Deng F, Gross R A
Polytechnic University, Polymer Research Institute, Brooklyn, NY 11201, USA.
Int J Biol Macromol. 1999 Jun-Jul;25(1-3):153-9. doi: 10.1016/s0141-8130(99)00029-x.
The affects of lipase concentration on ring-opening bulk polymerizations of epsilon-caprolactone and trimethylene carbonate were studied by using Novozym 435 (immobilized form of lipase B from Candida antarctica) as biocatalyst. The polymerization of epsilon-caprolactone was carried out in bulk at 70 degrees C. Three lipase concentrations of 9.77, 1.80 and 0.50 mg/mmol epsilon-CL were used in the experiment. The results showed that increasing the lipase concentration used in the polymerization system resulted in an increased rate of monomer consumption. For an enzyme concentration of 9.8 mg lipase per mmol monomer, an 80% monomer conversion was achieved in a 4-h time period, while for the lower enzyme concentration of 1.8 mg lipase per mmol monomer, 48 h were needed to reach monomer conversion. Linear relationships between Mn and monomer conversions were observed in all three enzyme concentrations, suggesting that the product molecular weight may be controlled by the stoichiometry of the reactants for these systems. At the same monomer conversion level, however, Mn decreased with increasing enzyme concentration. After correcting for the amount of monomer consumed in initiation, the plot of ln[([M]o - [M]i)/([Mt] - [M]i)] versus reaction time was found to be linear, suggesting that the monomer consumption followed a first-order rate law and no chain termination occurred. For the TMC systems, the polymerization was carried out in bulk at 55 degrees C. Similar to the epsilon-CL systems, increasing the Novozym 435 concentration from 8.3 to 23.6 mg/mmol TMC increased the rate of monomer conversion. Unlike the epsilon-CL systems, however, nonlinear relationships were obtained between Mn and monomer conversion, indicating that possible chain transfer and/or slow initiation had taken place in these systems. Consistent with the above result, nonlinear behavior was observed for the plot of ln[[M]o/[M]t] versus reaction time.
以诺维信435(南极假丝酵母脂肪酶B的固定化形式)作为生物催化剂,研究了脂肪酶浓度对ε-己内酯和碳酸三亚甲基酯的本体开环聚合反应的影响。ε-己内酯的聚合反应在70℃下本体进行。实验中使用了三种脂肪酶浓度,分别为9.77、1.80和0.50mg/mmol ε-CL。结果表明,提高聚合体系中使用的脂肪酶浓度会导致单体消耗速率增加。对于每mmol单体9.8mg脂肪酶的酶浓度,在4小时内实现了80%的单体转化率,而对于每mmol单体1.8mg脂肪酶的较低酶浓度,则需要48小时才能达到单体转化率。在所有三种酶浓度下均观察到Mn与单体转化率之间的线性关系,这表明对于这些体系,产物分子量可能由反应物的化学计量比控制。然而,在相同的单体转化率水平下,Mn随着酶浓度的增加而降低。在校正引发过程中消耗的单体量后,发现ln[([M]o - [M]i)/([Mt] - [M]i)]对反应时间的曲线是线性的,这表明单体消耗遵循一级速率定律且没有链终止发生。对于碳酸三亚甲基酯(TMC)体系,聚合反应在55℃下本体进行。与ε-己内酯体系类似,将诺维信435浓度从8.3mg/mmol TMC提高到23.6mg/mmol TMC会增加单体转化率。然而,与ε-己内酯体系不同的是,Mn与单体转化率之间得到了非线性关系,这表明在这些体系中可能发生了链转移和/或缓慢引发。与上述结果一致,ln[[M]o/[M]t]对反应时间的曲线也观察到了非线性行为。