• 专利附录
  • 专利说明
  • 权利要求
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    • 专利摘要:
    The subject of the invention is a method for cooling an aluminum alloy rolling plate, after the metallurgical homogenization heat treatment of said plate and before its hot rolling, characterized in that the cooling of a value of 30 to 150 ° C is carried out at a rate of 150 to 500 ° C / h, with a homogeneity of less than 40 ° C throughout the treated portion of the tray. The invention also relates to the installation for implementing said method and said implementation.
    公开号:FR3024058A1
    申请号:FR1401679
    申请日:2014-07-23
    公开日:2016-01-29
    发明作者:Vincent Duhoux；Bruno Magnin；Daniel Bellot；Jose Roche；Pierre Aucouturier
    申请人:Constellium France SAS；
    IPC主号:
    专利说明:

    [0001] FIELD OF THE INVENTION The invention relates to the field of rolling plates or trays made of aluminum alloys. More specifically, the invention relates to a particularly fast, homogeneous and reproducible cooling process of the plate between the homogenization and hot rolling operations. The invention also relates to the installation or equipment for implementing said method. STATE OF THE ART The transformation of the aluminum alloy rolling plateaux resulting from the casting requires, before hot rolling, a metallurgical homogenization heat treatment. This heat treatment is operated at a temperature close to the solvus of the alloy, which is higher than the hot rolling temperature. The difference between the homogenization temperature and the hot rolling temperature is between 30 and 150 ° C, depending on the alloys. The plate must therefore be cooled between its exit from the homogenization furnace and its hot rolling. For reasons of productivity or metallurgical structure, especially to avoid certain surface defects on the finished sheet, it is very desirable to be able to carry out the cooling of the plate between its exit from the homogenization furnace and the hot rolling mill. fast. This desired plate cooling rate is between 150 and 500 ° C / h. Considering the high thickness of the aluminum alloy rolling platens, between 250 and 800 mm, the air cooling is particularly slow: the air cooling rate of a 600 mm plate The thickness is 3024058 2 between 40 ° C / h in calm air or under natural convection, and 100 ° C / h in ventilated air or forced convection. Air cooling therefore does not achieve the desired cooling rates. Cooling by means of a liquid or a mist (mixture of air and liquid) is much faster because the value of the exchange coefficient, known to those skilled in the art as the HTC (Heat Transfer Coefficient), between a liquid or a mist and the hot surface of the metal plate is significantly greater than the value of the same coefficient between the air and the plate.
    [0002] The liquid chosen alone or in the mist is for example water and, in this case, ideally deionized water. Thus, the HTC coefficient is between 2000 and 20000 W / (m2.K) between water and the hot tray while it is between 10 and 30 W / (m2.K) between air and the hot tray.
    [0003] On the other hand, the cooling by means of a liquid or fog usually generates in a natural way strong thermal gradients in the plateau: The non-dimensional number of Biot illustrates the thermal homogeneity of the cooling. It corresponds to the ratio of the internal thermal resistance of a body (internal heat transfer by conduction) to its surface thermal resistance (heat transfer by convection and radiation). HTC - D HTC being the exchange coefficient between the fluid and the plate, D, the characteristic dimension of the system, here the half thickness of the plate, X, the thermal conductivity of the metal, for example, for an aluminum alloy 160 W / (m2.K). If Bi "1, the system is practically isothermal, the cooling is uniform. If Bi >> 1, the system is thermally very heterogeneous and the plateau is the seat of strong thermal gradients.
    [0004] For a 600 mm thick plate, the Biot number is: Bi = 2 3024058 3 - Between 0.02 and 0.06 for cooling in calm or ventilated air. The number of Biot is small in front of 1, the plate is cooled isothermally. - Between 4 and 40 for cooling with water. The number of Biot is strong before 1, the plate is cooled very heterogeneously in its thickness.
