Submerged nozzle for continuous casting apparatus

Abstract

A submerged nozzle for continuous casting of molten metal, wherein two or more discharge hole flow passages are provided on a cylindrical side surface of a submerged nozzle, and first and second inner surface side walls and first and second outer surface side walls of the discharge hole flow passages in a horizontal cross-section of the submerged nozzle when in use are composed by straight lines formed so as to be inflected at an inner side point of inflection and an outer side point of inflection.

Claims

1. A submerged nozzle for continuous casting of molten metal, wherein two or more discharge hole flow passages are provided on a cylindrical side surface of a submerged nozzle having a nozzle hole, and first and second inner surface side walls and first and second outer surface side walls of the discharge hole flow passages in a horizontal cross-section of the submerged nozzle when in use are composed by straight lines formed so as to be inflected at an inner side point of inflection and an outer side point of inflection, wherein the discharge hole flow passages in the horizontal cross-section of the submerged nozzle when in use are composed by straight lines formed so as to be inflected at the outer side point of inflection and an angle of 15 to 85, wherein the angle is formed between a first center line between the two straight lines, and extension lines thereof, formed by the first inner surface side wall and the first outer surface side wall on the inner side of the submerged nozzle from the inflection section in the discharge hole flow passage, and a second center line between the two straight lines, and extension lines thereof, formed by the second inner surface side wall and the second outer surface side wall on the outer side of the submerged nozzle from the inflection section.

2. The submerged nozzle for continuous casting of molten metal according to claim 1, wherein a further angle , which is formed between a straight line that links first and second intersection points where an outer edge of the nozzle hole intersects with two straight lines formed by the first inner surface side wall and the first outer surface side wall on the inner side of the discharge hole flow passages of the submerged nozzle, and a first center line, which intersects with the straight line and passing through a hole center of the nozzle hole, is 45 to 135.

3. The submerged nozzle for continuous casting of molten metal according to claim 1, wherein, when a thickness of the submerged nozzle is t, a distance from the hole center of the nozzle hole to the inner side point of inflection is a, a distance from the hole center to the outer side point of inflection is represented by b, and ri is the radius of the nozzle hole, then
0.2(ari)/t and (bri)/t0.9 are established.

4. A submerged nozzle for continuous casting of molten metal, wherein two or more discharge hole flow passages are provided on a cylindrical side surface of a submerged nozzle having a nozzle hole, and first and second inner surface side walls and first and second outer surface side walls of the discharge hole flow passages in a horizontal cross-section of the submerged nozzle when in use are composed by straight lines formed so as to be inflected at an inner side point of inflection and an outer side point of inflection, wherein a circular or polygonal bottom hole is provided in a nozzle bottom of the submerged nozzle, and when an opening surface area of the bottom hole is S.sub.b, and a total opening surface area which is the sum of an opening surface area of the discharge hole flow passages and the opening surface area of the bottom hole is S.sub.t, then S.sub.b/S.sub.t is 0 to 0.4 is established.

5. The submerged nozzle for continuous casting of molten metal according to claim 2, wherein, when a thickness of the submerged nozzle is t, a distance from the hole center of the nozzle hole to the inner side point of inflection is a, a distance from the hole center to the outer side point of inflection is represented by b, and ri is the radius of the nozzle hole, then
0.2(ari)/t and (bri)/t0.9 are established.

6. The submerged nozzle for continuous casting of molten metal according to claim 2, wherein a circular or polygonal bottom hole is provided in a nozzle bottom of the submerged nozzle, and when an opening surface area of the bottom hole is S.sub.b, and a total opening surface area which is the sum of an opening surface area of the discharge hole flow passages and the opening surface area of the bottom hole is S.sub.t, then S.sub.b/S.sub.t is 0 to 0.4 is established.

7. The submerged nozzle for continuous casting of molten metal according to claim 3, wherein a circular or polygonal bottom hole is provided in a nozzle bottom of the submerged nozzle, and when an opening surface area of the bottom hole is S.sub.b, and a total opening surface area which is the sum of an opening surface area of the discharge hole flow passages and the opening surface area of the bottom hole is S.sub.t, then S.sub.b/S.sub.t is 0 to 0.4 is established.

