Article ID Journal Published Year Pages File Type
168218 Chinese Journal of Chemical Engineering 2014 8 Pages PDF
Abstract

The liquid–solid countercurrent fluidization process in an extraction column was numerically simulated based on the particle trajectory model of Eulerian–Lagrangian method. The simulation approach was validated by previous experiments. A power function correlation was proposed for dimensionless slip velocity Uslip/Ut and hold-up fraction ϕ, and the operational zone in the countercurrent fluidization was determined. Simultaneous countercurrent fluidization of particles with different diameters was also simulated. The comparison shows that the simulation results are consistent with the calculation values from the multi-particle free sedimentation model based on non-interference assumption, verifying the reliability of the approach in present work.

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Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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