Production equipment line for hot-rolled steel strip and production method for hot-rolled steel strip

Abstract

A production equipment line for a hot-rolled steel strip comprises a rough rolling mill comprising rough rolling mills for hot rolling a material, which is heated to a predetermined temperature to a finish rolling start sheet thickness and a finish rolling mill comprising finish rolling mills for controlled-rolling the material to a final sheet thickness. At least one of the rough rolling mills is a reversible rolling mill. The production equipment line is provided on an upstream side of the reversible rolling mill with one of a slow cooling apparatus for slowly cooling at a water volume density of less than 1000 L/min.Math.m.sup.2 and a rapid cooling apparatus for rapidly cooling after the slow-cooling at a water volume density of not less than 1000 L/min.Math.m.sup.2 and the other of the slow cooling apparatus and rapid cooling apparatus on a downstream side of the reversible rolling mill.

Claims

1. A production equipment line for a hot-rolled steel strip comprising a rough rolling mill group comprised of plural rough rolling mills for hot rolling a material to be rolled which is heated up to a predetermined temperature to a finish rolling start sheet thickness and a finish rolling mill group comprised of plural finish rolling mills for controlled-rolling the material to be rolled to a final sheet thickness, characterized in that at least one of the plural rough rolling mills is a reversible rolling mill, and one of a slow cooling apparatus for slowly cooling the material to be rolled at a water volume density of less than 1000 L/min.Math.m.sup.2 or a rapid cooling apparatus for rapidly cooling the material to be rolled after the slow cooling at a water volume density of not less than 1000 L/min.Math.m.sup.2 is arranged on an upstream side of the reversible rolling mill and the other of the slow cooling apparatus or the rapid cooling apparatus is arranged on a downstream side of the reversible rolling mill, such that at least one of the slow cooling apparatus and the rapid cooling apparatus is arranged between the reversible rolling mill and another one of the plural rough rolling mills.

2. The production equipment line for a hot-rolled steel strip according to claim 1, wherein at least a rough rolling mill arranged on a most downstream side among the plural rough rolling mills is a reversible rolling mill.

3. The production equipment line for a hot-rolled steel strip according to claim 1, wherein the slow cooling apparatus is arranged on the upstream side of the reversible rolling mill and the rapid cooling apparatus is arranged on the downstream side thereof.

4. The production equipment line for a hot-rolled steel strip according to claim 2, wherein the slow cooling apparatus is arranged on the upstream side of the reversible rolling mill and the rapid cooling apparatus is arranged on the downstream side thereof.

5. The production equipment line for a hot-rolled steel strip according to claim 1, wherein the slow cooling apparatus is positioned relative to the plural rough rolling mills such that the material to be rolled is slowly cooled by the slow cooling apparatus when the sheet thickness is not less than 80 mm and the rapid cooling apparatus is positioned relative to the plural rough rolling mills such that the material to be rolled is rapidly cooled by the rapid cooling apparatus when the sheet thickness is less than 80 mm.

6. The production equipment line for a hot-rolled steel strip according to claim 2, wherein the slow cooling apparatus is positioned relative to the plural rough rolling mills such that the material to be rolled is slowly cooled by the slow cooling apparatus when the sheet thickness is not less than 80 mm and the rapid cooling apparatus is positioned relative to the plural rough rolling mills such that the material to be rolled is rapidly cooled by the rapid cooling apparatus when the sheet thickness is less than 80 mm.

7. The production equipment line for a hot-rolled steel strip according to claim 3, wherein the slow cooling apparatus is positioned relative to the plural rough rolling mills such that the material to be rolled is slowly cooled by the slow cooling apparatus when the sheet thickness is not less than 80 mm and the rapid cooling apparatus is positioned relative to the plural rough rolling mills such that the material to be rolled is rapidly cooled by the rapid cooling apparatus when the sheet thickness is less than 80 mm.

8. The production equipment line for a hot-rolled steel strip according to claim 4, wherein the slow cooling apparatus is positioned relative to the plural rough rolling mills such that the material to be rolled is slowly cooled by the slow cooling apparatus when the sheet thickness is not less than 80 mm and the rapid cooling apparatus is positioned relative to the plural rough rolling mills such that the material to be rolled is rapidly cooled by the rapid cooling apparatus when the sheet thickness is less than 80 mm.

9. The production equipment line for a hot-rolled steel strip according to claim 1, wherein each cooling time in the slow cooling apparatus and the rapid cooling apparatus is set so as to render a surface temperature of the material to be rolled during the cooling into not lower than 600° C.

