Although emulsion polymerization has been used for a long time, relatively
little attention has been paid to the technological issues of this polymeri
zation technique. This paper describes the research on chemical engineering
aspects of emulsion polymerization in (semi-)batchwise operated stirred ta
nks. The objective of this work was to improve the operation of current pro
cesses and to allow for improvements in the development of novel emulsion p
olymerization processes. For this purpose, different issues have shown to b
e important, for which the work described in this paper has been focused on
four topics: emulsification, colloidal stability, rheology in high solids
polymerization and heat transfer. These topics have been studied using the
polymerization of styrene and vinyl acetate as two representative model sys
tems.
Our results reveal that sufficient emulsification is essential for proper c
ontrol of the polymerization process. For the emulsifier used in this study
, the colloidal stability of the polymer particles is mainly governed by th
e physico-chemical properties of the reaction mixture. During high solids e
mulsion polymerization, the particle size distribution of the polymer parti
cles considerably influences the rheological properties of the reaction mix
ture and thereby the Row pattern in the reactor. Heat transfer to the react
or wall depends strongly on reactor geometry, impeller type and diameter as
well as stirrer speed. Additionally, the physical properties of the reacti
on mixture, being related to solids content, conversion and monomer type, a
re important for heat transfer.