COOLING SECTION WITH VALVES AND PRESSURE VESSELS FOR PREVENTING PRESSURE SHOCKS

Abstract

A device for cooling a metal rolling stock (1) rolled in a rolling train, having multiple cooling devices (4), to which water (5) is supplied via a respective branch line (7) and by means of which the water (5) is applied to the rolling stock (1). The branch lines (7) are equipped with a respective valve (8), by means of which the water flow flowing through the respective branch line (7) is adjusted. Each of the valves (8) is paired with a drive (9), via which the respective valve (8) is actuated. The cooling devices (4) form multiple groups, each of which is paired with a dedicated pressure vessel (10) in a proprietary manner. Each pressure vessel (10) is connected to a respective feed line (12) at a respective connection point (11), and the water (5) is supplied to the branch lines (7) of the cooling devices (4) of the corresponding group via said feed line. When viewed in the flow direction of the water (5), each connection point (11) is arranged upstream of the valves (8) of the respective group of cooling devices (4).

Claims

1. An apparatus for cooling metal stock rolled in a rolling mill, wherein the apparatus has a plurality of cooling devices, and to each of the cooling devices water is fed via a respective spur conduit and each of the spur conduits applies the water, wherein a valve sets the water stream flowing through the respective spur conduit and the valve is arranged in each of the spur conduits, wherein a respective drive for controlling the respective valve is assigned to each of the valves, the cooling devices form a plurality of the groups of the cooling devices and each group is assigned a dedicated pressure vessel, each respective pressure vessel is connected at a respective connection position to a respective feed conduit via which the water is supplied to the spur conduits of the cooling devices of the corresponding group, so that the respective connection position is arranged upstream, in the flow direction of the water, of the valves of the respective group of cooling devices.

2. The apparatus as claimed in claim 1, further comprising at least part of the groups of cooling devices in each case comprises only a single cooling device.

3. The apparatus as claimed in claim 1, further comprising the drives are configured as electric drives.

4. The apparatus as claimed in claim 3, further comprising the electric drives are configured as step motors.

5. The apparatus as claimed in claim 1, wherein each pressure vessel assigned to a respective group of cooling devices has a vessel volume and the vessel volume is in the range from n×20 l to n×200 l, where n is the number of cooling devices of the respective group.

6. The apparatus as claimed in claim 1, further comprising a respective flow resistance is arranged between the respective connection position and the respective pressure vessel.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0024] The above-described properties, features and advantages of the present invention and also the way in which these are achieved will become clearer and more easily understood in connection with the following description of the working examples which are explained in more detail in conjunction with the drawings. Here, the drawings schematically depict:

[0025] FIG. 1 a rolling stand and a cooling section,

[0026] FIG. 2 part of a cooling section,

[0027] FIG. 3 a cooling section,

[0028] FIG. 4 a time profile of a fill level and

[0029] FIG. 5 a time profile of a volume stream,

[0030] FIG. 6 a time profile of a pressure.

DESCRIPTION OF THE EMBODIMENTS

[0031] In FIG. 1, stock 1 is rolled in a rolling mill. Only the last rolling stand 2 of a multistand rolling mill is depicted in FIG. 1. The stock 1 is often a flat stock, i.e. a strip or a rough sheet. However, the stock 1 can also have a different format. For example, it can be a profile or a bar-shaped stock 1. The stock 1 often consists of steel, sometimes of aluminum and in rare cases of a different metal or a corresponding alloy.

[0032] A cooling section 3 follows the rolling mill. The stock 1 is cooled in the cooling section 3. The cooling section 3 is thus an apparatus for cooling the metal stock 1 rolled in the rolling mill. The present invention will be explained in conjunction with the cooling section 3 depicted in FIG. 1, which cooling section follows the rolling mill. The term “cooling section” is thus used in the sense of the apparatus mentioned. However, the present invention can also be realized when the apparatus is arranged within the rolling mill, i.e. between the rolling stands 2 of the multistand rolling mill. Furthermore, it can also be realized when the apparatus is installed upstream of the rolling mill.

