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Optimum solids concentration for solids suspension and solid–liquid mass transfer in agitated vessels
Journal article   Peer reviewed

Optimum solids concentration for solids suspension and solid–liquid mass transfer in agitated vessels

Eng Ying Bong, Nicky Eshtiaghi, Jie Wu and Rajarathinam Parthasarathy
Chemical engineering research & design, Vol.100, pp.148-156
01/08/2015

Abstract

Agitated vessels Impeller energy efficiency Solids suspension Solid–liquid mass transfer
•Solid–liquid mass transfer was studied at high solids concentrations.•Specific impeller power consumption is the lowest for solids concentration of 0.2 (v/v).•Solid–liquid mass transfer coefficient (kSL) is the highest between solids concentration of 0.15 and 0.20 (v/v).•A mathematical correlation is proposed to estimate kSL with increasing solids concentration. The effect of solids concentration on specific impeller power consumption and solid–liquid mass transfer coefficient was investigated in a 0.2m diameter baffled agitated vessel with standard six-bladed Rushton turbine for solids concentration up to 0.40 (v/v). It was found that the increase of solids concentration significantly increases the mass transfer coefficient up to an optimum solids concentration and decreases thereafter when the system is operated at a just-suspended condition. The increase in mass transfer coefficient with an increase of solid concentrations is mainly due to the increase in Njs (critical impeller speed) with increasing solids concentration, thereby leading to an upsurge of turbulence around the particles. The solids concentration at which the highest mass transfer coefficient is obtained is designated as the effective solids concentration. In a geometrically similar 0.3m diameter tank, the trends in impeller energy efficiency and solid–liquid mass transfer coefficient values with increasing solids concentration are similar. The experimental data are satisfactorily correlated using the concept of the Kolmogoroff's theory of isotropic turbulence to develop an equation to estimate the solid–liquid mass transfer coefficient in agitated vessels.

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