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NOBLE METALS AND ALLOYS
Название Nitric acid loosening of rebellious sulphide concentrates containing precious metals
DOI 10.17580/tsm.2018.12.05
Автор Rogozhnikov D. A., Rusalev R. E., Dizer О. А., Naboychenko S. S.
Информация об авторе

Ural Federal University Named after the First President of Russia B. N. Yeltsin, Yekaterinburg, Russia:

D. A. Rogozhnikov, Senior Researcher at the Department of Non-Ferrous Metals, e-mail: darogozhnikov@yandex.ru
R. E. Rusalev, Postgraduate Student, Researcher at the Department of Non-Ferrous Metals
О. А. Dizer, Postgraduate Student, Researcher at the Department of Non-Ferrous Metals
S. S. Naboychenko, Visiting Professor at the Department of Non-Ferrous Metals

Реферат

This paper examines the most popular techniques of processing rebellious goldcontaining materials that cannot be cyanided using conventional techniques due to gold nanoparticles disseminated in the sulfide minerals. To loosen such rebellious concentrates, it is proposed to use nitric acid, which is an effective oxidizer and leaching agent. A gold sulphide concentrate from the Udereysk deposit was used in the study, which had been subjected to selective separation of antimony in alkaline sulphide solutions. The main gold-containing minerals in the concentrate include pyrite and arsenopyrite. The paper looks at the standard reactions between these minerals and nitric acid. The authors found a rather high thermodynamic probability of these reactions within a broad temperature range. Through building Pourbaix diagrams for arsenic and iron compounds in the considered heterogeneous systems, the authors demonstrate that in order to obtain the desired products from the interactions in view, the oxidation potential of the system should be maintained at the minimum level of 0.6 V. With the help of the mathematical methods of experiment design, the authors selected the nitric acid leaching parameters applicable to the test material: liquid-to-solid ratio = 8:1; nitric acid concentration — 6 mol/dm3; process duration — 75 minutes. The adequacy of the obtained data is confirmed by the calculated values of the determination coefficients, which were close to 100%. The extraction of iron and arsenic into the solution was around 97 and 92%, respectively. The obtained solid leaching residues, in which the concentration of gold can reach 100 g/t, are then sent to further extraction by conventional techniques. The leaching solutions containing iron and arsenic are neutralized and precipitate as low-solubility compounds.

This research was funded by the Russian Science Foundation (Project No. 18-19- 00186). The study of the thermodynamics of the processes under consideration was funded under the Governmental Assignment No. 11.4797.2017/8.9.

Ключевые слова Nitric acid, rebellious sulfide concentrate, leaching, gold, pyrite, arsenopyrite
Библиографический список

1. Meretukov M. A., Sanakulov K. S., Zimin A. V., Arustamyan M. A. Gold: The chemistry for steel makers and beneficiation specialists. Moscow : “Ore and Metals” Publishing House, 2014. 412 p.
2. Vorobiev-Desyatovsky N. V. Refractory and double refractory gold ores. The Russian problem of the present and the future and possible solutions. Proceedings of the International Conference “Intensification of hydrometallurgical processing of natural and manmade materials. Techniques and equipment”. Saint Petersburg, May 28 – June 1, 2018. pp. 18–19.
3. Meretukov M. A. Gold. Chemistry. Mineralogy. Metallurgy. Moscow : “Ore and Metals” Publishing House, 2008. pp. 226–242.
4. Majzlan J., Chovan M., Andras P., Newville M., Wiedenbeck M. N. The nanoparticulate nature of invisible gold in arsenopyrite from Pezinok (Slovakia). Neues Jahrbuch für Mineralogie Abhandlungen. 2010. Bd. 187, No. 1. pp. 1–9.
5. Palenik C. S., Utsunomiya S., Reich M., Kesler S. E., Wang L., Ewing R. C. “Invisible” gold revealed: Direct imaging of gold nanoparticles in a Carlin-type deposit. American Mineralogist. 2004. Vol. 89, No. 10. pp. 1359–1366.
6. Yang S., Blum N., Rahders E., Zhang Z. The nature of invisible gold in sulfides from Xiangxi Au – Sb – W ore deposit in Northwestern Hunan, People’s Republic of China. The Canadian Mineralogist. 1998. Vol. 36. pp. 1361–1372.
7. Cabri L. J., Newville M., Gordon R. A., Crozier E. D., Suton S. R., McMahon G., Jiang D. T. Chemical speciation of gold in arsenopyrite. The Canadian Mineralogist. 2000. Vol. 38. pp. 1265–1281.
8. Chen T. T., Cabri L. J., Dutrizac J. E. Characterizing gold in refractory sulfide gold ores and residues. Journal of The Minerals, Metals & Materials Society. 2002. Vol. 54, No. 12. pp. 20–22.

