TUNDISH FOR CONTINUOUS CASTING

Abstract

The present invention provides a tundish for continuous casting, the tundish having an inner volume including an inlet portion including an inlet for receiving molten metal, an outlet portion including at least one outlet for discharging molten metal, and a flow separator. The tundish further includes an EMS stirrer for electromagnetic stirring, wherein, the flow separator is positioned between the inlet portion and the outlet portion, the EMS stirrer is disposed outside of the tundish, at a vertical position below the top of the inner volume of the tundish and above the bottom of the inner volume of the tundish, the EMS stirrer is disposed to make the molten metal in the outlet portion flow in a horizontal direction, and the flow which is directly induced by the EMS stirrer flows away from the inlet.

Description

TECHNICAL FIELD

The present invention relates to a tundish for continuous casting, in particular to a tundish having an EMS stirrer for electromagnetic stirring, a method of stirring a molten metal in a tundish, and the use of an EMS stirrer for stirring a molten metal in a tundish.

BACKGROUND

Several methods for improving the temperature homogenization and steel cleanliness in a tundish have been proposed. One method is EMS stirring. Gas purging has also been applied to increase the mixing of steel in tundish and inclusion removal.

US 20170173687A1 and WO 2015/110984A1 disclose the use of external electromagnetic stirrers to homogenize the temperature in a tundish.

Due to the increasingly stringent requirements for cleanliness of metals, even small inclusions should be removed from the molten metal in the tundish. It is therefore desired to remove inclusions with higher efficiency, especially also inclusions with small particle diameters.

Also, especially for a tundish with more than 2 strands, temperature homogenization is important, to keep the constant sequential casting of every strand.

SUMMARY

The present inventors carried out diligent research in view of achieving the above objective. In particular, the present inventors investigated the stirring direction of electromagnetic stirring, as well as the configuration of tundish furniture in relation to the electromagnetic stirring, as well as the stirring speed, and other factors, to achieve the present invention as described below.

The inventors realized that it is advantageous to combine EMS stirring with flow separator devices such as dams/weirs/baffles in order to define the region in which stirring takes place, and to control the flow of molten metal in that region during stirring.

The inventors also realized that the flow separator devices may cause a dead zone in the tundish. The dead zone has a low exchange of molten metal flow and a low heat transfer with the surrounding molten metal. Thus, the dead zone can cause temperature inhomogeneities, and can easily lead to clogging of the nozzles. It is also difficult to remove inclusions in the dead zone. The flow separator devices should therefore be arranged in a manner that does not lead to an excessive dead zone.

Thus, according to an aspect of the present invention, a tundish for continuous casting according to claim 1, and a method of stirring a molten metal in a tundish according to claim 11 is provided.

Embodiments of present invention may reduce the volume fraction of inclusions, particularly small inclusions (smaller than 10 μm) and medium size inclusions (between 10 μm and 60 μm), and/or allow stirring a high proportion of the volume of the tundish, to minimize or eliminate dead zones, and/or achieve excellent temperature homogenization, while also reducing slag entrapment at the inlet.

DESCRIPTION OF DRAWINGS

FIG. 1 shows an example of a tundish according to the present invention, and

FIG. 2 shows a comparative tundish.

FIG. 3 is a view from above the example of the tundish according to the present invention.

FIGS. 4a and 4b show a water model used to simulate the example of a tundish according to the present invention. FIG. 4a shows the water model from above, and FIG. 4b shows the water model from the side.

FIGS. 5a and 5b respectively show the measured RTD curves at the outlets of the examples of the comparative and inventive tundish.

FIG. 6 shows the proportions of dead zone volume, mixing flow volume, and plug flow volume of the examples of the comparative and inventive tundish.

FIGS. 7a and 7b respectively show the flow velocity vector plots at the horizontal midplane, of the examples of the comparative and inventive tundish.

FIGS. 8a and 8b respectively show the distribution of volume fraction of inclusions at the vertical cross section across the outlets after 300 seconds, for the examples of the comparative and inventive tundish.

FIG. 9a shows the volume fraction of inclusions inside the tundish, and FIG. 9b shows the volume fraction of inclusions at the outlets of the tundish over time, for the examples of the comparative and inventive tundish.

