WO2020153195A1 - Immersion nozzle - Google Patents
Immersion nozzle Download PDFInfo
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- WO2020153195A1 WO2020153195A1 PCT/JP2020/001078 JP2020001078W WO2020153195A1 WO 2020153195 A1 WO2020153195 A1 WO 2020153195A1 JP 2020001078 W JP2020001078 W JP 2020001078W WO 2020153195 A1 WO2020153195 A1 WO 2020153195A1
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- WIPO (PCT)
- Prior art keywords
- immersion nozzle
- inner hole
- protrusions
- protrusion
- molten steel
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/04—Continuous casting of metals, i.e. casting in indefinite lengths into open-ended moulds
- B22D11/0408—Moulds for casting thin slabs
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D41/00—Casting melt-holding vessels, e.g. ladles, tundishes, cups or the like
- B22D41/50—Pouring-nozzles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/10—Supplying or treating molten metal
Definitions
- the present invention relates to a dipping nozzle for continuous casting in which molten steel is poured from a tundish into a mold, and particularly in a lateral direction (vertical direction) near a discharge hole of a dipping nozzle such as used for thin slabs and medium-thickness slabs. Perpendicular to the direction)
- the section relates to a flat immersion nozzle.
- a continuous casting immersion nozzle (hereinafter, simply referred to as “immersion nozzle”) installed at the bottom of a tundish is used. Molten steel is poured into the mold.
- an immersion nozzle is composed of a pipe body having a bottom portion, the upper end portion of which is a molten steel introduction port, and a molten steel flow passage (inner hole) extending downward from the molten steel introduction port is formed inside thereof.
- a pair of discharge holes communicating with the molten steel flow path (inner hole) are formed facing each other.
- the immersion nozzle is used with its lower part immersed in the molten steel in the mold. As a result, the molten steel poured is prevented from scattering, and the contact between the molten steel and the atmosphere is blocked to prevent oxidation.
- the immersion nozzle the molten steel in the mold is rectified so that impurities such as slag and non-metallic inclusions floating on the molten metal surface are prevented from being caught in the molten steel.
- Patent Document 1 discloses a flat immersion nozzle in which a discharge hole is provided on a short side wall
- Patent Document 2 discloses a flat immersion nozzle in which a discharge hole is further provided on a lower end surface.
- the width of the inner hole is enlarged between the molten steel introduction port and the discharge hole to the mold.
- the molten steel flow in the immersion nozzle is likely to be disturbed, and the discharge flow to the mold is also disturbed.
- This turbulence of the molten steel flow is also a cause of increased fluctuations of the molten metal surface (molten steel surface) in the mold, entrainment of powder in the slab, temperature non-uniformity, and other factors causing poor slab quality and increased operational risk. Become. Therefore, it is necessary to stabilize the molten steel flow in the immersion nozzle and discharged.
- Patent Document 3 discloses an immersion nozzle in which at least two bending facets are formed from a point (center) on the plane below the inner hole toward the lower edge of the discharge hole. Has been done. Further, Patent Document 3 discloses an immersion nozzle equipped with a flow divider that divides the molten steel flow into two streams. The flat immersion nozzle shown in Patent Document 3 has a molten steel flow in the immersion nozzle, as compared with the immersion nozzle which does not have a means for changing the flow direction and shape in the internal space as in Patent Documents 1 and 2. Will be more stable.
- the molten steel flow rate is approximately 0 based on the operating conditions, particularly the minimum cross sectional area position in the region where the transverse cross sectional shape of the inner hole near the top of the submerged nozzle is circular.
- the present inventors have found that in continuous casting performed under conditions such as 04 (t/(min. ⁇ cm 2 )) or more, the effects such as stabilization of the molten metal surface in the mold may still be insufficient.
- the problem to be solved by the present invention is to provide a flat immersion nozzle that stabilizes the molten metal surface in the mold, that is, reduces the fluctuation.
- a protruding portion is installed mainly in the center of the inner hole, and based on that, for fine adjustment adjustment of the discharge flow, shape, etc., the same or protruding to the center also on the side thereof. Install a protrusion with a small thickness.
- symmetrical projecting portions are installed laterally, and the space between the projecting portions is based on the space without the projecting portion or the lateral projecting portion, and the projecting length is longer than that of the lateral projecting portion. Install a small protrusion.
- the molten steel flow in the inner hole is set to have a larger flow amount to the side (in the width direction of the flat portion of the nozzle; the same applies hereinafter) than the direction directly below the center. Lead.
- the molten steel flow rate from the discharge hole tends to increase, and the fluctuation of the molten metal level in the mold may increase under conditions such as a large molten steel flow rate per unit time or unit area.
- the molten steel flow in the inner hole is adjusted so as to increase the flow rate directly below the center, and the flow rate to the side is relatively reduced.
- the ratio of the flow rate in the direction directly below the center/the flow rate in the lateral direction is made relatively larger than in the case of the structure of the immersion nozzle of Patent Document 4.
- the ratio is adjusted in the relationship of the flow rate in the direction directly below the center/the flow rate in the lateral direction. Absent.
- the present invention for obtaining the above-mentioned flow form is the following flat nozzles 1 to 8.
- An immersion nozzle having a flat shape in which the width Wn of the inner hole is larger than the thickness Tn of the inner hole and having a pair of discharge holes in the lower part of the short side wall, On the wall surface in the width direction of the flat portion, at a position axially symmetric with respect to the longitudinal center axis of the wall surface in the width direction, a portion that inclines downward in the width direction and protrudes in the thickness direction (hereinafter referred to as “side”).
- Protrusions are arranged in pairs, The lateral protrusions are arranged on both side walls in the width direction so as to face each other, The total protrusion length Ts in the thickness direction of the lateral protrusions, where the thickness of the inner hole at the position where the lateral protrusions are arranged is 1, is 0 for each of the two lateral protrusions forming the pair.
- Immersion nozzle that is the same between 18 and 0.90. 2.
- the projection length in the thickness direction is smaller than the projection length in the thickness direction of the lateral projections, and A protrusion having a total protrusion length Tp in the thickness direction of which the thickness of the inner hole at the position where the protrusion is arranged is 1 is 0.40 or less (not including zero) (hereinafter referred to as "central protrusion"). .) is installed, The immersion nozzle as described in 1 above. 3. 3. The immersion nozzle according to 2 above, wherein the upper end surface of the central protruding portion has a horizontal shape in the width direction or a curved shape having a vertex at the center or a shape protruding upward including a bending point. 4. 4. 4.
- One or both of the side protruding portion and the central protruding portion may have the same protruding length, or may be a straight line, a curved line, or a stepped shape that is shortened toward the center of the widthwise wall surface.
- Either one or both of the side protrusions provided with the side protrusions and the central protrusions are installed at a plurality of positions in the vertical direction, according to any one of 1 to 5 above.
- the immersion nozzle according to any one of 1 to 6 above which has an upward protruding portion near the center of the bottom of the inner hole.
- the immersion nozzle has a molten steel flow rate of 0.04 (t/(min. ⁇ cm 2 )) with reference to the minimum cross-sectional area position in a region where the transverse cross-sectional shape of the inner hole near the upper end of the immersion nozzle is circular.
- the width Wn and the thickness Tn of the inner hole are the width (length in the long side direction) of the inner hole at the upper end position of the pair of discharge holes provided on the short side wall of the immersion nozzle. , Thickness (length in the short side direction).
- the flat immersion nozzle of the present invention controls the molten steel flow in a continuous state in which the molten steel flow is gradually increased or decreased without being fixedly or completely separated from the central portion to the lateral portions. Therefore, it is possible to secure an appropriate balance of the molten steel flow in the immersion nozzle.
- the molten steel flow rate is approximately 0.04 (t/(min. ⁇ cm 2 )), based on the operating conditions, especially the minimum cross-sectional area position in the area where the horizontal cross-sectional shape near the top of the immersion nozzle is circular.
- FIG. 1A is an image diagram showing an example of the immersion nozzle of the present invention (a second embodiment of the present invention) in which a pair of side protrusions is installed in addition to the side protrusions of FIG. 1, (a) passing through the center of the short side.
