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Offset-free multi-model economic model predictive control for changing economic criterion

机译:不断变化经济标准的无偏移多模型经济模型预测控制

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摘要

Economic Model Predictive Controllers, consisting of an economic criterion as stage cost for the dynamic regulation problem, have shown to improve the economic performance of the controlled plant. However, throughout the operation of the plant, if the economic criterion changes - due to variations of prices, costs, production demand, market fluctuations, reconciled data, disturbances, etc. - the optimal operation point also changes. In industrial applications, a nonlinear description of the plant may not be available, since identifying a nonlinear plant is a very difficult task. Thus, the models used for prediction are in general linear. The nonlinear behavior of the plant makes that the controller designed using a linear model (identified at certain operation point) may exhibit a poor closed-loop performance or even loss of feasibility and stability when the plant is operated at a different operation point. A way to avoid this issue is to consider a collection of linear models identified at each of the equilibrium points where the plant will be operated. This is called a multi-model description of the plant. In this work, a multi-model economic MPC is proposed, which takes into account the uncertainties that arise from the difference between nonlinear and linear models, by means of a multi-model approach: a finite family of linear models is considered (multi-model uncertainty), each of them operating appropriately in a certain region around a given operation point. Recursive feasibility, convergence to the economic setpoint and stability are ensured. The proposed controller is applied in two simulations for controlling an isothermal chemical reactor with consecutive-competitive reactions, and a continuous flow stirred-tank reactor with parallel reactions. (C) 2017 Elsevier Ltd. All rights reserved.
机译:经济模式预测控制器,由经济标准组成的动态调节问题的阶段成本,已显示出改善受控厂的经济性能。但是,在整个工厂的运作中,如果经济标准发生变化 - 由于价格的数量,成本,生产需求,市场波动,和解数据,扰动等 - 最佳操作点也发生了变化。在工业应用中,植物的非线性描述可能无法使用,因为识别非线性工厂是一项非常困难的任务。因此,用于预测的模型是一般的线性的。工厂的非线性行为使得使用线性模型设计的控制器(在某些操作点识别)可能表现出较差的闭环性能,甚至在工厂在不同操作点操作时甚至失去可行性和稳定性。避免这个问题的一种方法是考虑在工厂将被操作的每个平衡点处识别的线性模型的集合。这被称为工厂的多模型描述。在这项工作中,提出了一种多模型经济MPC,这考虑了从非线性和线性模型之间的差异产生的不确定性,通过多模型方法:考虑了一个有限的线性模型系列(多重模型不确定度),它们中的每一个在给定操作点周围的某个区域中适当地操作。递归可行性,确保了对经济设定值和稳定性的收敛性。所提出的控制器应用于两种模拟,用于控制具有连续竞争反应的等温化合物,以及具有平行反应的连续流动搅拌罐反应器。 (c)2017 Elsevier Ltd.保留所有权利。

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