4 CONCLUSION
The process of dissipating heavy liquid into droplets
by mixing fluid phases with inert gas was performed
on the experimental device of the dredge extractor.
Depending on the mixing time at the constant phase
velocity values, the distribution of the droplets on
different gas velocity values by grinding and size was
determined by experiments. The regression equations
were processed using the computer.
Based on the results of the experimental studies,
the total surface diameters of the droplets were
determined. A formula for calculating the total
surface diameter of droplets, which is important for
the calculation of mass transfer processes, depending
on the physical and chemical properties of liquids,
was proposed, and theoretical and experimental
values were compared.The calculations carried out
completely confirmed the proposed formula. As a
result of the research, it was possible to determine the
surface surface diameter of the dispersion phase drop
and the relative phase contact surfaces, which is one
of the key determinants of the efficiency of the
proposed bubble extractor.
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