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Optimal control of molecular weight and particle size distributions in a batch suspension polymerization reactor

机译:间歇悬浮聚合反应器中分子量和粒度分布的最佳控制

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摘要

Mechanistic modelling is an engineering approach to simulate reasonable physical and chemical processes to develop a model to describe the behaviour of a system. Mathematical models are commonly adopted to explore the physical limits of a process, and are applied to process development, optimization and control. In this work, the population balance model and the moment technique have been utilized to model a suspension polymerization reactor and predict the dynamic evolution of particle size and molecular weight distributions. These distributions are two important factors that affect the physical, rheological and mechanical properties of a polymer, and its final product quality. The cell average technique has been applied to solve the population balance equation, and demonstrate the model predictive capability by comparing its predictions with those obtained from experimental data published in the literature. In addition, the effects of initiator, chain transfer agent, stabilizer concentrations, temperature, and agitation rate on the final particle size and molecular weight distributions have been investigated. An optimal control strategy has been used to obtain the desired molecular weight distribution by manipulating the initiator concentration, concentration of the chain transfer agent and its addition time, and controlling the reactor temperature. Also, the impeller speed and initial value of the stabilizer have been utilized to achieve the desired final particle size distribution. The simulation results indicate that the control objectives have been achieved, and show that the proposed controllers are robust to a mismatched model.
机译:机械建模是一种工程方法,用于模拟合理的物理和化学过程,以开发用于描述系统行为的模型。通常采用数学模型来探索过程的物理极限,并将其应用于过程开发,优化和控制。在这项工作中,人口平衡模型和矩技术已被用来对悬浮聚合反应器进行建模,并预测粒径和分子量分布的动态演变。这些分布是影响聚合物的物理,流变和机械性能及其最终产品质量的两个重要因素。单元平均技术已用于解决人口平衡方程,并通过将其预测与从文献中发表的实验数据中获得的预测进行比较,证明了模型的预测能力。另外,还研究了引发剂,链转移剂,稳定剂浓度,温度和搅拌速率对最终粒径和分子量分布的影响。通过控制引发剂浓度,链转移剂的浓度及其添加时间,并控制反应器温度,已采用最佳控制策略来获得所需的分子量分布。而且,已经利用叶轮速度和稳定剂的初始值来获得所需的最终粒度分布。仿真结果表明已经达到控制目标,并且表明所提出的控制器对于不匹配模型具有鲁棒性。

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