V. Alopaeus et al., Simulation of the population balances for liquid-liquid systems in a nonideal stirred tank. Part 1 Description and qualitative validation of the model, CHEM ENG SC, 54(24), 1999, pp. 5887-5899
A simulation model has been developed to model drop populations in a stirre
d tank. A multiblock stirred tank model has been used with the drop populat
ion balance equations developed in the literature. The stirred tank is mode
led separately so that local turbulent energy dissipation values and fluid
flows are used in the drop breakage and coalescence functions. This model h
as several attractive features, e.g. it can predict the inhomogenity of dis
persions and some scale-up phenomena. Because local conditions can be used
in the drop rate functions needed in the population balances, it is possibl
e to take these fundamental processes into closer examination. It seems tha
t the parameter values in the drop breakage and coalescence models depend o
n flow and turbulence averaging for the vessel. This proposes that for "int
rinsic" drop breakage and coalescence rates, a multiblock model for the sti
rred tank is needed in parameter estimation as well. The stirred tank flow
model may be obtained from measurements or from computational fluid dynamic
s simulations in a straightforward manner. (C) 1999 Elsevier Science Ltd. A
ll rights reserved.