A composition comprising a low density polyethylene (LDPE) and a peroxide-treated metallocene-catalyzed linear low density polyethylene (pmLLDPE), wherein the composition when extruded as a molten resin displays a neck-in value that is (i) decreased when compared to the neck-in value observed when using the LDPE alone, (ii) about equal to the neck-in value observed when using the LDPE alone, or (iii) increased by <10% of the neck-in value observed when using the LDPE alone. The composition when extruded as a molten resin displays a neck-in value that is decreased by ≥5% when compared with a neck-in value of an otherwise similar composition comprising the LDPE and a metallocene-catalyzed linear low density polyethylene (mLLDPE) that has not been peroxide-treated. The composition comprises 1-80 wt. % pmLLDPE. The pmLLDPE has a melt index of ≤0.9 g/10 min, when tested in accordance with ASTM D1238 under a force of 2.16 kg.

The invention relates to a method for calibrating adjusting means (120) for adjusting a nozzle slot (112) of a discharge nozzle (110) for a film track (FB) on a flat film machine (100), comprising the following steps: specifying a calibration position (KP) for the adjusting means (120), performing a controlling intervention to change the adjusting position (SP) of the adjusting means (120), acquiring the reaching of the calibration position (KP) of the adjusting means (120).

The present teachings include a method of measuring an entire film thickness. The method may include forming a polymeric film (10) and measuring the thickness of the film (10) with a camera (20) collecting spatial and spectral images of a plurality of points at one time. The camera may collect a line image from a line of the film. The camera may be a hyperspectral near-infrared camera. In analyzing raw data collected during the measuring step, fringes of the raw data may be corrected using a classical least squares analysis.

An extrusion head and a method for producing an elongated hollow body as an extrudate of an extrusion of extrusion material are provided. The extrusion head includes: a housing; a mandrel mounted in the housing, and a mouthpiece arranged downstream of the mandrel in a direction of extrusion. The extrusion material can flow around the mandrel in the direction of extrusion of the extrusion head. The mandrel includes an end-side mouthpiece section arranged in an opening of the mouthpiece so as to form a circumferential gap between the end-side mouthpiece section and an opening in the mouthpiece, and the mandrel is pivotable about at least one axis transverse to the direction of extrusion to change a geometry of the circumferential gap.

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. An applicator device for creating a tracking lane in the polymeric melt is located proximate the gap. A sensor system is located downstream from the gap in a measuring location. The sensor system locates a transverse point for the respective tracking lane in the polymeric film at the measuring location. The sensor system is in communication with the regulators to adjust the gap based on a correlation of tracking lane position at origin point and transverse point at the measuring location.

In a resin-film manufacturing apparatus of an embodiment, when a lip gap control is started, a difference between a state of a target heat bolt (THB) at a start of current control and a state of each of all the heat bolts at a start of last control is obtained, when the difference between the states of THB at the starts of the current and last control is a smallest one, a learning result of THB is set as an initial value of a control condition for THB, and when the difference between the states of THB is not the smallest one, either one of a learning result of the heat bolt of which the difference between the states is smaller than the difference between the states of THB and the learning result of THB is set as the initial value of the control condition for THB.

The invention relates to a method for switching the production of a flat film machine (100) from a feed product (EP) to a follow-on product (FP), comprising the following steps: recognizing a switching request for a switch from the feed product (EP) to the follow-on product (FP), determining a current feed control value (ES) of at least one control variable (SG) of the flat film machine (100) for the feed product (EP), determining a follow-on control value (FS) of the same at least one control variable (SG) for the follow-on product (FP), generating a control signal (SS) for a defined variation of the at least one control variable (SG) of the flat film machine (100) from the feed control value (ES) to the follow-on control value (FS).

An extrusion device includes a material inlet for feeding an extrusion material into the extrusion device; a material outlet, which is arranged opposite the material inlet along an axis, in order to expel the extrusion material from the extrusion device; a material guidance system for guiding the extrusion material from the material inlet to the material outlet; a body, which is arranged on the axis, is movable along the axis, passes through the material outlet and is designed in such a way that, as the body moves along the axis, a cross-sectional area through which the extrusion material is expelled from the material outlet changes; a drive device, arranged along the axis, for moving the body along the axis; a cooling line system for guiding coolant. Here, a first part of the cooling line system is arranged in the interior of the body and is suitable for guiding the coolant along the axis, a second part of the cooling line system is suitable for guiding the coolant out of the body away from the axis and for conducting said coolant around the drive device, and a third part of the cooling line system is suitable for guiding the coolant outwardly into a discharge line for the coolant at an incline to the axis. The second part of the cooling line system adjoins the first part of the cooling line system, and the third part of the cooling line system adjoins the second part of the cooling line system against a flow direction of the extrusion material from the material inlet to the material outlet.

A method for controlling the thickness of a continuous elongated element made of elastomeric material, applied according to coils wound on a forming support, includes: advancing a head end of the continuous elongated element toward the forming support; subjecting, during the advancement, the continuous elongated element to a first stretching with a first stretch coefficient before applying on the forming support; and subjecting, during the advancement, the continuous elongated element to a second stretching with a second stretch coefficient during the application on the forming support. During the first stretching, a span of the continuous elongated element adjacent to the head end is stretched with a supplementary stretch coefficient greater than the first stretch coefficient, in a manner so as to confer, also to the span adjacent to the head end, a stretch and a section similar or substantially equivalent to those of the rest of the continuous elongated element.

A method of producing a blown film with a controlled thickness profile, comprises the steps of: extruding molten plastic through an annular extrusion die; cooling the molten plastic using an annular blower around the extrusion die, positioning one or more sources of supplemental air at one or more desired circumferential positions about the annular extrusion die and adjacent to the extruded molten plastic, the annular blower and the one or more sources of supplemental air being operated to supply cooling air to the molten plastic between the annular extrusion die and the frost line where the molten plastic solidifies; and controlling the one or more sources of supplemental air to form one or more areas of increased thickness along a circumferential thickness profile of the blown film, the one or more areas of increased thickness having a thickness that is greater than an average thickness of the circumferential profile.