{"title":"The role of hydrogen peroxide in the acid dissolution of indium tin oxide (ITO) in the context of selective indium recovery from secondary sources","authors":"Daísa C.A. Gonçalves , Daniel Majuste","doi":"10.1016/j.hydromet.2025.106437","DOIUrl":null,"url":null,"abstract":"<div><div>This paper presents a thermodynamic, kinetic, and mechanistic examination of indium and tin extraction from indium tin oxide (ITO) in acidic sulfate solutions containing hydrogen peroxide (H<sub>2</sub>O<sub>2</sub>). The experimental approach included a comprehensive characterization of commercial ITO powder and leach residues by different techniques, as well as a systematic investigation of the effects of temperature, sulfuric acid (H<sub>2</sub>SO<sub>4</sub>) concentration, and hydrogen peroxide concentration on the leaching behavior (yield and rate) of indium and tin. The leaching tests showed that the presence of H<sub>2</sub>O<sub>2</sub> in the H<sub>2</sub>SO<sub>4</sub> solutions results in a significant increase in the leaching of indium, primarily at moderate temperatures. Furthermore, an increase in the H<sub>2</sub>O<sub>2</sub> concentration in the solutions leads to a decrease in the concentration of tin in the leach liquor. The extraction of indium from ITO appears to occur in two steps. The first step involves the spontaneous hydration of In<sub>2</sub>O<sub>3</sub> to form indium(III) hydroxide, In(OH)<sub>3</sub>, while the second step is the attack of this phase by protons (H<sup>+</sup>) to form soluble In<sup>3+</sup> species, which is also a spontaneous reaction. The rate-determining step of indium extraction from fine ITO particles (mean particle size = 18 μm) is likely the diffusion of H<sup>+</sup> through the pores of hydrated In<sub>2</sub>O<sub>3</sub> particles and the grains of SnO<sub>2</sub> surrounding these particles. With regard to the extraction of tin, the following sequence of steps was proposed: (i) the spontaneous reduction of the SnO<sub>2</sub> phase in the acid solutions to Sn<sup>2+</sup> by the active hydroperoxyl (HOO<sup>•</sup>) radical, which is formed from the decomposition reaction of H<sub>2</sub>O<sub>2</sub>; (ii) the spontaneous oxidation of Sn<sup>2+</sup> ions to Sn<sup>4+</sup> by the oxygen molecules and the active hydroxyl (HO<sup>•</sup>) radical, which are also formed from the decomposition reaction of H<sub>2</sub>O<sub>2</sub>; and (iii) the spontaneous precipitation of SnO<sub>2</sub> from the unstable Sn<sup>4+</sup> ions. A better understanding of the kinetics and mechanism of ITO dissolution in the H<sub>2</sub>SO<sub>4</sub>-H<sub>2</sub>O<sub>2</sub> media may be helpful in the design and improvement of leaching processes targeting high indium recovery by selective leaching.</div></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":"233 ","pages":"Article 106437"},"PeriodicalIF":4.8000,"publicationDate":"2025-01-18","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Hydrometallurgy","FirstCategoryId":"88","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0304386X25000027","RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"METALLURGY & METALLURGICAL ENGINEERING","Score":null,"Total":0}
引用次数: 0
Abstract
This paper presents a thermodynamic, kinetic, and mechanistic examination of indium and tin extraction from indium tin oxide (ITO) in acidic sulfate solutions containing hydrogen peroxide (H2O2). The experimental approach included a comprehensive characterization of commercial ITO powder and leach residues by different techniques, as well as a systematic investigation of the effects of temperature, sulfuric acid (H2SO4) concentration, and hydrogen peroxide concentration on the leaching behavior (yield and rate) of indium and tin. The leaching tests showed that the presence of H2O2 in the H2SO4 solutions results in a significant increase in the leaching of indium, primarily at moderate temperatures. Furthermore, an increase in the H2O2 concentration in the solutions leads to a decrease in the concentration of tin in the leach liquor. The extraction of indium from ITO appears to occur in two steps. The first step involves the spontaneous hydration of In2O3 to form indium(III) hydroxide, In(OH)3, while the second step is the attack of this phase by protons (H+) to form soluble In3+ species, which is also a spontaneous reaction. The rate-determining step of indium extraction from fine ITO particles (mean particle size = 18 μm) is likely the diffusion of H+ through the pores of hydrated In2O3 particles and the grains of SnO2 surrounding these particles. With regard to the extraction of tin, the following sequence of steps was proposed: (i) the spontaneous reduction of the SnO2 phase in the acid solutions to Sn2+ by the active hydroperoxyl (HOO•) radical, which is formed from the decomposition reaction of H2O2; (ii) the spontaneous oxidation of Sn2+ ions to Sn4+ by the oxygen molecules and the active hydroxyl (HO•) radical, which are also formed from the decomposition reaction of H2O2; and (iii) the spontaneous precipitation of SnO2 from the unstable Sn4+ ions. A better understanding of the kinetics and mechanism of ITO dissolution in the H2SO4-H2O2 media may be helpful in the design and improvement of leaching processes targeting high indium recovery by selective leaching.
期刊介绍:
Hydrometallurgy aims to compile studies on novel processes, process design, chemistry, modelling, control, economics and interfaces between unit operations, and to provide a forum for discussions on case histories and operational difficulties.
Topics covered include: leaching of metal values by chemical reagents or bacterial action at ambient or elevated pressures and temperatures; separation of solids from leach liquors; removal of impurities and recovery of metal values by precipitation, ion exchange, solvent extraction, gaseous reduction, cementation, electro-winning and electro-refining; pre-treatment of ores by roasting or chemical treatments such as halogenation or reduction; recycling of reagents and treatment of effluents.