- Sectional view (b) is a sectional view (view AA) passing through the center of the long side.
- FIG. 1A is an image diagram showing an example of the immersion nozzle of the present invention (a second embodiment of the present invention) in which a pair of side protrusions is installed in addition to the side protrusions of FIG. 1, (a) passing through the center of the short side.
- Sectional view (b) is a sectional view (view AA) passing through the center of the long side.
- FIG. 3 is an image view showing an example of the immersion nozzle of the present invention (third embodiment of the present invention) in which a central protrusion is installed between the side protrusions of FIG. 1, (a) is a cross-sectional view passing through the center of the short side, b) is a sectional view (view AA) passing through the center of the long side.
- FIG. 3A is an image diagram showing an example of the immersion nozzle of the present invention (fourth embodiment of the present invention) in which, in addition to the lateral protrusions and the central protrusion between them in FIG. Is a cross-sectional view passing through the center of the short side, and (b) is a cross-sectional view (view AA) passing through the center of the long side.
- FIG. 3A is an image diagram showing an example of the immersion nozzle of the present invention (fourth embodiment of the present invention) in which, in addition to the lateral protrusions and the central protrusion between them in FIG. Is a cross-sectional view
- FIG. 5 is an enlarged view of the vicinity of the portion where the central protrusion is installed between the side protrusions of FIG. 3 or FIG. 4, the central portion of the central protrusion is a straight mountain chevron, and the bottom protrusion is further formed.
- FIG. 6 is a cross-sectional view of the example in which the central portion of the above has a mountain shape with a straight line in the upward direction, and passing through the center of the short side.
- FIG. 6 is a top view of the inner hole of the immersion nozzle shown in FIG. 5, and is an image diagram showing a relationship between a side protrusion and a central protrusion.
- FIG. 6 is an image diagram showing a cross section that passes through the center of the short side of the immersion nozzle in an example where the upper end of the central protruding portion of FIG. 5 is a curved surface.
- FIG. 6 is an image diagram showing a cross section that passes through the center of the short side of the immersion nozzle in an example in which the upper end of the central protruding portion of FIG. 5 is a flat surface. It is an image figure which shows the cross section which passes along the long side side center of an immersion nozzle in the example of the shape which the upper surface of a side protrusion part or a center protrusion part inclines toward the inner hole center direction.
- FIG. 6 is a top view image diagram showing an example in which the protruding lengths of the upper surfaces of the side protruding portion and the central protruding portion of FIG. 5 are constant (the inner hole side end portion is parallel to the width direction wall surface).
- FIG. 6 is a top view image diagram showing an example in which the projection length of the upper surface of the central protruding portion of FIG. 5 is linearly reduced in the central direction.
- FIG. 6 is a top view image diagram showing an example in which the protruding length of the upper surface of the central protruding portion of FIG. 5 is curvilinearly reduced in the central direction.
- FIG. 6 is a top view image diagram showing an example in which the protrusion lengths of the upper faces of the side protrusions and the central protrusion of FIG. 5 are linear and integrally reduced continuously.
- FIG. 6 is an image diagram showing a cross section passing through the center of the short side in an example in which the upper surface of the bottom protruding portion of the immersion nozzle in FIG. 5 is a plane. It is an image figure which shows the cross section which passes along the center of a short side in the example which the upper surface of the bottom protrusion part of the immersion nozzle of FIG. 5 is a curved surface. It is an image figure which shows the cross section which passes along the center of a short side in the example which the upper surface of the bottom protrusion part of the immersion nozzle of FIG.
- FIG. 5 equips with a convex part in the center, and expands diameter toward the bottom. It is an image figure which shows the cross section which passes along the center of a short side in the example which equips the bottom protrusion part of the immersion nozzle of FIG. 5 with the hole for molten steel discharge.
- FIG. 3 is an image view showing a change in the mold and the molten metal surface (molten steel surface) in the mold, (a) is a top view image diagram near the mold molten metal surface (inner surface), and (b) is a short side near the molten metal surface (inner surface) It is an image figure of the cross-sectional view (longitudinal half) which passes along the center. It is a figure which shows the fluctuation
- the molten steel flow to the widthwise end portion side can be formed to some extent by installing the flow dividing means as in the above-mentioned Patent Document 3.
- a part of the inner hole that is, a molten steel flow separated into a single narrow area is generated, and a part having a different flow direction and flow velocity at each position of the inner hole is generated. It is easy to occur.
- the molten steel flow may be biased in one direction, and the discharge flow from the dipping nozzle into the mold and the molten surface may be significantly disturbed.
- the present invention for example, as shown in the first embodiment of FIG. 1, first, at the side portion of the wall surface in the width direction (long side) of the flat portion of the immersion nozzle 10, with respect to the center axis of the width direction wall surface.
- a pair of axially symmetric side protrusions 1 (see FIG. 1A and the like. Hereinafter, also simply referred to as “axisymmetric side protrusions”) are installed.
- the upper surfaces of the pair of side protrusions 1 are inclined from the center side of the side protrusions 1 in the width direction of the flat portion and downward, that is, in the direction of the discharge hole 4. With such an inclination, the flow velocity and flow form of the molten steel from the inner hole 3 or the discharge hole 4 can be gently changed while optimizing the generation of vortex and the like, and can be optimized.
- the pair of axisymmetric side protrusions are installed on the other widthwise wall surface sandwiching the inner hole so as to face each other in a plane-symmetric relationship with respect to the thickness direction of the flat portion (FIG. 1(b)).
- the side protrusions having a plane symmetry relationship are also simply referred to as “plane symmetry side protrusions.”
- the total length Ts in the thickness direction of the lateral protrusions 1 with the thickness Tn of the inner hole at the specified position being 1 is set to 0.18 or more and 0.90 or less, that is, the lateral symmetry of plane symmetry. There is a space through which molten steel passes between the parts.
- the molten steel flow is not fixedly and completely divided in the inner hole, but the flow direction and flow velocity of the portion where the molten steel flow passes are gently controlled. As a result, the molten steel flow can be mitigated from flowing toward the discharge hole with a clear boundary.
- the installation location, length, direction, etc. of the lateral protrusion it is possible to avoid concentrating the molten steel flow near the center or on the lateral side, and at the same time, on the width direction end side, that is, the discharge hole side and the center side. It is possible to give an appropriate balance to the molten steel flow while being dispersed. Moreover, not only is it simply dispersed, but since the space is in communication even in the area where the lateral protrusions are installed, the molten steel flow is not completely divided but forms a gentle boundary, and is gently mixed and homogenized. While becoming a dispersed flow.
- the installation location, length, direction, etc. of the lateral protrusion can be adjusted as appropriate.
- the lateral protrusions of FIG. 1 denoted by reference numeral 1a in FIG. 2 and hereinafter also referred to as “lower lateral protrusions”
- they are laterally upward.
- a pair of protrusions are installed.
- the protrusions having a smaller protrusion length than the axisymmetric side protrusions. can be installed.
- the central protrusion 1p is installed between the axially symmetrical side protrusions 1 and 1 shown in FIG. 1.
- the central protrusion 1p is provided.
- a central protrusion 1p is provided between the lower side protrusions 1a, 1a.
- Patent Document 4 by providing a protrusion having a protrusion length larger than that of the axisymmetric side protrusion, the structure is provided to a side of the molten steel flow between the axisymmetric side protrusions.
- This has the opposite effect of increasing the molten steel flow, that is, the effect of increasing the ratio of the molten steel flow between the axisymmetric lateral protrusions (central portion)/the lateral molten steel flow.
- the balance between the molten steel flow to the central part and the molten steel flow to the side is such as the magnitude of molten steel flow velocity (molten steel flow rate per unit time, per unit cross-sectional area), drawing speed, mold size/shape, immersion depth, and so on. It can be optimized depending on the nozzle structure such as the discharge hole area. Specifically, there is no central protrusion between the side protrusions that are axially symmetrical, such as the widthwise or downward angle of the side protrusions, the length in the width direction, the protrusion length, or the like. Methods such as adjusting the protruding height of the central protruding portion and adjusting the shape of the upper end surface can be adopted. Specifically, as shown in FIG.
