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Pulacayo Project Feasibility Study - Apogee Silver

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<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 />

25.1.3 Hydrogeology<br />

An in-depth study on the hydrogeological conditions has not been completed on this project<br />

thus far but seeing that this mine is in current operation and was in operation for many years,<br />

underground mine water is not expected to pose a risk to future mining operations. It is<br />

known that old workings are flooded, but the current level of this water is significantly below<br />

the planned lowest level in the new mine. However, this needs to be monitored regularly to<br />

see if there is a trend of rising water. If that occurs, a dewatering scheme will have to be<br />

implemented.<br />

25.1.4 Paste Backfill<br />

The mine design at present includes 100% cemented paste backfill, which is a conservative<br />

approach. Backfill testing has been completed to ascertain a suitable mix design, which<br />

includes 6% cement content. In addition, a reinforced plug at the bottom of each backfill<br />

section has been designed and will be constructed prior to backfilling taking place.<br />

25.1.5 Metallurgy and Mineral Processing<br />

As the material to be processed are mainly sulphides, a flotation method to improve and<br />

optimize the level of lead, zinc and silver recovery was selected. Challenges related to<br />

flotation selectivity and low lead concentrate grades were due to the presence of mixed,<br />

intertwined galena-sphalerite assemblage. The selectivity issue was overcome by selecting<br />

an adequate reagents suite. The consistency of the results obtained at the laboratory level,<br />

combined with higher recoveries, led to the selection of the conventional differential flotation.<br />

Bulk flotation did not render adequate performance (recovery and grade). Reclaimed<br />

process water was pre-treated with activated carbon in order to obtain higher lead<br />

concentrate grades as the carbon adsorbs the dissolved copper ions (Cu 2+ ) present in the<br />

water, which causes pre-activation of sphalerite and pyrite.<br />

The straightforward conventional selective lead-silver flotation (locked cycle tests) show that<br />

good lead recoveries of between 88% and 93% can be achieved with a large variation in<br />

head grade from 1.5% Pb to 4.3% Pb. The silver recoveries range between 67% and 93.5%<br />

with a variation in head grade of between 136 g/t Ag and 375 g/t Ag.<br />

Saleable lead and zinc concentrates can be produced from the <strong>Pulacayo</strong> ore using<br />

conventional mineral processing techniques including crushing, milling and differential<br />

flotation.<br />

For tailings disposal the underflow from the tailings paste thickener will be either sent to the<br />

TSF or used as paste fill for underground stope support. The paste thickener overflow water<br />

will be reclaimed for the plant process water.<br />

Results from metallurgical test work carried out in four stages have been used to guide<br />

process plant design. The <strong>Feasibility</strong> <strong>Study</strong> process comprises crushing, milling and<br />

classification, differential lead and zinc flotation, tailings disposal (tailings storage facility and<br />

cemented paste fill plant) and concentrate dewatering. Although a significant amount of test<br />

work has been completed, additional variability metallurgical tests for process flow circuit<br />

TWP Sudamérica S.A. Av. Encalada 1257 Of. 801, Santiago de Surco Lima 33, Perú (51-1) 4377473<br />

Page 289

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