Liquid-phase turbulence measurements in air-water two-phase flows using particle image velocimetry. (June 2020)

• Record Type: Journal Article
• Authors: Shi, Shanbin; Wang, Dewei; Qian, Yalan; Sun, Xiaodong; Liu, Yang; Tentner, Adrian
• Is Part Of: Progress in nuclear energy. Volume 124(2020)
• Publication Date: 2020-06
• Subjects: Two-phase flows -- Circular test section -- Liquid-phase turbulence -- Particle image velocimetry; Nuclear energy -- Periodicals; Nuclear engineering -- Periodicals; 333.7924
• DOI: 10.1016/j.pnucene.2020.103334
• Languages: English
• ISSNs: 0149-1970

Abstract

Abstract: Liquid-phase turbulence plays a vital role in determining various gas-liquid two-phase flow parameters, such as void fraction distribution, bubble morphology, bubble-bubble interactions, and interfacial area concentration. In this study, a two-phase flow database including both the gas- and liquid-phases measurements was developed focusing on three bubbly flow conditions in an air-water two-phase flow loop with a vertical one-inch diameter circular pipe test section. A particle image velocimetry (PIV) system integrating an optical phase separation method, i.e., the planar laser-induced fluorescence (PLIF) technique using fluorescent particles and optical filtration, was applied to measure the liquid-phase turbulence information, including the time-averaged velocity, Reynolds stress, and turbulent kinetic energy for the liquid phase. The PIV measurements were taken at three ports along the test section at 14.5, 51.5, and 88.5 pipe inner diameters downstream of a bubble injector. In addition, a double-sensor conductivity probe was used to measure radial distributions of the local time-averaged void fraction and gas velocity. The measured liquid-phase turbulence was used to benchmark Sato's turbulence model considering the bubble-induced shear stress for the three tested bubbly flows. The benchmark results showed good agreement between the PIV measurements and model predictions. In the two bubbly flows tested that have low void fractions being less than 3%, the effect of the bubble-induced turbulence was found not significant. However, the bubble-induced shear stress becomes important with the increase of the void fraction. Highlights: High resolution liquid-phase data were developed by employing a PIV technique in a vertical air-water two-phase flow loop. Local gas-phase information was measured by a double-sensor conductivity probe. Liquid-phase turbulence structures were analyzed from PIV measurements. Sato's turbulence model was benchmarked against the experimental data.