A new synthesis method based on targeting is presented for the design
of stagewise continuous crystallization processes. The methodology det
ermines the optimal flow distribution to each of the crystallizers in
addition to other common control variables, including temperature, con
centration, and vessel volume The resulting optimization model yields
a boundary-value differential equation system, which is transformed in
to a set of nonlinear equations through orthogonal collocation and sol
ved numerically. For the synthesis of the continuous KNO3 crystallizat
ion process considered here, the predicted optimal network solution sh
ows that the common tradeoff between high yield and large average crys
tal sizes has been successfully eradicated by the new design approach.