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JP6963192B2 - Immersion nozzle for continuous casting - Google Patents
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JP6963192B2 - Immersion nozzle for continuous casting - Google Patents

Immersion nozzle for continuous casting Download PDF

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JP6963192B2
JP6963192B2 JP2019228811A JP2019228811A JP6963192B2 JP 6963192 B2 JP6963192 B2 JP 6963192B2 JP 2019228811 A JP2019228811 A JP 2019228811A JP 2019228811 A JP2019228811 A JP 2019228811A JP 6963192 B2 JP6963192 B2 JP 6963192B2
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reduced diameter
diameter portion
cross
nozzle
sectional shape
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JP2021094585A (en
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宏泰 新妻
隆行 松長
亮太 岡崎
佳吾 藤田
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Shinagawa Refractories Co Ltd
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Description

本発明は、鋼の連続鋳造に用いられる連続鋳造用浸漬ノズルに関する。 The present invention relates to a dipping nozzle for continuous casting used for continuous casting of steel.

鋼の連続鋳造、特にスラブ連続鋳造に使用される連続鋳造用浸漬ノズルは、一般的にノズル側面に一対の吐出孔を有している。連続鋳造用浸漬ノズルを用いた鋼の鋳造においては、吐出孔を介してモールド内に供給される溶鋼流(以下、吐出流という)は一定ではなく常に変動することが知られている。そのため、吐出流全体としては浸漬ノズル内管側から外周側への流れ(正方向の流れ)であるのに対し、部分的に外周側からノズル内管側への吸い込み流(負方向の流れ)が発生する現象、すなわち吸い込み現象が発生する場合があることが知られている。 Immersion nozzles for continuous casting used for continuous casting of steel, particularly slab continuous casting, generally have a pair of discharge holes on the side surface of the nozzle. In the casting of steel using a dipping nozzle for continuous casting, it is known that the molten steel flow (hereinafter referred to as discharge flow) supplied into the mold through the discharge hole is not constant but constantly fluctuates. Therefore, the entire discharge flow is a flow from the inner tube side of the immersion nozzle to the outer peripheral side (flow in the positive direction), whereas a partial suction flow from the outer peripheral side to the inner tube side of the nozzle (flow in the negative direction). It is known that a phenomenon in which a suction phenomenon occurs, that is, a suction phenomenon may occur.

この吐出流の吸い込み現象が発生すると、通常は浸漬ノズル内部には到達しないモールドパウダースラグも吸い込まれ、ノズル内管の損傷につながり操業に支障をきたす可能性がある。また、通常とは異なる吐出流の状況となるため、介在物等により鋳片品質欠陥率が上昇する可能性がある。さらに、一度吸い込まれたモールドパウダースラグが吐出流によってモールドのより深い場所に運ばれることにより、浮上しきれずに鋳片に取り込まれて鋳片品質欠陥率の上昇の原因となる可能性がある。この吸い込み現象の原因としては、浸漬ノズル内に流入する溶鋼流に偏りがあることや、浸漬ノズル内管を介在物が閉塞すること等が挙げられる。 When the suction phenomenon of the discharge flow occurs, the mold powder slag that normally does not reach the inside of the immersion nozzle is also sucked, which may lead to damage to the inner pipe of the nozzle and hinder the operation. In addition, since the discharge flow condition is different from the usual one, there is a possibility that the slab quality defect rate may increase due to inclusions and the like. Further, once sucked mold powder slag is carried to a deeper part of the mold by the discharge flow, it may not be able to float and is taken into the slab, which may cause an increase in the slab quality defect rate. The cause of this suction phenomenon is that the molten steel flow flowing into the immersion nozzle is uneven, and that inclusions block the inner tube of the immersion nozzle.

浸漬ノズル内の溶鋼流の偏り(以下、偏流という)及び浸漬ノズル内管の閉塞を解決するための吐出孔の形状及び浸漬ノズル内管の構造については、例えば下記の特許文献に記載された構成を挙げることができる。
特許文献1には、吐出孔の寸法形状を横長形状とし、且つ内孔部断面積に対する吐出孔総断面積の比率が1.2以上2.6以下である浸漬ノズルが記載されている。
特許文献2には、浸漬ノズル内管に円状の縮径部を有する浸漬ノズルが記載されている。
特許文献3には、浸漬ノズル内管に段差状の縮径部を有する浸漬ノズルが記載されている。
特許文献4には、浸漬ノズル内管に複数の球状の突起を有する浸漬ノズルが記載されている。
特許文献5には、浸漬ノズル内管に複数の液滴状の突起を有する浸漬ノズルが記載されている。
特許文献6には、浸漬ノズル内管に複数の段状の突起を有する浸漬ノズルが記載されている。
The shape of the discharge hole and the structure of the immersion nozzle inner pipe for solving the bias of the molten steel flow in the immersion nozzle (hereinafter referred to as the drift) and the blockage of the immersion nozzle inner pipe are described in, for example, the following patent documents. Can be mentioned.
Patent Document 1 describes a dipping nozzle in which the dimensional shape of the discharge hole is a horizontally long shape and the ratio of the total cross-sectional area of the discharge hole to the cross-sectional area of the inner hole is 1.2 or more and 2.6 or less.
Patent Document 2 describes a dipping nozzle having a circular reduced diameter portion in the dipping nozzle inner tube.
Patent Document 3 describes a dipping nozzle having a stepped diameter-reduced portion in the dipping nozzle inner tube.
Patent Document 4 describes a dipping nozzle having a plurality of spherical protrusions on the dipping nozzle inner tube.
Patent Document 5 describes a dipping nozzle having a plurality of droplet-shaped protrusions on the inner tube of the dipping nozzle.
Patent Document 6 describes a dipping nozzle having a plurality of stepped protrusions on the dipping nozzle inner tube.

特開2001−129645号公報Japanese Unexamined Patent Publication No. 2001-129645 特開平4−220148号公報Japanese Unexamined Patent Publication No. 4-220148 特開平11−123509号公報Japanese Unexamined Patent Publication No. 11-123509 特開2004−255407号公報Japanese Unexamined Patent Publication No. 2004-255407 特開2005−297022号公報Japanese Unexamined Patent Publication No. 2005-297022 特開2004−283057号公報Japanese Unexamined Patent Publication No. 2004-283057

上記特許文献1〜6に記載の浸漬ノズルを用いることにより、浸漬ノズル内における偏流の解消及び浸漬ノズル内管の閉塞の防止について一定の効果を得ることができる。しかしながら、特許文献1〜6に記載の浸漬ノズルを用いても鋳造速度やモールドサイズ等の諸条件により吐出流の吸い込み現象が発生し、モールドパウダースラグの吸い込みが発生する場合がある。そのため、操業に支障をきたし、また鋳片品質欠陥率が上昇するという問題点を有していた。 By using the immersion nozzles described in Patent Documents 1 to 6, it is possible to obtain a certain effect on eliminating the drift in the immersion nozzle and preventing the inner tube of the immersion nozzle from being blocked. However, even if the immersion nozzles described in Patent Documents 1 to 6 are used, the suction of the discharge flow may occur depending on various conditions such as the casting speed and the mold size, and the suction of the mold powder slag may occur. Therefore, there is a problem that the operation is hindered and the slab quality defect rate increases.

本発明は、上記課題を解決するためになされたものであり、吐出流の吸い込み現象の発生を抑制し、モールドパウダースラグの吸い込みによる操業の支障及び鋳片品質欠陥の発生を抑制する連続鋳造用浸漬ノズルを提供することを目的とする。 The present invention has been made to solve the above problems, and is for continuous casting that suppresses the occurrence of the suction phenomenon of the discharge flow, hinders the operation due to the suction of the mold powder slag, and suppresses the occurrence of slab quality defects. It is an object of the present invention to provide an immersion nozzle.

