Analysis of the Possibility of Modeling Gas Separators using Computational Fluid Dynamics

IF 1.4 Q4 ENGINEERING, INDUSTRIAL Management Systems in Production Engineering Pub Date : 2024-02-26 DOI:10.2478/mspe-2024-0009
V. Mykhailiuk, M. Zasadzień, Mikhailo Liakh, Ruslan Deineha, Yurii Mosora, O. Faflei
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Abstract

Today, gas-liquid separators are usually used for the purification of gas mixtures from droplet liquid, and there are many designs of which. However, in order to improve the efficiency of their work, increase throughput, reduce mass and dimensions, they are constantly being improved. Usually, developing a new or improving an existing separator design is a long-term and relatively expensive process. Today, computer programs that implement the finite element method make it possible to speed up and reduce the cost of designing both a gas separator and other equipment. FloEFD program is one of these programs. However, it is more convenient during design to use one computer program that allows you to build 3D models (CAD) and in the same program to use a module for simulating the movement of gas and liquid flows (CFD). Such a program is SolidWorks with the FlowSimulation application module. As for the physical processes that occur during the operation of gas separators, they are quite complex, since a multiphase gas flow with an existing liquid phase is simulated. In the article, simulation modeling of the C-2-1 separator was carried out and the values and distributions of velocities and pressures in its various cross-sections were determined. Special attention was paid to the following cross-sections of the separator: along the axis of its inlet pipe; in the middle is the spigot of the blade screw; on a block of blinds. The difference in pressure at the outlet and inlet of the separator was determined, which is 20267 Pa. Based on the simulation results obtained, recommendations are given for further research and optimization of the separator design. The main parameter that characterizes the degree of separation of liquid from gas in the separator is the efficiency factor, which depends on the design of the separator, thermobaric conditions, parameters of the technological scheme, composition and physical and chemical properties of the gas-liquid flow. As a result of simulated modeling of the separator, its efficiency coefficient was determined when it extracted droplet liquid from the gas-liquid mixture in its various fractions (from 0.01 to 0.1 mm). The efficiency factor is about 100%.
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利用计算流体力学建立气体分离器模型的可能性分析
如今,气液分离器通常用于从液滴中净化气体混合物,其设计有很多种。然而,为了提高工作效率、增加吞吐量、减少质量和尺寸,分离器也在不断改进。通常,开发新的分离器或改进现有的分离器设计是一个长期且相对昂贵的过程。如今,采用有限元法的计算机程序可以加快气体分离器和其他设备的设计速度并降低成本。FloEFD 程序就是其中之一。不过,在设计过程中,更方便的做法是使用一种计算机程序,既能建立三维模型(CAD),又能在同一程序中使用模拟气体和液体流动的模块(CFD)。SolidWorks 就是这样一款带有流动模拟应用模块的软件。气体分离器运行过程中发生的物理过程相当复杂,因为需要模拟带有现有液相的多相气流。本文对 C-2-1 分离器进行了模拟建模,并确定了其各截面的速度和压力值及分布。特别关注了分离器的以下截面:沿进气管轴线;中间是叶片螺杆的拉钉;在一块百叶窗上。根据模拟结果,提出了进一步研究和优化分离器设计的建议。表征分离器中液体与气体分离程度的主要参数是效率系数,它取决于分离器的设计、热压条件、技术方案参数、气液流的组成和物理化学特性。通过对分离器进行模拟建模,确定了分离器从气液混合物中萃取不同粒度(从 0.01 毫米到 0.1 毫米)液滴时的效率系数。效率系数约为 100%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
CiteScore
4.30
自引率
13.30%
发文量
48
审稿时长
10 weeks
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