At 225℃. caprolactone has been polymerized in the presence of succinic acid under dry nitrogen atmosphere. Characterizations of the polymer through IR and molecular weight measurements by 1H-NMR and end group titrati...At 225℃. caprolactone has been polymerized in the presence of succinic acid under dry nitrogen atmosphere. Characterizations of the polymer through IR and molecular weight measurements by 1H-NMR and end group titration have shown that the polycaprolactone obtained is of two carboxyl end groups. The molecular weight of it increases with decreasing of the acid content in the reaction mixture under the same polymerization conditions. With a certain ratio of acid to caprolactone. the maximum of molecular weight of the polymer will be reached at the reaction time of 3h.展开更多
文摘At 225℃. caprolactone has been polymerized in the presence of succinic acid under dry nitrogen atmosphere. Characterizations of the polymer through IR and molecular weight measurements by 1H-NMR and end group titration have shown that the polycaprolactone obtained is of two carboxyl end groups. The molecular weight of it increases with decreasing of the acid content in the reaction mixture under the same polymerization conditions. With a certain ratio of acid to caprolactone. the maximum of molecular weight of the polymer will be reached at the reaction time of 3h.
文摘在300 t/d聚酯(PET)装置上通过减少锑系催化剂添加量,逐步将钛系催化剂添加比例由15%提高至100%,最终实现钛系催化剂生产环保型PET产品,分析了钛系催化剂替代量对PET切片质量、热性能以及过滤器切换周期的影响。结果表明:随着钛系催化剂替代比例的提高,PET切片色相b值大幅上升,将酯化Ⅰ釜温度由264℃下降至256℃,酯化Ⅱ釜温度由268℃下降至259℃,增大调色剂添加量控制在30μg/g以内,可保证色相L值不低于90;将预聚釜Ⅰ温度由271℃下降至265℃,预聚釜Ⅱ温度由276℃下降至274℃,终缩聚温度由278℃下降至276℃,可将端羧基含量控制在指标要求范围;将酯化Ⅰ釜压力由65k Pa提高至79 k Pa,工艺塔釜温由175℃提高至178℃,可缓解二甘醇含量下降幅度,但对二甘醇含量提高效果不明显;全钛系PET比全锑系PET降温峰值温度低13.66℃,降温峰值温度与冷结晶温度之差低20.29℃,有利于纺丝;全钛系PET生产中过滤器切换周期比全锑系PET的长。