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Investigation of Packing Effect on Mass Transfer Coefficient in a Single Drop Liquid Extraction Column

Zoha Azizi, +2 more
- Vol. 7, Iss: 4, pp 3-11
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TLDR
In this paper, a high interfacial tension chemical system of toluene-acetic acid-water in a structured packed column is investigated and the results showed that random and structured packing are effective only for a drop size less than 9 mm, while the structured ones are shown to have a positive effect on mass transfer coefficient in a wide drop size range.
Abstract
Mass transfer coefficients of rising drops in spray and packed columns with random and structured packing in a liquid-liquid extraction operation were experimentally measured and the results compared. In this work, a high interfacial tension chemical system of toluene-acetic acid-water in a structured packed column is investigated. Results of random and structured packing show that random types are effective only for a drop size less than 9 mm, while the structured ones are shown to have a positive effect on mass transfer coefficient in a wide drop size range. Furthermore, structured packing proved to be slightly more effective than random packing in improving the mass transfer coefficient. The effect of drop size on mass transfer coefficient has also been studied in this work and the results showed that when the drop diameter increases, the mass transfer coefficient increases too. Finally, new correlations for the prediction of the mass transfer coefficient in both a random and structured packed column have been introduced which are in better agreement with the experimental data in comparison with those resulted from Newman, Kronig-Brink and Handlos-Baron models.

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Citations
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A state-of-the-art review on single drop study in liquid-liquid extraction: Experiments and simulations

TL;DR: In this paper, a comprehensive survey of available experimental techniques and numerical approaches for single drop rising and falling were given, and the experimental and numerical investigations of single drop in liquid/liquid extraction system have been reviewed with particular focus on experimental techniques, and computational fluid dynamic simulation approaches.
Journal ArticleDOI

Experimental Investigation and CFD Modeling of Hydrodynamic Parameters in a Pulsed Packed Column

TL;DR: In this paper, a combination of computational fluid dynamics (CFD) and droplet population-balance model (DPBM) was applied to simulate the drop-size distributions and flow fields in a pilot-plant liquid-liquid extraction pulsed packed column.
Journal ArticleDOI

Mathematical modeling of high-pressure oil-splitting reactor using a reduced population balance model

TL;DR: In this paper, a reduced non-equilibrium bivariate population balance model is developed to model simultaneous reversible chemical reaction and extraction of an industrial scale high-pressure oil-splitting reactor with a first-order reversible kinetics.
Journal ArticleDOI

Effective diffusivity in a structured packed column: Experimental and Sherwood number correlating study

TL;DR: In this article, a new correlation for dispersed phase Sherwood number based on molecular diffusivity was established, and the correlation was re-established based on effective diffusivities, which can estimate the experimental drop Sherwood numbers with high accuracy (error of less than 5%).
Journal ArticleDOI

Coupling Solvent Extraction Units to Cyclic Adsorption Units

TL;DR: In this article, the possibility of regenerating the solvent of extraction units by cyclic adsorption was analyzed, and the proposed regeneration scheme has not been considered before in the open literature.
References
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Journal ArticleDOI

Mass and heat transfer from drops in liquid‐liquid extraction

TL;DR: In this article, a simple correlation for the over-all mass transfer coefficient is presented, which holds with a probable error of 20% for both directions of transfer with either phase dispersed, and is useful for the extrapolation of performance from system to system in a given piece of equipment.
Journal ArticleDOI

Correlations for Prediction of Mass Transfer Coefficients in Single Drop Systems and Liquid–Liquid Extraction Columns

TL;DR: In this paper, empirical correlations for the prediction of mass transfer coefficients for single drops are presented, and the average absolute value of the relative error in the predicted values of overall dispersed-phase mass transfer coefficient from the experimental points by using the correlations for individual masstransfer coefficients is 24.5%.
Journal ArticleDOI

Circulation in liquid drops: (A heat-transfer study)

TL;DR: In this article, it was shown that circulation within a liquid drop results in an effective mass or thermal diffusivity of 2·25 times the molecular value, which is in general agreement with much reported work and with the mathematical model of K ronig and B rink which applies to liquid drops undergoing internal circulation.
Journal ArticleDOI

Mass transfer from large oscillating drops

TL;DR: In this paper, a mass transfer model for vigorously oscillating single liquid drops moving in a liquid field has been developed with the concepts of interfacial stretch and internal droplet mixing, taking into account both amplitude and frequency of drop oscillations.
Journal ArticleDOI

Effect of packing on drop swarms extraction of high viscosity solvents

TL;DR: In this paper, the effect of viscosity on drop behavior in a column packed with super mini ring (SMR) packing has been investigated, and it is clear from the results that Kod decreases sharply with the increase of viscoities, whereas drop size only has a little effect on Kod.
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