Patent Application
20220062984
The present invention relates to a stopper for continuous casting with a gas blowing function, the stopper controlling a flow rate of molten steel by being fitted from above to a nozzle placed in a bottom of a tundish mainly in discharging molten steel from the tundish into a mold in continuous casting of motel steel, and a continuous casting method using the stopper.
Some stoppers controlling a flow rate of molten steel in discharging molten steel from a tundish into a mold in continuous casting of molten steel have a gas blowing function for the purpose of floating inclusions in molten steel or preventing deposition of inclusions on a nozzle inner wall or the like.
For example, Patent Literature 1 discloses a pouring apparatus including a gas discharge port (gas jetting port) from which gas guided through a stopper is discharged (jetted) and is passed from an inlet to a lower outlet of a nozzle hole in a pouring vessel bottom, thereby discharging molten metal remaining in the nozzle hole downwardly from the nozzle hole, the pouring apparatus being in a state where, to prevent molten metal from flowing into the gas discharge port, gas pressure is applied to the gas discharge port during pouring.
Patent Literature 1: Japanese Patent Application Laid-open No. 2013-043199
Typically, a gas discharge amount from the stopper (hereinafter simply referred to as “gas discharge amount”) needs to be changed according to individual operating conditions such as casting speed, i.e., molten steel discharge speed and steel type. Thus, it is necessary to design the size of a through hole for discharging gas and the number of through holes so as to obtain a gas discharge amount required when the changing operating conditions are maximum.
Meanwhile, since the gas discharge amount greatly influences the quality of steel, it is necessary to appropriately control the discharge amount (flow rate) in response to the condition change during casting.
Suppose that the gas discharge amount is controlled to a certain amount or below, especially to a small amount. In this case, as indicated in Patent Literature 1, even if the gas discharge port is to be maintained in a gas pressure (backpressure) applied state, the gas pressure, i.e., backpressure, around a gas discharge portion is reduced since the gas pressure is typically controlled only by an apparatus in a gas supply source located apart from the gas discharge port of the stopper serving as the gas discharge portion. Thus, it is usually difficult to grasp or control the backpressure around the gas discharge portion.
An object of the present invention is to improve the precision of grasping or controlling backpressure around a gas discharge portion in a stopper for continuous casting.
The present invention provides a stopper for continuous casting according to the following items 1 to 4, and a continuous casting method according to the following item 5.
1. A stopper for continuous casting including
2. The stopper for continuous casting according to the above item 1, in which
3. The stopper for continuous casting according to the above item 1 or 2, in which
(−0.44×Hd2+1.88Hd−0.08)≤Ha≤{1.67×ln(Hd)+3.66} Equation 1
Hn=Ha÷(Hd2×π÷4) Equation 2, where
4. The stopper for continuous casting according to the above item 3, in which
5. A continuous casting method using the stopper for continuous casting according to any one of the above items 1 to 4, the method comprising
2×10−2 (MPa) and 8×10−2 (MPa) both inclusive.
The present invention will be described in detail below.
For a structure in which a gas discharge hole is placed at an end of a cavity as a gas flow path within a stopper, gas backpressure tends to vary greatly and become unstable during an operation of discharging gas from around a distal end of the stopper. The stopper is immersed in molten steel, and is located close to a nozzle hole for discharging molten steel at its distal end. The stopper also controls a flow rate of molten steel. Thus, molten steel flow velocity varies greatly. This causes a flow rate and pressure of gas discharged from around the stopper distal end to vary greatly as well, making it difficult to control them accurately and precisely.
In the present invention, a component that cuts off continuity of the cavity within the stopper to divide the cavity into two upstream and downstream spaces and control pressure (the pressure control component) is placed around a stopper end of the cavity.
The pressure control component controls gas pressure in the upstream space (cavity) without directly transmitting pressure variation from the stopper distal end to the upstream side.
The pressure control component is placed in a part of the reduced-diameter region around the stopper distal end, the part being above the gas discharge hole within the cavity.
The inventors have discovered that when the control component includes a porous refractory the substantially entire of which has gas permeability, the gas permeability within the porous refractory is gradually reduced with the lapse of casting time, and passage or discharge of gas stops in many cases. This is not caused by a single reason, and its mechanism has not necessarily become clear.
However, the inventors have discovered that the phenomenon of stopping passage or discharge of gas in the porous refractory can be resolved by forming the pressure control component with the dense refractory and including the through hole, through which the gas can pass, within the pressure control component or between the outer periphery of the pressure control component and the stopper body.
To accurately and precisely control the pressure or flow rate of gas, the gas pressure in a zone in which the gas pressure is to be adjusted is preferably high.
