Hydrodynamic and kinetic characterization of industrial columns in rougher circuit |
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| Authors: | M Massinaei M Kolahdoozan M Noaparast M Oliazadeh J Yianatos R Shamsadini M Yarahmadi |
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| Affiliation: | 1. Faculty of Engineering, Department of Mining Engineering, University of Birjand, Birjand, Southern Khorasan Province 97175 376, Iran;2. Department of Mining Engineering, University of Tehran, P.O. Box 14395-515, Tehran, Iran;3. Chemical Engineering Department, Santa María University, P.O. 110-V, Valparaíso, Chile;4. National Iranian Copper Industries Company (N.I.C.I.Co.), Kerman, Iran;1. Automation and Supervision Centre for Mining Industry, CASIM, Department of Chemical and Environmental Engineering, Federico Santa Maria Technical University, P.O. Box 110-V, Valparaíso, Chile;2. Nuclear Trace and Engineering Ltd., Santiago, Chile;1. Automation and Supervision Centre for Mining Industry (CASIM), Department of Chemical and Environmental Engineering, Federico Santa Maria Technical University, P.O. Box 110-V, Valparaíso, Chile;2. Department of Mining and Materials Engineering, McGill University, 3600 University, Montreal, QC H3A 0C5, Canada;3. Nuclear Trace and Engineering Ltd., Santiago, Chile |
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| Abstract: | In the present investigation the relationship between collection zone rate constant (kc) and gas dispersion parameters, viz. bubble size (db), superficial gas velocity (Jg), gas hold-up (εg) and bubble surface area flux (Sb) was evaluated. Experiments were conducted in an industrial (4 m in diameter and 12 m high) and a pilot (0.1 m in diameter and 4 m high) flotation column in rougher circuit at Miduk copper concentrator in Iran. Gas hold-up was measured using pressure difference technique and mean bubble sizes were estimated from a drift flux analysis. It was found that the collection zone rate constant was not correlated with db and Jg solely but was linearly dependent on εg and Sb for the range of interest. Collection efficiency (Ek) and floatability factor (P) in the industrial columns were quantified (Ek = 3.1%; P = 7.7 × 10?3). The influence of operating parameters comprising superficial gas velocity, slurry solids% and frother dosage/type on Sb and flotation kinetics was discussed. Analysis of available industrial data suggested that Sb and εg were related by Sb = 4.46εg over the range 30 < Sb < 60 s?1 and 7% < εg < 14%. |
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