Pulacayo Project Feasibility Study - Apogee Silver
Pulacayo Project Feasibility Study - Apogee Silver
Pulacayo Project Feasibility Study - Apogee Silver
You also want an ePaper? Increase the reach of your titles
YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.
<strong>Pulacayo</strong> 1 000 t/d Phase I <strong>Feasibility</strong> <strong>Study</strong> - NI 43-101 Technical Report<br />
090644-3-0000-20-IFI-100<br />
rougher cell (Imhoflot G cell 1.4, 0400-CL-001/6) and the tailings are directed to the zinc<br />
rougher/scavenger cell (Imhoflot G cell 1.4, 0400-CL-002/7). Similarly, the zinc<br />
rougher/scavenger cell tailings are sent to the zinc scavenger cell (Imhoflot G cell 1.4, 0400-<br />
CL-003/8).<br />
The zinc scavenger tailings are pumped to the paste thickener (backfill area). The zinc<br />
rougher, rougher/scavenger and scavenger concentrates are directed to the zinc cleaner<br />
circuit. Hydrated lime and Aero 3418A collector are added into the cleaner feed pump boxes<br />
(0400-PB-006/8 and 0400-PB-014/16). The zinc cleaner circuit has two flotation cells in<br />
series (two Imhoflot G cell 0.8, 0400-CL-004/9, 0400-CL-005/10).<br />
The final zinc concentrate flows to zinc concentrate surge tank (0400-TK-002) and it is<br />
pumped to the zinc recessed plate pressure filter for dewatering.<br />
17.1.5 Carbon Columns Area<br />
The lead concentrate filter filtrate, zinc concentrate filter filtrate, paste thickener overflow and<br />
run-off water report to three carbon in column (CIC) tanks in series where the copper ions<br />
and organic flotation reagents is adsorbed onto 6 x 12 mesh granular coconut carbon. The<br />
train of CIC tanks is made up of three 2 m diameter x 1 m high columns. The CIC treated<br />
solution water is pumped to the process water tank (1200-TK-006).<br />
17.1.6 Concentrate Filtration Area<br />
Lead concentrate slurry is pumped to the lead concentrate pressure filter, the filter size is<br />
1.4 m x 7.59 m (W x L). The dewatered concentrate (< 10% moisture) is discharged through<br />
a chute onto a belt conveyor and conveyed to the lead concentrate stockpile.<br />
The filtrate solution drains to a pump box and is pumped to the CIC system to adsorb<br />
dissolved metal ions that might be present in solution. The lead concentrate filter section<br />
floor spillage is pumped with the sump pump to the mill discharge pump box.<br />
Zinc concentrate slurry is pumped to the zinc concentrate pressure filter, the filter size is<br />
1.4 m x 8.58 m (W x L). The dewatered concentrate (< 10% moisture) is discharged through<br />
a chute onto a belt conveyor and conveyed to the zinc concentrate stockpile. The filtered<br />
solution is recovered in the pump box, and sent to the CIC system to adsorb the dissolved<br />
metal ions that might be present in solution.<br />
The zinc concentrate filter section floor spillage is pumped with a pump sump to the zinc<br />
section conditioning tank. A vehicle weighbridge will be used to determine the mass of<br />
concentrates dispatched.<br />
17.1.7 Backfill Area<br />
The final zinc flotation tailings slurry is pumped through a series of pumps to an 8.4 m<br />
diameter paste thickener. The thickener overflow reports to flushing water tank (1500-TK-<br />
001), this tank will provide water for piping flushing, to the high shear mixing tank (1500-TK-<br />
004) and to the plant process water tanks. The excess water is pumped to a series of the<br />
carbon columns to adsorb dissolved metal ions and organic flotation reagents before<br />
reporting to the plant process water tanks. The paste thickener underflow is either pumped<br />
TWP Sudamérica S.A. Av. Encalada 1257 Of. 801, Santiago de Surco Lima 33, Perú (51-1) 4377473<br />
Page 174