The phrase "average of bubbles" is correct and usable in written English.
It can be used in contexts related to statistics, data analysis, or discussions about measurements involving bubbles, such as in scientific experiments or product evaluations.
Example: "To determine the quality of the soap solution, we calculated the average of bubbles produced during the test."
Alternatives: "mean of bubbles" or "bubbles' average".
It was detected that the rate average of bubble detachment from the heating surface in salt water (5 g/L) is faster than that of tap water.
We submitted the model to the same experiment as human observers (collapsed across Smith et al [1] and Schyns et al [2] data), using as parameters the average accuracy per expression (n = 17 observers), the average number of bubbles per expression and the total number of trials (25,800) per expression.
While the helium bubble size distribution becomes narrower with increasing dose, the average size of bubbles remains unchanged and the density of bubbles increases somewhat with dose.
By using an image analyzer the cluster size, the average size of bubbles in the clusters and independent bubbles, i.e. those had not aggregated were investigated as a function of dodecane concentration.
Participants who were shown the slide-show popped an average of 120 bubbles compared with 100 for the neutral images and just 80 for the funny picture.
Local gas holdup data were obtained from the values of light absorbance measured by the first probe and the average values of bubble chord length (vertical bubble dimension) were then calculated from respective values of local gas holdup and bubble frequency data determined at given working conditions by the auxiliary probe.
It is observed that the ensemble average flux profiles of bubbles for two-way coupling case are farther skewed towards the high-speed stream of the shear layer in contrast to its one-way coupling case.
Experimental results show that for beds of small particles fluidized under pressure the flow of gas through the emulsion phase is higher than that expected on the basis of existing theories, but it is shown that average rise velocities of bubbles may be obtained from results of bed collapse measurements.
Results indicated that when a flow regime changed from bubbly to either trickling or pulsing flow, the number of average sized bubbles significantly decreased and the shape of the majority of the bubbles was no longer spherical.
The results show that if the average bubble diameter of a group of bubbles is less than about 3.5 mm, the void fraction distribution will peak near the pipe wall for both uniform and non-uniform bubble flows.