本発明に係る連続鋳造用浸漬ノズルは、ノズル中心軸に沿って延在する内管を有する円筒状のノズル本体を備え、ノズル本体には内管に連通する吐出孔が形成され、吐出孔のうち少なくとも2つはノズル本体の側壁部に形成され、内管の上端はノズル本体の上端で開口してなる連続鋳造用浸漬ノズルであって、内管は、相似な形状を有する少なくとも2つの縮径部を備え、ノズル本体の側壁部に形成された吐出孔のうち2つの吐出孔の開口中心を通る吐出軸及びノズル中心軸を含む平面に沿って、ノズル本体を切断した場合のノズル本体の断面形状のうち、縮径部のうち最も下側に位置する最下縮径部の断面形状は、最下縮径部の断面形状の上端点と、最下縮径部の断面形状の下端点と、最下縮径部の断面形状の内管の径方向に対して最も突出する最縮径点とを頂点とする三角形に外接し、且つ上端点から最縮径点までの距離は下端点から最縮径点までの距離よりも大きい形状を有し、最下縮径部の上側に隣り合う隣接縮径部の断面形状と、最下縮径部の断面形状とは、隣接縮径部と最下縮径部との中間においてノズル中心軸に直交する面に対して鏡像対称であり、最下縮径部の断面形状の上端点及び下端点を通る直線から最縮径点までの距離と、縮径部以外の位置における内管の直径である内管径との比の値が、0.09以上0.12未満であり、最下縮径部の断面形状の下端点と、吐出孔の断面形状の上端との距離は、50mm以上200mm以下であり、最下縮径部の断面形状の最縮径点と、隣接縮径部の断面形状の最縮径点との距離は、50mm以上150mm以下である。 The immersion nozzle for continuous casting according to the present invention includes a cylindrical nozzle body having an inner tube extending along the central axis of the nozzle, and the nozzle body is formed with a discharge hole communicating with the inner tube. At least two of them are immersion nozzles for continuous casting formed on the side wall of the nozzle body, and the upper end of the inner pipe is opened at the upper end of the nozzle body, and the inner pipe has at least two contractions having a similar shape. The nozzle body is provided with a diameter portion and is formed when the nozzle body is cut along a plane including a discharge shaft passing through the opening centers of two discharge holes and a nozzle center shaft among the discharge holes formed on the side wall portion of the nozzle body. Of the cross-sectional shapes, the cross-sectional shape of the lowest reduced diameter portion located on the lowermost side of the reduced diameter portion is the upper end point of the cross-sectional shape of the lowest reduced diameter portion and the lower end point of the cross-sectional shape of the lowest reduced diameter portion. The distance from the upper end point to the lowest diameter point is the lower end point. The cross-sectional shape of the adjacent diameter-reduced portion, which has a shape larger than the distance from the diameter-to-maximum diameter-reduced portion and is adjacent to the upper side of the bottom-reduced diameter portion, and the cross-sectional shape of the bottom-reduced diameter portion are the adjacent diameter-reduced portions. and Ri mirror symmetry der respect to a plane perpendicular to the nozzle central axis in the middle of the lowermost reduced diameter portion, the straight line passing through the upper point and lower point of the cross-sectional shape of the bottom reduced-diameter portion to the outermost contraction径点The value of the ratio of the distance to the inner diameter, which is the diameter of the inner pipe at a position other than the reduced diameter portion, is 0.09 or more and less than 0.12. The distance from the upper end of the cross-sectional shape of the discharge hole is 50 mm or more and 200 mm or less, and the distance between the most contracted diameter point of the cross-sectional shape of the lowest diameter-reduced portion and the most contracted diameter point of the cross-sectional shape of the adjacent diameter-reduced portion is , 50 mm or more and 150 mm or less.

また、ノズル本体の断面形状は、2つの吐出孔の開口中心を通る吐出軸及びノズル中心軸を含む平面に沿ってノズル本体を切断した場合の断面形状であって、最下縮径部の断面形状の上端点及び下端点を通る直線から最縮径点までの距離と、縮径部以外の位置における内管の直径である内管径との比の値が、0.09以上0.12未満であってもよい。
また、最下縮径部の断面形状の下端点と、吐出孔の断面形状の上端との距離は、50mm以上200mm以下であってもよい。
また、最下縮径部の断面形状の最縮径点と、隣接縮径部の断面形状の最縮径点との距離は、50mm以上150mm以下であってもよい。
Further, the cross-sectional shape of the nozzle body is a cross-sectional shape when the nozzle body is cut along a plane including a discharge shaft passing through the opening centers of the two discharge holes and the nozzle center shaft, and is a cross section of the lowest diameter-reduced portion. The value of the ratio of the distance from the straight line passing through the upper end point and the lower end point of the shape to the most reduced diameter point and the inner diameter of the inner pipe at a position other than the reduced diameter portion is 0.09 or more and 0.12. It may be less than.
Further, the distance between the lower end point of the cross-sectional shape of the lowermost reduced diameter portion and the upper end of the cross-sectional shape of the discharge hole may be 50 mm or more and 200 mm or less.
Further, the distance between the most reduced diameter point of the cross-sectional shape of the lowest reduced diameter portion and the most reduced diameter point of the cross-sectional shape of the adjacent reduced diameter portion may be 50 mm or more and 150 mm or less.

本発明によれば、浸漬ノズルのノズル本体の内管に、適切な形状の最下縮径部と、最下縮径部に隣接する隣接縮径部とが形成され、隣接縮径部の断面形状と最下縮径部の断面形状とは、隣接縮径部と最下縮径部との中間においてノズル中心軸に直交する水平面に対して鏡像対称に形成されているため、吐出流の吸い込み現象の発生を抑制し、モールドパウダースラグの吸い込みによる操業の支障及び鋳片品質欠陥の発生を抑制することができる。 According to the present invention, the inner pipe of the nozzle body of the immersion nozzle is formed with a bottom reduced diameter portion having an appropriate shape and an adjacent reduced diameter portion adjacent to the lowest reduced diameter portion, and a cross section of the adjacent reduced diameter portion. Since the shape and the cross-sectional shape of the lowest reduced diameter portion are formed symmetrically with respect to the horizontal plane orthogonal to the nozzle center axis between the adjacent reduced diameter portion and the lowest reduced diameter portion, the suction of the discharge flow is absorbed. It is possible to suppress the occurrence of the phenomenon, and it is possible to suppress the hindrance of operation and the occurrence of slab quality defects due to the suction of the mold powder slag.

本発明の実施の形態1に係る連続鋳造用浸漬ノズルの断面図である。It is sectional drawing of the immersion nozzle for continuous casting which concerns on Embodiment 1 of this invention. 図1に記載の下流縮径部、上流縮径部及び吐出孔を示す断面図である。It is sectional drawing which shows the downstream diameter-reducing part, the upstream-diameter part and the discharge hole which are shown in FIG. 図2に記載の下流縮径部を示す断面図である。It is sectional drawing which shows the downstream diameter reduction part described in FIG. 図2に記載の上流縮径部を示す断面図である。It is sectional drawing which shows the upstream diameter reduction part described in FIG. 従来の浸漬ノズルの吐出流のベクトル図である。It is a vector diagram of the discharge flow of the conventional immersion nozzle. 従来の浸漬ノズルの吐出流付近における溶鋼の流速分布を示す図であるIt is a figure which shows the flow velocity distribution of molten steel in the vicinity of the discharge flow of the conventional immersion nozzle. 図1に記載の連続鋳造用浸漬ノズルの吐出流のベクトル図である。It is a vector figure of the discharge flow of the immersion nozzle for continuous casting which is shown in FIG. 図1に記載の連続鋳造用浸漬ノズルの吐出流付近における溶鋼の流速分布を示す図である。It is a figure which shows the flow velocity distribution of molten steel in the vicinity of the discharge flow of the immersion nozzle for continuous casting described in FIG. 本発明の実施の形態2に係る連続鋳造用浸漬ノズルの断面図である。It is sectional drawing of the immersion nozzle for continuous casting which concerns on Embodiment 2 of this invention.

実施の形態1.
以下、実施の形態1について図面を参照して詳細に説明する。
図1に示すように、連続鋳造用浸漬ノズル1は、鋼を連続鋳造するための浸漬ノズルであり、鉛直方向に延びる円柱状形状のノズル本体10を有している。ノズル本体10は、耐火物により形成されている。この耐火物としては、例えばアルミナ−黒鉛質、マグネシア−黒鉛質、スピネル−黒鉛質、ジルコニア−黒鉛質、アルミナ質、粘土質、スピネル質、溶融石英質等を適宜に使用することができる。なお、ノズル本体10及び後述する内管11の各部分の表面材質等の詳細な構成は既知であるため説明を省略する。
Embodiment 1.
Hereinafter, the first embodiment will be described in detail with reference to the drawings.
As shown in FIG. 1, the continuous casting immersion nozzle 1 is an immersion nozzle for continuously casting steel, and has a columnar nozzle body 10 extending in the vertical direction. The nozzle body 10 is made of a refractory material. As the refractory, for example, alumina-graphite, magnesia-graphite, spinel-graphite, zirconia-graphite, alumina, clay, spinel, molten quartz and the like can be appropriately used. Since the detailed configuration of the surface material and the like of each part of the nozzle body 10 and the inner tube 11 described later is known, the description thereof will be omitted.

ノズル本体10の内部には内管11が形成されている。内管11は、鋼の連続鋳造時に溶鋼をタンディッシュから鋳型内に注入する際の溶鋼の流路を形成している。内管11は、ノズル本体10の中心軸であり鉛直方向に延びるノズル中心軸12に沿って、上端であるノズル上端10aから下端であるノズル下端10bへ延在している。溶鋼は、内管11を上流側のノズル上端10a側から下流側のノズル下端10b側へと流動する。なお、以下の説明において「上側」とは、ノズル本体10におけるノズル中心軸12に沿った鉛直方向上側をいい、「下側」とは、ノズル本体10におけるノズル中心軸12に沿った鉛直方向下側をいう。 An inner tube 11 is formed inside the nozzle body 10. The inner pipe 11 forms a flow path for the molten steel when the molten steel is injected into the mold from the tundish during continuous casting of the steel. The inner tube 11 extends from the upper end 10a of the nozzle to the lower end 10b of the nozzle along the central axis 12 of the nozzle body 10 which is the central axis of the nozzle body 10 and extends in the vertical direction. The molten steel flows through the inner pipe 11 from the upstream nozzle upper end 10a side to the downstream nozzle lower end 10b side. In the following description, the "upper side" means the upper side in the vertical direction along the nozzle central axis 12 in the nozzle body 10, and the "lower side" means the lower side in the vertical direction along the nozzle central axis 12 in the nozzle body 10. Refers to the side.