[0033] The cooling section 3 in FIG. 1 has a plurality of cooling devices 4. Water 5 is applied to the stock 1 by the cooling devices 4. The cooling devices 4 are generally configured as spray bars which apply the water 5 to the stock 1 over the entire width of the stock 1 (FIG. 2). The water 5 in its totality is fed to the cooling section 3 via a supply conduit 6. Within the cooling section 3, the water 5 is distributed until it enters spur conduit 7 via which the water 5 is fed to the respective cooling device 4. One (1) valve 8, which sets the amount of water 5 fed to the respective cooling device 4 per unit of time, is arranged in each of the spur conduits 7. There is thus a 1:1 assignment of cooling devices 4, spur conduits 7 and valves 8. The amount of water 5 which is fed per unit time to the respective cooling device 4 represents a respective water flow.

[0034] A total of eight cooling devices 4 are depicted in FIG. 1, with part of the cooling devices 4 applying the water 5 from above to the stock 1 and a further part of the cooling devices 4 applying the water 5 from below to the stock 1 in the depiction of FIG. 1. Furthermore, the cooling devices 4 are staggered one after the other in the transport direction x of the stock 1. However, these situations are purely illustrative. Thus, more or less than eight cooling devices 4 can also easily be present. It is also possible for the water 5 to be applied exclusively from above or exclusively from below to the stock 1 by means of the cooling devices 4. When the stock 1 is flat stock, it is also possible for a plurality of cooling devices 4 to be arranged next to one another in the width direction y of the stock 1, as depicted in FIG. 2. It is critical that the respective valve 8 by means of which the water stream flowing through the respective spur conduit 7 can be set is arranged in the respective spur conduit 7.

[0035] A drive 9 is assigned as an actuating device to each of the valves 8. In the depiction in FIG. 2, the drives 9 are configured as electric drives. The respective valve 8 is controlled by the respective drive 9. This is also the case for the valves 8 of FIG. 1. However, this is not shown in FIG. 1 in order not to overload FIG. 1. Due to the design of the actuating devices as electric drives, switching times of significantly less than 1 second, for example 0.2 second or below, can be realized for the valves 8. Furthermore, electric drives can be set precisely very quickly. This makes both rapid and precise setting of a respective valve position possible.

[0036] The electric drives can, for example, be configured as step motors. Step motors can be moved through 90° without problems in a time of less than 0.2 second. This angle corresponds to the angle of rotation of a conventional valve 8 between the completely closed position and the completely open position. The respective valve 8 can thus be changed from the completely closed position into the fully open position and vice versa in a time of 0.2 second and less. Furthermore, the adjustment in the case of a step motor usually occurs in angled steps which are (mechanically) significantly below 1°, for example 0.1° (or a similarly small angle). In this case, it is possible to change the respective valve 8 between the completely closed position and the fully open position in steps of 0.1° (or a similarly small angle). Furthermore, the control electronics of an electric drive is sufficiently simple and inexpensive. Wear and risk of failure are much lower than in the case of a pneumatic drive. The required encapsulation for protection against spray water and the like (for example of the protection type IP 65) can easily be realized. This applies both to the respective electric drive itself and also to the control electronics for the drive.

[0037] Regardless of the specific geometric arrangement of the cooling devices 4, the cooling devices 4 as depicted in FIG. 3 continue to form a plurality of groups. A dedicated pressure vessel 10 is assigned to each of the groups. The expression “assigned to a dedicated” is intended to mean that the respective pressure vessel 10 acts in conjunction only with the cooling devices 4 of the respective group. In particular, the respective pressure vessel 10 is connected at a respective connection position 11 to a respective feed conduit 12. Water 5 is supplied via the respective feed conduit 12 to the spur conduits 7 of the cooling devices 4 of the respective group. In the flow direction of the water 5, the respective connection position 11 is thus located upstream of the valves 8 of the respective group of cooling devices 4. On the other hand, the water 5 is not conveyed via the respective feed conduit 12 to the spur conduit 7 of other cooling devices 4. The respective connection position 11 is thus not located upstream, in the flow direction of the water 5, of the valves 8 of other groups of cooling devices 4. The pressure vessel 10 thus defines the respective group of cooling devices 4: all cooling devices 4 whose water 5 flows via the respective connection position 11 form one (1) group of cooling devices 4. All other cooling devices 4 do not belong to this group.

