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Studies on transfer processes in mixing vessels: suspending of solid particles in liquid by modified Rushton turbine agitators
Authors:R. V. Roman  R. Z. Tudose
Affiliation:(1) Research Centre for Antibiotics, Chemical Pharmaceutical Research Institute, 6647-Valea Lupului, 6600 Jassy, Romania;(2) Faculty of Industrial Chemistry, Technical University "ldquo"Gh. Asachi"rdquo", Splai Bahlui 71, 6600 Jassy, Romania
Abstract:The modified blade turbines are attractive alternatives to the standard Rushton turbine as they do not require any modification in the electrical engine motor and drive assemblies are simple to manufacture and have a reduced power consumption.The modified blades were obtained through increase in the blade height of the Rushton turbine simultaneously with perforation of the blade surface. The field surface of the modified blade is equal to the blade surface of the standard Rushton turbine.In this study the modified blade turbine with the surface fraction of the perforations equal to 0.353 is used.The complete suspension speed and the power dissipation in transition and turbulent regimes using standard and modified Rushton turbine agitators positioned singly or doubly on same shaft, in five solid-liquid systems were investigated.The solid particles used have the mean diameter between 15–1000 mgrm.The modified blade turbine, noted as TP3, was found to be more efficient than the standard turbine in complete and homogeneous suspension.List of Symbols A distance between turbine and the vessel bottom (m) - c dimensionless constant (-) - d agitator diameter (m) - dp surface-to-volume mean diameter of the particle (m) - D vessel diameter (m) - (HL)1 suspension height for one turbine immersed (m) - (HL)2 suspension height for two turbines immersed (m) - K consistency index (Pa sn) - lk eddy-size characteristic (m) - N flow behaviour index (-) - Np number of blades of the mixing system (-) - N agitator speed (s–1) - Njs agitator speed that just causes complete suspension (s–1) - Ne PL/rhovLN3d5 power number in liquid system (-) - (Ne)g Pg/rhovspN3d5 power number in solid-liquid system (-) - PL power consumption in liquid system (W) - Ps power consumption in solid-liquid system (W) - r coefficient of correlation (-) - R distance between turbines (m) - Re rhovspNd2/eegra Reynolds number (-) - S suspension parameter in Zwietering equation (2) (-) - SC full surface of the blade (m2) - SG surface of the perforations applied on the blade (m2) - SG/SC surface fraction of the perforations (-) - X particle concentration (g/l) - w baffle width (m) - epsivjs specific power input per mass at the complete suspension state (W/kg) - eegra apparent viscosity under mixing conditions (Pa s) - ngrL kinematic viscosity of the liquid (m2/s) - rhovL density of liquid (Kg/m3) - rhovs density of solid (Kg/m3) - rgrsp density of suspension (Kg/m3)
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