Article ID Journal Published Year Pages File Type
7089671 Chemical Engineering and Processing: Process Intensification 2016 6 Pages PDF
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 0.15-0.80 mL/min and organic phase flow rate of 0.10-0.75 mL/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 (∼1.2 mL). 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 × 104 m2/m3. It is of the same order of that observed in a 50-mm centrifugal extractor with identical aqueous-organic pair.
Related Topics
Physical Sciences and Engineering Chemical Engineering Process Chemistry and Technology
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