The hydrodynamic behaviour of an external airlift reactor is modelled
using simple elementary models : the liquid now in the riser and the d
owncomer is represented as plug flow with axial dispersion, while the
gas-liquid separator and the bottom junction are considered as CSTR's
for the liquid The system of differential equations resulting from the
mass balances applied to the different sections of the reactor are so
lved in the real time domain using a powerful software (MODEST). The m
odel parameters are evaluated by adjusting the experimental and simula
ted responses reactor to a tracer impulse injection at six different l
ocations in the riser and the downcomer. A sensitivity analysis shows
that the liquid velocities determined this way are much more precisely
known than the axial dispersion coefficients. The velocities thus obt
ained compare well with data measured by a thermal tracer technique.