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Evaluation of neural networks-based controllers in batch polymerisation of methyl methacrylate

机译:评估甲基丙烯酸甲酯间歇聚合中基于神经网络的控制器

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The importance of batch reactors in today's process industries cannot be overstated. Thus said, it is important to optimise their operation in order to consistently achieve products of high quality while minimising the production of undesirables. In processes like polymerisation, these reactors are responsible for a greater number of products than other reactor types and the need for optimal operation is therefore greater. An approach based on an offline dynamic optimisation and online control strategy is used in this work to generate optimal set point profiles for the batch polymerisation of methyl methacrylate. Dynamic optimisation is carried out from which controller set points to attain desired polymer molecular end point characteristics are achieved. Temperature is the main variable to be controlled, and this is done over finite discrete intervals of time. For on-line control, we evaluate the performance of neural networks in two controllers used to track the derived optimal set points for the system. The controllers are generic model control (GMC), ([P.L. Lee, G.R. Sullivan, Generic model control, Comput. Chem. Eng. 12(6) (1998) 573-580]) and the neural network-based inverse model-based control (IMBC), ([M.A. Hussain, L.S. Kershenbaum, Implementation of an inverse model based control strategy using neural networks on a partially simulated exothermic reactor, Trans. IchemE 78(A) (2000) 299-311]). Although the GMC is a model-based controller, neural networks are used to estimate the heat release within its framework for on-line control. Despite the application of these two controllers to general batch reactors, no published work exists on their application to batch polymerisation in the literature. In this work, the performance of the neural networks within each controller's algorithm for tracking and setpoint regulation of the optimal trajectory and in robustness tests on the system is evaluated.
机译:在当今的过程工业中,间歇式反应器的重要性不可低估。因此,重要的是优化它们的操作,以便始终如一地获得高质量的产品,同时使不希望的产品的产生最小化。在诸如聚合的过程中,这些反应器比其他类型的反应器负责更多的产品,因此对最佳操作的需求更大。在这项工作中,使用了一种基于离线动态优化和在线控制策略的方法,以生成用于甲基丙烯酸甲酯间歇聚合的最佳设定值曲线。进行动态优化,从中实现达到所需聚合物分子终点特性的控制器设定点。温度是要控制的主要变量,它是在有限的离散时间间隔内完成的。对于在线控制,我们在两个控制器中评估神经网络的性能,该控制器用于跟踪系统得出的最佳设定点。控制器是通用模型控制(GMC),([PL Lee,GR Sullivan,Generic model control,Comput.Chem.Eng.12(6)(1998)573-580])和基于神经网络的逆模型控制(IMBC),([MA Hussain,LS Kershenbaum,在部分模拟的放热反应堆上使用神经网络实施基于逆模型的控制策略,Trans。IchemE 78(A)(2000)299-311])。尽管GMC是基于模型的控制器,但是神经网络用于估计其在线控制框架内的热量释放。尽管将这两种控制器应用于一般的间歇反应器,但是在文献中尚无关于将其应用于间歇聚合的公开工作。在这项工作中,评估了每个控制器算法中神经网络的性能,这些算法用于跟踪和调整最佳轨迹并在系统的稳健性测试中进行评估。

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