- the protrusion length Tp/2 of the central protrusion is smaller than the protrusion length Ts/2 of the lateral protrusion 1, and
- the total protrusion length Tp with the thickness Tn of the inner hole at the position where the directional protrusion 1 is arranged being 1 is set to 0.40 or less. In other words, Tp ⁇ Ts and Tp/Tn ⁇ 0.40.
- the upper end surface of the central protruding portion has a horizontal shape in the width direction as shown in FIG. 8 or a shape protruding upward including a curved surface or a bending point having the center at the apex as shown in FIGS. 5 and 7. be able to. With such a shape, the flow velocity and flow form of molten steel can be further changed and optimized.
- the upper end surface of the lateral protrusion or the central protrusion has a boundary portion with the wall surface in the width direction (long side) of the flat portion of the immersion nozzle as an apex in the thickness direction of the flat portion of the immersion nozzle. It is also possible to incline downward in the central direction, that is, in the central direction of the inner hole (space side). With such an inclination, the flow velocity and flow form of molten steel can be further changed and optimized.
- the protrusion length of the upper end surface of the side protrusion or the central protrusion can be the same as shown in FIG. 10, and as shown in FIGS. It is also possible to incline so that the length becomes shorter toward the center of the wall surface. With such an inclination, the flow velocity and flow form of molten steel can be further changed and optimized.
- the discharge holes on the short side wall are opened long in the vertical direction, so there may be a part where the discharge flow velocity decreases at the upper side, especially near the upper end.
- a backflow phenomenon that draws into the submerged nozzle is also often seen. Therefore, in the present invention, as shown in FIG. 2 and FIG. 4, for example, in addition to the above-mentioned axially symmetric and plane symmetric lower side protrusions 1a, one or a plurality of axially symmetric and plane symmetric side protrusions are provided above the lower side protrusions 1a.
- 1b upper side protrusion
- the upper side protruding portion 1b can have the same optimized structure as the lower side protruding portion 1a.
- the upper side protruding portion 1b suppresses a decrease in flow velocity particularly above the discharge hole, or suppresses turbulence of the molten steel flow such as backflow near the upper end to uniformize the flow velocity distribution at each vertical position of the discharge hole. It also has the function of adjusting the flow balance in the upper limit direction while complementing the function of Also between the upper side protrusions 1b and 1b, a central protrusion can be installed in the same manner as between the lower side protrusions 1a and 1a described above.
- the bottom part 5 inside the immersion nozzle may be a wall surface as a partition wall with a mold, instead of forming a discharge hole near the center as shown in FIG. 14, or FIG. 1 to FIG. 5, FIG. 7, FIG.
- the structure may be such that the central portion is projected upward and the bottom projection portion is included.
- a discharge hole 6 may be provided in the bottom portion 5.
- Such a protruding structure of the bottom portion is useful for changing the flow direction/form, flow velocity, etc. when converting the molten steel flow to the central portion into the discharge hole direction.
- Example A is the second embodiment of the present invention shown in FIG. 2, that is, axially symmetric and plane symmetrical two-sided protrusions 1a and 1b are installed as protrusions, and the lower side protrusions 1a and 1a are arranged between them.
- the specifications of the immersion nozzle are as follows. ⁇ Total length: 1165 mm ⁇ Melted steel inlet: ⁇ 86mm ⁇ Inner hole width (Wn) at the top of the discharge hole: 255 mm ⁇ Inner hole thickness (Tn) at the top of the discharge hole: 34 mm ⁇ Height from the lower end surface of the nozzle at the upper end position of the discharge hole: 146.5 mm ⁇ Height of central protruding portion (height from the lower end surface of the nozzle): 155 mm ⁇ Wall thickness of immersion nozzle: Approx.
- the conditions of the mold and fluid are as follows. ⁇ Width of mold: 1650mm -Thickness of mold: 65 mm (center upper end 185 mm) ⁇ Dip depth (from top of discharge hole to water surface): 83mm ⁇ Fluid supply rate: 0.065t/(min ⁇ cm 2 ) *Value converted to molten steel
- the index of drift in the mold is set to be 1.0 when there is no drift, and 0.8 is the index of drift in the mold ⁇ 1.2, and the height of fluctuation of the molten metal in the mold (mm) is ⁇ 15 mm. It was considered that the effect was obtained, and it was used as the evaluation standard.
- the drift index in the mold is measured in water model experiments by measuring the flow velocities of the left and right set molten metal surfaces (30 mm underwater from the upper end of the set water level) of the immersion nozzle in the mold, and comparing the left and right flow rates. It is the absolute value when expressed by, that is, the value of the left flow velocity/the right flow velocity (or the right flow velocity/the left flow velocity), and the level of fluctuation of the molten metal in the mold is the maximum value of Sw in FIG.
- the drift index in the mold and the fluctuation level of the molten metal surface in the mold can satisfy the criteria when the ratio of Ts to Tn (Ts/Tn) is 0.18 or more and 0.90 or less for the lateral protrusion. Further, in the case where the central protruding portion is installed, when the protruding length is smaller than the protruding length of the lateral protruding portion (Tp ⁇ Ts) and the Tp ratio (Tp/Tn) to Tn is 0.4 or less, It turns out that the criteria can be met.
- Example B In Example B, in the fourth mode of the present invention shown in FIG. 4, the upper end surfaces of the lower side protruding portion 1a and the central protruding portion 1p are inclined downward in a plane toward the center of the inner hole as shown in FIG. These are the results of water model experiments showing the degree of fluctuation in the molten metal level in the mold when the shape is changed.
- Other conditions are the same as in Example A.
- the vertical axis of FIG. 19 is a value obtained by averaging the maximum melt level fluctuation value Sw (mm) in the left and right directions of the discharge hole regardless of whether the inclination angle ⁇ is 0 degrees or 45 degrees.
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Abstract
Description
本発明は,タンディッシュから鋳型内に溶鋼を注湯する連続鋳造用の浸漬ノズルに関し、特に,薄スラブ,中厚スラブ等用として用いられるような,浸漬ノズルの吐出孔付近の横方向(鉛直方向に垂直な方向)断面が,扁平状の浸漬ノズルに関する。 The present invention relates to a dipping nozzle for continuous casting in which molten steel is poured from a tundish into a mold, and particularly in a lateral direction (vertical direction) near a discharge hole of a dipping nozzle such as used for thin slabs and medium-thickness slabs. Perpendicular to the direction) The section relates to a flat immersion nozzle.
溶鋼を連続的に冷却凝固させて所定形状の鋳片を形成する連続鋳造工程では,タンディッシュの底部に設置された連続鋳造用浸漬ノズル(以下では,単に「浸漬ノズル」ともいう。)を介して鋳型内に溶鋼が注湯される。 In a continuous casting process in which molten steel is continuously cooled and solidified to form a slab having a predetermined shape, a continuous casting immersion nozzle (hereinafter, simply referred to as “immersion nozzle”) installed at the bottom of a tundish is used. Molten steel is poured into the mold.
一般に,浸漬ノズルは,上端部が溶鋼の導入口とされ,この溶鋼導入口から下方に延びる溶鋼流路(内孔)が内部に形成された,底部を有する管体からなり,管体の下部側面には,溶鋼流路(内孔)と連通する一対の吐出孔が対向して形成されている。浸漬ノズルは,その下部を鋳型内の溶鋼中に浸漬させた状態で使用される。これにより,注湯された溶鋼の飛散を防止すると共に,溶鋼と大気との接触を遮断して酸化を防止している。また,浸漬ノズルを使用することにより鋳型内の溶鋼が整流化され,湯面を浮遊するスラグや非金属介在物などの不純物が溶鋼中へ巻き込まれないようにしている。 In general, an immersion nozzle is composed of a pipe body having a bottom portion, the upper end portion of which is a molten steel introduction port, and a molten steel flow passage (inner hole) extending downward from the molten steel introduction port is formed inside thereof. On the side surface, a pair of discharge holes communicating with the molten steel flow path (inner hole) are formed facing each other. The immersion nozzle is used with its lower part immersed in the molten steel in the mold. As a result, the molten steel poured is prevented from scattering, and the contact between the molten steel and the atmosphere is blocked to prevent oxidation. In addition, by using the immersion nozzle, the molten steel in the mold is rectified so that impurities such as slag and non-metallic inclusions floating on the molten metal surface are prevented from being caught in the molten steel.
