Method of production and/or processing as well as winding an endless material of thermoplastic plastic with output of a quality signal as well as a takeup machine

Abstract: In such a process in which a quality signal Q is output as a function of a continuously measured process parameter, one selects a parameter of state of the forming package (33) as an indicative process parameter, one acquires same, a value derived therefrom, or the value varying with respect to time during the entire winding cycle of the formed packages (33), and one compares the values with a predetermined representative value or its tolerance range, so as to release a quality signal in the event of an undue deviation of the parameter of state or the derived value from the desired value. This [signal] may used to cause an alarm, to classify the production results of the continuously produced packages (33) and/or intervene in the process control, so as to counteract the detected deviations or tendencies to such deviations. To carry out the method, a suitable sensor winding head is described, which enables a continuous determination of the weight of packages (33) during the winding cycle.

Description: GB-A-2 243 573 describes a method of producing and/or processing as well as winding an endless material to a package with output of a quality signal according to the preamble of claim 1, wherein the contour of the package is measured and this value is used to find out how the thickness of the endless material has to be changed in order to obtain a package with an adequatly precious cylindrical contour. The invention relates to a method of producing and/or processing as well as winding an endless material of a thermoplastic substance as defined in the preamble of claim 1 as well as a takeup machine as claimed in claims 32 and 33. This method is known from EP-A-0 207 471 for texturing a yarn, and characterized in that from a continuously measured product parameter indications relating to the quality of the produced package or produced yarn are obtained for quality parameters which are not directly subject of the measuring. The known method is successfully applied to textured yarns which are produced by the false twist texturing method. Endless material in the meaning of the present invention are understood to be yarns, slit-film tapes, films, and foils. These endless materials are characterized in that they are produced continuously or need to be processed continuously, with a plurality of packages being produced one after the other from the continuously advancing strand. It is the object of the present invention to devise a method as described above, in particular for winding flat yarns, in particular yarns which are spun from manufactured fibers as endless synthetic filaments and wound in the spinning machine, in which a value representative of the quality of the end product is derived continuously, which value permits a classification of the end product and/or a control of the process. This solution is set forth in the characterizing portion of claim 1. The invention is based on the recognition that the buildup of the package on which the yarn is wound, is decisively influenced by the quality of the produced yarn such that the condition of the package as defined by one or more of its parameters of state represents a reliable indication as to the quality of the yarn at any instant of the winding cycle (winding of the yarn to a package). The special advantage of the invention in comparison with previously applied methods is that a parameter or the parameters of state of the package reflect on the one hand the course of the process and the actual situation of the process, but on the other hand also the condition of the product. As a result of acquiring a parameter or the parameters of state of the package and their output and evaluation as a quality signal, a binding indication is made with respect to the state of the process and the quality of the product. In particular it shows that the diameter progression over the entire or predetermined portions of the winding cycle and/or the diameter of the package at certain instants of the winding cycle is representative of an abundance of quality parameters of the yarn and/or the cross-wound package to be produced. It is also possible that derived values, for example, the layer thickness which forms on the tube or package at certain time intervals, the increase in diameter (derivation of diameter as a function of time), the time function of the diameter, coefficients of the time function, and others take the place of the package diameter. It is of advantage to square the value of the diameter as measured and to then draw the first derivative of that value (d 2 ). The advantage is, on the one hand, that by squaring the diameter regularity is improved and that, on the other hand, the derivative of this square is a constant if no irregularity occurs. The first derivative is proportional to the quantity of yarn wound in a given unit of time as long as no disturbances occur. By constant monitoring of this derivative it is, therefore, possible to control the proper functioning of the yarn production from extruder, spinning pump, spinning beam, on the like. In any event, a comparison occurs with predetermined representative values or representative courses or preset tolerance ranges/-courses (desired values, desired ranges, desired courses). These desired values are predetermined for yarns and cross-wound packages which are acceptable with respect to quality. As aforesaid, it is possible to surround the determined representative values/-courses with tolerance ranges, so that a quality signal is emitted only in the event of a deviation from the tolerance ranges. However, it is also possible to determine the exact consistency of the measured package diameter or the value derived therefrom with the