JP7292001B2 - Copper ore evaluation method and copper smelting method - Google Patents

Description

The present invention relates to a copper ore evaluation method and a copper smelting method. More specifically, the present invention relates to a method for predicting copper leaching from copper ores. Furthermore, the present invention relates to a copper smelting method applying the prediction method.

One method for recovering copper from copper ore is the L-SX-EW method. In the L-SX-EW method, copper ore is leached with sulfuric acid or the like (L, Leaching), copper ions are selectively recovered and concentrated from the copper leaching solution by solvent extraction (SX, Solvent Extraction), and this copper sulfate solution is produces electrolytic copper by electrowinning (EW).

Copper ores can be classified into copper oxide ores, secondary copper sulfide ores, primary copper sulfide ores, and the like. Copper oxide ores are susceptible to leaching under the action of acids. Secondary copper sulfide ore can be leached by ferric leaching or the like. On the other hand, primary copper sulfide ore is known as copper ore that is difficult to leach out. However, primary copper sulfide ore accounts for a large proportion of copper ore. Therefore, it would be beneficial to be able to leach primary copper sulfide ore by leaching. JP-A-2013-189687 discloses leaching with a solution containing iodide ions and iron (III) ions as a method for recovering primary copper sulfide ore by leaching.

A column leaching test is commonly used as a basic test for optimizing leaching operations. The advantage of this method is that the results can be obtained in good agreement with the results of copper leaching at the level of actual operation. On the other hand, the drawback of this method is that it takes too long to obtain results (eg several months).

In view of the drawbacks mentioned above, a method developed is sequential analysis. Regarding this sequential analysis, for example, Japanese Patent Application Laid-Open No. 2013-189687 discloses the following procedure.
(1) Add sulfuric acid to a sample pulverized to a certain particle size and stir for a certain period of time. Quantitation of eluted copper.
(2) Add a sodium cyanide solution to the solid portion obtained by the solid-liquid separation of the sample in (1) above, and stir for a certain period of time. Quantitation of eluted copper.
(3) Add nitric acid and perchloric acid to the solid portion obtained by the solid-liquid separation of the sample in (2) above, dry on a hot plate, add hydrochloric acid and distilled water, and dissolve the solid. Quantitation of eluted copper.

In the sequential analysis, the amount of leaching determined in (1) above is regarded as the amount of leaching corresponding to copper oxide. In addition, the leaching amount quantified in (2) above is regarded as the leaching amount corresponding to the secondary copper sulfide ore. Furthermore, the leaching amount quantified in (3) above is regarded as the leaching amount corresponding to the primary copper sulfide ore.

In the sequential analysis, each of the steps (1) to (3) described above takes only about one hour, and therefore the entire steps are completed in several hours. In this respect, the sequential analysis is superior to the 1 m column test.

JP 2013-189687 A

Therefore, it is useful to be able to estimate the amount of copper leaching by performing a more convenient sequential analysis before performing a time-consuming test such as a column test (e.g., by a simple method, If you can predict in advance that the copper leaching is low, you can decide not to run the column test, thereby saving the time spent on the column test). Despite these advantages, the sequential analysis described above has a problem with the accuracy of leaching amount estimation. For example, the leaching amount of secondary copper sulfide ore estimated from the sequential analysis results was sometimes greatly different from the leaching amount of secondary copper sulfide ore in the column test.

In addition, as a problem other than the above, there was a discrepancy in the estimated leaching amount corresponding to the primary copper sulfide ore in the sequential analysis. When the cause of this problem was investigated, the following points were found. That is, there is a method of leaching with a solution containing iodine and iron (III) ions in order to leach primary copper sulfide ore in a column test. Some ores have properties that do not leach even in this solution. Furthermore, some of these ores are leached in sequential analysis with the leach solution for estimating the leaching amount corresponding to primary copper sulfide ores. For this reason, there are ores that are leached in the sequential analysis but not in the leaching process in the column test. It is difficult to estimate the leaching amount of

In view of the above points, an object of the present invention is to provide a method for estimating the results of a 1 m column test with higher accuracy than sequential analysis.

As a result of intensive research, the inventors have found the following findings. Traditionally, sequential analysis has used sodium cyanide to leach copper in order to estimate the amount of leaching corresponding to secondary copper sulfide ores.

Furthermore, sequential analysis used nitric acid and perchloric acid to leach copper ore to estimate the amount of leaching corresponding to primary copper sulfide ore.

Therefore, the inventor made the following changes. First, in order to estimate the leaching amount corresponding to secondary copper sulfide ore, copper was leached using a solution containing iron (III) ions instead of sodium cyanide. Next, in order to estimate the leaching amount corresponding to primary copper sulfide ore, copper was leached using a solution containing iron (III) ions and iodide ions instead of nitric acid and perchloric acid. It was found that this modification can estimate the leaching amount corresponding to the secondary copper sulfide ore more accurately than the conventional sequential analysis. In addition, the present inventors have found that it is possible to evaluate the potential of applying leaching with a solution containing iron (III) ions and iodide ions, which has been difficult with conventional sequential analysis.

