Numerals0 = mid axis origin 1 2 1 h = experimental = initial condition or upper phase = final condition or lower phase LITERATURE CITED 1. Cockbain, E. G., and T. S. McRoberts, J. Colloid Sci., 8, 440 ( 1953).
Simultaneous population and mass balances have been solved together with a generalizedform of nucleation-growth rate kinetics to obtain the form of crystal size distribution (CSD)for several idealized modes of crystallizer operation, including seed crystal removal, product classification, arbitrary solids concentration, and staged vessels. The effect of holding time and feed supersaturation on crystal size in a mixed suspension, mixed product removal (MSMPR) crystallizer was also studied. A representative CSD from an MSMPR crystallizer plus the relative kinetic order of nucleation to growth rate can be used to predict CSD from any of the above modes of operation.Crystal size distribution (CSD) is one of the most important and troublesome properties of an operating crystallizer and is a property which cannot presently be designed without prior experience with the crystal system and the type of crystallizer used. Saeman (I), in a classical con-A notable addition to the recent literature is a paper by Bennett (7) which tabulates experimental CSD data from a large class of crystallizers and crystal systems. A property of any CSD is the so-called coeficient of variation (C.V.)," or relative size spread over which the majority +a Not to be confused with coefficient of velocity, also referred to as