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A new aerator suitable for microbubble generation by fluidic oscillation has been designed and tested with the view of getting a uniform bubble distribution across the aerator.
The phase distributions for uniform bubble flows were also measured for analysis of the effect of the bubble size on the behaviour of the bubbly flows.
The test results showed that uniform bubble flow was presented after the mixture passes through the buffer tank and no aggregations of big bubbles were observed.
In a system with homogeneous regime, the bubble-size distribution is narrow and a uniform bubble size, generally in the range 1 7 mm, is found.
To explain this dual effect, possible physical mechanisms of the solid phase influence on the uniform bubble bed were discussed.
It is known that uniform bubble domains are observed in thin films with Q =Ku/Kd) \ \gg \) 1, where Ku and Kd are the perpendicular anisotropy and stray field energy densities, respectively26.
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Furthermore, limiting conditions for uniform bubbling can be read off a state diagram of the uniform bubbling regime.
A relation which defines the drag of spherical particles in more or less concentrated suspensions was employed to describe bubble column behaviour in the uniform bubbling regime.
A plot of gas drift flux as a function of gas hold-up reveals the uniform bubbling and churn-turbulent types of behaviour familiar in gas-liquid two-phase flow.
Using propane, butane and air as the dispersed phases and different SDS PEG solutions as the continuous phases, two kinds of bubble generating phenomena, named "single-bubble generation" flow and "dual-bubble generation" flow, were observed in experiment and uniform bubbles with average diameters ranging from 391 μm to 713 μm and polydispersity less than 2.9% were successfully prepared.
Phase distributions were studied experimentally in fully developed laminar bubbly flow with non-uniform bubble sizes.
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CEO of Professional Science Editing for Scientists @ prosciediting.com