[0038] The respective connection position 11 for the respective pressure vessel 10 should be arranged as close as possible to the valves 8 of the respective group. When, as on the left-hand side of FIG. 3, the respective group of cooling devices 4 comprises only a single cooling device 4, the respective connection position 11 should thus be as close as possible to the valve 8 of this cooling device 4. When, as at the right-hand side of FIG. 3, the respective group of cooling devices 4 comprises a plurality of cooling devices 4, the respective connection position 11 should be arranged as close as possible to a distributor point 13 at which the feed conduit 12 branches for the first time to the cooling devices 4 of the respective group.

[0039] In the depiction in FIG. 3, part of the groups of cooling devices 4 in each case comprises only a single cooling device 4. This is specifically the case for the two cooling devices 4 shown at left in FIG. 3. In these cases, the respective feed conduit 12 is identical to the respective spur conduit 7. As an alternative, it is likewise possible for the groups of cooling devices 4 each to comprise a plurality of cooling devices 4. This is specifically the case for the two cooling devices 4 shown at right in FIG. 3. In these cases, the respective feed conduit 12 is located upstream of the respective spur conduits 7.

[0040] A definitive criterion for the arrangement of the pressure vessels 10 is the amount of water 5 which is present between the respective connection position 11 and the respective valves 8 or, in the case of a single downstream valve 8, the respective valve 8. This is because this amount of water cannot be diverted into the corresponding pressure vessel 10. This amount thus has to be directly and quickly stopped before the respective valves 8 when these valves 8 are closed quickly. In general, this is not critical when the distances of the respective valves 8 from the respective pressure vessel 10 is small enough, for example 10 m or less, in particular less than 5 m. This is intended to be made clear by an example involving a single valve 8.

[0041] It is assumed that the flow velocity of the water 5 in the corresponding spur conduit 7 is 3 m/s. The respective valve 8 is closed completely within 0.2 second. The water 5 then has to be slowed from 3 m/s to 0 m/s within 0.2 second. This involves an average acceleration of 15 m/s.sup.2, i.e. approximately 1.5 times the acceleration due to gravity. Furthermore, it is known that a 10 m high column of water generates a pressure of 1 bar. The same applies to a 10 m long column of water which is stopped at the acceleration due to gravity. It is further assumed that the distance from the respective connection position 11 to the respective valve 8 is 5 m. In this case, it is not necessary to stop a 10 m long column of water at 1.0 times the acceleration due to gravity, but instead a 5 m long column of water at 1.5 times the acceleration due to gravity. Thus, this column of water generates a pressure of 0.75 bar under the prevailing operating conditions on slowing from 3.0 m/s to 0 m/s in 0.2 second.

[0042] In the absence of the pressure vessels 10, on the other hand, rapid closure of a respective valve 8 would lead to a pressure shock since in this case the water 5 flowing in the feed conduit 12 would also have to be stopped if it is present upstream, in the flow direction of the water 5, of the respective connection position 11. However, such pressure shocks can be significantly alleviated by the pressure vessels 10 since in this case the water 5 flowing in the respective feed conduit 12 is diverted into the dedicated pressure vessel 10 assigned to the respective group of cooling devices 4.

[0043] As is generally known, pressure vessels 10 serve to equalize the water management. They should therefore be able, if required, to accommodate water 5 from the feed conduit 12 to which they are connected in the event of a rapid reduction in the water requirement and secondly be able to feed water 5 back into the feed conduit 12 in the case of a sudden increase in the water requirement. For the pressure vessels 10 to be able to accommodate and return this water 5, the pressure vessels 10 are, in the depiction in FIG. 3, each partly filled with water 5 and partly filled with air 14 during operation. In general, a fill level F of water 5 (see FIG. 4) of about 50% should be sought. However, some deviations, for example in the range from 40% to 60%, are quite possible. The pressure vessels 10 are thus designed to be partly filled with water 5 and partly with air 14 during operation.

