Abstract: A polymer composition, stretched and unstretched articles and processes to make stretched and unstretched articles from that composition are set forth wherein the composition comprises a blend of a polyamide wherein the amino to carboxyl end group ratio of the polyamide polymer is less than 1.0 when the relative viscosity of the polyamide polymer is less than 2.0, and less than 0.30 when the relative viscosity is in the range of 2.0 to 2.3 and less than 0.20 when the relative viscosity is greater than 2.3, a crystallizable polyester and an interfacial tension reducing agent.

Abstract: A polymer composition, stretched and unstretched articles and processes to make stretched and unstretched articles from that composition are set forth wherein the composition comprises a blend of a polyamide wherein the amino to carboxyl end group ratio of the polyamide polymer is less than 1.0 when the relative viscosity of the polyamide polymer is less than 2.0, and less than 0.30 when the relative viscosity is in the range of 2.0 to 2.3 and less than 0.20 when the relative viscosity is greater than 2.3, a crystallizable polyester and an interfacial tension reducing agent.

Abstract: A polymer composition, stretched and unstretched articles and processes to make stretched and unstretched articles from that composition are set forth wherein the composition comprises a blend of a polyamide wherein the amino to carboxyl end group ratio of the polyamide polymer is less than 1.0 when the relative viscosity of the polyamide polymer is less than 2.0, and less than 0.30 when the relative viscosity is in the range of 2.0 to 2.3 and less than 0.20 when the relative viscosity is greater than 2.3, a crystallizable polyester and an interfacial tension reducing agent.

Abstract: This invention discloses a process for producing a polyester resin having a low acetaldehyde generation rate comprised of the steps of polycondensing the polyester resin in the presence of tin and antimony; wherein the tin is present within the range of 50 to 110 ppm of the polyester resin and the antimony is present from 105 ppm to 265 ppm of the polyester resin, and solid phase polymerizing the polyester resin for sufficient time so as to increase the intrinsic viscosity of the polyester resin by at least 0.15 dl/g.

Abstract: A process for crystallizing a polyethylene naphthalate copolymer by:a) copolymerizing at least 60 mole % of 2,6-naphthalene dicarboxylic acid, based on the total moles of carboxylic acids, with polyols such as at least 80 mole % of ethylene glycol and from 2 mole % to 20 mole % of a polyol having three or more carbon atoms, each based on the total moles of polyols, to form PEN copolymer solids, andb) subsequently crystallizing the PEN copolymer solids by heating the solids to at least their sticking temperature at an average rate of at least 10.degree. C./min, to form agglomerate-free crystallized solids.The process may be performed under agitation. The pellets heated up in a during the crystallization step do not agglomerate or suddenly expand as the temperature rises to and through the sticking temperature of the PEN copolymers. The process allows one to rapidly heat up PEN during crystallization, and do so without conducting a prior drying step or a devolitilization step.

Abstract: To control the orientation of curative groups in an elastomer formulation, in order to maximize the properties obtained in the vulcanized elastomer, cure accelerators are deposited on the surface of a fiber. This method results in a fiber type orientation of crosslink sites in an elastomer matrix, resulting in enhanced modulus properties. An added benefit of the method is the chemical attachment of the fiber to the elastomer formulation, which also results in enhanced modulus properties.

Abstract: A process for making a random polyalkylene terephthalate/naphthalate copolymer by synthesizing a bis-(hydroxyalkyl)-naphthalate composition under transesterification conditions, and subsequently combining the bis-(hydroxyalkyl)-naphthalate, a terephthalic acid, and an alkylene glycol under direct esterification conditions to form a random polyaklylene terephthalate/naphthalate copolymer. The preferred bis-(hydroxyalkyl)-naphthalate is bis-(2-hydroxyalkyl)-2,6-naphthalate, with bis-(2-hydroxyethyl)-2,6-naphthalate being the most preferred. Preferably, the bis-(hydroxyalkyl)-naphthalate is added at the initial stage of an acid-based polymer process, and polymerization is initiated or continued to produce a polyester copolymer. Alternatively, the bis-(hydroxyalkyl)-naphthalate is added to phthalate-based oligomers after the initial direct esterification stage, and polymerization is continued to produce a polyester copolymer.