Abstract

Hydrodynamic experiments were conducted in a microbore helix based passive mixer for the system of HNO3/30% TBP/n-dodecane under non-mass transfer conditions. Hold up and drop sizes were experimentally measured for an aqueous phase flow rate of 0.15–0.80mL/min and organic phase flow rate of 0.10–0.75mL/min for various A/O ratios from 0.2 to 5. Although a fine dispersion was generated in the mixer, it did not affect coalescence and clear streams emerged from exit points of a mini settler (∼1.2mL). Due to smaller drop sizes generated, the observed specific interfacial area was huge and for the experimental conditions reported, it was ranged about 2.84×104 to 8.56×104m2/m3. It is of the same order of that observed in a 50-mm centrifugal extractor with identical aqueous-organic pair.

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