A system and method for reducing draw resonance of a plastic material in molten state, so-called melt, leaving an extrusion group of a plant for the production of plastic film, includes at least one thermostatically-controlled cylinder, having an embracement angle of the melt on the cylinder that is adjustable on the basis of the process rate, i.e., the linear movement speed of the plastic film, and/or on the basis of the temperature measured in the proximity of or in correspondence with the clamping area of the melt in a thermoforming, calibration and cooling group included in the plant and positioned downstream of the system.

The present invention relates to a device and to a method for producing a texturized filament or yarn, wherein at least one filament is guided into a draw device, is guided there by a pair of intake rollers towards at least two pairs of drafting system rollers and drawn by the same, downstream of which is disposed a texturizing device with a cooling drum. Downstream the texturizing device with the cooling drum is disposed at least one cooled drafting system roller, by which the filament, respectively the yarn is cooled to a temperature of 0° C. to 50° C.

A system for controlling parameters of polymeric film includes an extruder and a die which has a gap. A plurality of regulators are positioned along the die for regulating the gap. A cooling cylinder is located downstream of the die and a polymeric melt extends from the die to the cooling cylinder. A haze generator for creating a haze lane in the polymeric melt is located proximate the gap. A haze sensor system is located downstream from the gap in a measuring location. The haze sensor system is locates a transverse point for the respective haze lane in the polymeric film at the measuring location. The haze sensor system is in communication with the regulators to adjust the gap based on a correlation of haze lane position at origin point and transverse point at the measuring location.

A synthetic board stock for packaging food product is described, as well as a process for producing the synthetic board stock. The synthetic board stock has multiple layers with chosen properties. The board stock has a density less than 1.0 g/cm3 in order to meet the post-consumer waste stream recycling requirements for polypropylene, polyethylene and other polyolefin polymers. A process for making the synthetic board stock is also described, wherein the process eliminates a step from the prior related to dual print passes.

Systems for manufacturing a composite extruded product formed of a substrate and a film. The system includes an extruder, a film application section for integrally bonding the film to the substrate, a heating section for increasing the temperature of the composite extruded product, an embosser for embossing a pattern into the composite extruded product, and a cooling section for cooling the composite extruded product. The cooling section applies pressure to the composite extruded product and sprays cooling fluid onto the composite extruded product such that the composite extruded product is cooled and the pattern embossed into the first surface is permanently set.

The invention concerns a multilayer mono-material PE assembly that achieves durability, versatility and customization, lightness and chemical resistance, gas and moisture barrier chemical resistance, gas and moisture barrier, while being at the same time environmentally sustainable and recyclable with low effort. The invention relates also to a process for producing it and its use in packaging.

This disclosure relates to an article that includes a nonwoven substrate, a first film supported by the nonwoven substrate, and a second film such that the first film is between the nonwoven substrate and the second film. The first film includes a first polymer and a pore-forming filler. The difference between a surface energy of the first film and a surface energy of the nonwoven substrate is at most about 10 mN/m. The second film includes a second polymer capable of absorbing and desorbing moisture and providing a barrier to aqueous fluids.

A thermoplastic polymer advanceable by solid state polymerization is blended with at least one dissimilar thermoplastic polymer. The blend is solid state polymerized to provide a modified polymer alloy blend having at least one physical or chemical property different from that of the blend before solid state polymerization. The modified polymer alloy blend may be coextruded with a layer of thermoplastic extrusion polymer having a melt viscosity similar to that of the modified polymer alloy.

A method and apparatus for extrusion of an article is provided. A die assembly can apply flows of thermoplastic material to an array of reinforcing cables to form a composite extrusion. A slider fabric can be bonded to one side of the composite extrusion. After exiting the die assembly, the slider fabric can act to support the extrudate as it passes along an elongate mandrel, which can cause the base of the slider fabric to change shape from a flat profile to the final internal profile of the article. The extruded article can then be cooled to solidify the material. The die can include cooling for the slider fabric and means for promoting penetration of the thermoplastic into reinforcing cables.

The invention relates an extrusion device (100) for extruding a semi-finished product made of elastomeric material, comprising an extrusion body (10) extending along a feeding direction (A) and a pump (20) arranged downstream of the extrusion body (10) along said feeding direction (A). The extrusion body (10) comprises a hopper (30) for loading an elastomeric material and an extrusion screw (50) extending along said feeding direction (A) and having an inlet portion (50a) arranged close to the hopper (30) and an exit portion (50b) arranged close to the pump (20). The extrusion body (10) also comprises a motorised roller (40) arranged at the inlet portion (50a) of the extrusion screw (50) and configured to receive the elastomeric material from the hopper (30) and feed it to the extrusion screw (30). The extrusion screw (50) has a length and a diameter such that the ratio between length and diameter is comprised between 4 mm and 8 mm. The invention also relates to an extrusion process carried out through the aforementioned extrusion device (100).