corresponding representative value and to signal any deviation as a quality signal. With respect to claim 7 and the mean value introduced therein, the following explanation applies: The mean value is here not understood strictly in its mathematical sense. In practice, a mean value is rather formed in that the parameter of state or the value derived therefrom is supplied to a filter with a predetermined time constant. The selection of the time constant allows to predetermine to which number of measured values the mean value is related. Technically, however, other electronic components are also available to obtain a formation of a mean value, for example, a low-pass filter. The specific problem arises that in particular in the production and/or processing of yarns of a thermoplastic material very high winding speeds are applied, which amount in texturing machines already to more than 1000 meters per minute, and in spinning machines to more than 3000 meters per minute. The problem of determining the diameter, which arises therefrom as a result of the measuring technique, is advantageously solved at a constant surface speed of the takeup package by claims 21 and 22, and in the case of films and foils by claim 10. An additional or alternative indication can further be obtained from the suggestions of claims 13 and 15. The problems resulting therefrom with respect to the measuring technique are solved without contacting the endless material by claim 14. A further indicative package parameter to consider is in accordance with claims 16 and 17 the density of the package. The density is here defined as the quotient of the measured weight and the measured package diameter. In so far, this quotient is indicative of the distribution of the yarn mass over the diameter of the package at a constant length of the package, which remains unchanged during the winding cycle. As previously indicated, it is necessary to produce and/or process endless materials of a thermoplastic substance at a constant speed. This however relates not only to the linear speed of the material, but also to the quantity produced per unit time, which must remain constant. It is obvious that such measurements are very difficult to carry out. The problem is solved by claim 18 in that the package weight is continuously determined, and the course of the weight is observed during the winding cycle. A suitable measuring method is indicated in claim 19. A further suitable measuring method of determining the package weight is described in claim 20, by which the weight variation of the entire takeup machine is determined. To this end, it is also possible to measure the torque or the change of the torque which the package exerts with respect to a certain bearing point of the takeup machine. Such a method may be particularly useful, when the direct determination of the deformation of spindle or spindle bearing is so sensitive that also other disturbances, such as oscillations, superimpose upon the weight-specific deformation, and falsify the measuring result. The output quality signal may be released as an alarm signal and/or be used for identifying the quality of the produced package and/or be used as a signal for controlling the process. When emitted as alarm signal, the signal may be optical or acoustic or be output as a continuous graphic record. However, it may also be used for identifying the quality of the produced package in that the actually measured values or the values from the comparison of the measured values with the representative value are divided into quality classes and assigned to the respectively obtained product as a quality level. As a process control signal the quality signal may serve again to disconnect the machine or to control the yarn delivery speed, the yarn takeup speed, the spinning speed, and/or other process parameters, which are suitable for correcting the quality parameter which is by experience responsible for the deviation of the determined package diameter or the value derived therefrom from the corresponding representative value. Corresponding methods are subject matter of claims 23-31. These methods are characterized in that they enable an effective, but also sensitive influencing of process, product, and quality during the current process and current production. As previously indicated, the process control of the present invention has the advantage that it allows to correct the production process and/or processing method immediately and without time delay. In the past, this control had to be done by hand, the possibility of intervening directly in the process was nonexistent. Consequently, it was necessary to accept in the meantime an inferior production until a manual control was performed. Furthermore, there results the possibility of measuring continuously several parameters of state of the package and of controlling different process parameters with each of the parameters of state. There further results as an advantageous alternative possibility that the measured parameter of state or its deviation from the desired value is classified and several process parameters are controlled by classes, for example, that during the production of a yarn with considerable denier deviations, the pump speed is adjusted, and in the event of deviations which are below a certain limit, the withdrawal speed and/or the draw ratio are adjusted. Further, in multiposition textile machines it is possible to perform a comparison between machines, and to signal the deviation from a predetermined mean value or a predetermined tolerance zone to the mean value. Unless the plurality of the takeup positions are wound in the same timing cycle, a correction with respect to the different starting times of the winding cycle is necessary, since a diameter comparison is useful only when the comparison occurs at identical instants of the winding