Based on the above findings, in one aspect, the present invention includes the following inventions.

(Invention 1)
A method of evaluating copper ore, the method comprising:
A first step of leaching copper from copper ore with a sulfuric acid solution and measuring the amount of leached copper A;
A second step of leaching copper from the copper ore with a solution containing iron (III) ions and measuring the leached copper amount B; and leaching copper from the copper ore with a solution containing iron (III) ions and iodide ions. A third step of measuring the leached copper amount C;
Here, the first to third steps may be performed in any order.
(Invention 2)
The method of Invention 1, further comprising a fourth step of measuring the total copper content D contained in the copper ore.
(Invention 3)
The method of invention 2, wherein the first to fourth steps are at least partially performed in parallel.
(Invention 4)
The method of invention 3, further comprising the step of estimating the amount of leaching according to the following relationship:
estimating the leaching rate a based on the values of the leached copper amount A and the total copper amount D;
Estimating the leaching rate b based on the difference between the leached copper amount B and the leached copper amount A, and the value of the total copper amount D; and the difference between the leached copper amount C and the leached copper amount B, and the total copper amount D Estimate the leaching rate c based on the value of
(Invention 5)
The method of Invention 2,
Performing the second step on the residue obtained in the first step,
Performing the third step on the residue obtained in the second step,
the method.
(Invention 6)
The method of invention 5, further comprising predicting the amount of leaching according to the following relationship:
estimating the leaching rate a based on the values of the leached copper amount A and the total copper amount D;
estimating a leaching rate b based on the values of the leached copper amount B and the total copper amount D; and estimating the leaching rate c based on the values of the leached copper amount C and the total copper amount D.
(Invention 7)
A method for producing electrolytic copper, the method comprising:
Evaluating copper ore according to the method of any one of inventions 1-6:
The process of leaching copper from copper ore:
A process of refining electrolytic copper from a copper leachate.
(Invention 8)
A method for producing electrolytic copper, the method comprising:
Step of evaluating copper leaching amount according to the method of any one of inventions 1 to 6:
A step of leaching copper from a copper ore using a solution containing iodide ions and iron (III) ions when (leaching rate a + leaching rate b + leaching rate c) > 80 (%):
A process of refining electrolytic copper from a copper leachate.

The method of the invention, in one aspect, comprises the steps of:
A second step of leaching copper from the copper ore with a solution containing iron (III) ions and measuring the leached copper amount B; and leaching copper from the copper ore with a solution containing iron (III) ions and iodide ions. A third step of measuring the amount of leached copper C.
This allows us to obtain a closer estimate of the amount of leaching in the column test. The appropriate leaching method to employ can then be determined.

2 shows the results of the leaching amount of secondary copper sulfide ore in Examples. 2 shows the results of the leaching amount of secondary copper sulfide ore in Examples. 2 shows the results of the leaching amount of primary copper sulfide ore in Examples.

Specific embodiments for carrying out the present invention will be described below. The following description is intended to facilitate understanding of the invention. it is not intended to limit the scope of the invention.

1. Types of Copper Ore The copper ore referred to herein may be coarse ore. The crude ore may be in a state in which various minerals (eg, arsenopyrite, chalcopyrite, chalcocite, etc.) are mixed. Alternatively, the copper ore mentioned herein may consist of one type of mineral (a single mineral).

Moreover, the copper minerals mentioned in this specification can be classified from various viewpoints. Non-limiting examples include copper oxide, primary copper sulfide ore, secondary copper sulfide ore, and the like in terms of leaching characteristics.

Copper oxide ores can include, by way of example,:
Atacamite;
Azurite;
Malachite;
Tenorite;
Chrysocolla;
Cuprite;
Native Copper

Copper oxide ore has the property of being easily dissolved in sulfuric acid.

Secondary copper sulfide ores can include, by way of example, the following: Chalcocite, Covellite. Secondary copper sulfide ore has the property of being easily dissolved in a sodium cyanide solution. In addition, secondary copper sulfide ore has the property of being easily dissolved in a solution containing iron (III) ions.

Primary copper sulfide ores can include, by way of example,: Bornite, Chalcopyrite. Primary copper sulfide ore is poorly soluble in the above-mentioned sulfuric acid, sodium cyanide solution, and solution containing iron (III) ions. Instead, primary copper sulfide ore has the property of being easily soluble in solutions containing nitric acid and perchloric acid. In addition, primary copper sulfide ore has the property of being easily dissolved in a solution containing iron (III) ions and iodide ions.

