Abstract:The coalescence of two growing bubbles presents unique characteristics compared to static bubble coalescence. The gas injection flowrate significantly affects the different stages of bubble evolution, which is poorly understood. In this study, we investigate the flowrate effects on the lateral coalescence of two growing bubbles experimentally. The synchronous bubbling from adjacent needles is achieved using water to push air. During the bubble growth process, we find that the initial nonlinear evolution of bub… Show more
“…As a result, the unbalanced surface tension at the neck propels, while the inertia hinders the neck expansion process. Moreover, continuous air injection exerts a significant impact on neck evolution …”
Section: Resultsmentioning
confidence: 99%
“…As for the theoretical expression for the neck radius, we proposed eq which includes air injection effects previously . The air-injection-induced pressure difference at the neck is modeled as a multiplier (α) of the Laplace pressure at the neck.…”
Section: Resultsmentioning
confidence: 99%
“…Moreover, continuous air injection exerts a significant impact on neck evolution. 17 Figure 8a depicts the temporal evolution of the gas−liquid interface during neck expansion (D = 1.05 mm, S = 2.10 mm, and Q = 20 mL•min −1 ). The overall bubble size and shape remain consistent as the neck expands outwardly.…”
Section: Neck Expansion Characteristicsmentioning
confidence: 99%
“…14−16 Experimental images illustrate that r n increases over time following the bubble merging until it reaches the value equal to the bubble size at contact. 12,17 As for the theoretical description of the neck radius, the power-law scaling is introduced for the self-similar universal solutions. 3,11,18 Paulsen et al 19 found that neck expansion is always dominated by the gas viscosity during asymptotically early times.…”
Section: Introductionmentioning
confidence: 99%
“…In the presence of gas injection during bubble coalescence, our previous study has demonstrated that continuous air injection significantly promotes neck expansion. 17 Nevertheless, the neck evolution with air injection under other needle configurations and air injection flow rates has not been thoroughly investigated. Moreover, a universal description of neck evolution is still lacking.…”
This study investigates the coalescence of two equal-sized bubbles with air injection in distilled water experimentally, numerically, and theoretically. The neck expansion is the most prominent characteristic within a few milliseconds after bubbles coalesce. The effects of needle configurations and air injection flow rates are mainly discussed. Air injection during bubble coalescence is identified as an additional driving force for neck expansion in addition to the capillary pressure. The neck expansion time increases linearly with the bubble size at contact while decreasing with the air injection flow rate. The dimensionless neck expansion time follows a consistent linear decrease with the air injection speed. A novel theoretical expression for the dimensionless neck radius is derived, by quantifying the air injection effects as a multiplier (α) of the Laplace pressure at the neck. α demonstrates a consistent linear increase in air injection speed at all the needle configurations and flow rates. Moreover, numerical results of velocity vectors reveal the mechanism of air injection promoting neck expansion.
“…As a result, the unbalanced surface tension at the neck propels, while the inertia hinders the neck expansion process. Moreover, continuous air injection exerts a significant impact on neck evolution …”
Section: Resultsmentioning
confidence: 99%
“…As for the theoretical expression for the neck radius, we proposed eq which includes air injection effects previously . The air-injection-induced pressure difference at the neck is modeled as a multiplier (α) of the Laplace pressure at the neck.…”
Section: Resultsmentioning
confidence: 99%
“…Moreover, continuous air injection exerts a significant impact on neck evolution. 17 Figure 8a depicts the temporal evolution of the gas−liquid interface during neck expansion (D = 1.05 mm, S = 2.10 mm, and Q = 20 mL•min −1 ). The overall bubble size and shape remain consistent as the neck expands outwardly.…”
Section: Neck Expansion Characteristicsmentioning
confidence: 99%
“…14−16 Experimental images illustrate that r n increases over time following the bubble merging until it reaches the value equal to the bubble size at contact. 12,17 As for the theoretical description of the neck radius, the power-law scaling is introduced for the self-similar universal solutions. 3,11,18 Paulsen et al 19 found that neck expansion is always dominated by the gas viscosity during asymptotically early times.…”
Section: Introductionmentioning
confidence: 99%
“…In the presence of gas injection during bubble coalescence, our previous study has demonstrated that continuous air injection significantly promotes neck expansion. 17 Nevertheless, the neck evolution with air injection under other needle configurations and air injection flow rates has not been thoroughly investigated. Moreover, a universal description of neck evolution is still lacking.…”
This study investigates the coalescence of two equal-sized bubbles with air injection in distilled water experimentally, numerically, and theoretically. The neck expansion is the most prominent characteristic within a few milliseconds after bubbles coalesce. The effects of needle configurations and air injection flow rates are mainly discussed. Air injection during bubble coalescence is identified as an additional driving force for neck expansion in addition to the capillary pressure. The neck expansion time increases linearly with the bubble size at contact while decreasing with the air injection flow rate. The dimensionless neck expansion time follows a consistent linear decrease with the air injection speed. A novel theoretical expression for the dimensionless neck radius is derived, by quantifying the air injection effects as a multiplier (α) of the Laplace pressure at the neck. α demonstrates a consistent linear increase in air injection speed at all the needle configurations and flow rates. Moreover, numerical results of velocity vectors reveal the mechanism of air injection promoting neck expansion.
In order to obtain the laws of the bubble's dynamic behaviours, the interFoam solver in OpenFOAM was used to simulate the bubbles, and the experimental device was built to prove the reliability of the results. The Eötvös number (Eo) and the Galileo number (Ga) were used to classify the bubbles into four regions according to their different dynamic behaviours: straight line without deformation region, slight zigzag without deformation region, zigzag with slight deformation region, and zigzag with strong deformation region. Eo of bubbles in the straight line without deformation region is extremely small and is greatly influenced by surface tension. The bubbles do not deform and rise linearly along the axis of symmetry. Eo of bubbles in the slight zigzag without deformation region is still small and the bubbles do not deform, but the path is curved for a period of time. As the value of Eo increases, the bubble in the zigzag with the slight deformation region is weakened. The path is a regular zigzag, and the axisymmetric structure of the bubbles is destroyed. In the zigzag with the strong deformation region, the values of Eo and Ga are large. The path amplitude increases and the periodic law is broken. The bubble's deformation and vortex shedding interact with each other, both of which are the causes of the bubble's path instability.
In the present paper, the hydrodynamic interactions between bubbles and the gas supply system to a needle were experimentally investigated. In experimental investigations in one of the needles, the air volume flow rate was constant, and in the neighbouring needle, it was changed. In the paper, the methods of data analysis: wavelet decomposition, and FFT were used. It was shown that the hydrodynamic interaction becomes stronger with the increase in air volume flow rate supply to the needle. The occurrence of hydrodynamic interaction modifies bubble growth time slightly, but it significantly modifies the bubble waiting time. In the case when the liquid penetration into the needle is repeatable, then the percentage disturbances in bubble growth time and bubble waiting time are close to each other. Moreover, it can be concluded that synchronized or alternative bubble departures from twin neighbouring needles (occurring due to hydrodynamic interaction) are possible by modifying the bubble waiting time. The modification of hydrodynamic interaction between bubbles, the bubbles themselves, and gas supply systems can be used to control the bubble departure process.
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