Patent Grant
8240524
The present invention relates to an upper nozzle adapted to be fitted into a discharge opening of a ladle or a tundish, and particularly to an upper nozzle capable of suppressing deposit formation.
In an upper nozzle adapted to be fitted into a discharge opening of a tundish or a ladle and formed with a bore for allowing molten steel to flow therethrough, alumina and other inclusions are apt to be attached inside the bore to form a deposit thereon, which narrows a flow passage to hinder a casting operation, or is likely to fully clog the flow passage to preclude the casting operation. As one example of a technique for preventing the deposit formation, it has been proposed to provide a gas injection port to inject an inert gas (see, for example, the following Patent Document 1 or 2).
However, an upper nozzle disclosed in the Patent Document 1 or 2 is a gas injection type, which needs to take a lot of time and effort for production due to its complicated structure, and requires an inert gas for a casting operation, resulting in increased cost. Moreover, even such a gas injection-type nozzle has difficulty in fully preventing the deposit formation.
An upper nozzle has been widely used, for example, in the following two configurations: one consisting of a reverse taper region formed on an upper (upstream) side of the upper nozzle and a straight region formed on a lower (downstream) side of the upper nozzle (see
As a result of calculation of a distribution of pressures to be applied to a wall surface of a bore (bore surface) of an upper nozzle (length: 230 mm) having the configuration illustrated in
Further, as a result of calculation of a distribution of pressures to be applied to a wall surface of a bore (bore surface) of an upper nozzle (length: 230 mm) having the configuration illustrated in
The rapid pressure change and the arc-curved pressure change is caused by a phenomenon that a molten steel flow is changed as the bore surface is changed from the reverse taper configuration to the straight configuration. Further, in a swirling nozzle adapted to intentionally change a molten steel flow, a deposit is observed around a position where the molten steel flow is changed. Thus, it is considered that a deposit inside the bore of the upper nozzle can be suppressed by creating a smooth molten steel flow, i.e., a molten steel flow having an approximately constant change in pressure on the bore surface.
As a technique of stabilizing a molten steel flow, there has been proposed an invention relating to a configuration of a bore of a tapping tube for a converter (see, for example, the following Patent Document 3).
However, a technique disclosed in the Patent Document 3 is intended to prevent a vacuum area from being formed in a central region of a molten steel flow, so as to suppress entrapment of slag and incorporation of oxygen, nitrogen, etc., but it is not intended to prevent the deposit formation. Further, the technique disclosed in the Patent Document 3 is designed for a converter (refining vessel), wherein a period when the effect of preventing entrapment of slag and incorporation of oxygen, nitrogen, etc., becomes important is a last stage of molten steel discharge (given that a tapping time is 5 minutes, the last stage is about 1 minute). In contract, for preventing the deposit formation in a ladle or a tundish (casting or pouring vessel), it is necessary to bring out an intended effect particularly in a period other than the last stage of molten steel discharge, i.e., a desired timing of bringing out an intended effect is different.
It is therefore an object of the present invention to provide an upper nozzle having a configuration of a bore, which is capable of facilitating stabilization of a pressure to be applied from an outer peripheral region of a molten steel flow onto a bore surface, so as to create a low-energy loss (smooth) molten steel flow to suppress the deposit formation.
The present invention provides an upper nozzle adapted to be fitted into a discharge opening of a tundish or a ladle and formed with a bore for allowing molten steel to flow therethrough. The bore comprises a bore surface having, as viewed in cross-section taken along an axis of the bore, a configuration which is a specific curve defined to have continuous differential values of r(z) with respect to z, between two curves represented by the following respective formulas: log(r(z))=(1/1.5)×log((H+L)/(H+z))+log(r(L)); and log(r(z))=(1/6)×log((H+L)/(H+z))+log(r(L)), wherein: L is a length of the upper nozzle; H is a calculational hydrostatic head height; and r(z) is a radius of the bore at a distance z from an upper (upstream) end of the bore, and wherein: the calculational hydrostatic head height H is represented by the following formula: H=((r(L)/r(0)n×L)/(1−(r(L)/r(0))n) (n=1.5 to 6); and the radius r(0) of the bore at the upper end thereof is equal to or greater than 1.5 times the radius r(L) of the bore at a lower (downstream) end thereof.
In the present invention, at least 80% of the bore surface as viewed in cross-section taken along the axis of the bore may be configured as the specific curve.
In the present invention, the bore surface as viewed in cross-section taken along the axis of the bore may be configured as a specific curve represented by the following formula: log(r(z))=(1/n)×log((H+L)/(H+z))+log(r(L)) (n=1.5 to 6). In this case, at least 80% of the bore surface may also be configured as the specific curve.