近年,連続鋳造時に薄スラブ,中厚スラブ等の,厚さが薄い鋳片を製造することが増えている。このような連続鋳造用の薄い鋳型に対応するための浸漬ノズルは扁平状にする必要がある。例えば特許文献1には短辺側側壁に吐出孔を設置した扁平状浸漬ノズルが,特許文献2にはさらに下端面にも吐出孔を設けた扁平状浸漬ノズルが示されている。これらの扁平状の浸漬ノズルでは一般的に,溶鋼導入口から鋳型への吐出孔の間でその内孔の幅を拡大させることになる。
In recent years, there has been an increase in the production of thin slabs such as thin slabs and medium-thickness slabs during continuous casting. The dipping nozzle for accommodating such a thin mold for continuous casting needs to be flat. For example,
しかし,このような内孔の幅が拡大する形状かつ扁平形状の場合,浸漬ノズル内の溶鋼流が乱れやすくなり,その鋳型への吐出流も乱れる。この溶鋼流の乱れは鋳型内の湯面(溶鋼表面)の変動増大や,パウダーの鋳片への巻き込み,温度不均一化等,鋳片品質不良や操業の危険性増大等を惹き起こす原因ともなる。したがって浸漬ノズル内及び吐出する溶鋼流を安定化させることが必要となる。 However, in the case of such a shape that the width of the inner hole expands and the shape is flat, the molten steel flow in the immersion nozzle is likely to be disturbed, and the discharge flow to the mold is also disturbed. This turbulence of the molten steel flow is also a cause of increased fluctuations of the molten metal surface (molten steel surface) in the mold, entrainment of powder in the slab, temperature non-uniformity, and other factors causing poor slab quality and increased operational risk. Become. Therefore, it is necessary to stabilize the molten steel flow in the immersion nozzle and discharged.
これら溶鋼流を安定化させるために,例えば特許文献3には,内孔の下方の平面上の点(中心)から吐出孔の下縁に向かう少なくとも2個の曲げファセットを形成した浸漬ノズルが開示されている。さらにこの特許文献3には,溶鋼流を2本のストリームに分流する分流器を備える浸漬ノズルが開示されている。この特許文献3に示された扁平状の浸漬ノズルでは,特許文献1や特許文献2のような内部空間に流動方向・形態を変える手段を備えない浸漬ノズルに比較すると,浸漬ノズル内の溶鋼流の安定性は高くなる。
In order to stabilize these molten steel flows, for example,
しかし,このような左右方向の溶鋼流を分流するような手段の場合,依然,左右の吐出孔間での溶鋼吐出流の変動が大きくなって,それによる鋳型内湯面の変動が大きくなることがある。 However, in the case of such a means for diverting the molten steel flow in the left-right direction, the variation of the molten steel discharge flow between the left and right discharge holes is still large, and the variation of the molten metal level in the mold may be increased accordingly. is there.
前述の背景下,本発明者らは特許文献4に示す扁平状の浸漬ノズルを発明し,鋳型内湯面等を安定化させることに寄与した。
Under the background described above, the present inventors have invented the flat immersion nozzle shown in
しかし,特許文献4の扁平状の浸漬ノズルでも,操業条件,特に浸漬ノズル上端付近の内孔横方向断面形状が円である領域の,最小断面積位置を基準にして,溶鋼流量が概ね0.04(t/(min.・cm2))以上等の条件で行う連続鋳造においては,鋳型内湯面の安定化等の効果が依然不十分な場合があることを本発明者らは知見した。
However, even with the flattened submerged nozzle of
そこで本発明が解決しようとする課題は,扁平状の浸漬ノズルにおいて,鋳型内湯面等を安定化させる,すなわちその変動を小さくする浸漬ノズルを提供することにある。 Therefore, the problem to be solved by the present invention is to provide a flat immersion nozzle that stabilizes the molten metal surface in the mold, that is, reduces the fluctuation.
特許文献4の扁平状の浸漬ノズルでは,主として内孔中央に突出部を設置し,それを基本として吐出流・形態等の微調整調整のために,その側方にも前記中央と同じ又は突出厚さの小さい突出部を設置する。
これに対し本発明では側方に対称の突出部を設置し,その側方突出部の間は突出部の無い空間又は前記側方突出部を基本として,前記側方突出部より突出長さの小さい突出部を設置する。
In the flat dipping nozzle of
On the other hand, in the present invention, symmetrical projecting portions are installed laterally, and the space between the projecting portions is based on the space without the projecting portion or the lateral projecting portion, and the projecting length is longer than that of the lateral projecting portion. Install a small protrusion.
特許文献4の扁平状の浸漬ノズルの構造では,内孔での溶鋼流を,中央直下方向よりも側方(ノズル扁平部分の幅方向を指す。以下同じ。)への流量を大きくするように導く。この場合,吐出孔からの溶鋼流速が大きくなる傾向となり,単位時間当たり,単位面積当たりの溶鋼流量が大きい条件等の場合では鋳型内湯面の変動が大きくなることがある。
これに対し,本発明の浸漬ノズルの構造では,内孔での溶鋼流を,中央直下方向への流量を大きくするように調整して側方への流量を相対的に減じるように導く。言い換えると,本発明では中央直下方向への流量/側方への流量の割合を,特許文献4の浸漬ノズルの構造の場合よりも相対的に大きくする,ということである。
なお,上述は基本的に中央直下方向への流量/側方への流量の関係においてその割合を調整するのであって,必ずしも中央直下方向への流量>側方への流量の関係にするものではない。
In the structure of the flat-shaped immersion nozzle of
On the other hand, in the structure of the immersion nozzle of the present invention, the molten steel flow in the inner hole is adjusted so as to increase the flow rate directly below the center, and the flow rate to the side is relatively reduced. In other words, in the present invention, the ratio of the flow rate in the direction directly below the center/the flow rate in the lateral direction is made relatively larger than in the case of the structure of the immersion nozzle of
In the above, basically, the ratio is adjusted in the relationship of the flow rate in the direction directly below the center/the flow rate in the lateral direction. Absent.
上述の流動形態を得るための本発明は,次の1から8の扁平状の浸漬ノズルである。
1.
内孔の幅Wnが内孔の厚さTnより大きい扁平状であって,短辺側側壁の下部に一対の吐出孔を備える浸漬ノズルにおいて,
扁平部分の幅方向の壁面上に,前記幅方向の壁面の縦方向中心軸に対して軸対称の位置に,前記幅方向かつ下方向に傾斜して厚さ方向に突出した部分(以下「側方突出部」という。)が対をなして配置されており,
前記側方突出部は前記幅方向の両壁面上に対向して配置されており,
当該側方突出部が配置された位置の内孔の厚さを1とする前記側方突出部の前記厚さ方向の合計突出長さTsは,前記対をなす2つの側方突出部それぞれ0.18以上0.90以下で同一である,浸漬ノズル。
2.
前記対をなす2つの側方突出部間の前記幅方向壁面上には,前記厚さ方向の突出長さが前記側方突出部の前記厚さ方向の突出長さよりも小さく,かつ当該側方突出部が配置された位置の内孔の厚さを1とする前記厚さ方向の合計突出長さTpが0.40以下(ゼロを含まない)である突出部(以下「中央突出部」という。)が設置されている,前記1に記載の浸漬ノズル。
3.
前記中央突出部の上端面は,前記幅方向に水平形状又は中央を頂点とする曲面若しくは屈曲点を含む上方に突出した形状である,前記2に記載の浸漬ノズル。
4.
