Determination of the optimal technological regime and parameters of the cyanidation process of the flotation concentrate obtained after the enrichment of resistant gold-bearing ores
DOI:
https://doi.org/10.51301/ejsu.2025.i5.01%20Keywords:
gold, flotation concentrate, cyanidation, sodium cyanide, concentration, activated carbonAbstract
As a result of comprehensive studies of the material composition of the flotation concentrate and the forms of gold presence, it was established that the chemical composition of the concentrate is 55.17% represented by lithophile components with the mass fraction of 55.17%. The main ones are silica and alumina with mass fractions of 36.4% and 8.26%, respectively. Ore mineralization of the flotation concentrate is represented by pyrite with the mass fraction of 40.7%. It has been established that gold in the flotation concentrate sample is present in native form. The bulk of gold grains is represented by particles with a size of 10-38 microns - 82.89%. About 63% of gold is in free form. The proportion of closed grains is 9.23%. The main mineral in the flotation concentrate sample, associated with gold, is pyrite – 25%. The portion of gold associated with quartz is 3.07%. For industrial operation, sorption type of cyanidation of flotation concentrates with a consumption of Norit RO 3520 activated carbon in an amount of 10% of the volume of the liquid phase is recommended as the optimal mode. The parameters for sorption cyanidation of flotation concentrate have been established: flotation concentrate size – P80 10 microns; sodium cyanide concentration – 0.1% (sodium cyanide consumption – 2.3 kg/t); pH – 10.5; pulp density – 40% (solid); duration of the process is 24 hours. With the established parameters, relatively high, at least 86%, extraction of gold into the solution was achieved.
References
Ghobadi, B., Noaparast, M., Shafaei, S.Z. & Unesi, M. (2014). Optimization of cyanidation parameters to increase the capacity of Aghdarre gold mill. Journal of Mining and Environment, 5(2), 121-128
Marsden, J., & House, C. (2006). The chemistry of gold extraction, vol 2. Society for Mining. Metallurgy and Explo-ration (SME), Littleton (CO), USA
Medina, D., & Anderson, C.G. (2020). A Review of the cyanidation treatment of copper-gold ores and concentrates. Metals, (10), 897. http://doi.org/10.3390/met10070897
Stapper, D., Dales, K., Velasquez, P. & Keane, S. (2021). Best management practices for cyanide use in the small-scale gold mining sector. PlanetGOLD Program (Global Environ-ment Facility and United Nations Environment Programme)
Ashley, P.M., Creagh, C.J. & Ryan, C.G. (2000). Invisible gold in ore and mineral concentrates from the Hillgrove gold - antimony deposits, NSW, Australia. Mineralium Deposit, 35(4), 285-301. https://doi.org/10.1007/s001260050242
Kovalev, K.R. (2011). Gold content of arsenopyrite in gold-sulfide deposits of Eastern Kazakhstan. Geology and Geo-physics, 52(2), 225-242. https://doi.org/10.1016/j.rgg.2010.12.014
Sanakulov, K.S. (2016). On the feasibility of using com-bined technologies for processing particularly refractory gold sulfide ores. Non-ferrous metals, (2), 9-14
Kanaeva, Z.K., Kanaev, A.T. & Semenchenko, G.V. (2014). Geological structure of the Bakyrchik gold-arsenic deposit in Eastern Kazakhstan. Fundamental Research, (11), 45
Meretukov, M.A. (2007). Gold and natural carbonaceous matter. Moscow: Ore and Metals
Zakharov, B.A., & Meretukov M.A. (2013). Gold: refractory ores. Moscow: Ore and metals
Földvári, M. (2011). Handbook of the thermogravimetric system of minerals and its use in geological practice. Occa-sional Papers of the Geological Institute of Hungary, 213, 1-118
Schmidt, C.M., & Heide, K. (2001). Thermal analysis of hydrocarbons in Paleozoic black shales. Journal of Thermal Analysis and Calorimetry, 64(3), 1297-1302. https://doi.org/10.1023/A:1011530020564
Gallagher, P.K., & Brown, M.E. (2003). Handbook of ther-mal analysis and calorimetry. Netherlands, Amsterdam: Else-vier Science
Chanturia, V.A. (2000). Change in the structural state of the surface of pyrite and arsenopyrite during electrochemical opening of refractory gold ores. Mining Journal, (2), 24-27
Hilson, G., & Monhemius, A.J. (2006). Alternatives to cya-nide in the gold mining industry: what prospects for the fu-ture? Journal of Cleaner Production, (14), 1158-1167. https://doi.org/10.1016/j.jclepro.2004.09.005
Adams, M.D. (2016). Gold ore processing: project develop-ment and operations. Gold Ore Processing, 525-531. http://doi.org/10.1016/B978-0-444-63658-4.00029-3
Habashi, F. (1967). Kinetics and mechanism of gold and silver dissolution in cyanide solution. Bureau of Mines and Geology, State of Montana, 1-42
Parga, J.R, Valenzuela, J.L. & Diaz, J.A. (2012). New tech-nology for recovery of gold and silver by pressure cyanida-tion leaching and electrocoagulation. Noble Metals. InTech, 71-94. http://doi.org/10.5772/32673
Mular, A.L., Halbe, D.N. & Barrate, D.J. (2002). Mineral processing plant design, Practice and control. Society for Mining, Metallurgy and Exploration, 1
Downloads
Published
How to Cite
Issue
Section
License
Copyright (c) 2025 Engineering Journal of Satbayev University

This work is licensed under a Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 International License.
<div class="pkpfooter-son">
<a rel="license" href="http://creativecommons.org/licenses/by-nc/4.0/"><img alt="Creative Commons License" style="border-width:0" src="https://i.creativecommons.org/l/by-nc/4.0/80x15.png"></a><br>This work is licensed under a <a rel="license" href="http://creativecommons.org/licenses/by-nc/4.0/">Creative Commons Attribution-NonCommercial 4.0 International License</a>.
</div>
