The present study deals with simulation of agglomeration reactors, based on
a CFD calculation method for describing the turbulent flow field, coupled
with a direct Monte-Carlo method for the agglomeration process. The potenti
ality of stochastic methods, well suited for simulation of spherical agglom
eration where complex kernels have to take into account the effects of the
particles size and of the composition of binding agent, is illustrated. Fur
thermore, it is shown that the coupling between hydrodynamics and kinetics
makes it possible to model very complex processes, and also to scale-up tho
se processes from batch to continuous mode operation. Application and resul
ts are presented for the complex case of agglomeration in suspension of an
organic pigment, performed in a standard stirred vessel equipped with a pit
ched blade turbine. (C) 2001 Elsevier Science Ltd. All rights reserved.