1. Field of the Invention
This invention relates generally to continuous hot rolling bar mills, and is concerned in particular with a system and method for delivering the hot rolled products of such mills to a cooling bed.
2. Description of the Prior Art
In modern bar mills currently in operation, hot rolled bar products exit the last mill stand, and are subjected to cooling by being passed through one or more water boxes. The bar products are then subdivided into bar segments by a dividing shear, which includes a switching mechanism for alternately directing the bar segments to one or the other of two downstream delivery paths leading to the cooling bed. Pinch roll units, friction pads, or the like serve to decelerate the bar segments traveling along the delivery paths, with the result that the bar segments gradually slide to a halt before being laterally transferred onto the cooling bed.
Relatively high tonnage rates can be achieved with this type of arrangement when the mill is rolling larger product sizes, e.g., those having diameters above about 10.0 to 12.0 mm. These larger products have enough column strength to resist buckling as they are being pushed through the water boxes at relatively high mill delivery speeds on the order of 10 to 30 m/sec.
However, as product sizes decrease, so do their column strengths decrease, with the result that mill delivery speeds must be reduced in order to avoid buckling when pushing the smaller product sizes through the water boxes.
Thus, for example, a single strand mill rolling 8.0 mm rod for delivery to a laying head can operate at a delivery speed of 60 m/sec or greater, yielding a capacity of 85 tons/hour. However, a similar mill rolling 8.0 mm bar for delivery to a cooling bed must necessarily roll at a significantly reduced delivery speed of about 32 m/sec with a reduction in capacity to about 45 tons/hour. The reduced delivery speed for bar products is due in large part to the inability of conventional bar handling systems to bring faster moving products to a halt before they are transferred laterally onto the cooling bed.
An objective of the present invention is to increase the tonnage rate at which mills are able to roll bar products, in particular smaller product sizes, e.g., those having diameters smaller than about 12.0 mm.
A companion objective of the present invention is to raise the speed at which the smaller bar products are delivered from the mill, and to then decelerate such bar products before they are cooled in the water boxes prior to being delivered to the cooling bed.
In accordance with the present invention, hot rolled bar products are subdivided by a dividing shear into bar segments, and the bar segments are alternately directed to one or the other of two downstream intermediate paths. A switch on each intermediate path then alternately directs the bar segments to one or the other of two downstream delivery paths leading to the cooling bed. The bar segments traveling along the four delivery paths are decelerated, preferably in at least two stages. The first deceleration stage operates to slow the bar segments to an intermediate speed lower than the speed at which the bar products are delivered from the mill, and the second deceleration stage operates to further slow the bar segments to a lower speed suitable for delivery to the cooling bed. The bar segments are cooled between the first and second deceleration stages while they are traveling at the intermediate speed.
With reference initially to FIGS. 1 and 2A–C, a system in accordance with the present invention is shown between the last roll stand 10 of a continuous hot rolling bar mill and a conventional carryover cooling bed 12. Bar product exiting from roll stand 10 along path PA is passed through a series of water boxes 14, after which it is subdivided into bar segments by a dividing shear 16. The shear 16, which can be of a conventional design known to those skilled in the art, includes a switch mechanism which alternately directs the subdivided bar segments to one or the other of two downstream intermediate paths PB, PC. A switch 18 on intermediate path PB then serves to alternately direct the bar segments to one or the other of two downstream delivery paths PD, PE, and a switch 20 on intermediate path PC similarly directs product segments alternately to one or the other of two downstream delivery path PF, PG. The side-by-side sets of delivery paths PD, PE and PF, PG lead through a series of water boxes 22 to pinch roll units 24, 26, then around a side loop defined in part by two opposed 180° curves C1, C2. Curve C1 is partially formed by a removable guide section 28. The side loop includes water boxes 30, and at curve C2, the two sets of delivery paths PD, PE and PF, PG are brought into vertical alignment before continuing to pinch roll units 32, 34 preceding the cooling bed 12.
With reference to
As can best be seen in
The pinch roll units 24, 26 are similarly constructed, but arranged slightly differently for alignment with the laterally disposed and vertically staggered guide paths.