For the stopper body, a so-called monoblock stopper (hereinafter referred to as “MBS”) obtained by integrally forming a refractory such as an alumina inorganic material-graphite is typically used. The inventors have discovered that gas permeates or dissipates into a side wall portion of a body of such a MBS when the gas pressure in the cavity is increased to roughly 1×10−1 (MPa) or more.
The inventors have further discovered that it is preferable to discharge gas into molten steel from the gas discharge hole of the stopper by setting the gas pressure in the cavity on the upstream side of the pressure control component to a value between 2×10−2 (MPa) and 8×10−2 (MPa) both inclusive in consideration of the case using such a MBS.
The value 8×10−2 (MPa) as the upper limit of the preferable range is a value including a so-called safety factor such as variation in the shape or the material of each MBS in a pressure of roughly less than 1×10−1 (MPa) for preventing gas permeation or dissipation from the side wall portion of the MBS body.
When the gas pressure is less than 2×10−2 (MPa), the accuracy and precision of pressure control may be reduced.
The dense refractory in the present invention means a refractory having such a property as not to allow gas permeation when a sample of the refractory having a length of 20 mm (a width and an area are not considered) is pressurized at 8×10−2 MPa in a method of measuring a refractory sample in a laboratory.
The pressurization at 8×10−2 MPa in this test is obtained by selecting the same pressurizing force as the upper limit value 8×10−2 MPa of the gas pressure during operation with the above-described MBS. The length is a practical axial length of the pressure control component, and is obtained by selecting a shortest (thinnest) length in consideration of its strength and placing stability.
If the length is greater than 20 mm, the gas permeability is reduced. Thus, if no gas permeates under this condition, a pressure control component greater than this length allows no gas to permeate during operation with the MBS.
The inventors have discovered by simulation that the diameter of the through hole and the number thereof in relation to the pressure control component required for such pressure control are preferably specified as described in the above item 3. The simulation was performed using ordinary fluid analysis software or the like.
In summary, this is a specific condition for determining the number of through holes required for setting the gas pressure in the cavity on the upstream side of the pressure control component to a range between 8×10−2 (MPa) and 2×10−2 (MPa) both inclusive with respect to any/specific through hole within a range between φ0.2 mm and φ2.0 mm both inclusive. The required number of through holes is obtained by dividing the total cross-sectional area of the through hole(s) obtained by the Equation 1 by the cross-sectional area of the through hole.
The through hole, which preferably has a circular shape, is not necessarily limited to the circular shape. A so-called single hole shape having relatively similar lengths in all directions radially such as an elliptical or another shape having a curved surface (non-perfect circle) and a polygonal shape, or a slit shape (slit) may be employed.
To apply the present invention, the size (diameter) of the single hole shape other than the circle may be determined by converting the hole into a circle based on the cross-sectional area of the hole.
The thickness and the length of the slit may be determined by the conversion method described in the above item 4.
Conventional techniques including no pressure control component have the following problems.
The stopper of the present invention can solve these problems by including therein the pressure control component.
That is, the present invention makes it possible to grasp the gas backpressure in a portion near the gas discharge hole around the stopper distal end. This enables more precise grasping and management/control of a state of gas discharged into molten steel. Distribution or the like of gas in molten steel can be thereby controlled more precisely. Consequently, the quality of steel can be stabilized or improved.
If the pressure control component is placed in an upper region other than the reduced-diameter region, molten steel may enter and clog the gas discharge hole especially when a gas discharge amount from the gas discharge hole placed around the stopper distal end is small.
In comparison, in the present invention, the pressure control component is provided in a part of the reduced-diameter region having a reduced refractory thickness from the stopper outer periphery to the inner cavity. Thus, the temperature of the pressure control component can be increased, and the temperature of gas passing through the pressure control component can be quickly increased. The gas pressure around the gas discharge hole can also be increased. This configuration can prevent molten steel entering the gas discharge hole, if any, from easily solidifying. Consequently, the possibility to clog the gas discharge hole can be reduced.
Moreover, for the phenomenon of stopping passage or discharge of gas due to a decrease in gas permeability in the porous refractory when the pressure control component includes the porous refractory the substantially entire of which has gas permeability as described above, the configuration can prevent a gas amount passing through the pressure control component and a gas discharge amount from the stopper distal end from being decreased or stopped.
Embodiments of the present invention will be described together with examples (water model experiment examples).
The stopper 10 includes a gas discharge hole 4 passing through from the cavity 2 to the outside in a distal center of a reduced-diameter region including a fitted portion 3 to the lower nozzle 20. The stopper 10 further includes a pressure control component 5 in a part of the reduced-diameter region above the gas discharge hole 4 within the cavity 2.