前記側方突出部及び前記中央突出部の上端面は,内孔中心方向に水平形状又は平面若しくは曲面で下方に傾斜する形状である,前記1から前記3のいずれか一項に記載の浸漬ノズル。
5.
前記側方突出部及び前記中央突出部のいずれか一方又は両方の個々の突出長さは,それぞれ同一又は当該幅方向の壁面の中心方向に向かって直線若しくは曲線又は段状で短尺化する形状である,前記1から前記4のいずれか一項に記載の浸漬ノズル。
6.
前記側方突出部及び前記中央突出部を備えた前記側方突出部のいずれか一方又は両方は,上下方向に複数箇所に設置されている,前記1から前記5のいずれか一項に記載の浸漬ノズル。
7.
内孔の底部中央付近に上方向の突出部を有する,前記1から前記6のいずれか一項に記載の浸漬ノズル。
8.
前記浸漬ノズルは,当該浸漬ノズル上端付近の内孔横方向断面形状が円である領域の,最小断面積位置を基準にして,溶鋼流量が0.04(t/(min.・cm2))以上の連続鋳造用である,前記1から前記7のいずれか一項に記載の浸漬ノズル。
The present invention for obtaining the above-mentioned flow form is the following
1.
An immersion nozzle having a flat shape in which the width Wn of the inner hole is larger than the thickness Tn of the inner hole and having a pair of discharge holes in the lower part of the short side wall,
On the wall surface in the width direction of the flat portion, at a position axially symmetric with respect to the longitudinal center axis of the wall surface in the width direction, a portion that inclines downward in the width direction and protrudes in the thickness direction (hereinafter referred to as “side”). "Protrusions") are arranged in pairs,
The lateral protrusions are arranged on both side walls in the width direction so as to face each other,
The total protrusion length Ts in the thickness direction of the lateral protrusions, where the thickness of the inner hole at the position where the lateral protrusions are arranged is 1, is 0 for each of the two lateral protrusions forming the pair. Immersion nozzle that is the same between 18 and 0.90.
2.
On the wall surface in the width direction between the two lateral projections forming the pair, the projection length in the thickness direction is smaller than the projection length in the thickness direction of the lateral projections, and A protrusion having a total protrusion length Tp in the thickness direction of which the thickness of the inner hole at the position where the protrusion is arranged is 1 is 0.40 or less (not including zero) (hereinafter referred to as "central protrusion"). .) is installed, The immersion nozzle as described in 1 above.
3.
3. The immersion nozzle according to 2 above, wherein the upper end surface of the central protruding portion has a horizontal shape in the width direction or a curved shape having a vertex at the center or a shape protruding upward including a bending point.
4.
4. The immersion nozzle according to any one of 1 to 3 above, wherein the upper end surfaces of the side protruding portion and the central protruding portion have a horizontal shape in a central direction of the inner hole or a shape inclined downward with a flat surface or a curved surface. ..
5.
One or both of the side protruding portion and the central protruding portion may have the same protruding length, or may be a straight line, a curved line, or a stepped shape that is shortened toward the center of the widthwise wall surface. The immersion nozzle according to any one of 1 to 4 above.
6.
Either one or both of the side protrusions provided with the side protrusions and the central protrusions are installed at a plurality of positions in the vertical direction, according to any one of 1 to 5 above. Immersion nozzle.
7.
7. The immersion nozzle according to any one of 1 to 6 above, which has an upward protruding portion near the center of the bottom of the inner hole.
8.
The immersion nozzle has a molten steel flow rate of 0.04 (t/(min.·cm 2 )) with reference to the minimum cross-sectional area position in a region where the transverse cross-sectional shape of the inner hole near the upper end of the immersion nozzle is circular. The immersion nozzle according to any one of 1 to 7 above, which is for continuous casting.
なお,本発明において前記の内孔の幅Wn,厚さTnとは,浸漬ノズルの短辺側側壁部に設けた一対の吐出孔の上端位置における内孔の幅(長辺方向の長さ),厚さ(短辺方向の長さ)のことをいう。 In the present invention, the width Wn and the thickness Tn of the inner hole are the width (length in the long side direction) of the inner hole at the upper end position of the pair of discharge holes provided on the short side wall of the immersion nozzle. , Thickness (length in the short side direction).
本発明の扁平状の浸漬ノズルにより,溶鋼流の方向を中央部から側方部に亘って固定的又は完全に分離することなく,その溶鋼流を漸次増減させた連続的な状態で制御することができ,浸漬ノズル内での溶鋼流の適度なバランスを確保することができる。これにより,操業条件,特に浸漬ノズル上端付近の横方向断面形状が円である領域の,最小断面積位置を基準にして,溶鋼流量が概ね0.04(t/(min.・cm2))以上等の条件で行う,側方の吐出孔側に高速度又は多量の溶鋼流を発生させる傾向にある連続鋳造においても,吐出孔から流出する溶鋼の流速又は流量を適度に抑制し,鋳型内湯面等を安定化させる,すなわちその変動を小さくすることができる。
ひいては,鋳型内湯面変動を抑制することから,鋳型内パウダー等の巻き込みを減じ,溶鋼内介在物の浮上を促進すること等により鋳片品質を向上させることができる。また,鋳型側壁への過度な溶鋼流を抑制することから,ブレークアウト等の事故発生の危険性をも減ずることができる。
The flat immersion nozzle of the present invention controls the molten steel flow in a continuous state in which the molten steel flow is gradually increased or decreased without being fixedly or completely separated from the central portion to the lateral portions. Therefore, it is possible to secure an appropriate balance of the molten steel flow in the immersion nozzle. As a result, the molten steel flow rate is approximately 0.04 (t/(min.·cm 2 )), based on the operating conditions, especially the minimum cross-sectional area position in the area where the horizontal cross-sectional shape near the top of the immersion nozzle is circular. Even in continuous casting, which is performed under the above conditions and tends to generate a high velocity or a large amount of molten steel flow on the side of the discharge holes, the flow velocity or flow rate of the molten steel flowing out from the discharge holes is suppressed appropriately, The surface can be stabilized, that is, its fluctuation can be reduced.
As a result, the fluctuation of the molten metal level in the mold is suppressed, so that the inclusion of powder and the like in the mold is reduced, and the floating of the inclusions in the molten steel is promoted, so that the quality of the slab can be improved. Further, since the excessive molten steel flow to the side wall of the mold is suppressed, the risk of accident such as breakout can be reduced.
前述の特許文献3のような分流手段を設置することでも或る程度,幅方向端部側への溶鋼流を形成することはできる。しかしそのような固定的又は完全な分流を行った場合は,内孔での一部分すなわち単一の狭い範囲ごとに分離した溶鋼流を生じ,内孔の場所ごとに流動方向及び流速が異なる部分を生じ易い。特に溶鋼流量制御等による流量や方向の変動があった場合には溶鋼流はどちらかに偏って,浸漬ノズル内から鋳型内への吐出流及び湯面等に著しい乱れを生じることがある。
The molten steel flow to the widthwise end portion side can be formed to some extent by installing the flow dividing means as in the above-mentioned
そこで本発明では,例えば図1の第1の形態に示すように,まず浸漬ノズル10の扁平部分の幅方向(長辺側)の壁面の側方部に,当該幅方向壁面の中心軸に対して軸対称の一対の側方突出部1(図1(a)等参照。以下,単に「軸対称の側方突出部」ともいう。)を設置する。
この一対の側方突出部1の上面は,当該側方突出部1の中央側から扁平部分の幅方向かつ下方向,すなわち吐出孔4の方向に傾斜させる。このような傾斜により,内孔3内ないしは吐出孔4からの溶鋼の流速や流動形態を,渦流等の発生を抑制しつつ穏やかに変化させ,最適化することができる。
Therefore, in the present invention, for example, as shown in the first embodiment of FIG. 1, first, at the side portion of the wall surface in the width direction (long side) of the flat portion of the
The upper surfaces of the pair of
前記一対の軸対称の側方突出部は,内孔を挟んだ他方の幅方向壁面にも,扁平部分の厚さ方向に対して面対称の関係で対向して設置する(図1(b)等参照。以下,面対称の関係にある側方突出部を単に「面対称の側方突出部」ともいう。本発明では例えば図6に示すように,面対称の側方突出部1が配置された位置の内孔の厚さTnを1とする側方突出部1の前記厚さ方向の合計長さTsは,0.18以上0.90以下とする。すなわち,面対称の側方突出部の間には溶鋼が通過する空間が存在する。
このような間隔の空間を存在させることにより,内孔での溶鋼流の固定的・完全な分流をせず,溶鋼流が通過する部分の流動方向・流速を緩やかに制御する。これにより,溶鋼流が吐出孔側に明確な境界をもって流動することを緩和することができる。
The pair of axisymmetric side protrusions are installed on the other widthwise wall surface sandwiching the inner hole so as to face each other in a plane-symmetric relationship with respect to the thickness direction of the flat portion (FIG. 1(b)). Etc. Hereinafter, the side protrusions having a plane symmetry relationship are also simply referred to as “plane symmetry side protrusions.” In the present invention, for example, as shown in FIG. The total length Ts in the thickness direction of the
By providing the space with such an interval, the molten steel flow is not fixedly and completely divided in the inner hole, but the flow direction and flow velocity of the portion where the molten steel flow passes are gently controlled. As a result, the molten steel flow can be mitigated from flowing toward the discharge hole with a clear boundary.
