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NOBLE METALS AND ITS ALLOYS
ArticleName Arsenic stabilization when processing refractory gold-bearing concentrates by the use of arsenatazing roasting
DOI 10.17580/tsm.2025.07.05
ArticleAuthor Senchenko A. E., Aksenov A. V., Rybkin S. G.
ArticleAuthorData

Institute TOMS, Irkutsk, Russia

A. E. Senchenko, CEO, e-mail: senchenko@tomsmineral.ru
A. V. Aksenov, Head of the Metallurgy Laboratory, Candidate of Technical Sciences, e-mail: aksenov@tomsmineral.ru
S. G. Rybkin, Senior Researcher, Candidate of Technical Sciences, e-mail: rybkin@tomsmineral.ru

Abstract

Processing of concentrates from gravity and flotation enrichment of refractory gold-bearing ores using the technology of arsenatizing roasting with subsequent cyanidation of cinders allows, along with high extraction of precious metals into the target product, to radically reduce the volumes of formed sulfur oxides (SO2, SO3) and arsenic (As2O3) and reduce the costs of their neutralization. The technology includes roasting concentrates in a mixture with lime and calcium chloride at a temperature of 600–700 °C and access to atmospheric oxygen. During this process, the carbonaceous substance contained in the concentrate burns, the sulfide components are transformed into calcium sulfate CaSO4 and calcium arsenate Ca3(AsO4)2, and iron transforms into hematite Fe2O3. The flotation concentrate cinder is processed using the method of sorption cyanide leaching. The gravity concentrate cinder is enriched on a shaking table to obtain a primary gold concentrate and tails. The primary gold concentrate is melted to form ligature gold, and the table tailings are sent to sorption cyanide leaching. It has been established that during cyanidation of cinders from arsenatizing roasting of concentrates containing calcium arsenate, the arsenic content in solutions is within 0.5–3.0 mg/dm3, which does not correspond to the reference data on the solubility of Ca3(AsO4)2 in water, which is 130 mg/dm3. Studies have been conducted on the synthesis of calcium arsenate by a hydrometallurgical method – precipitation from an arsenic acid solution with calcium hydroxide and by a thermal method – sintering crystalline arsenic acid with calcium hydroxide. It has been shown that the solubility in water of calcium arsenate obtained by a thermal method is an order of magnitude lower than for the compound synthesized by a hydrometallurgical method. This ensures safer utilization of cyanidation tailings from arsenatizing roasting concentrates of refractory gold-bearing ores. It is assumed that the significant difference in solubility in water for calcium arsenate synthesized by hydrometallurgical and thermal methods is explained by the higher energy of the crystal lattice of the compound obtained by the sintering method.

keywords Gold-bearing concentrates, arsenatizing roasting, cinder, calcium arsenate, solubility, cyanide leaching
References

1. Lodeyshchikov V.V. Technology of gold and silver extraction from refractory ores: in 2 volumes. Irkutsk : Irgiredmet, 1999. Vol. 1. pp. 275–278.
2. Aksyonov A. V., Rybkin S. G., Senchenko A. E. Method of processing sulphide concentrate containing precious metals. Patent RF, No. 2691153. Applied : 29.10.2018. Published : 11.06. 2019.
3. Rybkin S. G., Aksenov A. V., Senchenko A. E., Vinokurov M. Yu. Method for processing sulphide concentrate containing precious metals. Patent RF, No. 2687613. Applied : 12.07.2017. Published : 15.05. 2019.
4. Senchenko A. Y., Aksenov A. V., Rybkin S. G. Optimization of gold recovery concentrates processing by the use of arsenatizing roasting. IMPC 2020: ХХХ International Mineral Proceedings Congress. 18–22 October 2020, Cape Town, South Africa. pp. 2394–2403.
5. Lidin R. A., Andreeva L. L., Molochko V. A. Constants of inorganic substances. Moscow : Drofa, 2006. 619 p.
6. Asselin E., Shaw R. Developments in arsenic management in the gold industry. Gold Ore Processing. Project Development and Operations. Second Edition, 2016. Ch. 41. Elsevier. pp. 739–751.
7. GOST 33034–2014. Test methods for chemicals of environmental hazard. Water solubility. Introduced : 01.08.2015.
8. Technical Specification TU 113-12-112–89. Metal arsenic for semiconductor compounds extra pure 19-4, extra pure 17-4, extra pure 10-4. Introduced : 01.01.1990.
9. GOST 1125–84. Super pure nitric acid. Specifications. Introduced : 01.01.1986.
10. GOST 9262–77. Reagents. Calcium hydroxide. Specifications. Introduced : 01.01.1978.
11. GOST 177–88. Hydrogen peroxide. Specifications. Introduced : 01.07.1989.
12. PDF-2 Database Copyright International Centre for Diffraction Data (ICDD). Entry number 01-075-0899; 00-033-0265. Available at: https://www.icdd.com/pdf-2/# (accessed : 23.05.2025).
13. PDF-2 Database Copyright International Centre for Diffraction Data (ICDD). Entry number 01-073-1298.
14. PDF-2 Database Copyright International Centre for Diffraction Data (ICDD). Entry number 00-001-0933.
15. Kasenov B. K., Sharipova Z. M., Ashlyaeva I. V. Heat capacity and thermodynamic functions of calcium orthoarsenate. High temperature thermophysics. Vol. 29, Iss. 2. Moscow : Nauka, 1991. pp. 389–390.
16. PDF-2 Database Copyright International Centre for Diffraction Data (ICDD). Entry number 01-073-1298; 00-044-0278; 00-017-0444; 01-075-2337.
17. Zelikman A. N., Voldman G. M., Belyaevskaya L. V. Theory of hydrometallurgical processes. Moscow : Metallurgiya, 1983. pp. 48–51.

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