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Exact(30)
With the uncontrolled sized bubbles, the average bubble size corresponding to the two-dimensional bed is found, and is not affected by decrease or increase of flow rates.
The average bubble size was found to be affected by dodecane dosage.
In order to determine the average bubble size in a flowing foam, a novel approach to estimate the average bubble size was developed, based upon the overflowing foam liquid content and conductivity measurements.
However, for both designs, the average bubble size has been related to an invariant dimensionless parameter, the laminar Weber number.
Techniques have been developed to characterize chromatic information, average bubble size, froth texture, froth stability and mobility of surface froths.
Where average bubble size decreases, this can be attributed to the difference in slip velocity between different sized bubbles.
Similar(30)
It is shown that as the bed diameter is increased, average bubble sizes decrease although similar-sized bubbles rise faster because of lower wall resistance, both factors contributing to faster solids circulation.
All foamed emulsions were examined by light microscopy, and average bubble sizes were obtained by evaluating the respective images (see Supporting Information).
The dosage of frother plays vital role as it affects the bubble size distribution and mean bubble size.
The model predicts spatial distribution of gas holdup, average local bubble size and flow structure.
The interfacial area achem in a gas liquid contactor as determined by the chemical method deviates from the true geometrical interfacial area ageo, because the overall conversion of the gas phase reactant represents an incorrect average if bubble sizes and residence times are not uniform.
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