Sentence examples for mean bubble chord from inspiring English sources
Average bubble chord length, bubble frequency and sauter mean bubble chord length were obtained at various locations of the column by placing the probe at three axial and six radial positions.
Criteria for determining flow regime transitions, developed in air-water two-phase flow based on bubble frequency, Sauter mean bubble chord length and the time taken by a bubble to pass a given point, were successfully applied to gas-liquid-solid three-phase fluidized beds.
It was observed that the elasticity of the operating liquid reduced the average bubble chord length and increased the total gas holdup.
Distributions of air concentration and mean air water velocity, and bubble chord length distributions are presented for inflow velocities ranging from 2 to 8 m/s.
The number density distributions of the individual bubble chord length have been represented by the logarithmic normal distributions, by which the mean chord length of a bubble has been determined.
Bubble chord lengths are overestimated by optical probe signals because small bubbles are not detected.
Bubble chord time measurements showed pseudo-chord sizes of entrained bubbles ranging from less than 0.5 mm to more than 10 mm with an average pseudo-chord size were between 4 and 9 mm.
The bubble chord length and bubble velocity distributions became wider at higher superficial gas velocities and higher optical densities.
Three ideal bubble chord length distributions have been derived for three different bubble shapes (spherical, ellipsoidal and spherical-cap).
In view of the existence of the multiple bubble groups, the transformation from bubble chord length distribution to bubble size distribution is conducted based on the decomposition of the multiple bubble groups in the chord length distribution, and the evolution characteristics of the bubble size distributions at the pipe cross section are investigated as the flow condition changing.
