FR3044002A1 - PROCESS FOR THE PREPARATION OF AN ADSORBENT MATERIAL BASED ON THE BASIC MIXING OF A DRIED DRY POWDER OR OVEN OR BY ATOMIZATION AND METHOD OF EXTRACTING LITHIUM - Google Patents

Abstract

The present invention relates to the field of solid materials for the adsorption of lithium. In particular, the present invention relates to a new process for the preparation of a crystallized and shaped solid material, preferably in extruded form, of formula LiXx.2Al (OH) 3, nH2O with n being between 0 , 01 and 10, where x is 1 when X is an anion selected from chloride, hydroxide and nitrate anions, and x is 0.5 when X is an anion selected from sulfate and carbonate anions, comprising a step a ) precipitation of boehmite under specific temperature and pH conditions, a drying step in an oven, oven or by atomization so as to obtain a powder and at least one step of shaping said powder by basic extrusion, said method also comprising a final hydrothermal treatment step, all to increase the adsorption capacity of lithium and the adsorption kinetics of the materials obtained compared to the materials of the prior art when this it is used in a lithium extraction process of saline solutions.

Description

PROCESS FOR THE PREPARATION OF AN ADSORBENT MATERIAL BASED ON THE BASIC MIXING OF A DRIED DRY POWDER OR OVEN OR BY ATOMIZATION AND METHOD OF EXTRACTING LITHIUM

Technical area

The present invention relates to the field of solid materials for the adsorption of lithium. In particular, the present invention relates to a new process for preparing a crystallized and shaped solid material, preferably in extruded form, of the formula LiXx.2Al (OH) 3, nH20 with n being between 0 , 01 and 10, where x is 1 when X is an anion selected from chloride, hydroxide and nitrate anions, and x is 0.5 when X is an anion selected from sulfate and carbonate anions, comprising a step a ) precipitation of boehmite under specific temperature and pH conditions, a drying step in an oven, oven or by atomization so as to obtain a powder and at least one step of shaping said powder by basic extrusion, said method also comprising a final hydrothermal treatment step, the set of characteristics of the process for increasing the mechanical strength of the materials obtained and the lithium adsorption capacity and the kinetics of Adsorption of the obtained materials over the materials of the prior art when it is used in a lithium extraction process of saline solutions.

The present invention also relates to a method for extracting lithium from saline solutions using said crystalline solid material of formula UXx.2AI (OH) 3, nH20 with n, x and X having the above definition prepared according to the new process preparation according to the invention.

Prior art

Lithium ions coexist with massive amounts of metals such as, for example, alkalis, alkaline earths, boron and sulphates, especially in saline solutions such as brines. Thus, they must be extracted economically and selectively from these salt solutions. Indeed, the chemical properties of lithium and alkali metals, preferably sodium (Na), and potassium (K) and alkaline earth metals, preferably magnesium (Mg), calcium (Ca) and strontium ( Sr), make it difficult to separate these elements.

The solid materials of formula LiCl 2 Al (OH) 3, nH 2 O with n being between 0.01 and 10 are known for their use in the phenomena of adsorption / desorption of lithium ions and in particular in the processes of extraction of lithium ions. lithium from saline solutions. These unstable structures would allow the intercalation of lithium atoms in the structure and thus the extraction of lithium.

Several operating protocols leading to solids capable of selectively adsorbing lithium have been demonstrated in the prior art. In all cases, a solid aluminum trihydroxide AI (OH) 3, prepared or commercial, is contacted with a lithium precursor. Three main precursors are used: the most used is lithium chloride (LiCl). Aluminum hydroxide (LiOH) or lithium carbonate (U2CO3) can also be used.

US Pat. No. 6,280,693 describes a process for preparing a LiCl / Al (OH) 3 solid by adding an aqueous solution of LiOH to a polycrystalline hydrated alumina to form LiOH / Al (OH) 3, and thus create lithium sites active in the crystalline layers of alumina without altering its structure. The conversion of LiOH / Al (OH) 3 to LiCl / Al (OH) 3 is then carried out by adding dilute hydrochloric acid. The alumina pellets thus prepared are then used in a process for extracting lithium from brine at high temperature. The lithium extraction method described in US Pat. No. 6,280,693 uses the solid detailed above and comprises the following steps: a) Saturation of a bed of solid by a brine containing a lithium salt LiX, X being chosen from halides, nitrates, sulphates and bicarbonates, b) displacement of the brine impregnated with a concentrated solution NaX, c) elution of LiX salt captured by the solid by passage of an unsaturated solution of LiX, d ) Moving the impregnant with a concentrated solution of NaX, steps a) to d) are then repeated at least once.

The patent RU 2,234,367 describes a process for preparing a solid of formula LiCl 2 Al (OH) 3, nH 2 O comprising a step of mixing aluminum trichloride (AlCl 3) and lithium carbonate (Li 2 CO 3) in the presence of water at 40 ° C. The resulting residue is filtered and washed and then dried for 4 hours at 60 ° C. The balance thus obtained is not formatted.

The solid obtained is used for the extraction of lithium contained in saline solutions by contact with water in order to remove part of the lithium and then placed in contact with a saline solution containing lithium. The static capacity thus obtained is between 6.0 and 8.0 mg of lithium per g of solid.

CN1243112 discloses a process for the preparation of a solid of formula LiCI.2AI (OH) 3, nH20 comprising a step of precipitation of aluminum hydroxide microcrystals AI (OH) 3 by contacting AICI3 and sodium hydroxide NaOH, and then bringing said microcrystals into contact with a 6% solution of lithium chloride LiCl at 80 ° C. for 2 hours followed by filtration, rinsing and drying to obtain a powder LiCI.2AI (OH) 3, nH20 with an unordered and amorphous structure. A solution of a macromolecular polymer chosen from fluorinated resins, polyvinyl chloride (PVC), chlorinated polyvinyl chloride (CPVC), ethylene perchlorate and cellulose acetate butyrate (CAB) acting as binder is then mixed with LiCI.2Al (OH) 3, nH 2 O powder to obtain a paste which is then shaped by granulation followed by drying in air. The use of such a solid in a process for extracting lithium from salt lake brines makes it possible to obtain a low Mg / Li ratio and a lithium-rich mother liquor that complies with the standards for the production of carbonates or chlorides. lithium.

An object of the present invention is to provide a solid material for the selective extraction of lithium from brine, said solid material being of good quality, without apparent defects and having good cohesion and good mechanical strength when it is put in contact with a brine solution or in water.

An object of the present invention is to provide a new process for preparing such a solid material.

Another object of the present invention is to provide a method of extracting lithium from saline solutions using said solid material.

Another object of the present invention is to provide a solid material for carrying out a lithium extraction process of saline solutions, in which the solid material makes it possible to limit the generation of unwanted fine particles. In fact, the fine particles increase the pressure drop, favor the creation of preferential paths and increase the rate of renewal of the material during the passage of the brine through a bed of a material within a column.

Applicants have discovered a new process for preparing a crystallized solid material of formula LiXx.2AI (OH) 3, nH20 with n being between 0.01 and 10, x being 1 when X is an anion selected from chloride, hydroxide and nitrate anions, and x being equal to 0.5 when X is an anion chosen from sulphate and carbonate anions, comprising a specific step combination and in particular that carrying out both step a ) of precipitation of boehmite under specific temperature and pH conditions, a drying step in an oven followed by grinding or by atomization so as to obtain a powder and then a shaping step of the powder obtained by kneading extrusion in the presence of a base, then to carry out a final hydrothermal treatment step of the shaped materials makes it possible to obtain a crystallized solid material of formula LiXx.2AI (OH) 3, nH20 with no apparent defect having at the same time a good cohesion, good mechanical strength of the material when it is brought into contact with a brine solution or in water and having a lithium adsorption capacity and improved adsorption kinetics compared to the materials of the prior art when it is used in a lithium extraction process of saline solutions.

