Patent EA-000902-B1 (EA)
Title: A method for processing refractory auriferous sulfide ores involving preparation of a sulfide concentrate
Inventor: SIMMONS GARY L
IPC: C01G1/00
Filed: 1997-10-23
Abstract: 1. A method for flotation processing of a gold-bearing mineral material feed containing a plurality of different sulfide mineral species, including one or more refractory auriferous sulfide containing gold that is refractory due to its presence in the refractory auriferous sulfide, the method comprising the steps of: subjecting to flotation in a liquid medium said mineral material feed in particulate form, said flotation including passing bubbles of a flotation gas through said liquid medium; during said flotation, a first portion of said mineral material feed rising through said liquid medium with said bubbles and said first portion being collected from a flotation froth as a flotation concentrate, a second portion of said mineral material feed being collected as a flotation tail; said flotation concentrate being enriched, relative to said mineral material feed, in each of said plurality of different sulfide mineral species, including said one or more refractory auriferous sulfide, and in gold; said flotation tail being depleted, relative to said mineral material feed, in each of said plurality of different sulfide mineral species, including said one or more refractory auriferous sulfide, and in gold; wherein, said flotation gas comprises oxygen gas, if at all, at a volume fraction of oxygen gas that is smaller than the volume fraction of oxygen gas in ambient air, and wherein the flotation is substantially not selective as between said plurality of different sulfide mineral species. 2. The method of claim 1, wherein: said flotation gas comprises less than about 10 volume percent oxygen gas. 3. The method of claim 1, wherein: said flotation gas comprises less than about 5 volume percent oxygen gas. 4. The method of claim 1, wherein: said flotation gas comprises greater than about 95 volume percent of gas selected from the group consisting of nitrogen gas, carbon dioxide gas, helium gas, argon gas and combinations thereof. 5. The method of claim 1, wherein: said flotation gas comprises combustion exhaust. 6. The method of claim 1, wherein: said plurality of different sulfide mineral species comprise a plurality of different iron-containing sulfide mineral species and said flotation is subsantially not selective to flotation of said different iron-containing sulfide mineral species, so that said flotation concentrate is enriched, relative to said mineral material feed, in each of said plurality of different iron-containing sulfide mineral species. 7. The method of claim 1, wherein: after said flotation, said flotation tail is subjected to leaching to remove from said flotation tail non-refractory gold that is not associated with a sulfide mineral. 8. The method of claim 7, wherein: said leaching comprises cyanide leaching of gold from said flotation tail. 9. The method of claim 1, wherein: said liquid medium comprises deoxygenated water. 10. The method of claim 9, wherein: said deoxygenated water comprises less than about 2.0 parts per million by weight of oxygen. 11. The method of claim 9, wherein: said deoxygenated water, prior to said flotation, had been prepared by passing a gas through water to remove oxygen from said water. 12. The method of claim 1, wherein: prior to said flotation, said mineral material feed is subjected to wet comminution to reduce the particle size of said mineral material; water used during said wet comminution comprising deoxygenated water. 13. The method of claim 12, wherein: said comminution is conducted in an environment that is substantially free of air. 14. The method of claim 1, wherein: before said flotation, said mineral material feed is subjected to comminution to reduce the particle size of said mineral material feed; said comminution being conducted in equipment sealed to substantially prevent air from being drawn into said equipment. 15. The method of claim 14, wherein: said comminution comprises processing said mineral material through a sealed comminution unit having an inlet and an outlet; a blanketing gas being introduced into at least one of said inlet and said outlet; said blanketing gas comprising no greater than about 5 volume percent oxygen. 16. The method of claim 15, wherein: said blanketing gas comprises greater than about 95 volume percent of gas selected from the group consisting of nitrogen gas, carbon dioxide gas, helium gas, argon gas and combinations thereof. 17. The method of claim 14, wherein: beginning with said comminution and ending after said flotation, said mineral material feed is processed in an environment that is substantially free of oxygen gas. 18. The method of claim 1, wherein: before said flotation, said mineral material feed is subjected to comminution to reduce the particle size of said mineral material feed; said comminution being performed in the interior of a vessel having a nonmetallic interior lining to reduce the potential for contamination of said mineral material by iron. 19. The method of claim 1, wherein: before said flotation, said mineral material feed is subjected to comminution in the presence of grinding media to reduce the particle size of said mineral material; said grinding media comprising at least one of a corrosion resistant steel and a hardened steel alloy. 