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The dispersion of bubbles into a down-liquid flow in a vertical pipe is investigated.

The dispersion of bubbles into down-flowing liquids is often encountered in a number of industrial applications involving pipe flow, bubble columns and loop reactors.

The parameters such as initial bubble temperature, bubble injection location, and carrier fluid temperature have been chosen to examine their effects on the condensation and dispersion of bubbles.

Extension rate distributions have been calculated in a twin screw mixer for Newtonian and non-Newtonian fluids because they strongly affect dispersion of bubbles and the maximum stable diameter estimated from calculations of the Capillary number.

The RDM is used to describe turbulent dispersion of bubbles, and is validated here against the experimental data, and compared with predictions obtained by imposing an empirical turbulent dispersion force (TDF), but without introducing adjustable coefficients.

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The single helical disturbance causes the larger dispersion of bubble.

The sedimentation of a homogeneous dispersion of gas bubbles in water is studied, using double optical probe and hot-film anemometry, for high bubble Reynolds number (300 500), and high void fraction α (0 0.3).

In this process the dispersion of gas bubbles in molten salts has played an important role for the efficient mass and heat transfers.

However, CFD showed that a negative lift coefficient is required for simulations in order to reproduce the experimental dispersion of the bubbles curtain: wall and repulsion forces that were not taken into account in the model might play a major role in the expansion of the bubble swarm.

The increase in CO2 gas flow rate, led to a decrease in galvanic corrosion rate especially at high agitation velocity due to a high dispersion of gas bubbles in the solution.

The leading assumption is a separation of the ohmic resistance of the dispersion of gas bubbles in electrolyte between the electrodes into two parts: a stagnant boundary layer at the electrode(s) being enriched in gas and a flowing bulk in the centre region.

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