The term reactive extrusion characterizes a plastics processing method
in which an extruder is utilized for a continuous polymer synthesis a
nd modification. In this contribution, the production of polystyrene a
nd styrene-isoprene copolymers is described in a co-rotating, closely
intermeshing twin-screw extruder The results of process analysis show
that the living polymerization of styrene can be conducted in spite of
high reaction temperatures of 200-degrees-C in a screw reactor Proces
sing variants are homopolymers of styrene, copolymers of styrene-isopr
ene blends and sequential polymerization of styrene and isoprene; depe
nding on raw material, formulation and process parameters, this result
s in styrene polymers of quite different structural characteristics an
d final properties.