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reduction in power number caused by gassing, as described above Cooke et al (1988) found some success by substituting (P/V)1/3 for N in the usual expression for turbulent mixing (NtM = constant): This correlated single phase and gassed cases (for subsurface addition) when the total of the gassed impeller shaft power together with the gas buoyancy power was used Recent work (Gao et al, 2000; Zhao et al, 2001) has compared liquid mixing times in ungassed, cold, and hot sparged and boiling conditions It was shown that in an aerated standard tank, the mixing time correlates with the speci c power input (W kg 1 ) and super cial gas velocity (m s 1 ), provided that both the possible changes in the relative power demand of the impeller and the potential energy added by the sparged gas (the saturated volume in hot operation) are taken into consideration. asp.net data matrix reader ASP.NET Data Matrix Barcode Reading Decoder Library | Free VB ...
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