Device and Method for Impregnating Fiber Bundles with a Polymer Melt

Abstract

The invention relates to a device for impregnating fiber bundles with a polymer melt, in which device fiber bundles, which are inserted in parallel with one another into a slot-like infeed of an impregnation unit (4), are guided through between two guide plates (16, 17), which have undulating surfaces and are arranged so as to be complementary to one another at a defined spacing, and are discharged from the impregnation unit (4) via an outlet (28), the fiber bundles being saturated with the polymer melt while passing through the impregnation unit (4), which polymer melt following the slot-like infeed is introduced between the guide plates (16, 17) into the passage (29). According to the invention, the impregnation unit (4) comprises at least two passages (29) for a defined number of fiber bundles in each case, the passages (29) each comprising an inlet (26) for polymer melt.

Claims

1. Device for impregnating strand-like fiber bundles (32) with a polymer melt, in which device a plurality of fiber bundles (32), which are inserted in parallel with one another into a slot-like infeed (27) of an impregnation unit (4), are guided through between two guide plates (16, 17), which have undulating surfaces (22, 23), and are arranged so as to be complementary to one another at a defined spacing, and are discharged from the impregnation unit (4) via their outlet (28), the fiber bundles (32) being saturated with the polymer melt while passing through the impregnation unit (4), which polymer melt following the slot-like infeed (27) is introduced between the guide plates (16, 17) into the passage (29), characterized in that the impregnation unit (4) is formed from at least two sub-units (11, 12) arranged in parallel which are coupled laterally to each other, and in each case contain a slot-like infeed (27) and an outlet (28) for a defined number of fiber bundles (32) in each case, the passages (29) each comprising an inlet (26) for polymer melt.

2. (canceled)

3. Device according to claim 1, characterized in that the respective slot-like infeed (27) in the direction of travel of the fiber bundles has a region (35) of reduced slot height which makes a seamless transition into the respective passage between the guide plates (16, 17), and in that the passage height between the guide plates (16, 17) in the region of the inlet of the polymer melt is increased compared with the region of reduced slot height.

4. Device according to claim 1, characterized in that the region of reduced slot height causes the fiber bundles to be deflected out of their direction of travel in the passage (29) by increasing the tensile force on the fiber bundles.

5. Device according to claim 3, characterized in that the inlet (26) is located in the region of the first undulation peak or trough of the guide plates (16, 17) between a trough and a peak of the undulations of the guide plates (16, 17).

6. Device according to claim 3, characterized in that the polymer outlet (33) has a channel constriction in front of the outlet (33), via which deflection of the polymer melt in the direction of travel of the fiber bundles takes place.

7. Device according to claim 1, characterized in that the sub units (11, 12) contain at their outlet (28) in each case a die plate (18) by which the fiber bundles which are saturated with polymer melt are calibrated in diameter.

8. Device according to claim 1, characterized in that the sub-units (11, 12) are formed in multiple parts with side parts (13, 14), a front plate (15) and a main part (19) comprising the guide plates (16, 17), the infeed (27) of the fiber bundles being formed between the upper side of the front plate (15) and a front region of the upper guide plate (16).

9. Device according to claim 8, characterized in that the front plate (15) is flanged to the main part (19), and in that a runner (21) to the respective inlet (26) of polymer melt is formed between the end face of the main part (19) and the front plate (15).

10. Device according to claim 9, characterized in that the runner (21) for supplying polymer melt comprises a distributor region (20) in which the polymer melt is widened to a melt ribbon running across the full width of the impregnation unit (4) or of the sub-units (11, 12), which melt ribbon is supplied to the inlet (26) between the guide plates (16, 17).

11. Device according to claim 1, characterized in that the number of fiber bundles guided through each sub-unit (11, 12) is between 3 and 70.

12. Method for impregnating fiber bundles with a polymer melt, in which widely fanned-out fiber bundles (32) are guided through two guide plates (16, 17), arranged at a spacing from each other, which have undulating surfaces to an impregnation unit (4), wherein the polymer melt is introduced into the infeed region of the guide plates (16, 17), and the fiber bundles while passing through the impregnation unit (4) are saturated by the polymer melt, characterized in that the fiber bundles prior to entering the impregnation unit (4) are divided into at least two fiber bundle groups which are introduced into sub-units (11, 12) of the impregnation unit (4) in each case and in each case are saturated by polymer melt supplied separately to the sub-units (11, 12).

13. Method according to claim 12, characterized in that the tensile stresses and throughput rates of the fiber bundles of the individual fiber group bundles and/or the temperatures and pressures of the polymer melts can be controlled and regulated separately for each sub-unit (11, 12).