8. The submerged nozzle for continuous casting of molten metal according to claim 1, wherein the angle is 25 to 75.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is a cross-sectional schematic drawing showing a nozzle hole and discharge holes of a submerged nozzle for continuous casting of molten metal according to the present invention;

(2) FIG. 2 is a cross-sectional schematic drawing showing only a cross-section of the nozzle hole and the discharge holes in FIG. 1;

(3) FIG. 3 is an enlarged schematic drawing of a discharge hole in FIG. 1;

(4) FIG. 4 is a schematic drawing showing a composition of a pair of discharge holes according to a further mode of FIG. 1;

(5) FIG. 5 is a schematic drawing showing a composition of a pair of discharge holes according to a further mode of FIG. 1;

(6) FIG. 6 is a schematic drawing showing a composition of a pair of discharge holes according to a further mode of FIG. 1;

(7) FIG. 7 is a schematic drawing showing discharge flow rate measurement positions in the discharge holes in FIG. 1, as viewed from the outer side of a discharge hole of the submerged nozzle;

(8) FIG. 8 is a horizontal schematic diagram showing discharge flow rate measurement positions in a lateral cross-section at the position of the discharge holes in FIG. 1;

(9) FIG. 9 is a characteristic diagram showing the discharge flow rate measurement results in the case of the discharge hole cross-section shown in FIG. 2 by which a satisfactory rotational flow is obtained;

(10) FIG. 10 is a characteristic diagram showing the discharge flow rate measurement results in the case of the discharge hole cross-section shown in FIG. 12 by which a satisfactory rotational flow is not obtained;

(11) FIG. 11 is a schematic drawing showing a conventional shape where discharge hole flow passages are provided in a tangential direction to the nozzle hole (Patent Documents 1 to 4);

(12) FIG. 12 is a schematic drawing showing a conventional shape where discharge hole flow passages are provided in a tangential direction to the nozzle hole (Patent Documents 1 and 3);

(13) FIG. 13 is a schematic drawing showing a comparative example in which only the inner side of the discharge hole flow passage is inflected;

(14) FIG. 14 is a schematic drawing showing a comparative example in which only the outer side of the discharge hole flow passage is inflected; and

(15) FIG. 15 is a schematic drawing showing a case where a bottom hole is formed on the bottom of the nozzle, in a further mode of FIG. 1.

BEST MODE FOR CARRYING OUT THE INVENTION

(16) It is an object of the present invention to provide a submerged nozzle for continuous casting of molten metal whereby a stable rotational flow of molten steel is generated inside a mold, thus contributing to improvement in the quality of the cast metal.

Practical Examples

(17) A preferred embodiment of a submerged nozzle for continuous casting of molten metal according to the present invention is described below with reference to the drawings.

(18) Firstly, the process leading up to the development of the submerged nozzle for continuous casting of molten metal according to the present invention will be explained.

(19) In general, in order to obtain a stable rotational flow inside the mold without applying modifications to the manufacturing equipment, not to mention an electromagnetic churning apparatus, there are two important points: that the discharge flow which flows out from the submerged nozzle via the discharge hole (1) should be inclined by a prescribed amount with respect to the radiating direction viewed from the central axis of the submerged nozzle, and (2) should continue in a stable state as described above. Various discharge hole shapes were studied from this perspective, and respective hole shapes were assessed by carrying out water model experiments, leading to the development of the submerged nozzle according to the present invention.

(20) A water model of the submerged nozzle was a water model envisaging a continuous casting apparatus for 200 mm-diameter round billet, wherein the submerged nozzle has an inner diameter of 35 mm, an outer diameter of 75 mm, a material thickness of 20 mm, an output cross-section of the discharge hole of 24 mm22 mm, four discharge holes, and a casting draw rate of 2.0 m/minute.

(21) Firstly, as shown in FIG. 11, investigation was carried out into whether or not a rotational flow is generated by using a shape in which the nozzle hole 1 is provided with discharge hole flow passages 2 in the tangential direction as in Patent Documents 1 to 4, and by using a curved shape which is provided with discharge hole flow passages 2 in the tangential direction of the nozzle hole 1 as indicated in Patent Documents 1 and 3 and shown in FIG. 12, but although a rotational flow was obtained, a stable rotational flow was not achieved and the rotational flow repeatedly appeared and disappeared.

(22) Therefore, various shapes were investigated, and as shown in FIG. 2 it was discovered that when the discharge hole flow passages 2 are bent in a key shape which is inflected in a dog-leg shape at an intermediate point of the discharge hole flow passage 2, a rotational flow having a central axis at the submerged nozzle 3 is formed stably throughout the whole mold.

(23) Moreover, experiments were carried out in which only the inner side of the discharge hole flow passage 2 was inflected as shown in FIG. 13, and in which only the outer side of the discharge hole flow passage 2 was inflected as shown in FIG. 14, but in these cases a satisfactory rotational flow was not achieved.