10. The production equipment line for a hot-rolled steel strip according to claim 1, wherein a sheet thickness at an exit side of a final-stage finish rolling mill among the plural finish rolling mills is not less than 12 mm.

11. A method for producing a hot-rolled steel strip by hot rolling a material to be rolled which is heated to a predetermined temperature by a plurality of rough rolling mills to provide a finish rolling start sheet thickness and controlled-rolling the material to be rolled to a finish sheet thickness by a plurality of finish rolling mills, characterized in that at least one of the plural rough rolling mills is a reversible rolling mill, and one of a slow cooling apparatus for slowly cooling the material to be rolled at a water volume density of less than 1000 L/min.Math.m.sup.2 or a rapid cooling apparatus for rapidly cooling the material to be rolled at a water volume density of not less than 1000 L/min.Math.m.sup.2 is arranged on an upstream side of the reversible rolling mill and the other of the slow cooling apparatus or the rapid cooling apparatus is arranged on a downstream side of the reversible rolling mill, such that at least one of the slow cooling apparatus and the rapid cooling apparatus is arranged between the reversible rolling mill and another one of the plural rough rolling mills, and the material to be rolled is slowly cooled by the slow cooling apparatus at a water volume density of less than 1000 L/min.Math.m.sup.2 and thereafter the material to be rolled is rapidly cooled by the rapid cooling apparatus at a water volume density of not less than 1000 L/min.Math.m.sup.2.

12. The production method for a hot-rolled steel strip according to claim 11, wherein at least a rough rolling mill arranged on a most downstream side among the plural rough rolling mills is a reversible rolling mill.

13. The production method for a hot-rolled steel strip according to the claim 11, wherein the slow cooling apparatus is arranged on the upstream side of the reversible rolling mill and the rapid cooling apparatus is arranged on the downstream side thereof.

14. The production method for a hot-rolled steel strip according to the claim 12, wherein the slow cooling apparatus is arranged on the upstream side of the reversible rolling mill and the rapid cooling apparatus is arranged on the downstream side thereof.

15. The production method for a hot-rolled steel strip according to claim 11, wherein the material to be rolled is slowly cooled by the slow cooling apparatus when the sheet thickness is not less than 80 mm and rapidly cooled by the rapid cooling apparatus when the sheet thickness is less than 80 mm.

16. The production method for a hot-rolled steel strip according to claim 12, wherein the material to be rolled is slowly cooled by the slow cooling apparatus when the sheet thickness is not less than 80 mm and rapidly cooled by the rapid cooling apparatus when the sheet thickness is less than 80 mm.

17. The production method for a hot-rolled steel strip according to claim 13, wherein the material to be rolled is slowly cooled by the slow cooling apparatus when the sheet thickness is not less than 80 mm and rapidly cooled by the rapid cooling apparatus when the sheet thickness is less than 80 mm.

18. The production method for a hot-rolled steel strip according to claim 14, wherein the material to be rolled is slowly cooled by the slow cooling apparatus when the sheet thickness is not less than 80 mm and rapidly cooled by the rapid cooling apparatus when the sheet thickness is less than 80 mm.

19. The production method for a hot-rolled steel strip according to claim 11, wherein the material to be rolled is cooled by the slow cooling apparatus and rapid cooling apparatus so as to render a surface temperature of the material to be rolled into not lower than 600° C. during the cooling.

20. The production method for a hot-rolled steel strip according to claim 11, wherein a sheet thickness at an exit side of a final-stage finish rolling mill among the plural finish rolling mills is not less than 12 mm.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is a schematic block diagram of a usual production equipment line for a hot-rolled steel strip together with a rolling pass.

(2) FIG. 2 is a schematic block diagram of an embodiment of the production equipment line for a hot-rolled steel strip according to the invention for carrying out an embodiment of the production method for a hot-rolled steel strip according to the invention together with a rolling pass and a cooling timing.

(3) FIG. 3 is a graph showing a surface temperature history of a sheet bar when a sheet bar having a thickness of 40 mm is cooled at various volume densities of cooling water.

(4) FIG. 4 is a graph showing a cross-sectional average temperature of a sheet bar when a sheet bar having a thickness of 40 mm is cooled at various volume densities of cooling water.

(5) FIG. 5 is a graph showing a relation between a volume density of cooling water and a cross-sectional average limit temperature dropping quantity of a sheet bar when sheet bars having an initial surface temperature of 1000° C. and various sheet thicknesses are cooled to a sheet bar surface temperature of 600° C.

(6) FIG. 6 is a graph showing a relation between a volume density of cooling water and a cross-sectional average cooling rate of sheet bars having an initial surface temperature of 1000° C. and various sheet thicknesses.

