Effect of fluid dispersion coefficients on particle-to-fluid mass transfer coefficients in packed beds

Gas-phase and liquid-phase mass transfer data published in the literature are corrected for the axial fluid dispersion coefficient values proposed by W The corrected Sherwood numbers in the range of Reynolds number from about 3 to 10,000 are correlated by Sh = 2 + 1.1 Sc1/3Re0.6.