cycle, i.e., for example, at a certain time interval after the start of the winding cycle. To carry out the method of the present invention, it is necessary to solve the further problem of making available a takeup machine which cooperates with sensors which detect the selected parameter of state of the packages. Such a takeup machine is defined in claims 32 and 33. Both solutions are novel. A preferred embodiment of such a winding head which is designed and constructed as a weight sensor for the increasing package weight, is set forth in claim 34. This winding head is substantially supported along the line of its center of gravity, in particular mounted for pivotal movement, so that the weight of the winding head itself is balanced and does not influence the measured value determination of the package weight. In this sensor winding head, the measuring device in accordance with claim 35 is arranged preferably stationarily, and the action of force from a torque of the winding shaft with respect to the suspension of the winding head is measured continuously. Such sensor winding heads allow to provide a spinning system in accordance with claim 36, and a slit-film production line in accordance with claim 37, in each of which a continuous monitoring of production and quality as well as process control for optimizing the product quality is realized. In the following the invention is described with reference to the drawing, in which Figure 1 is a schematic view of a spinning system for filament yarns with the processing stages extrusion, drawing, and takeup; Figure 2 illustrates a yarn traversing mechanism with oppositely rotating blades and a measuring roll arranged on the package for determining the package diameter; Figure 3 illustrates the takeup portion of the spinning system of Figure 1 with means for determining the package weight; Figure 4 illustrates the yarn traversing mechanism of Figure 2 with an arrangement of the measuring roll for determining the package weight; Figure 5 shows the arrangement of Figure 3 for additionally determining and processing a signal indicating the length of the advancing yarn; Figure 6 shows a spinning system of Figures 1 and 5 with additional determination and processing of a signal for the yarn denier; Figure 7 shows the takeup portion of the spinning system with a winding head sensor for determining the change in weight of the package during the winding cycle; Figure 8 shows a further embodiment of a winding head with a weight sensor; Figure 9 is a schematic view of a slit-film production line with sensor winding heads and process control; Figure 10 is a schematic view of a wide-slot die with orifice adjustment; and Figure 11 shows a diagram of yarn tension developed over a predetermined period of time. Illustrated in the Figures are several embodiments which relate to the spinning of filament yarns. The following description of the spinning installation applies to all Figures. Special characteristics of the present invention, as they result from the individual embodiments, are then described separately. A filament yarn 1 is spun from a thermoplastic material. The thermoplastic material is supplied via a hopper 2 to an extruder 3 . The latter is driven by a motor 4 which is controlled by a motor control 49 . In extruder 3 , the thermoplastic material is melted. To this end, use is made of the elastic resilience (shearing energy) which is introduced to the material by the extruder. In addition, a heating system 5 , for example, in form of a resistance heater, is provided which is controlled by a heating control 50 . Through a melt line 6 which accommodates a pressure sensor 7 for measuring the melt pressure for a pressure-speed control of the extruder, the melt advances to a gear pump 9 which is driven by a pump motor 44 . The pump motor is controlled by a pump control 45 such that the pump speed is finely adjustable. The pump 9 delivers the melt flow to a heated spin pack 10 , the underside of which accommodates a spinneret 11 . From the latter, the melt exits in form of strands 12 of fine filaments. The strands of filaments advance through a cooling shaft 14 . In the latter an air current 15 is directed by blowing transversely or radially to the web of filaments 12 , thereby cooling the filaments. At the end of cooling shaft 14 , the web of filaments is combined to a yarn 1 by a spin finish application roll 13 and provided with a liquid spin finish. A delivery roll or godet 16 withdraws the yarn from cooling shaft 14 and spinneret 11 . The yarn loops several times about godet 16 . To this end a freely rotatable guide roll 17 in a crossed arrangement relative to godet 16 is used. The godet 16 is driven at a preadjustable speed by a motor 18 and frequency transmitter 22 . The withdrawal speed is by a multiple higher than the natural speed of exit of filaments 12 from spinneret 11 . Arranged downstream of godet 16 is a further draw roll or godet 19 with a further guide roll 20 . Both correspond in their arrangement to delivery roll 16 with guide roll 17 . For the drive of draw roll 19 a motor 21 with a frequency transmitter 23 is used. The input frequency of frequency converters 22 and 23 is uniformly preset by a controllable frequency transmitter 24 . In this manner, it is possible to adjust individually the speed of delivery roll 16 or draw roll 19 on frequency converters 22 and 23 . The speed level of draw roll 16 and draw roll 19 , however, is collectively adjusted on frequency converter 24 . From draw roll 19 , yarn 1 advances to a so-called "apex yarn guide" 25 and thence into a traversing triangle 26 . In Figure 1, a yarn traversing mechanism 27 in accordance with the illustration of Figure 2 is shown. This traversing mechanism employs oppositely rotating blades which traverse yarn 1 over the length of a package 33 . In so doing, the yarn loops, downstream