また,側方突出部の設置場所,長さ,方向等を調整することにより,溶鋼流を中心付近又は側方側に集中させることを避けつつ,幅方向端部側すなわち吐出孔側及び中央側に分散しつつ溶鋼流に適度なバランスを与えることができる。しかも単に分散するだけではなく,側方突出部を設置した領域でも空間が連通しているので,溶鋼流は完全に分断した状態ではなくなだらかな境界を形成しつつ,緩やかに混合されて均一化しながら分散する流れとなる。 In addition, by adjusting the installation location, length, direction, etc. of the lateral protrusion, it is possible to avoid concentrating the molten steel flow near the center or on the lateral side, and at the same time, on the width direction end side, that is, the discharge hole side and the center side. It is possible to give an appropriate balance to the molten steel flow while being dispersed. Moreover, not only is it simply dispersed, but since the space is in communication even in the area where the lateral protrusions are installed, the molten steel flow is not completely divided but forms a gentle boundary, and is gently mixed and homogenized. While becoming a dispersed flow.
なお,前述のとおり側方突出部の設置場所,長さ,方向等は適宜調整することができる。例えば図2に示す第2の形態では,図1の側方突出部(図2では1aの符号を付しており,以下「下部側方突出部」ともいう。)に加え,上方に側方突出部(図2では1bの符号を付しており,以下「上部側方突出部」ともいう。)を一対設置している。
Note that, as mentioned above, the installation location, length, direction, etc. of the lateral protrusion can be adjusted as appropriate. For example, in the second embodiment shown in FIG. 2, in addition to the lateral protrusions of FIG. 1 (denoted by
さらに本発明では,軸対称の側方突出部間には,図3及び図4に示す第3及び第4の形態のように前記軸対称の側方突出部よりも突出長さが小さい突出部(中央突出部)を設置することができる。なお,図3に示す第3の形態では,図1の軸対称の側方突出部1,1間に中央突出部1pを設置し,図4に示す第4の形態では,図2の軸対称の下部側方突出部1a,1a間に中央突出部1pを設置している。
Further, according to the present invention, between the axisymmetric side protrusions, as in the third and fourth embodiments shown in FIGS. 3 and 4, the protrusions having a smaller protrusion length than the axisymmetric side protrusions. (Center protrusion) can be installed. In the third embodiment shown in FIG. 3, the
この構造は,特許文献4において前記軸対称の側方突出部よりも突出長さが大きい突出部を設置することで,前記軸対称の側方突出部間への溶鋼流よりも側方への溶鋼流を大きくすることと逆の効果,すなわち,前記軸対称の側方突出部間(中央部)への溶鋼流/側方への溶鋼流の割合を大きくする効果をもたらす。溶鋼流量が大きい(概ね0.04(t/(min.・cm2)以上))連続鋳造では,前記軸対称の側方突出部間(中央部)への溶鋼流/側方への溶鋼流の割合を小さくすることが有効であることが多い。
In this structure, in
このような中央部への溶鋼流と側方への溶鋼流のバランスは,溶鋼流速(単位時間当たり,単位断面積当たりの溶鋼流量)の大きさ,引き抜き速度,鋳型サイズ・形状,浸漬深さや吐出孔面積等のノズルの構造等により,最適化することができる。具体的には,側方突出部の幅方向ないし下方向の角度,幅方向長さ,突出長さ等,それら軸対称の側方突出部の間の中央突出部が無い構造とするか,その中央突出部の突出高さを調整する,上端面形状を調整する,等の方法を採ることができる。
具体的に中央突出部の突出長さについては,図6に例示しているように,その突出長さTp/2は側方突出部1の突出長さTs/2よりも小さく,かつ当該側方突出部1が配置された位置の内孔の厚さTnを1とする合計突出長さTpが0.40以下となるようにする。言い換えれば、Tp<Ts,かつTp/Tn≦0.40とする。
The balance between the molten steel flow to the central part and the molten steel flow to the side is such as the magnitude of molten steel flow velocity (molten steel flow rate per unit time, per unit cross-sectional area), drawing speed, mold size/shape, immersion depth, and so on. It can be optimized depending on the nozzle structure such as the discharge hole area. Specifically, there is no central protrusion between the side protrusions that are axially symmetrical, such as the widthwise or downward angle of the side protrusions, the length in the width direction, the protrusion length, or the like. Methods such as adjusting the protruding height of the central protruding portion and adjusting the shape of the upper end surface can be adopted.
Specifically, as shown in FIG. 6, the protrusion length Tp/2 of the central protrusion is smaller than the protrusion length Ts/2 of the
また,中央突出部の上端面は,図8に示すように幅方向に水平形状,又は図5及び図7に示すように中央を頂点とする曲面若しくは屈曲点を含む上方に突出した形状とすることができる。このような形状により,溶鋼の流速や流動形態をさらに変化させ,最適化することもできる。 Further, the upper end surface of the central protruding portion has a horizontal shape in the width direction as shown in FIG. 8 or a shape protruding upward including a curved surface or a bending point having the center at the apex as shown in FIGS. 5 and 7. be able to. With such a shape, the flow velocity and flow form of molten steel can be further changed and optimized.
さらに側方突出部又は中央突出部の上端面は,図9に示すように浸漬ノズル扁平部分の幅方向(長辺側)壁面との境界部を頂点にして浸漬ノズル扁平部分の厚さ方向の中心方向すなわち内孔中心方向(空間側)かつ下方に傾斜させることもできる。このような傾斜により,溶鋼の流速や流動形態をさらに変化させ,最適化することもできる。 Further, as shown in FIG. 9, the upper end surface of the lateral protrusion or the central protrusion has a boundary portion with the wall surface in the width direction (long side) of the flat portion of the immersion nozzle as an apex in the thickness direction of the flat portion of the immersion nozzle. It is also possible to incline downward in the central direction, that is, in the central direction of the inner hole (space side). With such an inclination, the flow velocity and flow form of molten steel can be further changed and optimized.
さらに側方突出部又は中央突出部の上端面の突出長さは,図10に示すように同一とすることができるほか,図11~図13に示すように浸漬ノズル扁平部分の幅方向(長辺側)壁面の中心方向に向かって短尺化するように傾斜させることもできる。このような傾斜により,溶鋼の流速や流動形態をさらに変化させ,最適化することもできる。 Further, the protrusion length of the upper end surface of the side protrusion or the central protrusion can be the same as shown in FIG. 10, and as shown in FIGS. It is also possible to incline so that the length becomes shorter toward the center of the wall surface. With such an inclination, the flow velocity and flow form of molten steel can be further changed and optimized.
