Nonlinear Model Predictive Control of Batch Processes: An Industrial Case Study
Authors: | Nagy Zoltan, Univ. Stuttgart, Germany Mahn Bernd, BASF Aktiengesellschaft, Ludwigshafen, Germany Franke Rudiger, ABB Corporate Research, Ladenburg, Germany Allgower Frank, Univ. Stuttgart, Germany |
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Topic: | 6.1 Chemical Process Control |
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Session: | Knowledge Driven Batch Processes |
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Keywords: | Industrial control, maximum likelihood estimation, multiple shooting algorithm, nonlinear model predictive control, parameter adaptive extended Kalman filter, parameter estimation, state estimation, real-time control |
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Abstract
Batch processes play a significant role in the production of most modern high-value added products. The paper illustrates the benefits of nonlinear model predictive control (NMPC) for the setpoint tracking control of an industrial batch polymerization reactor. Real-time feasibility of the on-line optimization problem from the NMPC is achieved using an efficient multiple shooting algorithm. A real-time formulation of the NMPC that takes computational delay into account is described. The control relevant model used in the NMPC is derived from the complex first principles model and is fitted to the experimental data using maximum likelihood estimation. A parameter adaptive extended Kalman filter (PAEKF) is used for state estimation and on-line model adaptation. The performance of the NMPC implementation is assessed via simulation and experimental results.