Advanced control with parameter estimation of batch transesterification reactor. (September 2015)

• Record Type: Journal Article
• Authors: Kern, Richard; Shastri, Yogendra
• Is Part Of: Journal of process control. Volume 33(2015:Sep.)
• Page Start: 127
• Page End: 139
• Publication Date: 2015-09
• Subjects: Transesterification -- Optimal control -- Nonlinear model predictive control -- Parameter estimation; Process control -- Periodicals; Fabrication -- Contrôle -- Périodiques; Process control; Periodicals; Electronic journals; 660.281
• DOI: 10.1016/j.jprocont.2015.06.006
• Languages: English
• ISSNs: 0959-1524

Abstract

Abstract : Highlights: A batch transesterification reactor model is developed. An evolutionary algorithm is implemented for batch to batch parameter estimation. Optimal control problem is solved to develop open loop control profile. NMPC is used for closed loop tracking of reference trajectory using a reduced model. Impact of different productivity objectives and parameter mismatch is quantified. Abstract: The objective of this work is to enhance the economic performance of a batch transesterification reactor producing biodiesel by implementing advanced, model based control strategies. To achieve this goal, a dynamic model of the batch reactor system is first developed by considering reaction kinetics, mass balances and heat balances. The possible plant-model mismatch due to inaccurate or uncertain model parameter values can adversely affect model based control strategies. Therefore, an evolutionary algorithm to estimate the uncertain parameters is proposed. It is shown that the system is not observable with the available measurements, and hence a closed loop model predictive control cannot be implemented on a real system. Therefore, the productivity of the reactor is increased by first solving an open-loop optimal control problem. The objective function for this purpose optimizes the concentration of biodiesel, the batch time and the heating and cooling rates to the reactor. Subsequently, a closed-loop nonlinear model predictive control strategy is presented in order to take disturbances and model uncertainties into account. The controller, designed with a reduced model, tracks an offline determined set-point reactor temperature trajectory by manipulating the heating and cooling mass flows to the reactor. Several operational scenarios are simulated and the results are discussed in view of a real application. With the proposed optimization and control strategy and no parameter mismatch, a revenue of 2.76 $ min −1 can be achieved from the batch reactor. Even with a minor parameter mismatch, the revenue is still 2.01 $ min −1 . While these values are comparable to those reported in the literature, this work also accounts for the cost of energy. Moreover, this approach results in a control strategy that can be implemented on a real system with limited online measurements.