(479c) Scale-up Rules for Taylor-Couette Disc Contactor Design
AIChE Annual Meeting
2017
2017 Annual Meeting
Separations Division
Extractive Separations Fundamentals and Design
Wednesday, November 1, 2017 - 8:50am to 9:15am
The industrial scale implementation of processes for mass transfer with and without chemical conversion demands reliable scale up rules. Therefore, it is important to elaborate basic experiments for validation of CFD-simulation and for the dimensional analysis [2]. For liquid-liquid phase contactors the reliable prediction of hydrodynamics is a critical issue for the design and scale-up. Since design rules for the prediction of hydrodynamic data for the TCDC are still not available, correlations for the determination of the drop size distribution, the Sauter mean diameter and the dispersed phase hold-up where derived via dimensionless analysis [3]. The correlations have been validated with experimental data from 0.1 and 0.3 m diameter pilot plant scale operation with 1 m active column height. The results of mass transfer experiments have confirmed that the concentration profile and the separation efficiency can simply be modeled with CSTR cascade design [4]. The determination of the residence time distribution has confirmed CSTR cascade operation when exceeding a critical rotational speed. The outcome of CFD-analysis and the experiments provides simple tools for the basic design of the TCDC.
Literature
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[2] M. Zlokarnik, Chem. Eng. Technol. 2004, 27 (1), 23â27. DOI: 10.1002/ceat.200403158
[3] A. Grafschafter, M. Siebenhofer, Chemie Ing. Tech. 2017, 4, DOI: 10.1002/cite.201600142
[4] A. Grafschafter, E. Aksamija, M. Siebenhofer, Chem. Eng. Technol. 2016, 39 (11), 2087â2095. DOI: 10.1002/ceat.201600191