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Direct-contact dehumidification in bubble columns has been shown to significantly decrease dehumidifier size and cost.
A theoretical model for volumetric mass transfer coefficients in bubble columns has been developed.
A new two-region phenomenological model for liquid-phase mixing in churn-turbulent bubble columns has been proposed.
The gas liquid contact time has been defined in a new way (bubble surface-to-rate of surface formation) and the range of applicability of the penetration theory in both gas liquid and slurry bubble columns has been examined.
In addition, a modified version of the N-o-Z model for bubble columns has been simply derived from the impeller version, assuming the existence of a two-loop axisymmetrical circulation pattern induced by the non-uniform distribution of gas holdup in bubble columns.
The influence of alcohol concentration on the gas void fraction in open tube and annular gap bubble columns has been investigated using a vertical column with an internal diameter of 0.102 m, containing a range of concentric inner tubes, which formed an annular gap; the inner tubes had diameter ratios from 0.25 to 0.69.
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Bubble columns have been widely used for an ozonation system in the plants and laboratories.
Two bubble columns have been used: a narrow rectangular (2D) column and a cylindrical (3D) column.
The following geometries of bubble columns have been investigated in the past: (i) two-dimensional column with off-center sparging, (ii) two-dimensional column with central sparging, (iii) two-dimensional column with uniform sparging and (iv) cylindrical columns with uniform sparging.
The bubble column has been operated both in the batch mode and in the counter-current mode.
In this work a detailed experimental hydrodynamic characterization of a needle sparger rectangular bubble column has been performed.
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