JP2013112879A - Method for leaching gold out of mineral sulfide - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a method that can inhibit the gold concentration in a solution after leaching in time progress from dropping after gold is leached out of a sulfide mineral.SOLUTION: This method for leaching gold out the sulfide mineral or out of residual dross (hereinafter, referred to as a "raw material") after leaching is processed to the sulfide mineral, includes a process to leach a gold component out of a raw material by contacting acidic water solution containing chlorine ion, bromine ion, copper ion, and iron ion with the material under the supply of an oxidizing agent, and to keep the bromine ion concentration in the acidic water solution, out of which gold has been leached, to 40 g/L or higher and the oxidation-reduction potential to 500 mV (vs. Ag/AgCl) or higher.

Description

  The present invention relates to a method for leaching gold from sulfide ore. The present invention also relates to a method for recovering gold from an aqueous solution leached with gold.

  In recent years, a technique for recovering copper from sulfide ore by a wet method instead of the conventional dry method has attracted attention. The sulfide ore often contains a precious metal such as gold in a small amount, and a method for economically recovering the precious metal in addition to copper is required.

  As a technology for addressing such problems, alkali metal or alkaline earth metal chlorides and bromides and copper and iron chlorides or bromides are used, and the gold leaching process is performed on the residue after the copper leaching process. A method of carrying out is known (Japanese Patent Laid-Open No. 2009-235519). According to this method, it is said that copper and gold in copper sulfide ore can be leached and recovered at a high leaching rate only by using air without using a special oxidizing agent.

  In relation to the above technique, Japanese Patent Application Laid-Open No. 2009-235525 states that “a suitable oxidizing agent for leaching gold present in copper concentrate and the leached gold are reduced again and do not precipitate as metallic gold. In the present invention, gold is stably eluted by producing gold chloride using chlorine ions, but when bromine ions are used in combination, gold bromide is produced. Gold leaching can be further facilitated ”(paragraph 0014). The bromine ion concentration for use in the gold leaching reaction is necessary to form gold bromide and elute gold to form a complex. It is said that there is an upper limit of solubility because it is affected by the concentration, and it is 1 to 80 g / L in consideration of solubility, but it is described that about 10 to 26 g / L is desirable in view of the economical use amount of chemicals. (Paragraph 0017). In this publication, bromine ions in the leachate are added in the form of sodium bromide, and the higher the concentration, the better. However, because the solubility changes due to the influence of chlorine ion concentration and temperature at the same time, Practically, it is also described that the bromine ion concentration may be 1 to 50 g / L, preferably 10 to 26 g / L (paragraph 0025).

  Furthermore, in Japanese Translation of PCT International Publication No. 2009-526912, in order to promote leaching when recovering gold from the leaching residue or intermediate product after the copper sulfide raw material is leached with atmospheric chloride, alkali bromide in the leachate is reduced to 0. .5-30 g / L is proposed.

JP 2009-235519 A JP 2009-235525 A Special table 2009-526912

  In the technique described in the above-mentioned document, the halogen ions in the leachate used for gold leaching are mainly chlorine ions, and bromine ions are supplementarily added to the method to recover gold from the sulfide ore by a wet method. It proposes a commercially feasible technology. When gold leaching is performed using the conventional technique, gold exists in a high concentration in the solution after gold leaching immediately after leaching gold. However, it has been found that the conventional technique has a problem that the gold concentration in the solution after gold leaching rapidly decreases with time. In the actual operation for recovering gold from copper ore, the gold recovery process is not always performed immediately after the gold leaching process, and gold leaching is performed for about 1 to 3 days due to the solid-liquid separation operation and operation schedule. The gold recovery process may be performed after storing the post-solution. Therefore, a method capable of maintaining the dissolved gold concentration as much as possible while storing the solution after gold leaching is desired.

  Then, this invention makes it a subject to provide the method which can suppress the fall of the gold | metal density | concentration in the liquid after leaching with time passage after leaching gold from a sulfide mineral.

