Oil production technology includes a large number of processes in its cycle, such as extraction,
pressing, extraction, evaporation of miscella is one of the most complex and energy-intensive
processes. Intensification and optimization of these processes, increasing the efficiency of distillation
units is a very urgent task.
The study of heat and mass transfer in gas-liquid streams, taking into account the hydrodynamic
situation in distillation units, makes it possible to objectively assess the advantages and disadvantages
of devices, contributes to more targeted developments in the field of rational design of technological
units. An increase in the productivity and optimization of the distillation processes of oil miscells can
be achieved by organizing a rational structure of phase flows, which ensures the maximum gradients
of temperatures, concentrations and intensification of heat and mass transfer

Optimization,, efficiency

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