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Overall apparent number of transfer based on continuous phase.
Overall mass transfer coefficient based on continuous phase, s−1.
Overall height of transfer unit based on continuous phase, m.
Overall number of transfer units based on continuous phase.
Overall apparent height of transfer unit based on continuous phase, m.
Overall apparent mass transfer coefficient based on continuous phase, s−1.
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Hot spots existed on the continuous phase in zones perpendicular to the solid cubes and cold spots were in between the particles where the current density lacks.
For all stages, the efficiency curves derived from trajectories based on mean continuous phase velocities overestimate the 50% cut diameters and have unrealistically steep slopes when compared to the experimental calibration results.
The following correlation is developed by Venkatanarasaiah and Varma [17] for the prediction of overall apparent mass transfer coefficient based on the continuous phase: it K_{text{ocp}} a = K cdot ({text{Af}})^{0.84} cdot d_{text{o}}^{ - 0.21} cdot alpha^{ - 0.44} cdot p^{ - 0.41} cdot u_{text{d}}^{0.91}.
The equivalent number of ideal stages evaluated from the model is related to the flow numbers defined, based on the continuous phase velocity, the vibrating speed and plate geometry, which are the significant variables affecting the axial mixing of the continuous phase.
Further, in this study the effects of the Reynolds number (Reo), internal to external fluid characteristic viscosity ratio (k) and power-law index (no) on the continuous phase flow field, pressure drag (Cdp), friction drag (Cdf) and total drag (CD) coefficients have been analyzed over the range of parameters: 5⩽Reo⩽500, 0.1⩽k⩽50 and 0.6⩽no⩽1.6.
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