9. Chryssoulis S. L., McMullen J. Mineralogical investigation of gold ores. Development in mineral processing. Vol. 15. Advances in gold ore processing. Amsterdam : Elsevier, 2005. pp. 21–72.
10. Naboychenko S. S., Shneerson Ya. M., Kalashnikova M. I., Chugaev L. V. Pressure hydrometallurgy of non-ferrous metals. Yekaterinburg : GOU VPO UGTU — UPI, 2009. Vol. 1. pp. 52.
11. Shneerson Ya. M., Lapin A. Yu., Chugaev L. V. Some results of the work undertaken by the Hydrometallurgy Research Centre regarding the autoclave process of the hydrometallurgical complex operated by Petropavlovsk. Proceedings of the International Conference “Intensification of hydrometallurgical processing of natural and manmade materials. Techniques and equipment”. Saint Petersburg, May 28 – June 1, 2018. pp. 16–18.
12. Paphane B. D., Nkoane B. B. M., Oyetunji O. A. Kinetic studies on the leaching reactions in the autoclave circuit of the Tati Hydrometallurgical Demonstration Plant. Journal of the Southern African Institute of Mining and Metallurgy. 2013. Vol. 113, No. 6. pp. 485–489.
13. Hourn M. Refractory leaching solutions. Australian Mining. 2009. Vol. 101, No. 2. pp. 20.
14. Shneerson Ya. M., Nabojchenko S. S. Tendencies of non-ferrous metals autoclave hydrometallurgy development. Tsvetnye Metally. 2011. No. 3. pp. 15–20.
15. Dreisinger D. Hydrometallurgical process development for complex ores and concentrates. Journal of the Southern African Institute of Mining and Metallurgy. 2009. Vol. 109, No. 5. pp. 253–271.
16. Rogozhnikov D. A., Mamyachenkov S. V., Anisimov O. S. Nitric Acid Leaching of Copper-Zinc Sulfide Middlings. Metallurgist. 2016. Vol. 60, No. 1-2. pp. 229–233.
17. Rogozhnikov D. A., Mamyachenkov S. V., Karelov S. V., Anisimova O. S. Nitric acid leaching of polymetallic middlings of concentration. Russian Journal of Non-Ferrous Metals. 2013. Vol. 54, No. 6. pp. 440–442.
18. Anderson C. G., Harrison K. D., Krys L. E. Theoretical considerations of sodium nitrite oxidation and fine grinding in refractory precious-metal concentrate pressure leaching. Minerals and Metallurgical Processing. 1996. Vol. 13, No. 1. pp. 4–11.
19. Van Weert G., Fair K. J., Schneider J. C. Prochem's NITROX Process. CIM Bulletin. 1986. Vol. 79. pp. 84, 85.
20. Beattie M. J. V., Ismay A. Applying the redox process to arsenical concentrates. Journal of The Minerals, Metals & Materials Society. 1990. Vol. 42 (1). pp. 31–35.
21. La Brooy S. R., Linge H. G., Walker G. S. Review of gold extraction from ores. Minerals Engineering. 1994. Vol. 7, No. 10. pp. 1213–1241.
22. Rusalev R. E., Grokhovskii S. V., Rogozhnikov D. A., Naboichenko S. S. Investigation and Development of the Technology of Processing Gold-Antimony Flotation Concentrates. Journal Of Siberian Federal University-Chemistry. 2018. Vol. 11, No. 1. pp. 110–121.
23. Marsden J. O., House C. I. The Chemistry of Gold Extraction. Littleton : Society For Mining, Metallurgy, and Exploration, Inc., 2006.
24. Jian L., Shuming W., Dan L., Mengyang L. Response surface methodology for optimization of copper leaching from a lowgrade flotation middling. Minerals and Metallurgical Processing. 2011. No. 3. pp. 139–145.

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