| ArticleName |
Production of nepheline concentrate
from tailings of the Karnasurt processing facility
of the Lovozero Mining and Processing Plant |
| ArticleAuthorData |
Lovozero Mining and Processing Plant (Revda settlement, Lovozersky district, Murmansk region, Russia)
Fedyakov V. Yu., CEO, PhD in Law, info@ooolgok.ru
State Research and Design Institute of Rare Metal Industry (Moscow, Russia)
Shekhirev D. V., Leading Researcher, PhD in Engineering, shekhirev@list.ru Golovko V. V., Expert, PhD in Engineering, VaVasGolovko@rosatom.ru Fureev I. L., Head of Department, ILFureev@rosatom.ru |
| Abstract |
This study aims to develop a process for producing nepheline concentrate from tailings generated at the Lovozero Mining and Processing Plant during loparite ore beneficiation. The accumulated tailings exceed 18 million tons, with an annual increase of 400,000–450,000 tons. The work is relevant due to the shortage of bauxite feedstock for the aluminum industry. It was established that gravity separation and wet magnetic separation are ineffective for upgrading the original tailings without preliminary grinding. The effectiveness of dry magnetic separation applied to the 0.1 mm size fraction and reverse flotation with hydroxamic acids applied to the –0.1 mm fraction in producing marketable nepheline concentrate was demonstrated. A simplified process is recommended for obtaining high-grade nepheline concentrate with two products: the 0.1 mm size fraction is processed by magnetic separation, and the –0.1 mm fraction (including re-ground middlings from magnetic separation) is processed by reverse flotation, yielding a concentrate with Al2O3 content of 28.1 wt.% and recovery of 91.4 %. Additionally, a loparite-bearing aegirine product with a niobium content of 0.47 wt.% and recovery of 62.4 % was obtained. The process for obtaining nepheline concentrate from coarse and fine fractions considers the material composition of the tailings: coarse fractions are enriched in nepheline, fine fractions in aegirine and loparite, with particles larger than 1 mm being practically absent. The proposed process design reduces the volume of material sent for grinding to 10 % of the original tailings and for flotation to 31 %. |
| References |
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