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Switched control of uncertain nonlinear process systems subject to control and communication constraints

机译:受控制和通信约束的不确定非线性过程系统的切换控制

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This paper presents a switched control strategy for the robust stabilization of uncertain nonlinear process systems with both control and measurement sampling constraints. A model-based constrained Lyapunov-based controller is initially designed for each control actuator configuration. Next, the constrained stability regions and the terminal sets of all the configurations are characterized, in terms of the size of the control constraints, the sampling period and the plant-model mismatch, and analyzed. The analysis shows that the configuration with the largest stability region does not necessarily have the smallest terminal set, which leads to a conflict with the desired control objective of steering the process from a large initial state to a small terminal neighborhood of the equilibrium point. To resolve this conflict and attain the desired control objective, a switching strategy that executes a sequence of transitions between the available actuator configurations is developed. The key idea of the switching logic is to keep a configuration active until its terminal set is reached and then to switch to another stabilizing configuration with a smaller terminal set. The proposed robust hybrid control method is illustrated using a chemical process example.
机译:本文提出了一种具有控制和测量采样约束的不确定非线性过程系统鲁棒镇定的切换控制策略。最初为每种控制执行器配置设计了基于模型的基于Lyapunov约束的控制器。接下来,根据控制约束的大小,采样周期和工厂模型不匹配,对所有配置的受约束稳定区域和终端机进行表征,并进行分析。分析表明,具有最大稳定区域的配置不一定具有最小的端子组,这导致与将过程从大的初始状态转向平衡点的小端子邻域的所需控制目标发生冲突。为了解决此冲突并达到所需的控制目标,开发了一种在可用执行器配置之间执行一系列转换的切换策略。切换逻辑的关键思想是保持配置处于活动状态,直到到达其终端机为止,然后切换到具有较小终端机的另一稳定配置。所提出的鲁棒混合控制方法以化学过程示例为例。

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