Solid-liquid extraction of uranium from industrial phosphoric acid using macroporous cation exchange resins: MTC1600H, MTS9500, and MTS9570

The main objective of this research work is the application of a series of Purolite commercial resins: sulfonic cationic exchanger (MTC1600H), amino phosphonic-chelating resin (MTS9500), and phosphonic/sulfonic chelating reins (MTS9570) for uranium adsorption from crude dihydrate phosphoric acid. Th...

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Published inSeparation science and technology Vol. 56; no. 9; pp. 1562 - 1578
Main Author Taha, Mohamed H.
Format Journal Article
LanguageEnglish
Published Abingdon Taylor & Francis 13.06.2021
Taylor & Francis Ltd
Subjects
Cation exchange
cation exchange resins
Cation exchanging
Cationic polymerization
Cations
Chelating resins
Chelation
industrial phosphoric acid
Phosphoric acid
Resins
Shaking
Solid-liquid
Solvent extraction
Sorbents
Sorption
Uranium
Online AccessGet full text
ISSN0149-6395
1520-5754
DOI10.1080/01496395.2020.1787446

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Abstract The main objective of this research work is the application of a series of Purolite commercial resins: sulfonic cationic exchanger (MTC1600H), amino phosphonic-chelating resin (MTS9500), and phosphonic/sulfonic chelating reins (MTS9570) for uranium adsorption from crude dihydrate phosphoric acid. The impact of various parameters on the sorption efficiency such as shaking time, sorbent dose, phosphoric acid concentration, and reaction temperature has been investigated. The obtained data showed that the chelating resins MTS9500 and MTS9570 exhibit higher sorption efficiency than the cationic exchange resin MTC1600H. Kinetic, isotherms, and thermodynamics analysis for the obtained data has been performed.
AbstractList The main objective of this research work is the application of a series of Purolite commercial resins: sulfonic cationic exchanger (MTC1600H), amino phosphonic-chelating resin (MTS9500), and phosphonic/sulfonic chelating reins (MTS9570) for uranium adsorption from crude dihydrate phosphoric acid. The impact of various parameters on the sorption efficiency such as shaking time, sorbent dose, phosphoric acid concentration, and reaction temperature has been investigated. The obtained data showed that the chelating resins MTS9500 and MTS9570 exhibit higher sorption efficiency than the cationic exchange resin MTC1600H. Kinetic, isotherms, and thermodynamics analysis for the obtained data has been performed.
Author Taha, Mohamed H.
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SubjectTerms Cation exchange
cation exchange resins
Cation exchanging
Cationic polymerization
Cations
Chelating resins
Chelation
industrial phosphoric acid
Phosphoric acid
Resins
Shaking
Solid-liquid
Solvent extraction
Sorbents
Sorption
Uranium
Title Solid-liquid extraction of uranium from industrial phosphoric acid using macroporous cation exchange resins: MTC1600H, MTS9500, and MTS9570
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