A mathematical model of the mixing process in a two-rotor mixer is proposed
. The model developed takes into account the interrelations among the follo
wing essential features of the process: non-isothermal effects due to heat
exchange and energy dissipation in flow, non-Newtonian behavior of a materi
al and dependence of its properties on temperature and the degree of filler
agglomerate destruction, kinetics of changing carbon agglomerate sizes due
to mechanical distraction. The system of governing equations is formulated
and the procedure of its solution is described.
The theoretical model is compared with experimental data obtained in real t
echnological process of mixing of a rubber compound. In all cases quite sat
isfactory results of comparison were obtained. It means that the model prop
osed can be used for analysis of real technological processes of mixing and
choice of optimal technological regime and geometrical sizes of a mixer (p
rimarily size of the gap between a rotor and the wall of a chamber) as well
.