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Dynamic optimization of semi-batch emulsion co-polymerization reactor for styrene/butyl acrylate in the presence of a chain transfer agent

机译:链转移剂存在下苯乙烯/丁基丙烯酸丁酯的半批量乳液共聚反应器的动态优化

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We study dynamic optimization of a lab-scale semi-batch emulsion copolymerization reactor for styrene and butyl acrylate in the presence of n-dodecyl mercaptan as chain transfer agent (CTA). The previously developed mathematical model of the polymerization reactions is used to predict the glass transition temperature of produced polymer, the global monomer conversion, the number and weight average molecular weights, the particle size distribution, and the amount of residual monomers. This model is implemented within gPROMS environment for modeling and optimization. It is desired to compute optimal profiles of feed rate of pre-emulsioned monomers and CTA which optimize properties (quantitative as well as qualitative) of polymers produced during the reaction subject to operational conditions and constraints.
机译:我们研究了在N-十二烷基硫醇作为链转移剂(CTA)存在下苯乙烯和丙烯酸丁酯的实验室半批乳液共聚反应器的动态优化。先前开发的聚合反应的数学模型用于预测产生的聚合物的玻璃化转变温度,全局单体转化,数量和重均分子量,粒度分布和残留单体的量。该模型是在GPROM环境中实现的,用于建模和优化。期望计算预乳化单体和CTA的进料速率的最佳谱,其优化在反应期间产生的聚合物的性质(定量以及定性)进行操作条件和约束。

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