FIGS. 10a to 10d show the disposition of the flow separator, EMS stirrer(s), EMS stirring direction, and the flow circulation and vortices according to the present invention, for examples of various tundish configurations with 4 outlets.

FIG. 11a shows the influence of EMS on the number density of inclusions up to 10 μm at the outlet of tundish, and FIG. 11b shows the influence of EMS on the number density of inclusions from 10 μm to 60 μm at the outlet of tundish, for the examples of the comparative and inventive tundish.

DETAILED DESCRIPTION

The tundish 1 of the present invention is a tundish used for continuous casting of a molten metal. The molten metal may preferably be molten steel.

The inner volume 2 of a tundish 1 is defined as a volume enclosed by the side walls and bottom wall of the tundish, and optionally a tundish roof. The inner volume 2 is the portion of the tundish 1 which is configured to contain the molten metal. The total volume of the inner volume 2 of the tundish 1 may preferably be 1m³ to 10 m³, more preferably 2 m³ to 8 m³.

The inner volume 2 of the tundish 1 comprises at least an inlet portion 3 comprising an inlet 4 for receiving molten metal, an outlet portion 5 comprising at least one outlet 6 for discharging molten metal, and a flow separator 20.

The inlet portion 3 is a portion of the inner volume 2 of the tundish 1 which includes an inlet 4 which receives molten metal. The molten metal may be supplied to the tundish 1 from a ladle.

The outlet portion 5 is a portion of the inner volume 2 of the tundish 1 which comprises one or more outlets 6 for discharging molten metal. Each outlet 6 may also be referred to as a strand. The outlets 6 may provide the molten metal to a continuous casting mold. The outlets 6 are preferably located at a bottom wall of the tundish.

The flow separator 20 is positioned in the inner volume 2 of the tundish, between the inlet portion 3 and the outlet portion 5. The flow separator 20 may define the inlet portion 3 and the outlet portion 5 by separating them from each other. The flow separator 20 is preferably configured to restrict the stirring of the molten metal by the EMS stirrer 10 in the inlet portion 3. In this way, the flow separator 20 can be arranged to provide flow separation between the inlet portion 3 and the outlet portion 5 within the inner volume 2 of the tundish.

The inlet portion 3 and the outlet portion 5 may still communicate with each other, but the flow separator 20 provides sufficient separation so that a stirring in one of these portions, especially in the outlet portion 5, is not significantly transmitted to the other portion, especially to the inlet portion 3. As a result, one portion can be stirred without significant transfer of the stirring motion to the other portion. In other words, the flow separator 20 provides approximate boundary conditions for the stirring motion within the outlet portion 5.

The flow separator 20 is preferably at least one piece of tundish furniture. Examples of a flow separator 20 are a baffle, a weir, or a dam. For example, in the present invention, the flow separator 20 may comprise a combination of a weir 22 and a dam 21, e.g., with the weir 22 being attached to at an upper portion of a wall in the tundish inner volume 2, and the dam 21 being attached to a lower portion of a wall in the tundish inner volume 2. In this case, there may be a gap between the weir and the dam, so that molten metal in the inlet portion 3 is in communication with the molten metal in the outlet portion 5. As another example, the flow separator 20 may comprise a baffle, e.g, attached to the top and bottom portion of the walls in the inner volume 2 of the tundish.

The influence of the EMS stirring may cause turbulence at the inlet portion 3. Such turbulence can lead to slag entrapment, and reduce the cleanliness of the steel. Positioning the flow separator 20 between the inlet portion 3 and the outlet portion 5 reduces turbulence of the flow at the inlet portion 3 due to the EMS stirring, which can reduce slag entrapment and inclusions.

In the present invention, the flow separator 20 is preferably a combination of a weir and a dam. The weir and the dam are preferably configured to prevent the EMS stirring turbulence at the inlet portion 3 due to the EMS stirring.

Moreover, the flow separator 20 of the present invention is preferably a non-electromagnetic flow separator 20. This means that the flow separator 20 itself is not equipped to carry out electromagnetic braking, or electromagnetic stirring.

A non-electromagnetic flow separator is simple and inexpensive, requires less maintenance, and takes up less of the tundish inner volume 2, compared to an electromagnetic flow separator which is equipped to carry out electromagnetic stirring or braking.

