Experiments have been conducted to investigate the hydrodynamics
and mass transfer performance of some alternative mobile bed packings.
The polypropylene packings used in this work were 50 x 38 mm oblate
spheroids, 38 mm diameter plain spheres, 25 mm diameter plain spheres
and 25 mm diameter slotted spheres.
The perspex column was 22 cm internal diameter and 144 cm high and
was fitted with a supporting grid having 72% open area.
In the hydrodynamics studies, air and water were passed counter
currently through the column. Bed pressure drop, mean expanded bed
height, minimum expanding gas velocity and volume of liquid hold up for
all of the packings were measured at different air and water rates and
with two bed static heights of 10.5 and 16.5 cm.
The general hydrodynamic behaviour of the fluidized packings has
been observed and factors influencing pressure drop, liquid hold up,
expanded bed height and minimum expanding velocity have been identified.
Evidence for gas and liquid flow through the interiors of the slotted
packings and giving rise to higher liquid hold up and a smoother quality
of fluidization as compared with the other packings has been found.
Plain spheres and oblate spheroid packings appeared to have almost
identical hydrodynamic behaviour, although the oblate spheroid was found
to show more slugging fluctuation in the bed height at high gas
veloci ti e s .
In mass transfer studies, dilute C02 (2% voV Vol) was absorbed
into sodium hydroxide solutions and the interfacial area and liquid film
transfer coefficient were thereby established employing the pseudo first
order reaction model for the rate of absorption (known generally as the
Danckwerts' model) (41).
The experimental results on the Danckwerts' plot lay on a straight
line and therefore confirmed the applicability of the Danckwerts' model
from which (kL) and (a) could be estimated.
The interfacial area per unit volume of expanded bed (a) and per
unit volume static bed (as) was found to be higher for the slotted
packings than for the plain sphere packings and the oblate spheroid
packi ngs.
The interfacial area per unit volume of liquid hold up (aL) was
higher for the plain sphere packing than for the oblate spheroid and the
slotted sphere packings, however, the (a) and (as) for the plain sphere
packings were higher than for the oblate spheroid packings.
The liquid film transfer coefficient for the slotted sphere
packings was higher than for the other packings and was found to be
almost the same for the plain sphere and the oblate spheroid packings.
The operational mass transfer efficiency (defined as the ratio of
the volumetric liquid film mass transfer coefficient to the fluid energy
consumption in the bed) for the oblate spheroid packings was found to be
higher than for the plain and slotted sphere packings. This efficiency
ratio was also found to be higher for the slotted packings than for the
plain sphere packings. Finally, the slotted packings appear to offer
high volumetric mass transfer coefficients with a smoother quality of
fluidization and homogeneous contacting of gas and liquid