    [0005] This heterogeneity is also reflected in the width of the plate, due to the effects of edges and edges, naturally cooler than the large faces of the plate. It is also reflected in the length of the plate, by wedge effect, naturally cooled according to the three faces constituting it. Thermal heterogeneity is a major handicap for cooling with a liquid or mist. It poses a problem not only for the following process, ie hot rolling, but it is also potentially harmful for the final quality of the product, namely the aluminum alloy sold in the form of coils or metal sheets. high mechanical characteristics. The devices known from the prior art do not seek to limit this heterogeneity of cooling. Cooling processes using a cooling liquid known in the prior art, especially for heavy plates, operate either by immersion in a tank or by passage in a spray box but without particular attention to control the thermal equilibrium of the product. Thus, these methods do not allow: Ni to obtain a uniform thermal field in the cooled plate Ni to ensure the reproducibility of cooling from one tray to another. Problem The objective of the invention is to correct all the major defects related to thick plate cooling processes of the prior art and to ensure: rapid cooling, at a speed of at least 150 ° C./h and consequently, ie from 30 to 150 ° C of cooling from a temperature of the order of 450 to 600 ° C 3024058 4 A homogeneous thermal field and mastered throughout the plateau The assurance of a perfect reproducibility from one thick plate to another. OBJECT OF THE INVENTION The subject of the invention is a method for cooling an aluminum alloy rolling plate of typical dimensions of 250 to 800 mm in thickness, 1000 to 2000 mm in width and 2000 to 8000 mm in thickness. length, after the metallurgical homogenization heat treatment of said platen at a temperature typically between 450 to 600 ° C depending on the alloys and before its hot rolling, characterized in that the cooling, a value of 30 to 150 ° C, is carried out at a speed of 150 to 500 ° C / h, with a thermal difference of less than 40 ° C over the entire cooled plate from its homogenization temperature. By thermal deviation is meant the maximum difference between temperatures recorded over the entire volume of the tray, or DTmax. Advantageously, the cooling is carried out in at least two phases: A first phase of spraying during which the plate is cooled in an enclosure comprising nozzle or spray nozzles of liquid or mist cooling under pressure, distributed in the upper and lower parts of said cell, so as to spray the two large faces, upper and lower of said plate, a complementary phase of thermal uniformization in still air, in a tunnel with interior walls reflective, a duration of 2 to 30 minutes depending on the tray size and the cooling value.
    [0006] Typically, this time is about 30 minutes for a total cooling of the order of 150 ° C from substantially 500 ° C, and a few minutes for a cooling of the order of 30 ° C. According to a variant of the invention, the phases of spraying and thermal uniformization are repeated, in the case of very thick trays and for an overall average cooling greater than 80 ° C. Most commonly, the coolant, including in a mist, is water, and preferably deionized water.
    [0007] According to a particular embodiment, the head and the foot of the tray, typically 300 to 600 mm at the ends, are less cooled than the rest of the tray, so as to maintain a head and a warm foot, a configuration favorable to the engagement of the plate during a reversible hot rolling.
    [0008] To this end, the cooling of the head and the foot can be modulated either by starting or extinguishing the nozzle or spray nozzles, or by the presence of screens preventing or reducing the spraying by said nozzles or nozzles. On the other hand, the sprinkling phases, and not thermal uniformization, can be repeated, and the head and foot of the tray, typically 300 to 600 mm at the ends, cooled differently than the rest of the tray at least in one of the spraying cells. According to a version according to the latter option, the first spraying pass is made with a zero heel, or continuous watering of the plate as in Figure 14, followed, without first phase of thermal uniformization, a second pass Spraying with a bead of a pair of ramps as in Figure 12, thereby significantly reducing the duration of the final phase of uniformization necessary for the thermal balancing of the plate. According to a preferred variant of the invention, the longitudinal thermal uniformity of the plate is improved by a relative movement of the plate with respect to the spraying system 20: deflected or back and forth from the plate facing a fixed spraying system or vice versa , displacement of the nozzles or nozzles relative to the plate. Typically, the tray scrolls horizontally in the spray cell and its running speed is greater than or equal to 20 mm / s, ie 1.2 m / min. Also preferably, the transverse thermal uniformity of the plate is ensured by modulating the spray in the width of the plate by igniting / extinguishing nozzles or nozzles, or screening said spray. The invention also relates to an installation for carrying out the method as above, comprising a spraying cell provided with nozzles or nozzle nozzles for liquid spraying or cooling mist under pressure arranged in the upper part. and low of said cell, so as to sprinkle the two large faces, upper and lower of said plate, 3024058 6 A uniformization tunnel to calm air out of the cell spray, in a tunnel to the inner walls and the roof in an internally reflective material, allowing a thermal uniformization of the plate by diffusion of heat in said plate, the core by heating the surfaces.
    [0009] According to a preferred embodiment: the liquid or cooling mist nozzles generate sprays or solid cone jets whose angle is between 45 and 60 °. The axes of the lower nozzles are normally oriented on the lower surface. the upper nozzle ramps are matched in the direction of travel of the tray. In the same pair, the upper ramps are inclined so that: - The jets of the two paired upper nozzle ramps are oriented in opposition to one another. - The jets have a normal border to the upper surface of the plate 15 - The overlap of the two jets is between 1/3 and 2/3 of the width of each jet, and preferably substantially half - The envelope of Two jets thus formed form an M profile. The upper and lower nozzle manifold pairs are placed substantially facing each other, so that the upper and lower spray lengths are substantially equal and vis-à-vis to face. Due to the pairing of the upper nozzles in opposition and the M profile of the jets, the spray length is controlled so as to promote the lateral evacuation of the liquid or mist sprayed on the upper face, by guiding it towards the banks of the plateau where it evacuated in the form of a cascade without touching the small faces of the plate thus allowing a very homogeneous cooling temperature in the longitudinal and transverse directions of the plate. As for the liquid alone or contained in the cooling mist, it can be recovered, typically in a container located under the facility, recycled and thermally controlled.
