Experimental analysis of gas hold-up for gas-liquid system agitated in a vessel equipped with two impellers and vertical tubular baffles
Author:
Affiliation:
1. West Pomeranian University of Technology, Szczecin , Faculty of Technology and Chemical Engineering , al. Piastów 42, 71-065 Szczecin , Poland
Abstract
Publisher
Walter de Gruyter GmbH
Subject
General Chemical Engineering,General Chemistry,Biotechnology
Link
https://www.sciendo.com/pdf/10.2478/pjct-2018-0002
Reference27 articles.
1. 1. John, A.H., Bujalski, W. & Nienow, A.W. (1997). A novel reactor with independently-driven dual impellers for gas-liquid processing. Recents Progr. Genie Proced. 11, 5, 169–176.
2. 2. Bouaifi, M., Hebrard, G., Bastoul, D. & Roustan, M. (2001). A comparative study of gas hold-up, bubble size, interfacial area and mass transfer coefficients in stirred gas-liquid reactors and bubble columns. Chem. Eng. Proc., 40, 97–111. DOI: 10.1016/S0255-2701(00)00129-X.10.1016/S0255-2701(00)00129-X
3. 3. Majirova, H., Pinelli, D., Machon, Y. & Magelli, F. (2003). Gas flow behavior in a two-phase sparged reactor stirred with multiple turbines. 11th European Conference on Mixing, 14–17 October 2003 (pp. 245–252), Bamberg.
4. 4. Moucha, T., Linek, V. & Prokopova, E. (2003). Gas hold-up, mixing time and gas-liquid volumetric mass transfer coefficient of various multiple-impeller configurations: Rushton turbine, pitched blade and techmix impeller and their combinations. Chem. Eng. Sci., 58, 1839–1846. DOI: 10.1016/S0009-2509(02)00682-6.10.1016/S0009-2509(02)00682-6
5. 5. Pinelli, D., Bakker, A., Myers, K.J., Reeder, M.F., Fasano, J. & Magelli, F. (2003). Some features of a novel gas dispersion impeller in a dual-impeller configuration. Trans IChemE, 81, 448–454.10.1205/026387603765173709
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