The paper presents a model of the motion of a particle subjected to several
transport processes in connection with mixing in two phase flow. A residen
ce time distribution technique coupled with a one-dimensional dispersion mo
del was used to obtain the axial dispersion coefficient in the Liquid phase
, D-ax. The proposed model of D-ax for an external-loop airlift bioreactor
is based on the stochastic analysis of the two-phase flow in a cocurrent bu
bble column and modified for the specific how in the airlift reactor. The m
odel takes into account the riser gas superficial velocity, the riser liqui
d superficial velocity, the Sauter bubble diameter, the riser gas hold-up,
the downcomer-to-riser cross sectional area ratio. The proposed model can b
e applied with an average error of +/-20%.