The gas discharge hole 4 may be also provided in a side surface of the reduced-diameter region, and may be provided at a plurality of positions as illustrated in
As described above, the stopper of the present invention includes the pressure control component in a part of an area above the gas discharge hole, preferably in an area immediately above the gas discharge hole. This is because it is preferable to grasp and control pressure at a position as close as possible to the discharge hole in order to more accurately and precisely grasp and control a state of gas discharged from around a distal end of the stopper. The position as close as possible to the discharge hole is an area roughly below a diameter reduction starting position of the stopper distal end. To be more specific, the area is roughly within 150 mm from the distal end of the stopper body.
The gas discharge hole in the stopper of the present invention is a distal opening of the cavity for conveying gas. The discharge hole may be located at one position in the distal center of the reduced-diameter region or at a plurality of positions around the fitted portion (side surface). It should be noted that a total opening area of the gas discharge hole is preferably about 3.1 mm2 (equivalent to an opening area of a hole having a diameter of 2 mm) or less.
While the pressure control component may have any one of a porous body (porous refractory) form or a through hole form, the pressure control component preferably controls a flow rate of gas under higher pressure. The gas permeability characteristics of the pressure control component and the gas discharge hole defined in the above Equation 1 are individually measured in a laboratory.
Additionally, a decrease in gas amount, clogging or the like may occur when the pressure control component is a porous body (porous refractory). In this case, it is preferable to use a dense refractory for the pressure control component as described above and form a through hole within the pressure control component or between the outer periphery of the pressure control component and the stopper body so as to satisfy conditions in the equations or the like in the above item 3.
In the present invention, the through hole may have various shapes as in the examples of the through hole illustrated in
The through hole(s) may be located so as to fall under a range of an approximate curve representing a relation between a diameter and a total cross-sectional area of a circular through hole at a pressure of 2×10−2 (MPa) and 8×10−2 (MPa) (pressure of the cavity on an upstream side of the pressure control component) as illustrated in
The through hole may have a single hole shape such as the above circular shape, an elliptical or another shape having a curved surface (non-perfect circle), and a polygonal shape, or may have a slit shape.
The result shows that the circular shape and the slit shapes have little pressure difference. That is, for the slit-shaped through hole, the shape and number thereof may be determined using the conversion method described in the above item 4.
When the gas discharge hole is located at one position in the distal center of the reduced-diameter region of the stopper, the gas discharge hole is preferably disposed at a position within ±10 mm in a radial direction of the stopper from the vertical center axis of the stopper. This is because disposing the gas discharge hole at the above position makes it hard for the discharged gas flow to receive the effect of a molten steel flow flowing along the outer periphery of the stopper distal end (so-called head portion), and bubbles to hardly join together, thereby preventing generation of coarse bubbles. As a result, nozzle clogging can be efficiently prevented, and inclusion floatation in the mold can be efficiently promoted.
When the gas discharge hole is located at a plurality of positions around the distal end of the reduced-diameter region of the stopper, the gas discharge hole is preferably disposed at positions away from the vertical center axis of the stopper by 10 mm or more in the radial direction of the stopper up to the fitted portion (contact point with the lower nozzle). This is because disposing the gas discharge hole at the above positions allows the discharged gas flow to be dispersed, and makes it difficult for bubbles to join together, thereby preventing generation of coarse bubbles. As a result, nozzle clogging can be efficiently prevented, and inclusion floatation in the mold can be efficiently promoted. Discharging gas below the fitted portion (contact point with the lower nozzle) makes it possible to certainly blow the gas into an inner hole of the lower nozzle.
When the gas discharge hole is located at one position of the distal center or at a plurality of positions of the side surface of the reduced-diameter region of the stopper, experiment shows that the distal opening (discharge port) of the gas discharge hole preferably has a diameter of 2 mm or less. This is because the flow rate can be controlled more precisely, and there is a higher ratio of bubbles having a small diameter (roughly less than 3 mm), which allow inclusions in molten steel to easily float up and make it difficult to produce steel defects.
10 STOPPER
1 STOPPER BODY
2 CAVITY
3 FITTED PORTION
4 GAS DISCHARGE HOLE
5 PRESSURE CONTROL COMPONENT
6 THROUGH HOLE
7 JOINT FILLER
20 LOWER NOZZLE
| Number | Date | Country | Kind |
|---|---|---|---|
| 2018-241497 | Dec 2018 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2019/049519 | 12/18/2019 | WO | 00 |