(7) FIG. 7 is a schematic block diagram of another embodiment of the production equipment line for a hot-rolled steel strip according to the invention for carrying out another embodiment of the production method for a hot-rolled steel strip according to the invention together with a rolling pass and a cooling timing.

EMBODIMENTS FOR CARRYING OUT THE INVENTION

(8) A usual production equipment line and production method for a hot-rolled steel strip will be explained below, and then an embodiment of the invention will be described in detail with reference to the accompanying drawings. FIG. 1 is a schematic block diagram of a usual production equipment line for a hot-rolled steel strip together with a rolling pass.

(9) In the production of the usual hot-rolled steel strip, as shown in FIG. 1, a material to be rolled (slab) having, for example, a sheet thickness of 260 mm is heated to 1170° C. in a continuous heating furnace 1 and then shaped into a sheet bar 10 as a sheet-like material to be rolled having a predetermined thickness by a rough rolling mill group 3. In order to adjust the sheet width of the sheet bar 10, the material to be rolled is pressed to a given size in the widthwise direction by a sizing press 2 disposed at an exit side of the continuous heating furnace 1 and further pressed also in the widthwise direction by an edger 4 disposed in a position close to a rolling mill of the rough rolling mill group 3. Next, a front edge and a tail edge of the sheet bar 10 are cut by a crop shear 5, and thereafter the sheet bar 10 is finish-rolled to a predetermined thickness (for example, 20 mm) in a finish rolling mill group 6 to form a hot-rolled steel strip, which is then cooled to a given temperature in a runout table 7 and coiled with a coiler 8.

(10) In the illustrated example, the rough rolling mill group 3 is comprised of two rough rolling mills 31 and 32, among which a reversible rolling mill 31 capable of rolling reversibly is arranged on an upstream side (heating furnace side) of the rough rolling mill group 3 and a non-reversible rolling mill 32 capable of rolling only in a transporting direction toward a downstream side is arranged on the downstream side thereof. In the rough rolling mill group 3, for example, the rolling of about 5-11 passes is performed through the reversible rolling mill 31 and then the rolling of only 1 pass is performed through the non-reversible rolling mill 32.

(11) Conventionally, the sheet bar 10 rolled to a predetermined controlled-rolling start thickness is kept waiting under oscillation between the rough rolling mill group 3 and the finish rolling mill group 6 until the temperature thereof is lowered to a predetermined controlled-rolling start temperature. The surface temperature of the sheet bar 10 is measured with a radiation thermometer 33. After the surface temperature of the sheet bar 10 is confirmed to be decreased to the predetermined controlled-rolling start temperature, the sheet bar is transported to the finish rolling mill group 6 to perform controlled-rolling. In this case, it is necessary to keep the sheet bar waiting for about 60-300 seconds in order to decrease the temperature by about 150-250° C. by air cooling. During this period of time, the rolling cannot be performed in the finish rolling mill group 6, leading to the decrease of the rolling efficiency. When the thickness of the sheet bar 10 is 50 mm for example, the length of the sheet bar 10 is very long being about 50 m, so that it is not realistic to introduce a mechanism such as a lifting apparatus elevating the sheet bar or the like as disclosed in Patent Documents 3 and 4.

(12) Therefore, an embodiment of the invention adopts a construction wherein cooling and rolling in the rough rolling mill group 3 are simultaneously performed by arranging a rapid cooling apparatus 41 having a water volume density of not less than 1000 L/min.Math.m.sup.2 on an upstream side or downstream side of the reversible rolling mill 31 in the rough rolling mill group 3 and arranging a slow cooling apparatus 42 having a water volume density of less than 1000 L/min.Math.m.sup.2 on a downstream side or upstream side of the reversible rolling mill 31. Thus, the temperature of the sheet bar 10 can be adjusted so as to be equal to the controlled-rolling start temperature at a time of completing the rolling in the rough rolling mill group 3, and hence the waiting time for the controlled-rolling temperature can be largely shortened.

(13) A concrete arrangement example of these cooling apparatuses and a rolling method using them will be described below. FIG. 2 is a block diagram schematically showing an embodiment of the production apparatus for the hot-rolled steel strip according to the invention made by adding the rapid cooling apparatus 41 and the slow cooling apparatus 42 to the production equipment line shown in FIG. 1 for performing an embodiment of the production method for the hot-rolled steel strip according to the invention.