14. Method according to claim 12, characterized in that polymer melts of different material are supplied to the sub-units (11, 12).

15. Method according to claim 12, characterized in that the guide plates (16, 17) of the impregnation unit (4) are movable.

16. Method according to claim 15, characterized in that at least one of the guide plates (16, 17) is subjected to an oscillating movement.

17. Device according to claim 11, wherein the number of fiber bundles guided through each sub-unit (11, 12) is between 10 and 30.

Description

[0027] The invention will be discussed in greater detail below with reference to an embodiment.

[0028] FIG. 1 is an overall view of an installation for producing plastics granules with fiber material added thereto, in a side view,

[0029] FIG. 2 is a top view of an installation of FIG. 1,

[0030] FIG. 3 is an impregnation unit, consisting of two sub-units,

[0031] FIG. 4 is an exploded view of the individual parts of a sub-unit,

[0032] FIG. 5 is a front view of the front plate of a sub-unit,

[0033] FIG. 6 is a sectional view through a sub-unit,

[0034] FIG. 7 is a front view of the main part,

[0035] FIG. 8 is a view of the arrangement of the guide plates, and

[0036] FIG. 9 is a detail view of the inlet for polymer melt into the passage between the guide plates.

[0037] The device according to the invention is capable of impregnating fiber bundles of different types with polymer material. Fibers are to be understood to mean any type of fibers which have a great longitudinal strength, such as glass fibers, carbon fibers, fine strands, textile threads, aramid fibers or similar products. Suitable polymer materials for impregnation are in particular PA, PP, PE and other thermoplastic materials which are suitable for coating and impregnating fiber materials. Thermoplastic materials are however difficult to join to fiber materials, so intensive penetration of the fiber materials in an impregnation unit is necessary.

[0038] A roving is the bunching of a large number of the aforementioned fibers to form a strand, which here is referred to substantially as fiber bundle. The number of fibers in a strand may be up to several thousand, and a roving may be several kilometers long. It is usually rolled up on a roll.

[0039] Once a roving has been impregnated and coated, the strand produced is divided into short pieces and made available to plastics processors for further processing as granules. These may produce high-strength and lightweight products, such as tubes and other molded parts, from the granules. In the case of tape production, the impregnated rovings are wound up as a continuous tape.

[0040] FIG. 1 illustrates a side view of an installation for producing granules. A creel rack 1 contains, in a frame, a relatively large number of fiber bundles that can be unreeled, which are rolled up for instance in cord-like manner on rolls of the creel rack 1 and can be unreeled therefrom in controlled manner. The individual fiber bundles are then introduced into a tensioning unit 3, in which they are arranged in parallel next to one another and in each case are spread by stretching.

[0041] From the tensioning unit, the fiber bundles are transferred into the impregnation unit 4, in which they are permeated with polymer melt. In a subsequent water bath section 5, the composite consisting of fibers and polymer is cooled, and, at the end of the water bath section, converted into a cylindrical form via forming rollers 6. There follows a tape takeoff 7, by which the longitudinal tension of the fiber/polymer composite in the installation can be maintained. The fiber/polymer composite is then supplied to a granulator 8 and divided into pellets/granules.

[0042] FIG. 2 shows a top view of an installation according to FIG. 1. The creel rack is formed from two partial creel racks 9 and 10 arranged next to one another at an angle, which in each case receive a number of spools. The fiber bundles taken off therefrom run into the pretensioning unit 3, in which they are stretched and preheated and then are supplied to the impregnation unit 4, which is formed from two sub-units arranged in parallel.

[0043] Associated with the impregnation unit is an extruder 2 which makes available the polymer melt for impregnating the fiber bundles. The fiber bundle groups in the further process sequence are processed in parallel, but may also undergo different further process steps as required.

[0044] FIG. 3 shows an impregnation unit 4, which is composed of two sub-units 11 and 12. The sub-units are constructed in the same way, and can treat one group of fiber bundles in each case. The impregnation unit 4 may also be formed from more than two sub-units. With a number of 20 fiber bundles to be processed in each case, thus for three sub-units 60 fiber bundles can be processed simultaneously. The sub-units are preferably flanged to each other by a screw connection 25. They may however also be independent of each other.

[0045] FIG. 5 shows a dismantled sub-unit. It consists of a main part 19, which bears a lower guide plate 17 on the upper side. The main part is delimited in the transverse direction by side parts 13 and 14. On the end face of the main part (viewed counter to the infeed direction of the fibers) there is a front plate, and an upper guide plate 16 is arranged on the upper side of the main part. A die plate 18 is fastened to the rearward end.

