Process and device for the melt spinning and cooling of multifilament threads
10801130 · 2020-10-13
Assignee
Inventors
Cpc classification
D01D5/088
TEXTILES; PAPER
International classification
Abstract
Techniques for melt spinning and cooling of multifilament polyamide threads are described. The process involves multiple filament bundles spun alongside one another and cooled down separately by streams of cooling air flowing radially from the outside to the inside. Streams of cooling air are produced from a blowing chamber connected to a pressure source. Exhaust gases that occur during the spinning are removed through exhaust openings before the cooling of the filament bundles. An air pressure is set within the blowing chamber in such a way that the exhaust gases in the vicinity of the filament bundles are blown out through the exhaust openings from the inside outwards. A blowing box is assigned a pressure setting means for setting an air pressure within the blowing chamber, by which an air pressure for blowing out the exhaust gases can be set at the exhaust openings of a connection adapter.
Claims
1. An apparatus for melt spinning and cooling of multifilament threads of a polyamide, comprising multiple spinnerets on a bottom side of a spinning beam, comprising a blow box, which is connected to a compressed air source and which has, within a blow chamber, multiple cooling cylinders with gas-permeable walls, which cooling cylinders respectively form multiple inlet openings on a top side of the blow box, and comprising a connection adapter, which is held in a pressure-tight manner with respect to the blow box and with respect to the spinning beam and, per spinneret, at a passage, has at least one waste gas opening for the evacuation of waste gases, wherein to the blow box is assigned a pressure adjusting means for the adjustment of an air pressure within the blow chamber, by means of which an air pressure for blowing out the waste gases at the waste gas openings of the connection adapter can be set, wherein the waste gas openings are not connected to a suction device.
2. The apparatus as claimed in claim 1, wherein the blow box has a measuring port for measuring an air pressure within the blow chamber.
3. The apparatus as claimed in claim 1, wherein the pressure adjusting means is formed by an adjustable damper flap in a feed duct which opens out into the blow box.
4. The apparatus as claimed in claim 1, wherein the waste gas openings in the connection adapter are of slotted, round or oval configuration and extend individually, or in plural, at the passages, coaxially to the cooling cylinders.
5. The apparatus as claimed in claim 4, wherein to the waste gas openings within the connection adapter are assigned, per spinneret, at least one of a plurality of waste gas sockets for blowing out the waste gases, wherein the waste gas openings open out into one of multiple waste gas chambers.
6. The apparatus as claimed in claim 4, wherein to the waste gas openings within the connection adapter is assigned a common waste gas chamber, which is connected to a central waste gas socket for blowing out the waste gases.
7. The apparatus as claimed in claim 1, wherein a waste gas store is provided for the reception of the blown-out waste gases, wherein the waste gas store is connected to a disposal station.
8. The apparatus as claimed in claim 5, wherein the waste gas socket or the waste gas sockets open out with a free end into an external environment, and in that a suction socket connected to an extraction device and having a suction opening is assigned, at a distance (A) apart, to the free end of the waste gas socket or to the free ends of the waste gas sockets.
9. The apparatus as claimed in claim 1, wherein the blow box forms an upper blow chamber and a lower distributing chamber.
10. The apparatus as claimed in claim 9, wherein the upper blow chamber and the lower distributing chamber are separated from each other by a perforated plate.
11. The apparatus as claimed in claim 9, wherein in a vertical direction, to the cooling cylinders are assigned a plurality of passage cylinders, which are open toward both ends and which each have closed cylinder walls and penetrate the lower distributing chamber.
12. The apparatus as claimed in claim 1, wherein a waste gas chamber is configured annularly within the connection adapter and encloses the passage.
13. The apparatus as claimed in claim 1, wherein a cooling air stream generated by the blow chamber and the cooling cylinders is directed directly onto the filaments.
14. The apparatus as claimed in claim 1, wherein, for vertical adjustment of the blow box, two separate piston cylinder units are provided, which on an outlet side are directly coupled with the blow box.
Description
(1) The method according to the invention is explained in greater detail below on the basis of some illustrative embodiments of the apparatus according to the invention with reference to the appended figures, wherein:
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(12) In
(13) The illustrative embodiment of the apparatus according to the invention for the melt spinning and cooling of multifilament threads of polyamide has a spinning beam 1, which on its bottom side 12 holds a plurality of spinnerets 2 arranged side by side in rows. The spinnerets 2 are connected within the spinning beam 1 by a plurality of melt lines 6 to a spinning pump 3. The spinning pump 3 is driven by means of a pump drive, wherein the spinning pump 3 to each spinneret 2 has a separate conveying means. The spinning pump 3 is connected to a melt source (not represented here) via a melt inflow 5. The spinning beam 1 is of heated design, so that the spinnerets 2, the melt line 6 and the spinning pump 3 are heated.
