The current deterioration in the Sebaiya West phosphate flotation plant was
confirmed in the laboratory to be due to inefficient liberation in the - 0
.25 mm ground product and to the presence of calcite gangue mineral. Phosph
oconcentrates assaying from 26.9-27.8% P2O5 with recovery of 50-55% were ob
tained from a nm-of-mine having 20.3% P2O5 using sulfonated fatty acid, pur
e oleic acid or cationic fatty amine acetate-alcohol mixture as a selective
silica collector Double calcite silica flotation gave better results and a
cleaner concentrate assaying 29.2% P2O5 was obtained using H3PO4 as a phos
phate depressant in the former circuit and the sulfonated;fatty acid as a c
ollector. The concentrate grade increased to 30.70% P2O5 by using the catio
nic silica flotation circuit at an overall recovery of about 68%. Fine grin
ding of the flotation feed to less than 0.15 mm followed by desliming on 0.
04 mm screen led to a relative improvement concentrate grade to about 32% P
2O5 but with an overall recovery of 52.8% P2O5,. Super-phospho-concentrates
assaying about 34.8% P2O5 and 1.32% acid insolubles (I.R) were obtained by
double calcite-silica flotation of the -0.1 +0.04 mm finely ground ore but
at an overall recovery of 46.6%. This increased to 72.6% with a correspond
ing decrease in the concentrate grade to about 30% P2O5 by just silica flot
ation only using the sulfonated fatty acid. However, when this single flota
tion step was conducted using the cationic silica collector at pH 8 the con
centrate grade increased to an average 31.5% P2O5 with an overall recovery
of about 67%. Comparative cost estimate of the different flotation regimes
indicated that the cationic silica flotation of the finely ground Sebayia W
est phosphate is the least expensive with total reagents costs of only 1.71
Sit less than half the current cost of the plant using the agricultural by
-product rice bran oil without taking into account the grinding costs of th
e ore to less than 0.1 mm.