Without being bound to any theory, the applicants have demonstrated that the implementation of step a) of precipitation under the operating conditions of temperatures and pH as defined makes it possible to obtain a composite boehmite precipitate. crystallites of small size. In particular, the precipitate of boehmite obtained has a size, obtained by the Scherrer formula in X-ray diffraction along the crystallographic directions [020] and [120] is respectively between 0.5 and 10 nm and between 0.5 and 15 nm and preferably respectively between 0.5 to 2 nm and between 0.5 to 3 nm and very preferably respectively between 0.5 and 1.5 and between 0.5 and 2.5.

Scherrer's formula is a formula used in X-ray diffraction on powders or polycrystalline samples which connects the width at half height of the diffraction peaks to the size of the crystallites. It is described in detail in the reference: Appl. Cryst. (1978). 11, 102-113 Scherrer after sixty years: A survey and some new results in the determination of crystallite size, J. I. Langford and A. J. C. Wilson.

The method according to the invention thus makes it possible to obtain a crystallized solid final material of formula LiXx.2AI (OH) 3, nH20 with n being between 0.01 and 10, x having the above definition also poorly crystallized but having lithium adsorption capacity and adsorption kinetics improved over prior art materials when used in a lithium salt extraction process.

Moreover, the implementation of an extrusion shaping step in the presence of a base used in specific quantities makes it possible to obtain a final material having a good cohesion, as well as good mechanical strength when it is brought into contact with a brine solution or in water. Summary and interest of the invention

The term "material of formula LiXx.2Al (OH) 3, nH 2 O" is preferably understood to mean a material comprising essentially or consisting of a crystallized phase of formula LiXx.2AI (OH) 3, nH 2 O, n, x and X having the formula definition above.

The subject of the present invention is a process for the preparation of a crystallized solid material of formula LiXx.2AI (OH) 3, nH20 with n being between 0.01 and 10, where x is equal to 1 when X is an anion chosen from the anions chloride, hydroxide and nitrate, and x being equal to 0.5 when X is an anion chosen from sulfate and carbonate anions, said process comprising at least the following steps: a) a step of precipitation of boehmite, in the medium aqueous, at least one basic precursor selected from sodium aluminate, potassium aluminate, ammonia, sodium hydroxide and potassium hydroxide and at least one acid precursor selected from sulfate aluminum, aluminum chloride, aluminum nitrate, sulfuric acid, hydrochloric acid, and nitric acid, wherein at least one of the basic precursors or acid comprises aluminum, to obtain a suspension of boehmite, said step a) operating at a temperature ure between 5 and 35 ° C, and the quantië of the basic precursor being chosen so as to obtain a pH of end of precipitation in the reaction medium between 7.5 and 9.5, b) a step of washing and filtration of the boehmite precipitate obtained in step a), c) a step of contacting the precipitate obtained in step b) with at least one lithium source, d) a filtration step of the suspension obtained at step c) to obtain a paste, e) a step of drying the paste obtained at the end of step d), said drying step being carried out by atomization or in an oven or oven at a temperature between 20 and 80 ° C for a duration of preferably between 1h and 20h, said drying step being followed by a grinding step of the dried powder obtained in the case where the drying step is carried out in an oven or in a drying oven. oven, f) a step of forming said kneaded powder by kneading basic extrusion wherein said dried powder resulting from step e) is kneaded in the presence of a base amount of between 0.5 and 3% by weight relative to the dry matter, the dry matter being the mass of said powder of step e), dried in an oven at 200 ° C. for 6 h, said base being chosen from inorganic bases and organic bases in solution, and wherein said powder is then subjected to an extrusion step, g) a step hydrothermal treatment of the dried shaped material obtained at the end of step f), at a temperature between 50 and 200 ° C and for a period of preferably between 30 min and 12 hours.

An advantage of the preparation process according to the invention is that it makes it possible to obtain a crystallized solid material shaped, preferably in the form of extrudates, of the formula LiXx.2Al (OH) 3, nH20 with n, x and X having the above definition, of good quality, without apparent defects, and having a good cohesion and improved mechanical strength when it is brought into contact with a brine solution or a dilute solution and preferably in the 'water.

Another advantage of the present invention is to provide a process for preparing the reproducible material due to the passage through a powder. The method according to the invention is thus more easily transferable to different mixing tools and more easily extrapolated to the industrial level.

Another advantage of the present invention is to provide a process for preparing a crystallized solid material shaped, preferably in extruded form, of the formula LiXx.2AI (OH) 3, nH20 with n, x and X having the above definition, having a lithium adsorption capacity and adsorption kinetics improved over the materials of the prior art when it is used in a lithium extraction process of saline solutions.

The adsorption capacity of the aforementioned material is defined by the amount of lithium adsorbed for a given solution. It is calculated by those skilled in the art by integrating the amount of lithium fixed from a drilling curve also called leakage curve or saturation curve. The integration is carried out on the volume by the difference in lithium concentration between a solution after its loading on the aforementioned material and the theoretical concentration without loading. This amount of material can be related to the amount of material used to obtain a capacity in milligrams of lithium per gram of solid.

The kinetics of adsorption of the aforementioned material is measured by those skilled in the art by studying the shape of a drilling curve also called leakage curve or saturation curve. This curve is obtained by means of a column filled with the adsorbent material to form a homogeneous bed, percolating a saline solution containing lithium and by measuring the lithium concentration at the outlet of the adsorbent bed as a function of the volume of the solution used for a given flow.

By adsorption capacity improved over the materials of the prior art is meant an adsorption capacity greater than 4.5 mg Li / g dry solid material.

By dry solid material is meant a solid material dried at 200 ° C. for 6 hours.

By "shaping" is meant that the material is solid and has sufficient cohesion when the solid is brought into contact with a brine solution so that it substantially does not lose its physical integrity, that is, to say that it retains substantially its formatting. More specifically, a solid formed in the sense of the invention covers a solid maintaining its cohesion in the lithium extraction conditions defined in the examples.

The cohesion as well as the mechanical strength of the shaped material, preferably by extrusion, prepared according to the invention are tested during the production of drilling curves also called leakage curves or saturation curves. A solid exhibiting good mechanical strength does not produce fine particles and makes it possible to operate the column without observation of clogging. A solid having poor mechanical strength produces fine particles which induce clogging of the column.

The cohesion as well as the mechanical strength of the shaped material, preferably by extrusion, prepared according to the invention are also tested by means of an accelerated aging protocol on a stirring table, either in a brine or in the water.

The stirring table is animated by a horizontal unidirectional movement of amplitude 4 cm at a speed of 190 movements per minute. The shaped solids are stirred for a total of 330 hours. At the end of these 330 hours, the brine or water-shaped solid mixture is screened using a 315 μm mesh grid. Then the shaped solids remaining on the sieve are washed with the medium used during the stirring. The liquid fraction thus obtained, containing fine solid particles (diameter less than 315 pm) in suspension, is filtered using a Buchner equipped with a filter paper whose pores have a dimension of 0.45 pm. The cake formed by agglomeration of the fine particles is washed with deionized water. The solid residue thus obtained is dried in an oven at 200 ° C. until the mass stabilizes.

The ratio of the solid residue mass to the initial shaped solid mass is then calculated, giving access to a percent destruction of the shaped solids.

The percentage of destruction of the materials prepared according to the invention makes it possible to assess the cohesion of said materials.

Good cohesion is obtained in particular for materials whose percentage of destruction is less than 60%, and preferably less than 50%, when they are brought into contact with a solution of brine or other dilute solutions and particular of water.

The materials prepared according to the invention also have an improved mechanical strength compared to the materials of the prior art.

By "improved mechanical strength" is meant that the materials prepared according to the invention have a percentage of destruction, when they are brought into contact with a solution of brine or any other dilute solutions and in particular water, less than 30% and preferably less than 20%.

