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.authorID 0000-0003-3486-4184 en_US
dc.contributor.department AGÜ, Mühendislik Fakültesi, Malzeme Bilimi ve Nanoteknoloji Mühendisliği Bölümü en_US
dc.contributor.institutionauthor Top, Soner
dc.date.accessioned 2025-04-28T07:35:27Z
dc.date.available 2025-04-28T07:35:27Z
dc.date.issued 2025 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 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.identifier.endpage 21 en_US
dc.identifier.issn 1383-5866
dc.identifier.issn 1873-3794
dc.identifier.issue 7 en_US
dc.identifier.startpage 1 en_US
dc.identifier.uri https://doi.org/10.1016/j.seppur.2024.129355
dc.identifier.uri https://hdl.handle.net/20.500.12573/2512
dc.identifier.volume 354 en_US
dc.language.iso eng en_US
dc.publisher ELSEVIER en_US
dc.relation.isversionof 10.1016/j.seppur.2024.129355 en_US
dc.relation.journal Separation and Purification Technology en_US
dc.relation.publicationcategory Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı en_US
dc.relation.tubitak 123M062
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

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