An exemplary operation of the above-described system will now be further described with reference to the delivery to a cooling bed of a 8.0 mm diameter bar product exiting from the last roll stand 10 at a relatively high speed of 60 m/sec. and at a temperature of about 950–1050° C. The water boxes 14 are shut down, allowing the bar product to pass freely therethrough to the shear 16 where it is subdivided into successive bar segments. The switch mechanism of the shear alternately directs the bar segments to intermediate paths PB, PC. Bar segments traveling on path PB are then be alternately directed by switch 18 to delivery paths PD, PE, and bar segments traveling on intermediate path PC are likewise alternately directed by switch 20 to delivery paths PF, PG.
Pinch roll units 24 and 26 then operate to initially decelerate the bar segments to a lower intermediate speed of about 30 m/sec. The bar sections are directed by the curved guide section 28 around the side loop and through the water boxes 30. The linear distance between the pinch roll units 24, 26 and the water boxes 30 is preferably less than the length of the bar segments. Thus, the bar segments enter the water boxes 30 at a beneficially reduced speed and while they are still being acted upon by the pinch roll units 24, 26. The water boxes 30 operate to cool the bar segments down to about 500–600° C. before they negotiate curve C2. The pinch roll units 32, 34 then operate to further decelerate the bar segments to a speed of about 3–8 m/sec., which will allow the bar segments to slide to a halt at the entry end of the cooling bed 12. From here, transfer mechanisms (not shown) operate to shift the bar segments laterally onto and across the cooling bed where they undergo further cooling before reaching the delivery side of the bed.
Of particular importance to the present invention is the provision of multiple delivery paths for the successive bar segments exiting from the dividing shear 16 coupled with multiple delivery paths for the products passing through the switches 18, 20. In the preceding example, successive bar segments would be subjected repeatedly to the following sequence:
Only every fourth bar segment is directed to each delivery path, thus allowing ample time and space along each delivery path for one bar segment to begin decelerating before the next bar segment is received.
As shown in
In this operational mode, the increased column strength of the larger diameter product and the slower delivery speed of the mill will allow cooling to take place in the water boxes 22. Two stage deceleration will then take place, initially by the pinch roll units 24, 26 and then by the pinch roll units 32, 34.
It will thus be seen that the system of the present invention is extremely flexible in that it can accommodate a wide range of products at beneficially high tonnage rates. Smaller diameter products, e.g., those ranging in diameter from 6.35 to 12.0 mm can be handled at relatively high mill delivery speeds on the order of 60 to 32 m/sec. by passing freely through the water boxes 22 and undergoing initial deceleration by pinch roll units 24, 26 before cooling is effected in water boxes 30. Larger diameter products exceeding 12.0 mm in diameter and exiting the mill at slower speeds below about 30 m/sec. can be cooled in the water boxes 22 before initial deceleration by pinch roll units 24, 26.
As shown in
Number | Name | Date | Kind |
---|---|---|---|
2809545 | Norlindh | Oct 1957 | A |
3236084 | Kato | Feb 1966 | A |
3625043 | Neumann et al. | Dec 1971 | A |
3760931 | Buchheit | Sep 1973 | A |
3774433 | Pauels | Nov 1973 | A |
3831929 | Hellmer | Aug 1974 | A |
3951021 | Easter | Apr 1976 | A |
4176535 | Elsner et al. | Dec 1979 | A |
4250729 | Berz | Feb 1981 | A |
4307594 | Steinbock | Dec 1981 | A |
4363394 | Kirchhoff | Dec 1982 | A |
4528834 | Aoyagi et al. | Jul 1985 | A |
4554813 | Feldmann et al. | Nov 1985 | A |
4809530 | Wilson | Mar 1989 | A |
4884429 | Wilson | Dec 1989 | A |
5040440 | Harvey | Aug 1991 | A |
5174142 | Pong | Dec 1992 | A |
5423200 | Shore | Jun 1995 | A |
5893288 | Shore | Apr 1999 | A |
Number | Date | Country |
---|---|---|
0 319 317 | Dec 1988 | EP |
0 319 317 | Dec 1988 | EP |
0 319 317 | Jun 1989 | EP |
2118875 | Nov 1983 | GB |
06279215 | Nov 1994 | JP |
267114 | May 1983 | TW |
267114 | Sep 1983 | TW |
Number | Date | Country | |
---|---|---|---|
20050091818 A1 | May 2005 | US |