of traversing mechanism 27 , about a contact roll 28 . The contact roll rests against the surface of package 33 , and serves to measure the surface speed of package 33 . The package 33 is formed on a tube 35 secured on a winding spindle 34 . Winding spindle 34 is driven by a spindle motor 36 and spindle control 37 such that the surface speed of package 33 remains constant. To this end, the speed of contact roll 28 freely rotatable about a shaft 29 is scanned as a controlled value by means of a ferromagnetic insert 30 and a magnetic pulse generator 31 . It should be noted that yarn traversing mechanism 27 may also be a standard cross-spiralled roll with a yarn guide traversing in a cross-spiralled groove over the range of traverse. In Figure 1, the diameter of package 33 is continuously measured as parameter of state or a value derived from the diameter. Likewise, the weight may be considered as such a value, which is however accompanied by factors of interference, such as density of the wind, enclosed air, crossing angle, and others. Therefore, it is not possible to consider the determined weight as an absolute value but only as a measured value which can be compared with a reference value. To determine the diameter, the speed of spindle 34 and the speed of contact roll 28 lying against the surface of the package are measured. To this end use is made of ferromagnetic inserts 30 , 38 both in spindle 34 and in contact roll 28 as well as corresponding pulse generators 31 , 39 . While the speed of contact roll 28 is simultaneously supplied as controlled value for the adjustment of spindle motor 36 via spindle control 37 , the speed of spindle 34 is also used to control yarn traversing mechanism 27 , which is not described in further detail. In addition, however, both signals are converted into diameter D in a computer unit 46 . In a preferred embodiment a multiplier stage may be provided for continuously forming the square of the diameter. Thereafter, the first derivative of the square is formed. As may be seen from Fig. 11 the first derivative of the value(d[D 2 ])/t theoretically has to be a constant. For this first derivative is proportional to the quantity of furnished yarn. But ideally the quantity of yarn produced per unit time in the production of synthetic filaments is absolutely constant. In Fig. 11, there is depicted a diagram of yarn tension developed over a predetermined interval. A disturbance in the tension of the yarn was deliberately introduced into the diagram, by interference with the winding speed v. In parallel thereto, the first derivative of value (D 2 ) was continuously recorded. As may be seen, as deviations in thread tension occured, the continuity of the first derivative was disturbed in noticeable fashion. By coordinating the deviations in thread tension and deviations in the first derivative D 2 certain errors in the production process may be determined. As shown in Fig. 1, the signal representative of the diameter or the signal derived therefrom - as described above - is then supplied simultaneously with a previously stored reference signal from a memory 47 to a comparison unit 48 . The difference signal of comparison unit 48 will then serve as output signal for quality Q . In the embodiment of Figure 3, the weight of package 33 is determined. For this reason, spindle 34 is resiliently mounted in a bearing. The spring-elastic deflection of the bearing is measured. To this end a weight sensor 52 is shown. In practice, the latter includes strain gauges which are arranged on such bearing parts which are deformable as a function of the weight of the package. The course of the weight is compared with a desired value course stored in memory 47 . In a comparison unit 48 , the difference value is formed and the quality signal Q is derived therefrom. The quality signal again can be used to influence one or several process parameters in the extrusion (box E in Figure 1), or the drawing (box D in Figure 1), or even the spindle control 37 . Figure 4 shows a modified arrangement of winding spindle 34 and contact roll 28 , which is preferred when determining the package weight and its change during the winding cycle. In this embodiment, an action of force of contact roll 28 superimposing and possibly falsifying the package weight is compensated in that contact roll 28 is pressed laterally against the surface of package 33 . In the embodiment of Figure 5, the denier of yarn 1 on package 33 is continuously measured. To this end, the package weight G is continuously measured on the one hand, as to which reference may be made to Figure 3. In addition, the length L of the yarn advancing to package 33 is measured by a linear measuring device 53 . The quotient of weight G and length L of the yarn wound on the package results in the denier. The generated output signal Q , as described above, is further processed. To this end, the actual value from computer 46 is again compared in comparison unit 48 with the desired value input in memory 47 . Illustrated in Figure 6 is that the denier measurement is corrected in addition by determining the applied spin finish. Spin finish application is here described as the quantity of liquid applied to the yarn. To perform this application, a device 13 (spin finish applicator) is used which is arranged in cooling shaft 14 . To determine the application of the spin finish, the motor 44 of metering pump 9 is provided with a speed sensor not shown. Since the pump is a metering pump in which the discharge is highly speed-dependent, output signal 55 represents the throughput very accurately. Output signal 55 (throughput signal) is supplied to a computer component 56 . The latter also receives in addition via a weight signal 57 the weight G which is determined by weight sensor 52 . The difference between the weight determined by weight sensor 52 and the throughput