけるノズル閉塞指数の結果を示す
グラフである。
FIG. 7 is a graph showing a result of a nozzle blockage index in Example 1.

【図8】実施例1における介在物不良欠陥指数の結果を
示すグラフである。
FIG. 8 is a graph showing the results of inclusion defect index in Example 1.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 内壁に螺旋状突起を設けたことを特徴と
する連続鋳造用浸漬ノズル。
1. An immersion nozzle for continuous casting, wherein a spiral projection is provided on an inner wall.
【請求項2】 前記螺旋の数が2個または3個である請
求項1に記載のノズル。
2. The nozzle according to claim 1, wherein the number of the spirals is two or three.
【請求項3】 前記螺旋の起点が、 2重螺旋の場合は、同一の高さで互いに170〜190
゜の位置にあり、 3重螺旋の場合は、同一の高さで互いに110〜130
゜の位置にあるものである請求項1または2に記載のノ
ズル。
3. When the starting point of the helix is a double helix, the starting point of the helix is 170 to 190 at the same height.
In the case of a triple helix, it is 110-130 with each other at the same height.
The nozzle according to claim 1, wherein the nozzle is located at a position ゜.
【請求項4】 前記螺旋の終点が、ノズル吐出孔の内径
部上端より少なくとも100mmの位置にある請求項1
〜3のいずれかに記載のノズル。
4. The end point of the spiral is at least 100 mm from the upper end of the inner diameter of the nozzle discharge hole.
4. The nozzle according to any one of items 1 to 3,
【請求項5】 前記螺旋の下降角度が20〜70゜であ
る請求項1〜4のいずれかに記載のノズル。
5. The nozzle according to claim 1, wherein a descending angle of the spiral is 20 to 70 °.
【請求項6】 前記螺旋断面の高さが、ノズル内径に対
し5〜25%であり、螺旋断面の底面長さが10〜30
mmである請求項1〜5のいずれかに記載のノズル。
6. The height of the spiral cross section is 5 to 25% with respect to the inner diameter of the nozzle, and the bottom length of the spiral cross section is 10 to 30%.
The nozzle according to any one of claims 1 to 5, wherein the diameter is in mm.
JP20359597A 1997-07-29 1997-07-29 Immersion nozzle for continuous casting Expired - Fee Related JP3673372B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20359597A JP3673372B2 (en) 1997-07-29 1997-07-29 Immersion nozzle for continuous casting

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20359597A JP3673372B2 (en) 1997-07-29 1997-07-29 Immersion nozzle for continuous casting

Publications (2)

Publication Number Publication Date
JPH1147896A true JPH1147896A (en) 1999-02-23
JP3673372B2 JP3673372B2 (en) 2005-07-20

Family

ID=16476676

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20359597A Expired - Fee Related JP3673372B2 (en) 1997-07-29 1997-07-29 Immersion nozzle for continuous casting

Country Status (1)

Country Link
JP (1) JP3673372B2 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005297022A (en) * 2004-04-13 2005-10-27 Shinagawa Refract Co Ltd Nozzle for continuously casting steel
JP2006346688A (en) * 2005-06-13 2006-12-28 Kurosaki Harima Corp Long nozzle with swing flow
JP2008006456A (en) * 2006-06-28 2008-01-17 Kyocera Corp Stoke and low pressure casting apparatus using it
JP2008105929A (en) * 2006-09-27 2008-05-08 Hoya Corp Molten glass delivery pipe, glass production apparatus, glass molding production method, and optical element production method
US7905432B2 (en) 2002-07-31 2011-03-15 Shinagawa Refractories Co., Ltd. Casting nozzle
JP2012031061A (en) * 2006-09-27 2012-02-16 Hoya Corp Method of manufacturing glass formed body, and method of manufacturing optical element
EP2835193A1 (en) * 2013-08-05 2015-02-11 Refractory Intellectual Property GmbH & Co. KG Refractory ceramic nozzle

