OA19662A - Process for the recovery of lithium. - Google Patents

Abstract

A process is divulged for the recovery of lithium from metallurgic slags comprising the steps of roasting spodumene to convert it from the alpha to the beta variant; reacting the beta variant with sulfuric acid, using a stoichiometric excess of acid; repulping the reaction product with water, forming an acidic slurry; neutralizing the acidic slurry to a pH between 5 and 7, by addition of at least one neutralizing agent; filtrating the neutralized slurry, thereby obtaining a lithium bearing solution and a residue; characterized that, in either one or both of the steps of repulping and neutralizing the acidic slurry, lithium-bearing metallurgic slag is added as neutralization agent. The lithium-bearing metallurgic slag is used to substitute at least part of the classic neutralizing agent. The lithium in the slag is released, and added to the lithium liberated from the spodumene.

Description

Process for the recovery of lithium

The présent invention relates to an enhanced process for the recovery of lithium from a lithiumbearing slag.

Such a slag can be obtained when recycling lithium-ion batteries or their derived products using a pyrometallurgical smelting process. The batteries and a slag-forming flux, comprising one or more of oxides of Silicon, calcium, aluminum, magnésium, iron, and manganèse, are melted together at high température. An oxygen potential is chosen that resuit in the formation of a cobalt-nickel-copper metallic phase, and a slag. The more easily oxidized éléments, where under lithium, report to the slag. The organic fraction in the batteries is effectively pyrolized, and the residual volatiles are captured in an off-gas purification System.

The recovery of lithium from such slags has been studied but remains complex and expensive. According to known processes, the slag is leached in acidic conditions. A leachate containing most of the lithium is then obtained. The aluminum in the slag is however partially soluble, causing problems such as the précipitation of lithium aluminates and the formation of aluminum hydroxide flakes that tend to adsorb lithium. These phenomena may dégradé the lithium recovery yield.

Despite these technical hurdles, the slag issued from the pyrometallurgical treatment of lithiumion batteries represents a high-grade source of lithium.

CN105907983(A) proposes a method to extract lithium from such a slag. The slag is dissolved in sulfuric acid in dilute conditions, in order to prevent the précipitation of lithium aluminates when the solution is neutralized to a pH of about 6. The leachate needs to be concentrated by évaporation of water before being further processed. Although technically feasible, this process is not economical as the diluted operating conditions call for an expensive subséquent évaporation step. Also, the amounts of reagents needed for the subséquent neutralization and purification are considérable, leading to the production of gypsum that cannot be valorized.

WO2011141297(A1) uses a lithium-bearing slag produced from the pyrometallurgical treatment of lithium-ion batteries as an additive in concrète. This method takes advantage of the bénéficiai properties of lithium to reduce the reaction of alkali metals in the concrète. It provides for a meaningful utilization of the slag as such, but does not lead to the recovery of lithium. This reduces the économie value of the slag.

It thus appears that the séparation of lithium from aluminum- and lithium-bearing slags is problematic, as both aluminum and lithium leach during acid treatment, and tend to coprecipitate.

Another widely exploited source of lithium is spodumene. Spodumene is a pyroxene minerai consisting of lithium alumino-silicate, LiAI(SiO₃)2. The équivalent of approximately 80.000 tons of lithium carbonate is annually produced from this source. The spodumene processing flow sheet usually consists of a number of unit operations, comprising the steps of: - roasting spodumene to couvert it from the alpha to the beta variant;

- reacting the beta variant with sulfuric acid, using a stoichiometric excess of acid;

- repulping the reaction product with water, forming an acidic slurry;

- neutralizing the acidic slurry to a pH between 5 and 7, by addition of at least one neutralizing agent;

- filtrating the neutralized slurry, thereby obtaining a lithium bearing solution and a residue; - purification and précipitation of the lithium, typically as hydroxide or carbonate.

After spodumene ores hâve been mined, concentrated and comminuted, the finely divided material is submitted to a first high-temperature treatment step during which alpha spodumene is converted into beta spodumene. After the phase transformation, the material is mixed with sulfuric acid and submitted to a roasting step that aims to liberate the lithium from the minerai. This step is performed at 250-300 °C with an excess of acid w.r.t. lithium.

The roasted material is subsequently mixed with water, upon which the Li₂SO₄ dissolves, together with the free sulfuric acid. Remarkably, no aluminum is leached in this step. This is assumed to be due to the stable alumino-silicate framework that is formed during the alpha to beta conversion of spodumene. Next, a conventional neutralizing agent such as CaCO₃, CaO, or Ca(OH)₂ is added to neutralize the free acid and to precipitate a number of impurities.

Typically, the neutralization step is performed at a pH of 5 to 6 so as to remove impurities such as aluminum, Silicon and iron from the solution. A solid-liquid séparation step is applied to separate the crude Li₂SO₄ solution from the residue that contains aluminum silicates, gypsum and precipitated impurities mostly.

Further purification steps are then applied for the removal of calcium, magnésium, and other impurities.

Although variants of this process are being applied by different lithium producers, most of these flow sheets feature some inhérent drawbacks. In particular, the excess sulfuric acid that is used in the roasting step will need to be neutralized prior to the purification steps, and this will require considérable amounts of neutralizing agent. Classically, calcium-based compounds are used, leading to the formation of a large amount of gypsum, which is considered as an undesired, yet unavoidable waste.

It has now been found that the usual spodumene processing flow sheet, and the flow sheet for processing lithium- and aluminum-bearing slags, can be combined in a way to solve the problems associated with each.

To this end, a process is divulged for the recovery of lithium from métallurgie slags comprising the steps of roasting spodumene to convert it from the alpha to the beta variant; reacting the beta variant with sulfuric acid, using a stoichiometric excess of acid; repulping the reaction product with water, forming an acidic slurry (solid/liquid mixture); neutralizing the acidic slurry to a pH between 5 and 7, by addition of at least one neutralizing agent; filtrating the neutralized slurry, thereby obtaining a lithium bearing solution and a residue; characterized that, in either one or both of the steps of repulping and neutralizing the acidic slurry, lithium-bearing métallurgie slag is added as neutralization agent.

As the skilled person will appreciate, repulping and neutralization can be combined in a single step.

The lithium-bearing métallurgie slag is hereby used to substitute at least part of the conventional neutralizing agent. In this neutralization step, most of the lithium in the slag is released and suppléments the lithium liberated from the spodumene.

To ensure the optimum release of the lithium from the slag, it is preferred to neutralize with lithium-bearing slag up to a pH of less than 4. One can then proceed with a conventional neutralization agent to reach a pH between 5 and 7. This latter pH range provides for the preliminary purification of the leachate, in particular by précipitation of aluminum. Suitable conventional agents are CaCO₃, CaO, and Ca(OH)₂, which can be combined. Sodium-based agents are also suitable.

The lithium-bearing slag will typically originate from smelting of lithium-bearing primary or secondary batteries, or their derived products, such as spent batteries, battery scrap, black mass, etc., as long as appréciable quantifies of lithium remain présent.

Suitable slags may hâve a by-weight composition according to: 3% < Li₂O < 20%;

38% < AI₂O₃ < 65%; CaO < 55%; and, SiO₂ < 45%.

With respect to the recovery of lithium from aluminum- and lithium-bearing slags, the introduction of the slag in the spodumene flow sheet gives rise to only a modest increase of the aluminum concentration in the leachate. The amount of slag used to perform the neutralization is indeed relatively minor in view of the total quantity of leachate. It has been determined that this modest increase of the aluminum concentration can be dealt with, as it does not lead to unacceptable losses of lithium.

With respect to the spodumene flow sheet, the incorporation of the slag as neutralizing agent reduces significantly the amount of gypsum that is formed during conventional neutralization. Neutralizing with a lithium-bearing compound moreover enriches the solution in lithium, leading to generally better economy and recovery yield.

In another embodiment, a first neutralization step is performed using a conventional lithium-free neutralization agent. This is followed by a second neutralization step performed using lithiumbearing slag. Optionally, and for the reasons explained above, a third neutralization step can be performed, again using a conventional agent. The rationale behind this scheme is that less aluminum is leached from the slag, as it does not encounter the initial strongly acidic conditions. The contained lithium still leaches with high yields, as long as the pH remains below about 4.

In another embodiment, the lithium-bearing slag is added to the spodumene in the step of reacting. This embodiment is especially useful when the slag is richer in lithium than the spodumene, as it will lead to an advantageous increase of the lithium concentration in the leachate. However, the amount of gypsum is not reduced in this case.

In Example 1, a typical spodumene flow sheet is illustrated comprising the steps: - thermal treatment 1050 °C during 30 min.;

- sulphate roasting at 250 °C during 30 min., using 1.4 times the stoichiometric amount required for lithium leaching in spodumene (3,3 % U), corresponding to 330 g sulfuric acid per kg spodumene, of which 95 g is excess; and,

- leaching with a liquid/solid ratio of 1.85 for 15 min. at room température.

Table 1: Initial composition of roasted beta-spodumene (%)

Li	Ca	Al	Si
3,3	0	14	30

Table 2: Composition of the acidic leaching solution (g/L)

LI2SO4	H2SO4	Ca	Al	Si
140	51	0	0	0

The excess acid is neutralized by addition of Ca(OH)₂, followed by filtration. The elemental composition of the filtrate remains hereby essentially unchanged. The solution can be purified and lithium precipitated, resulting in a lithium yield of about 90%.

In Example 2, the same conditions as in Example 1 are applied. However, the excess acid is neutralized to about 1 g/l H₂SO₄, which corresponds to a pH of about 2, by addition of lithium bearing slag according to the composition reported in Table 3.

Table 3: Composition of the lithium-bearing slag (%)

Li	Ca	Al	Si
5.0	8,98	17,66	10,61

Table 4: Composition of the leaching solution after neutralization with slag (g/L)

LI2SO4	H2SO4	Al	Ca	Si
164	1	2,2	0,5	-

The lithium concentration in the solution is significantly higherthan when a conventional neutralizing agent is used, thanks to the contribution of the lithium in the slag. The leachate however contains a limited amount of aluminum. It is therefore important to show that this limited amount will not resuit in lithium losses.

This is the object of Example 3.

In this Example, an acidic solution containing 18 g/L Li (équivalent to 143 g/L Li₂SO₄) and 50 g/L H₂SO₄ is prepared. This corresponds to the composition of a typical spodumene leaching solution. This solution is heated to 70 °C and subsequently neutralized to a pH of 2.5 using a milled sample of lithium-containing slag. Lithium (3%), aluminum (19%), calcium (19%), and SiO₂ (21%) are the most important constituents of the slag, which is found to also contain traces of Co, Cu, Fe, Mg, Ni and Mn.

After neutralization to pH 2.5, a sample of the slurry is filtered and washed, and both the filtrate and the residue are analyzed for lithium and aluminum. The filtrate contains 6.4 g/L Al and the residue contains 0.11% Li. From these values, leaching yields of about 100% for lithium and aluminum are determined.

The pH of the slurry is further raised to 5.5 using lime, in order to purify it by precipitating the dissolved aluminum. This slurry is filtered and washed, and both the filtrate and the residue are analyzed for lithium and aluminum. The filtrate contains 1.1 mg/LAI, indicating that virtually ail the aluminum is precipitated. The residue is found to contain 0.58% Li.

The aluminum is thus thoroughly eliminated from the filtrate. As for lithium, it can be calculated that the solution contains, in addition to ail the lithium of the original solution, also about 60% of the lithium added with the slag. The overall lithium recovery in the purified filtrate is thus good.

Example 4 illustrâtes that a réduction in the amount of aluminum in the leaching solution further limits the loss of lithium when the solution is purified. Hitherto, the quantity of slag used in the neutralizing step is reduced, and complemented by another neutralizing agent such as lime.

The same acidic solution and milled slag as in Example 3 are prepared. This solution is however neutralized to a pH of 0.5 instead of 2.5 using the slag. The amount of slag is about half the amount needed in Example 3.

After neutralization to pH 0.5 using slag, the pH of the slurry is further raised to 5.5 using lime, in order to purify it by precipitating the dissolved aluminum. This slurry is filtered and washed, and both the filtrate and the residue are analyzed for lithium and aluminum. The filtrate contains 1 mg/LAI, indicating that virtually ail the aluminum is precipitated. The residue is found to contain 0.3% Li.

The aluminum is thus thoroughly eliminated from the filtrate. As for lithium, it can be calculated that the solution contains, in addition to ail the lithium of the original solution, also about 80% of the lithium added with the slag. The overall lithium recovery in the purified filtrate is thus excellent.

Claims (7)

1. Claims

   1. Process for the recovery of lithium from métallurgie slags comprising the steps of:

   - roasting spodumene to convert it from the alpha to the beta variant;

   - reacting the beta variant with sulfuric acid, using a stoichiometric excess of acid;

   - repulping the reaction product with water, forming an acidic slurry;

   - neutralizing the acidic slurry to a pH between 5 and 7, by addition of at least one neutralizing agent;

   - filtrating the neutralized slurry, thereby obtaining a lithium bearing solution and a residue;

   characterized that lithium-bearing métallurgie slag is added in one or more of the steps of reacting, repulping, and neutralizing the acidic slurry.
2. 2. Process according to claim 1, wherein the lithium-bearing métallurgie slag is added in either one or both of the steps of repulping and neutralizing the acidic slurry, as a neutralizing agent.
3. 3. Process according to claim 2, whereby, in the step of neutralizing the acidic slurry, lithium-bearing métallurgie slag is added as a first neutralization agent up to a pH of less than 4 is reached, where after a second neutralization agent is added until a pH between 5 and 7 is reached.
4. 4. Process according to claims 2 or 3, wherein the second neutralization agent comprises CaCO₃, CaO, or Ca(OH)₂.
5. 5. Process according to any one of claims 1 to 4, wherein the lithium-bearing métallurgie slag is produced by smelting of lithium-bearing batteries or their derived products.
6. 6. Process according to any one of claims 1 to 5, wherein the lithium-bearing métallurgie slag has a by a by-weight composition according to: 3% < Li₂O < 20%; 38% < AI₂O₃ < 65%;

   CaO < 55%; and, SiO₂ < 45%.
7. 7. Process according to any one of claims 1 to 6, comprising the further steps of purifying the lithium bearing solution, and of separating the lithium by précipitation.