Temperature and volume rate impact of the polymer melt on the sizes of the vortex area has been considered. The vortex area appears during the flow at the inlet of the slotted channel. A modified Vinogradov and Pokrovskii rheological model is used for the mathematical modeling of three-dimensional flow of the melt in the convergent plane-parallel channel. This model was extended to take account of the nature of non-monotonic gradient dependence of elongation viscosity. On the solid wall the sticking conditions were used for velocity. The temperature dependence of the initial shear viscosity of the polymer melt has Arrhenius form. The initial relaxation time was rated by comparison with experimental data for agradient based stationary viscosity in uniaxial tension, and on the basis of the molecular-kinetic approach. Discrete analogues of a system of equations of the dynamics for the polymer liquid were obtained via the method of controlling the volume with the division due to physical processes. The numerical algorithm was implemented so that the technology of parallel computing based on GPU was conveniently used. Calculations of hydrodynamic characteristics of polymer melt flows at different temperatures in a convergent channel with a rectangular cross section have shown that the sudden narrowing of the channel leads to the appearance of eddy flows. The sizes of these flows pass through a maximum with increasing melt temperature which is detected in the experiments. It also confirms that the rheological model can be used for the flows of polymer melts in areas with complex geometry. The results are proving the effectiveness of CUDA technology parallel computing for unsteady calculations of three-dimensional flows of nonlinear viscoelastic fluids with rheological law of behavior in differential form. The above calculations show that some convergent flow of polymermelts may show substantial three-dimensional picture, which manifests itself in a velocity component in a neutral flow direction. This should be taken into account when arranging experiments, as there are methods that cannot measure all velocity components. Also note that the velocity profile in the slit of the channel is set at a considerable distance from the entrance to the channel.
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