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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 />

17.1.12 Plant Layout<br />

The plant layout was developed from the basic process design criteria. These criteria<br />

defined the required steps to treat the ore received from the mining operations to produce<br />

acceptable concentrates for dispatch.<br />

The process plant steps were set out for the given site conditions, and the required<br />

infrastructure and services were added. The plant layout was constrained by a series of<br />

factors:<br />

<br />

The conveyor lengths required to reach the required heights of their respective<br />

discharge points<br />

<br />

Ground conditions.<br />

o<br />

o<br />

o<br />

The layout was then optimized in respect of the following:<br />

To reduce piping distances; and to position unit process steps, taking<br />

advantage of the site contours, to minimize the bulk earthworks and terracing<br />

required<br />

Evaluated for maintenance requirements, and the necessary access provided<br />

for the all the process equipment.<br />

The support facilities for operations were then integrated into the plant design. The change<br />

house facilities are located to the entrance to the concentrator area.<br />

The support functions for workshop, stores, reagent make-up and laboratory are located on<br />

the east side of the process area to allow easy and close access to the main plant sections<br />

The collection and delivery of the products have been optimized in terms of the in-plant road<br />

systems and layouts.<br />

Consideration was also made in the plant layout for future expansions and increases in the<br />

<strong>Pulacayo</strong> plant production. Consequently, these planned future plant expansions can be<br />

constructed without interference to the operations, except for final plant tie-ins and hot<br />

commissioning.<br />

17.1.13 Control Philosophy<br />

17.1.13.1 Process Plant Control Philosophy<br />

Standard process control equipment such as flow meters, level detectors, density gauges<br />

will provide important information on performance of the process plant. The mill will have a<br />

variable speed drive for start-up and speed adjustment and the float section pumps will also<br />

have variable speed drives to control the flow through the section. The paste thickener will<br />

be furnished with a dedicated PLC.<br />

17.1.13.2 Control Systems<br />

For all instruments located in the process plant, control system will be locally, there is no<br />

central control system. Main equipment such as cone crusher, jaw crusher, ball mills and the<br />

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

Page 180

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