On-line estimation and control strategies for a microalgae fermentation continuous process

E. Petre, Dorin Cendrescu
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引用次数: 1

Abstract

The design of some adaptive and robust-adaptive control strategies for a microalgae fermentation process that is carried out inside a Continuous Stirred Tank Reactor (CSTR) is presented. Initially, an indirect adaptive controller is designed by coupling a linearizing controller with a new parameter estimator used for estimation of unknown kinetics. Afterwards, under the realistic assumption that the reaction kinetics are unknown, time-varying and moreover the influent flow rate is uncertain and time-varying, but some lower and upper bounds of these uncertainties are known, two robust-adaptive control structures are proposed by combining a linearizing control law with two new appropriately parameter estimators able to estimates the unknown reaction rates. Numerical simulations are included to validate the designed controllers applied to a continuous fermentation bioprocess used for microalgae production.
微藻发酵连续过程的在线估计与控制策略
针对微藻在连续搅拌槽式反应器(CSTR)内发酵过程,设计了一些自适应和鲁棒自适应控制策略。首先,通过将线性化控制器与用于未知动力学估计的新参数估计器相耦合,设计了间接自适应控制器。然后,在反应动力学未知、时变且进水流量不确定、时变但不确定的下界和上界已知的现实假设下,将线性化控制律与两个能够估计未知反应速率的新的适当参数估计量相结合,提出了两种鲁棒自适应控制结构。数值模拟包括验证所设计的控制器应用于微藻生产的连续发酵生物过程。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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