Process for recovering gold and silver from refractory ores

• US 7,922,788 B2
• Filed: 09/11/2008
• Issued: 04/12/2011
• Est. Priority Date: 09/18/2007
• Status: Active Grant

• Current Assignee: Barrick Gold Corporation
• Original Assignee: Barrick Gold Corporation
• Inventors: Gorain, Barun, Hillier, Daniel, McMullen, Jacques
• Primary Examiner(s): Wyszomierski; George
• Assistant Examiner(s): MCGUTHRY BANKS, TIMA MICHELE
• Application Number:
  US12/208,968
• Publication Number:
  US 20090074607A1
• Time in Patent Office: 943 Days
• Field of Search: 757/11, 205/571, 423/26, 209/164
• US Class Current: 75/711
• CPC Class Codes: B03D 1/02 Froth-flotation processes
• CPC Class Codes: B03D 1/1456 Feed mechanisms for the slurry
• CPC Class Codes: C22B 1/00 Preliminary treatment of ores or scrap
• CPC Class Codes: C22B 11/00 Obtaining noble metals
• CPC Class Codes: C22B 11/08 by cyaniding
• CPC Class Codes: Y02P 10/20 Recycling

Abstract

The present invention is directed to flotation of refractory gold sulfide ores in which the ore is ground, floated, the tailings reground, and refloated to produce gold-bearing concentrates.

Claims

1. A method, comprising:

(a) providing a refractory feed material, the refractory feed material comprising gold, sulfides, a carbonaceous preg robbing component, and a clay;

(b) comminuting the refractory feed material to form a comminuted feed material having a first size distribution;

(c) during comminuting, adjusting chemical conditions of the refractory feed material by adding a sulfide activator and a polymeric clay dispersant;

(d) after the comminuting step (b), contacting the comminuted feed material with a carbonaceous component depressant, collector, and frother;

(e) floating the comminuted feed material, in the presence of the sulfide activator, the polymeric clay dispersant, the collector, the frother, and the carbonaceous component depressant, at a pH ranging from about pH 3.5 to about pH 6.5, and at an Eh ranging from about 25 to about 100 millivolts, to form first and second fractions, the first and second fractions each comprising at least some of the gold and sulfides in the refractory feed material;

(f) comminuting the second fraction to provide a comminuted second fraction, the comminuted second fraction having a second size distribution finer than the first size distribution;

(g) during comminuting, adjusting chemical conditions of the second fraction by adding the sulfide activator and polymeric clay dispersant;

(h) after the comminuting step (f), contacting the comminuted second fraction with the carbonaceous component depressant, collector, and frother; and

(i) further floating the comminuted second fraction, in the presence of the polymeric clay dispersant, the sulfide activator, the collector, the frother, and the carbonaceous component depressant, at a pH ranging from about 3.5 to about pH 6.5, and at an Eh ranging from about 25 to about 100 millivolts, to produce third and fourth fractions, the third fraction comprising at least most of the gold and sulfides in the second fraction.

2. The method of claim 1, wherein, in steps (b) and (f), the refractory feed material and second fraction, respectively, are wet milled and wherein the sulfide activator and polymeric clay dispersant are added during each of steps (b) and (f).

3. The method of claim 2, wherein the sulfide activator is a metal salt selected from the group consisting essentially of copper salts, lead salts, and mixtures thereof, wherein the first size distribution is a P₈₀ size ranging from about 100 to about 200 microns, wherein the second size distribution is a P₈₀ size ranging from about 25 to about 100 microns, wherein an amount of sulfide activator added during steps (b) and (f) is insufficient to oxidize substantially the collector.

4. The method of claim 2, wherein the collector is an anionic collector and further comprising before step (e):

after step (b) and before step (e), adjusting a pH of the comminuted feed material to provide the pH ranging from about pH 3.5 to about pH 6.5;

after pH adjustment, contacting the carbonaceous component depressant with the comminuted feed material;

after addition of the carbonaceous component depressant, contacting an anionic collector with the comminuted feed material;

after addition of the anionic collector, contacting the frother with the comminuted feed material;

after step (f) and before step (i), adjusting a pH of the comminuted second fraction to provide a pH ranging from about pH 3.5 to about pH 6.5;

after pH adjustment, contacting the carbonaceous component depressant with the comminuted second fraction; and

after addition of the carbonaceous component depressant, contacting the anionic collector with the comminuted second fraction;

after addition of the anionic collector, contacting the frother with the comminuted second fraction.

5. The method of claim 1, wherein the depressant is a sulfonate and is not added in a sufficient amount to depress sulfide flotation and wherein the comminuted feed material comprises gypsum and further comprising:

contacting the comminuted feed material with a sodium carbonate to clean exposed sulfide mineral surfaces of precipitated gypsum.

6. The method of claim 1, wherein the first and third fractions have a sulfide sulfur content of at least about 6.5 wt. %, wherein the refractory feed material comprises silicates, wherein at least most of the silicates in the refractory feed material are in the fourth fraction, wherein, in step (e), the first fraction comprises about 40% of more of the sulfides in the refractory feed material and no more than about 20% of the carbonaceous preg robbing component and wherein, in step (i), the third fraction comprises about 40% of more of the sulfides in the refractory feed material and no more than about 20% of the carbonaceous preg robbing component.

7. The method of claim 1, wherein step (e) is flash flotation and further comprising:

after step (e) and before step (f), size separating the second fraction to form oversized and undersized fractions and wherein the oversized fraction is recycled to step (b).

8. The method of claim 1, wherein step (i) is flash flotation and further comprising:

size separating the fourth fraction to form oversized and undersized fractions and wherein the oversized fraction is comminuted in step (f).

9. The method of claim 1, wherein, in each of steps (b) and (f), from about 10 to about 250 g/tonne of sulfide activator is added and from about 25 to about 250 g/tonne of polymeric clay dispersant is added.

10. The method of claim 1, wherein, in each of steps (e) and (i), flotation is performed in the presence of from about 1 to about 50 g/tonne of the carbonaceous material depressant and wherein the carbonaceous material depressant is a sulfonate to reduce consumption of collector and frother.

11. The method of claim 1, wherein each of steps (e) and (i) is performed in the presence of air bubbles.

12. The method of claim 1, wherein the sulfide activator is copper sulfate and wherein the sulfide activator substantially inhibits oxidation of sulfide surfaces exposed during comminution.

13. The method of claim 1, further comprising:

(j) recovering the gold from the first and third fractions.

14. A method, comprising:

(a) providing a refractory feed material, the refractory feed material comprising gold, sulfides, a carbonaceous preg robbing component, and a clay;

(b) comminuting the refractory feed material to form a comminuted feed material having a first size distribution;

(c) during comminuting, adjusting chemical conditions of the refractory feed material by adding a sulfide activator;

(d) after the comminuting step (b), contacting the comminuted feed material with a carbonaceous component depressant, collector, and frother;

(e) floating, in the presence of air bubbles, the comminuted feed material, in the presence of the sulfide activator, the collector, the frother, and the carbonaceous component depressant, at a pH ranging from about pH 3.5 to about pH 6.5, and at an Eh ranging from about 25 to about 100 millivolts, to form first and second fractions, the first and second fractions each comprising at least some of the gold and sulfides in the refractory feed material;

(f) comminuting the second fraction to provide a comminuted second fraction, the comminuted second fraction having a second size distribution finer than the first size distribution;

(g) during comminuting, adjusting chemical conditions of the second fraction by adding the sulfide activator;

(h) after the comminuting step (f), contacting the comminuted second fraction with the carbonaceous component depressant, collector, and frother; and

(i) further floating, in the presence of air bubbles, the comminuted second fraction, in the presence of the sulfide activator, the collector, the frother, and the carbonaceous component depressant, at a pH ranging from about 3.5 to about pH 6.5, and at an Eh ranging from about 25 to about 100 millivolts, to produce third and fourth fractions, the third fraction comprising at least most of the gold and sulfides in the second fraction, wherein an amount of sulfide activator added during steps (b) and (f) is insufficient to oxidize substantially the collector.

15. The method of claim 14, wherein, in steps (b) and (f), the refractory feed material and second fraction, respectively, are wet milled, wherein, in steps (c) and (g), a polymeric clay dispersant is added, and wherein the sulfide activator and polymeric clay dispersant are added during each of steps (b) and (f).

16. The method of claim 15, wherein the sulfide activator is a metal salt selected from the group consisting essentially of copper salts, lead salts, and mixtures thereof, wherein the first size distribution is a P₈₀ size ranging from about 100 to about 200 microns, and wherein the second size distribution is a P₈₀ size ranging from about 25 to about 100 microns.

