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Disperse phase volume fraction

Stainless steel flat six-blade turbine. Tank had four baffles. Correlation recommended for ( ) < 0.06 [Ref. 156] a = 6( )/<, where d p is Sauter mean diameter when 33% mass transfer has occurred. dp = particle or drop diameter <3 = iuterfacial tension, N/m ( )= volume fraction dispersed phase a = iuterfacial volume, 1/m and k OiDf implies rigid drops. Negligible drop coalescence. Average absolute deviation—19.71%. Graphical comparison given by Ref. 153. ... [Pg.616]

G. Liquid drops in baffled tank with flat six-blade turbine k ca = 2.621 xlf3 tank/ [E] Use arithmetic concentration difference. Studied for five systems. tfjto = imptfpC/RC> Noh = Rc/(pc imp<7)1/2 (J) = volume fraction dispersed phase. N = impeller speed (revolutions/time). For d nk = htank> average absolute deviation 23.8%. [144] p. 437... [Pg.75]

I. Liquid drops in baffled tank, low volume fraction dispersed phase... [Pg.442]

Since the volume of n drops = nn(average drop diameter) /6, the volume fraction dispersed phase is... [Pg.701]

The probability for phase inversion increases as drops get closer together. For uniform drops, the distance between drops is Sd/d = (Cp/ct))i/3 - 1, where Sd is the separation distance between drops, d the drop diameter, cj) the volume fraction dispersed phase, and Cp a packing parameter (0.7404 for face-centered cubic or hexagonal packing). [Pg.708]

See other pages where Disperse phase volume fraction is mentioned: [Pg.614]    [Pg.616]    [Pg.616]    [Pg.72]    [Pg.440]    [Pg.442]    [Pg.442]    [Pg.326]    [Pg.196]    [Pg.197]    [Pg.758]    [Pg.768]    [Pg.618]    [Pg.620]    [Pg.620]    [Pg.522]   
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Disperse phase

Disperse phase volume

Dispersion fractionation

Dispersive phase

Effect of Disperse Phase Volume Fraction

Foamed emulsions with large volume fraction of the disperse phase

Phase dispersion

Phase fractionation

Phase volume

Volume fraction phases

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