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Effective interfacial area and liquid side mass transfer coefficients in a packed column

โœ Scribed by W.S. Norman


Publisher
Elsevier Science
Year
1974
Tongue
English
Weight
95 KB
Volume
29
Category
Article
ISSN
0009-2509

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๐Ÿ“œ SIMILAR VOLUMES


Effective interfacial area and liquid an
โœ B.N. Sahay; M.M. Sharma ๐Ÿ“‚ Article ๐Ÿ“… 1973 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 587 KB

The theory of gas absorption accompanied by fast pseudo-m th order reaction was used to obtain values of effective interfacial area in a packed column, irrigated with aqueous solutions and provided with 1 in. ceramic Raschig rings, 1 in. P.V.C. Raschig rings, 1 in. ceramic Intalox saddles, 1 in. pol

Effective interfacial area in a packed c
โœ A.S. Jhaveri; M.M. Sharma ๐Ÿ“‚ Article ๐Ÿ“… 1968 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 644 KB

The theory of absorption accompanied by pseudo nth order reaction was used to evaluate values of effective interfacial area, a, as a function of the liquid flow rate in a laboratory packed column. Oxygen was absorbed in aqueous solutions of cuprous chloride and sodium dithionite. Isobutylene was abs

Gas-side mass transfer coefficient in pa
โœ A.D. Vidwans; M.M. Sharma ๐Ÿ“‚ Article ๐Ÿ“… 1967 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 932 KB

The effect of gas flow rate, liquid flow rate and dilfusivity of the solute in the gas-phase on the gas-side mass transfer coefficient was investigated in laboratory packed columns containing + in. (O-95 cm) ceramic Raschig rings. An eight-fold variation in the diffusivity was obtained. It was found