| Summary: | The article focuses on the gases cleaning various methods from the dispersed phase, that adversely affects on the holding of technological processes. The design and scheme of the drying gas separator from condensed moisture and the method of its calculation are presented. The dependence of the energy complex of the gas velocity for different nozzles, which shows that the best is to use nozzles "Inzhekhim-2000" with a surface nozzle area of 800 m2 / m3 . The separation efficiency calculations of water drops from a natural gasbearing strata gazasenomanskaya and oil aerosol ethylene –coolagents in this unit is calculated. Combined separator ensures high efficiency of the separator removal of the liquid phase (98-99%), larger than 3 microns and oil aerosol – more than 1 m. Thus, a combined separator has a relatively small geometrical dimensions. The device has a low hydrodynamic resistance, thereby energy costs for its operation are reduced.
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