The main challenge in the design of industrial crystallisers is to predict
the influence of crystalliser geometry, scale, operating conditions and pro
cess actuators on the process behaviour and product quality. The quality ch
aracteristics, such as the crystal size distribution, inclusion content and
morphology determine to a large extent the product performance and are the
refore of importance. The quality of the product crystals is basically dete
rmined by the rates at which crystals are born and attrited, grow or dissol
ve and agglomerate in the different regions of the crystalliser. An analysi
s technique is therefore introduced to describe the various crystallisation
phenomena as a function of local process conditions such as supersaturatio
n and energy dissipation. This technique is based upon:
the derivation of pure kinetic parameters from an MSMPR experiment.
setting up compartmental models for design alternatives in order to separat
e kinetic and hydrodynamic phenomena.
analysis of the process behaviour of the design alternatives by applying th
e same kinetic model and parameters for each compartments.
optimisation of the design alternatives with respect to product quality usi
ng crystalliser geometry, operating conditions and the appropriate process
actuators, like a fines removal system, as degrees of freedom.
The advantage of this technique over conventional techniques is illustrated
for an evaporative DTB crystalliser. (C) 1999 Elsevier Science B.V. All ri
ghts reserved.