[0046] Lower and upper guide plates 16 and 17 at a small spacing from each other of 0.5-8 mm have a passage through which the fiber bundles are guided. The surfaces of the guide plates 16 and 17 are provided with an undulating surface 22 or 23 respectively so as to be complementary to one another. On the end face of the main part 19 there can be seen one half of the runner 21, the other half of which (not shown) is formed on the rear side of the front part 15. The runner 21 opens upward into a distributor region 20, in which supplied polymer melt is distributed in the width and thus runs across the full width of the front side of the main part.

[0047] FIG. 5 shows an end view of the front plate 15 with side parts 13 and 14. The figure shows in particular the infeed 27, into which the fiber bundles are introduced into the impregnation unit.

[0048] FIG. 6 shows a sectional view of a sub-unit with main part 19, front plate 15, upper guide plate 16, lower guide plate 17 and the passage 29 between the upper and lower guide plates 16 and 17. Via the infeed 27, the fiber bundles are introduced into the impregnation unit, run under longitudinal tension through the passage 29 until they emerge from the passage 29 via the outlet 28, and then emerge from the impregnation unit calibrated through the subsequent die plate 18. The supply of the polymer melt takes place from below via the runner 21, which is connected to an extruder.

[0049] FIG. 7 once again shows the distributor region on the end face of the main part 19, the distributor region containing a plurality of distribution lands and deflections which ensure that the polymer melt is distributed uniformly across the full width of the sub-unit.

[0050] FIG. 8 shows an enlarged illustration of the arrangement of the guide plates 16 and 17 relative to each other. The arrangement of the plates defines a passage 29 of 0.5-8 mm, through which the fiber bundle 32 is drawn from the infeed 27 to the outlet 28. Owing to the longitudinal tension on the fiber bundle which is applied, the fiber bundle while passing through the passage contacts the respective peaks of the undulating guide plates at a number of points and thereby is penetrated by polymer melt in an improved manner. The necessary plasticity of the melt while the fiber bundles are passing through is maintained via a heating device 30.

[0051] The polymer melt is supplied to the passage via the melt flow-way 34, which extends across the full width of the sub-unit, at the polymer exit 33 and soaks the fiber bundle there.

[0052] FIG. 9 shows a view, enlarged further, of the region in which the polymer melt enters the passage 29 at the inlet 26. The polymer exit is located on a falling leg of the undulating passage 29 between a trough and a peak, and is angled in the direction of travel of the fiber bundle, so that the angle of deflection of the melt upon entry into the passage 29 is minimized. For better thermal control of the exit point, the passage is enlarged somewhat in this region, in order to concentrate a larger amount of melt at this point. In addition, a downstream direction is imposed, via a taper of the melt flow-way at the polymer inlet, on the melt which serves for better filling of the impregnation zone.

[0053] In a further configuration, the melt flow-way may be constricted or widened via an adjustable rail-like choke point 36, in order to be able to vary the pressure of the polymer melt.

[0054] If the inlet 26 into the passage 29 is displaced further onto a following rising leg between a trough and a peak, a shallower angle of the entry of the melt into the passage can be achieved. As an alternative to the illustration in FIG. 9, the undulating form of the guide plates can also be formed vertically mirrored, so that the inlet 26 into the passage 29 is already located on that (rising) leg between a trough and peak which is first in the direction of travel of the fiber bundles.

[0055] By a tensioning region 35 with reduced passage height following an infeed face 24 and with subsequent arcuate shape 31 at the beginning of the undulating passage 29, the tension on the fiber bundles which is necessary in the impregnating device can be increased further.

[0056] In order to achieve a still further improvement in the penetration of the polymer melt by the fiber bundles, the impregnating device may also contain a device for generating a slight oscillating movement of at least one of the guide plates.

REFERENCE NUMERALS

[0057] 1 creel rack 19 main part

[0058] 2 extruder 20 distributor region

[0059] 3 pretensioning unit 21 runner

[0060] 4 impregnation unit 22 lower surface

[0061] 5 water bath 23 upper surface

[0062] 6 forming rollers 24 infeed face

[0063] 7 tape takeoff 25 screw connection

[0064] 8 granulator 26 inlet

[0065] 9 partial creel rack 27 infeed

[0066] 10 partial creel rack 28 outlet

[0067] 11 sub-unit 29 passage

[0068] 12 sub-unit 30 heating means

[0069] 13 side plate 31 arc

[0070] 14 side plate 32 fiber bundle

[0071] 15 front plate 33 polymer exit

[0072] 16 upper guide plate 34 melt flow-way

[0073] 17 lower guide plate 35 tensioning region

[0074] 18 die plate 36 choke point