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7905432B2 (en) 2002-07-31 2011-03-15 Shinagawa Refractories Co., Ltd. Casting nozzle
JP2005297022A (en) * 2004-04-13 2005-10-27 Shinagawa Refract Co Ltd Nozzle for continuously casting steel
JP2006346688A (en) * 2005-06-13 2006-12-28 Kurosaki Harima Corp Long nozzle with swing flow
JP4713956B2 (en) * 2005-06-13 2011-06-29 黒崎播磨株式会社 Swirl long nozzle
JP2008006456A (en) * 2006-06-28 2008-01-17 Kyocera Corp Stoke and low pressure casting apparatus using it
JP2008105929A (en) * 2006-09-27 2008-05-08 Hoya Corp Molten glass delivery pipe, glass production apparatus, glass molding production method, and optical element production method
JP2012031061A (en) * 2006-09-27 2012-02-16 Hoya Corp Method of manufacturing glass formed body, and method of manufacturing optical element
KR101252314B1 (en) * 2006-09-27 2013-04-08 호야 가부시키가이샤 Glass effluent pipe, glass manufacturing device, method for manufacturing glass moldings, and method for manufacturing optical elements
EP2835193A1 (en) * 2013-08-05 2015-02-11 Refractory Intellectual Property GmbH & Co. KG Refractory ceramic nozzle
CN105358273A (en) * 2013-08-05 2016-02-24 里弗雷克特里知识产权两合公司 Refractory ceramic nozzle
US20160250687A1 (en) * 2013-08-05 2016-09-01 Refractory Intellectual Property Gmbh & Co. Kg Refractory ceramic nozzle

Also Published As

Publication number Publication date
JP3673372B2 (en) 2005-07-20

Similar Documents

Publication Publication Date Title
JP4508110B2 (en) Immersion nozzle for continuous casting and continuous casting method using the same
JP4419934B2 (en) Method for continuous casting of molten metal
RU2140340C1 (en) Pouring nozzle for distributing liquid metal in mold at continuous casting of slabs
JPH1147896A (en) Immersion nozzle for continuous casting
US6533992B1 (en) Tundish
JP2934507B2 (en) Refractory articles to prevent vortices in metallurgical vessels
JPWO2011055484A1 (en) Method for continuous casting of molten metal
JP2004514562A (en) Immersion injection nozzle and method of using the same
JP2005125389A (en) Immersion nozzle for continuous casting
JP6577841B2 (en) Immersion nozzle
EP0587759A1 (en) Tundish turbulence suppressor pad.
JP2004001057A (en) Dipping nozzle for continuous casting of thin slab
JP3566904B2 (en) Steel continuous casting method
JP3460185B2 (en) Immersion nozzle for casting
JPH1147897A (en) Immersion nozzle for continuously casting thin and wide cast slab
JP2005199325A (en) Method of continuous casting for metal
JP2001129645A (en) Immersion nozzle for continuous casting and continuous casting method
KR200285346Y1 (en) collecter nozzle or submerged entry nozzle for continuous casting
JPH10128506A (en) Immersion nozzle for continuous casting
JPH04220148A (en) Molten steel supplying nozzle
JP3573096B2 (en) Manufacturing method of continuous cast slab
JP2005305489A (en) Method for continuously casting steel
JP2009125750A (en) Submerged nozzle for continuous casting
JP4595186B2 (en) Continuous casting method
JPS617054A (en) Flow regulating nozzle for continuous casting

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20040721

A521 Written amendment

Effective date: 20040803

Free format text: JAPANESE INTERMEDIATE CODE: A523

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20050112

A131 Notification of reasons for refusal

Effective date: 20050118

Free format text: JAPANESE INTERMEDIATE CODE: A131

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050314

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20050412

A61 First payment of annual fees (during grant procedure)

Effective date: 20050422

Free format text: JAPANESE INTERMEDIATE CODE: A61

R150 Certificate of patent (=grant) or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 3

Free format text: PAYMENT UNTIL: 20080428

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090428

Year of fee payment: 4

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100428

Year of fee payment: 5

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 5

Free format text: PAYMENT UNTIL: 20100428

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 6

Free format text: PAYMENT UNTIL: 20110428

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120428

Year of fee payment: 7

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 8

Free format text: PAYMENT UNTIL: 20130428

LAPS Cancellation because of no payment of annual fees