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Mechanisms and kinetics of the anionic polymerization of acrylates, 2. Polymerization of <i>tert</i>‐butyl acrylate in a flow tube reactor and effect of lithium chloride and lithium <i>tert</i>‐butoxide
56
Citations
13
References
1992
Year
Macromolecular ChemistryEngineeringOrganic ChemistryChemistryPolymersAnionic PolymerizationFlow Tube ReactorChemical EngineeringPolymer TechnologyMacromolecular EngineeringPolymer ProcessingPolymer ChemistryLithium ChlorideMaterials SciencePolymer EngineeringPolymer ReactionRapid MixingPolymer ScienceRapid PolymerizationsPolymerization KineticsChemical KineticsPolymer Synthesis
Abstract The kinetics and the molecular weight distributions (MWD) in the anionic polymerization of tert ‐butyl acrylate (tBuA) in tetrahydrofuran at 23 ± 3°C were investigated. Tert ‐butyl α‐lithioisobutyrate (tBiB‐Li) was used as the initiator in the absence and presence of the additives lithium chloride and lithium tert ‐butoxide (tBuOLi). A flow tube reactor was used which allowed very rapid mixing of reagents, within milliseconds. The polymerization is extremely fast, half‐lives being 0,01 s for the system without additive, 0,05 s for LiCl and 3 s for tBuOLi as an additive. The rate of termination was estimated from the strong UV absorption of the enolized β‐oxoester end group formed. The number‐average degree of polymerization is a linear function of conversion, the absolute values, however, demonstrate initiator efficiencies of only ca. 30%. The MWD's of the polymers formed are narrow ( M w / M n = 1,35 without additive, M / M n = 1,08 in the presence of LiCl and M w / M n = 1,77 in the presence of tBuOLi). After precipitation these values are reduced to 1,17; 1,06 and 1,32, respectively. Experiments in a stirred tank reactor and in ampoules lead to much broader MWD's. This shows that the rate of mixing has a strong effect on the MWD and is of substantial importance in these rapid polymerizations.
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