    [0010] According to an improved embodiment, the entire installation, spray cell and uniformization tunnel, is controlled by a thermal model coded on PLC, the thermal model determining the settings of the installation according to the temperature estimated by thermal measurement at the beginning of the spray cell and depending on the target output temperature, in general the hot rolling start temperature. According to an advantageous embodiment, the implementation of the installation comprises the following steps: 5 - Centering of the plate, at the entrance of the installation - Measurement of the upper surface temperature of the plate - Calculation by the automate, using the thermal model, the adjustments of the spray cell as a function of the target inlet temperature and the target output temperature, ie the target cooling of the plateau, including the determination of the 10 number of ramps activated, the number of nozzles open on the banks, the speed of the tray in the spray cell, the start and stop of the spray booms, and the hold time in the tunnel - Scrolling of the plate in the spray cell, upper and lower watering according to the calculations of the automaton 15 - Transfer of the plate of the spray cell to the tunnel of uniformization - Maintenance of the plate in the tunnel of uniformization hangs for a period determined by the PLC. DESCRIPTION OF THE FIGURES FIG. 1 represents a block diagram of the method according to the invention in one pass. The plate is removed from the homogenization furnace 1 at its homogenization temperature. It is transferred to the cooling machine, laterally centered and then its surface temperature is measured (2) by surface thermocouple, by contact or by means of an infrared pyrometer but which will be less accurate. The thermal model determines the setting of the spraying cell 3 (number of activated ramp pairs and plateau speed). Then the tray is treated in the spray cell. At its exit, it is dry and transferred (4) to a uniformization tunnel 5 for a duration determined by thermal model or the amplitude of the cooling undergone. At the end, it is transferred to the hot rolling mill 6. FIG. 2 represents a schematic diagram of the method according to the invention in two or more passes. When the target cooling amplitude is greater than 3024058 at 100 ° C, a single pass through the cooling machine may be insufficient. In this case, the plate is cooled a first time in the first spraying cell 3. Then, with or without passage in the intermediate uniformization tunnel 5, the plate is transferred into the second cooling machine 5 composed of the elements 6 , 7 and 8, where it undergoes a complete cycle: spraying cell then obligatorily uniformization tunnel 8. The duration of the last phase of uniformization depends on the thermal diffusivity of the material, therefore of the alloy, of the target cooling amplitude, and the severity of target thermal uniformity before hot rolling 9.
    [0011] Multipass cooling can also be achieved with a single machine, by successive passages. Figure 3 is a schematic plan of the sprinkler machine, seen in profile, the tray scrolling from left to right. It illustrates the arrangement of jets of liquid or mist sprayed on the plate, seen in profile, on the upper face and on the lower face. The upper and lower irrigation booms are paired and in pairs, to ensure a good uniformity of cooling in the thickness of the tray. The paired upper ramps are oriented in opposition, which ensures an evacuation of liquid or mist sprayed transversely to the plate. The axes of the lower nozzles are oriented normally to the lower surface of the tray, the liquid flows by gravity. Ramps of compressed air (1 to 4) surround the ends of the spray cell to prevent residual runoff of liquid on the tray outside said cell. Figure 4 illustrates the impact of the upper liquid or mist jets, in top view of the plate. The concentration of the surface flux of liquid or fog at the intersection of the jets in opposition is noted. This watering scheme is favorable to the evacuation of the liquid along this transverse line with a high surface flow rate. FIG. 5 shows the thermal kinetics of a 600 mm plate, calculated in the case of a mean cooling of 40 ° C., in one pass in the spray machine, for an AA3104 type alloy according to the defined designations. by the Aluminum Association in the Registration Record Series, which it publishes regularly. There are the evolutions of the minimum temperatures Tmin, maximum Tmax and average Tmoy in the plateau, as well as the maximum temperature difference in the whole volume of the plateau, over time (DTmax).
    [0012] FIG. 6 represents the thermal kinetics of a 600 mm plate, calculated in the case of an average cooling of 130 ° C., in two passes in the spray machine, for an alloy of the AA6016 type according to the designations defined by the Aluminum Association in the Registration Record Series, which it publishes regularly. There are the same evolutions of the minimum temperatures Tmin, maximum Tmax and average Tmoy in the plateau, as well as the maximum temperature difference in the whole volume of the plateau, over time (DTmax).