(14) To the spinning beam 1 is assigned on the bottom side 12 a connection adapter 13. The connection adapter 13 has for each spinneret 2 respectively a passage 16, which adjoins the bottom side 12 of the spinning beam 1.
(15) As can be seen, in particular, from
(16) On the passage 16 are configured a plurality of waste gas openings 19, which are configured on a pitch circle, evenly distributed on the periphery of the passage 16. The waste gas openings 19 are formed in this illustrative embodiment by bores. In principle, the waste gas openings 19 can also be formed by oval or slotted cutouts.
(17) The waste gas openings 19 in the passage 16 open out into a waste gas chamber 14 within the connection adapter 13. The waste gas chamber 14 extends between a closed top side 17 of the connection adapter 13 and a closed bottom side 18 of the connection adapter 13. The waste gas chamber 14 is configured annularly within the connection adapter and encloses the passage 16. On a longitudinal side of the connection adapter 13 is configured a waste gas outlet 37, to which a waste gas socket 25 is connected. The waste gas outlet 37 connects the waste gas chamber 14 to the waste gas socket 25. A free end of the waste gas socket 25 emerges in a waste gas store 36.
(18) For the further illustration of the waste gas system, reference is made in particular, apart from to
(19) The connection adapter 13 has, in total, four passages 16 and four inner waste gas chambers 14. Each of the waste gas chambers 14 is connected to a separate waste gas socket 25. The waste gas sockets 25 are arranged on a longitudinal side of the connection adapter 13. The waste gas sockets 25 each have a waste gas duct, through which a waste gas stream is conducted outward out of the respective waste gas chambers 14.
(20) As can be seen from the representation in
(21) As can be seen from the representations in
(22) In this illustrative embodiment, the cooling device 4 is formed by a blow box 8, which in its top side 11 bears the connection adapter 13. In the blow box 8 forms an upper blow chamber 9 and a lower distributing chamber 10, wherein the upper blow chamber 9 and the lower distributing chamber 10 are separated from each other by a perforated plate 26.
(23) Within the blow chamber 9, the blow box 8 has coaxially to the passages 16 of the connection adapter 13 a plurality of cooling cylinders 23. The cooling cylinders 23 form on the top side 11 of the blow box a plurality of inlet openings 15, which are oriented coaxially to the passages 16 of the connection adapter 13. The cooling cylinders 23 are all configured identically within the blow chamber 9 and have a gas-permeable cylinder wall, which can be formed, for instance, in double-walled design with an inner perforated plate and an outer wire mesh or with metal gauze.
(24) In the vertical direction, to the cooling cylinders 23 are assigned a plurality of passage cylinders 27, which are open toward both ends and which each have closed cylinder walls and penetrate the lower distributing chamber 10. The blow box 8 is thus fully penetrated, from the top side to an outlet side, by the cooling cylinders 23 and the passage cylinders 27.
(25) The blow box 8 has on a longitudinal side an air duct 24, which opens out into the lower distributing chamber 10. The air duct 24 is connected via an air supply duct 29 to a compressed air source not represented here in detail. Within the air supply duct 29 is configured a pressure adjusting means 30. In this illustrative embodiment, the pressure adjusting means 30 is formed by an adjustable damper flap 31.
(26) As can be seen, in particular, from the representation in
(27) For the sealing and insulation, on the top side 11 of the blow box 8 is provided an insulating plate 22, which extends between the connection adapter 13 and the blow box 8.
(28) For the vertical adjustment of the blow box 8 are provided two separate piston cylinder units 28.1 and 28.2, which on an outlet side are directly coupled with the blow box 8. During operation, the blow box 8 is pressed with the connection adapter 13 against the bottom side 12 of the spinning beam 1 or against the pressure plate 20, respectively. In compact configurations, to the blow box 8 is usually assigned just one of the represented piston cylinder units, which preferably acts in the middle region of the blow box 8.
(29) During operation, a melt consisting of a polyamide, for instance a PA6 or PA6.6, is fed to the spinning pump 3 and is forwarded under pressure to the spinnerets 2. The spinning beam 1 comprising the, in total, four represented spinnerets 2 constitutes a spinning position, in order to produce four multifilament threads in, in total, four spinning sites.
(30) At this point it should basically be mentioned that the spinning positions can have a plurality of spinnerets arranged in a single or double row. The number of represented spinnerets 2 is thus exemplary.
(31) Each of the spinnerets 2 extrudes a multiplicity of filaments 7, which on the bottom side of the spinneret 2 pass out through a nozzle plate, not represented in detail here, having a multiplicity of nozzle openings. The filaments 7 form a filament bundle. In the extrusion of the filaments, volatile constituents, in particular monomers and oligomers, are here generated in the adjacent fine-spinning space 21, which are distributed as a waste gas in the fine-spinning space 21 and are blown out of the fine-spinning space 21 through the waste gas openings 19 by virtue of a positive pressure created by the blow chamber 8 of the cooling device 4. The waste gases are conducted via the waste gas openings 19 into the adjacent waste gas chambers 14 and are guided from there, via the waste gas sockets 25, into the waste gas store 36.
