The integration of flotation columns into existing flotation circuits of co
nventional mechanical cells is becoming increasingly common in industry. Ne
vertheless, the study of column circuit configuration is scarce and problem
s relating to the selection of the appropriate circuit have not been addres
sed.
Various column circuits for flotation of coal fines have been experimentall
y examined and theoretically analyzed in the present study to reveal the ef
fect of circuit configuration on the overall circuit performance evaluated
using separation efficiency and separation curves. The flotation circuits e
xamined in this study included single-stage (SS), rougher-scavenger (RS), r
ougher-cleaner (RC), rougher-scavenger-scavenger cleaner (RSSC), roogher-sc
avenger-cleaner (RSC), and rougher-cleaner-recleaner (RCRC). The flotation
tests were carried out with the Pittsburgh No. 8, Illinois No. 6 and Upper
Freeport coal samples that were precleaned using conventional flotation. It
has been demonstrated that the overall separation efficiency of the column
flotation system was rather insensitive to circuit arrangements due to the
unique characteristics of the unit flotation column distinguished from the
conventional flotation cell. The flotation separation efficiency changed w
ith ash or sulfur rejection and the Pittsburgh No. 8 and Illinois No. 6 coa
l samples showed a stronger dependence of separation efficiency on ash reje
ction than the Upper Freeport coal sample. The experimental results were sh
own to be in good agreement with theoretical circuit analysis conclusions.
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