Sentence examples for mean bubble diameters from inspiring English sources

Results are presented in the form of spatial distribution maps of Sauter mean bubble diameters and histograms of spherical bubble diameters.

For the n-alcohols (C1-C8), surfacec surfareasreas were calculated from experimental mean bubble diameters (Sauter diameters) and measured gas hold-up and compared to volumetric mass transfer coefficients from literature.

Estimates have been made using data from an instrumented pilot-scale bubble column of the volume fraction correction term over a range of local volume fractions (0.03 0.38) and mean bubble diameters (4 10 mm) for Bubble Size Distributions (BSDs) of varying 'broadness'broadness

Dynamic gas disengagement technique is utilized to measure bubble rise velocity and sauter mean bubble diameter.

Empirical correlations are also proposed to predict the Sauter mean bubble diameter.

The results show that the mean bubble diameter increases slightly with increasing superficial gas velocity.

As the mean bubble diameter becomes almost constant, the interfacial area increases slightly with superficial velocity.

The profile of the mean bubble diameter in the column and its variation with the superficial gas velocity is studied.

Methodology for analyzing raw data and obtaining bubble size distribution (i.e. Sauter mean bubble diameter) is described.

It was found that a constant superficial velocity, the Sauter mean bubble diameter decreases with increasing pressure and temperature.

The bubble size distribution and gas holdup were measured in the downflow diffuser to obtain correlations for the gas holdup and the Sauter mean bubble diameter.