Integrating dynamic economic optimization and model predictive control for optimal operation of nonlinear process systems

• Published in: Control engineering practice Vol. 22; pp. 242 - 251
• Main Authors: Ellis, Matthew, Christofides, Panagiotis D.
• Format: Journal Article
• Language: English
• Published: Elsevier Ltd 01.01.2014
• Subjects: Dynamical systems; Economic model predictive control; Economic process optimization; Economics; Feedback control; Mathematical models; Model predictive control; Nonlinear control; Nonlinear dynamics; Optimization; Process control; Stability; Trajectories; Model predictive control; Economic model predictive control; Process control; Nonlinear control; Economic process optimization
• ISSN: 0967-0661; 1873-6939
• DOI: 10.1016/j.conengprac.2013.02.016

In this work, we propose a conceptual framework for integrating dynamic economic optimization and model predictive control (MPC) for optimal operation of nonlinear process systems. First, we introduce the proposed two-layer integrated framework. The upper layer, consisting of an economic MPC (EMPC) system that receives state feedback and time-dependent economic information, computes economically optimal time-varying operating trajectories for the process by optimizing a time-dependent economic cost function over a finite prediction horizon subject to a nonlinear dynamic process model. The lower feedback control layer may utilize conventional MPC schemes or even classical control to compute feedback control actions that force the process state to track the time-varying operating trajectories computed by the upper layer EMPC. Such a framework takes advantage of the EMPC ability to compute optimal process time-varying operating policies using a dynamic process model instead of a steady-state model, and the incorporation of suitable constraints on the EMPC allows calculating operating process state trajectories that can be tracked by the control layer. Second, we prove practical closed-loop stability including an explicit characterization of the closed-loop stability region. Finally, we demonstrate through extensive simulations using a chemical process model that the proposed framework can both (1) achieve stability and (2) lead to improved economic closed-loop performance compared to real-time optimization (RTO) systems using steady-state models.