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Discontinuous feedback stabilization of minimum-phase semilinear infinite-dimensional systems with application to chemical tubular reactor

机译:最小相半线性无限维系统的间断反馈镇定及其在化学管式反应器中的应用

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This paper develops discontinuous control methods for minimum-phase semilinear infinite-dimensional systems driven in a Hilbert space. The control algorithms presented ensure asymptotic stability, global or local accordingly, as state feedback or output feedback is available, as well as robustness of the closed-loop system against external disturbances with the a priori known norm bounds. The theory is applied to stabilization of chemical processes around prespecified steady-state temperature and concentration profiles corresponding to a desired coolant temperature. Two specific cases, a plug flow reactor and an axial dispersion reactor, governed by hyperbolic and parabolic partial differential equations of first and second order, respectively, are under consideration. To achieve a regional temperature feedback stabilization around the desired profiles, with the region of attraction, containing a prescribed set of interest, a component concentration observer is constructed and included into the closed-loop system so that there is no need for measuring the process component concentration which is normally unavailable in practice. Performance issues of the discontinuous feedback design are illustrated in a simulation study of the plug flow reactor.
机译:本文针对希尔伯特空间中驱动的最小相位半线性无限维系统开发了间断控制方法。所呈现的控制算法确保了状态反馈或输出反馈可用时的全局或局部渐近稳定性,以及闭环系统针对具有先验已知范数边界的外部干扰的鲁棒性。该理论适用于围绕预定稳态温度和对应于所需冷却液温度的浓度曲线进行化学过程的稳定化。正在考虑分别由一阶和二阶双曲和抛物线偏微分方程控制的活塞流反应器和轴向弥散反应器这两种具体情况。为了在期望的轮廓周围实现区域温度反馈稳定化,在具有吸引人的区域(包含一组感兴趣的关注区域)的情况下,应构造一个成分浓度观测器并将其包含在闭环系统中,从而无需测量过程成分在实践中通常无法获得的浓度。活塞流反应器的仿真研究说明了不连续反馈设计的性能问题。

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