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Moreover the growth has to be balanced and sustainable, not based on another bubble.
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Drag forces on departing bubbles were calculated based on bubble movement and used to predict bubble propagation.
Absolute bubble velocity distributions are calculated based on an ideal bubble velocity distribution and rules of bubble-bubble interaction.
Nevertheless, these complementarity constraints may construct trivial phase equilibrium solutions, and a procedure based on embedded bubble and dew points calculations is proposed to avoid them.
Theoretical prediction of flow regime transition in bubble columns was studied based on the bubble size distribution by the population balance model (PBM).
The equation has been developed based on the bubble formation, drag at interface and the wettability effect of the liquid.
A multi-scale finite element method based on the bubble function approach has been developed and applied to this problem.
A model for the non-steady-state description of gas fluidized beds is derived, based on the bubble dispersion model.
The mean CH4 ebullition from Lake Postilampi was estimated to be in the range from 36 to 46 mg m−2 d−1, based on the bubble gas CH4 concentrations measured from the gas collectors and sediment, respectively.
Empirical correlations have been developed to predict the collapse pressure and the active volume of cavitation as a function of different operating parameters based on the bubble dynamics studies.
In seeking quantification of the bubble dispersion, the Eulerian approach based on the bubble number fluxes at different downstream cross-sections of the mixing layer in terms of ensemble trajectory statistics and Lagrangian approach based on the bubble mean square displacement are adopted.
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