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Numerical Simulation on Structure Optimization of Liquid-Gas Cylindrical Cyclone Separator

机译:液-气圆柱旋风分离器结构优化的数值模拟

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With the further development of oilfield, liquid-gas separation has become an essential problem. Cylindrical cyclone separators are popular in the industrial process due to the advantage that they are simple, compact, and inexpensive to manufacture. In this paper, a three-dimensional turbulence model including Reynolds stress model was established to describe the mixture flow field in the separator. Through the numerical simulation, the separation efficiency was investigated under different parameter cases such as separator length, gas phase outlet diameter, and inlet shape. It can be indicated from the simulation results that the separation efficiency decreases with the increase of the separator length, and the separation efficiency increases firstly and then decreases with the increase of the gas phase outlet diameter as well as the liquid phase outlet. Furthermore, the rectangular inlet is more suitable than the circular inlet with the separation efficiency changing from 66.45% to 79.04%. In the end, the optimal geometrical structure was presented with separation efficiency of 86.15%.
机译:随着油田的进一步发展,液气分离已成为必不可少的问题。圆柱形旋风分离器由于其简单,紧凑且制造便宜的优点而在工业过程中很流行。本文建立了包括雷诺应力模型的三维湍流模型来描述分离器内的混合流场。通过数值模拟,研究了分离器长度,气相出口直径和入口形状等不同参数情况下的分离效率。从仿真结果可以看出,分离效率随分离器长度的增加而降低,分离效率随气相出口直径和液相出口直径的增加先升高后降低。此外,矩形进样口比圆形进样口更合适,分离效率从66.45%变为79.04%。最后,提出了最佳的几何结构,分离效率为86.15%。

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