Another advantage of the preparation process according to the invention is that it makes it possible to obtain a crystallized solid material shaped, preferably in the form of extrudates, of the formula LiXx.2Al (OH) 3, nH20 with n, x and X having the above definition having no or few cracks which could cause detrimental swelling to the cohesion and mechanical strength of the material when it is brought into contact with a brine solution or a dilute solution and preferably in water.

The subject of the present invention is also a process for extracting lithium from saline solutions using said shaped crystallized solid material of formula ϋΧχ.2ΑΙ (OΗ) 3, ηΗ20 with n being between 0.01 and 10, where x is equal to at 1 when X is an anion chosen from chloride, hydroxide and nitrate anions, and x being equal to 0.5 when X is an anion chosen from sulfate and carbonate anions, prepared according to the new preparation method according to the invention.

An advantage of the extraction method according to the invention is to allow the selective extraction of lithium from a saline solution and thus obtain a high purification factor compared to the initial saline solution, calculated as the X / Li ratio which is equal to the molar ratio of X / Li concentrations in the initial saline solution divided by the molar ratio of X / Li concentrations in the final solution, X being selected from sodium (Na), potassium (K) , magnesium (Mg), calcium (Ca), boron (B), sulfur (S) and strontium (Sr).

The present invention also relates to a crystallized solid material of formula LiXx.2AI (OH) 3, nH20 with n being between 0.01 and 10, x being equal to 1 when X is an anion chosen from chloride anions, hydroxide and nitrate, and x being equal to 0.5 when X is an anion chosen from sulphate and carbonate anions, preferably in the form of extrudates, obtainable by a method of the invention.

The present invention also relates to a lithium extraction device of saline solution (s). The device according to the invention thus implements the extraction method according to the invention.

Description of the invention

According to the invention, the process comprises a step a) of precipitation of boehmite, in an aqueous reaction medium, of at least one basic precursor chosen from sodium aluminate, potassium aluminate, ammonia, sodium hydroxide and potassium hydroxide and at least one acidic precursor selected from aluminum sulphate, aluminum trichloride, aluminum nitrate, sulfuric acid, hydrochloric acid, and nitric acid, wherein at least one of the basic or acidic precursors comprises aluminum, to obtain a suspension of boehmite, said step a) operating at a temperature between 5 and 35 ° C, and the amount of the precursor basic being chosen so as to obtain a pH of end of precipitation in the reaction medium of between 7.5 and 9.5.

The mixture in the aqueous reaction medium of at least one basic precursor and at least one acidic precursor requires either that at least the basic precursor or the acidic precursor comprises aluminum, or that the two precursors basic and acidic include aluminum.

Preferably, the basic precursor is sodium hydroxide (NaOH).

Preferably, the acidic precursor is aluminum trichloride (AlCl 3).

Preferably, the basic precursor (s) and acid (s) are added in said first precipitation step a) in aqueous solutions.

Preferably, the aqueous reaction medium is water.

Preferably, said step a) operates with stirring.

Preferably, said boehmite precipitation step a) is carried out at a temperature between 5 and 30 ° C, and preferably between 10 and 30 ° C and very preferably between 10 and 25 ° C, and the quantity of the basic precursor being chosen so as to obtain a pH of the end of precipitation in the reaction medium of between 7.5 and 9 and preferably between 7.7 and 8.8.

Preferably, the precipitation step a) is carried out for a period of between 10 minutes and 5 hours, preferably between 15 minutes and 2 hours.

Said step a) of precipitation makes it possible to obtain a suspension of precipitated boehmite or aluminum oxyhydroxide (AIOOH).

The implementation of step a) of precipitation under the operating conditions of temperatures and pH as defined makes it possible to obtain a boehmite precipitate having small crystallites. By small crystallites is meant a precipitate of boehmite composed of crystallites whose size, obtained by the Scherrer formula in X-ray diffraction according to the crystallographic directions [020] and [120] is respectively between 0.5 and 10. nm and between 0.5 and 15 nm and preferably respectively between 0.5 to 2 nm and between 0.5 to 3 nm and very preferably respectively between 0.5 and 1.5 nm and between 0.5 and 2.5 nm.

According to the invention, the process comprises a step b) of filtration and washing of the boehmite precipitate obtained at the end of step a).

Preferably said washing step is a washing step with water.

According to the invention, the process comprises a step c) of contacting the boehmite precipitate obtained in step b) with at least one lithium source.

The lithium source (s) may be any compound comprising the lithium element and capable of releasing this element in aqueous solution in reactive form. Preferably, the source (s) of lithium is (are) chosen from among the lithium salts and preferably from lithium chloride (LiCl), lithium hydroxide (LiOH), nitrate of lithium lithium (LiNO 3), lithium sulphate (Li 2 SO 4) and lithium carbonate (Li 2 CO 3), alone or as a mixture.

Very preferably, the lithium source is lithium chloride (LiCl). In this case, X is the chloride anion and x = 1.

Preferably, the boehmite precipitate obtained in step b) and at least one lithium source are mixed in the presence of water to obtain a suspension in step c). Preferably, said mixing step c) is carried out with vigorous stirring.

Preferably, said contacting step c) is carried out at a temperature between 20 and 95 ° C and preferably between 50 and 95 ° C, and preferably between 70 and 95 ° C for a period of time between 15 minutes and 12 hours and preferably between 30 minutes and 5 hours.

According to the invention, the suspension obtained at the end of step c) undergoes a d) filtration step to obtain a paste.

According to the invention, the paste obtained at the end of step d) undergoes a drying step so as to obtain a powder, said drying step being carried out by atomization or in an oven or oven at a temperature between 20 and 120 ° C for a period preferably between 1h and 20h, said drying step being followed by a step of grinding the dried powder in the case where the drying step is carried out in an oven or in oven.

In the case where said drying step e) is carried out in an oven or in an oven, said step is carried out at a temperature of between 20 and 120 ° C., preferably between 30 and 100 ° C. for a period of time preferably between 1h and 20h, preferably between 1 and 12h and more preferably between 1 and 10h.

According to the invention, in the case where said drying step is carried out in an oven or in an oven, it is followed by a grinding step of the dried powder obtained. The grinding is advantageously carried out according to any method known to those skilled in the art, such as grinding with a knife mill, with a ball mill, hammer mill, air jet or gas mill, coffee grinder, mortar, or any other method making it possible to obtain a dry powder having a median diameter, determined by laser diffraction granulometry (Mastersizer 3000 - Malvern Instruments), between 1 and 200 μm, preferably between 2 and 180 μm, and preferably between 2 and 160 pm. The term "median diameter" refers to the D50, i.e., the diameter of the equivalent disk such that 50% by number of said particles has a size less than said diameter. Preferably the grinding is carried out cold, in this case cryo-grinding is preferably carried out in an ultracentrifugal mill cooled with liquid nitrogen.

Said grinding step may advantageously be carried out in step e) following drying in an oven or oven or in the shaping step f). In the case where it is carried out in the shaping step f), it is carried out in situ in the kneading step. The grinding step makes it possible to adjust the particle size of the dried powder obtained so as to facilitate its extrusion.

In the case where said drying step e) is carried out by atomization, the paste obtained at the end of step d) is resuspended in water. It is then sprayed into fine droplets in a vertical cylindrical chamber in contact with a stream of hot gas in order to evaporate the water according to the principle well known to those skilled in the art. The powder obtained is driven by the heat flow to a cyclone or a bag filter which will separate the gas from the powder.

Preferably, in the case where said drying step d) is carried out by atomization, the atomization is carried out according to the operating protocol described in the publication Asep Bayu Dani Nandiyanto, Kikuo Okuyama, Advanced Powder Technology, 22, 1-19 , 2011.