    [0013] FIGS. 7 to 9 illustrate three modes or strategies of watering in the direction of the spraying machine, with representation of the position of the nozzles on the spray bars, the spray machine being seen from the front in all case: Figure 7: Uniform thermal profile in the width of the plate Figure 8: Thermal profile with cold edges, created by a surplus of watering on the banks of the plate Figure 9: Thermal profile with hot banks, created by a deficit of watering on the banks of the plateau. FIG. 10 shows two modes or strategies of watering width of the same aluminum alloy plate 600 mm thick and 1700 mm wide, on the left a thermal profile in the cross-cold direction with cold edges. 11 nozzles in action, right a thermal profile with hot banks with 9 nozzles in action. FIG. 11 is the consequence on the thermal profile (temperature in ° C. as a function of the position in the cross direction, from the axis of the plate, in m) of these two modes of spraying.
    [0014] Figures 12 to 14 illustrate three examples of modes or strategies for triggering watering. Indeed, the thermal profile in the long direction of the plate is controlled by: The absence or very low runoff in the long direction of the plate, thanks to the mounting of the upper ramps in opposition, 30 The triggering and stopping of the watering each pair of ramps at a precise position of the plateau: this is the notion of watering heel.
    [0015] FIG. 12 corresponds to a management of the thermal profile in the long direction with hot ends, FIG. 13 with lukewarm ends and FIG. 14 with cold ends (with trickle at 1). Figure 15 illustrates the longitudinal thermal profiles (temperature in ° C 5 as a function of the position in the length L of the plate in m) for the three thermal management strategies of the ends of the above-mentioned plateau. In this example, the plate is alloy type AA6016, thickness 600 mm, its average cooling is 100 ° C in two passes, and the thermal uniformization box time is 10 min.
    [0016] FIGS. 16 to 18 illustrate the thermal field, in 3D visualization, of the same example, at the hot rolling inlet, for the three thermal management strategies of the above-mentioned ends of the plate, FIG. 16 with hot ends, FIG. lukewarm extremities and figure 18 with cold extremities. It can be seen that the sprinkler initiation strategy clearly makes it possible to control the longitudinal thermal profile of the plate. Figure 19 illustrates the thermal field of a 600 mm thick AA6016 type alloy tray cooled by approximately 50 ° C in one pass in the set sprayer with a watering heel of only ramp at the ends of the tray, according to Figure 13. This setting leads to a very uniform thermal field with slightly warmer ends, which is favorable to rolling. DESCRIPTION OF THE INVENTION The invention consists essentially of a cooling method using a cooling liquid or mist of an aluminum alloy rolling plate or platen, from 30 to 150 ° C in a few minutes, that is to say at an average cooling rate of between 150 and 500 ° C / hour. It consists mainly of two phases: A first phase of spraying the plate with a liquid or cooling mist, typically at the parade A second phase of thermal uniformization of the plate.
    [0017] During the first spraying phase, the plate is cooled in an enclosure comprising nozzles or nozzles for spraying fluid or mist that cools under pressure, typically water and preferably deionized. The nozzles or nozzles are distributed in the upper and lower parts of said cell, so as to spray the two large faces, upper and lower, of the plate. The option of a parade method limits the risk of hot spots related to the contacts between the plate and its support, usually consisting of cylindrical or conical rollers. The average plate cooling (ATmoy plateau) is controlled by the spraying time seen by each section of the tray. During this phase, the plateau is thermally very heterogeneous in its thickness, due to a high value of the Biot number. The homogeneity of cooling in the width of the plate is controlled by: a) the control of the watering width in the crosswise direction of the plate, by the number of nozzles activated or the use of screens; spraying favoring the lateral evacuation of the water sprayed on the upper face. Indeed, the coolant is guided to the banks of the plate and evacuated in the form of a cascade without touching the small faces of said plate. The cooling of the plate is therefore very homogeneous. This method consists in actually matching two ramps of nozzles, placed in opposition, as shown in particular in Figures 3 and 4. The homogeneity of cooling in the length of the plate is controlled by: c) The control of the beginning and the end of the sprinkling by triggering the spray bars at the desired position on the plateau or, again, by the use of screens. Thus the head and the foot of the tray may not be sprayed. This results in a plate with a head and a hot foot, which is favorable to its engagement during reversible hot rolling. D) The strong reduction of runoff in the long direction of the plate. This very low runoff is obtained by virtue of the characteristic b) above of the invention, favoring the lateral evacuation of the cooling liquid sprayed on the upper face of the plate.
    [0018] The spraying phase is therefore designed to limit the thermal heterogeneities in the three directions of the plateau. The invention makes it particularly possible to control the thermal profiles in the cross direction and in the long direction of the plate, which is very appreciable since any thermal gradients along these two large dimensions would be difficult to absorb in a short time. Follows the phase of thermal uniformization of the plate: After spraying, the plate is maintained a few minutes in a configuration of 10 low heat exchange with its environment. These thermal conditions allow the thermal uniformization of the plate, in a few minutes for cooling of less than 30 ° C and in about 30 minutes maximum for cooling of 150 ° C. This phase is essential to achieving the required thermal uniformity specifications. It makes it possible to reach a temperature difference of 15 DTmax of less than 40 ° C on a large plate. The invention can also be adapted to absolute values of high cooling. Thus, when the average cooling of the desired plateau is typically greater than 80 ° C, it is possible to cycle several times all the "spraying" and "uniformization" phases, reducing each "spraying-standardization" cycle. the average temperature of a very thick plateau. The method thus described ensures rapid and controlled cooling of a thick plate, in particular a rolling plate, made of aluminum alloy. It is also robust and avoids the known risks of local overcooling. The machine, or cooling system, itself consists of at least one spraying cell, typically horizontal to the parade, on the one hand and, on the other hand, at least one thermal uniformization tunnel.
