Production of High-Grade Antimony Oxide From Smelter Slag via Leaching and Hydrolysis Process

dc.contributor.author Ibrahim, Ahmedaljaali Ibrahim Idrees
dc.contributor.author Aboelgamel, Muhammed
dc.contributor.author Soylu, Kartal Kaan
dc.contributor.author Top, Soner
dc.contributor.author Kursunoglu, Sait
dc.contributor.author Altiner, Mahmut
dc.contributor.author Ibrahim Idrees Ibrahim, Ahmedaljaali
dc.contributor.author Kaan Soylu, Kartal
dc.date.accessioned 2025-09-25T10:55:36Z
dc.date.available 2025-09-25T10:55:36Z
dc.date.issued 2025
dc.description Kursunoglu, Sait/0000-0002-1680-5482; en_US
dc.description.abstract This study aimed to investigate the recovery of antimony (Sb) from slag generated in an antimony smelting plant using leaching followed by hydrolysis processes. The leaching behaviors of rare earth elements (REEs) were also examined. The physicochemical properties of the slag were determined using various analytical techniques. The slag (4.12 % Sb) was mainly composed of quartz and minor minerals, including microline, magnetite, heden-bergite, and stibiconite. The Sb types in the slag determined by XPS were found to be in the oxide form. The concentrations of REEs (La, Y, Ce, and Nd) in the slag were 169.21 g/t. Preliminary leaching experiment results indicate that (i) HCl was selected rather than other acids due to its high extraction ability on the Sb from the slag, (ii) a sample with a d50 of <25 mu m should be used, (iii) the slurry should be mixed at 300 rpm. In the following leaching tests, the effects of leaching parameters (HCl acid concentration, amount of tartaric acid, solid-to-liquid ratio, reaction temperature, and time) on the extraction rates of Sb, impurities, and REEs were investigated. At the best leaching conditions (HCl: 8 M, amount of tartaric acid: 1 g/L, stirring speed: 300 rpm, reaction tem-perature: 75 C-degrees, and time: 180 min), the extraction rates of Sb from the slag were determined to be 91.19 %, but the extraction rates of REEs were measured to be <= 50 %. The activation energy (Ea) for Sb leaching was found to be 46.75 kJ/mol, indicating that the reaction was governed by the chemically controlled mechanism. In particular, it was understood from the additional experimental results that the leaching procedure should be carried out for 20 h to extract La with an extraction rate of >90 %. However, the extraction rate of Sb was negligible in extended times. It was determined that using tartaric acid positively affected La's leaching mech-anism, and the required leaching time for La decreased to 180 min from 20 h with the increase of tartaric acid from 1 g/L to 6 g/L. Hydrolysis tests were conducted using the Taguchi approach (L32, 2<^>1 4<^>3). The effects of the alkaline type (NH4OH and NaOH), stirring speed (100, 200, 300, and 400 rpm), temperature (50, 60, 70, and 80 C-degrees), and pH (1.5, 2, 2.5, and 3) on the precipitation of Sb from the PLS were investigated. NH4OH was suggested for use in the hydrolysis test to obtain precipitates with higher purities. The product obtained under the optimal conditions comprised 81.43 % Sb, 16.23 % O, and 2.34 % Fe. The product was identified as antimony oxide by XRD en_US
dc.description.sponsorship Scientific and Technological Research Council of Turkey (TUBITAK) [123M062]; TUBITAK; Cukurova University Research Fund [FYL-2022-15229] en_US
dc.description.sponsorship This study was supported by the Scientific and Technological Research Council of Turkey (TUBITAK) under Grant Number 123M062. The author thanks TUBITAK for their support. Also, the author would like to thank Cukurova University Research Fund for financial support (FYL-2022-15229) . In addition, the authors would like to thank Dr. Burcu Selen CAGLAYAN for her help to evaluate XPS analysis. en_US
dc.description.sponsorship Türkiye Bilimsel ve Teknolojik Araştırma Kurumu, TÜBİTAK, (123M062); Çukurova Üniversitesi, CU, (FYL-2022-15229)
dc.identifier.doi 10.1016/j.seppur.2024.129355
dc.identifier.issn 1383-5866
dc.identifier.issn 1873-3794
dc.identifier.scopus 2-s2.0-85202149481
dc.identifier.uri https://doi.org/10.1016/j.seppur.2024.129355
dc.identifier.uri https://hdl.handle.net/20.500.12573/4484
dc.language.iso en en_US
dc.publisher Elsevier en_US
dc.relation.ispartof Separation and Purification Technology en_US
dc.rights info:eu-repo/semantics/closedAccess en_US
dc.subject Antimony en_US
dc.subject Smelter Slag en_US
dc.subject Hcl Leaching en_US
dc.subject Hydrolysis en_US
dc.subject Rare Earth Elements en_US
dc.title Production of High-Grade Antimony Oxide From Smelter Slag via Leaching and Hydrolysis Process en_US
dc.type Article en_US
dspace.entity.type Publication
gdc.author.id Kursunoglu, Sait/0000-0002-1680-5482
gdc.author.id IBRAHIM IEES IBRAHIM, AHMEDALJAALI/0009-0008-9809-5680
gdc.author.scopusid 59299665000
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gdc.author.wosid Top, Soner/H-3310-2015
gdc.author.wosid Kursunoglu, Sait/Aba-9352-2020
gdc.author.wosid Altiner, Mahmut/E-5044-2018
gdc.bip.impulseclass C5
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gdc.coar.access metadata only access
gdc.coar.type text::journal::journal article
gdc.collaboration.industrial false
gdc.description.department Abdullah Gül University en_US
gdc.description.departmenttemp [Ibrahim, Ahmedaljaali Ibrahim Idrees; Aboelgamel, Muhammed; Soylu, Kartal Kaan; Altiner, Mahmut] Cukurova Univ, Dept Min Engn, Div Mineral Proc, TR-01330 Adana, Turkiye; [Top, Soner] Abdullah Gul Univ, Dept Engn Sci, TR-38080 Kayseri, Turkiye; [Kursunoglu, Sait] Batman Univ, Dept Petr & Nat Gas Engn, TR-72100 Batman, Turkiye en_US
gdc.description.publicationcategory Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı en_US
gdc.description.scopusquality Q1
gdc.description.volume 354 en_US
gdc.description.woscitationindex Science Citation Index Expanded
gdc.description.wosquality Q1
gdc.identifier.openalex W4401836439
gdc.identifier.wos WOS:001303834800001
gdc.index.type WoS
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gdc.oaire.diamondjournal false
gdc.oaire.impulse 4.0
gdc.oaire.influence 2.6963514E-9
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gdc.openalex.collaboration National
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gdc.virtual.author Top, Soner
gdc.virtual.author Kurşunoğlu, Sait
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