HOMOGENEOUS MULTICOMPONENT AZEOTROPIC BATCH DISTILLATION

Mixed waste-solvent streams generated in pharmaceutical and specialty chemical manufacturing typically form multicomponent azeotropic mixtur es. This highly nonideal behavior often prevents separation and recove ry of the solvents. Batch distillation remains an important separation technology for these industries. The sequence of pure component and a zeotropic cuts produced in batch distillation depends strongly on the feed composition. For ternary- and four-component mixtures the separat ion behavior can be studied graphically in residue-curve maps. For mix tures with more components, this approach is infeasible. Other tools a re therefore required. Deficiencies in earlier work on ternary systems are demonstrated and addressed as well as a complete set of concepts to describe batch distillation of an azeotropic mixture with an arbitr ary number of components. The body of theory is derived from the field s of nonlinear dynamics and topology.