    [0019] The spraying cell allows the implementation of phase 1 of the method described above.
    [0020] 3024058 13 The tray processing steps in this machine or plant are as follows: 1) Centering the tray, at the machine inlet 2) Measuring the upper surface temperature of the tray 5 3) Calculation by the PLC, using the thermal model, adjustments of the spray cell as a function of the inlet temperature and the target output temperature, ie the target cooling of the plateau, including the determination of the number of ramps of activated nozzles, the number of nozzles open on the banks, the speed of travel of the plate in the spray cell, start-ups and stops 10 of the spray bars, the holding time in the tunnel of uniformization 4) Scrolling the tray in the spray cell, upper and lower watering according to the calculations of the automaton. The spraying cell consists of ramps provided with nozzles or nozzles for dispensing under pressure the liquid or cooling mist. In the case where the latter is water, it is ideally deionized or at least very clean and not very mineralized, to avoid clogging of the nozzles and to ensure the stability of the heat transfer between the water and the plateau. The spraying machine can advantageously, for reasons of economy in particular, operate in a closed cycle, with for example a recovery tank placed under the spray machine. The selected coolant or coolant nozzles generate full cone sprays or jets with an angle between 45 and 60 ° (in the example: LECHLER brand 60 ° angled solid cone nozzles) . The axes of the nozzles of the lower ramps are oriented normally to the lower surface. The upper ramps are paired. In the same pair of upper ramps, the ramps are inclined so that: The jets of the two ramps are oriented in opposition to each other The jets have a normal border to the upper surface of the plate 30 two jets is between 1/3 and 2/3 of the width of the jet, and preferably substantially half - The envelope of the two jets thus formed is therefore a profile in M 3024058 14 The pairs of upper nozzle ramps and lower are placed substantially vis-à-vis, so that the upper and lower spray lengths are substantially equal and vis-à-vis. In the case of a parade treatment, the speed of travel of the tray is greater than or equal to 20 mm / s, ie 1.2 m / min. On leaving the spraying cell, the plate is transferred, for example by means of automatic trolleys, into one or more tunnel (s) of uniformity. The purpose of the tunnel is to minimize the heat transfer between the plate and the air, 10 which is favorable to a better thermal uniformity of the plate. This thermal uniformization takes place by diffusion of heat in the tray, the core warming the surfaces of the tray. The uniformization tunnel consists of vertical walls and a roof in an ideally reflective material on the inside of the tunnel.
    [0021] It avoids drafts around the tray, ensuring the absence of heat transfer by forced convection. In addition, it reduces natural convection heat transfer and limits radiative transfer if the walls are reflective. Finally, the machine or cooling system composed of the spraying cell 20 and the uniformization tunnel, is controlled by a thermal model coded on the automaton of the machine. The thermal model determines the settings of the machine according to the temperature at the start of the spray cell, or inlet temperature, and depending on the target output temperature, usually the rolling temperature.
    [0022] EXAMPLES Example 1: 40 ° C. uniform cooling of an AA3104 alloy plate.
    [0023] FIG. 5 illustrates the 40 ° C. cooling of an AA3104 alloy plate according to the designations defined by the "Aluminum Association" in the registration record series which it regularly publishes. The thickness of the plate 3024058 is 600 mm, its width 1850 mm and its length 4100 mm. The tray leaves the homogenizing oven at 600 ° C. The method of cooling the tray is the one-pass process described in FIG. 1 The tray is transferred to the cooling machine in 180 s. This transfer time comprises: the displacement of the plate between the exit of the furnace and the inlet of the cooling machine; the lateral centering of the plate; the measurement of the upper surface temperature of the plate; the calculation time; controller of the settings of the cooling machine (spray cell and tunnel). Then the tray scrolls in the spray cell, each point of the plate off ends (head and foot) is watered for 46 seconds. The surface flow rate of spraying is 500 l / (min.m2) on the two large faces of the plate. The watering heel is set at a ramp torque, as described in FIG. 12. At its exit from the spray cell, the plate is dry and transferred in 30 s to a uniformization tunnel for a duration determined by the thermal model coded in the automaton, here of 300 s, is 5 minutes. At the end, the tray is transferred to the hot mill, with thermal uniformity better than 40 ° C on the complete tray. The plateau surface temperature drops to about 320 ° C, while the core of the plateau remains almost isothermal during the spraying phase. Then, by diffusion of heat between the heart and the surface, the heart gives up heat to the surface, the tray thermally uniformizes. The thermal gap in the plateau (DTmax) is maximum at the end of the spraying phase, its value is 280 ° C for this configuration. It shrinks rapidly when the sprinkling of the plateau stops: in 6 minutes of waiting (transfer and then uniformization in the tunnel), the thermal deviation DTmax is reduced to less than 40 ° C.
