Modeling of the Solvent Extraction Equilibrium of Uranium (VI) Sulfate with Alamine 336

The present study investigated the solvent extraction of uranium from sulfate acid solutions using Alamine 336 as an extractant dissolved in commercial kerosene Exxsol D-100 and 5% v/v of tridecanol as a modifying agent at room temperature (25±2) ºC and an aqueous/organic volumetric ratio of unity....

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Main Authors: Avelar, Erica, Alvarenga, C.L.G., Resende, G.P.S., Morais, C.A., Mansur, M.B.
Format: Journal Article
Language:English
Published: Brazilian Society of Chemical Engineering 2017
Online Access:http://hdl.handle.net/20.500.11937/81360
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author Avelar, Erica
Alvarenga, C.L.G.
Resende, G.P.S.
Morais, C.A.
Mansur, M.B.
author_facet Avelar, Erica
Alvarenga, C.L.G.
Resende, G.P.S.
Morais, C.A.
Mansur, M.B.
author_sort Avelar, Erica
building Curtin Institutional Repository
collection Online Access
description The present study investigated the solvent extraction of uranium from sulfate acid solutions using Alamine 336 as an extractant dissolved in commercial kerosene Exxsol D-100 and 5% v/v of tridecanol as a modifying agent at room temperature (25±2) ºC and an aqueous/organic volumetric ratio of unity. Experiments were carried out at typical concentration levels like those used at the uranium plant of INB (Indústrias Nucleares do Brasil), Brazil. Data fitting using the slope analysis method revealed that uranium is extracted by Alamine 336 as UO2SO4 and UO2(SO4)2 2- species, forming (R3NH+)2UO2(SO4)2 2- in the organic phase; the extraction of the species UO2(SO4)3 4- seems improbable for the operating conditions investigated. The extraction of uranium is significantly reduced when the concentrations of sulfate and chloride ions in the aqueous phase are increased.
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institution Curtin University Malaysia
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publishDate 2017
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spelling curtin-20.500.11937-813602021-01-07T07:46:47Z Modeling of the Solvent Extraction Equilibrium of Uranium (VI) Sulfate with Alamine 336 Avelar, Erica Alvarenga, C.L.G. Resende, G.P.S. Morais, C.A. Mansur, M.B. The present study investigated the solvent extraction of uranium from sulfate acid solutions using Alamine 336 as an extractant dissolved in commercial kerosene Exxsol D-100 and 5% v/v of tridecanol as a modifying agent at room temperature (25±2) ºC and an aqueous/organic volumetric ratio of unity. Experiments were carried out at typical concentration levels like those used at the uranium plant of INB (Indústrias Nucleares do Brasil), Brazil. Data fitting using the slope analysis method revealed that uranium is extracted by Alamine 336 as UO2SO4 and UO2(SO4)2 2- species, forming (R3NH+)2UO2(SO4)2 2- in the organic phase; the extraction of the species UO2(SO4)3 4- seems improbable for the operating conditions investigated. The extraction of uranium is significantly reduced when the concentrations of sulfate and chloride ions in the aqueous phase are increased. 2017 Journal Article http://hdl.handle.net/20.500.11937/81360 10.1590/0104-6632.20170341s20150301 English http://creativecommons.org/licenses/by/4.0/ Brazilian Society of Chemical Engineering fulltext
spellingShingle Avelar, Erica
Alvarenga, C.L.G.
Resende, G.P.S.
Morais, C.A.
Mansur, M.B.
Modeling of the Solvent Extraction Equilibrium of Uranium (VI) Sulfate with Alamine 336
title Modeling of the Solvent Extraction Equilibrium of Uranium (VI) Sulfate with Alamine 336
title_full Modeling of the Solvent Extraction Equilibrium of Uranium (VI) Sulfate with Alamine 336
title_fullStr Modeling of the Solvent Extraction Equilibrium of Uranium (VI) Sulfate with Alamine 336
title_full_unstemmed Modeling of the Solvent Extraction Equilibrium of Uranium (VI) Sulfate with Alamine 336
title_short Modeling of the Solvent Extraction Equilibrium of Uranium (VI) Sulfate with Alamine 336
title_sort modeling of the solvent extraction equilibrium of uranium (vi) sulfate with alamine 336
url http://hdl.handle.net/20.500.11937/81360