(24) In order to investigate the reasons why a rotational flow is generated or not generated, depending on the shape of the discharge hole flow passages 2, a propeller flow rate at measurement positions A, B, C and D was investigated to find the flow rate at respective positions in a discharge hole flow passage 2. FIG. 7 and FIG. 8 show schematic drawings indicating the measurement positions. FIG. 7 shows a state where the measurement positions are viewed from the outer side of the discharge hole flow passage 2 of the submerged nozzle 3, and FIG. 8 shows the lateral cross-section of the positions of the discharge hole flow passages 2. The measurement positions A and B are on the inner side of the discharge hole flow passage where a rotational flow is to be generated, and C and D are on the outer side.

(25) FIG. 9 shows the measurement results for the discharge flow rate in the case of the cross-section of the discharge hole flow passage 2 in FIG. 2, by which a sufficient rotational flow is obtained. The horizontal axis represents temporal change and the vertical axis represents the relative value of the average flow rate every 10 seconds, the value being higher towards the upper side and the value being lower towards the lower side. When the flow rate in the up/down direction of the discharge hole flow passage 2 is compared, the flow rate is greater at B and D on the lower side, but this is due to the effects of the downward flow from top to bottom inside the submerged nozzle 3. On the other hand, temporal change in the flow rate is observed, but this is because the flow rate is controlled by a well-known sliding plate directly above the submerged nozzle 3, and therefore a flow with a slight bias is obtained inside the submerged nozzle 3 and the flow rate also varies. When the flow rate values in the same horizontal plane (D and B, C and A) of the discharge hole flow passage 2 are compared, the flow rate is slower on the inner sides B and A of the inflection, compared to the outer sides C and D.

(26) In relation to this, FIG. 10 shows the measurement results for the discharge flow rate in the case of the cross-section of the discharge hole flow passage 2 in FIG. 12, by which a sufficient rotational flow is not obtained. If the flow rate values in the same horizontal plane of the discharge hole flow passage 2 (D and B, C and A) are compared, there is virtually no difference between the flow rates D and C on the outer side of the discharge hole flow passage 2 and the flow rates B and A on the inner side, and a reverse transfer phenomenon is observed in which the flow rate is faster on the inner side (B, A) of the time curve. Inside the mold during the measurement, an instable state occurs in which a rotational flow repeatedly appears and disappears.

(27) From this viewpoint, it can be seen that a sufficient rotational flow can be generated in a state where the flow on the outer side of the discharge hole flow passages 2 which is inflected or curved is large and stable, but that a sufficient rotational flow cannot be generated when the flow is instable, and it can also be seen that a rotational flow is generated when the flow passages are curved (FIG. 12 and FIG. 10) and when the flow on the outer side of the curve is large, but the rotational flow disappears if the flow becomes instable and reverses.

(28) This phenomenon can be regarded as being caused by the shape of the discharge hole flow passages 2. In other words, FIG. 3 is a schematic drawing showing the flow inside the flow passage when the discharge hole flow passage 2 is inflected. The B and A sides shown in FIG. 7 are the inner sides when the flow passage is inflected. If the discharge hole flow passage 2 is inflected, then a flow which separates from the passage walls, rather than flowing along the passage walls, is generated on the downstream side of the first inner surface side wall 6 from the inner side point of inflection 5. An eddy 6a is generated to the downstream side of the inner side point of inflection 5 due to the separation of the flow, and consequently, the flow rate to the downstream side of the inner side point of inflection 5 on the inner side of the inflection section 6A is slowed. As opposed to this, since the flow volume is uniform, the flow rate becomes faster on the outer side of the inflection section 6A, due to the decrease in the flow rate on the inside of the inflection section 6A. On the other hand, the flow on the outer side of the inflection section 6A becomes a flow which is inclined with respect to the radiating direction as viewed from the center of the submerged nozzle 3, due to the side wall on the downstream side of the outer side point of inflection 9. In this way, due to the dual effects of the increase in the flow rate on the outer side of the inflection section 6A as a result of the generation of an eddy 6a caused by the inner side point of inflection 5, and the directing of the flow by the outer side of the inflection section 6A, a flow inclined with respect to the radiating direction viewed from the center of the submerged nozzle 3 continues to occur in a stable fashion, as a result of which a stable rotational flow is generated.

