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Some Features of a Novel Gas Dispersion Impeller in a Dual-Impeller Configuration
Chemical Engineering Research and Design, 2003The performance of the concave blade BT-6 impeller was evaluated in a dual-impeller agitated tank (T= 0.48m, H/T=2). Power draw was measured and almost constant Pg/Pu ratio with aeration was found in agreement with what had been reported previously. Gas hold-up exhibited the same dependence on power per unit volume and superficial velocity as shown by ...
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An Evaluation of Impeller Blade Torque During an Impeller–Diffuser Interaction
Journal of Fluids Engineering, 2004An evaluation of the torque on an impeller blade interacting with a diffuser blade is presented. Comparisons of time averaged quantities are made between computed and measured results. The calculation of the impeller blade torque was based on the axial moment from fluid forces acting on a control volume surrounding an impeller blade passage.
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Chemical Engineering Science, 1995
Abstract Drop breakup in agitated vessels is one of the most important processes taking place in agitation of immiscible liquids. Suitability of a particular mixing equipment for liquid dispersion is usually studied in systems with very low fraction of the dispersed phase.
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Abstract Drop breakup in agitated vessels is one of the most important processes taking place in agitation of immiscible liquids. Suitability of a particular mixing equipment for liquid dispersion is usually studied in systems with very low fraction of the dispersed phase.
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