ノズル本体10の側壁部13には、吐出孔14が2個形成されている。各吐出孔14はノズル下端10bの上側に設けられている。各吐出孔14は内管11に接続されており、内管11とノズル本体10の周囲の空間とを連通している。また、各吐出孔14は互いに対向する位置に形成されており、各吐出孔14の開口中心20を通る軸である吐出軸21は、ノズル中心軸12に直交している。すなわち図1は、直交するノズル中心軸12及び吐出軸21を含む平面に沿ってノズル本体10を切断した場合の断面図である。以下の説明において、ノズル本体10に含まれる各部の断面形状とは図1に示す断面形状をいう。 Two discharge holes 14 are formed in the side wall portion 13 of the nozzle body 10. Each discharge hole 14 is provided above the lower end 10b of the nozzle. Each discharge hole 14 is connected to an inner pipe 11 and communicates the inner pipe 11 with the space around the nozzle body 10. Further, the discharge holes 14 are formed at positions facing each other, and the discharge shaft 21 which is an axis passing through the opening center 20 of each discharge hole 14 is orthogonal to the nozzle center axis 12. That is, FIG. 1 is a cross-sectional view of the nozzle body 10 cut along a plane including the orthogonal nozzle central shaft 12 and the discharge shaft 21. In the following description, the cross-sectional shape of each part included in the nozzle body 10 means the cross-sectional shape shown in FIG.

各吐出孔14は、内管11を流れる溶鋼がノズル本体10の外部へ流出する流路を形成している。内管11を流れる溶鋼が各吐出孔14から流出することで、鋳型(モールド)内に溶鋼が注入される。 Each discharge hole 14 forms a flow path through which the molten steel flowing through the inner pipe 11 flows out to the outside of the nozzle body 10. The molten steel flowing through the inner pipe 11 flows out from each discharge hole 14, so that the molten steel is injected into the mold.

各吐出孔14の開口部の最上辺と上側の内管11とを接続する吐出孔上部14aの断面形状は、下側が径方向外側に拡大するように直線を組み合わせた二段テーパとして形成されている。各吐出孔14の開口部の最下辺と内管11とを接続する吐出孔下部14bの断面形状は、下側が径方向外側へ拡大するように形成されている。各吐出孔14の上側には、下流縮径部15が形成されている。下流縮径部15の上側には、上流縮径部16が形成されている。下流縮径部15は、内管11において最も下側に位置する縮径部、すなわち最下縮径部を構成している。また、上流縮径部16は、内管11において最下段の縮径部である下流縮径部15の上側に隣り合う縮径部、すなわち隣接縮径部を構成している。 The cross-sectional shape of the discharge hole upper portion 14a connecting the uppermost side of the opening of each discharge hole 14 and the upper inner pipe 11 is formed as a two-step taper in which straight lines are combined so that the lower side expands radially outward. There is. The cross-sectional shape of the discharge hole lower portion 14b connecting the lowermost side of the opening of each discharge hole 14 and the inner pipe 11 is formed so that the lower side expands radially outward. A downstream diameter reduction portion 15 is formed on the upper side of each discharge hole 14. An upstream reduced diameter portion 16 is formed on the upper side of the downstream reduced diameter portion 15. The downstream reduced diameter portion 15 constitutes a reduced diameter portion located at the lowermost side in the inner pipe 11, that is, a lowest reduced diameter portion. Further, the upstream reduced diameter portion 16 constitutes a reduced diameter portion adjacent to the upper side of the downstream reduced diameter portion 15, which is the lowermost reduced diameter portion in the inner pipe 11, that is, an adjacent reduced diameter portion.

図2に示すように、図1に示した吐出孔14、下流縮径部15及び上流縮径部16の断面形状のうち左側のものを拡大して説明する。なお、図1における右側の吐出孔14、下流縮径部15及び上流縮径部16は、ノズル中心軸12に対して左側の吐出孔14、下流縮径部15及び上流縮径部16と鏡像対称であるため説明は省略する。 As shown in FIG. 2, the cross-sectional shape of the discharge hole 14, the downstream reduced diameter portion 15 and the upstream reduced diameter portion 16 shown in FIG. 1 will be described in an enlarged manner on the left side. The right discharge hole 14, the downstream reduced diameter portion 15 and the upstream reduced diameter portion 16 in FIG. 1 are mirror images of the left discharge hole 14, the downstream reduced diameter portion 15 and the upstream reduced diameter portion 16 with respect to the nozzle central axis 12. Since it is symmetric, the description is omitted.

下流縮径部15の断面形状は、鉛直方向における上端点15aと、鉛直方向における下端点15bと、上端点15a及び下端点15bとの間の位置において内管11の径方向に対して最も突出している最縮径点15cとを有している。上端点15aと最縮径点15cと下端点15bとは曲線15dにより接続されている。下端点15bと吐出孔14の最上辺14cとの距離Fは、50mm以上200mm以下となるように形成されている。 The cross-sectional shape of the downstream reduced diameter portion 15 projects most in the radial direction of the inner pipe 11 at a position between the upper end point 15a in the vertical direction, the lower end point 15b in the vertical direction, and the upper end point 15a and the lower end point 15b. It has a maximum contraction point of 15c. The upper end point 15a, the outermost diameter point 15c, and the lower end point 15b are connected by a curve 15d. The distance F between the lower end point 15b and the uppermost side 14c of the discharge hole 14 is formed so as to be 50 mm or more and 200 mm or less.

上流縮径部16の断面は、鉛直方向における上端点16bと、鉛直方向における下端点16aと、上端点16b及び下端点16aとの間の位置において内管11の径方向に対して最も突出している最縮径点16cとを有している。上端点16bと最縮径点16cと下端点16aとは曲線16dにより接続されている。 The cross section of the upstream reduced diameter portion 16 projects most in the radial direction of the inner pipe 11 at a position between the upper end point 16b in the vertical direction, the lower end point 16a in the vertical direction, and the upper end point 16b and the lower end point 16a. It has a maximum contraction point 16c. The upper end point 16b, the outermost diameter point 16c, and the lower end point 16a are connected by a curve 16d.

このとき、下流縮径部15の上端点15aと上流縮径部16の下端点16aとの中間において、ノズル中心軸12に直交する面を構成する水平面17を考えると、下流縮径部15の断面と上流縮径部16の断面とは水平面17に対して鏡像対称に形成されている。また、下流縮径部15の最縮径点15cと、上流縮径部16の最縮径点16cとの距離Gは50mm以上150mm以下となるように形成されている。 At this time, considering the horizontal plane 17 forming a plane orthogonal to the nozzle central axis 12 between the upper end point 15a of the downstream reduced diameter portion 15 and the lower end point 16a of the upstream reduced diameter portion 16, the downstream reduced diameter portion 15 The cross section and the cross section of the upstream reduced diameter portion 16 are formed symmetrically with respect to the horizontal plane 17. Further, the distance G between the maximum reduction point 15c of the downstream reduction portion 15 and the maximum reduction point 16c of the upstream reduction portion 16 is formed to be 50 mm or more and 150 mm or less.

図3に示すように下流縮径部15の断面において、上端点15aと下端点15bと最縮径点15cとを頂点とする、破線により示す不等辺の三角形15eを考えると、上端点15aと下端点15bとを接続する線分15f及び曲線15dにより構成される閉曲線が該三角形15eに外接している。すなわち、該閉曲線を構成する下流縮径部15の断面は、三角形15eに外接している。また、線分15fは、上端点15aと下端点15bとを通る直線の一部であって、内管11の壁面上に延びている。 As shown in FIG. 3, in the cross section of the downstream reduced diameter portion 15, considering the unequal side triangle 15e shown by the broken line having the upper end point 15a, the lower end point 15b, and the maximum reduced diameter point 15c as vertices, the upper end point 15a and A closed curve composed of a line segment 15f connecting the lower end point 15b and a curve 15d circumscribes the triangle 15e. That is, the cross section of the downstream reduced diameter portion 15 forming the closed curve circumscribes the triangle 15e. Further, the line segment 15f is a part of a straight line passing through the upper end point 15a and the lower end point 15b, and extends on the wall surface of the inner pipe 11.

上端点15aと最縮径点15cとの距離L1と、下端点15bと最縮径点15cとの距離L3とは、L1がL3よりも大きくなるように下流縮径部15は形成されている。また、線分15fと最縮径点15cとの距離H1と、下流縮径部15及び上流縮径部16(図2参照)以外の位置における内管11の直径である内管径D(図1及び図2参照)との比の値H1/Dは、0.09以上0.12以下となるように下流縮径部15は形成されている。 The distance L1 between the upper end point 15a and the maximum reduction point 15c and the distance L3 between the lower end point 15b and the maximum reduction point 15c are such that the downstream reduction portion 15 is formed so that L1 is larger than L3. .. Further, the inner diameter D (FIG. 2), which is the diameter of the inner pipe 11 at positions other than the distance H1 between the line segment 15f and the maximum diameter reduction point 15c and the downstream reduction portion 15 and the upstream reduction portion 16 (see FIG. 2). The downstream diameter reduction portion 15 is formed so that the value H1 / D of the ratio to 1 and FIG. 2) is 0.09 or more and 0.12 or less.

