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Switched Control of Uncertain Nonlinear Process Systems Subject to Control and Communication Constraints

机译:不确定非线性工艺系统进行控制和通信约束的切换控制

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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:本文介绍了具有控制和测量采样约束的不确定非线性工艺系统的强大稳定的交换控制策略。最初为每个控制执行器配置设计了基于模型的受限Lyapunov的控制器。接下来,根据控制约束的大小,采样周期和植物模型不匹配,并分析所有配置的约束稳定性区域和终端集。分析表明,具有最大稳定区域的配置不一定具有最小的终端集,这导致与从大初始状态转向到平衡点的小终端邻域的过程的所需控制目标的冲突。为了解决这一冲突并获得所需的控制目标,开发了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有效,直到到达其终端组,然后用较小的终端集切换到另一个稳定配置。使用化学过程示例说明所提出的稳健混合控制方法。

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