    [0024] EXAMPLE 2: 135 ° C. uniform cooling of an alloy plate of the AA6016 type. Figure 6 illustrates the 135 ° C cooling of an AA6016 type alloy tray. The thickness of the plate is 600 mm, its width 1850 mm and its length 4100 mm. The tray leaves the homogenization oven at 530 ° C. The method of cooling the tray is the two-pass process described in Figure 2. The tray is transferred to the cooling machine in 100 s. This transfer time comprises: - the displacement of the plate between the furnace outlet and the inlet of the cooling machine - the lateral centering of the plate - the measurement of the upper surface temperature of the plate 15 - the calculation time by the automaton of the settings of the cooling machines. Then the tray scrolls in the spraying cell, each point of the plate off ends (head and foot) is watered for 51 seconds. The surface flow rate of spraying is 800 l / (min.m2) on the two large faces of the tray. The watering heel is set to a ramp, as described in FIG. 13. At its exit from the spraying cell 20, the plate is transferred in 60 s to the second spraying cell without passing, in this example, by the optional intermediate standardization tunnel. The plateau then undergoes a second watering, identical to the first: each point of the plateau out of ends undergoes a watering of 51 seconds, at the flow rate of 800 1 / (min.m2). On leaving the second spray cell, the tray is transferred to the uniformization tunnel in 30 seconds. The board waits several minutes in the standardization tunnel. At the end, the tray is transferred to the hot rolling mill, with thermal uniformity better than 40 ° C on the complete tray. The surface temperature of the tray drops to about 60 ° C. The core of the plate 30 remains almost isothermal during the first phase of spraying and then cools during the second phase of spraying. Then, by diffusion of heat between the heart and the surface, the heart gives up heat to the surface, the plate becomes thermally uniform.
    [0025] The thermal gap in the plateau (DTmax) is maximum at the end of each of the sprinkling phases, its value is about 470 ° C for this configuration. It decreases rapidly when the sprinkling of the plateau stops: the temperature difference DTmax plateau is 55 ° C after 13 minutes of waiting in the tunnel and becomes less than 40 ° C after 23 minutes spent in the tunnel . Example 3: Uniform cooling of 125 ° C of an alloy plate of the AA6016 type.
    [0026] The thickness of the tray is 600 mm, its width 1850 mm and its length 4100 mm. The tray leaves the homogenization oven at 530 ° C. The method of cooling the tray is the two-pass process described in Figure 2. The tray is transferred to the cooling machine in 100 s. This transfer time comprises: - the displacement of the plate between the furnace outlet and the inlet of the cooling machine - the lateral centering of the plate - the measurement of the upper surface temperature of the plate 20 - the calculation time by the automaton of the settings of the cooling machines. Then the tray scrolls in the spray cell, each point of the tray is watered for 51 seconds. The surface flow rate of spraying is 500 l / (min.m2) on the two large faces of the plate. The watering heel is zero, as described in FIG. 14. The plate is thus completely completely watered, which generates a cold end longitudinal thermal profile. At its exit from the spraying cell, the plate is transferred in 60 s to the second spraying cell without passing, in this example, through the optional intermediate uniformization tunnel. The plateau then undergoes a second watering, different from the first. The plateau, but this time out of the ends, undergoes a second watering of 51 seconds, at the surface flow rate of 500 l / (min.m2). The watering heel is of a pair of ramps, as described in FIG. 12. This adjustment tends to straighten the cold-end thermal profile, thus generating an almost flat longitudinal thermal profile at the outlet of the second spray cell. On leaving the second spray cell, the tray is transferred to the uniformization tunnel in 30 seconds. The plateau is waiting only 10 minutes in the tunnel of standardization. At the end, the tray is transferred to the hot rolling mill, with thermal uniformity better than 40 ° C on the complete tray.
