Dispersion kinetics in mechanically agitated vessel

¹ University of Bologna, Department of Civil, Chemical, Environmental, and Materials Engineering, Via Terracini 28, Bologna, Italy
² Czech Technical University in Prague, Faculty of Mechanical Engineering, Department of Process Engineering, Technická 4, 166 07 Prague, Czech Republic
³ Czech Academy of Sciences, Institute of Hydrodynamics v.v.i, Pod Paťankou 30/5, 166 12 Prague, Czech Republic

^* Corresponding author: radek.sulc@fs.cvut.cz

Published online: 28 June 2019

Abstract

Agitation of two immiscible liquids or solid-liquid suspension is a frequent operation in chemical and metallurgical industries. Prediction of mean drop/particle size and drop/particle size distribution (DSD) is vital for emulsification, suspension polymerization, solid particle dispersion or crystallization. Simulation of particulate systems requires the knowledge of DSD and its time evolution. The time evolution of drop size distribution was investigated in baffled vessel mechanically agitated by a Rushton turbine and a high-shear tooth impeller. The system water –silicone oil was used as a model liquid. The volume fraction of the dispersed phase was 0.047 %. The drop sizes were determined by image analysis. The time evolution of the drops size d_p32 was studied for both impellers tested. The model used involves the first order kinetics. Finally, the following correlations predicted by the Kolmogorov-Hinze theory were evaluated at steady state: d_p32/D = C1.We^-0.6 and d_pmax/D = C₂.We^-0.6, where We is the impeller Weber number.