(14) In this embodiment, as shown in FIG. 2, the rapid cooling apparatus 41 is arranged on the downstream side of the reversible rolling mill 31, and the slow cooling apparatus 42 is arranged on the upstream side thereof. In the initial rolling, regarding an arbitrary rolling pass of the reversible rolling mill 31, as a rolling pass and a cooling timing are shown in a lower part of FIG. 2 for example, a pass-cooling of the sheet bar 10 is conducted by the slow cooling apparatus 42 before the first rolling through the reversible rolling mill 31 and between even number-th rolling passes (after the even number-th rolling and before the odd number-th rolling) through the reversible rolling mill 31. When the thickness of the sheet bar 10 reaches a predetermined thickness (late stage of rolling), discharge of water from the slow cooling apparatus 42 is stopped, while the rapid cooling apparatus 41 arranged on the downstream side of the reversible rolling mill 31 is operated to conduct a pass-cooling of the sheet bar 10 through the rapid cooling apparatus 41 in connection with the arbitrary rolling pass of the reversible rolling mill 31, for example, after the first rolling and before the second rolling in the reversible rolling mill 31 and in transfer to a non-reversible rolling mill 32.

(15) In this embodiment, the reason why the rapid cooling apparatus 41 and the slow cooling apparatus 42 are used properly in accordance with the thickness of the sheet bar 10, which is repeatedly rolled in the reversible rolling mill 31, is considered as follows. FIG. 3 shows a temperature history on the surface of the sheet bar 10 having a sheet thickness of 40 mm when cooled at various volume densities of cooling water as an example. In this figure, a time region where the temperature is rapidly decreased shows that water cooling is conducted, and a time region where the temperature is increased through a lower limit temperature shows that water cooling is stopped and radiation cooling (air cooling) is conducted. As seen from this figure, a cooling rate of the surface (time-gradient of temperature) becomes faster as the water volume density of cooling water is increased. On the other hand, when the temperature of the sheet bar 10 falls below 600° C., phase transformation from austenitic structure to ferritic structure is caused. When the controlled-rolling is performed at such a state, there is a risk of decreasing surface ductility to cause cracking from ferrite grain boundary. Accordingly, the temperature at an outermost surface layer of the sheet bar 10 during the water cooling is preferable to be held at not lower than 600° C. In the example shown in FIG. 3, water cooling is stopped when the surface temperature of the sheet bar 10 arrives at a lower limit temperature of 600° C. from this viewpoint. FIG. 4 shows a cross-sectional average temperature of the sheet bar 10 at that time. Similarly, a time region where the temperature is rapidly decreased shows that water cooling is conducted. When the water volume density of the cooling water is high, a time-gradient of the cross-sectional average temperature of the sheet bar 10, or a cooling rate becomes steep. However, the feed of the cooling water is stopped halfway from a viewpoint of holding the surface temperature at not lower than 600° C. to prevent cracking from ferrite grain boundary, so that the temperature at the end of cooling becomes higher as the water volume density of the cooling water becomes larger. Therefore, it can be seen that as the water volume density of the cooling water becomes smaller, the coolable temperature dropping quantity by one cooling can be increased.

(16) FIG. 5 shows a relation between a volume density of cooling water and a cross-sectional average temperature dropping quantity of sheet bars 10 having an initial surface temperature of 1000° C. and various sheet thicknesses when the sheet bars are cooled until the surface temperature becomes 600° C. As previously explained, since there is a restriction of holding the surface temperature at not lower than 600° C., as the sheet thickness becomes larger and as the water volume density of the cooling water becomes larger, the temperature dropping quantity by one water cooling becomes smaller. Hereinafter, the temperature difference which can be dropped by one cooling due to the restriction of holding the surface temperature at not lower than 600° C. is called as a limit temperature dropping quantity.

(17) FIG. 6 shows a relation between a volume density of cooling water and a cross-sectional average cooling rate of sheet bars 10 having an initial surface temperature of 1000° C. and various sheet thicknesses. As the volume density of cooling water becomes larger, the cooling rate becomes faster. Considering the above restriction together, when cooling within the limit temperature dropping quantity is performed, as the water volume density of the cooling water becomes higher, the temperature can be dropped for a shorter time, which is advantageous in the shortening of the rolling time.

(18) Considering the actual rolling process, a slab having a thickness of about 220-260 mm is rolled to about 45 mm by about 10 passes. In the initial stage of the rolling, the sheet thickness is large, so that the limit temperature dropping quantity tends to become small, and hence the slow cooling having a large limit temperature dropping quantity is advantageous from a viewpoint of a lower limit surface temperature per 1 pass. Under a condition that the sheet thickness is small in the later stage of the rolling, the limit temperature dropping quantity can be made larger, so that the rapid cooling which increases the cooling rate to perform water cooling for a short time becomes advantageous. Also, as the sheet thickness is smaller, the limit temperature dropping quantity is larger, so that when plural rough rolling mills are provided, it is preferable that the cooling is carried out on the upstream side or downstream side of the reversible rolling mill 31 arranged on a most downstream side in accordance with the smallest sheet thickness.