An EMS stirrer 10 is an electromagnetic stirrer. An electromagnetic stirrer stirs the molten metal in the tundish 1 by means of interaction between an induction coil and the electrically conductive molten metal in the tundish.

The EMS stirrer 10 is disposed outside of the tundish. Positioning the EMS stirrer 10 outside of the tundish 1 (i.e., outside of the tundish volume for the molten metal) has the advantage that it does not occupy a part of the inner volume 2 of the tundish 1, and allows ready access for maintenance.

The EMS stirrer 10 is disposed at a vertical position below the top of the inner volume 2 of the tundish, and above the bottom of the inner volume 2 of the tundish 1. The position of the EMS stirrer 10 is defined as the position of a center of the induction coil of the EMS stirrer 10. In other words, the center of the induction coil is preferably below the top of the inner volume 2 of the tundish, and above the bottom of the inner volume 2 of the tundish 1. More preferably, the EMS stirrer 10 is disposed at a vertical position below the level of the molten metal in the tundish 1 during operation of the tundish 1, and above the bottom of the inner volume 2 of the tundish. Positioning the EMS stirrer 10 in this way has the effect of maximizing the stirring efficiency.

The EMS stirrer 10 is disposed so as to cause a flow of the molten metal in a horizontal direction. Herein, a flow of the molten metal in a horizontal direction means that the flow directly caused by the EMS stirrer (e.g., the momentum imparted by the EMS stirrer without considering pre-existing flow, e.g., from inlet to outlet) is primarily horizontal. The vertical component of the flow is preferably as small as possible. In the present invention, “horizontal direction” means a direction which preferably differs by no more than ±45°, more preferably within ±30°, and more preferably ±15°, from horizontal. Horizontal is defined as being perpendicular to the direction of gravity.

The flow directly caused by the EMS stirrer is defined as the flow of the molten metal closest to the EMS stirrer (subject to the largest EM field exerted by the EMS stirrer), and caused by the electromagnetic force of the stirrer acting on the molten metal.

In the present invention, in order to achieve a flow of the molten metal in a horizontal direction, the center axis of the coil of the EMS stirrer is preferably as close to horizontal as possible, and preferably differs by no more than ±45°, more preferably within +35°, and more preferably ±15°, from horizontal.

Making the molten metal flow in a horizontal direction has the advantage of maximizing stirring of the outlet portion 5, while reducing the turbulence at the surface of the molten metal, which reduces entrapment of impurity particles, and allows for improved separation of impurity particles, particularly impurity particles with a particle diameter of less than 100 μm, and more particularly impurity particles with a diameter of less than 50 μm.

The EMS stirrer 10 is disposed so that the flow of molten metal which is directly induced by the EMS stirrer 10 flows away from the inlet 4. In other words, the electromagnetic force of the EMS stirrer 10 acting on the molten metal which is closest to the EMS stirrer 10 makes the molten metal closest to the EMS stirrer 10 flow in a direction away from the inlet 4. This can be achieved by suitably choosing the location of the EMS stirrer 10, and suitably controlling the supply of current to the EMS stirrer 10.

For example, as shown in each of FIGS. 10a to 10d, the molten metal is caused to circulate in the tundish 1 by one or two EMS stirrers 10. The portion of the flow of molten metal represented by the arrows which are closest to the EMS stirrer(s) 10 represents the flow which is directly induced by the EMS stirrer 10, and this flow flows away from the inlet 4 of the tundish. If more than one EMS stirrer 10 is present, each EMS stirrer 10 is disposed so as to make the molten metal in the outlet portion 5 flow in a horizontal direction, away from the inlet 4.

Preferably, the stirring causes no more than two vortices (as illustrated in FIGS. 10a-c), preferably no more than one vortex (as illustrated in FIG. 10d), of molten metal in the tundish. In the present invention, a flow which circulates in one circuit about the outlet portion 5 is defined as having one vortex. Such a flow is generally caused by a single EMS stirrer 10. Such a flow is illustrated in FIG. 10d. In contrast, a flow which flows in two circuits about the outlet portion 5 is defined as having two vortices. Such a flow is generally caused by two EMS stirrers 10. Such a flow is illustrated in FIGS. 10a, 10b, and 10c. A flow of no more than two vortices can be advantageous because of the reduced risk of dead zones and turbulence.

