Liquid back-mixing in packed-bubble column reactors: a state-of-the-art correlation |
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Authors: | Lamia Belfares Miryan Cassanello Bernard P A Grandjean Faïal Larachi |
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Affiliation: | a Department of Chemical Engineering and CERPIC, Université Laval, Ste-Foy, Québec, Canada G1K 7P4 b PINMATE, Departmento de Industrias, Facultad de Ciencias Exactas y Naturales, Universidad de Buenos Aires, Ciudad Universitaria, 1428 Buenos Aires, Argentina |
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Abstract: | The extent of liquid back-mixing in gas–liquid concurrent upflow packed-bubble column reactors is quantified in terms of an axial dispersion coefficient or its corresponding dimensionless Péclet number. Effects of reactor operating conditions on the axial dispersion coefficient are not properly accounted for by the available literature correlations, wherein most often the Péclet number is expressed solely in terms of the gas and liquid Reynolds numbers or superficial velocities. Based on the broadest experimental databank (1322 measurements, 11 liquids, four gases, 28 packing materials, 14 columns diameters, Newtonian, non-Newtonian, aqueous, organic, coalescing and non-coalescing liquids, high pressure, bubble and pulsing flow regime conditions), a state-of-the-art liquid axial dispersion coefficient correlation is obtained by combining neural network modeling and dimensional analysis. Thorough qualitative and quantitative analyses of the constructed databank demonstrate the robustness of the proposed correlation to restore the variety of trend variations of liquid Péclet numbers reported in the literature. |
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Keywords: | Gas–liquid upflow Packed-bubble column Liquid back-mixing Neural network |
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