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Biomimetic model-based advanced control strategy integrated with multi-agent optimization for nonlinear chemical processes

机译:基于仿生模型的先进控制策略,与非线性化学过程多智能体优化集成

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摘要

In this paper, a novel framework is proposed for integrating biomimetic-based advanced control and multi-agent optimization approaches for nonlinear chemical process applications. In particular, a Biologically-Inspired Optimal Control Strategy, denoted as BIO-CS, is combined with multi-agent optimization (MAO) techniques to provide optimal solutions for dynamic systems. In this combined framework, the BIO-CS algorithm employs gradient-based optimal control solvers for the intermediate problems associated with the leader-follower agents' local interactions. Also, the MAO uses the capabilities of heuristic based optimization techniques by sharing process information to obtain optimal operating setpoints for the controller considering an overall process objective. The applicability of the proposed method is demonstrated using a nonlinear, multivariable, process model of a fermentation system. Specifically, the optimal operating points are computed by the MAO implementation for setpoint tracking, trajectory tracking and plant-model mismatch scenarios for BIO-CS application. Results of the developed framework are compared to a gradient-based Sequential Quadratic Programming (SQP) technique and a classical proportional-integral (PI) controller in terms of optimization and control studies, respectively. As an additional contribution, BIO-CS is also cast as a model predictive controller (MPC) for the first time and compared to the agent-based BIO-CS approach in terms of computational time and tracking error. Closed-loop control results show up to 46% improvement in tracking performance during transient for the multi-agent BIO-CS when compared to BIO-CS as MPC for additional computational expense. The obtained results illustrate the capabilities of this novel integrated framework including BIO-CS as MPC to achieve desired nonlinear system performance for various scenarios. (C) 2018 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
机译:本文提出了一种新颖的框架,用于整合基于仿生的先进控制和用于非线性化学工艺应用的多剂量优化方法。特别地,表示为Bio-CS的生物学激发的最佳控制策略与多代理优化(MAO)技术相结合,为动态系统提供最佳解决方案。在该组合框架中,Bio-CS算法采用基于梯度的最佳控制求解器,用于与前照跟随者的局部相互作用相关的中间问题。此外,MAO通过共享过程信息来利用启发式基于优化技术的能力,以便考虑整体过程目标的控制器获得最佳操作设定值。使用发酵系统的非线性,多变量的过程模型来证明所提出的方法的适用性。具体地,最佳操作点由MAO实现来计算用于Bio-CS应用的设定点跟踪,轨迹跟踪和植物模型不匹配场景。将开发框架的结果与基于梯度的顺序二次编程(SQP)技术进行比较,分别在优化和对照研究方面和经典比例积分(PI)控制器。作为额外贡献,Bio-CS也首次作为模型预测控制器(MPC),并与基于代理的生物CS方法相比,在计算时间和跟踪误差方面。与Bio-CS相比,闭环控制结果显示出在多助剂Bio-CS的瞬态瞬态时的提高高达46%,因为与BIO-CS为MPC以获得额外的计算费用。所获得的结果说明了这种新颖的整合框架的能力,包括Bio-CS作为MPC,以实现各种场景的所需的非线性系统性能。 (c)2018化学工程师机构。 elsevier b.v出版。保留所有权利。

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