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Multi-scale control scheme: Stabilization of a class of fourth-order integrating-unstable systems

机译:多尺度控制方案:一类四阶积分不稳定系统的稳定性

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摘要

Even when based on simple models, a fed-batch fermentation process can demonstrate several different forms of complex dynamic behaviours throughout the course of its operation. One of the most intriguing forms of dynamic behaviours that can occur at some points during the fed-batch operation is represented by a fourth-order integrating-unstable system with multiple RHP zeros. To deal with the stabilization of this complex dynamics, a new triple-loop multi-scale control (TL-MSC) scheme is proposed. This scheme aims to first decompose the complex dynamics into three simpler sub-systems which are then separately addressed in a multi-scale structure. This paper presents both the fundamental of TL-MSC scheme and the details of its design. A typical fed-batch alcoholic fermentation is shown as an example to demonstrate the applicability of the new scheme. (c) 2017 The Franklin Institute. Published by Elsevier Ltd. All rights reserved.
机译:即使基于简单的模型,分批补料发酵过程也可以在其整个操作过程中表现出几种不同形式的复杂动态行为。在分批补料操作期间某些点上可能发生的最有趣的动态行为形式之一,是具有多个RHP零的四阶积分不稳定系统。为了应对这种复杂动力学的稳定,提出了一种新的三环多尺度控制(TL-MSC)方案。该方案旨在首先将复杂的动力学分解为三个更简单的子系统,然后将其分别以多尺度结构进行处理。本文介绍了TL-MSC方案的基本原理及其设计细节。以典型的分批补料酒精发酵为例,以证明该新方案的适用性。 (c)2017富兰克林研究所。由Elsevier Ltd.出版。保留所有权利。

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  • 来源
    《Journal of the Franklin Institute》 |2018年第1期|141-163|共23页
  • 作者

    Seer Qiu Han; Nandong Jobrun;

  • 作者单位

    Curtin Univ, Dept Chem Engn, Miri 98009, Sarawak, Malaysia;

    Curtin Univ, Dept Chem Engn, Miri 98009, Sarawak, Malaysia;

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  • 正文语种 eng
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