A general method for the calculation of various types of phase diagram
s for aqueous electrolyte mixtures is outlined. It is shown how the th
ermodynamic equilibrium precipitation process can be used to satisfy t
he operational needs of industrial crystallizer/centrifuge units. Exam
ples of simulation and optimization of fractional crystallization proc
esses are shown. In one of these examples, a process with multiple ste
ady states is analyzed. The thermodynamic model applied for describing
the highly non-ideal aqueous electrolyte systems is the Extended UNIQ
UAC model. (C) 1998 Published by Elsevier Science Ltd. All rights rese
rved.