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Batch Liquid-Liquid Extraction of Phenol from Aqueous Solutions

โœ Scribed by M. S. A. Palma; C. Shibata; J. L. Paiva; M. Zilli; A. Converti


Publisher
John Wiley and Sons
Year
2010
Tongue
English
Weight
135 KB
Volume
33
Category
Article
ISSN
0930-7516

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โœฆ Synopsis


Abstract

The aim of this work is the study of batch liquidโ€liquid extraction of phenol from aqueous solutions in a benchโ€scale wellโ€mixed reactor. The influence of the ratio of phase volumes, temperature, and rotational speed on phenol removal (0.72โ€“1.1โ€‰% w/w) was investigated using methyl isobutyl ketone as an extracting solvent. For this purpose, the ratio of phase volumes were set at 0.1 and 0.2, the temperature at 10, 20, and 30โ€‰ยฐC, and the rotational speed at 300, 400, and 500 rpm. A physical model based on the material balance of the phases as well as the equation of mass flux between the phases allowed the estimation of the overall coefficient of mass transfer coupled with the superficial area. Moreover, it proved to fit, satisfactorily well, the experimental data of residual phenol concentration in the organic phase versus time under all the conditions investigated.


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Supercritical extraction of organic mixt
โœ Sang-Do Yeo; Aydin Akgerman ๐Ÿ“‚ Article ๐Ÿ“… 1990 ๐Ÿ› American Institute of Chemical Engineers ๐ŸŒ English โš– 362 KB ๐Ÿ‘ 1 views

## Model for Phase Equilibria The equilibrium compositions of both the aqueous and the supercritical fluid (SCF) phase a t known temperature, pressure, and overall composition are carried out by the P-T flash calculation. The mole fraction of component i in the aqueous