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In previous papers of this work methodologies have been established i) to predict the molecular weight distribution (MWD) of living polymerisation processes in various reactor configurations, ii) and -in a reversed calculation process -to design reactor parameters and feed profiles for a single CSTR or a tubular reactor to meet a target MWD. In this paper a model of a series of continuous stirred tank reactors (CSTRs) with various initiator and monomer feed strategies have been used todoi:10.3311/pp.ch.2010-1.03 fatcat:mvgaqjryorh55herb4jiqtiq44