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Batch and continuous thermal free-radical copolymerization of styrene with glycidyl methacrylate at high reaction temperatures

机译:苯乙烯与甲基丙烯酸缩水甘油酯在高反应温度下的间歇和连续热自由基共聚

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Full Paper: Studies were performed on the free-radical thermal copolymerization of styrene and glycidyl methacrylate in a batch and a continuous stirred tank reactor. From experiments at low monomer conversions in a batch reactor the monomer reactivity ratios and their temperature dependence were determined between 110, 135, 160degreesC according to the terminal model. The cumulative copolymer composition could be satisfactorily described as a function of monomer conversion with the equation of Meyer-Lowry. The values of the reactivity ratios could be successfully extrapolated to higher monomer conversions and higher reaction temperatures. The steady-state behavior of a continuous stirred tank reactor could be very well simulated with respect to the copolymer composition and to the residual monomer ratio up to a reaction temperature of 190degreesC. At higher reaction temperatures the differences between theory and experimental results increased, perhaps due to the start of thermal decomposition of the copolymers. [References: 16]
机译:全文:在间歇式和连续搅拌釜式反应器中,对苯乙烯和甲基丙烯酸缩水甘油酯的自由基热共聚进行了研究。通过在间歇式反应器中低单体转化率下进行的实验,根据末端模型,在110、135、160℃之间确定了单体反应率和它们的温度依赖性。累积的共聚物组成可以用Meyer-Lowry方程令人满意地描述为单体转化率的函数。反应性比的值可以成功地推断为更高的单体转化率和更高的反应温度。关于共聚物组成和直至190℃反应温度的残余单体比率,可以很好地模拟连续搅拌釜反应器的稳态行为。在较高的反应温度下,理论和实验结果之间的差异增加了,这可能是由于共聚物开始热分解所致。 [参考:16]

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