    [0027] Example 3 shows that the judicious choice of watering heels makes it possible to significantly reduce the uniformization time after spraying. For a multi-pass cooling process, the choice of heels may be different from one pass to another. For a cooling process in 2 passes, the heel chosen in the first 10 passes wins to be opposite to the heel chosen in the second pass. In an optimized way and for a 2-pass cooling, a first pass with a zero heel (continuous watering of the plate) followed by a second pass with a heel of a pair of ramps can significantly reduce the uniformization time required for the thermal balancing of the plate. 15 20 25 30
    权利要求:
    Claims (17)
    [0001]
    REVENDICATIONS1. A method of cooling an aluminum alloy rolling plate of typical dimensions of 250 to 800 mm in thickness, 1000 to 2000 mm in width and 2000 to 8000 mm in length, after the metallurgical homogenization heat treatment of said tray to a temperature typically between 450 to 600 ° C depending on the alloys and before its hot rolling, characterized in that the cooling, a value of 30 to 150 ° C, is carried out at a speed of 150 to 500 ° C / h, with a thermal difference of less than 40 ° C over the entire cooled plate from its homogenization temperature.
    [0002]
    2. Method according to claim 1 characterized in that the cooling is carried out in at least two phases: A first phase of spraying during which the plate is cooled in an enclosure having nozzle ramps or nozzles for liquid spraying or pressurized cooling mist, distributed in the upper and lower parts of said cell, so as to spray the two large faces, upper and lower of said plate, A complementary phase of thermal uniformization with still air, in a tunnel with the walls reflective interior, lasting from 2 to 30 minutes depending on the tray format and the cooling value.
    [0003]
    3. Method according to claim 2, characterized in that the spraying and thermal uniformization phases are repeated, in the case of very thick trays and for overall average cooling greater than 80 ° C.
    [0004]
    4. Method according to one of claims 2 or 3, characterized in that the liquid, including in a fog, cooling is water, and preferably deionized water.
    [0005]
    5. Method according to one of claims 1 to 4, characterized in that the head and the foot of the tray, typically 300 to 600 mm at the ends, are cooled less than the rest of the tray so as to maintain a head and a warm foot, favorable configuration for the engagement of the plate during a reversible hot rolling. 5
    [0006]
    6. Method according to one of claims 2 to 5, characterized in that the cooling of the head and foot is modulated by the start or the extinction of the nozzle or spray nozzles ramps.
    [0007]
    7. Method according to one of claims 2 to 5, characterized in that the cooling of the head and foot is modulated by the presence of screens.
    [0008]
    8. Method according to one of claims 2 to 7, characterized in that the sprinkling phases, and no thermal uniformization, are repeated, and in that the head and the foot of the tray, is typically 300 to 600 mm at the ends, are cooled differently than the rest of the tray at least in one of the spraying cells.
    [0009]
    9. A method according to claim 8, characterized in that the first spraying pass is carried out with a zero heel, ie continuous watering of the plate, followed, without first thermal uniformization phase, a second pass of spraying with a heel of a pair of ramps as in Figure 12, thus significantly reducing the duration of the final phase of uniformization necessary for the thermal balancing of the plate. 25
    [0010]
    10. Method according to one of claims 2 to 9, characterized in that the longitudinal thermal uniformity of the plate is improved by a relative movement of the plate relative to the sprinkler system: parade or back and forth of the tray facing a stationary sprinkler system or vice versa. 30
    [0011]
    11. The method of claim 10, characterized in that the tray scrolls horizontally in the spray cell and its running speed is greater than or equal to 20 mm / s, 1.2 m / min. 3024058 21
    [0012]
    12. Method according to one of claims 2 to 11, characterized in that the transverse thermal uniformity of the plate is provided by modulating the spray in the width of the plate by ignition / extinguishing nozzles or nozzles, or screening said aspersion. 5
    [0013]
    13. Installation for carrying out the method according to one of claims 1 to 12, characterized in that it comprises: A spraying cell provided with nozzle ramps or nozzles for spraying liquid or mist cooling under pressure disposed in the upper and lower parts of said cell, so as to spray the two large faces, upper and lower of said plate, a uniformization tunnel in calm air out of the cell spray, in a tunnel walls internal and to the roof in an internally reflective material, allowing a thermal uniformization of the plate by diffusion of heat in said tray, the core by heating the surfaces.
    [0014]
    14. Installation according to claim 13, characterized in that: The liquid nozzles or cooling mist of the spray cell generate solid cone jets whose angle is between 45 and 60 ° 20 The axes of the lower nozzles are oriented normally at the bottom surface The upper nozzle ramps are matched in the direction of the tray. In the same pair, the upper ramps are inclined so that: - The jets of the two paired nozzle ramps are oriented in opposition to each other. - The jets have a normal border to the upper surface of the plate - The overlap of the jets of the two paired ramps is between 1/3 and 2/3 of the width of each jet, and preferably substantially half. The envelope of the two jets thus formed constitutes an M profile. The pairs of upper and lower nozzle ramps are placed substantially opposite one another, so that the upper and lower spray lengths are substantially equal and vis-à-vis. 3024058 22
    [0015]
    15. Installation according to one of claims 13 or 14, characterized in that the coolant is recovered after spraying, typically in a container located under the facility, recycled and thermally controlled. 5
    [0016]
    16. Implementation of the installation according to one of claims 13 to 15, characterized in that the entire installation, spraying cell and uniformization tunnel, is controlled by a thermal model coded on PLC the thermal model determining the settings of the plant as a function of the temperature estimated by thermal measurement at the beginning of the spray cell and depending on the target output temperature, in general the hot rolling start temperature.