2. Method for Predicting Leaching Amount The present invention includes, in one embodiment, a method for predicting the amount of copper leaching from copper ores (eg, coarse ores and/or elemental minerals). The method can include at least the following steps:
A first step of leaching copper from a sample of copper ore with a sulfuric acid solution and measuring the amount of leached copper A;
a second step of leaching copper from a sample of copper ore with a solution containing iron(III) ions to determine the amount of leached copper B; and a solution containing iron(III) ions and iodide ions from the sample of copper ore. A third step of leaching copper and measuring the amount of leached copper C.

In addition, the solution containing iron (III) ions and iodide ions used in the third step is different from the solution containing iron (III) ions used in the second step in that it does not substantially contain iodide ions. distinguished. The phrase "substantially free of iodide ions" may mean a concentration of 0 g/L of iodide ions, or it may mean that iodide ions are allowed to be contained up to a level that does not substantially contribute to the leaching reaction. (eg, 0 to 0.1 g/L, more preferably 0 to 0.01 g/L, still more preferably 0 to 0.001 g/L).

(1) Estimation of Leaching Amount Corresponding to Copper Oxide The purpose of the first step is to mainly estimate the leaching amount corresponding to copper oxide. As described above, copper oxide has the property of being easily dissolved in sulfuric acid. Therefore, it becomes possible to estimate the amount of leaching related to copper oxide.

The leaching conditions are not particularly limited, but may be as follows:
Temperature: 20-40°C (preferably 20-30°C)
Ingredient: Sulfuric acid (1-10% v/v, preferably 4-6% v/v)
Time: 0.5-2h (preferably 0.8h-1.5h)
Shaking speed: 100rpm-200rpm
Amount of ore: 10-70 g/L (for coarse ore), 0.5-1.0 g/L (for single mineral)
Mineral grain size: 50-150 μm

Note that other substances may be added to the solution components.

(2) Estimation of leaching amount corresponding to secondary copper sulfide ore The purpose of the second step is mainly to estimate the leaching amount corresponding to secondary copper sulfide ore. As described above, secondary copper sulfide ore has the property of being easily dissolved in a solution containing trivalent Fe ions.

For example, it is considered that the reaction of chalcocite, which is a type of secondary copper sulfide ore, proceeds according to the following reaction formula.
Cu ₂ S+4Fe ³⁺ →2Cu ²⁺ +4Fe ²⁺ +S

Moreover, the solution containing trivalent Fe ions has the property of dissolving not only the secondary copper sulfide ore but also the above-described copper oxide. Therefore, the amount of copper leaching from a solution containing trivalent Fe ions can be estimated as the total amount of both copper oxide and secondary copper sulfide ore. Therefore, by subtracting the leaching amount estimated in the first step from the leaching amount estimated in the second step, the leaching amount corresponding to the secondary copper sulfide ore can be estimated. Alternatively, after the copper oxide is leached in the first step, the residue may be subjected to the second step. In this case, the leaching amount estimated in the second step can be estimated as the leaching amount corresponding to secondary copper sulfide ore.

Also, compared to conventional techniques (eg, compared to sequential analysis), the analytical method of the present invention can provide estimates that closely match the leaching results of column tests. Although the following description is not intended to limit the present invention, in the case of samples containing Jarosite and carbonate, the amount of leaching in the 1 m column test is less than in the conventional sequential analysis, and the 1 m column test The results of conventional sequential analysis may deviate.

The leaching conditions are not particularly limited, but may be as follows:
Temperature: 20-65°C (preferably 45-55°C)
pH: 1.6-2.0 (preferably 1.7-1.9, no adjustment required)
Component: Fe ³⁺ (1-10 g/L, preferably 4-6 g/L)
Time: 0.5h to 200h (preferably 0.5 to 2h, or 20 to 30h, or 150 to 180h)
Shaking speed: 100rpm-200rpm
Amount of ore: 10-70 g/L (for coarse ore), 0.5-1.0 g/L (for single mineral)
Mineral grain size: 50-150 μm
Note that other substances may be added to the solution components.

As for the trivalent Fe ion supply source, a compound such as iron sulfate n-hydrate Fe ₂ (SO ₄ ) ₃ ·nH ₂ O can be used. Alternatively, a solution of divalent Fe ions (eg, ferrous sulfide) may be supplied and then converted to trivalent Fe ions by iron-oxidizing bacteria or the like.

(3) Estimation of Leaching Amount Corresponding to Primary Copper Sulfide Ore The purpose of the third step is mainly to estimate the leaching amount corresponding to primary copper sulfide ore. As described above, primary copper sulfide ore has the property of being easily dissolved in a solution containing trivalent Fe ions and iodide ions.

