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Gas Sparging with No Mechanical Agitation

Leaving the vicinity of a sparger, the bubbles may break up or coalesce with others until an equilibrium size distribution is reached. A stable size is achieved when turbulent fluctuations and surface tension forces are in balance (Calderbank, 1959). [Pg.234]

Akita and Yoshida (1974) determined the bubble-size distribution in bubble columns using a photographic technique. The gas was sparged through perforated plates and single orifices, while various liquids were used. The following correlation was proposed for the Sauter-mean diameter  [Pg.234]


Gas Sparging with No Mechanical Agitation In a two-phase system where the continuous phase remains in place, the hold-up is related to superficial gas velocity Vs and bubble rise velocity V, (Sridhar and Potter, 1980) ... [Pg.236]


See other pages where Gas Sparging with No Mechanical Agitation is mentioned: [Pg.234]    [Pg.198]    [Pg.234]    [Pg.198]    [Pg.1814]    [Pg.1574]    [Pg.1818]    [Pg.319]    [Pg.427]    [Pg.152]    [Pg.409]   


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Gas Sparging with Mechanical Agitation

Gas sparging

Mechanical Agitators

Mechanical agitation

Sparge gas

Sparging

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