The operating conditions of said drying step (e) in an oven or in an oven or by atomization make it possible to obtain a dried powder with a loss on ignition (PAF) of between 20 and 50% and preferably between 20 and 40%. The loss on ignition obtained allows the shaping, preferably by extrusion, of the dried pulp powder under good conditions and obtaining shaped materials, preferably in the form of extruded, resistant and without apparent defects, c is without crack. In order to determine the PAF before the shaping step, part of the powder obtained is removed and placed in an oven for 6 hours at 200 ° C. The PAF is obtained by difference between the mass of the sample before and after passage in the oven. At the end of the drying step, whether it is carried out in an oven, in an oven or by atomization, the dried powder is advantageously in the form of a powder consisting of solid particles having a median diameter, determined by laser diffraction particle size distribution. (Mastersizer 3000 - Malvern Instruments), between 1 and 200 μm, preferably between 2 and 180 μm, and preferably between 2 and 160 μm. The term "median diameter" refers to the D50, i.e., the diameter of the equivalent disk such that 50% by number of said particles has a size less than said diameter.

According to the invention, said powder obtained at the end of the drying step e) undergoes a step f) of shaping by basic extrusion kneading in which said dried powder resulting from step e) is kneaded by presence of a basic amount of between 0.5 and 3% by weight relative to the dry matter, the dry matter being the mass of said paste resulting from stage e), dried in an oven at 200 ° C. for 6 hours base being selected from inorganic bases and organic bases in solution, and wherein said powder is then subjected to an extrusion step.

The term "kneading-extrusion step" is understood to mean a step in which the dried powder obtained at the end of the drying step e) undergoes in a first kneading step, according to the invention, in the presence of a base, and then the paste obtained after kneading is then subjected to an extrusion step, for example by passing through a die, using, for example, a piston or a continuous twin-screw or single-screw extruder. The diameter of the die of the extruder is advantageously variable and is between 0.5 and 5 mm, preferably between 0.5 and 3 mm and preferably between 0.5 and 2 mm. The shape of the die, and therefore the shape of the material obtained in extruded form, is advantageously cylindrical, trilobal, quadrilobed or multilobed.

Said f) kneading-extrusion shaping step is advantageously carried out in a manner known to those skilled in the art.

Said f) kneading-extrusion forming step and in particular said kneading step may optionally be carried out in the presence of a binder or in the absence of binder.

Preferably, said dried powder obtained at the end of the drying step e), and optionally at least one binder, as well as the base in the case where they are present, are mixed, preferably at one time , in a mixer. The kneader is advantageously chosen from batch kneaders, preferably with a cam or Z-arm, or with the aid of a twin-screw mixer-mixer. The mixing conditions are adjusted in a manner known to those skilled in the art and aim to obtain a homogeneous and extrudable paste.

In extrusion kneading processes known to those skilled in the art, the extrudability of the powder may optionally advantageously be adjusted with the addition of water in order to obtain a powder suitable for carrying out step f) extrusion shaping.

Preferably, said dried powder is kneaded in the presence of a base amount of between 0.5 and 2.5% by weight relative to the dry matter, the dry matter being the mass of said paste resulting from the step. e), dried in an oven at 200 ° C for 6h.

In the case where the amount of base added is greater than 3% by weight, the performance of the adsorption solids is strongly degraded.

Preferably, the inorganic bases are chosen from sodium hydroxide, potassium hydroxide and ammonia, and the organic bases in solution are chosen from amines and quaternary ammonium compounds. Preferably, the organic bases in solution are chosen from alkyl-ethanol amines and alkylamines ethoxylated. The organic bases are preferably used in solution in water.

Very preferably, said base is ammonia and preferably ammonia in aqueous solution (NH4OH).

Preferably, no acid is added in the extrusion kneading shaping step f).

In the case where said step f) of kneading-extrusion forming and in particular said kneading step is carried out in the presence of a binder, said binder is advantageously chosen from organic or inorganic binders.

The at least one organic binder (s) which may be used in said forming step (f) is advantageously chosen from paraffins and polymers, taken alone or as a mixture.

Preferably, said at least one organic binder (s) is chosen from polyvinylpyrrolidone (PVP), polyvinyl alcohol (PVA), an aqueous dispersion of a mixture of paraffin waxes and of polyethylene, for example Examples include Cerfobol R75, polysaccharides, methylcellulose, hydroxypropylmethylcellulose, hydroxyethylcellulose and carboxymethylcellulose and taken alone or as a mixture, preferably from polyvinylpyrrolidone (PVP), polyvinyl alcohol (PVA) and Cerfobol R75 and preferred manner among polyvinylpyrrolidone (PVP) and polyvinyl alcohol (PVA).

A very preferred organic binder is polyvinylpyrrolidone (PVP).

Cerfobol R75 comprises 28.4% dry paraffinic organic mass diluted in an aqueous phase.

The proportion of said one or more organic binder (s) added in said shaping step (f) is advantageously between 0.5 and 20% by weight, preferably between 0.5 and 15% by weight. preferably between 1 and 13% by weight, relative to the total mass of dry pulp to be shaped. The addition of at least one organic binder in said step facilitates the extrusion shaping of step f) of the process according to the invention. The addition of at least one organic binder in said step f) also makes it possible to obtain a crystallized solid material in the form of extrudates exhibiting improved stirring resistance in contact with the brine or water.

Preferably, said inorganic binder (s) used in said shaping step f) are advantageously chosen from silicic binders, clay-type binders and inorganic binders which can be generated in the conditions of said step f) by adding precursors of inorganic binders.

Preferably, said inorganic binder (s) used in said shaping step (f) are advantageously chosen from silicic binders.

Preferably, the silicic binders are advantageously chosen from precipitated silica and silica derived from by-products such as fly ash such as, for example, silico-aluminous or silico-calcic particles, silicic acid, sodium metasilicate and silica fumes. Colloidal silica, for example in the form of a stabilized suspension, such as for example commercial products such as Ludox® or Klebosol® may also be used.

Preferably, the silicic binder is in amorphous or crystalline form. Very preferably, the silica is used in powder form or in colloidal form.

The proportion of said one or more inorganic binder (s) added in said shaping step (f) is advantageously between 0.5 and 20 by weight, preferably between 0.5 and 15% by weight, preferably between 1 and 13% by weight, relative to the total mass of dry pulp to be shaped. The addition of at least one inorganic binder in said step f) facilitates its extrusion forming. The addition of at least one inorganic binder in said step f) also makes it possible to obtain a shaped crystallized solid material, preferably in the form of extrudates, exhibiting improved stirring resistance in contact with the brine.

Preferably, the extrusion-shaped material obtained at the end of step f) undergoes an optional drying step at a temperature of between 20 and 200 ° C. for a period of time preferably comprised of 1 hour. and 20 hours, to obtain the crystallized solid material of formula ίίΧχ.2ΑΙ (0Η) 3, ηΗ20 shaped, in the form of extrudates.

Preferably, said drying step is carried out at a temperature of between 20 and 100 ° C, preferably between 20 and 80 ° C and very preferably between 20 and 60 ° C, preferably for a duration of preferably between 1 and 18 hours, preferably between 5 and 14 hours and preferably between 8 and 14 hours.

The specific conditions of said drying step make it possible to obtain a crystallized solid material having the desired LiXx.2Al (OH) 3, nH 2 O phase.

Said drying step is advantageously carried out according to the techniques known to those skilled in the art and preferably in an oven.

According to the invention, the extruded and possibly dried shaped material obtained (s) at the end of step f) is (are) subjected to a hydrothermal treatment step g) at a temperature of between 50 and 50.degree. 200 ° C and for a period of preferably between 30 min and 12 hours.

Preferably, said step g) is carried out at a temperature between 70 and 200 ° C, preferably between 70 and 180 ° C, and very preferably between 80 and 150 ° C, for example for a time between 30 minutes and 120 hours.

Said step g) of hydrothermal treatment is advantageously carried out according to a technique known to those skilled in the art.