(29) On the other hand, in the case of the curved flow path in FIG. 12, and when separation of the flow is not likely to occur inside the curved portion and the flow on the outer side is fast due to the curved shape, a rotational flow is generated, but if the flow in the submerged nozzle 3 is disturbed, then the discharge flow will be instable and the rotational flow is lost. The same can be envisaged when the discharge hole flow passages 2 are provided in a tangential direction to the nozzle hole 1 as in FIG. 11. Moreover, if the inner side only is inflected and the outer side is not inflected, as in FIG. 13, then even if an eddy 6a is generated to the downstream side of the inflection section on the inner side of the flow passage, this has little effect because the outer side flow passage is a straight line, and therefore the flow direction becomes a radiating shape and a rotational flow is not generated. Furthermore, if only the outer side is inflected as shown in FIG. 14, then an eddy 6a is not generated and therefore a rotational flow is not generated.

(30) The submerged nozzle for continuous casting of molten metal according to the present invention was obtained by the discoveries and analysis described above.

(31) Below, a preferred mode of the submerged nozzle for continuous casting of molten metal according to the present invention will be described on the basis of FIG. 1.

(32) Desirably, the discharge hole flow passages 2 are arranged at rotationally symmetrical positions below the submerged nozzle 3. In so doing, it is possible to continue a rotational movement by means of the flow from the discharge hole flow passages 2. Furthermore, desirably, the number of discharge hole flow passages 2 is two to four, but the number may also be greater than this.

(33) The most important technical feature of the present invention is that a structure is adopted in which the discharge hole flow passages 2 are inflected rather than curved at the inner side point of inflection 5, and a stagnating section occurs due to the flow separating from the wall surfaces. Therefore, desirably, the two side surfaces of the discharge hole flow passages 2 in the horizontal cross-section of the submerged nozzle 3 when in use are constituted substantially by straight lines that are inflected. By inflecting the first and second inner surface side walls 6 and 7 on the inner surface side, an eddy 6a is created on the downstream side from the inner side point of inflection 5, and the flow rate on the outer side of the flow passage can be raised. Furthermore, by inflecting the first and second outer surface side walls 10 and 11 on the outer surface side, it is possible to direct the flow in a direction that is inclined with respect to the radiating direction as viewed from the center of the nozzle hole 1, and a rotational flow can therefore be created. By combining these inflections, a stable rotational flow is created.

(34) Consequently, in order to generate a rotational flow in the mold, it is necessary to generate a constant bias in the flow rate inside the discharge hole flow passage 2, and therefore, it is important that the walls on both sides of the flow passage 2 should be inflected in the same direction and that the angle of inflection should be within a certain prescribed range. If only the inside is inflected and the opposite side is a straight line as shown in FIG. 13, the flow passes along the straight-line wall surface and is discharged in a substantially radiating fashion from the nozzle hole 1, and therefore a rotational flow cannot be generated inside the mold. Furthermore, if only the outer side is inflected, as in FIG. 14, then it is not possible to generate a sufficient rotational flow inside the mold.

(35) The inner side point of inflection 5 of the discharge hole flow passage 2, and the outer side point of inflection 9 may be provided with a small curved radius R in order to simplify the manufacturing process. On the inner side, in particular, if the curve R is too great, then the shape approaches a curved flow passage rather than an inflected flow passage, and it becomes impossible to obtain a sufficient rotational flow. More specifically, R is no more than 5 mm, and desirably, no more than 3 mm. Furthermore, the inner and outer sides may have different values of the curve R.

(36) The second angle which is formed between a first center line 15 between the two straight lines, and extension lines thereof, formed by the first inner surface side wall 6 and the first outer surface side wall 10 on the inner side of the submerged nozzle 3 from the inflection section 6A in the discharge hole flow passage 2, and a second center line 16 between the two straight lines, and extension lines thereof, formed by the second inner surface side wall 7 and the second outer surface side wall 11 on the outer side of the submerged nozzle 3 from the inflection section 6A, is desirably 15 to 85, and more desirably 25 to 75. If the second angle is less than 15, then a flow separating from the tube wall does not occur in the flow passage on the inner side of the inflection, and therefore in addition to not being able to achieve a sufficient flow rate differential inside the flow passage, the flow is discharged in a substantially radiating fashion from the center of the nozzle, and hence a rotational flow inside the mold is not achieved. On the other hand, if the second angle is greater than 85, then the rotational flow rate decreases. This is thought to be because the growth of the eddy generated on the inner surface side becomes too large, and increase in flow rate on the outer side is suppressed. Furthermore, since the material thickness of the second outer surface side wall 11 and the nozzle outer surface 3a is thin, then problems of cracking and detachment of the submerged nozzle 3 during use become liable to occur when an angle greater than the above angle is implemented.