Preferably, the EMS stirrer 10 is disposed so as to stir the entire volume of the molten metal in the outlet portion 5. By disposing the EMS stirrer 10 in this way, it is possible to prevent dead zones in the flow of the molten metal, which increases the temperature homogeneity of the molten metal in the tundish. Preferably, the dead zone volume of the tundish 1 is no greater than 10% of the total volume of molten metal in the outlet portion 5, more preferably no greater than 5%, more preferably no greater than 3%, and more preferably no greater than 2%.

The EMS stirrer 10 is preferably disposed along a long wall of the tundish. This can achieve stirring of the entire volume of the molten metal, and reduce the dead zone volume of the tundish. A long wall is defined as one of the two longest walls of the tundish. Examples of configurations where the EMS stirrer is disposed along a long wall of the tundish are shown in FIGS. 1, 3, and 10a to 10d.

A tundish 1 generally has a back side 8, which may also be referred to as the ladle turret side, and an operator side 7 which is opposite the back side 8. The two longest walls of the tundish are preferably at the operator side 7, and back side 8. Preferably, the EMS stirrer 10 is mounted on the back side 8 of the tundish 1, or on the operator side 7 of the tundish 1. Mounting the EMS stirrer 10 on the back side 8 or the operator side 7 of the tundish 1 can provide stirring of the entire volume of the molten metal.

Preferably, the stirring direction and stirring strength of each EMS stirrer 10 is adjustable.

Preferably, a maximum surface speed of the molten metal in the outlet portion 5 is no more than 0.5 m/sec. Higher values of the maximum surface speed may result in increased entrapment of slag, which reduces the cleanliness of the molten metal. The maximum surface speed of the molten metal in the outlet portion 5 is more preferably less than 0.5 m/sec, more preferably 0.4 m/sec or less, and more preferably 0.3 m/sec or less.

The maximum surface speed can be appropriately set by adjusting the position and stirring strength of each EMS stirrer 10. The maximum surface speed can also be computed by CFD.

Preferably, the volume average speed of the molten metal in the outlet portion 5 is no less than 0.05 m/sec. If the volume average speed of the molten metal in the outlet portion 5 is less than 0.05 m/sec, the temperature homogenization may become insufficient, or a dead zone may develop. The volume average speed of the molten metal in the outlet portion 5 is more preferably greater than 0.05 m/sec, more preferably 0.06 m/sec or more, more preferably 0.7 m/sec or more. The volume average speed is estimated by CFD simulation as below:

$\overline{V}=\frac{{\int }_0^{\Omega }\mathrm{abs}\left(V\right)d\Omega }{\Omega },$

where V is the speed in the melt, m/sec, Ω is the volume of the outlet portion, in m³, V is the volume average speed, in m/sec.

The volume average speed can be appropriately set by adjusting the position and stirring strength of each EMS stirrer 10.

The specific stirring energy is preferably no less than 8.0 w/ton. If the specific stirring energy is less than 8.0 w/ton, the temperature homogenization may become insufficient. The specific stirring energy is more preferably more than 8.0 w/ton, more preferably 9.0 w/ton or more, and more preferably 10.0 w/ton or more.

The present invention also encompasses a method of stirring a molten metal in a tundish 1. In the method of the present invention, the molten metal in the outlet portion 5 is stirred to flow in a horizontal direction, and so that the flow which is directly induced by the EMS stirrer 10 flows in a direction away from the inlet

EXAMPLES

Water Modeling

FIG. 1 shows a tundish 1 according to the present invention, including the tundish 1, the tundish inner volume 2, comprising the inlet portion 3, the outlet portion 5, and the flow separator 20. The EMS stirrer 10 is disposed on an outer wall of the tundish 1, as shown in FIG. 3. The inlet portion 3 includes the inlet 4, and the outlet portion 5 includes the outlets 6. For the water modeling, a tundish 1 according to the present invention, as shown in FIG. 1 was studied, with a maximum throughput of the tundish of 1.9 ton/min, a normal working capacity of 40 ton, a bath depth of 850 mm, a ladle size of 110 ton, and four outlets 6. The flow separator 20 comprises a dam 21 and a weir 22. The flow separator 20 divides the inner volume 2 into the inlet portion 3 and the outlet portion 5.

