Blown Foil System and Method for Producing a Foil Web

Abstract

The invention describes a blown foil system for producing a foil web with at least one extruder for providing a melt-like plastic, a blowing head with a circumferential die gap, with which the melt-like plastic can be transformed into a foil bubble emerging from the die gap, with at least one liquid cooling device for cooling the foil bubble, wherein a liquid can be supplied to the outer periphery and/or to the inner periphery of the foil bubble by means of the liquid cooling device, with a flat laying device by means of which the foil bubble can be formed into a double-layer foil web, wherein the two layers are in contact at least partially and in particular substantially over the full surface, and with at least one stretch unit for stretching the foil web in the longitudinal direction.

Claims

1. Blown foil system for the production of a foil web with at least one extruder for providing a melt-like plastic material a blowing head with a circumferential die gap, with which the melt-like plastic can be transformed into a foil bubble coming out of the die gap, with at least one liquid cooling device for cooling the foil bubble, a liquid being supplied to the outer circumference and/or to the inner circumference of the foil bubble by means of the liquid cooling device, with a flat laying device, by means of which the foil bubble can be formed into a double-layer foil web, the two layers being in contact with one another at least partially and in particular substantially over the full surface, at least one stretch unit for stretching the foil web in the longitudinal direction.

2. A method for producing a foil web, in which a melt-like plastic is provided by means of at least one extruder using a blowing head with a circumferential die gap, the melt-forming plastic is transformed into a foil bubble coming out of the die gap, the foil bubble is cooled by means of at least one liquid cooling device, a liquid being applied to the outer circumference and/or to the inner circumference of the foil bubble by means of the liquid cooling device, the foil bubble is formed into a double-layer foil web by means of a flat laying device, the two layers being in contact with one another at least partially and, in particular, substantially over the full surface, at least one stretch unit is used to stretch the foil web in the longitudinal direction.

Description

[0029] Further benefits, features and details of the invention will become apparent from the following description, in which various embodiments are explained in detail with reference to the figures. In this connection, the features mentioned in the claims and in the description may each be essential to the invention individually or any combination of features mentioned. Within the scope of the entire disclosure, features and details described in the context of the process according to the invention naturally also apply in connection with the blown foil system according to the invention, and vice versa in each case, so that, with regard to the disclosure, reference is or can always be made mutually to the various aspects of the invention. The individual figures show:

[0030] FIG. 1 Schematic side view of a blown foil system according to the invention.

[0031] FIG. 2 Illustration of a stretch unit

[0032] FIG. 3 Illustration of a winding device

[0033] The FIG. 1 shows an apparatus 1 for producing a foil web. A foil bubble 2 is extruded through an annular die gap of the blowing head 3 in the direction z, in particular in the downward direction of gravity. Through a feed line not shown, a gas is usually fed into the interior of the foil tube 2, which has an increased pressure compared to the ambient pressure. This is why the foil tube initially expands further during its transport in the z direction. Resulting from the gas content of the foil tube, this is referred to as a foil bubble. The expansion does not end until the foil tube enters a liquid cooling device 4, which is a substantially integral part of the apparatus 1. This is where the radial expansion possibility of the foil tube is limited by the inner wall 5. Often, the foil tube solidifies into a crystalline or semi-crystalline composite after entering the apparatus. This occurs by cooling below the melting point of the material of the foil tube. The circumferential line defined by the points of transition from molten to solid is referred to as the frost line 6. The liquid cooling device 4 includes a liquid reservoir 7, wherein the liquid can pass along the arrow 8 into the area between the inner wall 5 and the outer periphery of the foil bubble 2 to cool the foil bubble.

[0034] After passing through the liquid cooling device 4, the foil bubble 2 enters the effective area of a flat laying device 9, in which the circular foil tube is initially converted into an elliptical cross section with an increasing eccentricity until it finally forms, in the area of influence of the squeezing device, two foil webs lying one on top of the other, which are connected to each other at their lateral edges. In other words, a double-layer foil web 24 now exists.

[0035] The flat laying device 9 is rotatably arranged, the axis of rotation being substantially aligned with the tube axis 11, which is indicated by a dashed line in FIG. 1. The rotatability of the flat laying device is indicated by the arrow 12.

