Analytical studies were attempted to make clear the flow patterns of the liquid in the cylindrical mixing vessel without baffles, as the experimental results had already been obtained as shown in the previous reports.We could not well explain the details of the liquid flow patterns in the vessel by means of the so-called “Rankine's combined vortex” model (Refer to Fig. 1 and Eq.(1)). Therefore, we studied three important factors contributing to the momentum transfer in the agitated liquid; i.e., the liquid viscosity, the displacement of the liquid by the agitating impeller and the secondary circulation flow which is induced by the discharge flow from the tips of the impeller blades.In the range where Reynolds number was very small, the momentum transfer due to the viscosity effect was found to be predominant, so that the analytical results, obtained upon the assumption that the effects of the two factors other than the liquid viscosity are negligible, had a tendency to show good agreement with the experimental data on the tangential velocity distribution of the liquid in the vessel, as shown in Figs. 4 and 5.On the other hand, in the turbulent flow range where Reynolds number was very large, the secondary circulation flow had considerably important effects on the liquid flow pattern. Considering its contribution to the momentum transfer (Refer to Fig. 6), Eqs.(10) and (13) were analytically derived to express the tangential velocity distribution of the agitated liquid. The comparisons between the experimental data and the calculated results by these equations are shown in Fig. 8. They show good agreement.Furthermore, there were obtained data on the distributions of the turbulent kinematic viscosity and the static pressure in the vessel, as shown in Figs. 9 and 10, respectively.These results are considered to show the utility of the analysis.
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