  As a result of intensive studies, the present inventors have found that when the bromine ion concentration in the gold leaching solution based on an alkali chloride aqueous solution is extremely increased, the state in which the gold in the solution after leaching is dissolved is stably maintained. .

In one aspect, the present invention is a method for leaching gold contained in a sulfide mineral or a leaching residue after the leaching treatment for the sulfide mineral (hereinafter referred to as “raw material”),
A step of leaching the gold component in the raw material by contacting an acidic aqueous solution containing chlorine ion, bromine ion, copper ion, and iron ion with the raw material while supplying the oxidizing agent; and bromine in the acidic aqueous solution in which gold is leached And a step of storing while maintaining the ion concentration at 40 g / L or more and the oxidation-reduction potential at 500 mV (vs. Ag / AgCl) or more.

  In one embodiment of the gold leaching method according to the present invention, the bromine ion in the acidic aqueous solution is maintained at 80 g / L or more and the oxidation-reduction potential is maintained at 480 mV (vs. Ag / AgCl) or more.

  In another embodiment of the gold leaching method according to the present invention, the weight concentration ratio of bromine ions to chlorine ions in the acidic aqueous solution is 1 or more.

  In still another embodiment of the gold leaching method according to the present invention, the copper ion concentration in the acidic aqueous solution is 5 g / L or more and the iron ion concentration is 1 g / L or more.

  In another aspect, the present invention is a method for recovering gold from a raw material including a step of recovering gold from a solution after gold leaching obtained by performing the gold leaching method.

  In one embodiment of the gold recovery method according to the present invention, the storage period from the end of the gold leaching step to the start of the gold recovery step is 24 hours or more.

  In another embodiment of the gold recovery method according to the present invention, the bromine ion concentration in the solution after gold leaching is increased during the storage period.

  According to the present invention, after leaching gold from a leaching residue in a sulfide mineral or after leaching treatment to the sulfide mineral, it is possible to suppress a decrease in gold concentration in the leached solution over time. Therefore, the recovery efficiency of gold from sulfide mineral can be increased.

It is a graph which shows transition of the density | concentration of the gold | metal melt | dissolved in the liquid after leaching.

(Leaching process)
The gold leaching step includes a step of leaching a gold component in the raw material by bringing an acidic aqueous solution (gold leaching solution) containing chlorine ions, bromine ions, copper ions and iron ions into contact with the raw material while supplying an oxidizing agent. It is preferable to adjust the chlorine ion concentration in the acidic aqueous solution to 5 to 70 g / L, the bromine ion concentration to 40 g / L or more, the copper ion concentration to 5 g / L or more, and the iron ion concentration to 1 g / L or more. The raw material which is the object of the present invention is a sulfide mineral or a leaching residue after the leaching treatment for the sulfide mineral. Although there is no restriction | limiting in particular as a sulfide mineral, Typically, the primary copper sulfide ore (example: chalcopyrite) containing gold, the copper sulfide ore containing the silicate ore containing gold, and the pyrite containing gold are mentioned. In addition, intermediate products generated in various processes of sulfide minerals are also handled as sulfide minerals.

  Gold leaching proceeds by the elution of gold reacting with chlorine ions or bromine ions to form gold chloride complexes or gold bromide complexes. By using bromine ions in combination, the complex is formed at a lower potential, so that the leaching time can be shortened and the gold leaching efficiency can be improved, that is, the gold concentration in the liquid after leaching can be increased. In the present invention, by significantly increasing the bromine ion concentration in the gold leaching solution, the effect that the leached gold can be stably present for a long time in a dissolved state can be further obtained.

  The redox potential of the leachate also depends on the temperature, and when the liquid temperature is lowered by about 10 ° C., the redox potential is also lowered by about 10 mV. Therefore, if it is left as it is from a general leaching temperature of about 80 ° C., the temperature of the leaching solution is lowered, the oxidation-reduction potential is also lowered, and it becomes difficult to maintain the dissolution of gold.