FIG. 2 shows a comparative tundish, having an inlet portion 3 and an outlet portion 5 separated by a baffle 30. This comparative tundish had the same shape and size as the inventive tundish, however, the comparative tundish lacked an EMS stirrer, and instead of the flow separator 20 of the inventive tundish, the comparative tundish is provided with a baffle 30 with three holes, as shown in FIG. 2.

The above inventive and comparative tundishes were studied by water modelling. For the inventive tundish 1, three water pumps 12 were used to simulate the electromagnetic stirring, as shown in FIGS. 4a and 4b. FIG. 4a shows the water model of the inventive tundish 1 from above, and FIG. 4b shows a side view of the water model of the inventive tundish 1, seen through the operator side 8. The stirring direction of the water pumps could be adjusted towards the tundish inlet 4, or away from the inlet 4 as shown by the arrows in FIG. 4a.

A tracer color was added to the inlets 4 of both tundishes to visualize the mixing and homogenizing phenomena of different configurations. For the comparative tundish with a baffle wall 30 and without EMS stirring, about 409 seconds were required to achieve complete mixing in the tundish. However, for the tundish 1 of the present invention with EMS stirring, complete mixing was achieved in about 236 seconds. Complete mixing was determined by color homogenization at the outlet portion.

These RTD (residence time distribution) results are shown in FIG. 5a for the comparative tundish, and FIG. 5b for the inventive tundish 1. In FIGS. 5a and 5b, the vertical axis shows dimensionless concentration, and the horizontal axis shows dimensionless time. These figures show the measured residence time distribution (RTD) curves at each of the strands 1 to 4. The strands 1 to 4 respectively correspond to each of the outlets 6 shown in FIG. 4b, and are numbered so that strand 1 is located furthest from the inlet 4, and strand 4 is closest to the inlet 4. As can be seen by comparing FIGS. 5a and 5b, in the inventive tundish 1, strand similarity, namely, the homogeneity of the simulated molten metal among strands 1 to 4, was improved over the comparative tundish, and the RTD overall curve was significantly closer to an ideal mixing curve.

FIG. 6 shows a comparison of the dead zone volume, mixing flow volume, and plug flow volume of the inventive tundish 1 and the comparative tundish. The mixing flow volume, plug flow volume and dead zone volume were calculated from the RTD curves. In the comparative tundish, a relatively large proportion of plug flow volume and dead zone volume were found, which are significant disadvantages. In contrast, in the inventive tundish 1, the plug flow volume and dead zone volume are almost entirely eliminated as shown in FIG. 6.

The improved mixing and the smaller dead zone indicate that the temperature homogeneity of the inventive tundish 1 is significantly improved over the comparative tundish. Furthermore, from the reduced plug flow volume of the inventive tundish, a longer residence time, which leads to a reduction in inclusions, can be expected.

From this water modeling, it was also found that it is advantageous to set the stirrers 12 (which model the EMS stirrer) so that the flow which is directly induced by the stirrers flows away from the inlet 4, because this reduces turbulence at the inlet portion 3, which leads to a reduction in slag entrapment

CFD Modeling

The above examples of the inventive tundish 1 and comparative tundish were also studied by CFD (computational fluid dynamics), to investigate the flow characteristics such as flow velocity and stirring energy. FIG. 7a shows results for the comparative example, and FIG. 7b shows results for the inventive example. FIGS. 7a and 7b show the flow velocity vector plots at the horizontal midplane of tundish. In order to quantify the flow characteristics, the whole tundish volume was divided into the inlet portion 3 and the outlet portion 5. From FIGS. 7a and 7b, it can be seen that, with EMS stirring, a macro rotating flow is formed in the outlet portion 5. This rotating flow homogenizes the temperature among the outlets 6, and also transforms the whole outlet portion 5 into a mixing volume. It was thus confirmed that the entire volume of the molten metal in the outlet portion 5 of the tundish 1 can be stirred.

The specific stirring energy is defined as follows:

$\begin{array}{cc}\dot{\epsilon }=\frac{{\int }_0^{\Omega }\epsilon d\Omega }{{\int }_0^{\Omega }d\Omega }·g·{10}^3& \mathrm{Equation}1\end{array}$

Where ε is the specific stirring energy, w/ton, ε is the dissipation rate of the turbulent kinetic energy, m²/s³, g is the gravitational acceleration, m/s². The simulation was performed using ANSYS Fluent.

