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Application of leaching kinetics modelling to a gold cyanide leach plant by using real plant data

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Treść / Zawartość
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
Gold cyanide leach kinetics modeling was applied to the Bergama Ovacik gold cyanide leach plant in Turkey by processing the real plant data without need of any laboratory work. For this aim, solid ore samples were taken from each leaching tanks and analysed for gold contents as Au ppm while plant variables such as solid % concentrations in each tank, feed rate of plant as megagrams per hour (Mg/h), slurry flow rate as m3/h and the slurry residence times in each tank calculated and noted for modelling study. Five sampling work performed at plant at different times. Each sampling data were modelled seperately by the Anglo-American Research Laboratories (AARL) leach kinetics model to obtain five seperate model parameters and regression coefficient (R2) values. Then, total five sampling data were all together modelled to obtain just one model equation and R2 value to represent the plant generally. All R2 values were above 0.90 indicating that the AARL gold leaching kinetics model fits well on real plant leaching conditions. By using the model parameters, the residual gold contents in each tank were predicted for different possible ore feed rate tonnages such as 80, 90, 100, 110 and 120 megagrams per hour. Thus, leaching recoveries for any ore feed rate would be estimated for possible tonnage increases in the future.
Słowa kluczowe
EN
gold   cyanide   leach   kinetics   model  
Rocznik
Strony
109--114
Opis fizyczny
Bibliogr. 10 poz., rys., tab.
Twórcy
autor
  • Independent researcher, Izmir, Turkey
Bibliografia
  • 1. BELLEC, S., HODOUIN, D., BAZIN, C., KHALESI, M. R. AND DUCHESNE C. 2009. Modelling and simulation of gold ore leaching. World Gold Conference 2009, The Southern African Institute of Mining and Metallurgy, 51–60.
  • 2. CEROVIC, K., HUTCHISON, H., SANDENBERGH, R.F., 2005. Kinetics of gold and a gold – 10% silver alloy dissolution in aqueous cyanide in the presence of lead, Minerals Engineering 18, 585–590.
  • 3. DAVIDSON, R.J. AND SOLE, M.J. 2007. The major role played by calcium in gold plant circuits. The Journal of The Southern African Institute of Mining and Metallurgy ,Volume 107 refereed paper July 463–468.
  • 4. DE ANDRADE LIMA, L.R.P., 2007. Dynamic Simulation of the Carbon in Pulp and Carbon in Leach Processes Brazilian Journal of Chemical Engineering Vol. 24, No. 04, 623–635.
  • 5. GUO, H., DESCHÊNES, G., PRATT A., FULTON M., LASTRA R. 2004. Leaching Kinetics and Mechanisms of Surface Reactions During Cyanidation of Gold in the Presence of Pyrite or Stibnite SME Annual Meeting Denver, Colorado 1–8.
  • 6. JEFFREY, M. I., BREUER, P. L., CHOO W. L. 2001. A kinetic study that compares the leaching of gold in the cyanide, thiosulfate, and chloride systems Metallurgical and Materials Transactions B, Volume 32, Issue 6, 979–986.
  • 7. PLEYSIER, R., DAI, X., WINGATE, C.J., JEFFREY, M.I. 2008. Microtomography based identification of gold adsorption mechanisms, the measurement of activated carbon activity, and the effect of frothers on gold adsorption Minerals Engineering, Volume 21, Issue 6, May, 453–462
  • 8. RUBISOVA, D.H., PAPANGELAKISA, V.G., KONDOSA, P.D. 1996. Fundamental kinetic models for gold ore cyanide leaching Canadian Metallurgical Quarterly Volume 35, Issue 4, 353–361.
  • 9. SRITHAMMAVUT, W., LUUKKANEN, S., LAARI, A., KANKAANPÄÄ, T., TURUN I. 2011. Kinetic Modelling of Gold Leaching and Cyanide Consumption in Intensive Cyanidation of Refractory Gold Concentrate, Journal of the University of Chemical Technology and Metallurgy, Volume 46, 2, 181–190.
  • 10. WOOLLACOTT, L.C., STANGE, W. AND KING, R.P. 1990. Towards more effective simulation of CIP and CIL processes. 1. The modelling of adsorption and leaching J. S. Afr. Inst. Min. Metal/.,vol. 90, no. 10., 275–282.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-efdec012-6c42-4f37-b370-d123ce57b066
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