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Modelling and Simulation in Engineering
Volume 2012, Article ID 912071, 11 pages
http://dx.doi.org/10.1155/2012/912071
Research Article

Nonlinear MIMO Control of a Continuous Cooling Crystallizer

1Departamento de Ingenieria Quimica, Instituto Tecnológico de Celaya, Avenida Tecnológico y García Cubas S/N, 38010 Celaya, GTO, Mexico
2Facultad de Química, Universidad de Guanajuato, Noria Alta s/n, 36050 Guanajuato, GTO, Mexico

Received 11 April 2012; Accepted 20 September 2012

Academic Editor: Ahmed Rachid

Copyright © 2012 Pedro Alberto Quintana-Hernández et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

Abstract

In this work, a feedback control algorithm was developed based on geometric control theory. A nonisothermal seeded continuous crystallizer model was used to test the algorithm. The control objectives were the stabilization of the third moment of the crystal size distribution () and the crystallizer temperature (); the manipulated variables were the stirring rate and the coolant flow rate. The nonlinear control (NLC) was tested at operating conditions established within the metastable zone. Step changes of magnitudes ±0.0015 and ±0.5°C were introduced into the set point values of the third moment and crystallizer temperature, respectively. In addition, a step change of ±1°C was introduced as a disturbance in the feeding temperature. Closed-loop stability was analyzed by calculating the eigenvalues of the internal dynamics. The system presented a stable dynamic behavior when the operation conditions maintain the crystallizer concentration within the metastable zone. Closed-loop simulations with the NLC were compared with simulations that used a classic PID controller. The PID controllers were tuned by minimizing the integral of the absolute value of the error (IAE) criterion. The results showed that the NLC provided a suitable option for continuous crystallization control. For all analyzed cases, the IAEs obtained with NLC were smaller than those obtained with the PID controller.