Considerable attention is paid to the improvement of the processes of high-quality and productive separation of liquid heterogeneous systems SHAPE \\* MERGEFORMAT in the oil and gas industry from both manufacturers and scientists. To carry out these operations, various types of designs of sedimentation tanks, separators, hydrocyclones, etc. are used, the principle of operation of which is based on gravitational and centrifugal separation of inhomogeneous masses of various densities. It should be noted that when designing separators with a high value of the performance index, it is insufficiently possible to use numerous theoretical studies in the field of hydromechanics of flow in a centrifugal field. This is due to the extreme complexity of the conditions for the flow of the separated fluid in the rotor space. Therefore, experimental studies of intra-rotor flows have become very important at present. So, it was experimentally shown that, during the intensification of the separation process, it is impossible to study the operation of individual parts of the rotor separately, but it is necessary to consider the operation of the system, including the plate package, sludge space, high-pressure channels and an unloading device. Thus, we can conclude that the increase in the performance of separators due to the increase in their size has approached the limit and the use of some more reserves in this direction is obviously associated with the need to overcome great and unjustified difficulties. Further development of this direction is irrational. However, there is a way to intensify the separation process by equalizing the distribution of the rotor and batch flows, improving the packages, eliminating the flotation effect and the destruction of the dispersed phase, adapting the operating mode of the separators depending on changes in the properties of the separated liquid. In industrial conditions, for example, when cleaning a highly paraffinized formation fluid, crusts form in the hydrocyclone, periodically clogging the discharge hole. In order to ensure the best hydrodynamic process conditions for the separation of formation fluid in a hydrocyclone and to prevent clogging of the discharge outlet, an apparatus is proposed that contains only the cylindrical part of the housing. A feature of the proposed design is that the optimal ratio of length to diameter is in the range of 3-5 with other ratios of other characteristics used in the calculation, equal to the ratios of characteristics in known hydrocyclones. This length of the hydrocyclone provides the conditions for the effective separation of the reservoir fluid and the withdrawal of the condensed fraction through the discharge opening. The obtained results of studies performed on a real product at pressure and flow rate, corresponding to the production ones, made it possible to design and manufacture an industrial model of the apparatus. The experimental data can be used to calculate similar hydrocyclones intended for use in other mixtures.
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