For example, Chalcopyrite, which is a type of primary copper sulfide ore, is considered to undergo a reaction according to the following reaction formula.
2I ⁻ +2Fe ³⁺ →I ₂ +2Fe ²⁺ (Formula 2)
CuFeS ₂ +I ₂ +2Fe ³⁺ →Cu ²⁺ +3Fe ²⁺ +2S+2I ⁻ (Formula 3)

Further, the solution containing trivalent Fe ions and iodide ions has the property of dissolving not only the primary copper sulfide ore but also the above-described copper oxide and secondary copper sulfide ore. Therefore, the amount of copper leaching from a solution containing trivalent Fe ions and iodide ions can be estimated as the total amount of copper oxide, primary copper sulfide ore, and secondary copper sulfide ore. Therefore, by subtracting the leaching amount measured in the second step (in this case, the total leaching amount of copper oxide and secondary copper sulfide ore) from the leaching amount measured in the third step, the leached amount corresponding to the primary copper sulfide ore Quantity can be estimated. Alternatively, after the copper oxide and secondary copper sulfide ore are leached in the first step and/or the second step, the residue may be subjected to the third step. In this case, the leaching amount estimated in the third step can be estimated as the leaching amount corresponding to the primary copper sulfide ore.

Also, compared to conventional techniques (eg, compared to sequential analysis), the analytical method of the present invention can provide estimates that closely match the leaching results of column tests. Although the following description is not intended to limit the present invention, in the conventional sequential analysis, the amount dissolved by nitric acid and perchloric acid was estimated as the leached amount of primary copper sulfide ore. However, depending on the type of ore, even if it can be leached with nitric acid and perchloric acid, it may not be leached with a solution containing iodide ions and iron (III) ions. Therefore, the estimated amount based on the amount dissolved in nitric acid and perchloric acid is the amount of ore leached with a solution containing iodide ion and iron (III) ion, and the amount of iodide ion and iron (III) ion. There was a possibility that it contained a portion that did not leach out in a solution containing Therefore, it was difficult to estimate the amount of leaching in a solution containing iodide ions and iron (III) ions based on the results of sequential analysis.

In this regard, in the present invention, the above-mentioned third step is performed using iodide ions and iron (III) ions, so that the conditions are similar to the column test (in the column test, the iodine method described later) , leaching primary copper sulfide ore). This can improve the accuracy of the estimated leaching amount. It also reduces the possibility that minerals that do not leach out in the column test will be included in the estimated quantity.

The leaching conditions are not particularly limited, but may be as follows:
Temperature: 20-65°C (preferably 45-55°C)
Components: Fe ³⁺ (1-10 g/L, preferably 4-6 g/L), iodide ion (100-2000 mg/L, preferably 1500-1700 mg/L)
Time: 12h to 200h (preferably 20h to 180h)
Shaking speed: 100rpm-200rpm
Amount of ore: 10-70 g/L (for coarse ore), 0.5-1.0 g/L (for single mineral)
Mineral grain size: 50-150 μm
As for the components, other substances may be added (for example, sulfuric acid, etc.).

As for the trivalent Fe ion supply source, a compound such as iron sulfate n-hydrate Fe ₂ (SO ₄ ) ₃ ·nH ₂ O can be used. Alternatively, a solution of divalent Fe ions (eg, ferrous sulfide) may be supplied and then converted to trivalent Fe ions by iron-oxidizing bacteria or the like.

Also, iodide ions may be supplied in any form. For example, it may be added in the form of simple iodine (chemically reacts to produce iodide ions in solution), iodide (eg, potassium iodide), or the like.

(4) Total amount of copper contained in the copper ore In one embodiment, the method of the present invention can include a fourth step of measuring the total amount of copper contained in the copper ore. The total amount of copper contained in the copper ore can be measured by the method of alkali fusion/wet analysis (ICP-OES) after filtering the leached solution. Also, the total amount of copper can be obtained by directly measuring the amount of copper contained in crude ore. Alternatively, the total amount of copper can be obtained by totaling the amount of copper contained in each of the post-leaching solution and the leaching residue. By calculating the total amount of copper, the leaching rate can be calculated. Therefore, based on the estimated amount obtained from the sample, the amount of leaching in the column test can be estimated.

The first to third steps described above can be performed in any order. Alternatively, the first to third steps can be performed at least partially in parallel. Furthermore, the step of measuring the total amount of copper contained in the copper ore can also be performed in any order, and can be performed at least partially in parallel with the first to third steps.

When performed in parallel, the sample may be divided into three portions and each subjected to steps 1-3. Alternatively, the sample may be divided into four parts and subjected to steps 1-4 respectively. In addition, it is possible to shorten the time by implementing in parallel.

