2021
DOI: 10.31643/2021/6445.33
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Recovery of niobium from wastes generated in titanium production by cation exchange sorbents

Abstract: This article presents the technology of niobium recovery by processing of chloride residues generated during the chlorination of titanium slags. For waste processing, a two-stage leaching technology is proposed. Water is used at the first stage of leaching and hydrochloric acid 4.0 M is used at the second stage. For the purpose of sorption of niobium from the solution composition obtained during leaching, cation-exchange sorbents Purolite-C104 and KU-2-8 H were used. By the usage of Purolite-C104 ion exchange … Show more

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Cited by 4 publications
(6 citation statements)
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“…An analysis of the available literature review shows that most studies have been conducted for high-grade niobium-containing raw materials (Shikika et al, 2020). Moreover, very few studies have been conducted on the recovery of niobium from titanium production waste (Baigenzhenov et al, 2021;Kudryavsky, 2004).…”
Section: Introductionmentioning
confidence: 99%
“…An analysis of the available literature review shows that most studies have been conducted for high-grade niobium-containing raw materials (Shikika et al, 2020). Moreover, very few studies have been conducted on the recovery of niobium from titanium production waste (Baigenzhenov et al, 2021;Kudryavsky, 2004).…”
Section: Introductionmentioning
confidence: 99%
“…Works [9,10] describe the processing of chloride wastes generated in the titanium slag chlorination process. Niobium sorption under static conditions from the leaching solutions of chloride waste containing up to 2 g/L Nb was considered.…”
Section: Introductionmentioning
confidence: 99%
“…Purolite-C104 and KU-2-8 H cation-exchange sorbents were used to sorb niobium from the solution obtained in the leaching process. When the Purolite-C104 ion-exchange resin was used, the niobium sorption rate from the solution with a concentration of 2 g/L for 3.5 h was about 71.0% (0.071 g/g), and this rate was about 89.0% (0.089 g/g) for the KU-2-8 H ion-exchange resin [9]. The sorption kinetics at three different initial concentrations of niobium (1.0, 1.5, and 2.0 g/L) were studied [10].…”
Section: Introductionmentioning
confidence: 99%
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“…In other studies, the authors investigated the recovery of niobium from chloride residues generated from the chlorination of titanium slags [ [14], [15]]. In order to recover two-stage leaching process was suggested.…”
Section: Introductionmentioning
confidence: 99%