According to a preferred embodiment, said step g) is carried out in an autoclave, under autogenous pressure and under a saturated water atmosphere. Preferably, said step h) is carried out by introducing a liquid at the bottom of the autoclave, said liquid being chosen from water, alone or as a mixture with at least one acid, a base or a lithium salt. Preferably, the shaped and dried material, and preferably the extrudates obtained at the end of step f) are not in contact with the liquid at the bottom of the autoclave.

In the case where water is introduced into the autoclave in admixture with an acid, the acid is advantageously chosen from nitric acid, hydrochloric acid, sulfuric acid and carboxylic acid.

In the case where water is introduced into the autoclave in admixture with a base, the base is preferably selected from lithium hydroxide, sodium hydroxide, potassium hydroxide and ammonia.

In the case where water is introduced into the autoclave mixed with a lithium salt, the lithium salt is advantageously chosen from lithium chloride and lithium carbonate.

Preferably, said step g) is carried out in the presence of a humid atmosphere comprising a water content of between 5 and 50% by weight, and preferably between 5 and 45% by weight, and preferably between 5 and 40% by weight. mass.

According to one embodiment, said step g) can be carried out in a climate drying oven, in the presence of a humid air stream containing between 5 and 50% by weight of water, preferably between 5 and 45% by weight, and preferably between 4 and 40% by weight of water, or in an oven operating under a moist air stream containing between 5 and 50% by weight of water, preferably between 5 and 45% by weight and preferably between 5 and 40% by weight. according to the methods known to those skilled in the art. Stage g) of hydrothermal treatment in a controlled atmosphere makes it possible to obtain a crystallized solid material of formula LiXx.2AI (OH) 3, nH20 with n being between 0.01 and 10, x being equal to 1 when X is an anion chosen from chloride, hydroxide and nitrate anions, and x being equal to 0.5 when X is an anion chosen from sulphate and carbonate anions, preferably shaped in the form of extrudates, having good behavior and good mechanical strength when it is placed in contact with a brine or a dilute solution and preferably water. At the end of said step g), the shaped material preferably in the form of extrudates obtained is then advantageously recovered and may optionally be washed.

Said shaped material and preferably the extrudates obtained at the end of step g) can then optionally be subjected to a drying step h), said drying step preferably operating at a temperature of a temperature of between 15 and 50 ° C. for a duration of preferably between 1 hour and 12 hours to obtain the crystallized solid material of formula LiXx.2AI (OH) 3, nH20 with n being between 0.01 and 10, x being equal to 1 when X is an anion selected from chloride, hydroxide and nitrate anions, and x is 0.5 when X is an anion selected from sulfate and carbonate anions shaped.

Said drying step h) is advantageously carried out according to the techniques known to those skilled in the art, and preferably in an oven.

The process according to the present invention thus makes it possible to obtain a crystallized solid material of formula LiXx.2AI (OH) 3, nH20 with n being between 0.01 and 10, preferably between 0.1 and 5, and preferred between 0.1 and 1, where x is 1 when X is an anion selected from chloride, hydroxide and nitrate anions, and x is 0.5 when X is an anion selected from sulfate and carbonate anions, preferably in the form of extrusions with a cross section or diameter of between 0.2 and 5 mm, preferably between 0.3 and 4 mm, preferably between 0.3 and 3 mm, very preferably between 0.3 and 2 mm. mm and even more preferably between 0.3 and 1.8 mm.

The best results in terms of mechanical strength and cohesion of the crystallized solid material obtained according to the preparation method according to the invention are obtained in the case of extrusions of section or diameter between 0.2 and 5 mm and preferably between 0.3 and 1.8 mm, said extrudates having been obtained by the combination of a specific shaping step as described above and a final drying step carried out at a temperature between 20 and 200 ° C, preferably between 20 and 60 ° C, for a period of preferably between 1 and 20 hours, preferably between 5 and 14 hours, preferably between 8 and 14 hours and in particular for 8 hours.

The crystalline solid material of formula LiXx.2AI (OH) 3, nH20 shaped, preferably in the form of extrudates, prepared according to the sequence of steps a) to g) of the preparation process according to the invention can be characterized according to the following techniques: nitrogen adsorption for the determination of the specific surface area according to the BET method; X-ray diffractometry, in the diffraction angle range 2Θ = 0.8 to 40 ° ± 0.02 ° in reflection geometry to ientify the structure of said material and the elemental analysis.

The crystalline solid material of formula LiXx.2AI (OH) 3, nH20 shaped, preferably in the form of extrudates, advantageously has a specific surface area measured according to the BET method of between 1 and 30 m 2 / g and preferably between 1 and 30 m 2 / g. and 20 m2 / g.

The X-ray diffraction pattern of the material in the form of extrudates corresponds to a crystallized solid of formula LiXx.2AI (OH) 3, nH20 according to JCPDS sheet No. 0031-07-00, with n being between 0.01 and 10, preferably between 0.1 and 0.5, preferably between 0.1 and 5 and very preferably between 0.1 and 1, obtained according to the invention, shaped, advantageously in the form of extrudates .

The preparation method according to the present invention thus makes it possible to obtain a crystallized solid material of formula LiXx.2AI (OH) 3, nH 2 O, n, x and X having the above definition shaped preferably in the form of extrudates. , having both a low BET surface area, a good cohesion, and having no apparent defect and having good strength and good mechanical resistance when it is placed in contact with a brine or a solution diluted and preferably in water.

The good properties of the obtained material result from the combined effect of shaping, preferably by extrusion of a paste, in the absence of a binder, directly, after a drying step operating under specific conditions, of the implementation a drying step according to the shaping, also operating under specific conditions and also the implementation of a final hydrothermal treatment step operating preferably in an autoclave.

Furthermore, the crystallized solid material formed, preferably in the form of extrudates, thus obtained of formula LiXx.2AI (OH) 3, nH 2 O with n, x and X having the above definition, has a capacity of adsorption of lithium and adsorption kinetics improved over prior art materials when it is used in a lithium extraction process of saline solutions.

The materials obtained according to the invention have an improved adsorption capacity compared to the materials of the prior art greater than 4.5 mg Li / g of dry solid material, that is to say of solid material dried to 200 ° C, preferably between 4.5 and 10 mg Li / g, preferably between 4.5 and 8 and very preferably between 4.5 and 7 mg Li / g dry solid material.

The subject of the present invention is also a process for extracting lithium from a saline solution using said crystalline solid material of formula LiXx.2AI (OH) 3, nH20 with n being between 0.01 and 10, where x is equal to 1 when X is an anion chosen from chloride, hydroxide and nitrate anions, and x being equal to 0.5 when X is an anion chosen from sulphate and carbonate anions, prepared according to the invention or as defined according to for the extraction of lithium from saline solutions.

Said saline solution used in the extraction process according to the invention advantageously comprises a lithium concentration of between 0.001 mol / L and 0.5 mol / L, preferably between 0.02 mol / L and 0.3 mol / L. .

Said saline solution also contains other species, such as for example the species chosen from the following list: Na, K, Rb, Cs, Mg, Ca, Sr, Ba, F, Cl, Br, I, SO4, CO3, N03, and HC03. Said saline solution may advantageously be saturated with salts or not.

Said saline solution may be any natural saline solution, concentrated or resulting from a lithium extraction or transformation process. For example, said saline solution used in the extraction process according to the invention may advantageously be chosen from brine from salt lakes or from geothermal sources, brines subjected to evaporation to obtain brines concentrated in lithium, water of sea, effluents from cathode production plants, or production of lithium chloride or hydroxide and the effluents of the lithium extraction process from minerals.

The lithium extraction process according to the invention is preferably a selective extraction process of lithium. Indeed, it allows the separation of lithium from alkali metals, preferably sodium (Na), and potassium (K) and alkaline earth metals, preferably magnesium (Mg), calcium (Ca) and strontium ( Sr), present in a massive amount in the saline solutions treated in said extraction process.

