Model based control of a reactive distillation column
(2001) Advanced Control of Chemical Processes 2000. (ADCHEM 2000). Proceedings volume from the IFAC Symposium — Location: Pisa, Italy (14.June.2000)
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- Authors
Bastin, Georges 
- Abstract
- The design and the performances of hybrid model based control of an industrial reactive distillation column are presented. The model structure is a combination of first principles with standard black-box techniques. The approach is based on easily established mass balance equations, the stoichiometry of the system and a model reduction from fast system dynamics. This model makes use of a combined physically meaningful variable from several physical inputs of the process. It is also a key variable for the optimization and the control of the underlying process. This model structure has been successfully used in an IMC scheme for the on-line control of this process.
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Citations
Libei Chen, Jie Zhang, Bastin, G., & Hontoir, Y. (2001). Model based control of a reactive distillation column. In Biegler, L.T.; Brambilla, A.; Scali, C.; Marchetti, G.; (ed.), Advanced Control of Chemical Processes 2000 (ADCHEM 2000). Proceedingsvolume from the IFAC Symposium (p. Vol. 1, p. 99-104). Elsevier science. https://hdl.handle.net/2078.5/225605