Patent classifications
C08J2327/08
POLYAMIDE FILM AND PRODUCTION METHOD FOR SAME
Provided is a polyamide film which is a stretched film including a polyamide resin composition containing 1 to 10% by mass of a polyester thermoplastic elastomer, wherein the polyamide film satisfies all of the following conditions (A) to (C): (A) elastic moduli in MD and TD of the film are each 1.0 to 2.3 GPa; (B) a ratio between the elastic moduli in MD and TD of the film (MD/TD) is 0.9 to 1.5; and (C) a haze of the film is 7% or less.
POROUS POLYMER COATINGS
The present invention provides porous polymer coatings having adhesive and air flow resistive properties. The porous polymer coating comprises a polymeric foam having a void fraction of greater than about 15% and an air permeability greater than 3 cubic feet per minute per square foot as measured based on ASTM D737-04, wherein the polymeric foam comprises a clay and/or pigment optionally having an aspect ratio of about 2:1, 5:1, or 10:1 to about 20:1, 50:1, or 100:1. In some embodiments, the porous polymer coating comprises a chlorinated polymer and a fluorochemical.
MASTER BATCH FOR EXPANSION MOLDING AND FOAM MOLDED BODY
The present invention aims to provide a masterbatch for foam molding which can be suitably used in molding involving high shear force or molding requiring low molding temperature and which can provide a foam molded article having a high expansion ratio and good appearance quality. The present invention also aims to provide a foam molded article formed from the masterbatch for foam molding. Provided is a masterbatch for foam molding, containing: a base resin; and a thermally expandable microcapsule, the masterbatch having a true specific gravity of 0.80 g/cm.sup.3 or more, the base resin containing an olefin elastomer, the masterbatch containing the thermally expandable microcapsule in an amount of 40 to 300 parts by weight relative to 100 parts by weight of the base resin.
Crosslinkable fluoropolymers
The present invention pertains to a process for the manufacture of a crosslinkable fluoropolymer, to said crosslinkable fluoropolymer and the crosslinked fluoropolymer obtainable therefrom, to a film comprising said crosslinkable fluoropolymer or said crosslinked fluoropolymer and to uses of said crosslinked fluoropolymer film in various applications.
Process For Preparing Single Phase Vinylidene Chloride-Based Additive Blends
Provided is a process for preparing a PVDC additive blend in which an additive is blended with PVDC under high shear blending to produce a highly uniform blend in which the additive is homogeneously distributed throughout the PVDC. It has been found that performing high shear blending in multiple successive stages in which the concentration of the additive in the blend is reduced in each successive stage helps in prove the uniformity of the PVDC additive blend. For example, the high shear blending may be carried out in 2 to 6 stages, and in particular, from 2 to 4 stages. Also provided is a PVDC additive blend having a uniform blend of PVDC and an additive, such as a blend of a PVDC copolymer of vinylidene chloride and methyl acrylate and a fluorescing agent, such as 2,2(2,5-thiophenylendiyl)bis(5-tert-butylbenzoxazole).
CELLULOSE COMPOSITE FILM, AND ITS PREPARATION METHOD
A cellulose composite film, and a method for producing a cellulose composite film are provided. The cellulose composite film includes a cellulose film, a primer layer that is disposed on one side of the cellulose film, and a barrier layer that is disposed on one side of the primer layer. The cellulose film includes a regenerated cellulose film, the primer layer includes polyurethane film-forming resin, and the barrier layer includes a polyvinylidene chloride (PVDC) coating with an anti-fogging agent.
METHOD AND SYSTEM FOR RECYCLING POLYVINYLIDENE CHLORIDE CONTAINING COMPOSITE MATERIAL
A method of recycling a composite material of polyolefin and polyvinylidene chloride. The composite material is subjected to a polar aprotic solvent to dissolve the polyvinylidene chloride from the composite material into the solution of the polar aprotic solvent. The undissolved composite material from the solution can be collected and rinsed. The collected undissolved composite material being substantially free from polyvinylidene chloride. The polyvinylidene chloride can be precipitated out of the solution. The precipitated polyvinylidene chloride being substantially pure polyvinylidene chloride.
UPCYCLING MIXED WASTE PLASTIC THROUGH CHEMICAL DEPOLYMERIZATION AND BIOLOGICAL FUNNELING
The provided methods and systems describe the breakdown of plastic materials into valuable products, thereby both eliminating waste and providing reusable materials. The described systems and methods utilize catalytic depolymerization and biological funneling via bacteria, which may reduce the costs of recycling plastics in terms of expensive catalysts, energy, and time. Advantageously, some embodiments may target mixed plastic streams, which due to having multiple chemical compositions, may not be easily recycled via conventional recycling techniques. Such mixed plastic streams are currently often discarded (e.g., landfilled) rather than recycled due to the cost and effort required for separating the various compositions present.
TRANSPARENT POLYMER FILM WITH DISCOLORATION COMPENSATION
A single-layer or multilayer film formed from one or more polymeric materials has CIE colour values a* and b* such that 7a*0, 15b*0 and an optical transmission T such that 60%T95%. The inventive transparent films provide discoloration compensation that alleviates yellowing caused by UV light.
Integration of Polymeric Waste Co-Processing in Cokers to Produce Circular Chemical Products from Coker Naphtha
Systems and methods are provided for integration of polymeric waste co-processing in cokers to produce circular chemical products from coker naphtha, including a method of producing circular chemical products comprising: providing a coker naphtha that is at least partially derived from polymeric waste, wherein the coker naphtha has a total halide content of about 1 wppm to about 0.5 wt %, a 2-3 ring aromatic content of about 0 wt % to about 5 wt %, and a sulfur content of about 750 ppm to about 2 wt %; and converting the coker naphtha into at least a polymer.