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The role of ore properties (density, particle size, and mineralogy) in thickening process was studied in this research. The shaking table was used to prepare the sample for the tests. The tailings were continuously fed on the table by gravity to separate the tailings in three products as slime, middling and coarse particles. The solid density and particle size of the samples were different. To study the effect of mineralogical properties, the sedimentation behavior of the feed and middling samples were tested. The results showed that the free settling velocity of the feed (2–6 mm/s) was less than that of the middling sample (18–23 mm/s), and the compressibility of middling (density: 0.63–0.86 Mg/m3) was more than that of feed (density: 0.33–0.47 Mg/m3). This was due to the amount of clay reduction in the middling sample. The sedimentation behavior of the slime and the coarse samples were also compared in order to study the effect of particle size and density. The settling velocity of the slime and the coarse particles was obtained as 0.1-0.4 and 26 mm/s, respectively, and the maximum underflow density were obtained as 0.35 and 1.57 Mg/m3, respectively. Therefore, the particle size and density reduction reduced the thickener performance. In order to study the effect of particle size, the sedimentation behavior of the slime and coarse samples were compared, and it was obtained that the settling velocity and underflow density increased with the increasing in the particle size.
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Tom
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783--794
Opis fizyczny
Bibliogr. 24 poz., rys.
Twórcy
autor
- Department of Mining Engineering, Science and Research branch, Islamic Azad University, Tehran, Iran
autor
- University of Tehran, Tehran, Iran
autor
- University of Tehran, Tehran, Iran
autor
- Department of Mining Engineering, Science and Research branch, Islamic Azad University, Tehran, Iran
Bibliografia
- 1. BURGER R., BUSTOS M.C., CONCHA F., 1999, Settling velocities of particulate systems: 9. Phenomenological theory of sedimentation processes: numerical simulation of the transient behavior of flocculated suspensions in an ideal batch or continuous thickener, International Journal of Mineral Processing, 55, 267–282.
- 2. BUSCALL R., MCGOWAN I.J., MILLS P.D.A., STEWART R.F., SUTTON D., WHITE L.R., YATES G.E., 1987, The Rheology of strongly flocculated suspensions, Non-Newtonian Fluid Mechanics, 24, 183–202.
- 3. BUSTOS M.C., CONCHA F., BURGER R., TORY E.M., 1999, Sedimentation and Thickening, Kluwer Academic Publishers, Dordrecht, Netherlands, 285.
- 4. COE H. S., CLEVENGER G. H., 1916, Methods for determining the capacities of slime thickening tanks, Trans AIME, 55, 356–384.
- 5. CONCHA F., BUSTOS M.C., BARRIENTOS A., 1996, Phenomenological Theory of Sedimentation, Chapter 3 in Sedimentation of small particles in a viscous Fluid, Computational Mechanics Publications, Southampton, UK, 51-96.
- 6. DAHLSTORM D.A., FITCH E.B., 1985, Mineral Processing Handbook, N.L. Wiess (ed), SME/AIME, Chapter 9, 2-14.
- 7. DEVENTER B.G., USHER S.P., KUMAR A., RUDMAN M., SCALES P.J., 2011, Aggregate densification and batch settling, Chemical Engineering Journal, 171, 141–151.
- 8. GARRIDO P., BURGOS R., CONCHA F., BURGER R., 2003, Software for the design and simulation of gravity thickeners, Minerals Engineering, 16, 85–92.
- 9. GARRIDO P., CONCHA F., BURGER R., 2003, Settling velocities of particulate systems: 14. Unified model of sedimentation, centrifugation and filtration of flocculated suspensions, International Journal of Mineral Processing, 72, 57–74.
- 10. GLADMAN B.R., RUDMAN M., SCALES P.J., 2010, Experimental validation of a 1-D continuous thickening model using a pilot column, Chemical Engineering Science, 65, 3937–3946.
- 11. GREEN M.D., 1997, Characterization of suspensions in settling and compression, PhD thesis, Department of Chemical Engineering, University of Melbourne Parkville Victoria 3052, Australia.
- 12. KELLY E.G., SPOTISSWOOD D.G., 1989, Introduction to Mineral Processing, Mineral Engineering Services, Denver.
- 13. KYNCH G. J., 1952, a theory of sedimentation, Trans Faraday Society, 48, 166–176.
- 14. LANDMAN K.A., WHITE L.R., BUSCALL R., 1988, The Continuous-flow gravity thickener: Steady State Behavior, AIChE Journal, 34, 239–252.
- 15. LESTER D.R., RUDMAN M., SCALES P.J., 2010, Macroscopic dynamics of flocculated colloidal suspensions, Chemical Engineering Science, 65, 6362–6378.
- 16. MCFARLANE A., BREMMELL K., ADDAIMENSAH J., 2005, Microstructure, rheology and dewatering behavior of smectite dispersions during orthokinetic flocculation, Minerals Engineering, 18, 1173.
- 17. OLTMANN H.H, 1975, Filtration and Separation, 12, 6, 636.
- 18. OSBORNE D.G., 1977, Solid-Liquid Separation, Chapter 5, L. Svarovsky (ed), Butterworth, London, Boston, 75–99.
- 19. TALMAGE W. P., FITCH E.B., 1955, Industrial and Engineering Chemistry, 47, 38.
- 20. USHER S.P., SCALES P.J., 2005, Steady state thickener modeling from the compressive yield stress and hindered settling function, Chemical Engineering Journal, 111, 253–261.
- 21. USHER S.P., SPEHAR R., SCALES P.J., 2009, Theoretical analysis of aggregate densification: Impact on thickener performance, Chemical Engineering Journal, 151, 202–208.
- 22. WILHELM J. H., NAIDE Y., 1981, Sizing and operating continuous thickeners, Mining Engineering, 1710–1718.
- 23. YALCIN T., 1988, Bulletin of the Canadian Institute of Metallurgy, 81, 910, 69.
- 24. YOSHIOKA N., HOTTA Y, TANAKA S., NAITO S., TONGAMI S. 1957, Continuous thickening of homogeneous slurries, Chemical Engineering, Tokyo, 21, 66-74.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-f5981fbb-c54d-4ab2-94d6-b2ef1109f222
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