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technical report on the nechalacho deposit, thor lake project ...

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Based <strong>on</strong> <strong>the</strong> data, Melis Engineering designed a comminuti<strong>on</strong> circuit comprising crushing to -<br />

15 mm followed by rod and ball milling to achieve <strong>the</strong> target grind of 80% passing 38 µm.<br />

The SAGDesign tests showed that <strong>the</strong> ore was amenable to semi-autogenous grinding (SAG)<br />

and this opti<strong>on</strong> may be examined again in future testwork and design studies.<br />

FLOTATION<br />

Numerous open circuit and locked cycle flotati<strong>on</strong> tests have been d<strong>on</strong>e at SGS by Srdjan<br />

Bulatovic of SBM Mineral Processing and Engineering Services Ltd. Testwork is c<strong>on</strong>tinuing but<br />

at <strong>the</strong> time of <strong>the</strong> pre-feasibility study, it had been established through work <strong>on</strong> numerous<br />

samples covering different ore grades and compositi<strong>on</strong>s that <strong>the</strong> flotati<strong>on</strong> flowsheet should<br />

comprise grinding to 80% passing 38 µm, desliming at about 8 µm, <strong>the</strong> removal of magnetic<br />

materials followed by flotati<strong>on</strong>.<br />

The flotati<strong>on</strong> process detailed in <strong>the</strong> pre-feasibility study comprised a partial soluti<strong>on</strong> change,<br />

c<strong>on</strong>diti<strong>on</strong>ing, rougher-scavenger flotati<strong>on</strong>, four stages of counter-current cleaning, and a gravity<br />

upgrading step.<br />

At 18% mass pull to a final c<strong>on</strong>centrate, <strong>the</strong> circuit described above was expected to yield 90%<br />

recovery of zirc<strong>on</strong>ium, 69% recovery of niobium, 63% recovery of tantalum, and 80% recovery<br />

of <strong>the</strong> rare earths and yttrium.<br />

Optimizati<strong>on</strong> of mass pull (affecting c<strong>on</strong>centrate handling and hydrometallurgical operating and<br />

capital costs) vs. recovery (affecting revenue) for <strong>the</strong> c<strong>on</strong>centrator, and <strong>the</strong> evaluati<strong>on</strong> of <strong>the</strong><br />

resp<strong>on</strong>se of o<strong>the</strong>r ore samples will be carried out at <strong>the</strong> Feasibility stage.<br />

Testwork is c<strong>on</strong>tinuing at SGS to evaluate o<strong>the</strong>r ore samples and to fur<strong>the</strong>r increase <strong>the</strong><br />

upgrading effect whilst holding, or improving, recovery levels through <strong>the</strong> rejecti<strong>on</strong> of biotite.<br />

When <strong>the</strong>se tests are completed it is planned to operate a pilot plant comprising grinding, feed<br />

preparati<strong>on</strong>, and flotati<strong>on</strong> to both dem<strong>on</strong>strate <strong>the</strong> process and generate a bulk sample for <strong>on</strong>going<br />

hydrometallurgical work and, eventually, a hydrometallurgical pilot plant.<br />

HYDROMETALLURGY<br />

The minerals in <strong>the</strong> flotati<strong>on</strong> c<strong>on</strong>centrate are chemically refractory – especially zirc<strong>on</strong>. Zirc<strong>on</strong> is<br />

routinely decomposed (cracked) at several operati<strong>on</strong>s around <strong>the</strong> world using fused sodium<br />

hydroxide and this process has been extensively investigated by SGS Mineral Services <strong>on</strong> Thor<br />

Lake material. The tests have shown that caustic cracking will very effectively decompose not<br />

<strong>on</strong>ly <strong>the</strong> zirc<strong>on</strong> but also all o<strong>the</strong>r value-bearing minerals.<br />

Technical Report 43-101 – March 13, 2011 Page 16-2<br />

Prepared by Aval<strong>on</strong> Rare Metals Inc.

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