Volume 42, Issue 4 pp. 788-796
Research Article

Influence of Impeller Diameter on Crystal Growth Kinetics of Borax in a Mixed Dual-Impeller Batch-Cooling Crystallizer

Antonija Čelan

Corresponding Author

Antonija Čelan

University of Split, Faculty of Chemistry and Technology, Department of Chemical Engineering, R. Boškovića 35, 21000 Split, Croatia

Correspondence: Antonija Čelan ([email protected]), University of Split, Faculty of Chemistry and Technology, Department of Chemical Engineering, R. Boškovića 35, 21000 Split, Croatia.Search for more papers by this author
Marija Ćosić

Marija Ćosić

University of Split, Faculty of Chemistry and Technology, Department of Chemical Engineering, R. Boškovića 35, 21000 Split, Croatia

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Igor Pehnec

Igor Pehnec

University of Split, Faculty of Electrical Engineering, Department of Mechanical Engineering and Naval Architecture, R. Boškovića 32, 21000 Split, Croatia

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Nenad Kuzmanić

Nenad Kuzmanić

University of Split, Faculty of Chemistry and Technology, Department of Chemical Engineering, R. Boškovića 35, 21000 Split, Croatia

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First published: 23 January 2019
Citations: 3

Abstract

The influence of impeller diameter on crystal growth kinetics of borax decahydrate in a batch-cooling crystallizer of non-standard aspect ratio was evaluated. The dual-impeller configuration consisted of a pitched-blade turbine which was mounted below a straight-blade turbine on a single shaft. Three different impeller-to-tank diameter ratios were investigated. In all experiments, mixing was conducted at just-suspended impeller speed. To examine hydrodynamic conditions, mixing times were measured. The fluid flow pattern and velocity distribution were determined by computational fluid dynamics. Results showed that the smallest but also more regularly shaped crystals were produced in a system with standard diameter impellers. Product yield and power consumption were highest in this case.

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