When carried out sequentially, the sample is first subjected to the first step and after the first step the residue is removed by solid-liquid separation. Next, the residue is subjected to the second step, and then the residue is taken out by solid-liquid separation. Finally, the residue may be taken out by solid-liquid separation and subjected to the third step. With the sequential method, even if the sample amount is small, it can be evaluated without loss of accuracy (for example, with the parallel method described above, the sample must be divided, so one less sample for analysis). Also, the sequential method can reduce the problem of sample variation (eg, the parallel method described above cannot rule out the possibility of bias when the sample is split).

3. Leaching Method in Column Test After performing the above analysis with a sample of copper ore, leaching of copper in a column test can be performed.

(1) Copper oxide ore and secondary copper sulfide ore For example, if the copper ore is judged to have a large proportion of copper oxide ore through the above analysis results, a leaching method suitable for copper oxide ore can be adopted. Further, when it is judged from the above analysis results that the copper ore contains a large proportion of secondary copper sulfide ore, a leaching method suitable for the secondary copper sulfide ore can be adopted. Suitable leaching methods for copper oxide ores and secondary copper sulfide ores include, but are not limited to, dump leaching and heap leaching.

In adopting the above-described leaching method, the estimated amounts obtained in the above-described first to third steps (more preferably first to fourth steps) can be referred to.

For example, when the first to third steps (more preferably, the first to fourth steps) are performed at least partially in parallel, the leaching rate estimated based on the leaching amount obtained in the second step can be referred to. In one example, when the leaching rate is 70% or more, it may be determined to adopt a leaching method suitable for copper oxide and secondary copper sulfide ore.

As another example, when the first to third steps are performed sequentially, the leaching rate estimated based on the leaching amounts obtained in the first and second steps can be used as a reference. In one example, when the leaching rate is 70% or more, it may be determined to adopt a leaching method suitable for copper oxide and secondary copper sulfide ore.

(2) Primary copper sulfide ore As a leaching method suitable for primary copper sulfide ore, the iodine method is mentioned. The iodine method is a method of leaching copper with a solution containing iron (III) ions and iodide ions.

In the present specification, the “leaching method using the iodine method” includes any one of the following leaching methods A to C or a combination thereof.

<Leaching method A using iodine>
A method of leaching copper from an ore using a solution containing iodide ions and iron (III) ions as a leachant.

Although the following description is not intended to limit the present invention, for example, the above leaching proceeds through a series of iodine-catalyzed reactions shown in (Equation 1) and (Equation 2) below.
2I ⁻ + 2Fe ³⁺ → I ₂ + 2Fe ²⁺ (equation 1)
CuFeS ₂ + I ₂ + 2Fe ³⁺ → Cu ²⁺ + 3Fe ²⁺ + 2S + 2I ⁻ (equation 2)

This catalytic reaction by iodine enables efficient leaching of copper from the copper sulfide ore.

Since iodine has low solubility in water, iodide, which is easily dissolved in the leachate and dissociated into iodide ions, is added to the leachate. Any iodide may be used as long as it is soluble in water and generates iodide ions. For example, sodium iodide, potassium iodide, ammonium iodide, hydrogen iodide and the like can be used.

The leaching method can utilize a leaching form such as copper hydrometallurgy using a sulfuric acid solution as the leaching liquid. That is, copper can be leached from the ore using a sulfuric acid solution containing iodide ions and iron (III) ions. Further, for example, heap leaching, dump leaching, or the like may be used in which sulfuric acid is sprayed on a piled ore and copper is leached into the sulfuric acid, in addition to batch stirring leaching. Furthermore, in-place leaching can also be used as a method similar to laminate leaching, in which a leaching solution is poured into an ore body located underground for leaching.

In addition, iodine recovered from the post-leaching liquid by an anion exchange resin, post-oxidation aeration (blowout) with an oxidizing agent, solvent extraction, or the like, is in the form of a solution containing iodine in the form of the above various iodide forms or in other forms. It can also be reused.

In the leaching method, the leaching temperature is not particularly specified, but the leaching can be carried out at room temperature without the need for heating.

In addition, the total iodine concentration in the leachate can be appropriately determined depending on the reaction mode, the type, shape, and copper grade of the target copper sulfide ore. /L or 8 mg/L to 100 mg/L as shown in Japanese Patent No. 4950257 is preferred.

In addition, the ratio of the iron (III) ion concentration to the total iodine concentration in the leachate is, for example, 20 times or more by weight (iron (III) ion concentration is 2 g/L or more with respect to the iodide ion concentration of 100 mg/L). It is preferable to The source of iron (III) ions is not particularly limited, and iron (III) sulfate, iron (II) chloride, or those obtained by oxidizing iron (II) ions in an iron (II) sulfate solution, or as described later. An iron (II) ion-containing acidic solution obtained in the iron oxidation step can be preferably used. As the leachate, it is preferable to use one whose pH is adjusted to 2.5 or less with sulfuric acid or the like in order to prevent precipitation of iron (II) ions.

<Leaching method B using iodine>
A method of leaching copper from an ore using a sulfuric acid solution containing iron(III) ions as a leaching solution, and further leaching copper from the ore with a solution containing iodide ions and iron(III) ions for the leaching residue. .

In the above-described leaching method, a first-stage leaching step in which copper is leached by an oxidative leaching reaction of iron (III) ions that do not contain iodine, such as a ferric leaching method or a bacterial leaching method, and after the first-stage leaching step, iodine is and a second leaching step of leaching with a solution containing oxide ions and iron (III) ions.

Conditions such as the total iodine concentration in the leachate in the second stage leaching process, the ratio of iron (III) ion concentration to the total iodine concentration, pH, temperature, etc. good.

In the first-stage leaching process, copper oxide ore and secondary copper sulfide ore mixed in the leachate are leached by oxidation leaching reaction such as ferric leaching method or bacterial leaching method that does not contain iodine. Therefore, since iodine is not used in this first-stage leaching, there is no loss of iodine.

In addition, first, relatively soluble copper oxide ore and secondary copper sulfide ore are leached by the oxidizing power of iron (III) ions, and after the initial leaching, iodine is used to dissolve the insoluble primary sulfide ore. Therefore, the loss of iodine due to volatilization and the loss of iodine due to the reaction of iodide ions with Cu ²⁺ in (Formula 2) to produce CuI, which is poorly soluble, can be reduced.

In the first-stage leaching process, the leaching treatment of the secondary copper sulfide ore in the copper ore is continued until the leaching rate reaches 80% or more, to the extent that iodide ions and copper do not precipitate. It is preferable from the viewpoint of lowering the copper concentration of the leachate. Furthermore, in the first-stage leaching step, it is preferable from the viewpoint of setting an appropriate first-stage leaching period that the copper sulfide ore is leached by spraying 1 to 3 m ³ of the leaching solution per 1 ton of ore.

In the first stage leaching step, the concentration of iron (III) ions in the leaching solution is preferably 2 g/L or more from the viewpoint of keeping the leaching rate from being too low, and a realistic range from the viewpoint of reuse. is preferably 5 g/L or less.

In addition to the leaching method shown in A above, the analysis method according to one embodiment of the present invention is the leaching method shown in B above. , and the amount of copper leached by the leaching methods shown in A and/or B above can be quantified with high accuracy.

<Leaching method C using iodine method>
The leaching methods A-B described above may be modified so that the leaching solution further comprises sulfuric acid. This sulfuric acid is a component corresponding to the solution used in the first step in the analysis method described above. By using this leaching method, it is possible to obtain a leaching result that matches the estimated leaching amount obtained by the analysis method described above.

<Conditions for adopting the iodine method>
In one embodiment, the conditions for employing the iodine method as the leaching method may be as follows.
CuIns <= 20% (more preferably CuIns + CuIod > 30%)
here,
CuIns: The ratio of undissolved Cu in the solution containing trivalent Fe ions and iodide ions described in "(3) Estimation of leaching amount corresponding to primary copper sulfide ore"
CuIod: Percentage of dissolved Cu in the solution containing trivalent Fe ions and iodide ions described in "(3) Estimation of leaching amount corresponding to primary copper sulfide ore"

4. Method for Selecting Copper Ore and Method for Selecting Leaching Means The analysis method can be applied in various ways. For example, when there are multiple candidate copper ores, selecting a copper ore suitable for a particular leaching method (e.g., iodine method, dump leaching, heap leaching, etc.) based on the results of the above analytical methods. can be done. In another example, when selecting the optimum leaching method for a mined copper ore, the leaching method can be selected based on the results of the analytical methods described above. In another example, whether the extracted copper ore is suitable for a particular leaching method (e.g., iodine method, dump leaching, heap leaching, etc.) can be determined based on the results of the above analytical methods. .

5. Manufacture of Electrolytic Copper The present invention, in one embodiment, can include a method for manufacturing electrolytic copper. The method can include performing the prediction method described above (the method described in the section “2. Prediction method of leaching amount”). Further, the method for producing electrolytic copper may include a step of actually leaching copper from the copper ore after estimating the amount of leaching. The step of leaching copper can include performing the leaching method described above (the method described in the section “3. Leaching method in column test”). A copper leaching solution can be obtained through the above steps. From the resulting leachate, copper ions can be selectively recovered-concentrated by Solvent Extraction (SX). Electrolytic copper can be produced from the copper liquid by electrowinning (EW).

The following examples are intended to facilitate a further understanding of the invention. it is not intended to limit the scope of the invention.

