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

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In a typical test, for example CCr-27, c<strong>on</strong>centrate was treated with sodium hydroxide at 600°C<br />

for three hours, cooled, <strong>the</strong>n water washed to remove excess sodium hydroxide and <strong>the</strong><br />

phosphates and silicates formed in <strong>the</strong> cracking process. The solids were <strong>the</strong>n leached with<br />

hydrochloric acid and yielded 96% zirc<strong>on</strong>ium extracti<strong>on</strong> and more than 96% solubilizati<strong>on</strong> of <strong>the</strong><br />

rare earths.<br />

O<strong>the</strong>r approaches to <strong>the</strong> caustic cracking process have been investigated including cracking<br />

tests using sodium carb<strong>on</strong>ate, cracking in an autoclave using str<strong>on</strong>g caustic soluti<strong>on</strong>, cracking in<br />

<strong>the</strong> presence of reductants, and low temperature attriti<strong>on</strong> milling with sodium hydroxide. Some<br />

of <strong>the</strong>se tests provided encouraging results and fur<strong>the</strong>r tests have been planned.<br />

Ano<strong>the</strong>r approach to cracking refractory minerals is acid baking in which <strong>the</strong> feed material is<br />

mixed with c<strong>on</strong>centrated sulphuric acid and held at a temperature of 200°C or more for a few<br />

hours. This method is widely used in China for decomposing <strong>the</strong> rare earth c<strong>on</strong>centrates from<br />

Bayan Obo and elsewhere.<br />

SGS has investigated <strong>the</strong> use of acid baking for <strong>the</strong> Thor Lake c<strong>on</strong>centrate and it has been<br />

seen to solubilize about 80% of <strong>the</strong> light rare earths and 50% of <strong>the</strong> heavy rare earths. Zirc<strong>on</strong><br />

extracti<strong>on</strong> is minimal, less than 4%, even under extreme acid bake c<strong>on</strong>diti<strong>on</strong>s clearly indicating<br />

<strong>the</strong> refractory nature of zirc<strong>on</strong>.<br />

SGS Mineral Services has also investigated <strong>the</strong> use amm<strong>on</strong>ium sulphate or amm<strong>on</strong>ium chloride<br />

as acid baking reagents. Some elements were extracted but no fur<strong>the</strong>r work is planned.<br />

A combinati<strong>on</strong> of acid baking and caustic cracking has also been investigated and shown to<br />

offer high recoveries and preferred reagent c<strong>on</strong>sumpti<strong>on</strong> levels and operating costs. As<br />

<str<strong>on</strong>g>report</str<strong>on</strong>g>ed in <strong>the</strong> previous Technical Report, extracti<strong>on</strong>s under favourable c<strong>on</strong>diti<strong>on</strong>s are typified<br />

by <strong>the</strong> results of AB-19 in which overall zirc<strong>on</strong>ium recovery was 99%, overall light rare earth<br />

(lanthanum, cerium and neodymium) extracti<strong>on</strong> was 98%, and extracti<strong>on</strong> of <strong>the</strong> heavy rare<br />

earths and yttrium was 99%. Niobium extracti<strong>on</strong> was 83%<br />

Although it is clear that a very effective process for solubilizing <strong>the</strong> valuable elements in <strong>the</strong><br />

Thor Lake c<strong>on</strong>centrate had been identified, testwork is c<strong>on</strong>tinuing at SGS Mineral Services to<br />

fur<strong>the</strong>r define <strong>the</strong> process parameters and optimize <strong>the</strong> flowsheet for <strong>the</strong> initial solubilizati<strong>on</strong><br />

step.<br />

Extracting valuable elements from <strong>the</strong> refractory minerals of <strong>the</strong> c<strong>on</strong>centrate is a key part of <strong>the</strong><br />

hydrometallurgical process. Once <strong>the</strong> elements of interest are in soluti<strong>on</strong>, it is necessary to<br />

separately recover <strong>the</strong> zirc<strong>on</strong>ium, rare earths, yttrium, niobium and tantalum and this has been<br />

investigated in <strong>the</strong> laboratory. The flowsheet that was selected for <strong>the</strong> pre-feasibility study<br />

Technical Report 43-101 – March 13, 2011 Page 16-3<br />

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

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