AIChE Journal · 2003 · 299 citations · 41 references
EngineeringIndustrial EngineeringManufacturing EngineeringProcess ControlProcess Systems EngineeringUncertainty QuantificationBatch Process ControlController DesignModel Predictive ControlOptimal ControlProcess RobustnessRobust ControlExtended Kalman FilterNonlinear Model Predictive ControlParameter Uncertainty AnalysisParameter Uncertainty QuantificationRobust Nonlinear ControlRobust PerformanceRobustness AnalysisState Feedback Control
NMPC explicitly handles constraints and nonlinearities in batch process feedback control. The algorithm incorporates parameter uncertainty into state estimation and feedback via an EKF that estimates process‑noise covariance, employs a shrinking‑horizon NMPC minimizing a weighted sum of nominal performance, its variance, and deviation from the nominal trajectory, and quantifies robustness through a distributional analysis of the performance index, demonstrated on a simulated batch crystallization process. The robust NMPC improves performance sixfold over open‑loop optimal control and twice over nominal NMPC, with Monte Carlo simulations confirming the distributional robustness analysis.
Abstract NMPC explicitly addresses constraints and nonlinearities during the feedback control of batch processes. This NMPC algorithm also explicitly takes parameter uncertainty into account in the state estimation and state feedback controller designs. An extended Kalman filter estimates the process noise covariance matrix from the parameter uncertainty description and employs a sequential integration and correction strategy to reduce biases in the state estimates due to parameter uncertainty. The shrinking horizon NMPC algorithm minimizes a weighted sum of the nominal performance objective, an estimate of the variance of the performance objective, and an integral of the deviation of the control trajectory from the nominal optimal control trajectory. The robust performance is quantified by estimates of the distribution of the performance index along the batch run obtained by a series expansion about the control trajectory. The control and analysis approaches are applied to a simulated batch crystallization process with a realistic uncertainty description. The proposed robust NMPC algorithm improves the robust performance by a factor of six compared to open loop optimal control, and a factor of two compared to nominal NMPC. Monte Carlo simulations support the results obtained by the distributional robustness analysis technique.
41
Constrained model predictive control: Stability and optimality
D.Q. Mayne, James B. Rawlings, Christopher V. Rao et al. · Automatica · 2000 · 8.5K citations
Model predictive control: Theory and practice—A survey
Carlos E. García, David M. Prett, Manfred Morari · Automatica · 1989 · 5.3K citations
Some problems in particle technology
Hugh M. Hulburt, Stacy Katz · Chemical Engineering Science · 1964 · 1.6K citations