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Drop dispersion and coalescence phenomena depend on the fine-scale properties of turbulence, including its intermittency.
Correction factors for the traditional equations used for micromixing and drop dispersion were easily derived from the β-model.
Examples of such corrections are given for micromixing and drop dispersion as well as for the scale-up of these operations.
The identification of stretching and compression regions of strain and the quantification of the relevant terms is discussed in the context of drop dispersion and with reference to previously reported observations.
A free turbulent jet discharging into a tank is a simple device and can develop local turbulent energy dssipation rates on the order of 103 104 W kg−1, which are suitable for fast reactions and drop dispersion.
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A drop of dispersion was then transferred to carbon coated grid for further analysis.
For samples containing between 10 000 and 20 000 ppm sodium a moderate drop in dispersion and an increase in heats of CO and H2 chemisorption were observed.
A drop of dispersion was placed onto a glass substrate and left to dry.
It is apparent that such low effluent concentrations from gravity separators can only be realized, in general, if the finest drops in a dispersion, secondary drops (drops with diameters less than 100 μm), coalesce and are separated from the continuous phase.
TEM samples were prepared by drop-casting dispersion onto copper grids covered by carbon film.
The samples were prepared by dropping the dispersion of gold products onto the carbon-coated copper grid and dried in ambience.
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