In this work, the numerical simulation of the non-isothermal steady co-extrusion fiber spinning with flow-induced crystallization is explored. The model is based on the formulation originally proposed by China et al. in which Newtonian and Phan-Thien-Tanner (PTT) fluids are considered the core and the skin layer, respectively. The polymeric flow rate fraction, Deborah dimensionless number and the PTTs parameters on the temperature, the velocity and the crystallization profiles are analyzed. The numerical results show: the temperature profile is sensitive to the polymeric layer flow rate and the deformation parameters (shear thinning and extensional), the tensile stress induced crystallization parameter has a strong influence at the onset of...
A numerical model that incorporates temperature-dependent non-Newtonian viscosity was developed to s...
Semi-crystalline fibers, such as nylon, orlon, and spectra, play a crucial role in modern society in...
The efficiency of polymer extrusion processes can be severely limited by the occurrence of viscoelas...
Fiber spinning and extrusion flow in general, of viscoelastic liquids through dies, are the primary ...
Amacroscopic model for the description of low- and high-speed fiber spinning of crystallizing polyme...
A macroscopic model for the description of low- and high-speed fiber spinning of crystallizing polym...
Traditionally ultrafine fibers below 1 dpf are produced by extrusion followed by mechanical drawing....
Abstract Flow-induced crystallisation in the course of melt spinning changes properties of as-spun f...
Short fiber-filled polymers experience increasing applications in melt extrusion additive manufactu...
Extrusion of viscoelastic liquids through planar and circular dies to form films and fibers is a fun...
A continuum-level model for non-isothermal polymer crystallization following a complex flow is prese...
A model is presented to describe flow-induced crystallization in isotactic polypropylene at high she...
In many spinning processes, as for example in dry spinning, solvent evaporates out of the spun jets ...
In this dissertation a model of melt spinning (by Doufas, McHugh and Miller) has been investigated. ...
The purpose of this work is to present a 2-D thermo-rheological model for high take up velocities th...
A numerical model that incorporates temperature-dependent non-Newtonian viscosity was developed to s...
Semi-crystalline fibers, such as nylon, orlon, and spectra, play a crucial role in modern society in...
The efficiency of polymer extrusion processes can be severely limited by the occurrence of viscoelas...
Fiber spinning and extrusion flow in general, of viscoelastic liquids through dies, are the primary ...
Amacroscopic model for the description of low- and high-speed fiber spinning of crystallizing polyme...
A macroscopic model for the description of low- and high-speed fiber spinning of crystallizing polym...
Traditionally ultrafine fibers below 1 dpf are produced by extrusion followed by mechanical drawing....
Abstract Flow-induced crystallisation in the course of melt spinning changes properties of as-spun f...
Short fiber-filled polymers experience increasing applications in melt extrusion additive manufactu...
Extrusion of viscoelastic liquids through planar and circular dies to form films and fibers is a fun...
A continuum-level model for non-isothermal polymer crystallization following a complex flow is prese...
A model is presented to describe flow-induced crystallization in isotactic polypropylene at high she...
In many spinning processes, as for example in dry spinning, solvent evaporates out of the spun jets ...
In this dissertation a model of melt spinning (by Doufas, McHugh and Miller) has been investigated. ...
The purpose of this work is to present a 2-D thermo-rheological model for high take up velocities th...
A numerical model that incorporates temperature-dependent non-Newtonian viscosity was developed to s...
Semi-crystalline fibers, such as nylon, orlon, and spectra, play a crucial role in modern society in...
The efficiency of polymer extrusion processes can be severely limited by the occurrence of viscoelas...