The lithium extraction process according to the invention also allows the selective separation of lithium from other compounds such as boron and sulphates.

The lithium extraction process according to the invention is advantageously carried out in a unit comprising at least one column, said column or columns comprising at least one bed of said crystallized solid material of formula

LiXx.2AI (OH) 3, nH20, with n, x and X having the above definition, shaped and prepared according to the preparation method according to the invention.

Preferably, said lithium extraction method according to the invention is implemented in a unit comprising at least two columns, and preferably between two and three columns, comprising at least one bed of crystallized solid material of formula LiXx. 2AI (OH) 3, nH 2 O, with n, x and X having the above definition.

Said lithium extraction method advantageously comprises at least the following steps: an activation step of said crystallized solid material of formula

LiXx.2AI (OH) 3, nH20, with n, x and X having the above definition, - a step of loading said adsorption-activated material produced by passing said saline solution on said activated material, - optionally at least one step of washing the saline solution impregnating said material by passing a washing solution on said material, - a lithium desorption step carried out by passing water or an aqueous solution of lithium salt on said material to obtain an eluate comprising at least lithium.

Preferably, the lithium extraction method according to the invention comprises a prior step of setting said material in a column.

Preferably, said extraction method comprises an optional step of washing the saline solution impregnating said material by passing a washing solution on said material, said washing step preferably being carried out between the charging step and the desorption stage.

Preferably, said step of activating the crystallized solid material of formula LiXx.2AI (OH) 3, nH20, with n, x and X having the above definition, preferably shaped, and preferably in the form of extrudates, is carried out only once during the columnization of the synthesized material and shaped according to the preparation method according to the invention.

Said activation step makes it possible to activate the sites intended to selectively adsorb lithium.

Preferably, said activation step is advantageously carried out by the passage of an activation solution chosen from water and a lithium salt solution having a concentration of between 0.001 mol / L and 0.1 mol / L, preferably between 0.001 mol / L and 0.05 mol / L and preferably between 0.01 and 0.04 mol / L.

Preferably, the lithium salt used in solution in said activation step is chosen from lithium chloride (LiCl), lithium nitrate and lithium bromide.

Very preferably, the lithium salt used in solution in said activation step is lithium chloride (LiCl).

Said activation step is advantageously carried out at a temperature between 0 ° C. and 90 ° C., and preferably between 10 ° C. and 60 ° C., and preferably between 10 ° C. and 30 ° C. with a residence time of the activation solution in the column preferably between 0.03 and 10 h, and preferably between 0.06 and 1 h.

The amount of solution required for activation is advantageously between 1 and 30 column volumes, preferably between 2 and 20 column volumes.

The column volume or "Bed Volume" according to the English terminology is also called the volume occupied by the bed of the solid in the column or BV according to the terminology specific to the technical field known to those skilled in the art.

Said crystallized solid material may optionally undergo the activation step before a washing step with a washing solution and preferably a solution of lithium chloride (LiCl) or a mixture of lithium chloride (LiCl) and sodium chloride (NaCl).

Said step of loading said adsorption-activated material is advantageously carried out by passing the treated saline solution in the extraction process according to the invention on said activated material.

Said loading step is advantageously carried out at a temperature of between 0 ° C. and 90 ° C., and preferably between 10 ° C. and 70 ° C., with a residence time of said solution, preferably of said treated salt solution, in the column preferably between 0.03 and 10 h, and preferably between 0.06 and 1 h.

The amount of solution necessary to saturate said material depends on the adsorption capacity of said material and the lithium concentration of the saline solution.

The adsorption capacity of the materials according to the invention is greater than 4.5 mg Li / g of dry solid material, preferably between 4.5 and 10 mg Li / g, preferably between 4.5 and And most preferably between 4.5 and 7 mg Li / g dry solid material.

In the case where said lithium extraction method according to the invention is implemented in a unit comprising two columns, the first column is advantageously saturated with lithium during said charging step. The second column, receiving the output stream of the first column, is advantageously charged until a lithium leak not exceeding 10% of the lithium concentration of the inlet stream is obtained, preferably 5%, thus making it possible to maximize the recovery yield of lithium.

In the case where said lithium extraction process according to the invention is carried out in a unit comprising three columns, the third column, already saturated with lithium, is devoted to the lithium washing and then desorbing steps described below. after, while loading the other two columns.

The first fraction of the output stream of said adsorption loading step, advantageously between 0 and 1 column volumes, corresponds to the elimination of the impregnant resulting from the activation step of the solid material. This fraction can be considered as an effluent or recycled, and preferably recycled as an input stream of the desorption step. In the case of the treatment of a natural brine or seawater, beyond 1 column volume, the entire output stream of said adsorption loading step, hereinafter referred to as raffinate, which does not No chemical treatment is desirably and preferably returned to the original salt solution deposit. At the end of the step of loading by passing the saline solution treated in the process according to the invention on the activated material, the saline solution impregnates said activated material.

The saline solution impregnating the activated material is optionally washed in at least one washing step by passing a washing solution on said material.

Said step (s) of washing the saline solution impregnating said material, is (are) advantageously carried out (s) by upward or downward passage of a washing solution on said material, and preferably downward.

Preferably, said washing solution is selected from water and an aqueous solution of sodium salt and preferably sodium chloride (NaCl), optionally comprising a lithium salt and preferably lithium chloride (LiCl), said solution advantageously having a concentration of sodium salt and preferably sodium chloride (NaCl), greater than 0.5 mol / l, preferably of between 1 mol / l and saturation and a concentration of lithium salt and preferably in lithium chloride (LiCl), between 0 mol / L and 2 mol / L.

According to a preferred embodiment, said saline solution impregnating the activated material undergoes a final washing step by passing an aqueous washing solution of sodium chloride (NaCl) optionally comprising lithium chloride (LiCl), on said material.

Said washing step is advantageously carried out at a temperature between 0 ° C. and 90 ° C., and preferably between 10 ° C. and 0 ° C., and with a residence time of said solution, preferably of said washing solution in the column is between 0.03 and 10 h, and preferably between 0.06 and 1 h. The amount of solution required for washing is between 0.1 and 10 column volumes, and preferably in the range 0.5 to 5 column volumes.

The outlet stream of said washing step is considered as an effluent or is advantageously recycled, and preferably recycled at the inlet of the loading stage or directly at the inlet of the second column in the case where said process of extraction of the lithium according to the invention is carried out in a unit comprising at least two columns.

Said washing step allows the washing of the saline solution impregnated in said material during the step of loading said material by adsorption, while limiting the desorption of lithium.

In the case where said washing solution is a concentrated aqueous solution of sodium chloride (NaCl), said washing step not only makes it possible to eliminate the saline solution impregnated in said material during the step of loading said material by adsorption but also desorb elements such as boron, sulphates, alkalis other than lithium and sodium and alkaline earths. The lithium desorption step is then carried out by passing water or an aqueous solution of lithium chloride (LiCl) on said material at the end of the washing step to obtain an eluate comprising at least lithium .

Preferably, said desorption step is carried out by ascending or descending, and preferably descending, passage of a desorption solution chosen from water and a solution of lithium chloride (LiCl) containing from 0.001 mol / l to 2 mol / L LiCl, and preferably from 0.01 mol / L to 1 mol / L.

Said desorption step is advantageously carried out at a temperature of between 0 ° C. and 90 ° C., and preferably between 10 ° C. and 70 ° C., with a residence time of said desorption solution in the column preferably between 0.degree. 03 and 10 h, and preferably between 0.06 and 1 h.

The amount of lithium chloride solution (LiCl) required for the desorption is advantageously between 0.01 and 10 column volumes, and preferably between 0.05 and 5 column volumes.