(19) As seen from FIG. 5, when the sheet thickness is as relatively large as 80 mm and 120 mm, the limit temperature dropping quantity becomes larger at a low water volume density when the water volume density of cooling water is not more than 1000 L/min.Math.m.sup.2. Therefore, a large limit temperature dropping quantity can be ensured by making the water volume density of the cooling water less than 1000 L/min.Math.m.sup.2 in the case of a sheet thickness of not less than 80 mm from a viewpoint of preventing ferrite cracking in the surface of the sheet bar 10.

(20) In the embodiment of the invention, therefore, the cooling to a given temperature desirable for the controlled-rolling (controlled-rolling start temperature) is divided into plural passes, in which the cooling within a temperature range of about 20-30° C. is performed per 1 pass. Considering the above theory, the cooling is performed by the slow cooling apparatus 42 having a water volume density of less than 1000 L/min.Math.m.sup.2 in the initial rolling in which the sheet thickness is relatively large, particularly being not less than 80 mm, while the cooling is performed by the rapid cooling apparatus 41 having a water volume density of not less than 1000 L/min.Math.m.sup.2 in the later rolling in which the sheet thickness is relatively small, particularly being less than 80 mm, whereby efficient cooling can be performed while preventing ferrite cracking on the surface of the sheet bar 10, and thus the rolling time can be shortened.

(21) In the slow cooling apparatus 42, as the water volume density of the cooling water is decreased, the temperature dropping quantity by water cooling per 1 pass becomes larger, but the cooling rate becomes slower, and hence the effect of increasing the efficiency becomes small. Therefore, the cooling water volume by the slow cooling apparatus 42 is preferable to be not less than 200 L/min.Math.m.sup.2. In the rapid cooling apparatus 41, as the volume density of cooling water becomes larger, the temperature dropping quantity by water cooling per 1 pass becomes smaller while the cooling rate becomes faster. Therefore, the increase of the equipment cost associated with the increase of the cooling water volume is caused within a range where the critical cooling capacity per 1 pass is not much changed, so that the water volume density of the cooling water is preferable to be not more than 6000 L/min.Math.m.sup.2.

(22) Each of the cooling apparatuses 41 and 42 may be of any system such as group jet cooling comprised of plural round nozzles, pipe laminar, mist cooling, spray cooling and so on. In the rapid cooling apparatus 41, since an amount of cooling water is large, thick retained water is liable to be generated on the sheet bar 10, and there is a possibility that stable cooling cannot be obtained because the retained water blocks collision of the jetted cooling water onto the surface of the steel sheet. Therefore, a group jet cooling apparatus having a plurality of round nozzles (a section of the nozzle may have an elliptical form or a polygonal form) with a high penetrating power to a liquid film is preferable to be used in the rapid cooling apparatus 41. In the group jet cooling apparatus, a jet flow jetted from a jetting port of each nozzle continuously travels straight, not in a spraying form or a film form, until the jet flow impinges on the surface of the steel strip, and thus a section thereof is substantially kept at a circular form. On the other hand, the slow cooling apparatus 42 has no limits, so that a pipe laminar system usually used in a cooling apparatus for hot-rolled steel strips or a spraying system can be used.

(23) A preferable arrangement of the cooling apparatuses 41 and 42 will be described below. It is preferable that the rapid cooling apparatus 41 and the slow cooling apparatus 42 are arranged in a position nearer to the reversible rolling mill 31 as much as possible from a viewpoint of the rolling efficiency, because a time required for transferring the sheet bar 10 between the cooling apparatuses 41 and 42 and the reversible rolling mill 31 can be shortened as the rapid cooling apparatus 41 and the slow cooling apparatus 42 are arranged closer to the reversible rolling mill 31. As a cooling system by the cooling apparatuses 41 and 42 are included a stop type cooling system where the sheet bar 10 is cooled in a stopped or oscillation state and a pass type cooling system where the sheet bar 10 is cooled while passing through the cooling apparatuses 41 and 42. In the stop type cooling system, the installation length of the cooling apparatuses 41 and 42 is required to be longer than a length of the sheet bar 10, and hence the cooling apparatuses 41 and 42 are increased in size. Therefore, the cooling apparatuses 41 and 42 can be downsized by adopting the pass type cooling system and arranged closest to the reversible rolling mill 31.

