Article ID Journal Published Year Pages File Type
4998241 Chemical Engineering and Processing: Process Intensification 2017 7 Pages PDF
Abstract

•Extraction with chemical reaction was carried out in the Oldshue-Rushton column.•The slip and characteristic velocities of the reactive system (Sm, Gd and D2EHPA) were investigated.•Slip velocities in the reactive extraction system were higher than those in the physical systems.•The variation in the slip velocity is related to the interfacial active properties of D2EHPA.

The slip and characteristic velocities of the reactive system (samarium, gadolinium and D2EHPA) were investigated in the pilot plant Oldshue-Rushton extraction column. The experiments were carried out at the extraction and stripping stage. The influences of the agitation speed, dispersed as well as continuous phase velocity were studied. An increase in dispersed phase velocity led to the increase of the slip velocity while it decreased with agitation speed and continuous phase velocity. More buoyancy and faster upward movement of larger drops accelerate the slip velocity in the stripping condition as compared with the case of extraction condition. The experimental data were compared with the proposed correlations by Asadollahzadeh et al., and the related deviation was within 26% from these equations. Therefore, the modified correlations for prediction of slip and characteristic velocities were proposed with the experimental data and the data from the physical systems in the literature.

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Physical Sciences and Engineering Chemical Engineering Process Chemistry and Technology
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