{"title":"Reducing silica in zirconium leachate from washed and dried frit powder: Role of cold and concentrated nitric acid and avoidance of crud formation","authors":"Sandeep Singh Tomar , Garima Pandey , Nirvik Sen , Gaurav Varshney , Sulekha Mukhopadhyay","doi":"10.1016/j.hydromet.2024.106434","DOIUrl":null,"url":null,"abstract":"<div><div>Traditionally zirconium is leached from washed dried frit (WDF) powder using commercial-grade nitric acid at 80 °C, which results in a leachate containing significant colloidal silica, leading to emulsion and solvent loss. This work used red fuming nitric acid (RFNA) which consists of 84 % nitric acid, 13 % dinitrogen tetroxide and 1–2 % water, as a novel leaching agent. The reduced water content in RFNA enhances the acid strength and prevents colloidal silica formation. This improves zirconium recovery and reduces co-leaching of silica. Optimization efforts focused on operating parameters (impeller speed, temperature, time, acid concentration, liquid-to-solid ratio during reaction and washing steps) to maximize zirconium recovery while minimizing silica in the pregnant leach solution (PLS). Avrami-Erofeev model was used to identify the reaction regime and estimate the apparent rate of leaching. The leaching process was found to follow a complex mechanism. Fourier-transform infrared (FT-IR) spectra of leach residue were analysed to characterize the silica. Zirconium concentration in the PLS from WDF powder dissolved in concentrated nitric acid reached approximately 87 g/L compared to 67 g/L using hot acid leaching (29.8 % increase). Silica concentration decreased from 6500 mg/L to 400 mg/L (93.8 % decrease) using this novel approach, achieving nearly 30 % higher zirconium concentration in the PLS compared to traditional methods.</div></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":"232 ","pages":"Article 106434"},"PeriodicalIF":4.8000,"publicationDate":"2025-02-01","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/S0304386X24001749","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
Traditionally zirconium is leached from washed dried frit (WDF) powder using commercial-grade nitric acid at 80 °C, which results in a leachate containing significant colloidal silica, leading to emulsion and solvent loss. This work used red fuming nitric acid (RFNA) which consists of 84 % nitric acid, 13 % dinitrogen tetroxide and 1–2 % water, as a novel leaching agent. The reduced water content in RFNA enhances the acid strength and prevents colloidal silica formation. This improves zirconium recovery and reduces co-leaching of silica. Optimization efforts focused on operating parameters (impeller speed, temperature, time, acid concentration, liquid-to-solid ratio during reaction and washing steps) to maximize zirconium recovery while minimizing silica in the pregnant leach solution (PLS). Avrami-Erofeev model was used to identify the reaction regime and estimate the apparent rate of leaching. The leaching process was found to follow a complex mechanism. Fourier-transform infrared (FT-IR) spectra of leach residue were analysed to characterize the silica. Zirconium concentration in the PLS from WDF powder dissolved in concentrated nitric acid reached approximately 87 g/L compared to 67 g/L using hot acid leaching (29.8 % increase). Silica concentration decreased from 6500 mg/L to 400 mg/L (93.8 % decrease) using this novel approach, achieving nearly 30 % higher zirconium concentration in the PLS compared to traditional methods.
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.