Evaluation of anion exchange resin for sorption of selenium (IV) from aqueous solutions

Abstract In this work, selenium (IV) ions were adsorbed from aqueous solutions by the strongly basic anion exchange resin Amberlite IRA-400. The morphology of the resin before and after Se(IV) sorption was investigated using different techniques such as energy dispersive X-ray spectroscopy (EDX), Fo...

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Main Authors: A. El-Tantawy, E. M. Abu Elgoud, S. E. A. Sharaf El-Deen
Format: Article
Language:English
Published: BMC 2025-01-01
Series:BMC Chemistry
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Online Access:https://doi.org/10.1186/s13065-024-01356-3
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author A. El-Tantawy
E. M. Abu Elgoud
S. E. A. Sharaf El-Deen
author_facet A. El-Tantawy
E. M. Abu Elgoud
S. E. A. Sharaf El-Deen
author_sort A. El-Tantawy
collection DOAJ
description Abstract In this work, selenium (IV) ions were adsorbed from aqueous solutions by the strongly basic anion exchange resin Amberlite IRA-400. The morphology of the resin before and after Se(IV) sorption was investigated using different techniques such as energy dispersive X-ray spectroscopy (EDX), Fourier transform infrared spectroscopy (FTIR), and scanning electron microscopy (SEM). To determine the ideal sorption conditions, a batch approach was used to examine the variables affecting Se(IV) sorption performance, including pH, shaking time, adsorbent dosage, initial metal ion concentration, and temperature. The results showed the optimal parameters for the highest percentage of selenium (80.25%) at an initial concentration of 100.0 mg L−1, pH 3.0, the adsorbent dosage of 10.0 mg, and the shaking time of 60.0 min. According to the experimental findings, the sorption process was satisfactorily explained by the pseudo-second-order kinetic model. The maximum adsorption capacity at pH 3.0 was 18.52 mg g−1, and the adsorption rather well followed the Langmuir adsorption isotherm. Moreover, exothermic and spontaneous sorption reaction was the result of thermodynamic properties (negativity of both ΔG° and ΔH°). The adsorption phase's random distribution of the resin-solution interface is indicated by the positive value of ΔSo. Finally, the desorption study was performed using different concentrations of desorbing agents; HNO3, HCl, and sodium acetate. The results illustrated that the effective desorbing agent was 1.0 mol L-1 HNO3, with desorption efficiency reaching about 96.4%. Finally, the Amberlite IRA-400 demonstrated excellent adsorption–desorption behavior over five times, suggesting that the Amberlite IRA-400 could be an effective candidate for the sorption of Se(IV) from several metal ions that occur in fission products.
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spelling doaj-art-147486a100ce4d529ca07849a1258ef92025-01-12T12:06:41ZengBMCBMC Chemistry2661-801X2025-01-0119111110.1186/s13065-024-01356-3Evaluation of anion exchange resin for sorption of selenium (IV) from aqueous solutionsA. El-Tantawy0E. M. Abu Elgoud1S. E. A. Sharaf El-Deen2Nuclear Fuel Technology Department, Hot Laboratories Center, Egyptian Atomic Energy AuthorityNuclear Fuel Chemistry Department, Hot Laboratories Center, Egyptian Atomic Energy AuthorityNuclear Chemistry Department, Hot Laboratories Center, Egyptian Atomic Energy AuthorityAbstract In this work, selenium (IV) ions were adsorbed from aqueous solutions by the strongly basic anion exchange resin Amberlite IRA-400. The morphology of the resin before and after Se(IV) sorption was investigated using different techniques such as energy dispersive X-ray spectroscopy (EDX), Fourier transform infrared spectroscopy (FTIR), and scanning electron microscopy (SEM). To determine the ideal sorption conditions, a batch approach was used to examine the variables affecting Se(IV) sorption performance, including pH, shaking time, adsorbent dosage, initial metal ion concentration, and temperature. The results showed the optimal parameters for the highest percentage of selenium (80.25%) at an initial concentration of 100.0 mg L−1, pH 3.0, the adsorbent dosage of 10.0 mg, and the shaking time of 60.0 min. According to the experimental findings, the sorption process was satisfactorily explained by the pseudo-second-order kinetic model. The maximum adsorption capacity at pH 3.0 was 18.52 mg g−1, and the adsorption rather well followed the Langmuir adsorption isotherm. Moreover, exothermic and spontaneous sorption reaction was the result of thermodynamic properties (negativity of both ΔG° and ΔH°). The adsorption phase's random distribution of the resin-solution interface is indicated by the positive value of ΔSo. Finally, the desorption study was performed using different concentrations of desorbing agents; HNO3, HCl, and sodium acetate. The results illustrated that the effective desorbing agent was 1.0 mol L-1 HNO3, with desorption efficiency reaching about 96.4%. Finally, the Amberlite IRA-400 demonstrated excellent adsorption–desorption behavior over five times, suggesting that the Amberlite IRA-400 could be an effective candidate for the sorption of Se(IV) from several metal ions that occur in fission products.https://doi.org/10.1186/s13065-024-01356-3Amberlite IRA-400 Cl−Se(IV)SorptionIsotherm and kineticsDesorption and regeneration
spellingShingle A. El-Tantawy
E. M. Abu Elgoud
S. E. A. Sharaf El-Deen
Evaluation of anion exchange resin for sorption of selenium (IV) from aqueous solutions
BMC Chemistry
Amberlite IRA-400 Cl−
Se(IV)
Sorption
Isotherm and kinetics
Desorption and regeneration
title Evaluation of anion exchange resin for sorption of selenium (IV) from aqueous solutions
title_full Evaluation of anion exchange resin for sorption of selenium (IV) from aqueous solutions
title_fullStr Evaluation of anion exchange resin for sorption of selenium (IV) from aqueous solutions
title_full_unstemmed Evaluation of anion exchange resin for sorption of selenium (IV) from aqueous solutions
title_short Evaluation of anion exchange resin for sorption of selenium (IV) from aqueous solutions
title_sort evaluation of anion exchange resin for sorption of selenium iv from aqueous solutions
topic Amberlite IRA-400 Cl−
Se(IV)
Sorption
Isotherm and kinetics
Desorption and regeneration
url https://doi.org/10.1186/s13065-024-01356-3
work_keys_str_mv AT aeltantawy evaluationofanionexchangeresinforsorptionofseleniumivfromaqueoussolutions
AT emabuelgoud evaluationofanionexchangeresinforsorptionofseleniumivfromaqueoussolutions
AT seasharafeldeen evaluationofanionexchangeresinforsorptionofseleniumivfromaqueoussolutions