2005
DOI: 10.1016/j.powtec.2005.04.010
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Optimal control of a batch cooling seeded crystallizer

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Cited by 71 publications
(44 citation statements)
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“…Mazzotti et al [166,167] used model-based optimization techniques to control CSD in batch cooling crystallisation of paracetamol in ethanol and also the combined cooling/antisolvent crystallisation of acetylsalicylic acid in ethanol-water mixtures. Rohani and co-workers (see for example [168][169][170][171][172][173][174]) minimized the optimization objective function with respect to a parameter vector temperature input, subject to the mass balance dynamics as well as the PB equation to obtain optimal cooling policy for product quality control. They also developed real-time model-based optimal control of anti-solvent semi-batch crystallisation processes and seeded batch crystallisation processes using real-time single and multi-objective optimization, rigid logic and fuzzy logic control methods [171][172][173][174][175].…”
Section: Optimisation and Control Of Crystal Size Distribution (Csd)mentioning
confidence: 99%
“…Mazzotti et al [166,167] used model-based optimization techniques to control CSD in batch cooling crystallisation of paracetamol in ethanol and also the combined cooling/antisolvent crystallisation of acetylsalicylic acid in ethanol-water mixtures. Rohani and co-workers (see for example [168][169][170][171][172][173][174]) minimized the optimization objective function with respect to a parameter vector temperature input, subject to the mass balance dynamics as well as the PB equation to obtain optimal cooling policy for product quality control. They also developed real-time model-based optimal control of anti-solvent semi-batch crystallisation processes and seeded batch crystallisation processes using real-time single and multi-objective optimization, rigid logic and fuzzy logic control methods [171][172][173][174][175].…”
Section: Optimisation and Control Of Crystal Size Distribution (Csd)mentioning
confidence: 99%
“…Finally, m vap can be replaced in Equation (3). The kinetics parameter cryst is estimated via reverse technique thanks to seven databases supplied by the Bois-Rouge factory.…”
Section: Energy and Mass Balancementioning
confidence: 99%
“…In this aim, several advanced control algorithms (nonlinear model-based predictive control, generic model control, H  -control, etc.) were developed for both continuous and batch crystallization processes in numerous fields of application [1][2][3][4][5][6][7]. Even if modelbased strategies have proved to be efficient, in crystallization, the model design remains a crucial and difficult issue.…”
Section: Introductionmentioning
confidence: 99%
“…Generally, the CSD is directly affected by the non-equilibrium state of the system measured via supersaturation. Since supersaturation is a function of a crystallizer temperature, the slurry temperature is often used as the manipulated variable to control the non-equilibrium driving force of the system [3,4]. However, to achieve the objective of the control, an optimal condition and effective controllers are required.…”
Section: Introductionmentioning
confidence: 99%