In this payer, a 1D hydrodynamic model has been developed for gas hold-up a
nd liquid circulation velocity prediction in air-lift reactors. The model i
s based on momentum balance equations and has been adjusted to experimental
data collected on a pilot plant reactor equipped with two types of gas dis
tributors and using water and water/butanol as the liquid phase. Different
techniques of signal analysis have also been applied to pressure fluctuatio
ns in order to extract information about flow regimes and regime transition
s. A good knowledge of the now pattern is essential to establish adequate c
orrelations for the hydrodynamic model.