Process of leaching gold
View Patent ↗A process of leaching gold comprising the steps of: a) leaching copper from copper sulfide ore material that contains gold or contains silicate ore containing gold until the copper grade is reduced to 7.9 wt % or less; b) mixing the resulting material having a copper grade of 7.9 wt % or less with a gold leaching solution selected from the group consisting of a first solution containing chloride ions and ferric ions, and a second solution containing chloride ions and iron ions, the iron ions having been oxidized to trivalent ferric ions by air bubbled into the second solution; c) adjusting the pH of the gold leaching solution to 1.9 or less with stirring to leach at least gold in the material into the gold leaching solution by the oxidative activity of the ferric ions contained in the gold leaching solution, wherein the concentration of gold is reduced by selectively removing gold from part or all of the gold leaching solution during gold leaching. This process efficiently leaches at least copper and gold from a copper sulfide ore.
1. A process of leaching gold comprising the steps of:
a) leaching copper from copper sulfide ore material that contains gold or contains silicate ore containing gold until the copper grade is reduced to 7.9 wt % or less;
b) mixing the resulting material having a copper grade of 7.9 wt % or less with a gold leaching solution selected from the group consisting of a first solution containing chloride ions and ferric ions, and a second solution containing chloride ions and iron ions, the iron ions having been oxidized to trivalent ferric ions by air bubbled into the second solution; and
c) adjusting the pH of the gold leaching solution to 1.9 or less with stirring to leach at least gold in the material after step b) into the gold leaching solution by the oxidative activity of the ferric ions contained in the gold leaching solution, wherein the concentration of gold is reduced by selectively removing gold from part or all of the gold leaching solution by adding activated carbon to the gold leaching solution during gold leaching, and optionally adding lead nitrate.
2. A process of leaching gold comprising the steps of:
a′) leaching copper from copper sulfide ore material that contains gold or contains silicate ore containing gold until the copper grade is reduced to 7.9wt % or less by a leaching solution containing chloride ions and iron ions to form a third solution (hereafter called “gold leaching solution”);
b′) oxidizing the gold leaching solution by bubbling with air to oxidize iron ions into trivalent ferric ions by the action of oxygen contained in the air; and
c) adjusting the pH of the gold leaching solution to 1.9 or less with stirring to leach at least gold in the material after step b′) into the gold leaching solution by the oxidative activity of the ferric ions contained in the gold leaching solution, wherein the concentration of gold is reduced by selectively removing gold from part or all of the gold leaching solution by adding activated carbon to the gold leaching solution during gold leaching, and optionally adding lead nitrate.
3. The process according to claim 1 or 2 , wherein the gold leaching solution contains copper ions.
4. The process according to claim 1 or 2 , wherein the gold leaching solution contains bromide ions.
5. The process according to claim 1 or 2 , wherein the gold leaching solution contains iron ions in a concentration of 0.01 g/l or more.
6. The process according to claim 1 or 2 , further comprising bubbling the gold leaching solution with air which oxidizes divalent iron ions into trivalent iron ions during said stirring.
7. The process according to claim 1 or 2 , wherein the gold leaching solution contains chloride ions and bromide ions in a concentration of 120 g/L to 200 g/L in total.
8. The process according to claim 1 or 2 , wherein a leaching temperature is 60° C. or more.
9. The process according to claim 1 or 2 , further comprising comminuting the material until 80% or more of the material have a particle size of 40 μm or less before starting step a) or before starting step a′).