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Effect of air flow rate and froth depth on the flotation performance : an industrial case study in a 10 m3 cell

Treść / Zawartość
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The main purpose of the froth zone in flotation is to transport all the valuable particles from the pulp zone into the concentrate. However, in practice, a complete recovery of these particles is rarely achieved since some of them are detachment from the bubbles and return to the pulp zone. While this is an important topic in the mineral flotation industry, the previously published papers are mainly limited to small laboratory scales. Therefore, this study aimed to examine the effect of two main flotation variables (air flowrate and froth depth) on the flotation of iron ore in a 10 m3 industrial scale cell. It was found that, when the air flowrate increased from 45 to 146 m3/h, the velocity of the bubble coalescence also increased. In addition, when the froth depth increased from 5 to 30 cm, the product grade showed on average 2 unit increase (for instance, from 12% to 14%) due to the detachment of particles and liquid drainage. It was also found that the flotation concentrates recovery decreased with the increasing froth depth and air flowrate.
Słowa kluczowe
Rocznik
Strony
art. no. 154852
Opis fizyczny
Bibliogr. 24 poz., rys., tab., wykr.
Twórcy
  • Iranian Mines & Mining Industries Development & Renovation Organization (IMIDRO), Tehran, Iran
  • Process Optimisation for Future, Adelaide, Australia
  • Iranian Mines & Mining Industries Development & Renovation Organization (IMIDRO), Tehran, Iran
  • School Mining Engineering, College of Engineering, University of Tehran, Tehran, Iran
Bibliografia
  • ARANCIBIA-BRAVO, M.P., LUCAY, F.A., LOPEZ, J., CISTERNAS, L.A., 2019. Modeling the effect of air flow, impeller speed, frother dosages, and salt concentrations on the bubbles size using response surface methodology. Minerals Engineering, 132, 142–148.
  • ATA, S., AHMED, N., JAMESON, G.J., 2003. A study of bubble coalescence in flotation froths. International Journal of Mineral Processing, 72, 255–266.
  • ATA, S., 2009. The detachment of particles from coalescing bubble pairs. Journal of Colloid & Interface Science, 338, 558–565.
  • ATA, S., 2012. Phenomena in the froth zone of flotation- A review. International Journal of Mineral Processing, 102-103, 1–12.
  • BOURNIVAL, G., ATA, S., 2010. Packing of particles on the surface of bubbles. Minerals Engineering, 23, 111–116.
  • CASTRO, S., MIRANDA, C., TOLEDO, P., LASKOWSKI, J.S., 2013. Effect of frothers on bubble coalescence and foaming in electrolyte solutions and seawater. International Journal of Mineral Processing, 124, 8-15.
  • CILEK, E.C., UMUCU, Y., 2001. A statistical model for gangue entrainment into froths flotation of supplied ores. Minerals Engineering, 14, 9, 1055-1066.
  • CILEK, E.C., 2009. The effect of hydrodynamic conditions on true flotation and entrainment in flotation of a complex sulphide ore. International Journal of Mineral Processing, 90, 35-44.
  • FALUTSU, M., 1994. Column flotation froth characteristics - stability of the bubble–particle system. International Journal of Mineral Processing, 40, 3–4, 225–243.
  • GORAIN, B., ORAVAINEN, H., ALLENIUS, H., PEAKER, R., WEBER, A., AND TRACYZK, F., 2009. Mechanical froth flotation cells. In Froth Flotation a Century of Innovation. Fuerstenau, M. C., Jameson, G. J., Yoon (Eds), Society for Mining, Metallurgy, and Exploration, SME, Colorado, 709-710.
  • FARROKHPAY, S., 2011. The significance of froth stability in mineral flotation - A review. Advances in Colloid and Interface Science, 166, 1–7.
  • IRELAND, P.M., 2009. Coalescence in a steady-state rising foam. Chemical Engineering Science, 64 (23), 4866–4874.
  • LANGEVIN, D., 2015. Bubble coalescence in pure liquids and in surfactant solutions. Current Opinion in Colloid & Interface Science, 20, 92–97.
  • MAVROS, P., MATIS, K.A., 1992. Innovations in Flotation Technology. NATO Science Series E: (NSSE, volume 208), Mavros, P. and Matis, K.A. (Eds), Spring Science, Greece.
  • NEETHLING, S.J., CILLIERS, J.J., 2002. Solids motion in flowing froths. Chemical Engineering Science, 57, 4, 607–615.
  • OSTADRAHIMI, M., FARROKHPAY, S., GHARIBI, K., DEHGHANI, A., 2019. Estimating bubble loading in industrial flotation cells. Minerals, 9, 222.
  • OSTADRAHIMI, M., FARROKHPAY, S., GHARIBI, K., DEHGHANI, A., 2021. Effects of operating parameters on the froth and collection zone recovery in flotation: An industrial case study in a 10 m3 cell. Minerals, 11, 494.
  • PAL, R., MASLIYAH, J., 1990. Flow in froth zone of a flotation column. Canadian Metallurgical Quarterly, 29(2), 97–103.
  • SEAMAN, D.R., MANLAPIG, E.V., FRANZIDIS, J.P., 2006. Selective transport of attached particles across the pulp–froth interface. Minerals Engineering, 19, 841-851.
  • STEVENSON, P., 2006. Dimensional analysis of foam drainage. Chemical Engineering Science, 61, 14, 4503–4510.
  • WANG, P., CILLIERS, J.J., NEETHLING, S.J., BRITO-PARADA, P.R., 2019. The behavior of rising bubbles covered by particles. Chemical Engineering Journal, 365, 111–120.
  • YIANATOS, J.B., MOYS, M. H., CONTRERAS, F., VILLANUEVA, A., 2008. Froth recovery of industrial flotation cells. Minerals Engineering, 21, 817- 825.
  • YIANATOS, J., VALLEJOS, P., MATAMOROS. C., DÍAZ, F., 2018. Froth liquid transport in a two-dimensional flotation cell. Minerals Engineering, 122, 227–232.
  • ZHANG, W., 2016. The effects of frothers and particles on the characteristics of pulp and froth properties in flotation- A critical review. Journal of Minerals and Materials Characterization and Engineering, 4, 251-269.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-c618bc50-eb5a-4496-b3bd-7b74a03adfed
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