Process for producing at least one filament, vapour-depositing apparatus for carrying out such a process and filament-production installation with such a vapour-depositing apparatus
20240124262 ยท 2024-04-18
Inventors
Cpc classification
B65H54/88
PERFORMING OPERATIONS; TRANSPORTING
D01D5/16
TEXTILES; PAPER
International classification
B65H51/16
PERFORMING OPERATIONS; TRANSPORTING
B65H59/38
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A method for producing at least one filament comprises at least one stretching step in which the at least one filament is stretched, wherein the at least one filament is in a vapor-depositing region flown around by water vapor before and/or during a stretching.
wherein at least one vapor parameter of the water vapor located in the vapor-depositing region is controlled so as to counteract a formation of droplets on the at least one filament, wherein the vapor parameter is monitored by at least one sensor element of a vapor-depositing apparatus, wherein a control or regulation unit of the vapor-depositing apparatus or of a filament-production installation comprising the vapor-depositing apparatus adjusts the vapor parameter such that a condensation of the water vapor on the filament is counteracted.
Claims
1-13. (canceled)
14. A method for producing at least one filament, in particular an artificial-lawn filament, a packaging tape or a monofilament, preferentially a cohort of filaments, with at least one stretching step in which the at least one filament, in particular the artificial-lawn filament, the packaging tape or the monofilament, is stretched, wherein the at least one filament, in particular the artificial-lawn filament, the packaging tape or the monofilament, is in a vapor-depositing region flown around by water vapor before and/or during a stretching, wherein at least one vapor parameter of the water vapor located in the vapor-depositing region, in particular in the form of dry vapor, is controlled so as to counteract a formation of droplets on the at least one filament, wherein the vapor parameter is monitored by at least one sensor element of a vapor-depositing apparatus, wherein a control or regulation unit of the vapor-depositing apparatus or of a filament-production installation comprising the vapor-depositing apparatus adjusts the vapor parameter such that a condensation of the water vapor, in particular the dry vapor, on the filament is counteracted
15. The method according to claim 1, wherein for an adjustment of the vapor parameter, the water vapor, in particular the dry vapor, is heated to a temperature of more than 125? C. before entry into the vapor-depositing region.
16. The method according to claim 14 or 15, wherein for an adjustment of the vapor parameter, the water vapor is overheated before entry into the vapor-depositing region, in particular in order to generate dry vapor.
17. The method according to claim 1, wherein in at least one method step, a temperature which the water vapor, in particular the dry vapor, is brought to before entry into the vapor-depositing region is adjusted depending on the vapor parameter of the vapor-depositing region.
18. The method according to claim 1, wherein the water vapor, in particular the dry vapor, is expanded upon entry into the vapor-depositing region.
19. The method according to claim 1, wherein an inlet valve for letting the water vapor, in particular the dry vapor, into the vapor-depositing region is regulated depending on the vapor parameter.
20. The method according to claim 1, wherein a temperature of the water vapor, in particular the dry vapor, in the vapor-depositing region is maintained above a condensation temperature of the water vapor, in particular the dry vapor.
21. The method according to claim 1, wherein the water vapor, in particular the dry vapor, is actively removed, in particular suctioned, out of the vapor-depositing region.
22. The method according to claim 1, wherein in order to achieve a homogeneous distribution of the water vapor, in particular the dry vapor, the water vapor, in particular the dry vapor, is let into the vapor-depositing region in distributed fashion via several vapor inlets.
23. The method according to claim 1, comprising a further stretching step, before and/or during which the at least one filament, in particular the artificial-lawn filament, the packaging tape or the monofilament, is flown around by hot air.
24. The method according to claim 1, comprising at least one fixing step, during which the at least one filament, in particular the artificial-lawn filament, the packaging tape or the monofilament, is flown around by hot air or water vapor, in particular dry vapor.
