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Improvement of Parameters for the Multi-Functional Oil-Gas Separator of “HEATER-TREATER” Type

机译:改进的“加热处理”型油气分离器参数的改进

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This The article deals with the modeling of separation processes in a multifunctional oil-gas separator of “HEATER-TREATER” type, which allow effectively separating a gas-liquid hydrocarbon mixture into separate components by the combination of different methods of separation (processes of heating, separation, and dehydration). The engineering technique for design calculation of sections of the device is developed considering the main factors influencing the separation process and determines the optimal hydrodynamic and structural parameters. The method of testing the hypothesis of increasing the parameters of linear motion for the mixture in the apparatus more than 2.0-2.5 times is proposed by using CFD model of the porous medium. This approach is aimed at reducing finite volume grid, which contains a significant number of elements. According to this technique, it is necessary to determine the related constant (which contains in viscous coefficient of resistance) separately for each type of plate according to the results of the numerical experiment. For the less laborious and consumptive determination of the constants, the proposed approach should be based on the results a numerical experiment.
机译:本文涉及“ HEATER-TREATER”型多功能油气分离器中分离过程的建模,该分离器可通过组合不同的分离方法(加热过程)有效地将气液烃混合物分离为单独的组分,分离和脱水)。考虑到影响分离过程的主要因素并确定最佳流体力学和结构参数,开发了用于设备截面设计计算的工程技术。利用多孔介质的CFD模型,提出了一种检验装置中混合物线性运动参数增加2.0-2.5倍以上的假说的方法。该方法旨在减少有限体积的网格,该网格包含大量元素。根据该技术,有必要根据数值实验的结果分别确定每种类型的板的相关常数(其包含在粘性电阻系数中)。对于较省力和耗时的常数确定,建议的方法应基于结果进行数值实验。

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