Sentence examples for mean bubble sizes from inspiring English sources

Results show that contaminants and alcohol addition suppress bubble coalescence and induces a decrease of mean bubble sizes.

The mean bubble sizes D32 of the two are both related to the pressure drop between import and export, gas ratio and liquid flow.

In particular, mean bubble sizes can be predicted from simultaneous measurements of the superficial velocities of gas and liquid and of the gas holdup, respectively.

The mean bubble sizes in the absence of swirl body are smaller than that in the presence of swirl under different operating conditions.

Maximum stable bubble diameters and effective shear rate for break-up calculated at different locations in the mixer using the fundamental capillary number theory for drop and bubble break-up correlated well with the measured local mean bubble sizes and the mean local shear rates calculated using FEM simulations of the flow.

Detailed information of the liquid and gas flow pattern is provided to the zone model by the hydrodynamic model, while the hydrodynamic model gets its required information about local mean bubble sizes and the local mass flux between gas and liquid from the zone model.

The Sauter mean bubble size was found to vary over the range of 1.2 2.9 mm.

The dosage of frother plays vital role as it affects the bubble size distribution and mean bubble size.

Meanwhile, the rise velocity of bubble swarm and the Sauter mean bubble size are evaluated using ERT based on dynamic gas disengagement theory.

Finally, the influence of pressure on the Sauter mean bubble size in a number of pure liquids (mono-ethylene glycol, n-heptane and deionized water) is also studied and correlated with a new empirical equation on the basis of photos in combination with literature results.

With given operating conditions, the overall Sauter means bubble size in the hot systems appears to be about 21% greater than when cold.