Experimental research and numerical simulation on gas-liquid two-phase flow of bubble velocity distribution in aeration tank

被引：0
|
作者：
Wand M. [1 ,2 ]
Sun N. [3 ]
Wang Y. [1 ]
Cheng W. [1 ]
机构：
[1] State Key Laboratory Base of Eco-Hydraulic Engineering in Arid Area, Xi'an University of Technology, Xi'an
[2] Shanxi Institute of Water Conservancy Construction and Development, Taiyuan
[3] Shanxi Institute of Water Conservancy and Hydroelectric Power Research, Taiyuan
来源：
| 1600年 / International Research and Training Center on Erosion and Sedimentation and China Water and Power Press卷 / 47期
关键词：
Bubble population balance model; Gas-liquid two-phase flow; Particle image velocimetry; Velocity distribution;
D O I：
10.13243/j.cnki.slxb.20160530
中图分类号：
学科分类号：
摘要：
The gas-liquid two-phase flow widely exists all over the industry sectors, such as hydraulic and wastewater treatment projects. The flow patterns and velocity field distributions can directly affect the operation devices performance, which are studied in this article employing the numerical simulation along with experimental research. A PIV experimental study of gas-liquid two-phase flow has been carried on a cylindrical experimental device, and the gas velocity vector fields are obtained accurately by image processing and particle image velocimetry technology. After considering the situations of turbulence and interphase forces, by using the Euler-Euler two-fluid model and bubble population balance model (BPBM), numerical simulations of two-phase flow are performed and compared with experiment results, the error of mathematical models is about 10%. The research result shows that the proposed model and calculation method can achieve accurate result of flowing regularity and velocity distributions in gas-liquid two-phase flow. © 2016, China Water Power Press. All right reserved.
引用
收藏
页码：1322 / 1331
页数：9
相关论文
共 6 条
  • [1] Fukagata K., Kasagi N., Ua-Arayaporn P., Et al., Numerical simulation of gas-liquid two-phase flow and convective heat transfer in a micro tube, International Journal of Heat & Fluid Flow, 28, 1, pp. 72-82, (2007)
  • [2] Xiong R., Chung J.N., An experimental study of the size effect on adiabatic gas-liquid two-phase flow patterns and void fraction in micro channels, Physics of Fluids, 19, 3, pp. 1139-1158, (2007)
  • [3] Besbes S., Hajem M.E., Aissia H.B., Et al., PIV measurements and Eulerian-Lagrangian simulations of the unsteady gas-liquid flow in a needle sparger rectangular bubble column, Chemical Engineering Science, 126, pp. 560-572, (2015)
  • [4] Amadori D., Corli A., Solutions for a hyperbolic model of multi-phase flow, ESAIM Proceedings, 40, pp. 1-15, (2013)
  • [5] Chaudhri A., Bell J.B., Garcia A.L., Et al., Modeling multi-phase flow using fluctuating hydrodynamics, Physical Review E, 90, 3, pp. 185-198, (2014)
  • [6] Tan C., Dong F., Wu M., Identification of gas/liquid two-phase flow regime through ERT-based measurement and feature extraction, Flow Measurement & Instrumentation, 18, 5, pp. 255-261, (2007)
1