The process of antisolvent precipitation of particles, termed solution enhanced dispersion by supercritical fluids (SEDS (TM)), is applied to precipitate the model drug, paracetamol, from ethanol solutions. In the SEDS process the substrate solution is quickly mixed in a mixing chamber of the coaxial two-component nozzle with an antisolvent, represented in this case by the supercritical CO2. Resulting partially mixed, highly supersaturated solution is introduced into the precipitation vessel as a jet, which generates intensive circulation of residual fluids that dilute the fresh supersaturated solution. Nucleation starts in the nozzle chamber, whereas particle growth completes the process in the precipitation vessel. The process is carried out above the mixture critical pressure; the antisolvent is thus completely miscible with the solvent. Under such conditions the macro-, meso-, and micro-mixing processes can affect the particle size distribution (PSD) and should be considered when the process is scaled up. Scaling up considerations of the precipitation process are based on scale-up rules, CFD simulations and experimental data for paracetamol precipitation. In simulations the model presented earlier (Baldyga et al., 2004) that is based on the population balance equation and CFD modelling of compressible flow processes is applied. Results of experimental investigations and numerical simulations are applied to verify scale-up strategies for the SEDS processes. (C) 2010 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.