(37) Desirably, the first angle between the straight line 1a which links a pair of first and second intersection points 13 and 14 where the nozzle hole 1 intersects with two straight lines formed by the first inner surface side wall 6 and the first outer surface side wall 10 on the inner side of the submerged nozzle 3 from the inflection section 6A, and the first center line 15 which passes through the hole center P between the two straight lines formed by the first inner surface side wall 6 and the first outer surface side wall 10 on the inside of the submerged nozzle 3 from the inflection section 6A, is 45 to 135. More desirably, the first angle is 50 to 120. If the first angle is less than 45, or greater than 135, then the wall thickness between the nozzle hole 1 and the discharge hole flow passage 2 becomes thinner, and manufacture becomes difficult.

(38) The distance Wi between the pair of first and second intersection points 13 and 14 where the two straight lines formed by the first inner surface side wall 6 and the first outer surface side wall 10 on the inner side of the submerged nozzle 3 from the inflection section 6A intersect with the nozzle hole 1 is desirably 0.15Wi/ri1.6, and more desirably, 0.2Wi/ri1.4, where ri is the radius of the nozzle hole 1. If Wi/ri is less than 0.15, then this is not desirable since the discharge hole flow passage 2 becomes too small and the flow volume cannot be guaranteed, and if Wi/ri is greater than 1.6, then the material thickness at the nozzle outer surface 3a becomes thin, and therefore problems such as cracks and detachment of the submerged nozzle 3 during use become more liable to occur, which is undesirable.

(39) Taking the thickness of the submerged nozzle 3 to be t, the radius of the nozzle hole 1 to be ri, and the distance from the center of the submerged nozzle 3 to the inner side point of inflection 5 to be a, then desirably (ari)/t is no less than 0.2, and more desirably, no less than 0.3.

(40) If (ari)/t is less than 0.2, then the flow from the nozzle hole 1 of the submerged nozzle 3 to the discharge hole flow passage 2 is insufficient, and therefore the eddy on the downstream side from the points of inflection 5 and 9 does not grow sufficiently. Therefore, a sufficient rotational flow is not obtained. The maximum value of (ari)/t is not specified in particular, and is determined in accordance with the shape of the discharge hole flow passages 2 which is described below.

(41) On the other hand, if the distance from the center of the nozzle hole 1 to the outer side point of inflection 9 on the outer side surface of the inflection section is taken to be b, then (bri)/t is desirably no more than 0.9 and more desirably, no more than 0.85. If the distance b is greater than 0.9, then this is undesirable, since a sufficient effect cannot be obtained in causing the flow on the outer side of the inflection section to become inclined with respect to the radiating direction as viewed from the center of the nozzle hole 1, by means of the side wall on the downstream side of the outer side point of inflection 9.

(42) The width of the discharge hole flow passage 2 is essentially uniform, but does not have to be uniform. More specifically, the width on the inner side from the outer side point of inflection 9 may vary, and may be larger at the inlet to the discharge hole flow passage 2, and smaller on the side of the inflection section 6A, or alternatively larger on the side of the inflection section 6A. Furthermore, the width may also vary similarly to the outer side from the inner side point of inflection 5. Moreover, the width may also vary before and behind the inflection section 6A.

(43) In addition to providing discharge hole flow passages 2 in the side surfaces of the submerged nozzle 3, as described in FIG. 15, a bottom hole 17 may also be provided in the bottom surface of the nozzle.

(44) Due to the relationship between the cross-sectional area of the mold, and the passed volume of molten steel inside the submerged nozzle 3, if the passed volume of molten steel inside the submerged nozzle 3 is large and the discharge flow from the discharge hole flow passages 2 provided in the side surfaces is too great compared to the cross-sectional area of the mold, then the discharge flow generating a rotational flow becomes too strong, the meniscus vibration becomes large, and the casting process becomes instable. In this case, a bottom hole 17 is provided, and the flow volume required to create a rotational flow is caused to flow out from the discharge hole flow passages 2 on the side surfaces, while the remaining flow of molten steel is introduced to the downstream side of the mold, from the bottom hole 17, thereby achieving both a stable rotational state, and the suppression of meniscus vibrations.