下流縮径部15の断面と上流縮径部16の断面とは水平面17に対して鏡像対称に形成されていることから、図4に示すように上流縮径部16の断面において、上端点16bと下端点16aと最縮径点16cとを頂点とする、破線により示す不等辺の三角形16eを考えると、上端点16bと下端点16aとを接続する線分16f及び曲線16dにより構成される閉曲線が該三角形16eに外接している。すなわち、該閉曲線を構成する上流縮径部16の断面は、三角形16eに外接している。また、線分16fは、上端点16bと下端点16aとを通る直線の一部であって、内管11の壁面上に延びている。 Since the cross section of the downstream reduced diameter portion 15 and the cross section of the upstream reduced diameter portion 16 are formed symmetrically with respect to the horizontal plane 17, the upper end point 16b is formed in the cross section of the upstream reduced diameter portion 16 as shown in FIG. Considering an unequal-sided triangle 16e indicated by a broken line with the apex of the lower end point 16a and the outermost diameter point 16c, a closed curve composed of a line segment 16f and a curve 16d connecting the upper end point 16b and the lower end point 16a. Is circumscribing the triangle 16e. That is, the cross section of the upstream reduced diameter portion 16 forming the closed curve circumscribes the triangle 16e. Further, the line segment 16f is a part of a straight line passing through the upper end point 16b and the lower end point 16a, and extends on the wall surface of the inner pipe 11.

下端点16aと最縮径点16cとの距離L2と、上端点16bと最縮径点16cとの距離L4とは、L2がL4よりも大きくなるように上流縮径部16は形成されている。また、上端点16bと下端点16aとを接続する線分である16fと最縮径点16cとの距離H1と、下流縮径部15及び上流縮径部16以外の位置における内管11の直径である内管径Dとの比の値H2/Dは、0.09以上0.12以下となるように上流縮径部16は形成されている。 The distance L2 between the lower end point 16a and the maximum reduction point 16c and the distance L4 between the upper end point 16b and the maximum reduction point 16c are such that the upstream reduction portion 16 is formed so that L2 is larger than L4. .. Further, the distance H1 between 16f, which is a line segment connecting the upper end point 16b and the lower end point 16a, and the maximum diameter reduction point 16c, and the diameter of the inner pipe 11 at a position other than the downstream reduction portion 15 and the upstream reduction portion 16. The upstream diameter reduction portion 16 is formed so that the value H2 / D of the ratio to the inner diameter D is 0.09 or more and 0.12 or less.

次に、従来の浸漬ノズルにおける鋳造時の吐出孔近傍における吐出流の状態について説明する。従来の浸漬ノズルによる連続鋳造中に、モールドパウダースラグの吸い込みの発生につながる吐出流の吸い込み流(負方向の流れ)が発生する場合がある。鋳造時に吸い込み流が発生した鋳造ノズルと同じ形状の鋳造ノズル形状を用い、発生時の鋳造条件に対応させて実施された水モデル試験を実施することより、この吸い込み流の発生頻度が高い位置は吐出孔の上側であることが判明している。 Next, the state of the discharge flow in the vicinity of the discharge hole at the time of casting in the conventional immersion nozzle will be described. During continuous casting with a conventional immersion nozzle, a suction flow (negative direction flow) of a discharge flow that leads to the generation of suction of mold powder slag may occur. By using a casting nozzle shape that has the same shape as the casting nozzle that generated the suction flow during casting and conducting a water model test that was carried out in response to the casting conditions at the time of generation, the position where the suction flow is frequently generated is located. It is known to be above the discharge hole.

上記水モデル試験と同じ条件において、コンピュータによる流体解析を実施したところ、吸い込み流が発生しているモデルでは、鉛直方向上側から流下してくる溶鋼流は浸漬ノズルの内管の壁面部分においては遅い状態であることが判明している。また、吐出孔部においてはそれまで略鉛直方向下向きに流れていた溶鋼流が急激に流れる方向を変えるが、その際に吐出孔上面から吐出流が剥離した状態となることが判明している。 When fluid analysis was performed by computer under the same conditions as the above water model test, in the model in which the suction flow was generated, the molten steel flow flowing down from the upper side in the vertical direction was slow on the wall surface of the inner pipe of the immersion nozzle. It is known to be in a state. Further, in the discharge hole portion, it has been found that the molten steel flow, which had been flowing downward in the substantially vertical direction until then, suddenly changes the direction of flow, but at that time, the discharge flow is separated from the upper surface of the discharge hole.

吐出流の剥離が発生すると、剥離が発生した該領域において溶鋼流の圧力が低下して吐出流の逆流が生じることが知られている。浸漬ノズルの吐出孔部においては、溶鋼流が内管から吐出孔へ流入する箇所において吐出流の剥離が発生しやすいため、剥離箇所の下流側にあたる吐出孔上部の領域において逆流が発生する可能性が高い。この吐出流の剥離領域が拡大し、逆流が吐出孔外側にまで影響を及ぼす場合に、吸い込み流となることが判明している。 It is known that when the discharge flow is peeled off, the pressure of the molten steel flow is reduced in the region where the peeling occurs, and the discharge flow is backflowed. In the discharge hole of the immersion nozzle, the discharge flow is likely to peel off at the point where the molten steel flow flows from the inner pipe to the discharge hole, so there is a possibility that backflow will occur in the area above the discharge hole on the downstream side of the peeling point. Is high. It has been found that when the peeling region of the discharge flow expands and the backflow affects the outside of the discharge hole, it becomes a suction flow.

浸漬ノズルにおいて内管の一部分に縮径領域を形成することにより、該縮径領域において溶鋼流が集中し、該縮径領域を通過後に再び拡散する。このときに溶鋼流が整流化され、偏流が解消されることが一般的に知られている。しかしながら、整流化した溶鋼流は中心部の流速が大きく、内管壁面部の流速は比較的小さい。このため、そのまま溶鋼流が吐出孔部へ流入すると、大きな吐出流の剥離領域が発生する。 By forming a reduced diameter region in a part of the inner pipe in the immersion nozzle, the molten steel flow is concentrated in the reduced diameter region and diffuses again after passing through the reduced diameter region. At this time, it is generally known that the molten steel flow is rectified and the drift is eliminated. However, the rectified molten steel flow has a large flow velocity in the central portion and a relatively small flow velocity in the inner pipe wall surface portion. Therefore, if the molten steel flow flows into the discharge hole as it is, a large peeling region of the discharge flow is generated.

これに対して、鉛直方向に沿って浸漬ノズルの内管に縮径部を複数段設けることにより、最下段の一段上の縮径部で溶鋼流を一旦集中させ、偏流を解消した後にその下流で緩やかに内管径を拡大、縮小させ、さらに最下段の縮径部の下流において再び内径部を拡大する構成を用いることができる。この構成を用いることにより、このような内管形状の最下段を溶鋼が通過した後に縮径部の下流に強い剥離領域が発生し、縮径部の下流の剥離領域とそれ以外の領域との圧力差により縮径部通過後の溶鋼流は内管壁面に強く引き付けられる。これにより、内管壁面の近傍における溶鋼流の流速が大きくなる。そして、内管壁面近傍の流速が大きい状態で吐出孔へ溶鋼が流入することで、吐出孔から吐出された吐出流の剥離領域の発達を抑制することが可能となることが知られている。 On the other hand, by providing a plurality of diameter-reduced portions in the inner pipe of the immersion nozzle along the vertical direction, the molten steel flow is once concentrated at the diameter-reduced portion one step above the bottom stage to eliminate the drift, and then downstream thereof. It is possible to use a configuration in which the inner pipe diameter is gradually expanded or contracted, and the inner diameter portion is expanded again downstream of the diameter-reduced portion in the lowermost stage. By using this configuration, a strong peeling region is generated downstream of the reduced diameter portion after the molten steel has passed through the lowermost stage of such an inner pipe shape, and the peeling region downstream of the reduced diameter portion and the other region Due to the pressure difference, the molten steel flow after passing through the reduced diameter portion is strongly attracted to the inner pipe wall surface. As a result, the flow velocity of the molten steel flow in the vicinity of the inner pipe wall surface increases. Then, it is known that the development of the peeled region of the discharge flow discharged from the discharge hole can be suppressed by the molten steel flowing into the discharge hole in a state where the flow velocity in the vicinity of the inner pipe wall surface is high.

従来の浸漬ノズルにおいても、複数段の縮径部が形成されている例が知られている。例えば特許文献3には、内管に鉛直方向に沿って特定の範囲にわたって形成された縮径部を複数段有する浸漬ノズルが記載されている。この浸漬ノズルは、縮径部における内管径を小径化すると浸漬ノズルの内管を通過し得る溶鋼の単位時間当たり流量、すなわちスループットが減少してしまうため、縮径部の内管径を小径化することが困難であるということが知られている。 It is known that even in the conventional immersion nozzle, a plurality of steps of reduced diameter portions are formed. For example, Patent Document 3 describes a dipping nozzle having a plurality of stages of reduced diameter portions formed in an inner tube over a specific range along a vertical direction. In this immersion nozzle, if the inner pipe diameter in the reduced diameter portion is reduced, the flow rate per unit time of molten steel that can pass through the inner pipe of the immersion nozzle, that is, the throughput, is reduced. It is known that it is difficult to change.

また例えば特許文献5には、浸漬ノズルの水平方向において非連続な複数の突起を形成して縮径部とする構成が記載されている。この浸漬ノズルは、流下する溶鋼流を内管壁面に引き寄せる効果が乏しく、吐出孔から吐出された溶鋼流の剥離を抑制することが困難であることが知られている。 Further, for example, Patent Document 5 describes a configuration in which a plurality of discontinuous protrusions are formed in the horizontal direction of the immersion nozzle to form a reduced diameter portion. It is known that this immersion nozzle has little effect of attracting the flowing molten steel flow to the inner pipe wall surface, and it is difficult to suppress the peeling of the molten steel flow discharged from the discharge hole.

