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Journal ArticleDOI

Spray and packed liquid–liquid extraction columns: drop size and dispersed phase mass transfer

TLDR
In this paper, the effects of holdup on Sauter mean drop diameter, D32, and dispersed phase mass transfer coefficient have been studied in the spray and packed extraction columns.
Abstract
The effects of holdup on Sauter mean drop diameter, D32, and dispersed phase mass transfer coefficient have been studied in the spray and packed extraction columns. For both columns, two well-defined regions for the dependence of D32 on holdup were observed. D32 increased and decreased with an increase in holdup at low and high levels of holdup, respectively. Changes in dispersed phase mass transfer coefficient against holdup were shown to be similar to D32 for both columns. Moreover, empirical correlations have been derived to predict D32 and dispersed phase mass transfer coefficient for both columns. It has been shown that the derived correlations are in a good agreement with the experimental data. © 2013 Curtin University of Technology and John Wiley & Sons, Ltd.

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Extraction of nitrobenzene from aqueous solution in impinging stream-rotating packed bed

TL;DR: A liquid-liquid extraction of nitrobenzene (NB) in impinging stream-rotating packed bed (IS-RPB) was proposed using cyclohexane as an extractant, presented for its improvement of micromixing and mass transfer performance.
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Separation of sulfur-containing compounds from diesel by oxidation followed by solvent extraction in a single drop column

TL;DR: In this paper, a single drop column for the extraction of oxidized sulfur-containing compounds of diesel as a real fuel has been investigated using extraction in a single-drop column.
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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.
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Packing effect on mass transfer and hydrodynamics of rising toluene drops in stagnant liquid

TL;DR: In this paper, the effects of packing height on terminal velocity and mass transfer of rising drops in a stagnant liquid were experimentally measured, and it was shown that a 30% increase in Sherwood number could be achieved using a packing with 40 cm in height, while simultaneously increasing packing height and flow rate consistently enhanced the mass transfer coefficient.

Biphasic Cellulose Acetate/Rtil Membranes And Functionalized Graphene Adsorbents For Natural Gas Processing: Experimental And Molecular Simulation Studies

Amir Khakpay
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References
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Journal ArticleDOI

Experimental study of drop size distributions at high phase ratio in liquid–liquid dispersions

TL;DR: In this paper, an experimental investigation has been carried out in order to analyse the drop size distributions of a liquid-liquid dispersion in a stirred vessel at high phase ratio, and the results showed that the energy dissipation cannot be considered as uniformly distributed in the mixer.
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Transient rise velocity and mass transfer of a single drop with interfacial instabilities - : experimental investigations

TL;DR: An experimental study of transient drop rise velocities and mass transfer rates was carried out in the system toluene/acetone/water which is known to show interfacial instabilities as mentioned in this paper.
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Hydrodynamics and mass transfer in spray and packed liquid-liquid extraction columns

TL;DR: In this paper, a garnissage de 10,2 cm de diameters was presented, a garnisse with different garnissages (metallique or ceramiques).
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Drop size and continuous‐phase mass transfer in agitated vessels

TL;DR: In this article, the authors developed a realistic mechanism involving periodically varying rates of surface renewal associated with droplet circulation through varying degrees of turbulence around the vessel and obtained relationships for optimized design and scale-up.
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Conjugate heat transfer in an enclosure under the condition of internal mass transfer and in the presence of the local heat source

TL;DR: In this article, the effects of Grashof number (Gr), buoyancy ratio (Br), and transient factor on flow modes, heat and mass transfer were investigated in a two-dimensional and laminar natural convection in a cavity with heat-conducting walls.
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