Apparatus for making a spunbond web from filaments
An apparatus for continuously making a spunbond web of filaments comprises a spinneret, a cooling chamber into which process air for can be introduced for the purpose of cooling the filaments, a monomer suction device between a spinneret and cooling chamber, a stretcher and a deposition device for depositing the filaments of the spunbond web. The cooling chamber is divided into two cooling compartments, and process air can be suctioned out from a first upper cooling compartment at a volumetric flow rate (V M ) to a monomer suction device. Process air exits from the first upper cooling compartment at a volumetric flow rate (V 1 ) into a second lower cooling compartment and from the first upper cooling compartment at a volumetric flow rate (V 1 ) into a second lower cooling compartment. A ratio (V M /V 1 ) is 0.1 to 0.35.
1. An apparatus for making a spunbond web of filaments, the apparatus comprising:
a spinneret generating thermoplastic filaments in a direction,
a cooling chamber downstream from the spinneret subdivided into upper and lower cooling compartments,
means for introducing process air for cooling the filaments into the chamber,
a monomer suction device between the spinneret and the cooling chamber for receiving the filaments from the spinneret and feeding the filaments to the cooling chamber,
a stretcher downstream of the monomer suction device and receiving the filaments from the cooling chamber,
a deposition device downstream of the stretcher for deposition of the filaments by the stretcher as the web,
recirculating means for
withdrawing a portion of the process air from the upper cooling compartment at a volumetric flow rate of V M ,
feeding the withdrawn portion of the process air to the monomer suction device,
feeding another portion of the process air at a volumetric flow rate V 1 into the lower cooling compartment such that a volumetric flow-rate ratio V M /V 1 is 0.1 to 0.35, and
withdrawing process air at a volumetric flow rate V 2 from the lower cooling chamber portion such that a volumetric flow rate V 1 /V 2 is 0.1 to 0.45.
2. The apparatus according to claim 1 , further comprising:
an air supply cabin positioned next to the cooling chamber and divided into upstream and downstream cabin sections, the recirculating means introducing process air into the upper cooling compartment from the upstream cabin section and into the lower cooling compartment from the downstream cabin section.
3. The apparatus according to claim 1 , wherein a distribution of nozzle holes of the spinneret is homogeneous everywhere or across the entire nozzle plate of the spinneret.
4. The apparatus according to claim 1 , wherein a spacing between the spinneret and the cooling chamber can be varied.
5. The apparatus according to claim 1 , wherein air from outside is blocked from entry into the cooling chamber and at the transition area between the cooling chamber and the stretcher.
6. The apparatus according to claim 1 , further comprising:
a diffuser between the stretcher and the deposition unit.
7. An apparatus for making a spunbond web, the apparatus comprising:
means for supplying polypropylene having an average isotactic sequence length of at least 65 and an onset temperature of at least 120°;
a spinneret having a nozzle plate forming a plurality of nozzle holes homogeneously distributed across the entire nozzle plate and connected to the means for heating for receiving the heated polypropylene and extruding filaments of the heated polypropylene through the homogeneously distributed nozzle holes such that the filaments travel in a flow direction and are spaced apart homogeneously in a direction transverse to the flow direction;
a monomer suction device downstream of the spinneret and through which the homogeneously spaced and extruded filaments move in the flow direction;
a cooling chamber downstream of the monomer suction device and divided into upper and lower cooling compartments through which the filaments move in the direction after exiting the monomer suction device;
blower means for
feeding cool process air into the cooling chamber to cool the filaments in the compartments thereof,
sucking a portion from the upper cooling compartment and into the monomer suction device at a volumetric flow rate V M ,
feeding another portion of the process air from the upper compartment at a volumetric flow rate V 1 into the lower cooling compartment,
withdrawing process air from the lower cooling compartment at a volumetric flow rate V 2 ;
control means connected to the blower means for setting the flow rates relative to each other such that a volumetric flow-rate ratio V M /V 1 is 0.1 to 0.3 and a volumetric flow-rate ratio V 1 /V 2 is 0.1 to 0.45;
a stretcher downstream of the lower cooling compartment for receiving and stretching the filaments therefrom; and
a deposition device downstream of the stretcher for receiving the stretched filaments.