  The concentration of bromide ions in the gold leaching solution may be about 5 g / L only from the viewpoint of reaction rate and solubility, but the gold concentration in the leaching solution is stably dissolved at 2 mg / L or more. In order to maintain the dissolved state even if it is kept for several days or the temperature of the solution after leaching is lowered from about 80 ° C. which is a general leaching temperature to room temperature, it is necessary to be 40 g / L or more. 80 g / L or more, more preferably 100 g / L or more, and still more preferably 120 g / L or more. However, from the viewpoint of cost, the bromine ion concentration in the gold leachate is generally low, and is preferably 80 to 100 g / L.

  The concentration of chlorine ions in the gold leaching solution is preferably 5 g / L or more, and more preferably 15 g / L or more, from the viewpoint of the formation of Cu (I). However, if the chlorine ion concentration is too high, the ion concentration of the bath will increase, and the problem of precipitation will occur during operation, so it should be 70 g / L or less, and it should be 20-40 g / L. preferable.

  Iron ions, which are trivalent iron ions oxidized from the supply of an oxidizing agent or trivalent iron ions from the beginning, serve to oxidize gold. The concentration of iron ions in the gold leaching solution is preferably 1 g / L or more, more preferably 3 g / L or more.

  Copper ions are not directly involved in the reaction, but the presence of copper ions increases the oxidation rate of iron ions. As for copper ions, divalent copper ions function as oxidation. The concentration of copper ions in the leachate is preferably 5 g / L or more, and more preferably 20 g / L or more.

  The supply source of chlorine ions is not particularly limited, and examples thereof include hydrogen chloride, hydrochloric acid, metal chloride, chlorine gas, and the like. In consideration of economy and safety, supply in the form of metal chloride is preferable. Examples of the metal chloride include copper chloride (cuprous chloride, cupric chloride), iron chloride (ferrous chloride, ferric chloride), and alkali metals (lithium, sodium, potassium, rubidium, cesium, francium). Chlorides and chlorides of alkaline earth metals (beryllium, magnesium, calcium, strontium, barium, radium) can be mentioned, and sodium chloride is preferable from the viewpoint of economy and availability. Moreover, since it can utilize also as a supply source of copper ion and iron ion, it is also preferable to utilize copper chloride and iron chloride.

  The bromine ion supply source is not particularly limited, and examples thereof include hydrogen bromide, hydrobromic acid, metal bromide, bromine gas, and the like. In consideration of economy and safety, it is in the form of metal bromide. It is preferable to supply. Examples of the metal bromide include copper bromide (cuprous bromide, cupric bromide), iron bromide (ferrous bromide, ferric bromide), alkali metals (lithium, sodium, potassium, Examples thereof include bromides of rubidium, cesium, and francium) and bromides of alkaline earth metals (beryllium, magnesium, calcium, strontium, barium, and radium), and sodium bromide is preferable from the viewpoint of economy and availability. Moreover, since it can utilize also as a supply source of copper ion and iron ion, it is also preferable to utilize copper bromide and iron bromide.

The supply source of copper ions and iron ions is usually supplied in the form of these salts. For example, it can be supplied in the form of a halide salt. From the viewpoint that it can also be used as a source of chlorine ions and / or bromine ions, copper ions are preferably supplied as copper chloride and / or copper bromide, and iron ions are preferably supplied as iron chloride and / or iron bromide. As copper chloride and iron chloride, it is preferable to use cupric chloride (CuCl ₂ ) and ferric chloride (FeCl ₃ ) from the viewpoint of oxidizing power, respectively, but cuprous chloride (CuCl) and ferric chloride are preferable. Even if (FeCl ₂ ) is used, supplying an oxidizing agent to the leachate will oxidize to cupric chloride (CuCl ₂ ) and ferric chloride (FeCl ₃ ), respectively, so there is no significant difference.

  Accordingly, in a preferred embodiment of the gold leaching step, at least one of hydrochloric acid and bromic acid, cupric chloride, and copper chloride are selected on the condition that the gold leaching solution is selected to contain both chlorine ions and bromine ions. A mixed solution containing at least one of cupric bromide, at least one of ferric chloride and ferric bromide, and at least one of sodium chloride and sodium bromide can be used.

