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On the kinetics of polymerization and copolymerization of poly(oxyethylene) macromonomers and styrene
62
Citations
45
References
1992
Year
Polymer ParticlesEngineeringMacromolecular ChemistryChemistryPolymersChemical EngineeringPolymer MaterialMacromolecular EngineeringPolymer ProcessingParticle ConcentrationPolymer ChemistryMaterials ScienceBiopolymersDispersion PolymerzationPolymer SciencePolymer CharacterizationPolymerization KineticsPolymer ReactionPolymer Synthesis
Abstract The homogeneous and the dispersion polymerzation 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°C. The batch polymerizations in N , N ‐di‐methylformamide 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 ) 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 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 increses up to 50% conversion. The particle growth is suggested to proceed via association of partcles and by propagation within polymer particles. The decrese of the number of radicals per particles as conversion proceeds is ascribed to the decrese 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.
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