The present invention relates to an extrusion die for producing a plastic profile with a first die plate having a flow channel for the plastic profile to be produced.
When extruding window profiles, the starting material (dryblend) is prepared in an extruder so that a homogeneous melt is produced, which is pressed through an extrusion die at a pressure of approx. 300 bar. In the extrusion die, the melt approximately assumes the contours of the profile. At a short, distance after the die, the profile strand enters the dry calibration and then passes through a wet calibration. Depending on the profile wall thickness, the lengths of the dry and wet calibration are approx. 0.5 m and 6 m at low pull-off speeds and up to 1 m and 18 m at high pull-off speeds. The calibration has the task of supporting the profile during the cooling process. The exact, geometry of the shaping surfaces of the calibration depends on the shrinkage behavior of the plastic and the extrusion speed and is decisive for dimensionally accurate profiles within the tolerances. After the wet calibration, the now largely cooled profile is captured by the caterpillar pull-off, which transports the profile at a constant speed through the calibration section to the saw or cutter. In the sawing unit, the endless extruded profile is cut to profile bars of usually 6 m length, which are then deposited in a deposit table and from there transferred to a container.
It is known that the impact of air on the profile surface immediately after leaving the extrusion die has a significant effect on the surface quality of the profile as well as on the feeding behavior in the first dry calibration. The distance between the end faces of the extrusion die and the first dry calibration is usually about 6 to 10 mm. After leaving the extrusion die, the hot melt swells slightly, i.e. the wall thicknesses increase before they are reduced again according to the pull-off speed. This is a critical process, especially in the case of single-walled, protruding profile sections, so-called extremities, because they have contact with the calibration on both sides. Usually, the gap at the beginning of the dry calibration is about 0.2 mm larger than the wall thickness of the finished profile. The melt in the transition zone in these profile sections can be thicker for a short time than in the cooled profile, so that there is a risk of getting stuck. This transition zone starts at the end face of the die and extends up to 50 mm into the calibration. Blowing with cold or hot air reduces both the friction of the melt against the calibrator wall (with cold blowing air), the tensile strength of the profile segment by cooling the edge layer (with cold blowing air) and the swelling of the melt in the transition zone (with hot blowing air). The hot blowing air causes the particularly high internal stresses of the melt in the edge layer to relax more quickly and therefore the swelling is reduced. Experiments should be carried out to determine which effect predominates, so that the feed behavior into the first dry calibration can be optimized.
EP 1 023 983 A shows how the profile surface is exposed to air after leaving the extrusion die. It is shown that the air flow is directed towards single-wall profile sections protruding from the profile. A disadvantage of this arrangement is that the bore for the air outlet nozzle is incorporated directly into the die plate and therefore cannot be changed with little effort and flexibly with regard to flow velocity, angle of impact and exact position of impact in the course of matching the nozzle and calibration.
AT 519 313 A discloses a similar arrangement for applying air to the profile surface, with a die plate in the air outlet area.
The known devices can basically be set up in such a way that the profile is selectively exposed to air for cooling or heating in order to reduce the problems described above. However, it is difficult to reproducibly restore the same conditions in case of modifications to the extrusion die or extrusion line, since the profile is sensitive to changes in location, direction and intensity of air flows. Furthermore, the temperature of the air is critical. Even a quick adaptation to different profile geometries is not possible in a satisfactory way.
With both cited patent specifications, it is difficult and laborious to realign the air flow when adjusting the extrusion die in order to optimize the profile quality and to define these improved conditions in an exactly reproducible manner. In the first case, the extrusion line must be shut down and the extrusion die must be completely disassembled. Only then can existing air outlet nozzles be closed and new nozzles drilled, often new supply bores must also be made. In the second case, if the nozzle body is magnetically fixed to the face of the extrusion die, the nozzle body could be moved, but the angle of impact could not be changed. In addition, the exact position of the nozzle body cannot be determined in a reliably reproducible manner. Unintentional displacements of the nozzle body because someone tugged at its air supply line could lead to rejects or to an interruption of production. In addition, any components protruding from the end face of the die will interfere with the normal operating sequence when adjusting the extrusion die and during the ongoing extrusion.
It is the object of the present invention to further develop an extrusion die of the above type so that the extruded profile can be flexibly and reproducibly exposed to air in order to optimize the profile quality. In particular, individual areas of the profile strand should be able to be selectively exposed to air flow.
It is provided according to the invention that at least one recess is provided in the first die plate for receiving exchangeable air nozzle inserts, which have an air channel with at least one air outlet nozzle, wherein at least one air supply bore leads from a connection on the outside of the first die plate into each recess.
The solution according to the invention offers the advantage that it is possible to design an extrusion die in a modular way, wherein a standardized recess can accommodate different air nozzle inserts that are adapted to the circumstances. If necessary, the air nozzle insert can be easily and cost-effectively reworked or replaced by an alternative air nozzle insert. This also ensures that an optimized setting can always be reproduced exactly if the extrusion die or extrusion line has to be modified in the meantime.
It is particularly advantageous if the air outlet nozzle is directed at an area of the profile to be produced. This area can be cooled or heated as required.
A special flexibility in the technical implementation can be achieved in that the air channel has several supply openings for connection with an air supply bore. An extrusion die is a complex component with bores for dowel pins, screws and the like. It is therefore not always possible to install an air supply bore in a certain area. An air nozzle insert has several feed openings, so that it can be used in different extrusion dies that require different positions for the air supply bore.
A particularly advantageous embodiment variant of the invention provides for the air supply to flow into a distribution chamber. From this distribution chamber one or more air outlet nozzles originate, each of which can be individually designed with regard to exact position, diameter and angular position.
In another embodiment, the air nozzle insert has a depression or groove on the outside that is connected to the air channel. This makes it possible to guide the air also in this depression on the outside of the air nozzle insert in the recess, which further improves the variability in difficult space conditions.
The present invention also relates to an extrusion process of plastic profiles using an extrusion die with a flow channel for forming a profile with a first die plate in which recesses are provided for accommodating air nozzle inserts which have air outlet nozzles for the blowing air, wherein the blowing air is directed at an angle between 0° and 45° onto the profile strand exiting the extrusion die.
In the following, the invention is explained in more detail by means of exemplary embodiments, wherein:
The intensity of the air jet as well as its temperature can be varied within wide limits by means of a control device, which will not be discussed in detail. The flow velocity of the air jet 10 can be varied by pressurizing the heating probe 8 with compressed air at different pressures in the range of 0 to 4 bar. The cross-sections and lengths of the actual air outlet nozzle 9 as well as in the supply line in the air nozzle insert 6 and in the die plate 1 limit the air flow rate to reasonable values, max. approx. 0.4 Nm3/min. The diameters in the supply line are deliberately kept “small”, approximately from 0.8 to 2 mm. The temperature of the blowing air can be adjusted within a range from room temperature to 600° C. If necessary, the blowing air can also be cooled, for which purpose the cold air is sucked in with a compressor from an air heat exchanger, which can be cooled down to −40° C.
In
Number | Date | Country | Kind |
---|---|---|---|
A 60263/2019 | Nov 2019 | AT | national |