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Natural high grade chalcocite samples were leached in column under controlled Eh, constant temperature and solution pH to investigate the effect of particle size on dissolution kinetics. Moreover, low grade ores of larger size fractions were leached in column using raffinate from the industrial heap as an irrigation solution to simulate the real heap conditions. The leaching rate of large particle sizes (31-200 mm) were very slow without inflection point which are normally present in the leaching of small particle sizes (0.054-31 mm). The effect of particle size was more remarkable in the dissolution of large particles than that of small particles during the first stage (<45% dissolution). However, the dissolution rate of the second stages (>45% dissolution) were not noticeably affected by the particle size. Results of kinetics analysis of leaching of small particles using shrinking core model indicated that the first stage was controlled by fluid diffusion and confirmed by the low activation energies (20.98 kJ/mol). The kinetics of second stage was controlled by chemical reaction and product layer diffusion and the later control became prominent with increasing particle size. Similarly, product layer diffusion was the rate-controlling step for the first and second stages of leaching of large particles. X-ray CT and SEMEDS studies observed the increasing numbers of cracks and porosity and the formation of sulfur layer on the surface of the residue samples. The findings in this study provided some useful implications to optimize the heap performance and understand the leaching behavior of large particles.
Słowa kluczowe
Rocznik
Tom
Strony
676--692
Opis fizyczny
Bibliogr. 35 poz., rys., tab.
Twórcy
autor
- CAS Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, PR China
- National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Chinese Academy of Sciences, Beijing 100190, PR China
- University of Chinese Academy of Sciences, Beijing 10049, PR China
- Wanbao Mining Ltd, Beijing 100053, PR China
autor
- CAS Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, PR China
- National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Chinese Academy of Sciences, Beijing 100190, PR China
- State Key Laboratory of Biochemical Engineering Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, PR China
autor
- CAS Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, PR China
- National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Chinese Academy of Sciences, Beijing 100190, PR China
- State Key Laboratory of Biochemical Engineering Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, PR China
autor
- Wanbao Mining Ltd, Beijing 100053, PR China
autor
- Wanbao Mining Ltd, Beijing 100053, PR China
autor
- CAS Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, PR China
- National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Chinese Academy of Sciences, Beijing 100190, PR China
- State Key Laboratory of Biochemical Engineering Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, PR China
autor
- CAS Key Laboratory of Green Process and Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, PR China
- National Engineering Laboratory for Hydrometallurgical Cleaner Production Technology, Chinese Academy of Sciences, Beijing 100190, PR China
Bibliografia
- ARACENA, A., CAMILA E., OSCAR J., DANILO C., ALDONZA J., 2019. Dissolution kinetics of secondary covellite resulted from digenite dissolution in ferric/acid/chloride media. Physicochem. Probl. Miner. Process. 55, 840-851.
- BOBECK, G., SU, H., 1985. The kinetics of dissolution of sphalerite in ferric chloride solution. Metall. Trans. B 16, 413-424.
- BOLORUNDURO, S.A., 1999. Kinetics of leaching of chalcocite in acid ferric sulfate media: Chemical and bacterial leaching. Phd thesis, The University of British Columbia.
- BRIERLEY, J.A., 2001. Present and future commercial applications of biohydrometallurgy. Hydrometallurgy 59, 233-239.
- CASTILLO, J., SEPÚLVEDA, R., ARAYA, G., GUZMÁN., TORO, N., PÉREZ, K., RODRÍGUEZ, M., NAVARRA, A., 2019. Leaching of white metal in a NaCl-H2SO4 system under environmental conditions. Minerals 9, 319.
- CHENG, C.Y., FRANK, L., 1991a. The kinetics of leaching chalcocite in acidic oxygenated sulphate-chloride solutions. Hydrometallurgy 27, 249-268.
- CHENG, C.Y., FRANK, L., 1991b. The kinetics of leaching covellite in acidic oxygenated sulphate-chloride solutions. Hydrometallurgy 27, 269-284.
- CRUNDWELL, F.K., 2013. The dissolution and leaching of minerals: Mechanisms, myths and misunderstandings. Hydrometallurgy 139, 132-148.
- DEVECI, H., 2004. Effect of particle size and shape of solids on the viability of acidophilic bacteria during mixing in stirred tank reactors. Hydrometallurgy 71, 385-396.
- FANG, C., YU, S., WANG, X., ZHAO, H., QIN, W., QIU G., WANG, J., 2018. Synchrotron radiation XRD investigation of the fine phase transformation during synthetic chalcocite acidic ferric sulfate leaching. Minerals 8, 461.
- GEET, M.V., SWENNEN, R., WEVERS, M., 2000. Quantitative analysis of reservoir rocks by microfocus X-ray computerised tomography. Sediment. Geol. 132, 25-36.
- GHORBANI, Y., BECKER, M., MAINZA, A., FRANZIDIS, J.P., PETERSEN, J., 2011. Large particle effects in chemical/biochemical heap leach processes – a review. Miner. Eng. 24, 1172-1184.
- GHORBANI, Y., BECKER, M., PETERSEN, J. , MORAR, S. H. , MAINZA, A., FRANZIDIS, J.P., 2011. Use of X-ray computed tomography to investigate crack distribution and mineral dissemination in sphalerite ore parti-cles. Miner. Eng. 24, 1249-1257.
