Abstract
AbstractIn a recently published paper(1), it has been demonstrated that the drag coefficient—Reynolds number relationship for a single spherical solid particle may be applied to multi‐particle systems as well, provided that modified definitions of the drag coefficient and Reynolds number incorporating suitable functions of the particles volume fraction are used.This generalised approach is now extended to include the case of a fluid dispersed phase. This done by incorporating a function of the ratio of the phase viscosities, based on theoretical derivations due to Hadamard—Rybczinski and Taylor in the modified definition of Reynolds number.All available experimental data (88 points from 3 sources, on 12 different liquid‐liquid systems) were recalculated and correlated on this basis.
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have