An exponential scaling law based on Power, Froude, and Richardson numbers unifies mixing time data from simulations varying Reynolds and Richardson numbers in stirred tanks.
Characterization of the Gas Dispersion Behavior of Multiple Impeller Stages by Flow Regime Analysis and
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Mixing of miscible liquids: Dimensionless scaling for intermediate-to-large density differences in a stirred tank
An exponential scaling law based on Power, Froude, and Richardson numbers unifies mixing time data from simulations varying Reynolds and Richardson numbers in stirred tanks.