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An empirical correlation is proposed for the estimation of the Sauter mean drop diameter.
From these measurements, Sauter mean drop diameter (d3,2) has been estimated.
The mean drop diameter decreases all along with increasing jet flow rate.
The Sauter mean drop diameter decreases with increasing continuous-phase viscosity, but increases with increasing stirring speed.
It was observed that the mean drop diameter downstream of the restriction linearly increases as a function of the inverse of the square root of the pressure drop.
By means of this equation the mean drop diameter could be evaluated for intensive flow pulsation (or plate vibration) within 20% accuracy.
Similar(48)
In this study, drop size distribution and Sauter mean drop diameters were measured and correlated under operating variables and physical properties of the systems using a 113 mm diameter Kühni column.
The simplified correlation of Kumar and Hartland could be used for estimating the Sauter-mean drop diameter.
The Sauter-mean drop diameter was found to depend on the specific power consumption in accordance with the turbulent model due to the turbulent energy dissipation in well-mixed regions around perforated plates.
The main goal was to define the effects of the vibration intensity and the important reaction operating conditions on the pressure fluctuation at the reactor bottom, the power consumption, the dispersed phase holdup, the Sauter-mean drop diameter and the specific interfacial area.
The first model requires as input the average drop diameter and the residence time while the second model uses the measured drop diameter distribution.
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