6. Analysis method In order to measure the ratio of copper oxide ore, primary copper sulfide ore, and secondary copper sulfide ore in copper ore, sequential analysis (as a comparative example), 1m column test (as a reference example), and an analysis method using iodine ( as an example) was performed.

6-1. Sequential analysis Sequential analysis was performed by the following procedure.
(1) Copper oxide ore: Add sulfuric acid to a sample pulverized to a certain particle size and stir for a certain period of time. Quantification of eluted copper (CuAS).
(2) Secondary copper sulfide ore: A sodium cyanide solution was added to the solid portion obtained by solid-liquid separation for analysis of copper oxide ore, and the mixture was stirred for a certain period of time. Quantification of eluted copper (CuCN).
(3) Primary copper sulfide ore: Nitric acid and perchloric acid were added to the solid portion obtained by solid-liquid separation of secondary copper sulfide ore, and after drying on a hot plate, hydrochloric acid and distilled water were added to dissolve the solid. Quantification of eluted copper (CuIns).

6-2.1 m column test The 1 m column test is a test method that can obtain results close to the leaching results obtained on the scale of actual operation. However, the drawback is that it takes several months to obtain results. The 1m column test includes a 1m column conventional method test and a 1m column iodine method test.

In order to make the sample representative of the whole, the sample was first reduced (sample reduction). After that, it was classified using a 4.75 mm sieve. The sample that passed through the sieve and the sample that remained on the sieve were mixed, and a total of 12 kg of the sample was packed in a column with a height of 1 m and a spread area of 7.85×10 ⁻³ m ² . An infusion was then prepared. In the case of the 1 m column conventional method test, a leaching solution having a pH of 1.6 and an iron (III) concentration of 5 g/L (Fe source is iron sulfate n-hydrate) was prepared. In the case of the 1 m column iodine method test, for example, pH 1.6, iron (III) concentration 5 g / L (Fe source is iron sulfate n-hydrate), iodide ion concentration 100 mg / L (iodide ion source (potassium iodide) was prepared. The leachate was supplied from the top of the column at a rate of 1 L/day. This was done for up to 120 days. Then, the amount of Cu contained in the solution passed through the column was measured.

6-3. Analytical method using iodine The analytical method using iodine was carried out according to the following procedure.
A copper ore sample was divided into four. An analytical laboratory was commissioned to determine the total amount of copper (CuT) contained in the first copper ore sample. The second copper ore sample was leached under the following conditions, and the leaching amount of Cu was measured (CuAS).
Temperature: 25°C
Ingredient: Sulfuric acid (5% v/v)
Time: 1h
Shaking speed: 180rpm
Ore amount: 40g/L
Mineral particle size: -100 μm (i.e., the size that passes through a sieve with a mesh size of 100 μm, and so on)

A third copper ore sample was leached under the following conditions. Then, the leaching amount of Cu was measured (CuFe).
Temperature: 50°C
Ingredients: Fe ³⁺ (5g/L)
Time: 24h
Shaking speed: 120rpm
Ore amount: 40 g/L (coarse ore), 0.8 g/L (single mineral)
Mineral grain size: -100 μm

A fourth copper ore sample was leached under the following conditions. Then, the leaching amount of Cu was measured (CuIod).
Temperature: 25°C
Ingredients: Fe ³⁺ (5 g/L), I ⁻ (1600 mg/L)
Time: 24h
Shaking speed: 120rpm
Ore amount: 40 g/L (coarse ore), 0.8 g/L (single mineral)
Mineral grain size: -100 μm

The copper concentration and iron concentration in the leachate were measured by an ICP emission spectrometer (ICP-AES), and the iodine concentration was quantified by an ion electrode method after reduction to iodide ions.

The amount of copper leaching in each sample was measured by the above method. The CuT recovery was then calculated by dividing the measured value by the total amount of copper (CuT) in the sample.

7. Leaching amount corresponding to secondary copper sulfide ore and difference due to analysis method Four types of coarse ore (samples A to D) were adopted as samples from different mines.

The three types of analysis methods described above were performed (however, for the 1m column test, the usual method was adopted), and the leaching amount corresponding to the secondary copper sulfide ore was measured. The results are shown in FIG. In the graph of FIG. 1, for the sequential analysis, the point in time when 80% of the CuAS is leached is plotted as the point in time when the amount of the leaching liquid corresponds to 0.5 m ³ /t. Further, for the analysis method using iodine, the point at which 80% of the CuFe is leached is plotted as the point at which the amount of the leaching liquid corresponds to 0.5 m ³ /t.
For all crude ores (Samples A, B, D), the results of analysis by 1 m column test and analytical method using iodine were similar to the results of sequential analysis. On the other hand, for the sample containing Jarosite/carbonate (Sample C), where there was a discrepancy between the results of the 1 m column test and the results of the sequential analysis, the results of the analysis method using iodine were better than the results of the sequential analysis. The result was close to the result.

