Closed-Loop Control of Reactive Crystallization. Part I: Supersaturation-Controlled Crystallization of L-Glutamic Acid

The feedback control policy of the reactive crystallization process is studied. A concentration of a crystallizing compound is used to compute the feedback in the closed‐loop control of semi‐batch precipitation. The pH is used as a second feedback value, and the dynamic change of the set value is ba...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:Chemical engineering & technology 2010-05, Vol.33 (5), p.743-750
Hauptverfasser: Alatalo, H. M., Hatakka, H., Louhi-Kultanen, M., Kohonen, J., Reinikainen, S.-P.
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
Beschreibung
Zusammenfassung:The feedback control policy of the reactive crystallization process is studied. A concentration of a crystallizing compound is used to compute the feedback in the closed‐loop control of semi‐batch precipitation. The pH is used as a second feedback value, and the dynamic change of the set value is based on the mass of added acid. The concentration of L‐glutamic acid is determined from measured MID‐IR attenuated total reflection‐Fourier transform infrared (ATR‐FTIR) spectra based on a multivariate model. The importance of the supersaturation level control at the nucleation moment and the effect of different supersaturation levels on the quality of the product crystals are studied by using a 50‐L crystallizer. The studied crystal properties of the product are polymorphism (reported metastable α‐ and stable β‐forms) and crystal size. The results show that the feedback process control system developed in this study makes it possible to control the formation of polymorphs effectively. The feedback control policy of the reactive crystallization process was studied. The concentration of L‐glutamic acid was determined from measured MID‐IR ATR‐FTIR spectra based on a multivariate model. The importance of the supersaturation level control at the nucleation moment and the effect of different supersaturation levels on the quality of the product crystals was studied using a 50‐L crystallizer.
ISSN:0930-7516
1521-4125
DOI:10.1002/ceat.200900550