(24) The production equipment line for the hot-rolled steel strip according to this embodiment may be provided with a rolling pass schedule preparing apparatus 51 and a cooling pass schedule preparing apparatus 52 as shown in FIG. 2. The rolling pass schedule preparing apparatus 51 is constructed with a personal computer or the like, wherein pass schedules such as a rolling reduction, pass number and the like in each of the rough rolling mills 31 and 32 are calculated and prepared from the input slab thickness, controlled-rolling start thickness and the like so as to decrease the pass number within the limit of rolling reduction in each rolling pass as much as possible.

(25) The cooling pass schedule preparing apparatus 52 is constructed with a personal computer or the like, wherein slow cooling by the slow cooling apparatus 42 is allocated in the case that the thickness of the sheet bar 10 is not less than 80 mm and rapidly cooling by the rapid cooling apparatus 41 is allocated in the case that the thickness of the sheet bar 10 is less than 80 mm to each cooling pass based on the thickness of the sheet bar 10 and the like after the each rolling pass calculated by the rolling pass schedule preparing apparatus 51, while a cooling pass number and cooling time are calculated from a relation between the volume density of cooling water and temperature dropping quantity for a predetermined sheet thickness obtained by pre-experiments or the like and a relation between the surface temperature and cooling time of a sheet bar 10 for a predetermined volume density of cooling water obtained by pre-experiments or the like. In this case, the cooling pass schedule preparing apparatus 52 calculates a cooling time and a passing rate in the slow cooling apparatus 42 and the rapid cooling apparatus 41 in such a manner so that the surface temperature of the sheet bar 10 does not fall below 600° C. during the cooling. Moreover, the cooling pass schedule prepared by the cooling pass schedule preparing apparatus 52 may be fed back to the rolling pass schedule preparing apparatus 51. When the rolling pass number is lacking for the calculated cooling pass number, a rolling pass with a rolling reduction of zero is added by the rolling pass schedule preparing apparatus 51 and water cooling may be performed after this rolling pass. The thus prepared rolling pass schedule and cooling pass schedule are output to each of the rough rolling mills 31 and 32 and cooling apparatuses 41 and 42, whereby rolling and cooling in each apparatus of 31, 32, 41, and 42 are conducted according to these schedules.

(26) In the above embodiment, it is explained that the rough rolling mill group 3 is comprised of one reversible rolling mill 31 and one non-reversible rolling mill 32. However, the rough rolling mill group 3 may be provided with a plurality of reversible rolling mills 31. In FIG. 7 are shown a production equipment line for a hot-rolled steel strip according to another embodiment of the invention and a production method for a hot-rolled steel strip using the same. In this embodiment shown in the figure, the rough rolling mill group 3 is comprised of three reversible rolling mills 31. The slow cooling apparatus 42 is arranged on an upstream side of a reversible rolling mill 31 arranged at a most downstream side viewing in the rolling direction, and the rapid cooling apparatus 41 is arranged on the downstream side thereof. In a lower part of this figure is also shown a water cooling timing in the rolling process. In this production equipment line, rolling is started from the reversible rolling mill 31 arranged at a most upstream side at the left of the figure, and rolling of 3 passes is conducted in each of the reversible rolling mills 31. In this case, the most upstream reversible rolling mill 31 and the central reversible rolling mill 31 perform rolling in accordance with a rolling schedule for the sheet bar 10 having a sheet thickness of not less than 80 mm, while the most downstream reversible rolling mill 31 performs rolling in accordance with a rolling schedule for the sheet bar 10 having a sheet thickness of less than 80 mm. As shown in this figure in connection with the central reversible rolling mill 31, pass cooling can be conducted by the slow cooling apparatus 42 after the first rolling, before the second rolling and in the transfer to the most downstream reversible rolling mill 31. Thus, when the slow cooling is performed in connection with the rolling pass of the most downstream reversible rolling mill 31, it is preferable to arrange the slow cooling apparatus 42 close to the central reversible rolling mill 31. It is because a moving distance of the sheet bar 10 from the central reversible rolling mill 31 to the slow cooling apparatus 42 can be decreased to shorten the rolling time in the slow cooling.

EXAMPLE

(27) An example according to the invention will be described below. A rolling raw material to be a target (material to be rolled) is a steel material, which has a product thickness of 15 mm or 22 mm and a controlled-rolling reduction of 65% as shown in the following Table 1. That is, a controlled-rolling start thickness is 43 mm or 63 mm. Also, a controlled-rolling start temperature is 880° C. In Comparative Examples 1 and 2 using a line shown in FIG. 1, the rolling raw material is heated to 1170° C. in a continuous heating furnace 1 and then rolled by a rough rolling mill group 3 to a controlled-rolling start thickness shown in Table 1 to form a sheet bar 10, which is subjected to rolling by a finish rolling mill group 6 after a surface temperature of the sheet bar 10 is confirmed to be 880° C.±5° C. by means of a radiation thermometer 33. When the temperature of the sheet bar 10 is higher than a target controlled-rolling start temperature, the sheet bar 10 is kept waiting between the rough rolling mill group 3 and the finish rolling mill group 6 under oscillation until a predetermined controlled-rolling start temperature is obtained.

