Wang Wei, Nikitin Anatoly N, Hutchinson Robin A
Department of Chemical Engineering, Dupuis Hall, Queen's University, Kingston, Ontario K7L 3N6, Canada.
Macromol Rapid Commun. 2009 Dec 1;30(23):2022-7. doi: 10.1002/marc.200900445. Epub 2009 Oct 9.
n-Butyl acrylate (BA) starved-feed solution semibatch experiments with varying final polymer content and monomer feed times were carried out at 138 °C. A full mechanistic model of the system implemented in Predici includes intermolecular chain transfer to polymer and macromonomer propagation as well as backbiting, chain scission, and midchain radical propagation and termination. The importance of macromonomer propagation under these conditions of industrial interest is illustrated by experiment and simulation, with the macromonomer reaction responsible for the significant increase in polymer weight-average molecular weight ($\overline M _{\rm w}$) with time. Rate coefficients for macromonomer propagation (k(mac) ) and β-scission (k(β) ) of k(mac) /k(p) = 0.55 and k(β) = 12 s(-1) (with k(p) the rate coefficient for BA chain-end propagation) provide a good representation of experimental $\overline M _{\rm w}$ and macromonomer end group data at 138 °C.
在138°C下进行了丙烯酸正丁酯(BA)饥饿进料溶液半间歇实验,实验中改变了最终聚合物含量和单体进料时间。在Predici中实现的该系统的完整机理模型包括聚合物分子间链转移、大分子单体增长以及回咬、链断裂、链中自由基增长和终止。实验和模拟表明了在这些具有工业意义的条件下大分子单体增长的重要性,大分子单体反应导致聚合物重均分子量($\overline M _{\rm w}$)随时间显著增加。大分子单体增长速率系数(k(mac) )和β-断裂速率系数(k(β) ),其中k(mac) /k(p) = 0.55且k(β) = 12 s(-1) (k(p) 为BA链端增长速率系数),能很好地反映138°C下的实验$\overline M _{\rm w}$和大分子单体端基数据。