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Modeling of the carbon in pulp (cip) process in gold cyanide leaching plants using the plant data

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Języki publikacji
EN
Abstrakty
EN
An improved method to model CIP plants by plant data is presented. The Turkish gold cyanide leaching CIP plants, Bergama Ovacik, Gumushane Mastra and Eskisehir Kaymaz were modeled by using gold concentrations of monthly carbon, solution and solids spot samples of adsorption tanks without a need of laboratory work. Five carbon adsorption models were used namely k-n, Nicol-Fleming, Dixon, Film Diffusion with Langmuir isotherm and Film Diffusion with Freundlich isotherm (Johns model). Several monthly obtained plant data were collected and modeled separately and model parameters as well as regression coefficient R2 values were found by non-linear regression. By comparing R2 values, the best fit model for the three CIP plants was determined as Film Diffusion with Langmuir Isotherm that R2 values were above 0.95. Thus, by using the best fit model, the Kaymaz plant was optimized for existing 49 Mg per hour ore feed tonnage and plant parameters were predicted according to planned feed tonnage increase to 120 Mg per hour.
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841--852
Opis fizyczny
Bibliogr. 10 poz., rys., tab.
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autor
  • Koza Altın Isletmeleri A.S., Kaymaz Gold Mine, Eskisehir, Turkey
Bibliografia
  • 1. ADAMS M.D., MCDOUGALL G.J., HANCOCK R.D., REES K.L., VAN DEVENTER, J.S.J., DUNNE, R.C., 1987, Models for the adsorption of aurocyanide onto activated carbon. Part II: Extraction of aurocyanide ion pairs by polymeric adsorbents, Hydrometallurgy, 18, 139–154.
  • 2. AHMED F.E., YOUNG B.D., BRYSON A.W., 1992, Comparison and modelling of the adsorption kinetics of gold cyanide onto activated carbon and resin in a silica slurry, Hydrometallurgy, 30, 257–275.
  • 3. DAVIDSON R.J., 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 ,107, 463–468.
  • 4. FLEMING C.A., NICOL M.J., 1984, The adsorption of gold cyanide onto activated carbon. III. Factors Influencing the Rate of Loading and the Equilibrium Capacity, J.S.Afr.Inst.Min.Metall., 84, 85–93.
  • 5. FLEMING C.A., MEZEI A., BOURRICAUDY E., CANIZARES M., ASHBURY M., 2011, Factors influencing the rate of gold cyanide leaching and adsorption on activated carbon, and their impact on the design of CIL and CIP circuits, Minerals Engineering, 24, 484–494.
  • 6. JONES W.G., LINGE H.G., 1989, Effect of ore pulp on the adsorption rate of gold cyanide on activated carbon, Hydrometallurgy, 22, 231–238.
  • 7. LE ROUX J.O., BRYSON A.W., YOUNG B.O., 1991, A comparison of several kinetic models for the adsorption of gold cyanide onto activated carbon, J. S. Afr. Inst. Min. Metal., 91, 95–103.
  • 8. 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, 21, 453–462.
  • 9. REES K.L, VAN DEVENTER J.S.J, 2001, Gold process modelling. I. Batch modelling of the processes of leaching, preg-robbing and adsorption onto activated carbon, Minerals Engineering, 14, 753-773.
  • 10. SYNA N., VALIX M., 2003, Modelling of gold (I) cyanide adsorption based on the properties of activated bagasse, Minerals Engineering,16, 421–427.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-ab112f5a-98bd-4c2e-963f-125352db104f
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