扁平状の浸漬ノズルでは短辺側側壁部の吐出孔が縦方向に長く開放する形態になるので,その吐出孔では上方側に吐出流速が小さくなる部分が生じることがあり,特に上端部付近では浸漬ノズル内に引き込む逆流現象もしばしば観られる。そこで,本発明では例えば図2及び図4に示すように,前述の軸対称及び面対称の下部側方突出部1aに加え,その上方に1又は複数の軸対称及び面対称の側方突出部1b(上方側方突出部)を設置することができる。この上方側方突出部1bは,前述の下方側方突出部1aと同様な最適化構造とすることができる。
In a flat dipping nozzle, the discharge holes on the short side wall are opened long in the vertical direction, so there may be a part where the discharge flow velocity decreases at the upper side, especially near the upper end. A backflow phenomenon that draws into the submerged nozzle is also often seen. Therefore, in the present invention, as shown in FIG. 2 and FIG. 4, for example, in addition to the above-mentioned axially symmetric and plane symmetric
この上方側方突出部1bは,特に吐出孔上方での流速の低下,ないしは上端部付近での逆流等の溶鋼流の乱れを抑制して吐出孔の縦方向の位置ごとの流速分布を均一化する機能を補完すると共に,上限方向での流量バランスを調整する機能をも有する。
この上部側方突出部1b,1b間にも,前述の下方側方突出部1a,1a間と同様に中央突出部を設置することもできる。
The upper
Also between the
なお,浸漬ノズル内部の底部5は,図14のように中央付近に吐出孔を形成しないで,単なる鋳型との隔壁としての壁面としてもよく,又は図1~図5,図7,図8,図15,図16等のように中央部を上方に突出させて底部突出部を含む構造としてもよい。さらに図17のように底部5には吐出孔6を設けてもよい。このような底部の突出構造は,中央部への溶鋼流を吐出孔方向に変換する際の流動方向・形態,流速等を変化させるのに役立つ。
The
次に本発明を実施例と共に説明する。 Next, the present invention will be described together with examples.
[実施例A]
実施例Aは図2に示す本発明の第2の形態,すなわち突出部として軸対称かつ面対称の側方突出部2段1a,1bを設置し,下部側方突出部1a,1a間には中央突出部を設置しない形態,及び図4に示す本発明の第4の形態,すなわち突出部として軸対称かつ面対称の側方突出部2段1a,1bを設置し,下方側方突出部1a,1a間に中央突出部1pを設置した形態の浸漬ノズルにつき,下方側方突出部1a及び中央突出部1pの浸漬ノズル内孔空間方向への突出長さ(面対称一対の突出部の合計の長さ)Ts,Tpの,浸漬ノズル内孔の厚さ(短辺方向の長さ)Tnに対する比Ts/Tn,Tp/Tnと,鋳型内湯面変動程度(鋳型内偏流指数及び鋳型内湯面変動高さ)の関係を示す,水モデル実験結果である。
[Example A]
Example A is the second embodiment of the present invention shown in FIG. 2, that is, axially symmetric and plane symmetrical two-
浸漬ノズルの仕様は次の通りである。
・全長 : 1165mm
・溶鋼導入口 : φ86mm
・吐出孔上端位置の内孔幅(Wn) : 255mm
・吐出孔上端位置の内孔厚さ(Tn) : 34mm
・吐出孔上端位置のノズル下端面からの高さ : 146.5mm
・中央突出部の高さ(ノズル下端面からの高さ) : 155mm
・浸漬ノズルの壁厚さ : 約25mm
・浸漬ノズルの底部の厚さ(中央部頂点) : 高さ100mm
・上方側方突出部(1b) : 浸漬ノズル幅方向の長さ(左右各々)は25mm,
Ts/Tn比=0.74,
吐出孔方向への傾斜角度は45度,
上端面の浸漬ノズル幅方向及び厚み方向は水平,
側方突出部間は100mm,
中央突出部は無し
・下方側方突出部(1a) : 浸漬ノズル幅方向の長さ(左右各々)は40mm,
Ts/Tn比=0.1~1.0(空間無し),
吐出孔方向への傾斜角度は45度,
上端面の浸漬ノズル幅方向及び厚み方向は水平,
側方突出部間は60mm,
中央突出部Tp/Tn比=0(無し)~0.7
The specifications of the immersion nozzle are as follows.
・Total length: 1165 mm
・Melted steel inlet: φ86mm
・Inner hole width (Wn) at the top of the discharge hole: 255 mm
・Inner hole thickness (Tn) at the top of the discharge hole: 34 mm
・Height from the lower end surface of the nozzle at the upper end position of the discharge hole: 146.5 mm
・Height of central protruding portion (height from the lower end surface of the nozzle): 155 mm
・Wall thickness of immersion nozzle: Approx. 25 mm
・Thickness of bottom of dipping nozzle (top of central part): Height 100mm
・Upward lateral protrusion (1b): The length in the width direction of the immersion nozzle (each on the left and right) is 25 mm,
Ts/Tn ratio=0.74
The inclination angle to the discharge hole direction is 45 degrees,
The immersion nozzle on the top surface is horizontal in the width and thickness directions,
100 mm between the lateral protrusions,
No central protruding part ・Lower lateral protruding part (1a): 40 mm in length (left and right) in the width direction of the immersion nozzle
Ts/Tn ratio=0.1 to 1.0 (no space),
The inclination angle to the discharge hole direction is 45 degrees,
The immersion nozzle on the top surface is horizontal in the width and thickness directions,
60 mm between the lateral protrusions,
Central protrusion Tp/Tn ratio=0 (none) to 0.7
鋳型,流体の条件は次の通りである。
・鋳型の幅 : 1650mm
・鋳型の厚さ : 65mm(中央上端部185mm)
・浸漬深さ(吐出孔上端から水面まで): 83mm
・流体の供給速度 : 0.065t/(min・cm2)
※溶鋼に換算した値
The conditions of the mold and fluid are as follows.
・Width of mold: 1650mm
-Thickness of mold: 65 mm (center upper end 185 mm)
・Dip depth (from top of discharge hole to water surface): 83mm
・Fluid supply rate: 0.065t/(min·cm 2 )
*Value converted to molten steel
ここで鋳型内偏流指数を偏流が無い場合を1.0とする指数で0.8≦鋳型内偏流指数≦1.2,鋳型内湯面変動高さ(mm)を≦15mmを本発明の課題解決効果が得られたとみなし,評価の基準とした。
なお,鋳型内偏流指数とは水モデル実験にて鋳型内の浸漬ノズル吐出孔側左右各々の設定湯面(設定水位上端面から30mmの水中位置)の流速を測定し,前記左右の流速を比で表したときのその絶対値,すなわち,左流速/右流速(又は右流速/左流速)の値であり,鋳型内湯面変動高さとは,図18中のSwの最大値である。
Here, the index of drift in the mold is set to be 1.0 when there is no drift, and 0.8 is the index of drift in the mold ≦1.2, and the height of fluctuation of the molten metal in the mold (mm) is ≦15 mm. It was considered that the effect was obtained, and it was used as the evaluation standard.
The drift index in the mold is measured in water model experiments by measuring the flow velocities of the left and right set molten metal surfaces (30 mm underwater from the upper end of the set water level) of the immersion nozzle in the mold, and comparing the left and right flow rates. It is the absolute value when expressed by, that is, the value of the left flow velocity/the right flow velocity (or the right flow velocity/the left flow velocity), and the level of fluctuation of the molten metal in the mold is the maximum value of Sw in FIG.
結果を表1に示す。
鋳型内偏流指数及び鋳型内湯面変動高さは,側方突出部については,Tnに対するTs比率(Ts/Tn)が0.18以上0.90以下で基準を満足できることができることがわかる。
また,中央突出部を設置した場合については,その突出長さが側方突出部の突出長さより小さく(Tp<Ts),かつTnに対するTp比率(Tp/Tn)が0.4以下の場合に基準を満足することができることがわかる。
It can be seen that the drift index in the mold and the fluctuation level of the molten metal surface in the mold can satisfy the criteria when the ratio of Ts to Tn (Ts/Tn) is 0.18 or more and 0.90 or less for the lateral protrusion.
