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Detailed Modelling of Hydrocarbonaceous Media Separation Process

机译:烃类介质分离过程的详细建模

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This paper presents the results of a detailed study of the separation process in the range of characteristic values temperature (T ≌ 0 ÷ 70°C) and pressure (P ≌ 50 ÷ 700 kPa). The critical analysis of hydrocarbonaceous media separation process problem is made within functioning processing equipment on objects of the "Vyngapurovskoe" oil field in Russia. Modelling of first stage separation process is illustrated from data of reservoir fluid with detailed characteristic of evolution some components concentration into off-gas in dependence of temperature and pressure. Recommendations to the calculation of the component composition of hydrocarbonaceous fluids under the provisions of equilibrium thermodynamics using the model of Peng-Robinson are extradited. It has been established that the heavy hydrocarbons (C_(4+higher)) concentration decreasing into off-gas theoretically could be achieved up to 48.41%.
机译:本文介绍了特征值温度(T = 0×70℃)和压力范围内的分离过程的详细研究结果(P≥50±700kPa)。烃类媒体分离过程问题的临界分析是在俄罗斯“vyngapurovskoe”油田的物体上的运作处理设备中。第一阶段分离过程的建模由储层流体的数据进行说明,其在依赖温度和压力的情况下将一些成分浓度的详细特征浓缩到废气中。引入了使用PENG-Robinson模型的平衡热力学规定下计算碳氢化合物流体组成的建议。已经确定,在理论上降至废气中的重质烃(C_(4 +更高))浓度可实现高达48.41%。

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