I am looking for ways to increase the average molecular weight of expanded polystyrene (EPS) produced through a Free Radical Suspension Polymerization process. Currently, we use a two-stage initiation system consisting of dibenzoyl peroxide (BPO) as the primary initiator and tert-butyl peroxy-2-ethylhexyl carbonate as the secondary initiator to control residual monomer. While reducing the BPO concentration has led to an increase in molecular weight, further reductions are constrained due to process limitations. Our production process is conducted in 50-ton reactors, and we are exploring alternative approaches without significantly altering the overall process parameters. Specifically, we are limited by the reactor's pressure limit of 12 bar, preventing us from significantly increasing the reaction temperature, and by production rate constraints that limit the available reaction time.