{"title":"A thermodynamic and kinetic study of efficient selenium removal from highly acidic TeCl4 solution using tellurium powder","authors":"Wenqiu Wang, Huazhen Cao, Weilun Qian, Anyang Tang, Junfeng Kong, Lining Yu, Zhengzheng Liu, Huibin Zhang, Guoqu Zheng","doi":"10.1016/j.hydromet.2025.106470","DOIUrl":null,"url":null,"abstract":"<div><div>High-purity tellurium is in high demand for applications in high-tech fields such as semiconductors and solar cells. To produce high-purity tellurium, one of the challenges is to effectively reduce selenium content of telluride (IV) solution. This study reports the thermodynamic and kinetic analysis for selenium removal by tellurium powder substitution in a TeCl<sub>4</sub> solution. The thermodynamic analysis revealed that the separation window of tellurium and selenium significantly varies with pH. Solutions of weak acidity or basicity are unfavorable for the separation of these two elements. In highly acidic systems, tellurium coexists with selenite ions in the form of Te<sup>4+</sup> ions, and the redox equilibrium potential values for E(Te<sup>4+</sup>/Te) and E(H<sub>2</sub>SeO<sub>3</sub>/Se) significantly differ, indicating the thermodynamic feasibility of selenium removal through tellurium powder replacement. Under optimal reaction condition, the selenium removal efficiency in highly acidic tellurium tetrachloride could reach ∼99.9 % with a residual selenium concentration of 0.1 mg/L. Kinetic studies indicated that selenium removal by tellurium powder substitution is primarily controlled by a chemical reaction with an apparent activation energy of 84.6 kJ/mol. This study provides a simple but efficient method for of selenium impurity removal toward high-purity tellurium.</div></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":"234 ","pages":"Article 106470"},"PeriodicalIF":4.8000,"publicationDate":"2025-03-12","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/S0304386X25000350","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
High-purity tellurium is in high demand for applications in high-tech fields such as semiconductors and solar cells. To produce high-purity tellurium, one of the challenges is to effectively reduce selenium content of telluride (IV) solution. This study reports the thermodynamic and kinetic analysis for selenium removal by tellurium powder substitution in a TeCl4 solution. The thermodynamic analysis revealed that the separation window of tellurium and selenium significantly varies with pH. Solutions of weak acidity or basicity are unfavorable for the separation of these two elements. In highly acidic systems, tellurium coexists with selenite ions in the form of Te4+ ions, and the redox equilibrium potential values for E(Te4+/Te) and E(H2SeO3/Se) significantly differ, indicating the thermodynamic feasibility of selenium removal through tellurium powder replacement. Under optimal reaction condition, the selenium removal efficiency in highly acidic tellurium tetrachloride could reach ∼99.9 % with a residual selenium concentration of 0.1 mg/L. Kinetic studies indicated that selenium removal by tellurium powder substitution is primarily controlled by a chemical reaction with an apparent activation energy of 84.6 kJ/mol. This study provides a simple but efficient method for of selenium impurity removal toward high-purity tellurium.
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.