The output stream of said lithium desorption step generates the final product of the process, called the eluate. The eluate is advantageously recovered between 0 and 4 column volumes, and preferably between 0.2 and 3 column volumes. All the other fractions of the output stream of this stage not constituting the final product called the eluate, is considered as an effluent or is advantageously recycled, and preferably recycled at the inlet of the loading, washing or elution. The eluate obtained at the end of the extraction process according to the invention is a solution containing mainly Li, Na and Cl elements as well as impurities preferably chosen from K, Mg, Ca, Sr, B or SO4. The eluate is then advantageously concentrated and purified to obtain a high purity lithium salt.

Said lithium extraction method according to the invention allows the selective extraction of lithium from a saline solution and thus makes it possible to obtain a high purification factor with respect to the initial saline solution, calculated as being the ratio X / Li which is equal to the molar ratio of concentration X / Li in the initial saline solution divided by the molar ratio of concentration X / Li in the eluate, X being chosen from sodium (Na), potassium (K), magnesium (Mg), calcium (Ca), boron (B), sulfur (S) and strontium (Sr).

The present invention also covers a lithium extraction device characterized in that it comprises a unit comprising at least one column, said column comprising at least one lining comprising the crystallized solid material of formula LiXx.2AI (OH) 3, nH20 with n being between 0.01 and 10, x being 1 when X is an anion selected from chloride, hydroxide and nitrate anions, and x being 0.5 when X is an anion selected from sulfate anions and carbonate, as defined according to the present invention or as prepared according to a process according to the invention.

More particularly, the invention covers a device implementing the lithium extraction method according to the invention. Even more specifically, the device of the present invention comprises units or means implementing the various steps of the lithium extraction process according to the invention.

By "according to the invention" or equivalent terms, it is meant to cover any embodiment, variant, advantageous or preferred characteristic, taken alone or in any of their combinations, without any limitation.

Description of the figures:

FIG. 1 and FIG. 2 respectively represent the X-ray diffraction pattern of the solid material of formula UXx.2AI (OH) 3, nH20 with X = Cl, x = 1 and n being between 0.01 and 10 obtained under extruded form in Examples 2 and 3 according to the invention.

FIG. 3 represents the X-ray diffraction pattern of the solid material of formula LiXx.2AI (OH) 3, nH20 with X = Cl, x = 1 and n being between 0.01 and 10 obtained in the form of extrudates in examples 6 not in accordance with the invention.

Figure 4 illustrates the saturation curves obtained for extrusions (see Example 7). The invention is illustrated by the following examples, which in no way present a limiting character.

Examples:

Example 1: (non-compliant)

A solid material of formula LiCl 2 Al (OH) 3, nH 2 O is prepared with n being between 0.01 and 1, according to a synthesis method not in accordance with the invention, in that the synthesis step AI (OH ) 3 is carried out at pH = 10.5 1 / synthesis AI (OH) g

In a beaker cooled by an ice bath to ensure a temperature of 25 C, a solution containing 326 ml of deionized water and 135.6 g of aluminum chloride hexahydrate (AlCl 3) is prepared. Then with magnetic stirring, sodium hydroxide (NaOH) is added slowly until pH 10.5 is reached. This cake is suspended in a 3 L beaker with 320 mL of water. 2 / Addition of lithium chloride LiCl.

A solution containing 78.5 g of lithium chloride LiCl provided by Prolabo and 1326 ml of water which is added to the plumped cake is prepared. This reaction medium is stirred and heated at 80 ° C. for 2 hours.

Filtration and drying in an oven at 80 ° C for 8 hours follow the first 2 steps. 3 / Spray drying

400 g of cake resulting from the filtration step are plumped into 1000 ml of water with magnetic stirring. Atomization is carried out on a Buchi B-290 laboratory tool, with a 2 mm nozzle and a 2.8 mm cap. The inlet temperature is 120 ° C and the outlet temperature is 51 ° C

The median diameter, that is to say the D50 of the particles of said powder is about 28 pm. The loss on ignition of the powder measured after drying at 200 ° C. for 6 hours is 24%. 4 / Malaxaae extrusion The shaping step is performed by mixing and extrusion. For the kneading step, 35.5 g of powder obtained above is introduced into a Brabender-type mixer (80ml volume of the tank) with 1.39 g of ammonia solution at 20.18% by weight, which corresponds to 1% by weight. base (NH4OH) relative to the dry matter, the dry material being the mass of said powder from the previous drying, dried in an oven at 200 ° C for 6h. The ammoniacal solution is mixed with 16 g of demineralized water and is added in 2 minutes under a kneading at 50 rpm. A supplement of water of about 2.7 g is added in order to obtain a cohesive, homogeneous and extrudable paste. The mixing is continued at the same speed for 30 minutes after the end of the addition of ammonia and water.

The paste obtained is shaped using a piston extruder (MTS) equipped with a cylindrical die 1 mm in diameter.

The extrudates obtained are then subjected to a hydrothermal treatment step in an autoclave comprising water. 10 g of extrudates are placed in a basket placed in a 500 ml autoclave. In the bottom of the autoclave are put 20 g of distilled water. The extrudates are not in contact with the liquid at the bottom of the autoclave.

The hydrothermal treatment is carried out at a temperature of 100 ° C. for 6 h under a saturated water atmosphere.

Extrusions of the solid material of formula LiCl 2 Al (OH) 3, nH 2 O with n = 0.25 having a good cohesion and a good appearance are obtained. A LiCI.2AI (OH) 3, nH 2 O phase is detected on the X-ray diffraction pattern of the extrudates of the solid material of formula LiCl 2 Al (OH) 3, nH 2 O with n = 0.25 obtained in Example 1.

The extrudates obtained are also characterized by the following measurements: Elemental analysis shows a good Li / Al / Cl stoichiometry corresponding to the composition of a LiCI.2Al (OH) 3, nH 2 O structure

Al = 21.2% mass; Li = 4.2% mass; Cl, = 19% mass.

The extrudates obtained have a specific surface area: SBet = 4 m 2 / g.

The extrudates obtained according to Example 1 have a good visual cohesion, have no or few cracks and have both a very good cohesion and a very good mechanical strength when they are in contact with a brine (percentage destruction rate of less than 8% in the cohesion test) or water (percentage of destruction less than 14% in the cohesion test).

EXAMPLE 2 (according to the invention, spray drying then basic extrusion mixing):

A solid material of formula LiCl 2 Al (OH) 3, nH 2 O, with n being between 0.01 and 1, is prepared according to a synthesis method according to the invention, in which the forming step is carried out. work by direct extrusion, without binder.

1 / boehmite precipitation AIOOH

In a beaker cooled by an ice bath, a solution containing 326 ml of deionized water and 135.6 g of aluminum chloride hexahydrate (AlCl 3) is prepared. Then, with magnetic stirring, 67.5 g of sodium hydroxide (NaOH) are added for 30 minutes to adjust the pH. The pH reached at the end of the synthesis is 8. The temperature is maintained at 20 ° C. throughout the course of the precipitation step. The suspension obtained is filtered and then washed with water. The cake is suspended in a 3 L beaker with 320 mL of water.

A sample of the precipitate obtained is taken from the reaction medium. The XRD of the precipitate shows that the precipitate obtained in Example 2 is indeed a boehmite precipitate. The boehmite precipitate obtained in Example 2 is poorly crystallized. 2 / Addition of lithium chloride LiCl.

A solution containing 78.5 g of lithium chloride LiCl provided by Prolabo and 1326 ml of water which is added to the plumped cake is prepared. This reaction medium is stirred and heated at 80 ° C for 2 h.