17. The method of claim 15, wherein the collector is an anionic collector and further comprising before step (e):

after step (b) and before step (e), adjusting a pH of the comminuted feed material to provide the pH ranging from about pH 3.5 to about pH 6.5;

after pH adjustment, contacting the carbonaceous component depressant with the comminuted feed material;

after addition of the carbonaceous component depressant, contacting the anionic collector with the comminuted feed material;

after addition of the anionic collector, contacting the frother with the comminuted feed material;

after step (f) and before step (i), adjusting a pH of the comminuted second fraction to provide a pH ranging from about pH 3.5 to about pH 6.5;

after pH adjustment, contacting the carbonaceous component depressant with the comminuted second fraction;

after addition of the carbonaceous component depressant, contacting the anionic collector with the comminuted second fraction;

after addition of the anionic collector, contacting a frother with the comminuted second fraction.

18. The method of claim 14, wherein the depressant is a sulfonate and is not added in a sufficient amount to depress sulfide flotation and wherein the comminuted feed material comprises gypsum and further comprising:

contacting the comminuted feed material with a sodium carbonate to clean exposed sulfide mineral surfaces of precipitated gypsum.

19. The method of claim 14, wherein the first and third fractions have a sulfide sulfur content of at least about 6.5 wt. %, wherein the refractory feed material comprises silicates, wherein at least most of the silicates in the refractory feed material are in the fourth fraction, wherein, in step (e), the first fraction comprises about 40% of more of the sulfides in the refractory feed material and no more than about 20% of the carbonaceous preg robbing component and wherein, in step (i), the third fraction comprises about 40% of more of the sulfides in the refractory feed material and no more than about 20% of the carbonaceous preg robbing component.

20. The method of claim 14, wherein step (e) is flash flotation and further comprising:

after step (e) and before step (f), size separating the second fraction to form oversized and undersized fractions and wherein the oversized fraction is recycled to step (b).

21. The method of claim 14, wherein step (i) is flash flotation and further comprising:

after step (i), size separating the fourth fraction to form oversized and undersized fractions and wherein the oversized fraction is comminuted in (f).

22. The method of claim 15, wherein, in each of steps (b) and (f), from about 10 to about 250 g/tonne of sulfide activator is added and from about 25 to about 250 g/tonne of polymeric clay dispersant is added.

23. The method of claim 14, wherein, in each of steps (e) and (i), flotation is performed in the presence of from about 1 to about 50 g/tonne of the carbonaceous material depressant and wherein the carbonaceous material depressant is a sulfonate to reduce consumption of the collector and frother.

24. The method of claim 14, wherein the sulfide activator is copper sulfate and wherein the sulfide activator substantially inhibits oxidation of sulfide surfaces exposed during comminution.

25. The method of claim 14, further comprising:

(j) recovering the gold from the first and third fractions.

26. A method, comprising:

(a) providing a refractory feed material, the refractory feed material comprising gold, sulfides, a carbonaceous preg robbing component, and a clay;

(b) comminuting the refractory feed material to form a comminuted feed material having a first size distribution;

(c) during comminuting, adjusting chemical conditions of the refractory feed material by adding a sulfide activator and a polymeric clay dispersant;

(d) after the comminuting step (b), contacting the comminuted feed material with a carbonaceous component depressant, collector, and frother;

(e) floating, in the presence of air, the comminuted feed material, in the presence of the sulfide activator, the polymeric clay dispersant, the collector, the frother, and the carbonaceous component depressant, at a pH ranging from about pH 3.5 to about pH 6.5, and at an Eh ranging from about 25 to about 100 millivolts, to form first and second fractions, the first and second fractions each comprising at least some of the gold and sulfides in the refractory feed material;

(f) comminuting the second fraction to provide a comminuted second fraction, the comminuted second fraction having a second size distribution finer than the first size distribution;

(g) during comminuting, adjusting chemical conditions of the second fraction by adding the sulfide activator and polymeric clay dispersant;

(h) after the comminuting step (f), contacting the comminuted second fraction with the carbonaceous component depressant, collector, and frother; and

(i) further floating, in the presence of air, the comminuted second fraction, in the presence of the polymeric clay dispersant, the sulfide activator, the collector, the frother, and the carbonaceous component depressant, at a pH ranging from about 3.5 to about pH 6.5, and at an Eh ranging from about 25 to about 100 millivolts, to produce third and fourth fractions, the third fraction comprising at least most of the gold and sulfides in the second fraction, wherein, in each of steps (b) and (f), from about 10 to about 250 g/tonne of sulfide activator and from about 25 to about 250 g/tonne of polymeric clay dispersant are added and wherein, in each of steps (e) and (i), flotation is performed in the presence of from about 1 to about 50 g/tonne of the carbonaceous material depressant.