[0044] To be able to set the respective fill level F, the pressure vessels 10 can, for example, have a respective air valve 15. Via the respective air valve 15, air 14 can be introduced into the respective pressure vessels 10 or air 14 can be discharged from the respective pressure vessel 10. In the simplest case, the respective air valve 15 is a manually operated nonreturn valve (for example like the valve of a bicycle or another road vehicle having pneumatic tires). In this case, the respective pressure vessel 10 preferably has a fill level indicator and/or a pressure indicator. The fill level indicator can, for example, be a simple sight glass, and the pressure indicator can be a conventional pressure gage. As an alternative or in addition, the respective air valve 15 can be able to be controlled by a control device (not shown) of the cooling section 3. In this case, the respective air valve 15 is preferably divided into two valve paths, with one of the two valve paths being connected with a compressed air supply for introducing additional air 14 into the respective pressure vessel 10 and the other of the two valve paths having an outlet to the surroundings for letting air 14 out of the respective pressure vessel 10. Furthermore, the respective fill level F and/or the pressure prevailing in the respective pressure vessel 10 are in this case preferably measured by instrumentation and transmitted to the abovementioned control device.

[0045] The water moving in the respective feed conduit 12 is thus slowed gently by the respective pressure vessel 10. Due to the fact that the groups of cooling devices 4 are generally relatively small, usually not more than from six to ten cooling devices 4, the pressure vessels 10 can also be made relatively small. This is explained below in conjunction with FIG. 4 to 6 showing an embodiment in which the respective group of cooling devices 4 comprises only a single cooling device 4. However, the associated explanations also apply when the respective group of cooling devices 4 comprises a plurality of cooling devices 4. In this case, the explanations below have to be modified so as to assume uniform operation of the valves 8 of the respective group.

[0046] When the respective valve 8 is fully open, a respective volume flow V of water 5, for example 100 liters per second, travels in the respective feed conduit 12, which in the case of a group having a single cooling device 4 is identical to the spur conduit 7. This state is shown at left in FIG. 5. The fill level F is initially about 50% in the depiction in FIG. 4. The respective pressure vessel 10 is thus filled to an approximately equal extent with water 5 and air 14.

[0047] At a particular point in time t0, the corresponding valve 8 is moved from the fully open position into the completely closed position. The movement from the fully open position into the completely closed position is carried out as quickly as possible, for example in a time of 0.1 second or 0.2 second. In order to be able to explain the dimensioning of the respective pressure vessel 10 better, it will be assumed in the following that the closure of the corresponding valve 8 occurs completely abruptly, so that the time required for closure can be disregarded.

[0048] If the respective pressure vessel 10 were not present, a high pressure shock would occur on closure of the respective valve 8 since the respective volume flow V travelling in the respective feed conduit 12 would have to be decreased abruptly to zero. However, owing to the respective pressure vessel 10, the respective volume flow V can be diverted into the respective pressure vessel 10. In this way, the respective pressure vessel 10 is filled to beyond its previous fill level F. As a result of the filling of the respective pressure vessel 10, the air 14 present in the respective pressure vessel is compressed, so that the air pressure there is increased. The increased air pressure provides an increasing resistance to further introduction of water 5 into the respective pressure vessel. The respective fill level F therefore does initially increase after the point in time t0, but then attains a maximum and subsequently decreases again. A slight, usually substantially damped, oscillation may occur. This can be seen most readily from the change in sign of the volume flow in FIG. 5. The maximum fill level F is usually attained within 1 second, sometimes even within a shorter time of, for example, only 0.5 second.

[0049] At the point in time t0 itself, i.e. at the beginning of slowing of the flow, the entire respective volume flow V has to be accommodated, as indicated in the depiction in FIG. 4. If the respective volume flow V were to be maintained unchanged, the respective pressure vessel 10 would be completely filled after, for example, 0.5 second from the point in time t0, as indicated in FIG. 4. 50% of the volume of the respective pressure vessel 10 would thus flow into the respective pressure vessel 10 in 0.5 second. Accordingly, 100% of the volume of the respective pressure vessel 10 would flow into the respective pressure vessel 10 in 1 second. As can be seen from the depiction in FIG. 4, the ratio of the respective vessel volume (unit: liter or cubic meter) and the respective volume flow V (unit: liters/second or cubic meters/second) is thus 1 second. Nevertheless, certain deviations from this value (1 second) are possible. However, the abovementioned ratio should be in the range from 0.2 second to 2.0 seconds. In practice, this corresponds to a volume of from 20 l to 200 l, usually in the range from 50 l to 125 l, in particular about 100 l, in the case of a single cooling device 4. If the group comprises a plurality of cooling devices 4, the volume values mentioned have to be scaled accordingly.