  The pH of the gold leaching solution is preferably about 0 to 3 and more preferably about 0.5 to 2.0 for securing the dissolution of trivalent iron ions. The redox potential (vs Ag / AgCl) of the leaching solution at the start of the gold leaching step is preferably 500 mV or more, more preferably 550 mV or more because of the effect of bromine ions. The temperature of the gold leaching solution is preferably 60 ° C. or more from the viewpoint of leaching efficiency and material of the apparatus, and more preferably 70 to 90 ° C. from the viewpoint of leaching speed.

  The gold leaching process is performed while supplying the oxidizing agent, thereby managing the redox potential. Although there is no restriction | limiting in particular as an oxidizing agent, For example, oxygen, air, chlorine, a bromine, hydrogen peroxide, etc. are mentioned. An oxidant with an extremely high redox potential is not necessary and air is sufficient. Air is also preferable from the viewpoint of economy and safety.

  There are no particular limitations on the method of contacting the gold leachate and the raw material, and there are methods such as spraying and dipping. From the viewpoint of reaction efficiency, a method of dipping the residue in the leachate and stirring is preferred.

(Copper recovery)
Since the liquid after leaching obtained by the copper leaching step contains a large amount of copper component, copper can be recovered from the liquid after leaching. Although there is no restriction | limiting in particular as a copper collection | recovery method, For example, solvent extraction, ion exchange, substitution precipitation with a base metal, electrowinning, etc. can be utilized. The copper in the solution after leaching contains both monovalent and divalent states, but in order to perform solvent extraction and ion exchange smoothly, all of them should be oxidized beforehand to be divalent copper ions. Is preferred. The method of oxidation is not particularly limited, but a method of leaching air or oxygen into the liquid after leaching is simple.

(Gold collection)
Gold is dissolved in the leaching reaction solution obtained by the gold leaching step, and gold can be recovered from the leaching reaction solution. Although there is no restriction | limiting in particular as a collection | recovery method of gold | metal | money, Activated carbon adsorption | suction, electrowinning, solvent extraction, ion exchange, etc. can be utilized. By collecting gold during the leaching reaction, the gold concentration in the leaching reaction solution can be reduced, and the gold leaching rate can be increased.

  According to the present invention, the stability of the gold dissolved in the solution after leaching after gold leaching is high, so that after the gold leaching process is finished, the storage period until the gold recovery process is started can be extended. it can. For example, the storage period can be 5 days or more, and can be 1 week or more. However, since there are few merits even if it preserve | saves for too long, it is preferable to set it within two days.

  In order to maintain the state in which gold is stably dissolved in the solution after leaching for a long period of time, the bromine ion concentration in the solution after leaching of gold can be increased during the storage period. Specifically, after completion of the gold leaching step, a bromine ion source can be added to the leached solution within 1 day, preferably within half a day, more preferably within 6 hours, and even more preferably within 1 hour. . Examples of the bromine ion supply source include the compounds described above, and sodium bromide is preferred from the viewpoints of economy and availability.

  In addition, after the gold leaching step, the period from the start of the gold recovery step to when the bromine ion concentration in the acidic aqueous solution leached with gold is 40 g / L or more, the redox potential of the solution after gold leaching Is maintained at 500 mV or higher (vs. Ag / AgCl) at room temperature or higher (25 ° C. or higher), so that dissolution of gold can be maintained. This is a value 40 mV or more lower than the redox potential immediately after leaching. If the bromine ion concentration in the acidic aqueous solution leached with gold is 80 g / L or more, the oxidation-reduction potential of the solution after gold leaching should be controlled at 480 mV or higher (vs. Ag / AgCl) at room temperature or higher (25 ° C. or higher). Is also possible. Although there is no problem with the higher oxidation-reduction potential, the cost becomes higher if it is controlled to be higher than necessary. Therefore, it is preferably 700 mV or less (vs. Ag / AgCl), preferably 600 mV or less (vs. Ag / AgCl). It is more preferable to do. Moreover, although the solubility of gold | metal | money becomes higher, so that management temperature is high, since the expense for heat insulation requires, it is preferable to preserve | save at room temperature (20-60 degreeC, typically 25-40 degreeC).

