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Experimental Investigation on void structure velocity and estimation of velocity jump boundaries in a 3X3 rod bundle at low gas flow conditions
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Experimental Investigation on void structure velocity and estimation of velocity jump boundaries in a 3X3 rod bundle at low gas flow conditions

Shao-Wen Chen, Pei-Syuan Ruan, Lung-Hung Huang, Wen-Chen Tsai, Hsiang Lee, Chia-Kuan Chen, Min-Song Lin, Jong-Rong WangJin-Der Lee
The International journal of heat and fluid flow, 卷.110, 頁.109653
12/2024

摘要

Conductivity meters Cross-correlation Rod bundles Transient void fraction Two-phase flow Void structure velocity
•Gas-liquid two-phase flow tests were performed in a rod bundle channel.•Global/local void signals were analyzed with cross-correlation technique.•Void structure velocities were determined, and velocity jumps were observed.•Empirical models were proposed for estimating velocity jump boundaries. Air-water two-phase flow tests were performed in a 3X3 rod bundle channel under low gas-flow conditions. Gas and liquid superficial velocities of < jg> = 0.035–1.0 m/s and < jf> = 0.6–1.7 m/s were tested, which may cover the flow regimes of bubbly to cap-bubbly or slug/churn flows, and global and local void fractions were measured via non-intrusive conductivity void meters at different axial locations. The transient void signals were analyzed with cross-correlation technique to obtain the void structure velocities at various local/global regions, and these velocities were compared with one-dimensional (1D) drift-flux model. Under relatively low gas flow conditions, the void structure velocities were clearly lower than the average gas velocity estimated by 1D drift-flux model. While increasing gas flow rate, the void structure velocities at different regions can jump up and become comparable to the average gas velocities calculated by the 1D drift-flux model (DFM). These velocity jump conditions could be roughly explained by the changes of bubble sizes/shapes and distributions, and the transition boundaries of velocity jumps can be successfully estimated by introducing energy balance between fluid turbulent kinetic energy and bubble surface free energy of various sizes.

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