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The maximum stable drop diameter ds derived from the model, shows a dependence of NWe−0.6.
A viscous silicone oil was dispersed in the jet and the measured maximum stable drop size was compared with predictions based on the maximum energy dissipation rates.
The maximum stable drop sizes, dmax, formed in turbulent stirred dispersions were found to increase significantly on addition of a drag-reducing agent (DRA) to the continuous phase.
It is only when the drop nears the value of the maximum stable drop diameter that it breaks into equal parts.
The sampling and measurement procedure was found to be highly reproducible with a standard deviation for the maximum stable drop size for independent experiments of approximately 10%.
Equations traditionally used to calculate the rate of micromixing and the maximum stable drop size in a dispersion take no account of intermittency.
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Models have been successfully exploited in determining the correlationship between agitation and fermentation process, such as maximum stable (equilibrium) drop size in intermittent turbulence [ 8, 9], hydrodynamic stress [ 10], eddy length [ 11], and energy dissipation [ 12].
In the present work, in order to calculate the maximum stable size of drops and bubbles, the A factor of break-up, Ay (Ay=ωa/U), that is the ratio of the break-up rate in developed turbulent flow to the mean velocity of the flow has been introduced and the effect of the pipe roughness on this factor has also been given.
Theoretical evidence is also presented that a long period of time is required to reach the true steady state in pipe flow and thus to estimate directly from measurements the maximum stable drop/bubble size, dmax.
max: Maximum stable bubble diameter(m).
Section 3 investigates the maximum stable HP throughput.
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