A. Kumar et S. Hartland, PREDICTION OF DROP SIZE, DISPERSED-PHASE HOLDUP, SLIP VELOCITY, AND LIMITING THROUGHPUTS IN PACKED EXTRACTION COLUMNS, Chemical engineering research & design, 72(A1), 1994, pp. 89-104
Empirical correlations for the prediction of drop size, dispersed-phas
e holdup, slip velocity, and maximum throughputs in packed columns are
presented. Published experimental results obtained with both random a
nd ordered packings are considered. The drop-size correlation, which i
s based on measurements from 376 runs with and without mass transfer f
rom nine different sources for conditions when the continuous phase we
ts the packing, reproduces the data with an average absolute value of
the relative deviation of 15.7%. A large bank of data (2023 points wit
h and without mass transfer from 10 different groups of investigators;
continuous-phase wetting; d(p) > d(p, cr) for random packings; phi <
phi(f)) has been used to develop a correlation for the prediction of d
ispersed-phase holdup. The same body of data has also been used to der
ive a correlation for slip velocity without using holdup. By using the
correlation for dispersed-phase holdup, the average absolute values o
f the relative deviation in holdup and slip velocity are 18.7 and 16.4
%, respectively. The corresponding figures for the slip-velocity corre
lation are 20.1 and 15.6%, respectively. On the basis of data from 845
measurements with both continuous-phase and dispersed-phase wetting,
an equation for maximum throughputs is derived which reproduces the da
ta with an average absolute value of the relative deviation of 19.5%.