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Free radical copolymerization of N,N-dimethylaminoethyl methacrylate with styrene and methyl methacrylate: monomer reactivity ratios and glass transition temperatures

机译:N,N-甲基丙烯酸N,N-二甲基氨基乙酯与苯乙烯和甲基丙烯酸甲酯的自由基共聚合:单体反应率和玻璃化转变温度

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BACKGROUND: The properties of copolymers depend strongly on their composition; therefore in order to tailor some for specific applications, it is necessary to control their synthesis, and, in particular, to know the reactivity ratios of their constituent monomers. Free radical copolymerizations of N,/V-dimethylaminoethyl methacrylate (DMAEM) with styrene (ST) and methyl methacrylate (MMA) in toluene solution using 1-di(ferf-butylperoxy)-3,3,5-trimethylcyclohexane as initiator at 70 °C were investigated. Monomer reactivity ratios were determined for low conversions using both linear and nonlinear methods.RESULTS: For the DMAEM/ST system the average values are r1 = 0.43 and r2 = 1.74; for the DMAEM/MMA system the average values are r1 = 0.85 and r2 = 0.86. The initial copolymerization rate, R_p, for DMAEM/ST sharply decreases as the content of ST in the monomer mixture increases up to 30 mol% and then attains a steady value. For the DMAEM/MMA copolymerization system the composition of the feed does not have a significant influence on Rp. The glass transition temperatures (T_g) of the copolymers were determined caiorimetrically and calculated using Johnston's sequence length method. A linear dependence of T_g on copolymer composition for both systems is observed: T_g increases with increasing ST or MMA content.CONCLUSION: Copolymerization reactivity ratios enable the design of high-conversion processes for the production of copolymers of well-defined properties for particular applications, such as the improvement of rheological properties of lubricating mineral oils.
机译:背景:共聚物的性能在很大程度上取决于其组成。因此,为了针对某些特定应用定制一些,必须控制它们的合成,尤其是要了解其组成单体的反应率。 N,/ V-甲基丙烯酸N,V-二甲基氨基乙酯(DMAEM)与苯乙烯(ST)和甲基丙烯酸甲酯(MMA)在甲苯溶液中以1-二(叔丁基过氧)-3,3,5-三甲基环己烷为引发剂的自由基共聚C进行了调查。结果:对于DMAEM / ST系统,平均值为r1 = 0.43和r2 = 1.74;对于DMAEM / ST系统,其低转化率的单体反应率是确定的。对于DMAEM / MMA系统,平均值为r1 = 0.85和r2 = 0.86。 DMAEM / ST的初始共聚速率R_p随单体混合物中ST含量增加至30 mol%而急剧下降,然后达到稳定值。对于DMAEM / MMA共聚体系,进料的组成对Rp没有明显影响。量热测定共聚物的玻璃化转变温度(T_g),并使用约翰斯顿序列长度法计算。观察到两种体系中T_g对共聚物组成的线性依赖性:T_g随着ST或MMA含量的增加而增加。结论:共聚反应活性比可以设计出高转化率的工艺,以生产具有特定用途的性能明确的共聚物,例如改善矿物油的流变性。

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