一方、この発明の実施の形態1に係る連続鋳造用浸漬ノズル1は、上記において説明した通り、図2に示すようにノズル本体10の内管11に下流縮径部15及び上流縮径部16の2個の縮径部を有している。また、図3に示すように、下流縮径部15の断面は不等辺な三角形15eに外接しており、図4に示すように上流縮径部16の断面は不等辺な三角形16eに内接している。また、下流縮径部15(図3参照)は、その断面形状について、上端点15aと最縮径点15cとの距離L1が、下端点15bと最縮径点15cとの距離L3よりも大きくなるように形成されており、上流縮径部16(図4参照)は、その断面形状について、下端点16aと最縮径点16cとの距離L2が、上端点16bと最縮径点16cとの距離L4よりも大きくなるように形成されている。そして、図2に示すように、下流縮径部15の断面形状と上流縮径部16の断面形状とが水平面17に対して鏡像対称になるように、下流縮径部15及び上流縮径部16は形成されている。 On the other hand, as described above, the immersion nozzle 1 for continuous casting according to the first embodiment of the present invention has a downstream reduced diameter portion 15 and an upstream reduced diameter portion 16 in the inner pipe 11 of the nozzle body 10 as shown in FIG. It has two reduced diameter portions. Further, as shown in FIG. 3, the cross section of the downstream reduced diameter portion 15 circumscribes the isosceles triangle 15e, and as shown in FIG. 4, the cross section of the upstream reduced diameter portion 16 is inscribed in the isosceles triangle 16e. ing. Further, regarding the cross-sectional shape of the downstream reduced diameter portion 15 (see FIG. 3), the distance L1 between the upper end point 15a and the maximum reduced diameter point 15c is larger than the distance L3 between the lower end point 15b and the maximum reduced diameter point 15c. The upstream diameter reduction portion 16 (see FIG. 4) has a cross-sectional shape in which the distance L2 between the lower end point 16a and the maximum diameter reduction point 16c is the upper end point 16b and the maximum diameter reduction point 16c. It is formed so as to be larger than the distance L4 of. Then, as shown in FIG. 2, the downstream reduced diameter portion 15 and the upstream reduced diameter portion 15 and the upstream reduced diameter portion so that the cross-sectional shape of the downstream reduced diameter portion 15 and the cross-sectional shape of the upstream reduced diameter portion 16 are mirror image symmetric with respect to the horizontal plane 17. 16 is formed.

連続鋳造用浸漬ノズル1は、内管11の下流縮径部15が上記の形状を有していることにより、内管11を通過可能な溶鋼のスループットに大きな影響を与えることなく、最下段の縮径部である下流縮径部15における内管径を従来の浸漬ノズルよりも小径化することが可能となる。そのため、下流縮径部15における内管11の最小径である最縮径点16cに対して、その下流における内管11の径をより大径化することが可能となる。これにより、下流縮径部15の通過後に下流に溶鋼流の強い剥離域が発生し、剥離部とそれ以外の領域との圧力差により、下流縮径部15通過後の溶鋼流を内管11の壁面に強く引き付けられる効果をより大きくすることが可能となる。 In the continuous casting immersion nozzle 1, the downstream diameter-reduced portion 15 of the inner pipe 11 has the above-mentioned shape, so that the lowermost stage of the immersion nozzle 1 does not significantly affect the throughput of molten steel that can pass through the inner pipe 11. The inner pipe diameter of the downstream reduced diameter portion 15 which is the reduced diameter portion can be made smaller than that of the conventional immersion nozzle. Therefore, the diameter of the inner pipe 11 in the downstream can be made larger than the maximum diameter point 16c which is the minimum diameter of the inner pipe 11 in the downstream reduced diameter portion 15. As a result, a strong peeling region of the molten steel flow is generated downstream after passing through the downstream reduced diameter portion 15, and due to the pressure difference between the peeled portion and the other region, the molten steel flow after passing through the downstream reduced diameter portion 15 is passed through the inner pipe 11. It is possible to increase the effect of being strongly attracted to the wall surface of.

また、最下段の縮径部である下流縮径部15の断面形状とその一段上の上流縮径部16の断面形状とが水平面17に対して鏡像対称となるように、下流縮径部15及び上流縮径部16を形成し、さらに上流縮径部16と下流縮径部15との間の内管径の変化を緩やかな変化とすることにより、下流縮径部15を通過した後の内管径Dの拡大による溶鋼流の内管11の壁面への引き寄せ効果を最大限に発揮させることが可能となる。 Further, the downstream reduced diameter portion 15 is such that the cross-sectional shape of the downstream reduced diameter portion 15 which is the lowermost reduced diameter portion and the cross-sectional shape of the upstream reduced diameter portion 16 one step above the reduced diameter portion are mirror image symmetric with respect to the horizontal plane 17. After passing through the downstream reduced diameter portion 15 by forming the upstream reduced diameter portion 16 and making the change in the inner pipe diameter between the upstream reduced diameter portion 16 and the downstream reduced diameter portion 15 a gradual change. By expanding the inner pipe diameter D, it is possible to maximize the effect of attracting the molten steel flow to the wall surface of the inner pipe 11.

下流縮径部15の最大縮径部である最縮径点15cと内管11の壁面上に延びる線分15fとの距離H1、及び上流縮径部16の最大縮径部である最縮径点16cと内管11の壁面上に延びる線分16fとの距離H2は、流下する溶鋼流の整流化と、上流縮径部16及び下流縮径部15を通過した溶鋼流の内管11の壁面への引き寄せ効果とに顕著な影響を及ぼすことが知られている。距離H1と内管11の内管径Dとの比の値であるH1/Dが0.09以上0.12以下であり、また距離H2と内管径Dとの比の値であるH2/Dが0.09以上0.12以下であるときに最も上記溶鋼流の整流化効果及び引き寄せ効果を得られる好ましい値であることが本発明の検討により知られている。H1/D又はH2/Dが0.09未満である場合には、上記整流化効果及び引き寄せ効果が低下するという問題が生じる。また、H1/D又はH2/Dが0.12より大きい場合には、内管11における溶鋼のスループットが減少するという問題が生じる。 The distance H1 between the maximum reduced diameter point 15c, which is the maximum reduced diameter portion of the downstream reduced diameter portion 15, and the line segment 15f extending on the wall surface of the inner pipe 11, and the maximum reduced diameter portion, which is the maximum reduced diameter portion of the upstream reduced diameter portion 16. The distance H2 between the point 16c and the line segment 16f extending on the wall surface of the inner pipe 11 is the rectification of the molten steel flow flowing down and the inner pipe 11 of the molten steel flow passing through the upstream diameter reduction portion 16 and the downstream diameter reduction portion 15. It is known to have a significant effect on the pulling effect on the wall surface. H1 / D, which is the value of the ratio of the distance H1 to the inner pipe diameter D of the inner pipe 11, is 0.09 or more and 0.12 or less, and H2 /, which is the value of the ratio of the distance H2 to the inner pipe diameter D. It is known from the study of the present invention that when D is 0.09 or more and 0.12 or less, it is the most preferable value for obtaining the rectifying effect and the attracting effect of the molten steel flow. When H1 / D or H2 / D is less than 0.09, there arises a problem that the rectifying effect and the attracting effect are lowered. Further, when H1 / D or H2 / D is larger than 0.12, there arises a problem that the throughput of molten steel in the inner pipe 11 decreases.

吐出孔14の最上辺14cと、最下段の縮径部である下流縮径部15の下端点15bとの距離Fは、50mm以上200mm以下の範囲内であることが好適であり、より好ましくは75mm以上150mm以下の範囲内であることが望ましい。 The distance F between the uppermost side 14c of the discharge hole 14 and the lower end point 15b of the downstream reduced diameter portion 15 which is the lowermost reduced diameter portion is preferably in the range of 50 mm or more and 200 mm or less, more preferably. It is desirable that it is within the range of 75 mm or more and 150 mm or less.

距離Fが上記好適な範囲よりも大きい場合には、内管11の壁面近傍における溶鋼流の速度が吐出孔14に到達するまでの間に低下しすぎている。そのため、内管11の壁面近傍の流速が大きい状態で吐出孔14へ溶鋼が流入することで、吐出流の剥離領域の発達を抑制するという下流縮径部15の効果が損なわれるという問題が生じる。また、距離Fが上記好適な範囲よりも小さい場合には、下流縮径部15の直下に形成される溶鋼の剥離領域が吐出孔14から吐出される吐出流にも影響を及ぼすため、吐出流が不安定化するという問題が生じる。 When the distance F is larger than the above-mentioned preferable range, the velocity of the molten steel flow in the vicinity of the wall surface of the inner pipe 11 is too low until it reaches the discharge hole 14. Therefore, when the molten steel flows into the discharge hole 14 in a state where the flow velocity near the wall surface of the inner pipe 11 is large, there arises a problem that the effect of the downstream diameter-reduced portion 15 of suppressing the development of the peeled region of the discharge flow is impaired. .. Further, when the distance F is smaller than the above-mentioned preferable range, the peeling region of the molten steel formed immediately below the downstream diameter-reduced portion 15 also affects the discharge flow discharged from the discharge hole 14, so that the discharge flow Causes the problem of instability.

