B29C48/78

Microporous sheet product and methods for making and using the same
10829600 · 2020-11-10 ·

Microporous sheet product and methods of making and using the same. In one embodiment, the microporous sheet product is made by a process that includes melt-extruding a sheet material using an extrusion mixture that includes a thermoplastic polymer, a non-cross-linked elastomer having a molecular weight of at least 50,000 Da, and a compatibilizing agent. By way of example, the thermoplastic polymer may be a polyolefin, the non-cross-linked elastomer may be a polyisobutylene, and the compatibilizing agent may be mineral spirits. After extrusion, the sheet material may be cooled, and the sheet material may be stretched. The microporous sheet product may be used, for example, as a battery separator, as a food packaging material, as a diffusion barrier in the ultrafiltration of colloidal matter, and in disposable garments.

EXTRUDER WITH FEED BLOCK FOR PROMOTING INCREASED MASS TRANSPORT RATE
20200307061 · 2020-10-01 ·

A feeder for an extruder includes a feed flow passage extending in an axial direction from a feeder inlet to a feeder outlet, and an axially extending rotatable screw provided in the feed flow passage. Rotation of the screw draws a feedstock in a direction of flow to the feeder outlet. The feeder inlet has an inlet passage that overlies the screw. The inlet passage has a width in a plane transverse to the axial direction, and the width decreases in the direction of flow.

EXTRUDER WITH FEED BLOCK FOR PROMOTING INCREASED MASS TRANSPORT RATE
20200307061 · 2020-10-01 ·

A feeder for an extruder includes a feed flow passage extending in an axial direction from a feeder inlet to a feeder outlet, and an axially extending rotatable screw provided in the feed flow passage. Rotation of the screw draws a feedstock in a direction of flow to the feeder outlet. The feeder inlet has an inlet passage that overlies the screw. The inlet passage has a width in a plane transverse to the axial direction, and the width decreases in the direction of flow.

THERMAL BONDING OF NONWOVEN TEXTILES CONTAINING CELLULOSE ACETATE FIBERS

Nonwoven fabrics and textiles containing cellulose ester fibers particularly cellulose acetate fibers are thermally bonded. An aqueous plasticizing solution is applied to the surface of a nonwoven web and thereafter the web is thermally bonded to create a thermally bonded nonwoven textile. Alternatively, water can be applied to the dry surface of a nonwoven web containing organic plasticizer treated cellulose ester fibers to create the moistened nonwoven web and thereafter thermally bonding the moistened nonwoven web to make a thermally bonded nonwoven textile. The fabrics exhibit an increase in tensile strength and toughness greater than the individual contributions of water and plasticizer alone and greater than the additive contributions of water and plasticizer alone.

Method of three-dimensional printing
10711146 · 2020-07-14 · ·

A sustainable material suitable for three-dimensional printing is disclosed. The sustainable material comprises a resin derived from a bio-based diacid monomer and a bio-based glycol monomer. The resulting sustainable material provides a much more robust 3-D printing material with different properties than conventional materials.

EXTRUSION DIE WITH IMPROVED EXIT GAP CONTROL
20200207002 · 2020-07-02 ·

An extrusion die including a die body having a movable die lip, is provided with improved automated control of the exit orifice through which a flowable polymer is extruded. The automated control is provided by lip adjustment assemblies each of which includes a thermally responsive translator and each of which is in engagement with the movable die lip. Beneficially, the lip adjustment assemblies are also in engagement with a support structure located to reduce the effect of flow pressure-induced deflection. Improved automated control of the movable lip and the exit orifice gap provides a web having a prescribed thickness profile without manual intervention being required.

EXTRUSION DIE WITH IMPROVED EXIT GAP CONTROL
20200207002 · 2020-07-02 ·

An extrusion die including a die body having a movable die lip, is provided with improved automated control of the exit orifice through which a flowable polymer is extruded. The automated control is provided by lip adjustment assemblies each of which includes a thermally responsive translator and each of which is in engagement with the movable die lip. Beneficially, the lip adjustment assemblies are also in engagement with a support structure located to reduce the effect of flow pressure-induced deflection. Improved automated control of the movable lip and the exit orifice gap provides a web having a prescribed thickness profile without manual intervention being required.

Continuous Extruder Process for Manufacturing Rheology-Modified Polyolefin for Cable Insulation Layer, and Related Products
20200189166 · 2020-06-18 ·

Rheology-modified, additive-containing ethylenic polymer compositions are prepared in a continuously operated extruder comprising first, second and third zones by a process comprising the steps of: mixing in the second zone of the extruder an ethylenic polymer and a high-temperature decomposing peroxide at a temperature such that the half-life of the peroxide is equal to or greater than one minute and for a sufficient period of time to modify the rheology of the ethylenic polymer to produce a rheology-modified, melted ethylenic polymer for transfer to the third zone of the extruder; and adding to the third zone one or more additives to the rheology-modified, melted ethylenic polymer to produce the rheology-modified, additive-containing ethylenic polymer.

Continuous Extruder Process for Manufacturing Rheology-Modified Polyolefin for Cable Insulation Layer, and Related Products
20200189166 · 2020-06-18 ·

Rheology-modified, additive-containing ethylenic polymer compositions are prepared in a continuously operated extruder comprising first, second and third zones by a process comprising the steps of: mixing in the second zone of the extruder an ethylenic polymer and a high-temperature decomposing peroxide at a temperature such that the half-life of the peroxide is equal to or greater than one minute and for a sufficient period of time to modify the rheology of the ethylenic polymer to produce a rheology-modified, melted ethylenic polymer for transfer to the third zone of the extruder; and adding to the third zone one or more additives to the rheology-modified, melted ethylenic polymer to produce the rheology-modified, additive-containing ethylenic polymer.

LOW PERMEATION FUEL HOSE
20200158266 · 2020-05-21 ·

Low permeation fuel hose is provided comprising an outer cover layer prepared from a composition comprising a polyvinyl chloride (PVC), a thermoplastic copolyester elastomer and, optionally, a thermoplastic polyurethane (TPU), wherein the hose exhibits improved low and high temperature performance compared to conventional fuel hoses having an outer layer consisting of industrial grade PVC.