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Simulation results for on-line optimization of a batch bioreactor using nonlinear filtering and optimal control
1Grupo de Control de Procesos, Instituto de Desarrollo Tecnológico para la Industria Química (INTEC), Güemes 3450 (3000) Sante Fe, República Argentina. rdondo@ceride.gov.ar
ISA Transactions
|April 24, 2003
Summary
This study introduces a novel approach for batch bioreactor control, using an observer to estimate kinetic parameters for adaptive, near-optimal control trajectories. This method enhances fermentation process reliability despite model uncertainties.
Area of Science:
- Biotechnology
- Chemical Engineering
- Process Control
Background:
- Optimal control profiles for batch bioreactors often rely on simplified, empirical models.
- Model uncertainties can significantly impact the reliability of calculated control profiles.
- Existing methods may not adequately adapt to real-time fermentation dynamics.
Purpose of the Study:
- To develop a robust method for calculating near-optimal control trajectories in batch bioreactors.
- To address the challenge of model uncertainty in bioreactor process control.
- To create an adaptive control strategy for running fermentations.
Main Methods:
- Implemented a moving time horizon approach for successive control profile calculations.
- Utilized a mathematical model with kinetic parameters estimated by a nonlinear observer.
- Combined a nonlinear estimator with an optimizer for adaptive control.
Main Results:
- Numerical simulations were performed on xanthan-gum batch fermentations.
- The proposed method demonstrated reasonably good results in generating adaptive control trajectories.
- The nonlinear estimator plus optimizer arrangement proved effective for batch fermentors.
Conclusions:
- The developed method provides a reliable way to compute near-optimal control profiles for batch bioreactors.
- Adaptive control using real-time parameter estimation enhances fermentation process performance.
- This approach offers a promising advancement for optimizing bioprocesses with inherent model uncertainties.