H. Essadki et al., FRICTION ON A SOLID SPHERE EXPOSED TO GAS-LIQUID AND GAS-LIQUID-SOLIDFLOW IN BUBBLE-COLUMN AND FLUIDIZED-BED REACTORS, Journal of chemical technology and biotechnology, 62(3), 1995, pp. 301-309
Local velocity gradients on a solid spherical surface have been studie
d in a bubble column and in two- and three-phase fluidized beds, in or
der to clarify the influence of gas flow. The electrochemical method,
measuring apparent local mass transfer coefficients, was verified and
used to obtain the local velocity gradients, shear stresses and total
frictional forces. The observed mass transfer rate was independent of
liquid velocity, owing to a non-changing how structure around the part
icles and not to averaging opposing effects. The identity in flow stru
cture also held for three-phase fluidized beds up to a superficial gas
velocity of 5 cm s(-1). The dramatic increase in velocity gradient on
gas introduction was not a result of decreased homogenous density, bu
t was caused by a change in the turbulent structure around a particle,
leaving a larger portion of the total drag as frictional drag, thus i
mproving the mass transfer characteristics of the bed. Use of velocity
gradient measurements, including span of fluctuations and exposure ti
me, to predict biomass growth and mechanical degradation in a reactor
is also discussed.