[0036] The ring 4 can be divided into different circumferential sections. Each circumferential section of the liquid cooling device 4 may be capable of applying to the foil bubble a flow rate (amount of liquid per unit time) varying over the circumference of the foil bubble and/or a flow rate of liquid having a temperature varying over the circumference of the foil tube. Water is preferably provided as the liquid. This allows the circumferential section of the foil tube allocated to the relevant circumferential section of the liquid cooling device to be individually tempered, in particular lower cooled or even heated. The circumferential sections of the foil tube which “melt” to a large extent resulting from the lower cooling effect of the liquid cooling device form a thinness point 13. With a greater cooling effect, on the other hand, deliquescence is reduced, so that thickness points are formed here. Thickness points and thinness points have a greater or lesser thickness, respectively, as compared to the average thickness of the foil tube.

[0037] To ensure that the thinness point always arrives at a fixed position of the flat laying device, it is also necessary in connection with a stretch unit that the thinness point moves along the circumference, which is indicated in the figure by the arrow 14. This “wandering” of the thinness point is achieved by changing the parameters of the circumferential section of the ring that is closest in the direction of arrow 14, so as to now create a thinness point adjacent to the circumferential section of the foil tube that presently has a thinness point. The present thinness point is retracted in that the circumferential section of the ring in question now again has a stronger cooling effect on the angular section allocated to it.

[0038] In order to be able to record a thickness profile of the foil bubble 2, a measuring device for thickness 18 (also often referred to as a profile measuring device) can be provided, which, viewed in the transport direction z, is preferably arranged between the liquid cooling device 4 and the flat laying device 9. The measuring device for thickness 18 comprises, for example, a measuring head which can determine the thickness of the wall of the foil tube at its present position. To form the profile, the measuring head can be designed to be movable around the foil tube in order to be able to repeat the measurement at different positions, which is illustrated by the double arrow 19. The distance between two positions at each of which a thickness measurement can be carried out can be variably adjustable. To move the measuring head, it can be slidably arranged on a rail 20, the rail 20 gripping annularly around the foil tube.

[0039] Furthermore, an evaluation and/or control device 40 is provided, with which the liquid cooling device 4 can be controlled so that a desired thickness profile can be generated.

[0040] This thickness profile or the control parameters necessary for this can be generated dynamically for the individual segments of the liquid cooling device 4, so that the thickness profile created moves in phase and in particular with an offset with the rotation of the flat laying device. At the turning points of the flat laying device, the offset is preferably 0. The data line 41 is available for transmitting control commands. The measuring device for thickness 18 can measure a thickness profile, as already described. Measured values (in raw form or as a thickness profile already) are sent to the evaluation and/or control device 40 via the data line 42. The evaluation and/or control device 40 can now evaluate the measured thickness profile and, in particular, modify the control parameters so that the measured thickness profile matches the desired thickness profile. Thus, a control loop is provided. In accordance with the invention, it is additionally provided that evaluation and/or control device 40 also considers the thickness profiles that have been recorded with the measuring device for thickness 38 and with at least one of the thickness measuring devices 45. The factors influencing these individual measuring devices for thickness can be taken into account in a weighted manner when modifying the control commands. In particular, it is imaginable that the thickness profiles measured by the measuring device for thickness 45 are considered primarily for influencing the offset. It may be advantageous that the control parameters necessary to set the target profile are stored upon an approach to a turning point, and are reapplied or considered in a mirrored manner upon a departure from a turning point. This way, when the offset decreases at the turning point, the values can be taken into account in such a way that the same values are used to set the increase of the offset. This prevents the sluggishness of the control loop from leading to undesired thinness points. It should be noted that in the description of the figures, the term “liquid cooling device 4” is synonymous with all possibilities of influencing the thickness profile of the foil web. Thus, other or further devices for imprinting a thickness profile on the foil tube and/or the double-layer foil web and/or the first and/or the second foil web may also be provided.

[0041] FIG. 1 further shows a reversing device 15 which has the task of guiding the flattened foil bubble, i.e. the double-layer foil web, from the flat laying device to the stationary roller 16 without causing damage. The arrow 17 indicates that this foil tube is now guided for further processing, which will be explained in more detail in the following figures. “Reversing” here means that various elements, in particular the individual reversing rollers and reversing stands, move back and forth between two end points. Preferably, this movement is rotational or pivoting movement. The end points can therefore also be referred to as turning points.