Table 1 lists the flow speed quantification for the inventive tundish 1 and the comparative tundish. For the comparative tundish, the volume averaged speed and specific stirring energy is very low. This is unfavorable for inclusion collision and coalescence. For the inventive tundish 1, both the stirring speed and specific stirring energy are increased, and the inclusion collision and coalescence will be accelerated (as explained below). However, the maximum surface speed of the inventive tundish 1 was low, and close to that of the comparative example. A low surface speed can reduce or prevent slag entrapment.

	TABLE 1
		Volume	Max	Specific
		averaged	surface	stirring
		speed	speed in the	energy in the
		in the outlet	outlet zone	outlet zone
		zone (m/sec)	(m/sec)	(w/ton)
	Comparative	0.024	0.35	0.83
	tundish
	Inventive	0.11	0.38	15.3
	tundish

Inclusion Modeling

Mathematical modeling was also carried out to predict transient concentration and size distribution of inclusions, and the removal of inclusions at the slag layer was also modeled by considering the relationship between collision time and rupture time. The simulations of collisions, coalescence and growth of inclusions were carried out via Population Balance Model in Ansys Fluent. The coalescence rate was determined by the sum of Brownian, Stokes and turbulence collisions. To reduce the computation time, only Al₂O₃ inclusions were considered.

The inclusions were divided into 16 classes in diameter between 1 μm and 97 μm, and the initial volume fraction in the inlet portion 3 and tundish 1 was set as 10 ppm. A detailed description of the model is described in H. Ling, “Mathematical modeling on the growth and removal of non-metallic inclusions in the molten steel in a two-strand continuous casting tundish,” Metallurgical and Materials Transactions B, vol. 47B, pp. 2991-3016, October 2016. The simulated process time was 300 seconds.

FIG. 8a shows the result for the comparative tundish without EMS, and FIG. 8b shows the result for the inventive tundish 1. FIGS. 8a and 8b show the distribution of volume fraction of inclusion at the vertical cross section across the outlets 6 after 300 seconds simulation time. It can be seen that, for the inventive tundish 1, the volume fraction of inclusions is homogeneously distributed in the whole outlet portion 5 and reduced to a lower level than the comparative tundish.

FIG. 9a shows the volume fraction of inclusions inside the tundish, and FIG. 9b shows the volume fraction of inclusions at the outlets of the tundish over time. FIGS. 9a and 9b show that the volume fraction of inclusions both inside the tundish 1 and at the outlets 6 decreases at a faster rate for the inventive tundish.

FIGS. 11a and 11b show the influence of EMS stirring on the number density of inclusions with different sizes, at the outlet of tundish. FIG. 11a shows that small inclusions (diameters smaller than 10 μm) are reduced for the inventive tundish. FIG. 11b shows that medium size inclusions (diameters between 10 μm and 60 μm) are also reduced for the inventive tundish. However, the number density of large inclusions (larger than 60 μm) were small for both the inventive and comparative tundishes, and were considered negligible.

Configuration of Refractory Furniture and Stirring Direction

The electromagnetic stirring can circulate the molten metal throughout the whole tundish 1. However, it is not wished to have a strong turbulence in the inlet portion 3, because strong turbulence in the inlet portion 3 may cause slag entrapment. It is therefore necessary to add a flow separator 20 around the inlet portion 3 to reduce the influence of stirring momentum on the inlet portion 3.

FIGS. 10a to 10d show possible arrangements of the flow separator 20 and the EMS stirring direction by the EMS stirrer 10 in tundishes according to the present invention. The arrows in the EMS stirrers 10 represent the stirring direction of the EMS stirring, and the arrows in the outlet portion 5 represent the flow of molten metal. From the above studies, it was found that that a flow separator 20 should be positioned in the inner volume 2 of the tundish 1, between the inlet portion 3 and the outlet portion 5, and that the stirring direction of EMS should be away from the inlet 4, so that the electromagnetic stirring shall has a minimum effect on the turbulence level inside the inlet portion 3.

Based on the above, a tundish 1 and method of stirring according to the present invention can provide improved temperature homogeneity within the tundish 1, while also reducing the concentration of inclusions, particularly inclusions with a particle diameter smaller than 50 μm, in a tundish 1 for continuous casting.

