Vol. 25, No. 3 (2026), Sim26874 https://doi.org/10.24275/rmiq/Sim26874


Experimental implementation of MPC strategy by manipulating the stirring speed to control secondary nucleation in continuous crystallization


 

Authors

M. Presenda-de Dios, A. Reyes-Obando, L. A. Ricardez-Sandoval, P. A. Quintana-Hernández


Abstract

This paper presents the experimental implementation of a multivariable model predictive control (MPC) for the continuous crystallization of ammonium sulfate in a Mixed-Suspension, Mixed-Product-Removal (MSMPR) crystallizer. The strategy employs a dynamic model based on balances of mass, energy and population and coordinates stirring speed and coolant flow as manipulated variables for the simultaneous control of average crystal diameter D(4,3) and the crystallizer temperature. This multivariable control strategy is innovative because incorporates hydrodynamics effects on mechanically induced secondary nucleation. The experiments were conducted in a pilot plant equipped with Process Analytical Technology (PAT) for online monitoring of Crystal Size Distribution (CSD), temperature and solution concentration. The results demonstrated that the MPC was able to maintain operation within the metastable zone, reduced process oscillations, and improved setpoint tracking. Furthermore, the implementation of digital filtering and the adjustment of predictive horizons reduced the error associated with the CSD and stabilized control actions, validating the feasibility of the active use of agitation in the control of continuous crystallization systems.


Keywords

multivariable control, crystallization, ammonium sulfate, secondary nucleation, metastable zone operation.


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