25. A vapor-depositing apparatus for a filament-production installation, in particular an extrusion spinning installation, for the production of at least one filament, in particular an artificial-lawn filament, a packaging tape or a monofilament, following a method according to claim 1, with at least one control or regulation unit, which is configured to adjust the vapor parameter such that a condensation of the water vapor, in particular the dry vapor, on the filament can be counteracted, and with at least one vapor generator or at least one heating and/or cooling aggregate, the vapor generator being configured to vaporize water for a production of the water vapor, in particular the dry vapor, the heating and/or cooling aggregate being configured to adapt, before entry into the vapor-depositing region, the temperature of the water vapor, in particular the dry vapor, in particular the temperature of the water vapor, in particular the dry vapor, obtained from an external vapor source.
26. A filament-production installation, in particular an extrusion spinning installation, for the production of at least one filament, in particular an artificial-lawn filament, a packaging tape or a monofilament, with a vapor-depositing apparatus according to claim 15 and with at least one raw material processing station for spinning the filament.
Description
DRAWINGS
[0026] Further advantages will become apparent from the following description of the drawings. In the drawings an exemplary embodiment of the invention is illustrated. The drawings, the description and the claims contain a plurality of features in combination. Someone skilled in the art will purposefully also consider the features separately and will find further expedient combinations.
[0027] It is shown in: [0028] a schematic illustration of a filament-production installation according to the invention, [0029] a schematic illustration of a vapor-depositing apparatus according to the invention, [0030] a schematic illustration of a vapor generator of the filament-production installation, and [0031] a schematic flow chart of the method according to the invention.
DESCRIPTION OF THE EXEMPLARY EMBODIMENT
[0032]
[0033] The filament-production installation 28 in particular comprises a control or regulation unit 62 for implementing a method 10 for the production of the at least one filament 12, which will be explained in detail in
[0034]
[0035]
[0036] Preferably the vapor generator 34 comprises a vaporizer 76, in particular for a vaporization of the water from the feedwater tank 74. In particular, the feedwater tank 74 is fluidically connected to the vaporizer 76. Preferably the vapor generator 34 comprises at least one vaporizer heating element in the vaporizer 76 for a vaporization of the water. Preferably the vapor generator 34 comprises at least one vaporizer temperature sensor 82 for a monitoring of a temperature of a saturated vapor generated by the vaporizer 76. Preferably the vapor generator 34 comprises at last one vaporizer temperature adjuster 88, in particular an electric switch for an activation or deactivation of the vaporizer heating element, for an adjustment of a saturated-vapor temperature of the saturated vapor by the control or regulation unit 62. Especially preferentially, for a production of the water vapor 18, in particular the dry vapor, the saturated vapor is heated to a temperature between 130? C. and 180? C. Particularly preferably the control or regulation unit 62 defines a setpoint value for the saturated-vapor temperature of the saturated vapor depending on a pressure of the saturated vapor, in particular a set pressure of the water vapor 18, in particular the dry vapor. Preferably the vapor generator 34 comprises a water bypass 100, which is connected to the vaporizer 76, for letting water out of the vaporizer 76. The water bypass 100 preferably comprises a pneumatic regulating valve, which is in particular controlled by the control or regulation unit 62. Preferentially the vapor generator 34 comprises a vapor bypass, in particular with a pressure relief valve, which is connected to the vaporizer 76, for letting vapor out of the vaporizer 76. The vapor generator 34 in particular comprises a compensating reservoir 94. The water bypass 100 preferably opens into the compensating reservoir 94. The vapor bypass 102 preferably opens into the compensating reservoir 94. The compensating reservoir 94 in particular has a generator vapor outlet 96 for letting vapor, in particular vapor not used and/or not usable in the course of the method 10, out of the vapor generator 34. The compensating reservoir 94 in particular comprises a generator water drain 98 for letting water out of the vapor generator 34.
