Abstract: A process is provided for producing staple fibers that may be used in the formation of carpets from poly(trimethylene terephthalate). Poly(trimethylene terephthalate) may be melt spun to form filaments. The melt spun filaments may then be cooled with a liquid having a temperature of at most 20° C. The cooled filaments may then be drawn, and the drawn filaments may be cut into staple fibers. The resulting staple fibers have highly uniform physical characteristics such as denier, tenacity, and elongation at break that render the fibers particularly useful for forming carpets.

Abstract: The present invention provides a process of reducing acrolein byproduct from polytrimethylene terephthalate using selected phosphorous compounds to contact the polytrimethylene terephthalate or reactants in the process of producing polytrimethylene terephthalate. The selected phosphorous compounds are retained in the polytrimethylene terephthalate. The present invention also provides polytrimethylene terephthalate compositions containing amounts of phosphorous compounds.

Abstract: The present invention provides a process of reducing acrolein by product from polytrimethylene terephthalate using selected phosphorus compounds to contact the polytrimethylene terephthalate or reactants in the process of producing polytrimethylene terephthalate. The selected phosphorus compounds are retained in the polytrimethylene terephthalate. The present invention also provides polytrimethylene terephthalate compositions containing amounts of phosphorus compounds.

Abstract: A process for the production of polytrimethylene terephthalate (PTT), wherein the process comprises: (i) one or more esterification steps, wherein terephthalic acid (TPA) or an alkyl diester of terephthalic acid is reacted with 1,3-propanediol (PDO); and (ii) one or more subsequent polycondensation steps, wherein the process further comprises the addition of a protic acid, other than terephthalic or isophthalic acid, before and/or during the one or more esterification steps, wherein the protic acid has a dissociation constant of at most 4 (pKa measured in water at 25° C.), and wherein the total amount of protic acid added before and/or during the one or more esterification steps is in the range of from 0.001 to 10 millimole of acid per kilogram of polytrimethylene terephthalate produced.

Abstract: The friability of crystallized PTT and solid stated PTT can be effectively reduced by lowering the temperature of the quenching water used in the pelletizing of the melt polycondensation polymer to between 32° F. (0° C.) and 65° F. (18° C.). In addition, the robustness of solid stated PTT pellets is effectively increased by using a prepolymer with a lower intrinsic viscosity (IV) or by increasing the IV of the solid stated product.

Abstract: The friability of crystallized PTT and solid stated PTT can be effectively reduced by lowering the temperature of the quenching water used in the pelletizing of the melt polycondensation polymer to between 32° F. (0° C.) and 65° F. (18° C.). In addition, the robustness of solid stated PTT pellets is effectively increased by using a prepolymer with a lower intrinsic viscosity (IV) or by increasing the IV of the solid stated product.

Abstract: The invention relates to a process for the preparation of polyesters of a glycol and a dicarboxylic acid which comprises the following steps: a) introducing a feedstock comprising one or more glycols and one or more dicarboxylic acids or monoalcohol esters thereof into a reactor vessel, b) heating the feedstock to an elevated temperature to cause the glycols and the acids or monoalcohol esters thereof to polycondense into a polyester, c) removing all of the polyester from the reactor vessel, wherein step b) is carried out in the absence of a preformed polyester (“zero heel” process). A condensation catalyst is added in step a) or b) or both.

Abstract: The invention relates to a process for the preparation of polyesters of a glycol and a dicarboxylic acid which comprises the following steps: