Recovery of Eu and Y from Waste Fluorescent Lamps

Eu and Y were extracted from waste fluorescent lamps containing ~0.3% Eu and 7% Y by acidic leaching, hydrolytic precipitation and/or solvent extraction. The leaching tests showed that about 90% Eu and 95% Y were leached in 3M HCl or 3M HNO 3 at 80°C, liquid to solid ratio 10:1 in 30 min. Leaching in H 2 SO 4 provided lower Eu and Y extraction efficiency. Only around 85% Eu and 80% Y were extracted at temperatures higher than 70°C. Eu and Y started precipitating simultaneously at pH 1.5 and the precipitation completed at ~ pH 2. Solvent extraction of Eu and Y from sulfate solutions using D2EHPA is strongly influenced by solution pH. At pH 1.4 about 80% Eu and 100%Y were extracted while at pH 1.16 only 25% Eu was extracted together with 90% Y.

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Publication Details

Journal
Inżynieria Mineralna
Published
2025-10-12
DOI
https://doi.org/10.29227/im-2017-01-05
Citations
3
Primary Topic
Extraction and Separation Processes
Type
article
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article

Recovery of Eu and Y from Waste Fluorescent Lamps

J. Formánek, Trong D. Pham, H. Vu, Petr Dvořák
3 citations
Inżynieria Mineralna
Extraction and Separation Processes
article

Recovery of Eu and Y from Waste Fluorescent Lamps

J. Formánek, Trong D. Pham, H. Vu, Petr Dvořák
article en
3 citations

Abstract

Eu and Y were extracted from waste fluorescent lamps containing ~0.3% Eu and 7% Y by acidic leaching, hydrolytic precipitation and/or solvent extraction. The leaching tests showed that about 90% Eu and 95% Y were leached in 3M HCl or 3M HNO 3 at 80°C, liquid to solid ratio 10:1 in 30 min. Leaching in H 2 SO 4 provided lower Eu and Y extraction efficiency. Only around 85% Eu and 80% Y were extracted at temperatures higher than 70°C. Eu and Y started precipitating simultaneously at pH 1.5 and the precipitation completed at ~ pH 2. Solvent extraction of Eu and Y from sulfate solutions using D2EHPA is strongly influenced by solution pH. At pH 1.4 about 80% Eu and 100%Y were extracted while at pH 1.16 only 25% Eu was extracted together with 90% Y.

Inżynieria MineralnaVol. 1(1)
VSB - Technical University of Ostrava (CZ), University of Chemistry and Technology, Prague (CZ)
Clean water and sanitation
Openalex Percentile: Top 100%
Extraction and Separation Processes
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Recovery of Eu and Y from Waste Fluorescent Lamps — J. Formánek, Trong D. Pham, et al. · Inżynieria Mineralna (2025) | TGRS Research Map | TGRS