Abstract
AbstractThe hydrodrynamic behavior of a 1.0 × 10−1 m dia. Scheibel column packed with a material preferentially wetted by the dispersed phase has been investigated with and without mass transfer. Drop size and size distribution and dispersed phase holdup were measured as a function of flow rates, agitator speed, packing pad height, and mass transfer direction in a 24 factorial design. Flooding rates were measured and found to be dependent on the impeller position.
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