determined by the throughput sensor and integrated over the time results in the actual weight of the spin finish application P . The latter as applied per unit time results likewise from the difference of the weight measured per unit time and the time-dependent throughput. In component 58 , the spin finish application P is used to correct the denier value T' as is determined by the arrangement of Figure 5. Insofar reference may be made to the description of Figure 5. The output signal of computer component 58 represents then the real denier, namely either the mean value when measured integrated over the time, or the instantaneous value when the respective measurements occur per unit time. This denier T again can be used as quality signal Q . In the embodiment of Figure 7, the weight of packages 33 is determined in that the entire takeup machine, hereafter winding head, is mounted in a spring suspension. To this end, on the side facing away from spindle 34 the winding head is mounted for pivotal movement in a swing support 60 , with the pivoting plane extending substantially vertically. On the other side which faces spindle 34 and package 33 , the winding head is supported in a spring 61 . The latter is sufficiently strong, so that the weight increase of package 33 effects only a slight deflection which has no effect on the yarn path geometry. The deflection of the winding head is picked up by a measuring device 52 and supplied via computer unit 46 and desired value memory 47 to comparison unit 48 . This comparison unit generates the quality signal Q . The quality signal again can be used to influence one or several process parameters in the extrusion (box E of Figure 1), or the drawing (box D of Figure 1), or even the spindle control. The quality signals Q which have been generated, as previously described, by the takeup device, are further processed as follows: the quality signal Q may be output as optical or acoustic alarm or as a graphic record. The latter allows to mark and classify the produced package 33 . Alternatively or additionally, the quality signal Q may then be supplied to one or several of the control means 23 for draw roll 19 to influence the drawing; to 24 to control the withdrawal speed; 45 to control the pump speed; 49 to control the extruder speed; 50 to control the heater; or 51 to control the cooling device. The extruder control 49 is activated in particular when no metering pump 9 is used. In this instance, the extruder 3 functions as a pump and the activation of extruder control 49 , i.e., the rotational speed of the extruder, allows to influence the output of extruder 3 . When a metering pump 9 is used, the throughput quantity may be influenced by spin pack 10 and spinneret 11 by activation of pump control 45 , i.e., the rotational speed of metering pump 9 . The activation of cooling air control 51 allows to influence cooling. This has an effect on the yarn denier T . In particular, it is also possible to influence the uniformity of the individual filaments with the use of special cooling devices which allow to cool the webs of filaments 12 and/or spinneret 11 in sectors. In the embodiment of Figure 1 all parts of the system which are necessary to produce yarn 1 , i.e., to extrude the thermoplastic material, are combined in a box indicated at " E ". The individual parts of the system are possibly exchangeable. Accordingly in this event other parameters are controlled. In particular, it is possible to replace extruder 3 with a discharge pump, and likewise various other possibilities of cooling the filament web are given. Shown in the embodiment of Figure 1 is that the produced yarn 1 is drawn by godets 16 and 19 . All elements which in the embodiment are used for drawing, are combined in the box indicated at " D ". In the present high-speed spinning process, drawing by godets may also be eliminated. In this instance, the yarn 1 is withdrawn from spinneret 11 either by a single godet and advanced to the winding head, or it is withdrawn directly from the spinneret by the takeup device. On the other hand, drawing may also occur by further methods, so that in this instance, block " D " would have to be replaced or supplemented with further elements, for example, an additional godet, a heater, in particular a heating tube. In the illustrated embodiment, the quality parameter Q may be used to activate delivery control 24 and/or draw ratio control 23 . The activation of delivery control 24 allows to influence the speed of godet 16 and godet 19 without changing the speed ratio. In this instance, the draw ratio remains constant, whereas the yarn speed changes. As a result, the denier T can be influenced. The activation 37 of draw ratio control 23 allows to influence the speed ratio between godets 16 and 19 , and to thus change the draw ratio. The change of the draw ratio allows to vary the strength conditions of the yarn, but also the denier. Finally, the spindle control allows to also control by means of quality parameter Q the circumferential speed of package 33 which is regulated by contact roll 28 . This results in particular in an influence on the package buildup and the yarn tension under which the yarn is wound on the package. Figure 8 illustrates a winding head 74 of a spinning system or a slit film production line in accordance with Figure 9, which is modified in comparison with Figure 7. In this embodiment, the entire winding head 74 , consisting of winding spindle 34 , bearing and drive motor 36 , as well as contact roll 28 and yarn traversing mechanism 27 is pivotally supported along the line of its center of gravity, i.e. a vertical line through the center of gravity of winding head 74 without package 33 held thereon. The pivot bearing 63 of swing support 60 is arranged in a frame structure 62 such that the torque caused by the forming package 33 loads weight sensor (weighing cell) 52 stationarily arranged on frame structure 62 with respect to axis of rotation 63 of pivot frame 62 , which extends vertically to winding spindle 34 . The evaluation of the weight signals supplied by weight sensor 52 occurs as in Figure 7 and causes quality signals Q which are used to control the spinning and processing operations. Figure 9 is a schematic view of a system for producing slit films, for example, slit-film yarns for carpet backing, braids, binder twine, or the like. Also in this embodiment, the invention is realized with the use of takeup devices constructed as sensor winding heads 74 in accordance with Figure 7 or Figure 8, as is described below. The thermoplastic plastic which is plasticized in extruder 3 by friction and additional heating, is extruded through melt line 6 and a subsequent wide slot-die 64 with orifice adjustment 65 to a flat film web, and withdrawn by a speed-adjustable cooling roll 67 , and solidified by intensive cooling. Subsequently, the film web 66 passes through a cutting device 68 , where it is split into a web of slit films 69 . The latter is then drawn collectively through a first draw zone 70 with heat setting and a further draw zone 73 , heat set and adjusted in its shrinkage. Finally, all slit films of web 69 are individually wound to cross-wound packages 33 on winding heads 74 with weight sensors in accordance with Figure 7 or 8. The winding weights of packages 33 , which are determined continuously or in timed fashion by the individual sensors 52 of winding heads 74 are input together with the length of advance of the slit-film web 69 as determined at delivery system 73 at the end of the shrinkage zone, into a central computer unit 46 and compared therein with the course of a representative desired value curve. The quality signals which are output by this unit, appear optically and, if need be, acoustically on a display and alarm unit 75 , and trigger an alarm, when unacceptable deviations from the predetermined tolerance range occur. With a suitable programming of the evaluation unit, however, they are also output already when the tendency to such an unacceptable deviation becomes apparent, so as to warn the operating personnel as early as possible and to counteract these tendencies. However, the quality signals are also output as a graphic record on a printer 76 connected to display unit 75 . Finally, the quality signals are used to control the process, namely to control the delivery speed the withdrawal by cooling roll 67 , provided the signals of all package weight sensors 52 move in direction of an unacceptable deviation from the desired value or a predetermined tolerance range. However, when these signals fail to indicate a uniform tendency, but exhibit tendencies which possibly deviate in groups among each other, the quality signals will be used for adjustment 65 of the die orifice, so as to correct the thickness of the slit films in partial ranges of the extruded film web. Finally, shown in Figure 10 is a wide-slot die 64 with an adjustment 65 of the die orifice, as is used in the extrusion line of Figure 9. Such dies are known and commercially available. Figure 10 shows the basic setup of such a flat film die 64 . It consists of two halves 77 and 78 , which form between them a melt duct 79 with a melt distribution over the width of die orifice 80 . The one die half 77 is constructed substantially rigid, whereas the second die half 78 is provided with a flexible lip 81 as a result of a cross-sectional narrowing. This lip is divided, when viewed over its length, into several adjustment blocks which cooperate each with associated adjustment devices 82 , and which are controlled by adjustment 65 of the die orifice as a function of determined quality signals. The adjustment devices 82 consist of expansion pins 83 which are unilaterally held in second die half 78 and supported with their free end on the adjustment blocks of lip 81 . The expansion pins 83 may be heated by heating cartridges 84 and are thereby lengthened, they may be cooled by cooling bores 85 and are thereby shortened, so that the length of the expansion pins is thermally changed, as need arises. As a result, force is introduced to die lip 81 in sections such as the die orifice adjustment requires it for this associated section. It should further be noted that this adjustment can be only a finest adjustment of die orifice 80 in a range from few 1/100 mm up to several 1/10 mm, whereas a manual coarse adjustment must previously be made by the operating personnel at the startup of the line. The described measures and the control of the line by determined quality signals allow to provide for a substantially automated operation with simultaneous product monitoring and quality control. NUMERAL REFERENCE LIST 1 Filament yarn 2 Hopper 3 Extruder 4 Motor 5 Heating system 6 Melt line 7 Pressure sensor 9 Pump, gear pump 10 Spinning head, spin pack 11 Nozzle, spinneret 12 Filaments, strand of filaments 13 Spin finish application roll, spin finish applicator 14 Cooling shaft 15 Blowing, air current 16 Delivery roll, godet 17 Guide roll 18 Drive motor 19 Draw roll, godet 20 Guide roll 21 Drive motor 22 Frequency transmitter 23 Frequency transmitter, draw ratio control 24 Withdrawal control, controllable frequency transmitter 25 Apex yarn guide 26 Traversing triangle 27 Yarn traversing mechanism 28 Contact roll 29 Shaft of contact roll 30 Ferromagnetic insert 31 Pulse generator 33 Package 34 Spindle 35 Winding tube 36 Drive motor 37 Spindle control 38 Ferromagnetic insert 39 Pulse generator 40 Computer unit 41 Set-point adjuster 42 Comparison circuit 44 Pump motor 45 Pump control 46 Computer unit 47 Memory 48 Comparison unit 49 Extruder control 50 Heater control 51 Cooling control 52 Weight sensor 53 Linear measuring device 55 Throughput signal 56 Computer component 57 Weight signal 58 Computer component 60 Swing support 61 Spring 62 Frame, frame structure 63 Axis of rotation, pivot bearing 64 Wide-slot die 65 Adjustment of extrusion orifice 66 Film web 67 Withdrawal by cooling roll 68 Cutting device 69 Web of slit-film tapes 70 First draw zone 71 Hot air zone 72 Second draw zone with heat setting 73 Delivery system 74 Winding head, sensor winding head 75 Display unit with alarm 76 Printer 77 Die half (rigid) 78 Die half 79 Melt duct 80 Die orifice 81 Die lip 82 Adjusting device 83 Expansion pin 84 Heating cartridge 85 Cooling bore