[0050] Owing to the resistance offered by, calculated from the respective connection position 11, the respective spur conduit 7 and the respective cooling device 4, a respective conduit pressure p0 prevails in the region of the respective connection position 11 in the state initially assumed in FIGS. 4 and 5, i.e. when the corresponding valve 8 is in the fully open position. The respective conduit pressure p at this time thus has the value p0. This is shown at left in FIG. 6. Since an equilibrium state prevails before the point in time t0, the air 14 in the respective pressure vessel 10 is likewise under the pressure p0. At the point in time t0, i.e. at the point in time of closure of the respective valve 8, the entire volume flow V travelling in the respective feed conduit 12 firstly has to be diverted into the respective pressure vessel 10. The volume flow V through the feed conduit 12 brings about a pressure drop 5p, measured at the respective connection position 11 and shown in FIG. 5, at a respective flow resistance 16 located between the respective connection position 11 and the respective pressure vessel 10 on its way from the respective connection position 11 to the respective pressure vessel 10. The pressure drop 5p is preferably at least half the respective conduit pressure p0. Accordingly, the respective conduit pressure p has to increase abruptly to a value corresponding approximately to from 1.4 times to 1.6 times the value p0, i.e. approximately 1.5 times. In absolute values, the pressure drop 5p is in practice usually in the order of 1 bar. The respective conduit pressure p then decreases again.

[0051] The respective flow resistance 16 can be set by appropriate dimensioning of the respective connecting conduit between the respective connection position 11 and the respective pressure vessel 10, in particular by dimensioning of the cross section of the total respective connecting conduit or the cross section of a section of the respective connecting conduit. An oscillation tendency, in particular, is suppressed and damped by suitable dimensioning of the flow resistance 16.

[0052] The present invention has many advantages. In particular, pressure shocks can be avoided even when the valves 8 are switched very quickly (with switching times far below 1 s). The influence of the pressure vessels 10 on the amount of water actually fed to the cooling devices 4 can be taken into account using an appropriate model of the cooling section 3 or be equalized in a simple way by basic automation of the cooling section 3. Furthermore, pressure oscillations within the hydrodynamic system (consisting of the supply conduit 6, the feed conduits 12 and the spur conduits 7) are reduced by the pressure vessels 10. This simplifies the control of pumps that convey the water 5. This applies particularly when pressure measurements are employed for regulating the pumps. Furthermore, pressure decreases on opening of valves 8 are also reduced, since in this case water 5 is fed from the pressure vessels 10 into the corresponding feed conduits 12. The configuration of the drives 9 as electric drives makes reliable and fast actuation of the valves 8 possible in a simple way.

[0053] Although the invention has been illustrated and described in detail by the preferred working example, the invention is not restricted by the examples disclosed and other variants can be derived therefrom by a person skilled in the art without going outside the scope of protection of the invention.

LIST OF REFERENCE SYMBOLS

[0054] 1 Metal stock being rolled [0055] 2 Rolling stand [0056] 3 Cooling section [0057] 4 Cooling devices [0058] 5 Water [0059] 6 Supply conduit [0060] 7 Spur conduits [0061] 8 Valves [0062] 9 Electric drives [0063] 10 Pressure vessels [0064] 11 Connection positions [0065] 12 Feed conduits [0066] 13 Distributor point [0067] 14 Air [0068] 15 Air valves [0069] 16 Flow resistance [0070] F Fill level [0071] p, p0 Conduit pressure [0072] t0 Point in time [0073] V Volume flow [0074] x Transport direction [0075] y Width direction [0076] δp Pressure drop