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Study of the liquid circulation velocity in external-loop airlift bioreactors
Authors:M Gavrilescu  R Z Tudose
Institution:(1) Present address: Faculty of Industrial Chemistry Department of Transfer Phenomena and Chemical Engineering Technical University of Iasi, 6600 IASI, Romania;(2) Research Center for Antibiotics, Chemical Pharmaceutical Research Institute, Valea Lupului no. 1, 6647 IASI, Romania
Abstract:Liquid circulation velocity was studied in externalloop air-lift bioreactors of laboratory and pilot scale, respectively for different gas input rates, downcomer-to-riser cross-sectional area ratio, A D/AR and liquid phase apparent viscosities.It was found that, up to a gas superficial velocity in the riser v SGR ap 0.04 m/s the dependency of v SLR on v SGR is in the following form: v SLR = a v SGR b , with the exponent b being 0.40. Over this value of v SGR, only a small increase in liquid superficial velocity, v SLR is produced by an increase in v SGR. A D/AR ratio affects the liquid superficial velocity due to the resistance in flow and overall friction.For non-Newtonian viscous liquids, the circulation liquid velocity in the riser section of the pilot external-loop airlift bioreactor is shown to be dependent mainly on the downcomer-to-riser cross-sectional area ratio, A D/AR, the effective (apparent) liquid viscosity, eegr eff and the superficial gas velocity, v SGR.The equation proposed by Popovic and Robinson 11] was fitted well, with an error of ± 20%.List of Symbols A D m2 downcomer cross-sectional area - A Rm2 riser cross-sectional area - a = coefficient in Eq. (7) - b = exponent in Eq. (7) - c s m–1 Coefficient in Eq. (3) - D D m downcomer diameter - D R m riser diameter - g m2/s gravitational acceleration - H D m dispersion height - H L m ungassed liquid height - K Pa s n consistency index - K B = friction factor at the bioreactor bottom - K F = friction factor - K T = friction factor at the bioreactor top - V L m3 liquid volume in the bioreactor - V D m3 liquid volume in downcomer - V R m3 liquid volume in riser - v LDm/s downcomer linear liquid velocity - v LR m/s riser linear liquid velocity - v SGR m/s riser superficial liquid velocity - v SLR m/s riser superficial liquid velocity - 
$$\dot \gamma $$
s–1 shear rate - epsi GD = downcomer gas holdup - epsi GR = riser gas holdup - eegr eff Pa s effective (apparent) viscosity - tau Pa shear stress The authors wish to thank Mrs. Rodica Roman for the help in experimental data collection and to Dr. Stefanluca for the financial support.
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