下流縮径部15の最縮径点15cと上流縮径部16の最縮径点16cとの距離Gは、50mm以上150mm以下であることが好適である。距離Gが50mm未満である場合又は150mmを超える場合には、下流縮径部15及び上流縮径部16の上記整流化効果及び引き寄せ効果が低下するという問題が生じる。 The distance G between the maximum reduction point 15c of the downstream reduction portion 15 and the maximum reduction point 16c of the upstream reduction portion 16 is preferably 50 mm or more and 150 mm or less. When the distance G is less than 50 mm or more than 150 mm, there arises a problem that the rectifying effect and the pulling effect of the downstream reduced diameter portion 15 and the upstream reduced diameter portion 16 are lowered.

次に、従来の連続鋳造用浸漬ノズルにおける吐出流と、この発明の実施の形態1に係る連続鋳造用浸漬ノズル1の吐出流との例を挙げて説明する。
図5に、従来の内管径及び内管形状を有する浸漬ノズルの、モールド内の一方の吐出孔周辺の吐出流について、数値流体力学(CFD)により計算した結果をベクトル図として示す。ここで、従来の内管径及び内管形状とは、特許文献3に記載されているような段差状の縮径部を有する内管径及び内管形状である。また、図5及び後述する図6においては、本願の実施の形態1に係る浸漬ノズルと同等又は同様な要素は図1〜図4と同一符号により示す。
Next, an example of a discharge flow in the conventional immersion nozzle for continuous casting and a discharge flow in the immersion nozzle 1 for continuous casting according to the first embodiment of the present invention will be described.
FIG. 5 shows as a vector diagram the results of calculation by computational fluid dynamics (CFD) for the discharge flow around one discharge hole in the mold of a conventional immersion nozzle having an inner pipe diameter and an inner pipe shape. Here, the conventional inner pipe diameter and inner pipe shape are an inner pipe diameter and an inner pipe shape having a stepped reduced diameter portion as described in Patent Document 3. Further, in FIG. 5 and FIG. 6 described later, elements equivalent to or similar to the immersion nozzle according to the first embodiment of the present application are indicated by the same reference numerals as those in FIGS. 1 to 4.

このときのCFD計算条件は以下の通りである。
・モールドサイズ:240mm×1400mm
・鋳造速度:2.6m/min(スループット:6.3t/min)
・浸漬深さ:吐出孔上端から235mm、偏向はなし
The CFD calculation conditions at this time are as follows.
-Mold size: 240 mm x 1400 mm
-Casting speed: 2.6 m / min (throughput: 6.3 t / min)
・ Immersion depth: 235 mm from the top of the discharge hole, no deflection

この従来の内管形状において吐出孔下部14bは、断面形状の下側が径方向外側へ拡張するように形成されている。なお、図5及び後述するベクトル図の図7においては、溶鋼の流速は各図中の矢印により示されるベクトルの長さによって表されている。 In this conventional inner tube shape, the discharge hole lower portion 14b is formed so that the lower side of the cross-sectional shape extends outward in the radial direction. In FIG. 5 and FIG. 7 of the vector diagram described later, the flow velocity of the molten steel is represented by the length of the vector indicated by the arrow in each diagram.

図5に示すように、従来の浸漬ノズルの内管径、内管形状及び吐出孔の形状によって、吐出流のうち吐出孔14の下側の吐出流は、下降する下降流速が高速の吐出流30となる。 As shown in FIG. 5, depending on the inner pipe diameter, the inner pipe shape, and the shape of the discharge hole of the conventional immersion nozzle, the discharge flow below the discharge hole 14 among the discharge flows has a high downward flow velocity. It becomes 30.

図6は、従来の内管径及び内管形状を有する浸漬ノズルの、一方の吐出孔14付近におけるモールド内の溶鋼の流速分布を示す図である。下降流速が高速の吐出流30が発生することにより、モールドパウダースラグの吸い込みの発生につながる吸い込み流30aが吐出孔14の上方に発生する可能性が高くなる。なお、図6及び後述する流速分布を示す図8においては、溶鋼の流速が速い箇所を明るい色により表している。 FIG. 6 is a diagram showing a flow velocity distribution of molten steel in a mold in the vicinity of one discharge hole 14 of a dipping nozzle having a conventional inner pipe diameter and inner pipe shape. Since the discharge flow 30 having a high descending flow velocity is generated, there is a high possibility that the suction flow 30a, which leads to the generation of suction of the mold powder slag, is generated above the discharge hole 14. In FIG. 6 and FIG. 8 showing the flow velocity distribution described later, the portion where the flow velocity of the molten steel is high is represented by a bright color.

図7に、この発明の実施の形態1に係る連続鋳造用浸漬ノズル1の、モールド内における一方の吐出孔14からの吐出流31を示すベクトル図を示す。下流縮径部15及び上流縮径部16(図2参照)が内管11に形成されていることにより、従来の浸漬ノズルの吐出流30(図5参照)よりも、この実施の形態1の吐出流31の下降流速は低速となる。 FIG. 7 shows a vector diagram showing a discharge flow 31 from one discharge hole 14 in the mold of the continuous casting immersion nozzle 1 according to the first embodiment of the present invention. Since the downstream reduced diameter portion 15 and the upstream reduced diameter portion 16 (see FIG. 2) are formed in the inner pipe 11, the discharge flow 30 (see FIG. 5) of the conventional immersion nozzle is more than that of the first embodiment. The descending flow velocity of the discharge flow 31 becomes low.

図8は、この発明の実施の形態1に係る連続鋳造用浸漬ノズル1の、一方の吐出孔14付近におけるモールド内の流速分布を示す図である。従来の浸漬ノズルよりも吐出流31の下降流速が低速であるから、従来の浸漬ノズルと比較してこの発明に係る連続鋳造用浸漬ノズル1は、モールドパウダースラグの吸い込みの発生につながる吸い込み流が吐出孔14の上方に発生する可能性が低減される。 FIG. 8 is a diagram showing a flow velocity distribution in the mold in the vicinity of one discharge hole 14 of the continuous casting immersion nozzle 1 according to the first embodiment of the present invention. Since the descending flow velocity of the discharge flow 31 is slower than that of the conventional immersion nozzle, the continuous casting immersion nozzle 1 according to the present invention has a suction flow that leads to the generation of suction of the mold powder slag as compared with the conventional immersion nozzle. The possibility of occurrence above the discharge hole 14 is reduced.

次に、表1に示すように、異なる内管径、内管形状及び吐出孔の形状を有する複数の浸漬ノズルについて、吐出流の吸い込み流の発生頻度及び湯面の安定性を評価した比較例及び実施例を説明する。なお、本願の実施の形態1に係る浸漬ノズルと同等又は同様な要素は図1〜図4と同一符号により示す。比較例1〜及び実施例1〜の浸漬ノズルはノズル形状の特徴である、縮径部(上流縮径部16及び下流縮径部15)の数、上端点15aと最縮径点15cとの距離L1と、下端点15bと最縮径点15cとの距離L3との比の値であるL1/L3、線分15fと最縮径点15cとの距離H1と、内管径Dとの比の値であるH1/D、下端点15bと吐出孔14の最上辺14cとの距離F及び下流縮径部15の最縮径点15cと上流縮径部16の最縮径点16cとの距離Gをパラメータとして形成されている。 Next, as shown in Table 1, a comparative example in which the frequency of suction flow of the discharge flow and the stability of the molten metal surface were evaluated for a plurality of immersion nozzles having different inner pipe diameters, inner pipe shapes, and discharge hole shapes. And an embodiment will be described. Elements equivalent to or similar to the immersion nozzle according to the first embodiment of the present application are indicated by the same reference numerals as those in FIGS. 1 to 4. The immersion nozzles of Comparative Examples 1 to 9 and Examples 1 to 8 are characterized by the nozzle shape, the number of diameter-reduced portions (upstream-reduced portion 16 and downstream-reduced portion 15), the upper end point 15a and the maximum diameter-reduced point 15c. L1 which is the value of the ratio of the distance L1 to and the distance L3 between the lower end point 15b and the maximum diameter reduction point 15c, the distance H1 between the line segment 15f and the maximum reduction diameter point 15c, and the inner diameter D. H1 / D, which is the value of the ratio of The distance G is formed as a parameter.

Figure 0006963192
Figure 0006963192

比較例1〜及び実施例1〜の各例について、左側吐出孔に及び右側吐出孔における吸い込み流の発生頻度と、湯面の安定性とを評価点として各評価点の合計値を総合評価としている。また、このときのモールドサイズは220×1600mmであり、スループットは6t/分である。さらに、上流縮径部16及び下流縮径部15とは図2に示すように実施の形態1と同じく水平面17に対して鏡像対称に形成されている。 For each of Comparative Examples 1 to 9 and Examples 1 to 8 , the total value of each evaluation point is totaled with the frequency of suction flow in the left discharge hole and the right discharge hole and the stability of the molten metal as evaluation points. It is evaluated. The mold size at this time is 220 × 1600 mm, and the throughput is 6 t / min. Further, as shown in FIG. 2, the upstream reduced diameter portion 16 and the downstream reduced diameter portion 15 are formed symmetrically with respect to the horizontal plane 17 as in the first embodiment.