(32) For the cooling of the filament strands, the cooling air stream generated by the blow chamber 9 and the cooling cylinders 23 is directed directly onto the filaments. After this, the filaments 7 pass through the following passage cylinders 27 and leave the blow box on the outlet side.
(33) In order to be able to utilize the exiting cooling air stream in the to blow out the waste gases the fine-spinning space 21 and to cool the filaments, a specific air pressure must be set within the blow chamber 9 at the start of the process. For this purpose, the air supply of the compressed air source is able to be varied via the damper flap 31 and directly monitored via the measuring port 32 on the blow box 8 and the pressure gauge 33. The setting of the air pressure within the blow chamber 9 is chosen such that the waste gases can be reliably discharged at the free ends of the waste gas sockets 25. The collection of the waste gases by a waste gas store 36 and a subsequent disposal of the waste gases is thus possible. In parallel, care should here be taken to ensure, however, that the cooling air stream acting directly on the filaments produces a sufficient cooling effect.
(34) In that illustrative embodiment of the apparatus according to the invention which is represented in
(35) In order to improve the evacuation of the waste gases by the generated blow stream at the passages of the connection adapters, in
(36) The passage 16 is surrounded by a waste gas chamber 14 configured within the connection adapter 13. The waste gas chamber 14 has on a longitudinal side of the connection adapter 13 a waste gas outlet 37. A conducting means 40 is assigned to the waste gas outlet 37 in order to conduct the waste gas entering the waste gas chamber 14 via the waste gas outlet 37 into the waste gas socket 25. Very continuous blow flows are thus able to be realized for the evacuation of the waste gas.
(37) In principle, there is also the possibility, however, of arranging on the connection adapter 13 a plurality of waste gas sockets per spinning site. Thus, in
(38) In the illustrative embodiment represented in
(39) The illustrative embodiment according to
(40) In the illustrative embodiment represented in
(41) For the further illustration of the connection adapter 13, reference is additionally made to
(42) On a longitudinal side of the connection adapter 13 is provided a central waste gas socket 25, which is connected via a waste gas outlet 37 to the waste gas chamber 14.
(43) As can be seen from the representations in
(44) In the illustrative embodiment represented in
(45) A further alternative in particular to the adjustment of the positive pressure for blowing out the waste gases could also be formed by an adjustable drain flow restrictor. The drain flow restrictor could be integrated in the waste gas socket in order to influence the blow stream and ultimately the positive pressure atmosphere in the fine-spinning space. Thus, in the embodiment represented in
(46) In the illustrative embodiment represented in
(47) In
(48) In the illustrative embodiment represented in
(49) The connection adapter 13 has a passage 16, which encloses a fine-spinning space 21 configured substantially concentrically to a spinneret 2. The passage 16 has a waste gas opening 19, which is of slotted configuration and extends over a part of the periphery of the passage 16. The waste gas opening 19 opens out into laterally configured waste gas chamber 14. To the waste gas chamber 14 is assigned, at the connection adapter 13, a waste gas outlet 37. The waste gas outlet 37 opens out into a waste gas socket 25, which is fastened to the connection adapter 13. A free opposite end 41 of the waste gas socket 25 opens out directly into an external environment, so that a waste gas discharged from the waste gas socket 25 can pass freely into the external environment.
(50) For the take-up and evacuation of the waste gases, a suction socket 42, connected to an extraction device 44, is provided. The suction socket 42 is arranged with a suction opening 43 at a distance to the free end of the waste gas socket 41. The distance provided between the waste gas socket 25 and the suction socket 42 is labeled in
(51) The waste gases must be able to be discharged into the external environment at the waste gas socket 25 without affecting a suction effect of the suction socket 42. The suction effect produced by the suction socket 42 is designed such that only those waste gases which float around freely in the external environment are taken up and evacuated. As a result of the external environment, a reliable pressure decoupling between a blowing effect at the waste gas socket 25 and a suction effect at the suction socket 42 must be realized.
(52) In the connection adapter 13 represented in
(53) In the illustrative embodiment represented in
(54) Similarly, it would be possible for the waste gas opening 19, the waste gas chamber 14 and the waste gas outlet 37 to be formed in the connection adapter 13 by a continuous waste gas duct laterally to the fine-spinning space 21.
(55) In the represented illustrative embodiments of the connection adapter 13, only some of the possible configurations of the waste gas opening 19, the waste gas chamber 14 and the waste gas outlet 37 are shown. Fundamental to the invention is the generation of a blow stream from the fine-spinning space 21 into an external environment.
(56) In the illustrative embodiment according to
(57) The method according to the invention and the apparatus according to the invention are in particular suitable for producing synthetic threads having fine filaments. An entrainment of the waste gases through the filament bundle is advantageously avoided by the cooling air stream which is generated by the blow chamber.