The present invention can suppress deposit formation on the bore of the upper nozzle for allowing molten steel to flow therethrough.
a) and 2(b) are, respectively, a diagram showing a configuration of an upper nozzle, and a graph showing a pressure distribution during flowing of molten steel through the upper nozzle, wherein n=1.5.
a) and 3(b) are, respectively, a diagram showing a configuration of an upper nozzle, and a graph showing a pressure distribution during flowing of molten steel through the upper nozzle, wherein n=2.
a) and 4(b) are, respectively, a diagram showing a configuration of an upper nozzle, and a graph showing a pressure distribution during flowing of molten steel through the upper nozzle, wherein n=4.
a) and 5(b) are, respectively, a diagram showing a configuration of an upper nozzle, and a graph showing a pressure distribution during flowing of molten steel through the upper nozzle, wherein n=5.
a) and 6(b) are, respectively, a diagram showing a configuration of an upper nozzle, and a graph showing a pressure distribution during flowing of molten steel through the upper nozzle, wherein n=6.
a) and 7(b) are, respectively, a diagram showing a configuration of an upper nozzle, and a graph showing a pressure distribution during flowing of molten steel through the upper nozzle, wherein n=7.
a) and 8(b) are, respectively, a diagram showing a configuration of an upper nozzle, and a graph showing a pressure distribution during flowing of molten steel through the upper nozzle, wherein n=8.
a) and 9(b) are, respectively, a diagram showing a configuration of an upper nozzle, and a graph showing a pressure distribution during flowing of molten steel through the upper nozzle, wherein n=1.
a) and 10(b) are, respectively, a diagram showing a configuration of an upper nozzle, and a graph showing a pressure distribution during flowing of molten steel through the upper nozzle, wherein n=4, and a radius ratio=1.5.
a) and 11(b) are, respectively, a diagram showing a configuration of an upper nozzle, and a graph showing a pressure distribution during flowing of molten steel through the upper nozzle, wherein the radius ratio=1.
a) and 12(b) are, respectively, a diagram showing a configuration of a conventional upper nozzle, and a graph showing pressure distribution during flowing of molten steel through the conventional upper nozzle.
a) and 13(b) are, respectively, a diagram showing a configuration of a conventional upper nozzle, and a graph showing pressure distribution during flowing of molten steel through the conventional upper nozzle.
With reference to the accompanying drawings, the best mode for carrying out the present invention will now be specifically described.
In the present invention, the bore surface 14 has, as viewed in cross-section taken along an axial direction of the bore 11, a configuration (log(r(z)) which is a smooth curve defined between two curves 15, 16 represented by the following respective formulas: log(r(z))=(1/1.5)×log((H+L)/(H+z))+log(r(L)); and log(r(z))=(1/6)×log((H+L)/(H+z))+log (r(L)), and more preferably a curve represented by the following formula: log(r(z))=(1/n)×log((H+L)/(H+z))+log(r(L)) (n: 1.5 to 6). As used herein, the term “smooth curve” means a curve having continuous differential values of r(z), i.e., a line composed with a curve and a tangent to the curve.
On an assumption that a low-energy loss or smooth (constant) molten steel flow can be created by stabilizing a pressure distribution on a bore surface of an upper nozzle in a height direction of the upper nozzle, the inventors of this application has found a bore configuration of the present invention capable of suppressing a rapid change in pressure on a bore surface, as described below.
Although an amount of molten steel flowing through a bore of an upper nozzle is controlled by an SN unit disposed underneath (just downstream of) the upper nozzle, energy for providing a flow velocity of molten steel is fundamentally a hydrostatic head of molten steel in a tundish. Thus, a flow velocity v(z) of molten steel at a position where a distance from an upper end of the bore in a vertically downward (downstream) direction is z, is expressed as follows:
v(z)=k(2g(H′+z))1/2,
wherein: g is a gravitational acceleration; H′ is a hydrostatic head height of molten steel; and k is a flow coefficient.
A flow volume Q of molten steel flowing through the bore of the upper nozzle is a product of a flow velocity v and a cross-sectional area A. Thus, the flow volume Q is expressed as follows:
Q=v(L)×A(L)=k(2g(H′+L))1/2×A(L),
wherein: L is a length of the upper nozzle; v(L) is a flow velocity of molten steel at a lower end of the bore; and A(L) is a cross-sectional area of the lower end of the bore.
