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Implementation of BPBE leads to better agreement with data, especially in the churn-turbulent flow regime, compared to the simulation based on an estimated constant mean bubble diameter.
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It was found that a constant superficial velocity, the Sauter mean bubble diameter decreases with increasing pressure and temperature.
As the mean bubble diameter becomes almost constant, the interfacial area increases slightly with superficial velocity.
Statistical bubble parameters (bubble frequency, mean bubble rise velocity, mean pierced bubble length and mean bubble volume fraction) were evaluated.
Dynamic gas disengagement technique is utilized to measure bubble rise velocity and sauter mean bubble diameter.
Capacitance probe analysis was used to determine the mean bubble rise velocity, the mean bubble frequency, the mean pierced bubble length, the mean bubble volume fraction and the mean visible bubble flow rate.
The parameters compared were the mean bubble volume fraction, and the nondimensional forms of the mean bubble frequency, the mean pierced length of bubbles, the mean bubble rise velocity, and the local mean visible bubble flow rate per unit area.
The mean bubble rise velocity, the bubble frequency, the mean pierced length, the bubble volume fraction, and the visible bubble flow rate were measured using capacitance probes.
They do a mean bubble.
with constant mean power.
The dosage of frother plays vital role as it affects the bubble size distribution and mean bubble size.
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