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Laterite Leach Tests

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ANSTO Minerals Report C1206 to Lagoon Creek Resources – Westmoreland Deposits<br />

(iii) Effect of ORP<br />

The effect of oxidation potential is shown in Figure 4.10 for Junnagunna and Figure 4.11 for<br />

Redtree. In both cases, similar final uranium extraction results were achieved for leaching at<br />

ORP levels of 500-550 mV. Uranium extraction decreased when leaching at 450 mV.<br />

Addition of 1.0 g/L ferric ion at 500 had a slight impact on the rate of extraction, but there<br />

was little difference after 12 h. A similar result was achieved by leaching at 550 mV, and this<br />

approach would be preferred to adding iron.<br />

U Extraction (%)<br />

100<br />

95<br />

90<br />

85<br />

80<br />

75<br />

70<br />

65<br />

60<br />

0 5 10 15 20 25<br />

Time (h)<br />

550 mV (LC5 C) 500 mV and ferric (LC8 B) 500 mV (LC3 A) 450 mV (LC6 A)<br />

FIGURE 4.10 Effect of ORP on the <strong>Leach</strong>ing of Junnagunna Composite<br />

U Extraction (%)<br />

100<br />

95<br />

90<br />

85<br />

80<br />

75<br />

70<br />

65<br />

60<br />

0 5 10 15 20 25<br />

Time (h)<br />

550 mV (LC6 B) 500 mV and ferric (LC8 C) 500 mV (LC3 B) 450 mV (LC6 C)<br />

FIGURE 4.11 Effect of ORP on the <strong>Leach</strong>ing of Redtree Composite<br />

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