    [0017]
    17. Implementation of the installation according to claim 16, characterized in that it comprises the following steps: - Centering of the plate at the entrance of the installation - measurement of the upper surface temperature of the plate - Calculation by the PLC, using the thermal model, of the settings of the spraying cell as a function of the inlet temperature and the target output temperature, ie the target cooling of the plateau, including the determination of the number of ramps activated, the number of nozzles activated in banks, the speed of travel of the plate in the spraying cell, the start and stop of the spray booms, and the holding time in the tunnel d standardization - Scroll of the plate in the spray cell, upper and lower watering according to the calculations of the automaton 25 - Transfer of the plate of the spray cell to the tunnel of uniformization - Maintenance of the plate in the tunnel of unifor during a period determined by the PLC. 30
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    同族专利:
    公开号 | 公开日
    DE15753101T1|2017-07-27|
    CA2954711A1|2016-01-28|
    KR102336948B1|2021-12-09|
    MX2017000483A|2017-07-28|
    EP3171996A1|2017-05-31|
    JP2017521260A|2017-08-03|
    CN106661648B|2020-01-07|
    US10130980B2|2018-11-20|
    EP3398696A1|2018-11-07|
    CN106661648A|2017-05-10|
    JP6585155B2|2019-10-02|
    TWI593476B|2017-08-01|
    WO2016012691A1|2016-01-28|
    RU2017105464A3|2018-11-29|
    EP3398696B1|2021-05-12|
    US20180236514A1|2018-08-23|
    US20170189949A1|2017-07-06|
    EP3171996B1|2018-04-11|
    SA517380746B1|2021-04-15|
    TW201622843A|2016-07-01|
    FR3024058B1|2016-07-15|
    KR20170039166A|2017-04-10|
    RU2017105464A|2018-08-27|
    BR112017000205A2|2017-10-31|
    RU2676272C2|2018-12-27|
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    法律状态:
    2015-07-17| PLFP| Fee payment|Year of fee payment: 2 |
    2016-01-29| PLSC| Publication of the preliminary search report|Effective date: 20160129 |
    2016-07-26| PLFP| Fee payment|Year of fee payment: 3 |
    2017-07-26| PLFP| Fee payment|Year of fee payment: 4 |
    2017-09-01| TP| Transmission of property|Owner name: CONSTELLIUM NEUF-BRISACH, FR Effective date: 20170728 |
    2018-07-26| PLFP| Fee payment|Year of fee payment: 5 |
    2019-07-26| PLFP| Fee payment|Year of fee payment: 6 |
    2020-07-28| PLFP| Fee payment|Year of fee payment: 7 |
    2021-07-26| PLFP| Fee payment|Year of fee payment: 8 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1401679A|FR3024058B1|2014-07-23|2014-07-23|METHOD AND EQUIPMENT FOR COOLING|FR1401679A| FR3024058B1|2014-07-23|2014-07-23|METHOD AND EQUIPMENT FOR COOLING|
    DE15753101.3T| DE15753101T1|2014-07-23|2015-07-10|COOLING DEVICE AND METHOD|
    KR1020177002831A| KR102336948B1|2014-07-23|2015-07-10|Cooling facility and method|
    EP18159076.1A| EP3398696B1|2014-07-23|2015-07-10|Cooling facility and method|
    CN201580040948.2A| CN106661648B|2014-07-23|2015-07-10|Cooling method and apparatus|
    JP2017503588A| JP6585155B2|2014-07-23|2015-07-10|Cooling method and cooling facility|
    US15/326,753| US10130980B2|2014-07-23|2015-07-10|Cooling facility and method|
    RU2017105464A| RU2676272C2|2014-07-23|2015-07-10|Method and cooling device|
    CA2954711A| CA2954711A1|2014-07-23|2015-07-10|Cooling facility and method|
    EP15753101.3A| EP3171996B1|2014-07-23|2015-07-10|Cooling facility and method|
    PCT/FR2015/051915| WO2016012691A1|2014-07-23|2015-07-10|Cooling facility and method|
    BR112017000205A| BR112017000205A2|2014-07-23|2015-07-10|cooling process and equipment|
    MX2017000483A| MX2017000483A|2014-07-23|2015-07-10|Cooling facility and method.|
    TW104123584A| TWI593476B|2014-07-23|2015-07-21|Cooling method and equipment|
    SA517380746A| SA517380746B1|2014-07-23|2017-01-19|Cooling Facility and Method|
    US15/962,657| US20180236514A1|2014-07-23|2018-04-25|Cooling facility and method|
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