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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.
A functional form of equation for predicting pressure drop in a modified non-Newtonian downflow bubble column has been formulated.
Quality of mixing in a modified downflow bubble column has been analyzed by using information entropy theory.
In addition, a countercurrent bubble column has been commonly recommended than a cocurrent one because it has a higher ozone transfer efficiency.
The external loop airlift bubble column has been regarded as a promising type of gas liquid or gas liquid solid biooreactor because of the liquid circulating flow between the riser and downcomer.
Similar(52)
The experimental gas holdup data in such modified bubble column have been analyzed by slip velocity and drift-flux models.
Most of available gas liquid mass transfer data in bubble column have been obtained in aqueous media and in liquid batch conditions, contrary to industrial chemical reactor conditions.
Gas holdup, gas phase distribution and solids phase distribution in a high pressure bubble column have been examined using non-instrusive neutron techniques.
The main transition velocities Utrans in two semi-rings (from the cross-section of the bubble column) have been identified based on both the IE and RE values as well as a new parameter, which has been calculated from each signal reconstruction.
Direct-contact dehumidification in bubble columns has been shown to significantly decrease dehumidifier size and cost.
More suggestions(14)
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