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Table 18-12 (C<strong>on</strong>t’d) Principal Process Design Criteria<br />

Aval<strong>on</strong> Rare Metals Inc. – Thor Lake Project<br />

Principal Process Design Criteria<br />

Hydrometallurgical Plant<br />

Operating time hr/a 7,582<br />

Processing rate – initial Tph 8.7<br />

Processing rate – expansi<strong>on</strong> Tph 17.4<br />

Acid bake temperature °C 250<br />

Acid additi<strong>on</strong> kg/t c<strong>on</strong>centrate 700<br />

Caustic crack temperature °C 600<br />

Net caustic additi<strong>on</strong> kg/t c<strong>on</strong>centrate 140<br />

Post double salt precipitati<strong>on</strong> SX feed rate m 3 /h - initial throughput 41.5<br />

Post double salt precipitati<strong>on</strong> SX feed rate m 3 /h - expansi<strong>on</strong> throughput 83<br />

(All SX units sized for expansi<strong>on</strong>, some driers added for<br />

expansi<strong>on</strong>)<br />

Recovery to final products % ZrO 2 in c<strong>on</strong>centrate 90<br />

Sulphuric Acid Plant<br />

% TREO in c<strong>on</strong>centrate 93<br />

% HREO in c<strong>on</strong>centrate 93<br />

% Nb 2 O 5 in c<strong>on</strong>centrate 80<br />

% Ta 2 O 5 in c<strong>on</strong>centrate 50<br />

Annual average capacity – initial tpd 100% acid 350<br />

Annual average capacity – expansi<strong>on</strong> tpd 100% acid 700<br />

(Initial plant is built to handle expansi<strong>on</strong> t<strong>on</strong>nage and<br />

additi<strong>on</strong>s not required)<br />

Technical Report 43-101 – March 13, 2011 Page 18-38<br />

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

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