- HASHEMZADEH, M., DIXON, D.G., LIU, W., 2019. Modelling the kinetics of chalcocite leaching in acidified ferric chloride media under fully controlled ph and potential. Hydrometallurgy 186, 275-283.
- Jia, Y., SUN, H.Y., TAN, Q.T., GAO, H.S., FENG, X.L., RUAN, R.M., 2018. Linking leach chemistry and microbiology of low-grade copper ore bioleaching at different temperatures. Int. J. Min. Met. Mater. 3, 271-279.
- LEVEBSPIEL, O.J., 1999. Chemical reaction engineering. John Wiley and Sons, N.Y, USA
- LIDDELL, K.C., 2005. Shrinking core models in hydrometallurgy: What students are not being told about the pseudosteady approximation. Hydrometallurgy 79, 62–68.
- MALMSTRÖM, M.E., BERGLUND, S., JARSJÖ, J., 2008. Combined effects of spatially variable flow and mineralogy on the attenuation of acid mine drainage in groundwater. Appl. Geochem. 23, 1419-1436.
- MAZUELOS, A., ROMOERO, R., RODRÍGUEZ, G, CARRANZA, F.,2001. Ferric iron production in packed bed bioreactors: Influence of ph, temperature, particle size, bacterial support material and type of air distributor. Miner. Eng. 4, 507-514.
- MIKI, H., NICOL, M., VELÁSQUEZ-YÉVENES, L., 2011. The kinetics of dissolution of synthetic covellite, chalcocite and digenite in dilute chloride solutions at ambient temperatures. Hydrometallurgy 105, 321-327.
- MILLER, G.M., 2003. Ore geotechnical effects on copper heap leach kinetics. Hydrometallurgy: Inter. Sympo. TMS.
- NADERI, H., ABDOLLAHY, M., MOSTOUFI, N., 2015. Kinetics of chemical leaching of chalcocite from low-grade copper ore: Size-distribution behavior. J. Min. Env. 6, 109-118.
- NAZEMI, M., RASHCHI, F., MOSTOUFI, N., 2011. A new approach for identifying the rate controlling step applied to the leaching of nickel from spent catalyst. Int. J. Miner. Process. 100, 21-26.
- NIU, X.P., RUAN, R.M., TAN, Q.Y., JIA, Y., SUN, H.Y., 2015. Study on the second stage of chalcocite leaching in column with redox potential control and its implications. Hydrometallurgy 155, 141-152.
- OGBONNA, N., PETERSEN, J., LAURIE, H., 2006. An agglomerate scale model for the heap bioleaching of chalcocite. J. S. Afr. I. Min. Metall. 106, 433-442.
- PÉREZ, K., JELDRES, R.I., NIETO, S., SALINAS-RODRÍGUEZ, E., ROBLES, P., QUEZADA, V., HERNÁNDEZ, J., TORO, N., 2020. Leaching of pure chalcocite in a chloride media using waste water at high temperature. Metals 10, 1-9.
- PÉREZ, K., TORO, N., SALDAÑA, M., SALINAS-RODRÍGUEZ, E., ROBLES, P., TORRES D., JELDRES, R.I., 2020. Statistical study for leaching of covellite in a chloride media. Metals 10, 477.
- PETERSEN, J., DIXON, D.G., 2007. Principles, mechanisms and dynamics of chalcocite heap bioleaching, In Microbial processing of metal sulfides. Springer. 193-218.
- RUIZ, M.C., HONORES, S., PADILLA, R., 1998. Leaching kinetics of digenite concentrate in oxygenated chloride media at ambient pressure. Metall. Mater. Trans. A 29, 961-969.
- SCHIPPERS, A., SAND, W., 1999. Bacterial leaching of metal sulfides proceeds by two indirect mechanisms via thiosulfate or via polysulfides and sulfur. Appl. and Environ. Microbiol. 65, 319.
- STRÖMBERG, B., BANWART, S.A., 1999. Experimental study of acidity-consuming processes in mining waste rock: Some influences of mineralogy and particle size. Appl. Geochem. 14, 1-16.
- SUNI, J., HENEIN, H., WARREN, G.W., Reddy, D., 1989. Modelling the leaching kinetics of a sphalerite concentrate size distribution in ferric chloride solution. Hydrometallurgy 22, 25-38.
- TORO, N., BRICEÑO, W., PÉREZ, K., CÁNOVAS, M., TRIGUEROS, E., SEPÚLVEDA, R., HERNÁNDEZ, P., 2019. Leaching of pure chalcocite in a chloride media using sea water and waste water. Metals 9, 780.
- VIDELA, A.R., LIN, C.L., Miller, J.D., 2007. 3d characterization of individual multiphase particles in packedparticle beds by X-ray microtomography (XMT). Int. J. Miner. Process. 84, 321-326.
- WATLING, H.R., 2006. The bioleaching of sulphide minerals with emphasis on copper sulphides — a review. Hydrometallurgy 84, 81–108.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-5a6a4c7e-0f54-4cca-a8f4-4898a4b91c9e