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Analysis and design of heterogeneous control laws for nonlinear chemical processes.

机译:非线性化学过程的异构控制律的分析和设计。

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Most regulatory control paradigms for chemical processes assume that the process remains close to an equilibrium point, and that its behavior about this point is linear. However, modern chemical processes are often required to operate in wide operating regions where the linearity assumption does not apply. There is, therefore, a need for the design of global controllers that are valid over a wide operating region.; For nonlinear processes that have to be operated over a wide operating region where a linear approximation is not appropriate, a direct method of designing global controllers is by using model-based techniques with an explicit nonlinear model of the process. Some important theoretical results in this area have recently been achieved from techniques like feedback linearization, nonlinear internal model control, and nonlinear model predictive control. A different approach that has been widely applied in industry to design global controllers consists of dividing the operating space into different operating regions, designing local controllers in each one of these regions (usually linear controllers), and combining or switching the local control laws as the process evolves from one operating region to another.; In this dissertation a mathematical framework to define this class of controllers is presented, defining them as heterogeneous control laws. This framework is used to analyze fuzzy heuristic control and sliding mode control laws, and to show their similitude. Concepts from feedback linearization are used to identify good candidates to apply fuzzy heuristic control and sliding mode control.; A geometric interpretation of controlled dynamic systems using velocity fields is provided as a tool to help in the analysis of nonlinear systems, and it is applied to explain inverse dynamics, to represent control conditions as non-parametric geometric conditions, to design an heterogeneous controller, and to analyze robustness of some control laws.
机译:化学过程的大多数监管控制范式都假设过程保持在平衡点附近,并且其在该点附近的行为是线性的。但是,现代化学过程通常需要在线性假设不适用的宽工作区域内运行。因此,需要设计在广泛的工作区域内有效的全局控制器。对于必须在不适合线性近似的较宽工作区域内运行的非线性过程,设计全局控制器的直接方法是使用基于模型的技术和过程的显式非线性模型。最近通过反馈线性化,非线性内部模型控制和非线性模型预测控制等技术获得了该领域的一些重要理论成果。在行业中广泛用于设计全局控制器的另一种方法包括:将操作空间划分为不同的操作区域,在这些区域中的每个区域中设计本地控制器(通常是线性控制器),并将本地控制定律组合或切换为本地控制定律。过程从一个操作区域演变为另一个操作区域。本文提出了定义此类控制器的数学框架,并将其定义为异构控制律。该框架用于分析模糊启发式控制和滑模控制律,并显示其相似性。反馈线性化的概念被用来识别应用模糊启发式控制和滑模控制的良好候选者。提供了使用速度场对受控动态系统进行几何解释的工具,可帮助您分析非线性系统,并用于解释逆动力学,将控制条件表示为非参数几何条件,以设计异构控制器,并分析某些控制律的鲁棒性。

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