In this contribution a method for the calculation of crystal-crystal collis
ions in the flow field of an industrial crystalliser is proposed. The metho
d consists of two steps. The first step is to simulate the internal Row of
the crystalliser as a whole. For this purpose, the simulation of the intern
al Row of an 1100 1 draft tube baffled crystalliser at a Reynolds number of
240,000 is presented. This simulation was done with a lattice-Boltzmann sc
heme with a Smagorinsky sub-grid-scale turbulence model (c(s) was 0.11) on
approximately 35.5 x 10(6) grid nodes. The second step of the method consis
ts of simulating individual crystals in a fully periodic box with turbulent
conditions that represent the conditions in a point of the crystalliser. T
hus collision frequencies and intensities of the crystals under the local h
ydrodynamic regime can be obtained. In this contribution a feasibility stud
y of this second step is described. A theoretical framework is established
to identify the key parameters that determine the relationship between the
crystalliser flow and the box simulations. Based on this framework, conditi
ons for box simulations representing three monitor points in the simulated
crystalliser are calculated. Finally, to demonstrate the method of predicti
ng the motion of individual particles, sedimentation and consecutive collis
ion of a single sphere with a solid wall is simulated. (C) 2001 Elsevier Sc
ience Ltd. All rights reserved.