Further, the flow volume Q is constant at any position of the bore in a cross-section taken along a direction perpendicular to an axis of the bore. Thus, a cross-sectional area A(z) at a position where the distance from the upper end of the bore is z, is expressed as follows:
A(z)=Q/v(z)=k(2g(H′+L))1/2×A(L)/k(2g(H′+z))1/2
The above equation can be expressed as follows by dividing each of the left-hand and right-hand sides by A(L):
A(z)/A(L)=((H′+L)/(H′+z))1/2
Given that a ratio of the circumference of a circle to its diameter is π, A(z)=7πr(L)2. The above equation is expressed as follows:
A(z)/A(L)=πr(z)2/πr(L)2=((H′+L)/(H′+z))1/2r(z)/r(L)=((H′+L)/(H′+z))1/4 (1)
Thus, a radius r(z) at an arbitrary position of the bore is expressed as follows:
log(r(z))=(1/4)×log((H′+L)/(H′+z))+log(r(L))
Therefore, an energy loss can be minimized by setting a cross-sectional configuration of the bore surface to satisfy this condition.
During a casting operation, an amount of molten steel in a tundish is kept approximately constant, i.e., the hydrostatic head height of molten steel is constant. However, it is known that molten steel located adjacent to a molten-steel level in the tundish does not flow directly flow into an upper nozzle but molten steel located adjacent to a bottom surface of the tundish flows into the upper nozzle. Further, in a ladle, it is known that, although a molten-steel level height is changed, molten steel located adjacent to a bottom surface of the ladle flows into an upper nozzle in the same manner as that in the tundish. A radius (diameter) of the lower end (small end) of the bore of the upper nozzle is determined by a required throughput.
Through various researches, the inventors found that a rapid pressure change which may occur in a vicinity of the upper end of the bore can be suppressed by setting an inner radius (diameter) of the upper end (large end) of the bore to be equal to or greater than 1.5 times an inner radius (diameter) of the lower end (small end) of the bore. The reason is that, if the inner radius of the upper end is less than 1.5 times the inner radius of the lower end, it is difficult to adequately ensure a distance for smoothing a configuration from the tundish or ladle to the upper nozzle, and thereby the configuration is rapidly changed. Preferably, the inner radius of the upper end is equal to or less than 2.5 times the inner radius of the lower end. The reason is that, if the inner radius of the upper end becomes greater than 2.5 times the inner radius of the lower end, a discharge opening of the tundish or ladle will be unrealistically increased.
In accordance with the above equation (1), a radius ratio of the large end to the small end of the bore is expressed as follows:
r(0)/r(L)=((H+L)/(H+0))1/4=1.5 to 2.5
This means that, if respective inner radii of the upper end and the lower end, and a ratio of the upper end to the lower end, are determined, a calculational hydrostatic head height H can be obtained. Specifically, the calculational hydrostatic head height H is expressed as follows:
H=((r(L)/r(0))4×L)/(1−(r(L)/r(0))4)
Then, the inventors considered that, in an equation “log(r(z))=(1/n)×log((H+L)/(H+z))+log(r(L))” which is converted from the above equation “log(r(z))=(1/4)×log((H′+L)/(H′+z))+log(r(L))” by substituting the hydrostatic head height H′ of molten steel with the calculational hydrostatic head height H, even if n is a number other than 4, a molten steel flow may become smoother than ever before as long as an upper nozzle is formed with a bore which comprises a bore surface having a cross-sectional configuration obtained by changing a value of n, and verified a pressure on a bore surface in each of a plurality of upper nozzles where the bore surface is formed in various configurations by changing the value of n.
Further, in this verification, the parameter n was also applied to convert the above equation of the calculational hydrostatic head height H, as follows:
H=((r(L)/r(0)n×L)/(1−(r(L)/r(0)n)
The radius ratio of the large end to the small end of the bore is expressed as follows: r(0)/r (L)=((H+L)/(H+0))1/4=1.5 to 2.5. Thus, if respective inner radii of the upper end and the lower end, and a ratio of the upper end to the lower end, are determined, a calculational hydrostatic head height H in each value of n can be obtained.
The present invention will be more spastically described based on examples. It is understood that the following examples will be shown simply by way of illustrative embodiments of the present invention, and the present invention is not limited to the examples.
In the following examples, a distribution of pressures to be applied to a bore surface of an upper nozzle, wherein: a length of the upper nozzle is 230 mm; a diameter of a large end of a bore of the upper nozzle is 140 mm; and a diameter of a small end of the bore of the upper nozzle is 70 mm, and when a hydrostatic head height of a tundish or a ladle is 1000 mm. In Example 1, the pressure distribution was calculated using an upper nozzle illustrated in
an upper nozzle (Inventive Example 2) illustrated in
an upper nozzle (Inventive Example 3) illustrated in
an upper nozzle (Inventive Example 4) illustrated in
an upper nozzle (Inventive Example 5) illustrated in
an upper nozzle (Comparative Example 1) illustrated in
an upper nozzle (Comparative Example 2) illustrated in
an upper nozzle (Comparative Example 3) illustrated in
In Inventive Examples 1 to 3 (n=1.5 to 4), it was verified that the pressure is gradually changed in a region from the upper end to the lower end of the bore. In view of a fact that no rapid pressure change occurs, it is proven that a molten steel flow is approximately constant.
