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Influence of ionic liquid (R 4 PSCN) for selective separation and recovery of copper from spent Cu - Cr catalyst leach liquor

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dc.contributor.author Behera, SS
dc.contributor.author Parhi, PK
dc.date.accessioned 2024-07-25T04:17:11Z
dc.date.available 2024-07-25T04:17:11Z
dc.date.issued 2024
dc.identifier.citation Hydrometallurgy, 228, 2024; 106352
dc.identifier.issn 0304-386X
dc.identifier.uri http://ore.immt.res.in/handle/2018/3529
dc.description Department of Science and Technology (DST) Govt. of Odisha, India; Fakir Mohan University [ST-SCST-MISC-0026-2020, 4856/ST]; Departmental project research scheme
dc.description.abstract Separation and recovery of copper (Cu) from sulphate mediated CuCr spent catalyst leach solution through solvent extraction approach has been systematically investigated. A number of Ionic Liquid (IL) and other conventional extractants were used while investigating the selectivity and efficient extraction tendency of either IL or extractants towards Cu(II). In context of copper extraction efficiency, the adopted organic reagents followed the descending order: R4PSCN > R4PD > R4PCy > Cyphos 101 > Aliquot 336 > D2EHPA > Cyanex 272. The extraction behavior of Cu(II) was established based on slope analysis method. From the results it was noticed that extraction occurs through a cation exchange mechanism with association of a mole of Cu(II) per mole of R4PSCN. The plot of log D vs. log [R4PSCN] yield a linear relationship with a slope close to 4 which is used to propose extraction reaction mechanism/ stoichiometry. The nature of complex between Cu(II) and IL was further examined using FTIR analysis of the loaded organic phase with the diluent. Mc-Cabe Thiele diagram was constructed to predict quantitative extraction of Cu(II) which revealed the need for two stages at aqueous to organic (A:O) phase volume ratio of =3:1. The stripping isotherm constructed at optimum NH4OH concentration (0.4 M) suggests the need for two stages at O:A phase volume ratio of = 2:1 for complete stripping of copper with regeneration of R4SCN for further use. Both isotherm conditions were validated by 6 cycles of counter current simulation (CCS) study for obtaining the desired amount of Cu(II) loaded R4SCN (during extraction) and/or stripped copper solution (during stripping). Overall copper enrichment was similar to 6 fold leading to produce a copper(II) solution of 48 g/L from 6 g/L Cu(II). The stripped solution was subjected to crystallization study to produce copper sulphate crystals of high purity and was confirmed by XRD analysis of crystal phases.
dc.language en
dc.publisher Elsevier
dc.relation.isreferencedby SCI
dc.rights Copyright [2024]. All efforts have been made to respect the copyright to the best of our knowledge. Inadvertent omissions, if brought to our notice, stand for correction and withdrawal of document from this repository.
dc.subject Metallurgy & Metallurgical Engineering
dc.title Influence of ionic liquid (R 4 PSCN) for selective separation and recovery of copper from spent Cu - Cr catalyst leach liquor
dc.type Journal Article
dc.affiliation.author CSIR-IMMT, Bhubaneswar 751013, Odisha, India


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