SEMI-THEORETICAL PREDICTION OF VOLUMETRIC MASS TRANSFER COEFFICIENTS IN BUBBLE COLUMNS WITH ORGANIC LIQUIDS AT AMBIENT AND ELEVATED TEMPERATURES

Nedeltchev, S; Jordan, U; Schumpe, A

HERO ID

1119784

Reference Type

Journal Article

Year

2010

HERO ID 1119784
In Press No
Year 2010
Title SEMI-THEORETICAL PREDICTION OF VOLUMETRIC MASS TRANSFER COEFFICIENTS IN BUBBLE COLUMNS WITH ORGANIC LIQUIDS AT AMBIENT AND ELEVATED TEMPERATURES
Authors Nedeltchev, S; Jordan, U; Schumpe, A
Journal Canadian Journal of Chemical Engineering
Volume 88
Issue 4
Page Numbers 523-532
Abstract A semi-theoretical approach for predicting k(L)a values (referred to liquid volume) in 18 organic liquids [acetone, aniline, 1-butanol, benzene, cyclohexane, decalin, 1,2-dichloroethane, 1,4-dioxane, ethanol (96%), ethylacetate, ethylbenzene, ligroin, methanol, nitrobenzene, 2-propanol, tetralin, toluene, and xylene] at various operating conditions (including elevated temperatures and pressures) was developed. It was found that the approach is applicable regardless of the hydrodynamic regime (at u(G) <= 0.1 m/s). Temperatures up to 353 K and pressures up to 0.5 MPa were tested. Two different distributors (multiple-hole and single-hole type) were employed. The liquid-phase mass transfer coefficient k(L) was calculated theoretically from the penetration theory on the basis of original definition of gas-liquid contact time. The interfacial area a was defined with respect to the liquid volume. It was found that their product k(L)a must be multiplied by some correction factor in order to take account of the non-spherical (ellipsoidal) shape of the bubbles. When the correction term is correlated to both the Eotvos number (Eo) and the dimensionless temperature ratio, 198 experimental k(L)a values can be fitted reasonably well (average relative error 9.3%).
Doi 10.1002/cjce.20309
Wosid WOS:000280447200007
Url <Go to ISI>://WOS:000280447200007
Is Certified Translation No
Dupe Override No
Comments Source: Web of Science 000280447200007
Is Public Yes
Keyword bubble column; mass transfer; correction factor; bubble shape; temperature effect
Is Qa No