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With increasing pressure, the maximum bubble diameter at nucleate sites gradually decreases; the latent heat needed for a unit volume steam has a great effect on bubble growth rate under different system pressure.
Then series of bubble chord lengths at different locations are derived based on the rising velocities of the bubbles, and are compared with a model of maximum bubble diameter.
The maximum bubble diameter is one of the most important factors affecting bubble separation in a hydrocyclone and is essential to the analysis and design of a degassing hydrocyclone.
The model was tested experimentally for a range of column and jet diameters, jet velocities, and liquid physical properties, and it was found that the measured maximum bubble diameter was in good agreement with the model predictions based on a critical Weber number of 1.2.
The Mori and Wen [14] relation is used to obtain the maximum bubble diameter: d bm = 0.65 S U g - U mf 0.4 cm.
Using two pulsed Nd YAG lasers at λ = 1064 nm and ∼10 μJ/pulse, the dynamics of tandem bubble interaction (individual maximum bubble diameter of 50 μm with a corresponding collapse time of 5.7 μs) are examined at different phase delays.
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max: Maximum stable bubble diameter(m).
5 Bubbles grow continuously along the reactor height from their initial diameter until they reach the maximum stable bubble diameter.
The maximum vacuum degree with a geometric criterion K of 4.8, the maximum aeration capability with a K of 8.0, and the minimum bubble diameter with a K of 12 were achieved.
Critical capillary numbers and maximum stable bubble diameters depended much more on extension than shear rate.
Maximum stable bubble diameters were calculated at different locations in the mixer from numerical predictions of the critical capillary number and they were mapped inside the geometry of the mixer for the first time.
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