8. Leaching amount corresponding to primary copper sulfide ore and differences due to analysis method Six types of coarse ore (samples 1 to 6) were used as samples from different mines.

A sequential analysis, an analytical method using iodine, a 1 m column iodine method test, and a 1 m column conventional method test were performed. Then, ΔCuT was calculated according to the following formula.
ΔCuT=Cu leaching rate by 1 m column iodine method test−1 m column leaching rate by conventional method test This value represents the magnitude of merit of adopting the leaching method using the iodine method compared to the conventional method. FIG. 2 shows the leaching results for the primary copper sulfide ore from the above copper ore samples.

Referring to FIG. 2, samples 1, 5, and 6 had CuIns values greater than 20%. And the value of ΔCuT was low. Therefore, based on the analytical method using iodine, it can be judged that there is little merit in adopting the leaching method using the iodine method.
On the other hand, in samples 2 to 4, the CuIns value was 20% or less. And the value of ΔCuT was high. Therefore, based on the analytical method using iodine, it can be determined that there is a high merit in adopting the leaching method using the iodine method.

In this specification, the descriptions of "or" and "or" include cases where only one option is satisfied and cases where all options are satisfied. For example, in the case of the description "A or B" and "A or B", it includes the case where A is satisfied and B is not satisfied, the case where B is satisfied and A is not satisfied, and the case where A is satisfied and B is satisfied. intended to be

Specific embodiments of the present invention have been described above. The above embodiments are only specific examples of the present invention, and the present invention is not limited to the above embodiments. For example, technical features disclosed in one of the above embodiments can be provided in other embodiments. Also, for a particular method, some steps may be interchanged with other steps, and additional steps may be added between two particular steps. The scope of the invention is defined by the claims.

Claims (8)

A method for estimating the leaching amount of copper corresponding to copper oxide, secondary copper sulfide ore, and/or primary copper sulfide ore from copper ore, the method comprising:
A first step of leaching copper from copper ore with a sulfuric acid solution to measure the amount of leached copper A as copper oxide, the step being carried out under leaching conditions where the particle size of the mineral is 150 μm or less;
A second step of leaching copper from the copper ore or the leaching residue of the first step with a solution containing iron (III) ions and measuring the leached copper amount B, carried out under leaching conditions such that the grain size of the mineral is 150 μm or less. In the case of leaching from copper ore, the amount of leached copper B is the total leaching amount of copper oxide and secondary copper sulfide ore, and in the case of leaching from the leaching residue of the first step, The step of leaching copper from the copper ore or the leaching residue of the second step with a solution containing iron (III) ions and iodide ions. , a third step of measuring the leached copper amount C, which is a step performed under leaching conditions with a mineral grain size of 150 μm or less, and when leaching from a copper ore, the leached copper amount C is determined by copper oxide and secondary It is the total leached amount of copper sulfide ore and primary copper sulfide ore, and in the case of leaching from the leaching residue of the second step, the leached copper amount C is the leached amount of primary copper sulfide ore.
Here, when the second step and the third step are leaching from the copper ore, the first to third steps may be performed in any order. 2. The method of claim 1, further comprising a fourth step of determining the total copper content D contained in the copper ore. 3. The method of claim 2, wherein steps 1-4 are performed at least partially in parallel. 4. The method of claim 3, further comprising estimating the leaching rate according to the relationship:
estimating the leaching rate a based on the values of the leached copper amount A and the total copper amount D;
estimating the leaching rate b based on the difference between the leached copper amount B and the leached copper amount A leached from the copper ore , and the value of the total copper amount D; and
Estimate the leaching rate c based on the difference between the leached copper amount C leached from the copper ore and the leached copper amount B leached from the copper ore , and the value of the total copper amount D. The method of claim 2, wherein
Performing the second step on the residue obtained in the first step,
Performing the third step on the residue obtained in the second step,
the method. 6. The method of claim 5, further comprising estimating the leaching rate according to the relationship:
estimating the leaching rate a based on the values of the leached copper amount A and the total copper amount D;
estimating a leaching rate b based on the values of the leached copper amount B and the total copper amount D; and estimating the leaching rate c based on the values of the leached copper amount C and the total copper amount D. A method for producing electrolytic copper, the method comprising:
Evaluating a copper ore according to the method of any one of claims 1-6:
The process of leaching copper from copper ore:
A process of refining electrolytic copper from a copper leachate. A method for producing electrolytic copper, the method comprising:
Estimating copper leaching rate according to the method of any one of claims 4 and 6:
A step of leaching copper from a copper ore using a solution containing iodide ions and iron (III) ions when (leaching rate a + leaching rate b + leaching rate c) > 80 (%):
A process of refining electrolytic copper from a copper leachate.

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