(45) If the hole opening surface area of the bottom hole 17 is S.sub.b and the total opening surface area which is the sum of the opening surface area of the discharge hole flow passages 2 provided in the side surfaces and the opening surface area of the bottom hole 17 is S.sub.t, then the larger the value of the relative molten steel outflow volume S.sub.b/S.sub.t from the bottom hole 17, the greater the ratio of the molten steel volume flowing out from the bottom hole 17 with respect to the passed volume of molten steel in the nozzle. Furthermore, desirably, S.sub.b/S.sub.t is 0 to 0.4. More desirably, S.sub.b/S.sub.t is 0.1 to 0.35.

(46) Essentially, the cross-sectional shape of the bottom hole 17 in the direction parallel to the walls 17a of the bottom hole is circular, but it may also be a polygonal shape. Moreover, if the shape in the cross-sectional direction perpendicular to the bottom hole walls 17a forms a straight line, a curve or a combination of a plurality of straight lines and curves, it is possible to select a shape which is convex in the center.

(47) Furthermore, although not illustrated in the drawings, it is also possible to form a plurality of bottom holes 17. In this case, the value S.sub.b is the sum of the surface areas of the bottom holes 17. Furthermore, it is also possible to incline the discharge directions of a plurality of bottom holes 17 with respect to the nozzle axis, and to provide the bottom holes 17 in such a manner that the discharge directions thereof do not intersect with the nozzle axis.

(48) The shape of the mold in which the submerged nozzle 3 according to the present invention is used may be a round billet, a square billet, or bloom, having a diameter or long dimension of no more than 600 mm in the horizontal cross-section, and the passed molten steel volume is suitably in a range of 0.3 to 2.0 ton/min. Provided that the mold shape is close to a rectangular shape or circular shape, then a rotational flow is generated in the whole mold, but in the case of shapes with very long edges, such as a slab, although a good rotational flow is transmitted to the periphery of the nozzle, it is difficult to generate a rotational flow in the range of the shorter edge walls of the mold, which are distant from the nozzle. Considered in terms of the passed molten steel volume, with a low flow volume of no less than 0.3 ton/min, the discharge flow rate is very gentle and only an unsatisfactory rotational flow is generated. On the other hand, with a high flow rate of no less than 2.0 ton/min, great disruption is caused by the meniscus vibrations, and therefore the flow becomes instable.

(49) The submerged nozzle 3 according to the present invention relates to the shape of the discharge hole flow passages 2, and there are no restrictions on the structure of the nozzle hole 1 or the nozzle material. With regard to the structure of the nozzle hole 1, similar beneficial effects are obtained, for example, with a generic straight tube structure, and a structure wherein the diameter changes partially at an intermediate point of the tube, and a structure having recesses and projections in the inner tube. The nozzle material may be alumina-graphite, or magnesia-graphite, spinel-graphite, zirconia-graphite, alumina, clay, spinel, fused quartz, or the like. Even if the discharge hole flow passages 2 have an upwardly inclined angle or a downwardly inclined angle with respect to the horizontal plane, beneficial effects similar to those obtained when they are horizontal can be obtained.

Practical Examples and Comparative Examples

(50) A water model simulation apparatus of a similar scale to actual equipment was used to evaluate whether or not a stable rotational flow could be achieved using the submerged nozzles 3 indicated in Table 1.

(51) The water model of the submerged nozzle 3 was a water model envisaging a continuous casting apparatus for a 200 mm-diameter round billet, wherein the submerged nozzle 3 has an inner diameter of 35 mm, an outer diameter of 75 mm, a material thickness of 20 mm, an output cross-section of the discharge hole of 24 mm22 mm, two discharge holes, and a casting draw rate of 1.5 m/minute.

(52) The rotational flow was evaluated as indicated below. More specifically, an experiment was carried out for three minutes, and the occurrence of a steady rotational flow inside the mold during this time was assessed on the basis of the rate and stability of the rotational flow. The rotational flow rate was judged to be satisfactory if sufficiently large, was judged to be rather unsatisfactory if a rotational flow occurred but it was not very large, and was judged none if a rotational flow did not occur. Furthermore, stability was judged to be good when a stable rotational flow was obtained, was judged to be instable if the rotational flow repeatedly appeared and disappeared, and was judged none if the rotational flow did not occur.

(53) The water model experiment was carried out using various shapes of the discharge hole flow passage 2, and the characteristic features thereof were as follows.

(54) In cases where there was an inflection point at an intermediate point of the flow channel, a radius of R5 was applied in all cases. Table 1 shows the experiment results. The characteristics of the respective discharge hole shapes are expressed below.

(55) 1. Tangential: The shape described in documents 1 to 4 and illustrated in FIG. 11 in which the discharge hole path is formed by straight lines in a tangential direction to the inner diameter.