[0037] The vapor generator 34 preferably comprises a superheater 78, in particular for an overheating of the saturated vapor from the vaporizer 76. In particular, the superheater 78 is fluidically connected to the vaporizer 76. Preferably the vapor generator 34 comprises at least one dry-vapor heating element in the superheater 78 for an overheating of the saturated vapor. Preferably the vapor generator 34 comprises at least one dry-vapor temperature sensor 84 for a monitoring of a temperature of the water vapor 18, in particular the dry vapor, generated by the superheater 78. For an adjustment of a temperature of the water vapor 18, in particular the dry vapor, by the control or regulation unit 62, the vapor generator 34 preferably comprises at least one dry-vapor temperature adjuster 90, in particular an electric switch for an activation or deactivation of the dry-vapor heating element. Particularly preferably the water vapor 18, in particular the dry vapor, is heated to a temperature between 180? C. and 300? C. Especially preferentially the control or regulation unit 62 defines a setpoint value for the temperature of the water vapor 18, in particular the dry vapor, depending on a set pressure of the water vapor 18, in particular the dry vapor. A dry-vapor outlet of the superheater 78 is in particular connected to the vapor-depositing apparatus 26. Preferably the vapor generator 34 comprises a dry-vapor bypass 92 that is connected to the superheater 78 for letting the water vapor 18, in particular the dry vapor, out of the superheater 78. The dry-vapor bypass 92 preferably comprises a pneumatic regulating valve, which is in particular controlled by the control or regulation unit 62. The dry-vapor bypass 92 preferably opens into the compensating reservoir 94.
[0038]
[0039] The method 10 in particular comprises a vapor generating step 104. In particular, the vapor generator 34 produces the water vapor 18, in particular the dry vapor, in the vapor generating step 104. For an adjustment of the vapor parameter, the water vapor 18, in particular the dry vapor, is heated to a temperature of more than 125? C. before it is let into the vapor-depositing region 16. For an adjustment of the vapor parameter, the water vapor 18, in particular the dry vapor, is overheated before it is let into the vapor-depositing region 16. The method 10 in particular comprises a vapor feed-in step 106. In the vapor feed-in step 106, the water vapor 18, in particular the dry vapor, is let into the vapor-depositing region 16. In particular, the control or regulation unit 62 controls the inlet valve 20 during the vapor feed-in step 106 for the purpose of a controlled feeding of the water vapor 18, in particular the dry vapor, into the vapor-depositing region 16. The water vapor 18, in particular the dry vapor, is expanded upon entry into the vapor-depositing region 16. In order to achieve a homogeneous distribution of the water vapor 18, in particular the dry vapor, the water vapor 18, in particular the dry vapor, is let into the vapor-depositing region 16 in distributed fashion via the several vapor inlets 22, 24 of the distributor system 67. In particular, in the stretching step 14, the water vapor 18, in particular the dry vapor, flows around the section of the filament 12 that is situated in the vapor-depositing region 16. In particular, the water vapor 18, in particular the dry vapor, let into the vapor-depositing region 16 flows continuously from the vapor inlets 22, 24 to the vapor outlets 108, 116. In particular, the method 10 comprises a vapor removal step 110. The water vapor 18, in particular the dry vapor, is actively removed, in particular suctioned, from the vapor-depositing region 16. In the vapor removal step 110, the ventilator 60 suctions the water vapor 18, in particular the dry vapor, out of the vapor-depositing region 16.
[0040] Preferably the control or regulation unit 62 executes a pressure regulation 114. In particular, in the course of the pressure regulation 114, the control or regulation unit 62 controls the ventilator 60 and/or the inlet valve 20 and optionally the vapor generator 34. For a letting-in of the water vapor 18, in particular the dry vapor, into the vapor-depositing region 16, the inlet valve 20 is regulated depending on the vapor parameter. In particular, the control or regulation unit 62 executes the pressure regulation 114 in order to create a constant overpressure relative to the atmosphere in the vapor-depositing region 16, and in particular in order to support a homogeneous distribution of the water vapor 18, in particular the dry vapor. Preferably the control or regulation unit 62 executes a temperature regulation 112. In the course of the temperature regulation 112, the control or regulation unit 62 in particular controls the vapor generator 34 and optionally the inlet valve 20 and optionally the heating element 68. A temperature which the water vapor 18, in particular the dry vapor, is brought to before entry into the vapor-depositing region 16 is adjusted depending on the vapor parameter of the vapor-depositing region 16. In particular, the control or regulation unit 62 executes the temperature regulation 112 in order to prevent a cooling of the water vapor 18, in particular the dry vapor, below a threshold value. A temperature of the water vapor 18, in particular the dry vapor, in the vapor-depositing region 16 is maintained above an, in particular pressure-dependent, condensation temperature of the water vapor 18, in particular the dry vapor.