Further, in the case where the central protruding portion is installed, when the protruding length is smaller than the protruding length of the lateral protruding portion (Tp<Ts) and the Tp ratio (Tp/Tn) to Tn is 0.4 or less, It turns out that the criteria can be met.
[実施例B]
実施例Bは,図4に示す本発明の第4の形態において,下方側方突出部1a及び中央突出部1pの上端面を、図9に示すような内孔中心方向に平面で下方に傾斜する形状とした場合の鋳型内湯面変動程度を示す,水モデル実験結果である。
[Example B]
In Example B, in the fourth mode of the present invention shown in FIG. 4, the upper end surfaces of the lower
ここでは,下方側方突出部のTs/Tn比=0.74,中央突出部のTp/Tn比=0.18とし,下段側方突出部及び中央突出部の内孔方向への傾斜角度(図9のθ)は0度(水平)の場合と45度の場合を比較した。他の条件は実施例Aと同じである。 Here, the Ts/Tn ratio of the lower side protruding portion=0.74, the Tp/Tn ratio of the central protruding portion=0.18, and the inclination angles of the lower side protruding portion and the central protruding portion toward the inner hole ( 9 is compared with the case of 0 degree (horizontal) and the case of 45 degrees. Other conditions are the same as in Example A.
結果を図19に示す。図19の縦軸は,傾斜角度θが0度,45度いずれの場合も吐出孔左右方向の最大湯面変動値Sw(mm)を平均した値である。 The results are shown in Fig. 19. The vertical axis of FIG. 19 is a value obtained by averaging the maximum melt level fluctuation value Sw (mm) in the left and right directions of the discharge hole regardless of whether the inclination angle θ is 0 degrees or 45 degrees.
図19に示すように,傾斜角度θが0度,45度いずれの場合も基準の15mmより顕著に小さい値であるが,さらに45度の場合は2.0(mm)と,0度の場合の3.75(mm)の約1/2程度に低減されていることがわかる。 As shown in FIG. 19, when the inclination angle θ is 0 degree or 45 degrees, the value is significantly smaller than the reference value of 15 mm, but when the inclination angle θ is 45 degrees, the value is 2.0 (mm) and 0 degree. It can be seen that it is reduced to about 1/2 of 3.75 (mm).
10: 浸漬ノズル
1 : 側方突出部
1a: 下部側方突出部
1b: 上部側方突出部
1p: 中央突出部
2 : 溶鋼導入口
3 : 内孔(溶鋼流路)
4 : 吐出孔(短辺側の壁側)
5 : 底部
6 : 吐出孔(底部)
7 : 湯面
20: 鋳型
Wn: 浸漬ノズルの内孔の幅(長辺方向の長さ)
Wp: 側方突出部の両端部間の幅
Wc: 中央突出部の幅
Tn: 浸漬ノズルの内孔の厚さ(短辺方向の長さ)
Ts: 側方突出部の空間方向への突出長さ(一対の合計の長さ)
Tp: 中央突出部の空間方向への突出長さ(一対の合計の長さ)
ML: 鋳型幅(長辺)
Ms: 鋳型厚さ(短辺,側部)
Mc: 鋳型厚さ(短辺,中央部)
Sw: 鋳型内の湯面変動幅(上端,下端間の寸法)
10: Immersion nozzle 1:
4: Discharge hole (short side wall side)
5: Bottom part 6: Discharge hole (bottom part)
7: molten metal surface 20: mold Wn: width of inner hole of immersion nozzle (length in long side direction)
Wp: Width between both ends of the lateral protrusion Wc: Width of central protrusion Tn: Thickness of inner hole of immersion nozzle (length in short side direction)
Ts: protrusion length of the lateral protrusion in the space direction (total length of a pair)
Tp: Length of protrusion of the central protrusion in the space direction (total length of a pair)
ML: Mold width (long side)
Ms: Mold thickness (short side, side)
Mc: Mold thickness (short side, central part)
Sw: Fluctuation width of molten metal in the mold (dimension between upper and lower ends)
Claims (8)
扁平部分の幅方向の壁面上に,前記幅方向の壁面の縦方向中心軸に対して軸対称の位置に,前記幅方向かつ下方向に傾斜して厚さ方向に突出した部分(以下「側方突出部」という。)が対をなして配置されており,
前記側方突出部は前記幅方向の両壁面上に対向して配置されており,
当該側方突出部が配置された位置の内孔の厚さを1とする前記側方突出部の前記厚さ方向の合計突出長さTsは,前記対をなす2つの側方突出部それぞれ0.18以上0.90以下で同一である,浸漬ノズル。 An immersion nozzle having a flat shape in which the width Wn of the inner hole is larger than the thickness Tn of the inner hole and having a pair of discharge holes in the lower part of the short side wall,
On the wall surface in the width direction of the flat portion, at a position axially symmetric with respect to the longitudinal center axis of the wall surface in the width direction, a portion that inclines downward in the width direction and protrudes in the thickness direction (hereinafter referred to as “side”). "Protrusions") are arranged in pairs,
The lateral protrusions are arranged on both side walls in the width direction so as to face each other,
The total protrusion length Ts in the thickness direction of the lateral protrusions, where the thickness of the inner hole at the position where the lateral protrusions are arranged is 1, is 0 for each of the two lateral protrusions forming the pair. Immersion nozzle that is the same between 18 and 0.90.
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BR112021010225-6A BR112021010225A2 (en) | 2019-01-21 | 2020-01-15 | immersion nozzle |
| CA3121954A CA3121954C (en) | 2019-01-21 | 2020-01-15 | SUBMERSIBLE NOZZLE |
| US17/424,301 US20220134420A1 (en) | 2019-01-21 | 2020-01-15 | Immersion nozzle |
| CN202080007527.0A CN113226594B (en) | 2019-01-21 | 2020-01-15 | Dip Nozzle |
| EP20744229.4A EP3915696A4 (en) | 2019-01-21 | 2020-01-15 | SUBMERSIBLE NOZZLE |
| ZA2021/03504A ZA202103504B (en) | 2019-01-21 | 2021-05-24 | Immersion nozzle |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2019-007948 | 2019-01-21 | ||
| JP2019007948A JP7134105B2 (en) | 2019-01-21 | 2019-01-21 | immersion nozzle |
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| Publication Number | Publication Date |
|---|---|
| WO2020153195A1 true WO2020153195A1 (en) | 2020-07-30 |
Family
ID=71736051
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2020/001078 Ceased WO2020153195A1 (en) | 2019-01-21 | 2020-01-15 | Immersion nozzle |
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| Country | Link |
|---|---|
| US (1) | US20220134420A1 (en) |
| EP (1) | EP3915696A4 (en) |
| JP (1) | JP7134105B2 (en) |
| CN (1) | CN113226594B (en) |
| BR (1) | BR112021010225A2 (en) |
| CA (1) | CA3121954C (en) |
| TW (1) | TWI731561B (en) |
| WO (1) | WO2020153195A1 (en) |
| ZA (1) | ZA202103504B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2025004949A1 (en) * | 2023-06-27 | 2025-01-02 | 黒崎播磨株式会社 | Immersion nozzle |
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|---|---|---|---|---|
| WO2025004949A1 (en) * | 2023-06-27 | 2025-01-02 | 黒崎播磨株式会社 | Immersion nozzle |
Also Published As
| Publication number | Publication date |
|---|---|
| BR112021010225A2 (en) | 2021-08-24 |
| TWI731561B (en) | 2021-06-21 |
| ZA202103504B (en) | 2022-07-27 |
| TW202035036A (en) | 2020-10-01 |
| JP7134105B2 (en) | 2022-09-09 |
| JP2020116591A (en) | 2020-08-06 |
| EP3915696A1 (en) | 2021-12-01 |
| EP3915696A4 (en) | 2022-09-14 |
| CN113226594B (en) | 2023-03-14 |
| CA3121954A1 (en) | 2020-07-30 |
| CA3121954C (en) | 2025-03-11 |
| US20220134420A1 (en) | 2022-05-05 |
| CN113226594A (en) | 2021-08-06 |
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