(56) 2. Curved: The shape described in documents 1 and 3 and illustrated in FIG. 12, in which the discharge hole path is curved when viewed in the perpendicular direction during use.

(57) 3. Inside-only inflected: The shape illustrated in FIG. 13 in which the side walls of the discharge hole path are inflected on the inner side only, and the opposite side is formed by a straight line.

(58) 4. Outside-only inflected: The shape illustrated in FIG. 14 in which the side walls of the discharge hole path are inflected on the outer side only, and the opposite side is formed by a straight line.

(59) 5. Inflected: The shape illustrated in FIG. 2 in which both side walls of the discharge hole flow passage 2 are inflected in the same direction at an intermediate point.

(60) In the case of the tangential shape described in Documents 1 to 4 and the curved shape described in Documents 1 and 3, the flow rate of the rotational flow was weak, and therefore the rotational flow repeatedly appeared and disappeared, and the mold was in an instable state (Comparative Examples 1 and 2). When only the inner side of the discharge hole path was inflected (Comparative Examples 3 to 5), or when only the outer side thereof was inflected (Comparative Examples 6 to 9), a rotational flow did not occur. With a shape where both sides of the discharge hole flow passage 2 were inflected in the same direction, where was 15 to 85, and where the distances a and b from the nozzle center to the points of inflection 5 and 9 were respectively in ranges of 0.2(ari)/t and (bri)/t0.9, then a stable rotational flow was obtained with a sufficient flow rate (Products of the Invention 1 to 7), but if was within the stated range but the distance to the points of inflection was outside the stated range (Comparative Examples 10, 12, and 13), or if was outside the stated range (Comparative Examples 11, 14, and 15), then although a stable rotational flow occurred, the rotational flow was not very large.

(61) TABLE-US-00001 TABLE 1 Comp. Comp. Comp. Comp. Comp. Comp. Comp. Comp. Comp. Product Product Ex. 1 Ex. 2 Ex. 3 Ex. 4 Ex. 5 Ex. 6 Ex. 7 Ex. 8 Ex. 9 Invention 1 Invention 2 Feature of Tangential Curved Inside-only inflected Outside-only inflected Inflected hole shape 52.5 52.5 90 90 90 52.5 52.5 90 90 52.5 52.5 30 30 60 30 45 30 45 30 45 (a-ri)/t 0.4 0.8 0.5 0.21 0.23 (b-ri)/t 0.6 0.8 0.7 0.7 0.74 0.87 t 20 20 20 20 20 20 20 20 20 20 20 Wi 22 22 22 22 22 22 22 22 22 22 22 State of Unsatis- Unsatis- None None None None None None None Good Good rotational factory factory flow Stability of Instable Instable None None None None None None None Good Good rotational flow Comp. Comp. Comp. Product Product Comp. Comp. Product Product Product Comp. Ex. 10 Ex. 11 Ex. 12 Invention 3 Invention 4 Ex. 13 Ex. 14 Invention 5 Invention 6 Invention 7 Ex. 15 Feature of Inflected hole shape 52.5 90 90 90 90 90 142.5 142.5 142.5 142.5 142.5 60 10 30 30 60 80 10 30 60 80 90 (a-ri)/t 0.12 0.44 0.05 0.36 0.27 0.08 0.67 0.62 0.47 0.32 0.20 (b-ri)/t 0.93 0.61 0.33 0.70 0.84 0.92 0.59 0.66 0.81 0.86 0.86 t 20 20 20 20 20 20 20 20 20 20 20 Wi 22 22 22 22 22 22 22 22 22 22 22 State of Unsatis- Unsatis- Unsatis- Good Good Unsatis- Unsatis- Good Good Good Unsatis- rotational factory factory factory factory factory factory flow Stability of Good Good Good Good Good Good Good Good Good Good Good rotational flow

(62) Next, in order to confirm the state of generation of the rotational flow due to the mold shape, the submerged nozzles 3 according to the Product of the Invention 1 and the Comparative Example 1 of the present invention were used in an actual casting machine and the beneficial effects thereof were confirmed. FIG. 4 shows a cross-sectional diagram of the Product of the Invention 1, and Table 2 shows the test results. In the Comparative Examples, a sufficient rotational state could not be obtained, but when the Product of Invention 1 was used, it was possible to obtain a good rotational state, regardless of the size and shape of the mold.