In Inventive Examples 4 and 5 (n=5 and 6), it was verified that, although a relatively large pressure change was observed in a vicinity of the upper end of the bore, the pressure is subsequently gradually changed. It is proven that a molten steel flow is approximately constant in a region other than the vicinity of the upper end of the bore where a bore diameter is relatively large and a deposit problem is less likely to occur.
In Comparative Examples 1 and 2 (n=7 and 8), the pressure is largely changed from about 100 Pa or about 200 Pa in a vicinity of the upper end of the bore. Specifically, it was verified that a pressure greater than that in the conventional upper nozzle illustrated in
In Comparative Example 3 (n=1), where the bore inner wall has a reverse taper configuration, and a corner is formed in a contact region with the upper plate, it was verified that, although a pressure change in the upper nozzle is relatively small, a rapid pressure change occurs just after molten steel flows from the upper nozzle into the upper plate, as evidenced, for example, by a comparison between
As above, in the present invention, it is proven that a change in pressure to be applied to the bore surface is approximately constant during flowing of molten steel through the bore of the upper nozzle, i.e., a molten steel flow is low in energy loss, or constant. A molten-steel level in a ladle is gradually lowered from about 4000 mm, and a molten-steel level in a tundish is about 500 mm. However, as mentioned above, molten metal flowing into the discharge opening is molten metal located adjacent to a bottom surface of the tundish or the ladle. Thus, even if the molten-steel level height is changed, a pressure distribution has the same characteristic as those in Inventive and Comparative Examples, although a value of the pressure is changed.
In Inventive Example 6, the pressure distribution was calculated in the same manner as that in Inventive Example 1, using an upper nozzle illustrated in
In Comparative Example 4, the pressure distribution was calculated in the same manner as that in Inventive Example 1, using an upper nozzle illustrated in
In Comparative Example 4 where a radius (diameter) ratio of the large end to the small end of the bore is about 1 (1.06), a pressure change in a vicinity of the upper end of the bore is relatively large. In contract, in Inventive Example 6 where the radius ratio is 1.5 (the radius of the upper end: 1.5D), and Inventive Example 3 where the radius ratio is 2 (the radius of the upper end: 2D), it was verified that a pressure change is approximately constant even in a vicinity of the upper end of the bore. In the case where the configuration of the bore surface is represented by the log(r(z)), a wall surface continuously extending from a tundish or a ladle to the upper nozzle becomes smoother along with an increase in radius (diameter) of the bore. This proves that a rapid pressure change in the vicinity of the upper end of the bore can be suppressed by setting the radius (diameter) of the upper end of the bore to be equal to or greater than 1.5 times the radius (diameter) of the lower end of the bore.
Further, if there is a corner or a corner-like configuration, a rapid pressure change is observed as in the pressure changes in the conventional upper nozzle and Comparative Examples 1 to 4. Thus, when a bore surface is formed in a vertical cross-sectional configuration defined between log(r(z))=(1/1.5)×log((H+L)/(H+z))+log(r(L)) and log(r(z))=(1/6)×log ((H+L)/(H+z))+log(r(L)), in such a manner as to become smooth and free from formation of a corner, i.e., to have continuous differential values of r(z) with respect to z (d (r(z))/dz), a metal steel flow can be stabilized so as to suppress the deposit formation.
A configuration of a region adjacent to the upper end of the bore is likely to be determined by a factor, such as a configuration of a stopper. Further, the region adjacent to the upper end of the bore is relatively large in inner radius (diameter), and less affected by a deposit. In contract, a configuration of a region adjacent to the lower end of the bore is likely to be determined by a factor in terms of production. For example, in some cases, the region adjacent to the lower end of the bore has to be formed in a straight body due to a need for inserting a tool thereinto during a production process. Thus, the bore surface may be formed in the vertical cross-sectional configuration represented by log(r(z))=(1/n)×log((H+L)/(H+z))+log(r (L)) (n=1.5 to 6), by at least 80% thereof. Further, a bubbling mechanism adapted to inject an inert gas, such as Ar gas, may be used in combination.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2008-065154 | Mar 2008 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP2009/054877 | 3/13/2009 | WO | 00 | 3/29/2010 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2009/113662 | 9/17/2009 | WO | A |
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| Number | Date | Country | |
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| 20100219212 A1 | Sep 2010 | US |
