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Process for Gold and Silver Leaching with Thiourea Solutions

a technology of thiourea solutions and gold and silver leaching, which is applied in the field of mining and mineral treatment industry, can solve the problems of low efficiency of refractory minerals, high yield of cyanidation, and instability of thiourea solutions themselves

Inactive Publication Date: 2007-11-29
LAVINE GRETCHEN TERRI LAPIDUS +6
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0007] One objective of the present invention is to avoid the harmful effects of the external oxidizing agents on the thiourea solutions.
[0008] Another consists in recovering the gold and silver in their metallic form, once extracted from the mineral, in such a way that the electrical energy is employed in an optimal manner, by oxidizing part of the thiourea to formamidine disulfide in one of the compartments (anodic) and, in the other (cathodic), reducing the dissolved gold and silver reducing to their metallic state.
[0010] In summary, our invention reduces the inconveniences of the instability of thiourea in the presence of strong oxidants, permitting at the same time a clean recovery of the metallic values, and constitutes an improvement of the solution employed for leaching gold and silver from minerals and other materials that contain them, employing thiourea. These improvements are characterized by the controlled electro-oxidation of 10 to 30% of the thiourea originally in the solution and the simultaneous electrowinning of the gold and silver from said solution. On the other hand, it consists of a process which allows the application of this solution in a process which extracts and recovers the metallic values from the minerals which contain them.

Problems solved by technology

Basically two commercially implemented leaching techniques exist: cyanidation produces the highest yields in the majority of cases, however, with the problems of toxic residues and low efficiency in refractory minerals (those that contain organic material, arsenic or manganese) or those that contain high concentrations of silver sulfides.
One of the great obstacles for the industrialization of the thiourea process to extract silver and gold is the instability of the thiourea solutions themselves.
Another impediment related to the use of thiourea is that the methods employed for precious metal recovery from the leaching solutions results in their contamination, limiting the possibility of their recycle within the process.
Additionally, there exists a disequilibrium with respect to the utilization of electrical energy; on one side of the electrolytic cell, the thiourea is being partially oxidized while, on the other side, separated by a membrane, the generated potential is being wasted on a sacrifice reduction process.

Method used

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  • Process for Gold and Silver Leaching with Thiourea Solutions
  • Process for Gold and Silver Leaching with Thiourea Solutions

Examples

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example

[0020] One liter of aqueous solution containing 15.2 grams of thiourea, with the pH adjusted to 2 with sulfuric acid, was subjected to a reversible potential of 500 mV for 2 hours in a membrane cell, where the anodic and cathodic compartments are separated, to produce in-situ a quantity of FADS, equivalent to the oxidation of 18% of the initial thiourea. Following this step, the solution is placed in contact with 10 grams of sulfide concentrate which contains approximately 8 wt. % silver and 0.08 wt. % gold for 60 hours. After this time, 95% of the original thiourea was intact and more than 94% of the silver and 65% of the gold contained in the mineral were leached. The silver extraction was increased 36% with respect to the amount leached with an equivalent amount of cyanide. After removal of the solid residue, the pregnant solution was subjected to an electrolysis in the cathodic compartment of the same cell, where the thiourea was oxidized. After 2 hours, 98% of the silver and 92...

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Abstract

The present invention concerns the mining and mineral treatment industry. Specifically, it relates to a solution composition that permits the use of thiourea. Specifically, the patent refers to a process to form a solution that improves, on one hand, the velocity of gold and silver extraction, from minerals and other materials that contain them, improving the stability of the thiourea in the leaching solution and, on the other, the direct electrorecovery of said metals from the aforementioned solution. The invention consists of the leaching solution that, beforehand or simultaneously, has been subjected to a controlled electro-oxidation to produce formamidine disulfide (FADS) which acts as an oxidizing agent for the mineral phases that contain the gold and silver. In the preferred mode, the FADS is present as 10 to 30% of the total thiourea contained in the solution and the electrodeposition of the metals is performed in the same cell (cathodic compartment) in which the FADS is formed (anodic compartment).

Description

FIELD OF THE INVENTION [0001] The present invention concerns the mining and mineral treatment industry. Specifically, it relates to a process that uses thiourea, electro-oxidized under controlled conditions, to form in-situ an oxidizing agent capable of dissolving gold and silver from minerals which contain them and the electrolytic recovery of said metals in the same process. BACKGROUND OF THE INVENTION [0002] At present, the processing of gold and silver ores fundamentally depends on the form in which they are found in the mineral, using for this flotation, amalgamation and / or leaching. In this last technique, the solution employed plays an important role in the efficiency and environmental impact of the process. [0003] Basically two commercially implemented leaching techniques exist: cyanidation produces the highest yields in the majority of cases, however, with the problems of toxic residues and low efficiency in refractory minerals (those that contain organic material, arsenic ...

Claims

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Application Information

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IPC IPC(8): C22B3/16C22B3/04C22B11/00C25C1/20
CPCC22B3/045C25C1/20C22B11/04C22B3/1625Y02P10/20
Inventor LAVINE, GRETCHEN TERRI LAPIDUSESCUTIA, MARIA CONCEPCION LOPEZGUZMAN, MERCEDES TERESITA OROPEZAMARTINEZ, IGNACIO GONZALEZHERNANDEZ, FERNANDO RODRIGUEZDIAZ, MARIA ELENA POISOTBAUTISTA, ITA GIRON
Owner LAVINE GRETCHEN TERRI LAPIDUS