20. The method of claim 19, wherein: said grinding media comprises at least one of stainless steel, a chromium alloy steel and a nickel alloy steel. 21. The method of claim 1, wherein: before said flotation, said mineral material feed is subjected to magnetic separation to remove particles of magnetic iron to reduce galvanic interaction involving iron during said flotation. 22. The method of claim 1, wherein: a lead-containing activator contacts said mineral material feed during said flotation. 23. The method of claim 17, wherein: said lead-containing activator comprises at least one of lead nitrate and lead acetate.  24. The method of claim 1, wherein a copper-containing activator contacts said mineral material feed during said flotation. 25. The method of claim 1, wherein a xanthate collector contacts said mineral material feed during said flotation. 26. The method of claim 1, wherein during said flotation, said liquid medium is at an acidic pH.  27. The method of claim 1, wherein: during said flotation, said liquid medium is at a pH of smaller than about pH 6. 28. The method of claim 1, wherein: during said flotation, said liquid medium is at a pH of from about pH 3 to about pH 6. 29. The method of claim 1, wherein: said flotation comprises a first flotation stage of said mineral material feed to produce a first flotation concentrate enriched, relative to said mineral material feed, in sulfide species and in gold and to produce a first flotation tail depleted, relative to said mineral material feed, in said sulfide species and in gold; said flotation further comprising a second flotation stage wherein at least a portion of said first flotation tail is subjected to further flotation t o produce a second flotation concentrate enriched, relative to said first flotation tail, in said sulfide species and in gold and to produce a second flotation tail depleted, relative to said first flotation tail, in said sulfide species and in gold; after said first flotation stage and prior to said second flotation stage, said first flotation tail being subjected to comminution to reduce the size of p articles in said first flotation tail. 30. The method of claim 29, wherein: after said comminution and prior to said second flotation stage, said first flotation tail is subjected to size separation to separate said first flotation tail into two fractions, a first fraction of smaller-size particles and a second fraction of larger-size particles, said second fraction being subjected to said second flotation stage and said first fraction not being subjected to said second flotation stage. 31. The method of claim 1, wherein: said flotation is conducted in a sealed flotation apparatus having a vapor headspace above said liquid medium; gas is withdrawn from said vapor headspace and recycled for introduction into said liquid medium to form at least a part of said flotation g as. 32. The method of claim 31, wherein: said flotation apparatus comprises means for dispersing said flotation gas in said liquid medium, said means for dispersing creating a vacuum to suck s aid gas from said vapor headspace to introduce said gas into said liquid medium. 33. The method of claim 1, wherein: the one or more refractory auriferous sulfide includes an arsenian pyrite. 34. The method of claim 1, wherein: the one or more refractory auriferous sulfide includes an arsenian marcasite. 35. The method of claim 1, wherein: the one or more refractory auriferous sulfide includes an arsenian pyrrhotite. 36. The method of claim 1, wherein: the one or more refractory auriferous sulfide includes arsenopyrite. 37. The method of claim 1, wherein: the one or more refractory auriferous sulfide includes an iron-containing orpiment. 38. The method of claim 1, wherein: the one or more refractory auriferous sulfide includes an iron-containing realgar. 39. The method of claim 1, wherein: the plurality of different sulfide mineral species includes, in addition to the one or more refractory auriferous sulfide, at least one sulfide specie that is not a refractory auriferous sulfide. 40. The method of claim 39, wherein: the at least one sulfide specie includes an iron-containing sulfide. 41. The method of claim 1, wherein: the plurality of different sulfide mineral species includes a plurality of different pyrite species, a first pyrite specie having a morphology with a coarser grain size than a second pyrite specie, which has a morphology with a finer grain size; and the one or more refractory auriferous sulfide includes said second pyrite specie. 42. The method of claim 37, wherein: the first pyrite specie is substantially free of gold relative to the second pyrite specie. 43. The method of claim 1, wherein: the plurality of