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An improved multi-stage nonlinear model predictive control with application to semi-batch polymerization

机译:一种改进的多阶段非线性模型预测控制,应用于半批量聚合

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Nonlinear model predictive control (NMPC) has been widely applied in the chemical industry for its performance of dealing with the multiple input multiple output problem (MIMO) and handling constraints. However, the performance of NMPC would be affected by the accuracy of the model. The NMPC controller has to be robust to uncertainties in the model. In this paper, the scenario-tree based on multi-stage NMPC approach has been applied to the semi-batch polymerization reactor. In this approach, in order to ensure the reasonableness of the uncertain variables and scenario tree number, a Monte Carlo-based second-order nonlinear model and K-means cluster algorithm have been proposed. The weights of each scenario branches are also considered into variable. The simulation results show that the performance of the improved method is better and the variable weights has a good ability of improving the performance of controller.
机译:非线性模型预测控制(NMPC)已广泛应用于化学工业,以处理处理多输入多输出问题(MIMO)和处理约束。但是,NMPC的性能将受模型的准确性的影响。 NMPC控制器必须在模型中的不确定性稳健。本文基于多级NMPC方法的场景树已经应用于半批量聚合反应器。在这种方法中,为了确保不确定变量和场景树数的合理性,已经提出了一种基于蒙特卡罗的二阶非线性模型和K-Means簇算法。每个场景分支的权重也被认为是可变的。仿真结果表明,改进方法的性能更好,可变权重具有提高控制器性能的良好能力。

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