ABSTRACT:The formation of cyclic oligomers in the process of the anionic polymerization of E-caprolactam was studied. Cyclic oligomer contents increased with chain initiator concentration and decrease in catalyst concentration. Cyclic dimer content was much higher than that of cyclic trimer to cyclic hexamer and sensitively influenced by the concentrations of catalyst and chain initiator in comparison with cyclic trimer to cyclic hexamer. A mechanism is proposed in which cyclic dimer is peculiarly formed at the acyl-lactam terminal group.KEY WORDS Cyclic Oligomer/ Cyclic Dimer/ Nylon 6/ Anionic Polymerization/ E-Caprolactam/ Catalyst/ Chain Initiator / The anionic polymerization of e-caprolactam has been extensively investigated because of the high yield and rate of polymerization. 1 -4 Fundamental features such as various catalysts, 2 • 5 • 6 propagation mechanism, 7 -10 and kinetics 11 -16 are well known.The authors carried out systematic studies directed on high molecular weight nylon 6 and obtained stable high-molecular weight polymer (the weight average molecular weight, Mw=9.5 x 10 5 ) by controlling the water content in monomer and the concentration of the catalyst and chain initiator. 1 7 -19 The kinetic equations of their anionic polymerization are in agreement with the ideal rate equation. 20 The formation of cyclic oligomers in anionic polymerization of e-caprolactam has not been studied in detail. Cyclic oligomer content (up to heptamer) has been measured only in a few studies. 21 -23 The proposed mechanism of cyclic oligomer formation still seems insufficient. 24 This study deals with kinetic data of the cyclic oligomer formation in the polymerization as a function of the concentrations of catalyst and chain initiator. The mechanism of the formation is discussed.
EXPERIMENT AL
MaterialsIndustrial fiber grade e-caprolactam as monomer, ethyl magnesium bromide (EtMgBr; Aldrich Chemical Co., Inc.) as catalyst in 1.0 mo11-1 tetrahydrofuran solution and N-acetyl-e-caprolactam (Ac-CL; Tokyo Chemical Industry Co., Ltd.) as monofunctional chain initiator were used for polymerization.
PolymerizationWater in e-caprolactam was removed to less than 0.013 mol¾ by bubbling dry argon gas for 5 h in a three-neck flask at 120°C. Water content was controlled by adding water to this e-caprolactam and measured by a Karl Fischer auto titration equipment (Hiranuma industrial Co., AQV-5S). The chain initiator was injected into ecaprolactam with controlled water content. The mixture of monomer and initiator was poured into a glass 186 tube (inside diameter 20 mm, volume 20 ml) dried beforehand by heating above l00°C under 10Pa vacuum. The catalyst (EtMgBr) solution was injected into the tube via a syringe, and the tube was sealed after unnecessary solvent was evaporated at 10 Pa. The polymerization was carried out with shaking in an oil bath at 150°C (thermostated at± l .0°C).Polymerization was stopped by quenching to dry ice/methanol temperature ( -73°C). The product was shaved with a boring machine and analyzed.
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