このときの各浸漬ノズルに対する吸い込み流の発生頻度の評価方法は、鋳造中に5秒ごとに吐出流の平均流速を12回測定し、各回の測定毎に平均流速の値に基づいて左右の吐出孔14に吸い込み流が発生しているか否かを判定し、12回中の吸い込み流の発生回数を以下の評価点として評価する。
・吸い込み流が発生した回数が0回・・・評価点0
・吸い込み流が発生した回数が1回以上2回以下・・・評価点1
・吸い込み流が発生した回数が3回以上6回以下・・・評価点3
・吸い込み流が発生した回数が7回以上12回以下・・・評価点5
The method of evaluating the frequency of suction flow generation for each immersion nozzle at this time is to measure the average flow velocity of the discharge flow 12 times every 5 seconds during casting, and for each measurement, the left and right discharges are based on the value of the average flow velocity. It is determined whether or not a suction flow is generated in the hole 14, and the number of times the suction flow is generated in 12 times is evaluated as the following evaluation points.
・ The number of times the suction flow occurred is 0 ... Evaluation point 0
・ The number of times suction flow has occurred is 1 or more and 2 or less ... Evaluation point 1
・ The number of times suction flow has occurred is 3 or more and 6 or less ... Evaluation point 3
・ The number of times the suction flow occurred was 7 or more and 12 or less ... Evaluation point 5

また、このときの各浸漬ノズルに対する湯面の安定性の評価方法は、湯面の安定状態を以下の評価点として評価する。
・湯面が安定している場合・・・評価点0
・湯面が不安定な場合・・・評価点5
Further, in the method of evaluating the stability of the molten metal surface with respect to each immersion nozzle at this time, the stable state of the molten metal surface is evaluated as the following evaluation points.
・ When the surface of the water is stable ... Evaluation point 0
・ When the surface of the water is unstable ... Evaluation score 5

また、このときの各浸漬ノズルに対する総合評価は、評価点の合計値により以下のように決められる。
・評価点の合計値が1点以下・・・◎
・評価点の合計値が2点以上5点以下・・・△
・評価点の合計値が6点以上・・・×
すなわち、評価点の合計値がより低い浸漬ノズルが、鋳造時における吐出流の吸い込み流の発生が少なく、湯面が安定しており、鋳造に適した良好な浸漬ノズル形状を有すると評価される。
Further, the comprehensive evaluation for each immersion nozzle at this time is determined as follows based on the total value of the evaluation points.
・ The total value of evaluation points is 1 point or less ... ◎
・ The total value of evaluation points is 2 points or more and 5 points or less ... △
・ The total value of evaluation points is 6 points or more ... ×
That is, it is evaluated that the immersion nozzle having a lower total evaluation point has less suction flow of the discharge flow during casting, the molten metal surface is stable, and has a good immersion nozzle shape suitable for casting. ..

比較例1〜及び実施例1〜の各例のうち、実施例1〜3、実施例4,5、実施例6〜は、総合評価が◎であって鋳造に良好な浸漬ノズル形状を有すると評価される。 Of the examples of Comparative Examples 1 to 9 and Examples 1 to 8 , Examples 1 to 3, Examples 4 and 5, and Examples 6 to 8 have a comprehensive evaluation of ⊚ and a good immersion nozzle shape for casting. Is evaluated as having.

このように、ノズル中心軸12に沿って延在する内管11を有する円筒状のノズル本体10を備え、ノズル本体10には内管11に連通する吐出孔14が形成され、吐出孔14のうち少なくとも2つはノズル本体10の側壁部13に形成され、内管11の上端はノズル本体10の上端で開口してなる連続鋳造用浸漬ノズルであって、内管11は、相似な形状を有する2つの下流縮径部15及び上流縮径部16を備え、ノズル本体10の側壁部13に形成された吐出孔14のうち2つの吐出孔14の開口中心20を通る吐出軸21及びノズル中心軸12に平行な面に沿って、ノズル本体10を切断した場合のノズル本体10の断面形状のうち、縮径部のうち最も下側に位置する下流縮径部15の断面形状は、該下流縮径部15の鉛直方向における上端点15aと、該下流縮径部15の鉛直方向における下端点15bと、該下流縮径部15の内管11の径方向に対して最も突出する最縮径点15cとを頂点とする三角形15eに外接し、且つ上端点15aから最縮径点15cまでの距離L1は下端点15bから最縮径点15cまでの距離L3よりも大きい形状を有し、下流縮径部15の上側に隣り合う上流縮径部16の断面形状と下流縮径部15の断面形状とは、上流縮径部16と下流縮径部15との中間においてノズル中心軸12に直交する水平面17に対して鏡像対称であるため、吐出流の吸い込み現象の発生を抑制し、モールドパウダースラグの吸い込みによる操業の支障及び鋳片品質欠陥の発生を抑制することができる。 As described above, the cylindrical nozzle body 10 having the inner tube 11 extending along the central axis 12 of the nozzle is provided, and the nozzle body 10 is formed with a discharge hole 14 communicating with the inner tube 11, and the discharge hole 14 is formed. At least two of them are formed in the side wall portion 13 of the nozzle body 10, and the upper end of the inner tube 11 is an immersion nozzle for continuous casting which is opened at the upper end of the nozzle body 10, and the inner tube 11 has a similar shape. The discharge shaft 21 and the nozzle center are provided with the two downstream reduced diameter portions 15 and the upstream reduced diameter portion 16 and pass through the opening center 20 of the two discharge holes 14 among the discharge holes 14 formed in the side wall portion 13 of the nozzle body 10. Of the cross-sectional shapes of the nozzle body 10 when the nozzle body 10 is cut along a plane parallel to the shaft 12, the cross-sectional shape of the downstream reduced diameter portion 15 located at the lowermost side of the reduced diameter portion is the downstream. The upper end point 15a of the reduced diameter portion 15 in the vertical direction, the lower end point 15b of the downstream reduced diameter portion 15 in the vertical direction, and the most protruding maximum reduced diameter of the downstream reduced diameter portion 15 with respect to the radial direction of the inner pipe 11. It is circumscribed to a triangle 15e having a point 15c as an apex, and the distance L1 from the upper end point 15a to the maximum reduction point 15c has a shape larger than the distance L3 from the lower end point 15b to the maximum reduction point 15c, and is downstream. The cross-sectional shape of the upstream reduced diameter portion 16 adjacent to the upper side of the reduced diameter portion 15 and the cross-sectional shape of the downstream reduced diameter portion 15 are orthogonal to the nozzle central axis 12 between the upstream reduced diameter portion 16 and the downstream reduced diameter portion 15. Since it is mirror image symmetric with respect to the horizontal plane 17 to be formed, it is possible to suppress the occurrence of the suction phenomenon of the discharge flow, and it is possible to suppress the hindrance of operation and the occurrence of slab quality defects due to the suction of the mold powder slag.

また、ノズル本体10の断面形状は、2つの吐出孔14の開口中心20を通る吐出軸21及びノズル中心軸12を含む平面に沿ってノズル本体10を切断した場合の断面形状であって、下流縮径部15の断面形状の上端点15a及び下端点15bを通る線分15fから最縮径点15cまでの距離Hと、縮径部以外の位置における内管11の直径である内管径Dとの比の値が、0.09以上0.12未満であるため、内管11における溶鋼のスループットを確保しつつ下流縮径部15を通過した後の内管径Dの拡大による溶鋼流の内管11の壁面への引き寄せ効果を最大限に発揮させることができる。 The cross-sectional shape of the nozzle body 10 is a cross-sectional shape when the nozzle body 10 is cut along a plane including the discharge shaft 21 passing through the opening centers 20 of the two discharge holes 14 and the nozzle center shaft 12, and is downstream. The distance H from the line segment 15f passing through the upper end point 15a and the lower end point 15b of the cross-sectional shape of the reduced diameter portion 15 to the maximum reduced diameter point 15c, and the inner diameter D which is the diameter of the inner pipe 11 at a position other than the reduced diameter portion. Since the value of the ratio to and is 0.09 or more and less than 0.12, the molten steel flow due to the expansion of the inner diameter D after passing through the downstream diameter reduction portion 15 while ensuring the throughput of the molten steel in the inner pipe 11. The effect of attracting the inner pipe 11 to the wall surface can be maximized.

また、下流縮径部15の下端点15bと、吐出孔14の最上辺14cとの距離Fは、50mm以上200mm以下であるため、内管11の壁面近傍の流速が大きい状態で吐出孔14へ溶鋼が流入することがなく、吐出流の剥離領域の発達を抑制するという下流縮径部15の効果が損なわれず、また、下流縮径部15の直下に形成される溶鋼の剥離領域が吐出孔14から吐出される吐出流に影響を及ぼさないため、吐出流を安定にすることができる。 Further, since the distance F between the lower end point 15b of the downstream diameter reduction portion 15 and the uppermost side 14c of the discharge hole 14 is 50 mm or more and 200 mm or less, the flow velocity near the wall surface of the inner pipe 11 is large and the discharge hole 14 is reached. The effect of the downstream reduced diameter portion 15 that the molten steel does not flow in and suppresses the development of the peeled region of the discharge flow is not impaired, and the peeled region of the molten steel formed directly below the downstream reduced diameter portion 15 is the discharge hole. Since it does not affect the discharge flow discharged from 14, the discharge flow can be stabilized.