[0042] FIG. 2 now shows an example of a stretch unit 30 which is connected inline to the apparatus 1 shown in FIG. 1. In the context of the present invention, however, a stretch unit is not limited to the embodiment described below. In this context, inline means that the double-layer foil web 24 is fed from the apparatus 1 directly from the production process, i.e., without transporting the foil web in a handleable form.

[0043] The foil web 24 runs along the web transport direction z into the stretch unit 30. Here it is first guided by the directing roller 31 to the heating rollers 32, each of which is referred to by the reference sign 32. The function of the heating rollers 32 is to bring the foil web 24, which has already cooled down completely or partially, back to a temperature which is sufficient for a stretching or stretching process. Stretching processes are generally performed by stretching units, meaning that the foil has already cooled and must be brought back to stretching temperature. Stretch processes, such as those used in blown foil extrusion, are also conceivable (especially if the stretch unit follows a foil extrusion system inline) In such cases, the foil web has not yet cooled down completely.

[0044] Particularly if a stretch unit is directly subsequent to a blown foil system, i.e. if stretching takes place “inline”, it should also be possible to speak of a stretching unit as a stretching plant. However, this is more of a definitional than a technical matter.

[0045] After the foil web 24 has been returned to a stretching temperature in the area 28 of the heating rollers 32, it passes into the area of the stretch roller 22 and the nip roller 33 and crosses through the gap between these two rollers 22, 33. Thereupon, the foil web 24 passes through the stretch gap 21 to then reach the surface of the stretch roller 23 and leave the stretch gap 21. This stretch roller 23 forms a nip with the nip roller 36. Resulting from a lower circumferential speed of the first roller pair 22, 33 compared to the second roller pair 23, 36, the foil web 24 is elongated, i.e. stretched, in the stretch gap 21. Two effects occur which are not desired and make it necessary to cut off longitudinal strips at the sides of the foil webs. The first effect is a reduction in the film width during stretching (so-called necking). The second effect is a thickening of the edges of the foil web. It can be provided that the size of the stretch gap, i.e. the distance between the release edge of the foil web 24 from the roller 22 to the impact edge of the foil web on the roller 23, can be made variable. This makes it possible to influence the size of the neck-in and/or the thickening of the foil web at its edges.

[0046] Once it has passed through the stretch gap, of which there can also be several in series, the foil web 24 reaches area 29, which comprises cooling rollers each referred to by the reference sign 37, in which the foil web 24 is cooled again. After leaving this area 29, the foil web 24 has again reached a slightly lower temperature, so that its surface can survive transport over the directing roller 31 in the transport direction z without further damage. The foil web 24 is then moved on in the direction of the arrow 34 and, at the end of optional further processing, is fed to a winding device in which the foil web is wound up as a double-layer foil web or separately into two individual layers. In principle, it is not impossible for the foil web or the individual layers of the foil web to be given longitudinal cuts and wound up next to each other in several panels.

[0047] Before the foil web reaches the stretch unit 30, a cutting or puncturing device 35 can be provided, with which the double-layer foil web can be cut into or punctured, so that air or another gas that could still be inside the double-layer foil web could escape. Such a measure leads to an improved quality of the stretching process and to an increased accuracy of the thickness profiles of the double-layer foil web to be measured. In particular, it may be intended to longitudinally cut the foil web along or near a side edge so that the double-layer foil web is connected by only one side edge. It may also be desirable to cut the double-layer foil web at its two side edges. In particular, this is necessary from certain thicknesses of the foil web onwards, as the air transport to one side edge of the foil web may not be sufficiently fast.

[0048] A measuring device for thickness 38 is provided after the stretch unit 30 in the transport direction, with which a thickness profile of the double-layer foil web can be acquired after it has been stretched. It should be considered, however, that without further measures only the total thickness of the foil web can be measured here, i.e. the sum of the thicknesses of the individual layers. It is, however, thinkable, especially if the double-layer foil web has been given a longitudinal cut, to introduce a contrast medium, such as a metal sheet, between the two layers, so that one layer at a time can be measured separately with respect to its thickness.

