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Effect of fluid dispersion coefficients on particle-to-fluid mass transfer coefficients in packed beds:Correlation of sherwood numbers

Authors
Journal
Chemical Engineering Science
0009-2509
Publisher
Elsevier
Publication Date
Volume
33
Issue
10
Identifiers
DOI: 10.1016/0009-2509(78)85120-3

Abstract

Abstract 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 Sc 1/3 Re 0.6.

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