Claims: Method of producing and/or processing as well as winding an endless material of thermoplastic plastic (for example, foil, film, slit film, yarn) to a package with output of a quality signal as a function of a continuously measured process parameter, characterized in that a parameter of state of the package is measured and used as process parameter of the endless material, that the process parameter or a value derived therefrom is compared with a predetermined representative value (desired value) or its tolerance range, and that the quality signal of the quality of the endless material is output in the event of an unacceptable deviation of the parameter of state or derived value from the desired value. Method as in claim 1, characterized in that the time-dependent course of the parameter of state over the entire winding cycle or predetermined time intervals of the winding cycle is picked up and compared with a predetermined representative curve or its tolerance range (desired course), and the quality signal is output in the event of a deviation from the desired course. Method as in claim 1, characterized in that the parameter of state is determined a predetermined instant of the winding cycle and compared with a predetermined representative value or tolerance zone (desired value), and the quality signal is output in the event of a deviation of the representative value from the desired value. Method as in claim 1, characterized in that at the beginning and at the end of a predetermined time interval of the winding cycle, the parameter of state of the package is measured, and the increase of the parameter of state of the time interval is determined and compared with a representative value or tolerance range (desired value) of the increase of the parameter of state, and the quality signal is output in the event of a deviation from the desired value. Method as in claim 1, characterized in that the course of increase of the parameter of state per unit time is determined over the entire winding cycle or over a predetermined time interval of the winding cycle and compared with a predetermined representative course or tolerance range (desired value), and the quality signal is output in the event of a deviation from the desired value. Method as in claim 1, characterized in that during the winding cycle or a predetermined time interval of the winding cycle one of the coefficients of the time function of the parameter of state is determined and compared with a predetermined representative value or tolerance range (desired value), and the quality signal is output in the event of a deviation from the desired value. Method as in claim 1, characterized in that in a multiposition textile machine the parameter of state of the package of each winding position is continuously measured and a mean value is formed from the measured parameter of state of the package or values derived therefrom, and that the parameter of state or the value derived therefrom of each winding position is compared continuously or at certain instants with the mean value or a tolerance range predetermined to this end, and the quality signal is output in the event of a deviation. Method as in one of the foregoing claims, characterized in that the parameter of state of the package is its diameter. A method according to one of the foregoing claims, characterized in that for drawing results from the measurement of a diameter the diameter is continuously squared and the first mathematical derivative of the square is formed and continuously controllled. Method as in one of the foregoing claims 1-7, characterized in that in the production and takeup of films or foils the parameter of state is the actual thickness of the film/foil advancing to the package. Method as in one of the foregoing claims 1-7, characterized in that in the production and winding of a yarn to a cross-wound package the parameter of state is the denier of the yarn advancing to the package. Method as in claim 10 or 11, characterized in that the thickness or denier is measured by measuring the length of the endless material advancing to the package and the weight of the package. Method as in one of claims 1-7, characterized in that the parameter of state is the quantity or weight of the fluid which adheres to the yarn and the package (spin finish application). Method as in claim 13, characterized in that the spin finish application is measured by measuring the throughput on the thermoplastic material during the winding cycle or the throughput per unit time and the increase in weight of the package per unit time. Method as in one of claims 1-7, characterized by the combination of claims 11 and 12 or claims 11 and 13, the denier or the thickness being measured after removal of the spin finish application. Method as in one of claims 1-7, characterized in that the parameter of state is the density or the winding factor (crossing angle) of the package. Method as in claim 16, characterized in that the density of the package is measured by measuring the package diameter and the weight. Method as in one of claims 1-7, characterized in that the parameter of state is the weight. Method as in one of claims 12, 14, 15, 17, and 18, characterized in that the weight is determined by the deformation of the spindle or spindle bearing. Method