(28) TABLE-US-00001 TABLE 1 Controlled-rolling Controlled-rolling start thickness start temperature Slow Heating Product (Thickness before (Finish rolling cooling Rapid cooling temperature thickness finish rolling) temperature) apparatus apparatus Example 1 1170° C. 15 mm 43 mm 880° C. Use Use Example 2 1170° C. 22 mm 63 mm 880° C. Use Use Comparative 1170° C. 15 mm 43 mm 880° C. No use No use Example 1 Comparative 1170° C. 22 mm 63 mm 880° C. No use No use Example 2

(29) In Examples 1 and 2, water cooling is performed in a rough rolling process by arranging a slow cooling apparatus 42 on an upstream side and a rapid cooling apparatus 41 on a downstream side of a reversible rolling mill 31 in a rough rolling mill group 3, as shown in FIG. 2. The rolling and water cooling in Example 1 are conducted according to a pass schedule described in Table 2, while the rolling and cooling in Example 2 are conducted according to a pass schedule described in Table 3. Similarly, rolling in Comparative Example 1 and rolling in Comparative Example 2 are conducted according to the pass schedule of Table 2 and the pass schedule of Table 3 respectively, and water cooling is not conducted in Comparative Examples.

(30) TABLE-US-00002 TABLE 2 Thickness after Rolling Rolling Type of rolling Rolling rolling Cooling Cooling pass mill No. mill direction mm pass apparatus 1 1 Reversible type Downstream 230 Absence — side 2 1 Reversible type Upstream 190 Presence Slow cooling side (twice) apparatus 3 1 Reversible type Downstream 150 Absence — side 4 1 Reversible type Upstream 120 Presence Slow cooling side (twice) apparatus 5 1 Reversible type Downstream 90 Absence — side 6 1 Reversible type Upstream 85 Presence Slow cooling side (twice) apparatus- 7 1 Reversible type Downstream 75 Presence Rapid side (twice) cooling apparatus 8 1 Reversible type Upstream 65 Absence — side 9 1 Reversible type Downstream 54 Presence Rapid side (once) cooling apparatus 10 2 Non-reversible Downstream 43 Absence — type side

(31) TABLE-US-00003 TABLE 3 Thickness Rolling Rolling Type of rolling Rolling after rolling Cooling pass mill No. mill direction mm Cooling pass apparatus 1 1 Reversible type Downstream 230 Absence — side 2 1 Reversible type Upstream 190 Presence(twice) Slow cooling side apparatus 3 1 Reversible type Downstream 160 Absence — side 4 1 Reversible type Upstream 130 Presence(twice) Slow cooling side apparatus 5 1 Reversible type Downstream 105 Absence — side 6 1 Reversible type Upstream 87 Presence(twice) Slow cooling side apparatus 7 1 Reversible type Downstream 72 Presence(once) Rapid cooling side apparatus 8 2 Non-reversible Downstream 63 Absence — type side

(32) In the rapid cooling apparatus 41 is used a group jet cooling apparatus constructed by arranging a plurality of round tube nozzles with a hole diameter of 5 mm at a pitch of 60 mm in a transportation direction (rolling direction) and a widthwise direction, in which a volume density of cooling water is 2500 L/min.Math.m.sup.2. In the slow cooling apparatus 42 are used a hairpin type pipe laminar cooling apparatus disposed at an upper face side of the sheet bar 10 and a spray cooling apparatus disposed at a lower face side of the sheet bar 10, in which a volume density of cooling water is 800 L/min.Math.m.sup.2. Further, a rolling rate and a rate passing through the cooling apparatus are controlled so as to render the surface temperature of the sheet bar 10 during the cooling into not lower than 600° C.

(33) In Table 4 are shown results obtained by actually rolling the rolling raw materials of Examples 1 and 2 and Comparative Examples 1 and 2 under the aforementioned conditions. Example 1 is a case where the product thickness is 15 mm, in which a waiting time before the finish rolling mill group 6 is about 10 seconds and a total of the waiting time and the rough rolling time is 462 seconds. Moreover, the waiting time of 10 seconds is a time required for confirming a temperature by means of a radiation thermometer 33 before the finish rolling mill group 6, so that a real waiting time is not caused. In Comparative Example 1, the rolling is performed according to the same rolling pass schedule as in Example 1, but the cooling apparatuses 41 and 42 proposed in the present invention is not used, so that a temperature of the sheet bar 10 when arriving at the finish rolling mill group 6 is 948° C., which is higher by 68° C. than a target temperature of 880° C., and hence the sheet bar is kept waiting (air cooled) for 95 seconds before the finish rolling mill group 6 until the target temperature is obtained. A total of the waiting time and the rough rolling time is 516 seconds, which is longer by 54 seconds than that in Example 1.

(34) TABLE-US-00004 TABLE 4 Waiting Rough rolling Temperature time time (take out Waiting at entry side of before from heating time + Rough Use of finish rolling mill finish furnace - rough rolling pass cooling On Rolling rolling before finish rolling schedule apparatus arrival start mill rolling) time Example 1 Table 1 Use 887° C. 881° C. 10 sec 452 sec 462 sec Example 2 Table 2 Use 883° C. 882° C. 10 sec 446 sec 456 sec Comparative Table 1 No use 948° C. 882° C. 95 sec 421 sec 516 sec Example 1 Comparative Table 2 No use 989° C. 881° C. 221 sec  356 sec 576 sec Example 2

(35) Example 2 is a case where the product thickness is 22 mm. The waiting time before the finish rolling mill group 6 is about 10 seconds as in Example 1, and a total of the waiting time and the rough rolling time is 456 seconds, which is approximately the same rolling time as in Example 1. Moreover, the waiting time of 10 seconds is a time required for confirming a temperature by means of a radiation thermometer 33 before the finish rolling mill group 6, so that a real waiting time is not caused.

(36) In Comparative Example 2, the rolling is conducted according to the same rolling pass schedule as in Example 2. However, the cooling apparatuses 41 and 42 proposed in the present invention are not used in Comparative Example 2, so that a temperature of the sheet bar 10 when arriving at the finish rolling mill group 6 is 989° C., which is higher by 109° C. than a target temperature of 880° C., and hence the sheet bar is kept waiting (air cooled) for 221 seconds before the finish rolling mill group 6 until the target temperature is obtained. A total of the waiting time and the rough rolling time is 576 seconds, which is longer by 120 seconds than that in Example 2.

(37) From the above experimental results, it has been confirmed that a time from when the sheet bar is taken out from the heating furnace to when the finish rolling is started is shortened by 54 seconds in the case of the material for the product thickness of 15 mm and by 120 seconds in the case of the material for the product thickness of 22 mm by arranging the rapid cooling apparatus 41 and the slow cooling apparatus 42 in the rough rolling mill group 3 and properly using the rapid cooling and the slow cooling in accordance with the thickness of the sheet bar 10.

(38) The invention is described based on the above illustrated examples. However, the invention is not limited thereto, so that proper modifications and addition may be performed within a scope described in claims. For example, the cooling by the rapid cooling apparatus 41 and the slow cooling apparatus 42 may not be performed in connection with all of odd number-th or even number-th rolling passes in the reversible rolling mill 31. When the temperature dropping quantity by the water cooling is large and the temperature when arriving at the finish rolling mill falls below the predetermined start temperature of the finish rolling, water cooling in arbitrary pass may not be performed. In the above explanation, the slow cooling apparatus 42 is arranged on the upstream side of the most downstream reversible rolling mill 31 viewing in the rolling direction, and the rapid cooling apparatus 41 is arranged on the downstream side thereof. However, the rapid cooling apparatus 41 may be arranged on the upstream side of the reversible rolling mill 31 and the slow cooling apparatus 42 may be arranged on the downstream side thereof.

INDUSTRIAL APPLICABILITY

(39) According to the invention, hot-rolled steel strips can be produced efficiently while preventing the temperature of the surface layer of the sheet bar from falling below a phase transformation temperature during the cooling conducted prior to the controlled-rolling and decreasing a time required up to starting the controlled-rolling.

DESCRIPTION OF REFERENCE SYMBOLS

(40) 1 continuous heating furnace

(41) 2 sizing press

(42) 3 rough rolling mill group

(43) 4 edger

(44) 5 crop shear

(45) 6 finish rolling mill group

(46) 7 runout table

(47) 8 coiler

(48) 10 sheet bar

(49) 31 reversible rolling mill

(50) 32 non-reversible rolling mill

(51) 33 radiation thermometer

(52) 41 rapid cooling apparatus

(53) 42 slow cooling apparatus

(54) 51 rolling pass schedule preparing apparatus

(55) 52 cooling pass schedule preparing apparatus