生物发酵罐模型预测控制器的设计

C. Madhuranthakam, O. Khan
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引用次数: 0

摘要

模型预测控制(MPC)是一种利用过程模型来计算一系列控制动作的控制策略,其控制目标是跟踪被控变量的期望水平。为了确定模型预测控制器的调谐策略,已经进行了大量的工作。然而,大部分工作都集中在确定一组特定过程条件的最佳调优参数上,或者忽略了过程模型中存在的不确定性。这项工作旨在通过明确地考虑植物模型不匹配来开发鲁棒模型预测控制器。为此,对从微生物发酵罐获得的开环阶跃响应数据找到最适合的传递函数得到的三个二阶过程模型创建了模型预测控制器。此外,在没有不确定性的情况下,为标称情况确定了最优MPC设置(即控制水平、预测水平和权重)。根据观察到的实验不确定性,通过随机生成500个不匹配过程模型,将标称情景的最优设置告知不确定情景的最优设置。图形技术被用来寻找最优设置,使控制性能最大化,并使控制性能的变化最小化,以响应于设定点和干扰的阶跃变化。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Design of Model Predictive Controller for a Biological Fermenter
Model Predictive Control (MPC) is a control strategy which utilizes a process model to compute a sequence of control moves with a desired control objective of tracking the desired level of the controlled variable. Extensive work has been undertaken to determine tuning strategies for model predictive controllers. However, much of that work has focused on determining the optimal tuning parameters for a particular set of process conditions, or has ignored the presence of uncertainty in the process model. This work aims to develop robust model predictive controllers by explicitly accounting for plant-model mismatch. To do this, model predictive controllers are created for three second-order process models obtained from finding the best-fit transfer function to open-loop step-response data obtained from a microbial fermenter. Further, the optimal MPC settings (namely the control horizon, prediction horizon, and the weights) are determined for the nominal case when there is no uncertainty. The optimal settings for the nominal scenario are used to inform the optimal settings for the uncertain scenario, which are found by randomly generating 500 mismatched process models based on observed experimental uncertainty. Graphical techniques are used to find the optimal settings that maximize the control performance and minimize variation in the control performance in response to step changes in the set-point and the disturbance.
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