| نویسندگان | Mohammad Massinaei,,,,Yianatos Juan,, |
| نشریه | Minerals Engineering |
| شماره صفحات | 357-365 |
| شماره سریال | 22 |
| شماره مجلد | 22 |
| نوع مقاله | Full Paper |
| تاریخ انتشار | 2009 |
| رتبه نشریه | ISI |
| نوع نشریه | چاپی |
| کشور محل چاپ | ایران |
| نمایه نشریه | JCR،Scopus |
| کلید واژه ها | Froth flotation, Flotation kinetics, Flotation bubbles, Flotation machines |
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چکیده مقاله
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 (eg) 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 eg and Sb for the range of interest. Collection efficiency
(Ek) and floatability factor (P) in the industrial columns were quantified (Ek = 3.1%; P = 7.7 103). 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 eg were related by Sb = 4.46eg over the range 30 < Sb < 60 s1 and 7% < eg < 14%.
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