Claims

1. A tundish for continuous casting, the tundish comprising an inner volume having an inlet portion for receiving molten metal, having an outlet portion having at least one outlet for discharging molten metal, and a flow separator, the tundish further including an EMS stirrer for electromagnetic stirring, wherein,the flow separator is positioned between the inlet portion and the outlet portion,the EMS stirrer is disposed outside of the tundish, at a vertical position below the top of the inner volume of the tundish and above the bottom of the inner volume of the tundish,the EMS stirrer is disposed to make the molten metal in the outlet portion flow in a horizontal direction, and the flow which is directly induced by the EMS stirrer flows away from the inlet.

2. The tundish according to claim 1, wherein the stirring causes no more than two vortices of molten metal in the tundish.

3. The tundish according to claim ,1, wherein the EMS stirrer is disposed to stir the entire volume of the molten metal in the outlet portion.

4. The tundish according to claim 1, wherein the tundish has an operator side, and a back side which is opposite to the operator side, and the stirrer is mounted on the back side of the tundish, or on the operator side of the tundish.

5. The tundish according to claim 1, wherein the stirring direction of each stirrer is adjustable.

6. The tundish according to claim 1, wherein the stirring strength of each stirrer is adjustable.

7. The tundish according to claim 1, wherein the flow separator is at least one of a baffle, a weir, and a dam.

8. The tundish according to claim 1, wherein the flow separator is configured to restrict the stirring of the molten metal by the EMS stirrer in the inlet portion.

9. The tundish according claim 1, wherein a maximum surface speed of the molten metal in the outlet portion is no more than 0.50 m/sec, and/or the volume average speed of molten metal in the outlet portion is no less than 0.05 m/sec, and/or the specific stirring energy is no less than 8.0 w/ton.

10. A method of stirring a molten metal in a tundish having a tundish body provided with an inlet portion having an inlet for molten metal, an outlet portion having at least one outlet, a flow separator, and an EMS stirrer for electromagnetic stirring, wherein,the flow separator is positioned between the inlet portion and the outlet portionthe EMS stirrer is disposed horizontally, outside of the tundish,the method comprising stirring the molten metal in the outlet portion to flow in a horizontal direction, and so that the flow which is directly induced by the EMS stirrer flows away from the inlet.

11. The method of stirring a molten metal in a tundish according to claim 10, wherein the stirring causes no more than two vortices of molted metal in the tundish.

12. The method of stirring a molten metal in a tundish according to claim 10, wherein the molten metal is stirred in an essentially horizontal direction, with essentially no vertical component.

13. The method of stirring a molten metal in a tundish according to claim 10, wherein the strength and direction of stirring by the EMS stirrer stirs are adjusted so that a maximum surface speed of the molten metal in the outlet portion is no more than 0.50 m/sec, and/or the volume average speed of molten metal in the outlet portion is no less than 0.05 m/sec, and/or the specific stirring energy is no less than 8.0 w/ton.

14. A Use of an EMS stirrer for electromagnetic stirring of a molten metal in a tundish for continuous casting, the tundish having an inner volume comprising: an inlet portion having an inlet for receiving molten metal, an outlet portion including at least one outlet for discharging molten metal, and a flow separator, the flow separator being positioned between the inlet portion and the outlet portion, whereinthe EMS stirrer is disposed outside of the tundish, at a vertical position below the top of the inner volume of the tundish and above the bottom of the inner volume of the tundish,the EMS stirrer is disposed to make the molten metal in the outlet portion flow in a horizontal direction, andthe flow which is directly induced by the EMS stirrer flows away from the inlet.

15. The tundish according to any claim 2, wherein the EMS stirrer is disposed to stir the entire volume of the molten metal in the outlet portion.

16. The tundish according to claim 2, wherein the tundish has an operator side, and a back side which is opposite to the operator side, and the stirrer is mounted on the back side of the tundish, or on the operator side of the tundish.

17. The tundish according to claim 2, wherein the stirring direction of each stirrer is adjustable.

18. The tundish according to claim 2, wherein the stirring strength of each stirrer is adjustable.

19. The tundish according to claim 2, wherein the flow separator is at least one of a baffle, a weir, and a dam.

20. The tundish according to claim 2, wherein the flow separator is configured to restrict the stirring of the molten metal by the EMS stirrer in the inlet portion.