The mathematical models of acrylonitrile-butadiene-styrene (ABS) latex
coagulation processes that show the effect of major operation variabl
es on the particle-size distribution of recovered resins were derived-
to provide a guideline for process improvement to reduce the content o
f fine particles in the product. Kinetic equations for the coagulation
and breakup of particles taking place in a turbulent flow field were
incorporated into the population balance models for batch and continuo
us processes. A dimensional analysis for the process models leads to t
wo dimensionless groups, eta(c) and eta(b) that represent the relative
intensity of the coagulation and breakup phenomena. The eta(c)/eta(b)
ratio is designated as a design variable for controlling the particle
-size distribution in the steady-state operation of the coagulation pr
ocesses. This role is demonstrated by numerical simulation where incre
asing the ratio shifted the particle-size distribution toward large pa
rticles. The estimates of eta(c)/eta(b) obtained for a set of batch ex
periments also confirm that fine particles can be reduced by setting t
he operation variables to increase the ratio.