Mass-Transfer Control With Microbubbles in Highly Turbulent Decaying Flows

Abstract

We hypothesize that combining extreme turbulence with a minute reduction in surface tension σ (surface tension of the liquid) using surfactant provides a simple and scalable route for controlling micron scale bubble size in gas--liquid systems. To test this, we generate high-intensity turbulence using a multiphase pump [turbulent intensity 40\%; Taylor Reynolds number Reλ=O(103); bulk Reynolds number Re=O(105)] feeding a straight duct, which produces a decaying turbulent flow where, without additives, bubble coalescence dominates and causes monotonic downstream growth in the mean diameter davg of the bubbles. This growth is governed by the turbulent dissipation rate . High-speed imaging, back-lit shadowgraph and particle shadow velocimetry (PSV) quantify bubble statistics (davg, and the bubble-size distribution) and turbulence metrics (turbulent kinetic energy k, turbulence intensity I, and dissipation rate ). We then introduce a minute amount ( 0.01\% critical micelle concentration) of additive that produces a slight reduction in σ, used here only as an interfacial tuning knob because the same change in surface tension can be achieved with non surface active agents. This small decrease in σ enhances breakup, slightly suppresses coalescence, and makes smaller bubbles more breakup prone, resulting in reduced davg and a narrower bubble-size distribution. Turbulence statistics remain unchanged within experimental uncertainty, indicating that the effect arises entirely from interface rather than hydrodynamic changes. Overall, combining extreme turbulence with a minute reduction in surface tension offers a low complexity and tunable lever for setting bubble-size distributions and intensifying mass transfer in industrial multiphase flows.

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