ON THE KINETICS OF POLYMERIZATION AND COPOLYMERIZATION OF POLY(OXYETHYLENE) MACROMONOMERS AND STYRENE

The homogeneous and the dispersion polymerization and copolymerization of methacryloyl-terminated poly(oxyethylene) (MMA-PEG) and of p-vinylbenzyl-terminated poly(oxyethylene) (St-PEG) macromonomers and styrene, initiated by a radical initiator, was investigated using conventional gravimetric and NMR methods at 60-degrees-C. The batch polymerizations in N,N-dimethylformamide and in ethanol/water were conducted to either low or high conversion. The fractional conversion rates of the solution polymerization and copolymerization indicate that the homopolymerizations of macromonomers involve steady-state conditions, whereas copolymerizations proceed under non-stationary conditions. The ratios of the rate constants for propagation and termination (k(p)/k(t)0,5) for polymerization and copolymerization of MMA-PEG and St-PEG are by one order of magnitude higher than that for styrene. The increase in k(p)/k(t)0,5 is more pronounced in dispersion polymerization, which is ascribed to the decrease of both k(p) and k(t). The rates of dispersion polymerization are proportional to the particle concentration. The number of particles increases up to 50% conversion. The particle growth is suggested to proceed via association of particles and by propagation within polymer particles. The decrease of the number of radicals per particle as conversion proceeds is ascribed to the decrease of the growing radical activity and to the transfer of monomeric radicals to the continuous phase. The molecular weights correlate inversely with the particle size.