  Generally, the oxidation-reduction potential also decreases with a decrease in temperature. In the leachate having the composition shown here, the rate of decrease in temperature and decrease in redox potential is about 1 mV / ° C. That is, the temperature can be controlled by lowering by about 40 ° C.

  In the test, gold was leached to the residue after leaching the copper in the copper sulfide concentrate containing gold. The gold quality in the residue was 26 g / t, and the copper quality was 1.2%. For gold leaching, the Cl ion concentration is adjusted to 40 g / L, the Cu ion concentration is adjusted to 20 g / L, the Fe ion concentration is adjusted to 2 g / L, and the Br ion concentration is adjusted to 20 to 120 g / L. went. The oxidation-reduction potential at 80 ° C. was 537 to 557 mV (vs. Ag / AgCl).

  The solution after leaching was allowed to stand at room temperature (15 to 25 ° C.), and the concentration of gold dissolved in the leaching solution after 1 to 7 days was measured. In order to eliminate the influence of fine precipitates, the sampled leachate was filtered through a 0.1 μm membrane filter and then subjected to ICP analysis. The oxidation-reduction potential during the storage period was measured after the temperature of the solution after leaching dropped to 25 ° C.

The analysis results are shown in FIG. In the case of a leachate with a Br concentration of 20 g / L, it decreased to 1 mg / L or less after 1 day, but the leachate with a concentration of 40 g / L or more maintained the initial concentration until 7 days after the oxidation-reduction potential was 500 mV.
In addition, when the oxidation-reduction potential was 480 mV, the gold concentration of the leachate with a Br concentration of 60 g / L decreased to less than half after one day, but the gold concentration of the leachate with a Br concentration of 80 g / L was initially even after five days. Of gold concentration.

Claims (7)

A leaching method of gold contained in a leaching residue (hereinafter referred to as “raw material”) in a sulfidation mineral or after leaching treatment to the sulfidation mineral,
A step of leaching the gold component in the raw material by contacting an acidic aqueous solution containing chlorine ion, bromine ion, copper ion, and iron ion with the raw material while supplying the oxidizing agent; and bromine in the acidic aqueous solution in which gold is leached And a step of storing while maintaining the ion concentration at 40 g / L or more and the oxidation-reduction potential at 500 mV (vs. Ag / AgCl) or more. A leaching method of gold contained in a leaching residue (hereinafter referred to as “raw material”) in a sulfidation mineral or after leaching treatment to the sulfidation mineral,
A step of leaching the gold component in the raw material by contacting an acidic aqueous solution containing chlorine ion, bromine ion, copper ion, and iron ion with the raw material while supplying the oxidizing agent; and bromine in the acidic aqueous solution in which gold is leached And a step of storing while maintaining the ion concentration at 80 g / L or more and the oxidation-reduction potential at 480 mV (vs. Ag / AgCl) or more.   The gold leaching method according to claim 1 or 2, wherein a weight concentration ratio of bromine ions to chlorine ions in the acidic aqueous solution is 1 or more.   The gold leaching method according to any one of claims 1 to 3, wherein a copper ion concentration in the acidic aqueous solution is 5 g / L or more and an iron ion concentration is 1 g / L or more.   A method for recovering gold from a raw material, comprising a step of recovering gold from a solution after gold leaching obtained by performing the gold leaching method according to any one of claims 1 to 4.   The gold recovery method according to claim 5, wherein a storage period from the completion of the gold leaching step to the start of the gold recovery step is 24 hours or more.   The method for recovering gold according to claim 6, wherein the bromine ion concentration in the solution after gold leaching is increased during the storage period.