Droplet Size Distribution of the Liquid Phase in a Vortex Separation Device

IF 0.7 4区 工程技术 Q4 ENGINEERING, CHEMICAL
O. S. Dmitrieva, V. V. Kharkov, A. N. Nikolaev
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引用次数: 0

Abstract

The vortex form of multiphase flows is often organized in installations used in the electric power industry, the petroleum and chemical industries, and nuclear energy. Separators of various designs are used to separate gas-liquid flows. Predicting the composition of the dispersed phase is essential for the proper design, operation, and optimization of two-phase flow systems, because a parameter such as the efficiency of the separator strongly depends on the operating mode and the nature of droplet breakup. The dynamics of the gas–liquid flow under swirling conditions has been studied and is of great interest, and there are several mathematical models of droplet breakup. The analysis of the factors influencing the separation characteristics of the device depending on the characteristic zones of the droplet layer is carried out. On this basis, an experimental setup is uses to determine the size distribution of liquid droplets at the inlet to the vortex separation device with a change in the average velocity of the gas through the device from 15 to 23 m/s and a liquid phase rate of 150 kg/h. The electrical contact method is utilized in the study using a special two-needle probe with replaceable contact heads. In this work, experimental confirmation of the validity of using a logarithmic normal distribution is obtained to describe the dispersed composition of droplets at the swirler inlet. The calculation of the nonnormalized distribution function averaged over the section of the separation device for droplets flying through the interblade channels without interaction with the swirler blades is performed. Graphical dependences of the droplet distribution density function are presented. A calculated ratio is presented to determine the average value of the mass fraction of liquid droplets that does not interact with the swirler blades. An analysis of the dispersed composition of droplets flying through the interblade channels of the swirler without interaction with the blades shows that this phenomenon is typical only for fine droplets.

Abstract Image

涡流分离装置中液相液滴的粒径分布
在电力工业、石油和化学工业以及核能中使用的装置中经常组织多相流的涡旋形式。各种设计的分离器用于分离气液流动。预测分散相的组成对于两相流系统的正确设计、操作和优化至关重要,因为分离器的效率等参数在很大程度上取决于操作模式和液滴破碎的性质。旋流条件下气液流动的动力学研究引起了人们的极大兴趣,液滴破碎的数学模型有几种。根据液滴层的特征区,分析了影响装置分离特性的因素。在此基础上,利用实验装置确定了气流通过装置的平均速度为15 ~ 23 m/s,液相速率为150 kg/h时,涡流分离装置入口处液滴的大小分布。电接触方法在研究中使用了一种特殊的双针探针,具有可更换的接触头。在本工作中,实验证实了使用对数正态分布来描述旋流器入口液滴分散组成的有效性。计算了液滴在不与旋流叶片相互作用的情况下通过叶间通道的非归一化分布函数在分离装置截面上的平均值。给出了液滴分布密度函数的图形依赖关系。提出了一种计算比,用于确定不与旋涡叶片相互作用的液滴质量分数的平均值。分析了在不与叶片相互作用的情况下通过旋流器叶间通道飞行的液滴的分散成分,表明这种现象仅对细液滴是典型的。
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来源期刊
CiteScore
1.20
自引率
25.00%
发文量
70
审稿时长
24 months
期刊介绍: Theoretical Foundations of Chemical Engineering is a comprehensive journal covering all aspects of theoretical and applied research in chemical engineering, including transport phenomena; surface phenomena; processes of mixture separation; theory and methods of chemical reactor design; combined processes and multifunctional reactors; hydromechanic, thermal, diffusion, and chemical processes and apparatus, membrane processes and reactors; biotechnology; dispersed systems; nanotechnologies; process intensification; information modeling and analysis; energy- and resource-saving processes; environmentally clean processes and technologies.
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