Please use this identifier to cite or link to this item: http://elar.urfu.ru/handle/10995/130639
Title: Development of a Two-Stage Hydrometallurgical Process for Gold–Antimony Concentrate Treatment from the Olimpiadinskoe Deposit
Authors: Rusalev, R.
Rogozhnikov, D.
Dizer, O.
Golovkin, D.
Karimov, K.
Issue Date: 2023
Publisher: Multidisciplinary Digital Publishing Institute (MDPI)
Citation: Rusalev, R, Rogozhnikov, D, Dizer, O, Golovkin, D & Karimov, K 2023, 'Development of a Two-Stage Hydrometallurgical Process for Gold–Antimony Concentrate Treatment from the Olimpiadinskoe Deposit', Materials, Том. 16, № 13, 4767. https://doi.org/10.3390/ma16134767
Rusalev, R., Rogozhnikov, D., Dizer, O., Golovkin, D., & Karimov, K. (2023). Development of a Two-Stage Hydrometallurgical Process for Gold–Antimony Concentrate Treatment from the Olimpiadinskoe Deposit. Materials, 16(13), [4767]. https://doi.org/10.3390/ma16134767
Abstract: An integrated two-stage metallurgical process has been developed to process concentrates from the Olimpiadinskoe deposit, which contain high levels of antimony and arsenic. The optimal parameters for the alkaline sulfide leaching process of the initial concentrate from the Olimpiadinskoe deposit were determined to achieve the maximum extraction of antimony at a 99% level. The recommended parameters include an L:S ratio of 4.5:1, a sodium sulfide concentration of 61 g/L, a sodium hydroxide concentration of 16.5 g/L, a duration of 3 h, and a temperature of 50 °C. A synergistic effect of co-processing alkaline sulfide leach cakes with sulfuric and nitric acids was observed. The pre-treatment step reduced the nitric acid composition by converting carbonates into gypsum and increased the arsenic extraction by 15% during subsequent nitric acid leaching. The laboratory research on the nitric acid leaching of decarbonized cake established the key parameters for the maximum iron and arsenic extraction in solution (92% and 98%, respectively), including an L:S ratio of 9:1, a nitric acid concentration of 6 mol/L, and a time of 90 min. Full polynomial equations for the iron and arsenic extraction from the decarbonized cake were derived. The model demonstrated a high relevance, as evidenced by the determination coefficients (R2) of 96.7% for iron and 93.2% for arsenic. The technology also achieved a high gold recovery rate of 95% from the two-stage alkaline sulfide and nitric acid leach cake. Furthermore, the maximum deposition of arsenic from the nitrate leach solution in the form of insoluble As2S3 was determined to be 99.9%. A basic technological flow sheet diagram for processing the flotation gold–antimony concentrate from the Olimpiadinskoe deposit was developed, including two stages: the production of metallic antimony and the gold extraction from the nitric leach cake. © 2023 by the authors.
Keywords: ANTIMONY
ARSENIC
GOLD CYANIDATION
LEACHING
MATHEMATICAL PLANNING OF EXPERIMENTS
NITRIC ACID
OPTIMIZATION
REFRACTORY GOLD ORES
ANTIMONY
ANTIMONY COMPOUNDS
ARSENIC
DEPOSITS
EXTRACTION
FLOTATION
HYDROMETALLURGY
IRON
NITRIC ACID
ORE TREATMENT
ORES
POLYNOMIALS
SODIUM HYDROXIDE
SULFUR COMPOUNDS
ALKALINES
GOLD CYANIDATION
HYDROMETALLURGICAL PROCESS
MATHEMATICAL PLANNING OF EXPERIMENT
METALLURGICAL PROCESS
NITRIC ACID LEACHING
OPTIMISATIONS
PLANNING OF EXPERIMENTS
REFRACTORY GOLD ORE
S RATIO
LEACHING
URI: http://elar.urfu.ru/handle/10995/130639
Access: info:eu-repo/semantics/openAccess
cc-by
License text: https://creativecommons.org/licenses/by/4.0/
SCOPUS ID: 85164808500
WOS ID: 001030980600001
PURE ID: 41987146
ISSN: 1996-1944
DOI: 10.3390/ma16134767
metadata.dc.description.sponsorship: Russian Science Foundation, RSF: 075-03-2021-051/5, 22-79-10290, FEUZ-2021-0017
This work was funded by the Russian Science Foundation Project No. 22-79-10290. The XRF and XRD analyses were funded by the State Assignment, grant No. 075-03-2021-051/5 (FEUZ-2021-0017).
RSCF project card: 22-79-10290
Appears in Collections:Научные публикации ученых УрФУ, проиндексированные в SCOPUS и WoS CC

Files in This Item:
File Description SizeFormat 
2-s2.0-85164808500.pdf4,4 MBAdobe PDFView/Open


This item is licensed under a Creative Commons License Creative Commons