A precipitation process is considered in which completely miscible solution
and supercritical antisolvent are passed through premixing and diluting zo
nes of a turbulent flow. The influence of flow velocity on particle size an
d nuclei concentration is discussed in terms of mixing and precipitation ti
me constants and their supersaturation dependencies. The proposed model all
owed the major process parameters such as supersaturation profile, mixed fl
uid fraction and mean particle size to be calculated and compared with expe
rimental data. For the crystallization system paracetamol/ethanol/CO2 studi
ed, the supersaturation profile becomes established at Re congruent to 10(4
). The particle size and shape are defined. firstly. by increase of supersa
turation and relative volume of mixed (on molecular scale) fluid with incre
ase of flow velocity and, secondly, by decrease of residence time available
for nucleation with increase of flow velocity. These competitive processes
can result in minimum particle size at a defined flow rate, (C) 2001 Elsev
ier Science Ltd. All rights reserved.