Gas-phase and hqlud-phase mass transfer data published m the literature are corrected for the axial Hurd dlsperslon coefficient values proposed by Wakao et al El1 The corrected Sherwood numbers III the range of Reynolds number from about 3 to 10,000 are correlated by Sh = 2+ I I Sc"'Rc"" Ar Vapor mi
β¦ LIBER β¦
Effect of fluid dispersion coefficients on particle-to-fluid mass transfer coefficients in packed beds: Correlation of sherwood numbers
β Scribed by N. Wakao; T. Funazkri
- Publisher
- Elsevier Science
- Year
- 1978
- Tongue
- English
- Weight
- 829 KB
- Volume
- 33
- Category
- Article
- ISSN
- 0009-2509
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