is in one of claims 12, 14, 15, 17, and 18, characterized in that the weight of the package is measured by measuring the weight of the takeup machine. Method as in claim 8 or 17, characterized in that the package diameter is determined by measuring the surface speed and the rotational speed of the package. Method as in claim 21, characterized in that the surface speed is determined in that the surface of the package is scanned by means of a freely rotatable measuring roll, and its rotational speed is measured. Method as in one of the foregoing claims, characterized in that the quality signal is output for identifying the quality of the package. Method as in one of the foregoing claims, characterized in that the quality signal is output for monitoring and interrupting the process, if need arises. Method as in one of claims 1-22, characterized in that the quality signal is output for controlling a process parameter of the process. Method as in claim 25, characterized in that the thermoplastic material is supplied by means of a pump or an extruder to a die, and the rotational speed of the pump or extruder is controlled as a function of the quality signal. Method as in claim 25, characterized in that the thermoplastic material is supplied to the die in a plasticized condition, and that the heat supply to the thermoplastic material is controlled as a function of the quality signal. Method as in claim 25, characterized in that the thermoplastic material is extruded from the die in a molten condition and cooled upon leaving the die as a function of the quality signal. Method as in claim 28, characterized in that the thermoplastic material is extruded in molten condition as a strand of filaments or strand of slit film from a plurality of nozzle holes which are arranged in a nozzle plate, that each strand of filaments or slit film is processed to a yarn and wound on its own package, and that each strand of filaments or slit film is cooled upon leaving the spinneret as a function of the quality signal. Method as in claim 25 for the production of a foil or film, characterized in that the thermoplastic material is extruded from a wide-slot die, and that the width of the die orifice is controllable as a function of the quality signal. Method as in claim 30, characterized in that the foil web exiting from the wide-slot die is cut to tapes, and that after drawing each slit-film tape is wound to a package, and that the course of the orifice width is controlled over the width of the wide-slot die as a function of the quality signal associated with each package. Takeup machine for a continuously advancing endless material of a thermoplastic substance comprising a winding spindle for receiving and rotatably supporting a package, characterized in that the winding spindle (34) is connected with a measuring device (52) for determining the weight as a process parameter of the endless material whereby the process parameter of the endless material or a value derived therefrom is compared with a predetermined representative value (desired value) or its tolerance range and a quality signal of the quality of the endless material is output in the event of an unacceptable deviation of the parameter of state or derived value from the desired value. Takeup machine for a continuously advancing endless material of a thermoplastic substance comprising a winding spindle for receiving and rotatably supporting packages, characterized in that the takeup machine is connected with a measuring device (52) for determining its change of weight as a process parameter of the endless material whereby the process parameter of the endless material or a value derived therefrom is compared with a predetermined representative value (desired value) or its tolerance range and a quality signal of the quality of the endless material is output in the event of an unacceptable deviation of the parameter of state or derived value from the desired value. Takeup machine as in claim 32 or 33, characterized in that the winding head, consisting of winding spindle (34), yarn traversing mechanism (27), contact roll (28), and drive motor (36) is rotatably supported along the line of its center of gravity in a machine frame (62), and adapted to pivot about the axis of rotation of a swing support (60). Takeup machine as in claims 34, characterized in that the measuring device (52) for determining the weight or for determining the change in weight of the winding spindle (34) is stationarily mounted on machine frame (62) which is used for the suspension of the swing support (60). Spinning system for producing and/or processing as well as winding endless filaments or monofilaments, characterized in that it comprises a takeup machine as in claims 32 to 35, said takeup machine being provided with winding heads (74) which comprise a weight sensor (52) for determining the weight or the change of weight of the winding spindle (34) and the package or packages (33) placed thereon. Slit film production line for producing/and or processing as well as winding slit-film tapes cut from a film web, characterized in that it comprises a takeup machine according to one of claims 32 to 35, said takeup machine being provided with winding heads (74) which comprise a weight sensor (52) for determining the weight or change in weight of the winding spindle (34) and the package or packages (33) placed thereon, and that the [weights] determined by the weight sensors (52) are processed in a central computer unit (40) and compared with desired values, and that the quality signals output by the computer unit (40) are used for controlling the process (49, 65, 67).

Inventors: BINNER TOBIAS, SCHAEFER KLAUS DR, BINNER, TOBIAS, SCHAEFER, KLAUS DR., Schäfer, Klaus Dr.
Applicants: BARMAG BARMER MASCHF, BARMAG AG
Application year: 1993
Main classification: G01N33
IPC codes: G01N33, B65H63, B65H59