(63) TABLE-US-00002 TABLE 2 Comparative Product of Product of Product of Example 1 Invention 1 Invention 1 Invention 1 52.5 52.5 30 (a-ri)/t 0.21 (b-ri)/t 0.74 t 20 20 Wi 22 22 Shape of Bloom Bloom Round Square mold billet billet Dimension 500 500 300 300 of long edge (diameter) (mm) Flow rate Unsatisfactory Good Good Good of rotational flow Stability Unsatisfactory Good Good Good of rotational flow

(64) Furthermore, a water model simulation test was carried out in order to check the state of generation of the rotational flow depending on the through-put. A nozzle having the shape of the Product of the Invention 1 was used, and the mold size was a square shape of 500500 mm. Table 3 shows the results.

(65) Under all through-put conditions, a rotational flow was generated, but when the through-put was 0.2 ton/min, the rotational flow rate was slow and unsatisfactory. At through-puts of 0.4 and 1.8 ton/min, a good rotational state was obtained, but at 2.2 ton/min, the meniscus vibration was severe, and an instable state occurred.

(66) TABLE-US-00003 TABLE 3 52.5 30 (a-ri)/t 0.21 (b-ri)/t 0.74 t 20 Wi 22 Through- 0.2 0.4 1.8 2.2 put (ton/min) Dimension 500 500 500 500 of long edge (mm) Flow rate Unsatisfactory Good Good Good of rotational flow Stability Good Good Good Unsatisfactory of rotational flow

(67) A water model simulation test was carried out under similar conditions, in order to check the beneficial effects of providing a bottom hole 17. A plurality of submerged nozzles 3 having the shape according to the first embodiment of the present invention were prepared, and a round hole was provided in the bottom portion of the submerged nozzles 3. For comparison, a test was carried out with a nozzle provided only with a bottom hole 17. The mold size was taken to be a 500 by 500 mm square shape. In addition to the assessment items in the respective water model simulation tests described above, the amount of variation in the in-mold bath surface was also assessed. Table 4 shows the results. Although a rotational flow was generated under all through-put conditions, a tendency for increased variation in the in-mold bath surface was observed under high through-put conditions. When a bottom hole was provided, a favorable state was obtained in which the generation and stability of the rotational flow remained unchanged, but the amount of variation in the bath surface was suppressed. In a nozzle with a bottom hole 17 only (Comparative Example 16), no rotational flow was generated, and if the bottom hole 17 was too large, then there was a tendency for the rotational flow to be weak.

(68) TABLE-US-00004 TABLE 4 Experi- Experi- Experi- Experi- Experi- Experi- Experi- Experi- Experi- Experi- ment 1 ment 2 ment 3 ment 4 ment 5 ment 6 ment 7 ment 8 ment 9 ment 10 Product Product Product Product Product Product Product Product Product Product of Inven- of Inven- of Inven- of Inven- of Inven- of Inven- of Inven- of Inven- of Inven- of Inven- tion 1 tion 1 tion 1 tion 1 tion 8 tion 8 tion 8 tion 8 tion 9 tion 9 Inflow 0.5 1 2 3 0.5 1 2 3 0.5 1 volume (ton/min) Sbottom/Stotal 0 0 0 0 0.1 0.1 0.1 0.1 0.4 0.4 State of Good Good Good Good Good Good Good Good Good Good rotational flow Stability of Good Good Good Instable Good Good Good Good Good Good rotational flow Variation in Good Good Quite Rough Good Good Good Quite Good Good bath surface rough rough in mold Experi- Experi- Experi- Experi- Experi- Experi- ment 11 ment 12 ment 13 ment 14 ment 15 ment 16 Experi- Experi- Product Product Product Product Product Product ment 17 ment 18 of Inven- of Inven- of Inven- of Inven- of Inven- of Inven- Comparative Comparative tion 9 tion 9 tion 10 tion 10 tion 10 tion 10 Example 16 Example 16 Inflow 2 3 0.5 1 2 3 1 2 volume (ton/min) Sbottom/Stotal 0.4 0.4 0.5 0.5 0.5 0.5 1 1 State of Good Good Occurred Occurred Occurred Occurred None None rotational flow Stability of Good Good Instable Good Good Good rotational flow Variation in Good Quite Good Good Good Good Good Good bath surface rough in mold

INDUSTRIAL APPLICABILITY

(69) The submerged nozzle for a continuous casting apparatus according to the present invention can contribute to improvement of the quality of cast metal, by generating a stable rotational flow of molten steel inside a mold simply by improving the shape of discharge holes of the submerged nozzle, without making modifications to other equipment.