This paper addresses design and control issues related to a continuous
crystallization process. Design addresses the configuration of actuat
ors for this process. Results from both model studies and from experim
ental analysis show how different operation and design choices, relate
d to the actuators, influence the process behaviour. The main conclusi
on is that classified removal of small crystals (fines) and large prod
uct crystals improves the shape of the crystal size distribution (CSD)
at steady-state, however, at the expense of open-loop cycling of the
CSD. A simple SISO feedback control strategy that acts on the fines re
moval rate can be used to stabilize these cycles effectively. Fine par
ticles are classified with an annular zone. The size of the annular zo
ne can be decreased without affecting the dynamic controllability, sig
nificantly. Classified removal of product crystals from the crystalliz
er is achieved with a vibrating screen. The aperture size of the scree
n and the flow feeding the screen are considered important design para
meters. Good product quality is obtained with a low feed flow and a la
rge aperture size. Controllability analysis further reveals that for b
oth designs only two degrees of freedom exist, i.e. a quantity related
to the small particles in the CSD and the total mass production rate
per unit of time can be controlled independently.