また、下流縮径部15の最縮径点15cと、該下流縮径部15に隣り合う上流縮径部16の最縮径点16cとの距離Gは、50mm以上150mm以下であるため、下流縮径部15及び上流縮径部16の上記整流化効果及び引き寄せ効果を向上させることができる。 Further, since the distance G between the maximum reduction point 15c of the downstream reduction portion 15 and the maximum reduction point 16c of the upstream reduction portion 16 adjacent to the downstream reduction portion 15 is 50 mm or more and 150 mm or less, it is downstream. The rectifying effect and the pulling effect of the reduced diameter portion 15 and the upstream reduced diameter portion 16 can be improved.

実施の形態2.
次に、実施の形態2について説明する。なお、実施の形態2において、図1〜図8の参照符号と同一の符号は、実施の形態1と同一又は同様な構成要素であるので、その詳細な説明は省略する。
実施の形態2は、実施の形態1に対しノズル下端10bにさらに吐出孔を設けたものである。
Embodiment 2.
Next, the second embodiment will be described. In the second embodiment, the same reference numerals as those in FIGS. 1 to 8 are the same or similar components as those in the first embodiment, and thus detailed description thereof will be omitted.
In the second embodiment, a discharge hole is further provided at the lower end 10b of the nozzle as compared with the first embodiment.

図9に示すように、ノズル本体10cのノズル下端10bに、内管11に接続され鉛直方向に開口する下部吐出孔41が形成されている。これにより、ノズル本体10cの側壁部13に形成された吐出孔14に加えて下部吐出孔41からも、内管11を流れる溶鋼がモールド内に注入される。その他の形態は実施の形態1と同じである。 As shown in FIG. 9, a lower discharge hole 41 connected to the inner pipe 11 and opening in the vertical direction is formed at the lower end 10b of the nozzle of the nozzle body 10c. As a result, molten steel flowing through the inner pipe 11 is injected into the mold from the lower discharge hole 41 in addition to the discharge hole 14 formed in the side wall portion 13 of the nozzle body 10c. Other embodiments are the same as those in the first embodiment.

したがって、実施の形態2においても、実施の形態1と同じく吐出流の吸い込み現象の発生を抑制し、モールドパウダースラグの吸い込みによる操業の支障及び鋳片品質欠陥の発生を抑制することができる。 Therefore, in the second embodiment as well, the occurrence of the suction flow suction phenomenon can be suppressed, and the operation hindrance and the occurrence of the slab quality defect due to the suction of the mold powder slag can be suppressed as in the first embodiment.

なお、実施の形態1及び2においてノズル本体10の内管11は下流縮径部15及び上流縮径部16の2個の縮径部を有していたが、3つ以上の縮径部を有してもよい。 In the first and second embodiments, the inner tube 11 of the nozzle body 10 has two reduced diameter portions, a downstream reduced diameter portion 15 and an upstream reduced diameter portion 16, but three or more reduced diameter portions are provided. You may have.

また、実施の形態1及び2において、連続鋳造用浸漬ノズル1は鋼の連続鋳造用浸漬ノズルであったが、例えば銅等の鋼以外の金属の連続鋳造用浸漬ノズルであってもよい。 Further, in the first and second embodiments, the continuous casting dipping nozzle 1 is a continuous casting dipping nozzle for steel, but it may be a continuous casting dipping nozzle for a metal other than steel, for example, copper.

また、実施の形態1及び2においては各吐出孔14の吐出孔上部14aの断面形状は、下側が径方向外側に拡大するように直線を組み合わせた二段テーパとして形成されていたが、一段のテーパとして構成されていてもよい。さらに、各吐出孔14の吐出孔下部14bの断面形状は、下側が径方向外側へ拡大するように形成されていたが、下側が径方向内側へ縮小するように形成されていてもよい。 Further, in the first and second embodiments, the cross-sectional shape of the discharge hole upper portion 14a of each discharge hole 14 is formed as a two-step taper in which straight lines are combined so that the lower side expands radially outward. It may be configured as a taper. Further, the cross-sectional shape of the lower portion 14b of the discharge hole of each discharge hole 14 is formed so that the lower side expands radially outward, but the lower side may be formed so as to contract radially inward.

10 ノズル本体、11 内管、12 ノズル中心軸、14 吐出孔、14c 最上辺、15 下流縮径部(最下縮径部)、15a 上端点、15b 下端点、15c 最縮径点、15e 三角形、15f 線分、16 上流縮径部(隣接縮径部)、16a 下端点、16b 上端点、16c 最縮径点、16e 三角形、16f 線分、17 水平面、20 開口中心、21 吐出軸、D 内管径、F 距離、G 距離、H1,H2 距離、L1 距離、L2 距離、L3 距離、L4 距離。 10 Nozzle body, 11 Inner pipe, 12 Nozzle center axis, 14 Discharge hole, 14c Top side, 15 Downstream reduced diameter part (bottom reduced diameter part), 15a Upper end point, 15b Lower end point, 15c Maximum diameter point, 15e triangle , 15f line segment, 16 upstream reduced diameter part (adjacent reduced diameter part), 16a lower end point, 16b upper end point, 16c most reduced diameter point, 16e triangle, 16f line segment, 17 horizontal plane, 20 opening center, 21 discharge shaft, D Inner pipe diameter, F distance, G distance, H1, H2 distance, L1 distance, L2 distance, L3 distance, L4 distance.

Claims (1)

ノズル中心軸に沿って延在する内管を有する円筒状のノズル本体を備え、前記ノズル本体には前記内管に連通する吐出孔が形成され、前記吐出孔のうち少なくとも2つは前記ノズル本体の側壁部に形成され、前記内管の上端は前記ノズル本体の上端で開口してなる連続鋳造用浸漬ノズルであって、
前記内管は、相似な形状を有する少なくとも2つの縮径部を備え、
前記ノズル本体の側壁部に形成された吐出孔のうち2つの前記吐出孔の開口中心を通る吐出軸及び前記ノズル中心軸を含む平面に沿って、前記ノズル本体を切断した場合の前記ノズル本体の断面形状のうち、
前記縮径部のうち最も下側に位置する最下縮径部の前記断面形状は、該最下縮径部の前記断面形状の上端点と、該最下縮径部の前記断面形状の下端点と、該最下縮径部の前記断面形状の前記内管の径方向に対して最も突出する最縮径点とを頂点とする三角形に外接し、且つ前記上端点から前記最縮径点までの距離は前記下端点から前記最縮径点までの距離よりも大きい形状を有し、
前記最下縮径部の上側に隣り合う隣接縮径部の前記断面形状と、前記最下縮径部の前記断面形状とは、前記隣接縮径部と前記最下縮径部との中間において前記ノズル中心軸に直交する面に対して鏡像対称であり、
前記最下縮径部の前記断面形状の前記上端点及び前記下端点を通る直線から前記最縮径点までの距離と、前記縮径部以外の位置における前記内管の直径である内管径との比の値が、0.09以上0.12未満であり、
前記最下縮径部の前記断面形状の前記下端点と、前記吐出孔の前記断面形状の上端との距離は、50mm以上200mm以下であり、
前記最下縮径部の前記断面形状の前記最縮径点と、前記隣接縮径部の前記断面形状の前記最縮径点との距離は、50mm以上150mm以下である連続鋳造用浸漬ノズル。
A cylindrical nozzle body having an inner tube extending along the central axis of the nozzle is provided, and the nozzle body is formed with discharge holes communicating with the inner tube, and at least two of the discharge holes are the nozzle body. A dipping nozzle for continuous casting, which is formed on the side wall portion of the inner pipe and the upper end of the inner pipe is opened at the upper end of the nozzle body.
The inner tube comprises at least two reduced diameter portions having similar shapes.
Of the discharge holes formed on the side wall of the nozzle body, the nozzle body when the nozzle body is cut along a plane including the discharge shaft passing through the opening center of the discharge holes and the nozzle center axis. Of the cross-sectional shape
The cross-sectional shape of the lowest reduced diameter portion located on the lowermost side of the reduced diameter portion is the upper end point of the cross-sectional shape of the lowest reduced diameter portion and the lower end of the cross-sectional shape of the lowest reduced diameter portion. It is circumscribed in a triangle having a point and the most protruding diameter point of the bottom diameter portion of the cross-sectional shape in the radial direction of the inner pipe as the apex, and the most contraction point from the upper end point. The distance to is larger than the distance from the lower end point to the most contracted diameter point.
The cross-sectional shape of the adjacent reduced diameter portion adjacent to the upper side of the lowest reduced diameter portion and the cross-sectional shape of the lowest reduced diameter portion are in the middle between the adjacent reduced diameter portion and the lowest reduced diameter portion. Ri mirror symmetry der respect to a plane perpendicular to the nozzle central axis,
The inner pipe diameter, which is the distance from the straight line passing through the upper end point and the lower end point of the cross-sectional shape of the lowermost reduced diameter portion to the outermost reduced diameter point, and the diameter of the inner pipe at a position other than the reduced diameter portion. The value of the ratio with is 0.09 or more and less than 0.12.
The distance between the lower end point of the cross-sectional shape of the lowest diameter portion and the upper end of the cross-sectional shape of the discharge hole is 50 mm or more and 200 mm or less.
A dipping nozzle for continuous casting in which the distance between the most reduced diameter point of the cross-sectional shape of the lowest reduced diameter portion and the most reduced diameter point of the cross-sectional shape of the adjacent reduced diameter portion is 50 mm or more and 150 mm or less.
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