Simulation of mixing and crushing of liquid at the initial site by a high-temperature gas flow

A mathematical model of mixing and crushing of a liquid at the initial site of a device for supplying a solution with a high-temperature gas flow has been developed. The process of mixing and crushing using the energy of hot water vapor, cotton oil misc when it is fed to the final distillation process is considered. An analytical method for calculating the actual size of the initial section of the nozzle for the supply of solution has been developed. Based on the initial data of the process of final distillation of cotton oil misc in production, by methods of mathematical modeling of the hydrodynamics of phases, the radii of the nozzle nozzle for hot steam and liquid, the location of the location of the liquid input into the steam stream are theoretically determined. The dimensions of the mixing chamber and the length of the initial section are determined. The initial parameters of the main and passive flows are proposed based on the conditions of liquid crushing by the Weber and Reynolds criteria.

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