[0049] The thickness measuring device 38 may again be a measuring head movably arranged along a rail which extends at least partially transversely to the transport direction. The measuring head is again capable of taking a thickness measurement of the foil web 24 at its present position. Subsequently, the measuring head can be moved to a further position at which a further measurement can be carried out.

[0050] It is not necessary, however, that the measuring head be stopped in order to measure the thickness. Instead, it can be provided in principle that the measuring head performs measurements at adjustable time intervals, but the speed of movement is variable. For example, in conjunction with the present invention, it may in principle be desirable for the measuring head to move more slowly at the edges of the foil web in order to increase the density of the measurements here, which increases the accuracy of the thickness profile at the edges. Furthermore, it is basically thinkable that the measuring device for thickness 38 is designed and configured to also measure beyond the edge of the foil web in order to also be able to make statements about the present width of the foil web.

[0051] Finally, FIG. 3 shows a foil cutting device 50, which is shown here in connection with two winding stations, 60, 61, but can also be provided independently thereof. The foil web 34 may already have been subjected to a pretreatment before it enters the foil cutting device. Specifically, a first trimming of the edge may already have been performed in order to already cut off a part of the thickenings at the edge, which leads to an improved quality of an optional pretreatment. Within the foil cutting device, further cutting devices 51, in particular in the form of cutting knives, are provided, each of which performs the final trimming of the edge of the still double-layer foil web. For this purpose, the double-layer foil web is guided over rollers 52 and 53, which primarily provide the web tension required for the trimming of the edge. Not later than after the trimming of the edge, the double-layer foil web is separated into two individual layers which, however, still lie directly on top of each other.

[0052] The layers are actually separated by rollers 54, 55, which form a nip. After passing through the nip, the first layer is fed to the first winding station 60, where it passes over various other rollers and is wound onto the winder 62.

[0053] Downstream of the separating device, a second thickness measuring instrument 45 is provided, the design and operation of which are preferably similar to those of the thickness measuring instrument 38. Through a data line 44, the measurement results (in raw form or as an evaluated thickness profile) are fed, for example by wire and/or wirelessly, to the evaluating and/or control device 40.

[0054] The second layer can be fed to the winding station 61, the structure and function of which is identical to the first winding station. Likewise, a second thickness measuring instrument may also be provided for measuring the second layer. In this case, reference is made to the description in the preceding paragraph with regard to structure and function.

[0055] The thickness measurement profiles recorded on the downstream side of the separating device can be continuously added up by the evaluating and/or control device in order to be able to also record a roll sum profile, i.e. the addition of the thickness profiles of the individual layers in a winder. In a blown foil system with a reversing device but without a stretch unit, deviations of the foil thicknesses from the average foil thickness, i.e. thickness and/or thinness points, are distributed in the axial direction of the winder, so that overall a uniform circumference of the winder is obtained. If a stretch unit is provided, however, this can result in further thickness or thinness points that can no longer be rectified by reversing. The formation of a roll sum profile described above means that the occurrence of, for example, piston rings (local thickening) on the winder can be identified at an early stage and considered when setting the control parameters for the liquid cooling device.

TABLE-US-00001 Reference sign list 1 Device for the production of a foil web 2 Foil bubble 3 Blowing head 4 Liquid cooling device 5 Inner wall 6 Frost line 7 Liquid reservoir 8 Arrow 9 Flat laying device 10 11 Tube axis 12 Arrow for indicating the rotatability of the flat laying device 13 Thinness point 14 Arrow 15 Reversing device 16 Roller 17 Arrow 18 Measuring device for thickness 19 Double arrow 20 Rail 21 Stretch gap 22 Stretch roller 23 Stretch roller 24 Double-layer foil web 25 26 27 28 Area of the heating rollers 32 29 Area 30 Stretch unit 31 Directing roller 32 Heating roller 33 Nip roller 34 Arrow 35 Cutter or dotting device 36 Roller pair 37 Cooling rollers 38 Measuring device for thickness 39 40 Evaluating and/or control device 41 Data line 42 Data line 43 44 Data line 45 Thickness measuring instrument 46 47 50 Foil cutting device 51 Cutting device 52 Roller 53 Roller 54 Roller 55 Roller 60 Winding station 61 Winding station 62 Winder