同时测量管道中液固颗粒流动的速度场并分析流动特性

IF 2.8 2区 工程技术 Q2 ENGINEERING, MECHANICAL
Yue Feng , Lingjuan Zhang , Yiming Lei , Jiabin Jia , Weihua Meng , Suna Guo , Lide Fang
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引用次数: 0

摘要

水平管道内的液固颗粒流是一种典型的颗粒负载流。负载颗粒与载相之间的相互作用导致此类流动的动态行为非常复杂。我们研究了一种液固粒子流的动力学特性,即稀释、微浮力、百微米大小的球形粒子完全悬浮在管道内的湍流中,Re 为 7038。本研究考虑了固体体积分数为 0、2.67 × 10-4、5.33 × 10-4、8.00 × 10-4、1.07 × 10-3 和 1.33 × 10-3 的情况。利用实验测量技术,通过光场反馈获取两相流中颗粒在整个流场中的图像。粒子图像测速仪(PIV)和粒子跟踪测速仪(PTV)被用来同时获得液相速度场和粒子轨迹。这种方法可以全面描述各相的速度场。随后,根据宏观速度场、微观涡度场、粒子速度矢量和速度滑移的分布,详细解释和分析了液固粒子流的流动特性。结果发现,随着固体颗粒的加入和体积浓度的增加,固相的阻力效应和在下壁附近的堆积趋势导致液相速度剖面下降和抛物线形状变形。在体积浓度为 1.33 × 10-3 的液固颗粒流中,与单液相流相比,中心区域的速度标准偏差从 0.0097 m/s 增加到 0.0159 m/s,近壁区域的速度标准偏差从 0.0257 m/s 增加到 0.0347 m/s,分别增加了 1.54 倍和 1.26 倍。介质涡的比例从 17% 增加到 30%,几乎翻了一番。这项研究积极探索了液固颗粒流动的同步测量和流动特性。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Simultaneous measurement of velocity field of liquid–solid particle flow in pipelines and analysis of flow characteristics

The liquid–solid particle flow within a horizontal pipeline is a typical particle-laden flow. The interplay between loaded particles and carrier phase engenders significant complexities in the dynamic behavior of such flows. We investigated the dynamics of a liquid–solid particle flow featuring dilute, slightly buoyant, hundred-micron-sized spherical particles fully suspended in the turbulent flow in a pipe, where Re is 7038. Cases with solid volume fractions of 0, 2.67 × 10-4, 5.33 × 10-4, 8.00 × 10-4, 1.07 × 10-3 and 1.33 × 10-3 were considered in this study. Experimental measurement techniques were utilized to acquire images of particles in the two-phase flow across the entire flow field via optical field feedback. Particle image velocimetry (PIV) and particle tracking velocimetry (PTV) were employed to simultaneously obtain liquid-phase velocity fields and particle trajectories. This approach allowed for a comprehensive depiction of the velocity field of each phase. Subsequently, a detailed explanation and analysis of the flow characteristics of the liquid–solid particle flow were provided based on the distribution of macroscopic velocity fields, the microscopic vorticity field, particle velocity vectors, and velocity slip. As a result, it was found that with the addition of solid particles and an increase in volume concentration, the drag effect of the solid phase and the trend of accumulation near the lower wall caused a decrease in the liquid phase velocity profile and deformation of the parabolic shape. In the liquid–solid particle flow with a volume concentration of 1.33 × 10-3, compared to the single-liquid phase flow, the standard deviation of velocity in the central region increased from 0.0097 m/s to 0.0159 m/s, and in the near-wall region, it increased from 0.0257 m/s to 0.0347 m/s, representing increases of 1.54 times and 1.26 times respectively. The proportion of medium vortices increased from 17 % to 30 %, nearly doubling. This study actively explores the concurrent measurement and flow characteristics of liquid–solid particle flow.

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来源期刊
Experimental Thermal and Fluid Science
Experimental Thermal and Fluid Science 工程技术-工程:机械
CiteScore
6.70
自引率
3.10%
发文量
159
审稿时长
34 days
期刊介绍: Experimental Thermal and Fluid Science provides a forum for research emphasizing experimental work that enhances fundamental understanding of heat transfer, thermodynamics, and fluid mechanics. In addition to the principal areas of research, the journal covers research results in related fields, including combined heat and mass transfer, flows with phase transition, micro- and nano-scale systems, multiphase flow, combustion, radiative transfer, porous media, cryogenics, turbulence, and novel experimental techniques.
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