Filtration follows the first 2 steps. 3 / Spray drying

400 g of cake resulting from the filtration step are plumped into 1000 ml of water with magnetic stirring. Atomization is carried out on a Buchi B-290 laboratory tool, with a 2 mm nozzle and a 2.8 mm cap. The inlet temperature is 120 ° C and the outlet temperature is 51 ° C

The median diameter, that is to say the D50 of the particles of said powder is about 25 pm. The loss on ignition of the powder measured after drying at 200 ° C. for 6 hours is 25%. 4 / Extrusion mixing The shaping step is performed by kneading and extrusion. For the kneading step, 35.5 g of powder obtained above is introduced into a Brabender-type mixer (80ml volume of the tank) with 1.39 g of ammonia solution at 20.18% by weight, which corresponds to 1% by weight. base (NH4OH) relative to the dry matter, the dry material being the mass of said powder from the previous drying, dried in an oven at 200 ° C for 6h. The ammoniacal solution is mixed with 16 g of demineralized water and is added in 2 minutes under a kneading at 50 rpm. A supplement of water of about 2.7 g is added in order to obtain a cohesive, homogeneous and extrudable paste. The mixing is continued at the same speed for 30 minutes after the end of the addition of ammonia and water.

The paste obtained is shaped using a piston extruder (MTS) equipped with a cylindrical die 1 mm in diameter.

The extrudates obtained are then subjected to a hydrothermal treatment step in an autoclave comprising water. 10 g of extrudates are placed in a basket placed in a 500 ml autoclave. In the bottom of the autoclave are put 20 g of distilled water. The extrudates are not in contact with the liquid at the bottom of the autoclave.

The hydrothermal treatment is carried out at a temperature of 100 ° C. for 6 h under a saturated water atmosphere.

Extrusions of the solid material of formula LiCl 2 Al (OH) 3, nH 2 O with n = 0.25 having a good cohesion and a good appearance are obtained. A LiCI.2AI (OH) 3, nH 2 O phase is detected on the X-ray diffraction pattern of the extrusions of the solid material of formula LiCl 2 Al (OH) 3, nH 2 O with n = 0.25 obtained in Example 2 ( figure 1).

The extrudates obtained are also characterized by the following measurements: Elemental analysis shows a good Li / Al / Cl stoichiometry corresponding to the composition of a LiCI.2Al (OH) 3, nH 2 O structure

Al = 21.2% mass; Li = 4.2% mass; Cl, = 19% mass.

The extrudates obtained have a specific surface area: SBet = 3 m 2 / g.

The extrudates obtained according to Example 2 have a good visual cohesion, have no or only few cracks and have both a very good cohesion and a very good mechanical strength when they are in contact with a brine (percentage destruction of less than 4% in the cohesion test) or water (percentage of destruction less than 7% in the cohesion test).

EXAMPLE 3 (according to the invention, oven drying and then basic extrusion mixing)

A solid material of formula LiCl 2 Al (OH) 3, nH 2 O, with n being between 0.01 and 1, is prepared according to a synthesis method according to the invention, in which the forming step is carried out. work by direct extrusion, without binder.

1 / Boehmite Precipitation AIOOH

In a beaker cooled by an ice bath, a solution containing 326 ml of deionized water and 135.6 g of aluminum chloride hexahydrate (AlCl 3) is prepared. Then, with magnetic stirring, 67.5 g of sodium hydroxide (NaOH) are added for 30 minutes to adjust the pH. The pH reached at the end of the synthesis is 8. The temperature is maintained at 20 ° C. throughout the course of the precipitation step. This cake is suspended in a 3 L beaker with 320 mL of water.

A sample of the precipitate obtained is taken from the reaction medium. The XRD of the precipitate shows that the precipitate obtained in Example 2 is indeed a boehmite precipitate. The boehmite precipitate obtained in Example 2 is poorly crystallized. 2 / Addition of lithium chloride LiCl.

A solution containing 78.5 g of lithium chloride LiCl provided by Prolabo and 1326 ml of water which is added to the plumped cake is prepared. This reaction medium is stirred and heated at 80 ° C for 2 h.

Filtration and then washings follow the first 2 steps. 3 / Drying in an oven and grinding

The cake resulting from the filtration / washing step is put in an oven at 80 ° C. for 10 hours. the solid obtained is then milled with an ultracentrifugal mill cooled with liquid nitrogen.

The solid material thus prepared is characterized by the formula LiCl 2 Al (OH) 3, nH 2 O with n = 0.25 according to a synthesis method according to the invention.

The median diameter, that is to say the D50 of the particles of said powder is about 40 pm. The loss on ignition of the powder measured after drying at 200 ° C. for 6 hours is 35%. 4 / Extrusion mixing The shaping step is performed by kneading and extrusion. For the kneading step, 35.5 g of powder obtained above is introduced into a Brabender-type kneader (bowl volume 80 ml). with 1.39 g of ammonia solution at 20.18% by weight, which corresponds to 1% by weight of base (NH 4 OH) relative to the dry matter, the dry matter being the mass of the said powder resulting from the preceding drying, dried in an oven at 200 ° C for 6h. The ammoniacal solution is mixed with 16 g of demineralized water and is added in 2 minutes under a kneading at 50 rpm. A supplement of water of about 2.7 g is added in order to obtain a cohesive, homogeneous and extrudable paste. The mixing is continued at the same speed for 30 minutes after the end of the addition of ammonia and water.

The paste obtained is shaped using a piston extruder (MTS) equipped with a cylindrical die 1 mm in diameter.

The extrudates obtained are then subjected to a hydrothermal treatment step in an autoclave comprising water. 10 g of extrudates are placed in a basket placed in a 500 ml autoclave. In the bottom of the autoclave are put 20 g of distilled water. The extrudates are not in contact with the liquid at the bottom of the autoclave.

The hydrothermal treatment is carried out at a temperature of 100 ° C. for 6 h under a saturated water atmosphere.

Extrusions of the solid material of formula UCI.2AI (OH) 3, nH20 with n = 0.25 having good cohesion and a good appearance are obtained. A LiCI.2AI (OH) 3, nH 2 O phase is detected on the X-ray diffraction pattern of the extrudates of the solid material of formula LiCl 2 Al (OH) 3, nH 2 O with n = 0.25 obtained in Example 3 ( Figure 2).

The extrudates obtained are also characterized by the following measurements: Elemental analysis shows a good Li / Al / Cl stoichiometry corresponding to the composition of a LiCI.2Al (OH) 3, nH 2 O structure

Al = 21.2% mass; Li = 4.2% mass; Cl, = 19% mass.

The extrudates obtained have a specific surface area: SBet = 3 m 2 / g.

The extrudates obtained according to Example 2 have a good visual cohesion, have no or only few cracks and have both a very good cohesion and a very good mechanical strength when they are in contact with a brine (percentage destruction rate of less than 5% in the cohesion test) or water (percentage of destruction less than 10% in the cohesion test).

EXAMPLE 4 Comparative drying in an oven without grinding

A solid material of formula LiCl 2 Al (OH) 3, nH 2 O, with n being between 0.01 and 1, is prepared according to a synthesis method according to the invention, in which the forming step is carried out. work by direct extrusion, without binder.

1 / Boehmite Precipitation AIOOH

In a beaker cooled by an ice bath, a solution containing 326 ml of deionized water and 135.6 g of aluminum chloride hexahydrate (AlCl 3) is prepared. Then, with magnetic stirring, 67.5 g of sodium hydroxide (NaOH) are added for 30 minutes to adjust the pH. The pH reached at the end of the synthesis is 8. The temperature is maintained at 20 ° C. throughout the course of the precipitation step. The suspension obtained is filtered and then washed with water. The cake is suspended in a 3 L beaker with 320 mL of water.

A sample of the precipitate obtained is taken from the reaction medium. The XRD of the precipitate shows that the precipitate obtained is indeed a precipitate of boehmite. The boehmite precipitate obtained in Example 4 is poorly crystalline. 2 / Addition of lithium chloride LiCl.

A solution containing 78.5 g of lithium chloride LiCl provided by Prolabo and 1326 ml of water which is added to the plumped cake is prepared. This reaction medium is stirred and heated at 80 ° C for 2 h.

Filtration follows the first 2 steps. 3 / Drying in an oven

The cake resulting from the filtration / washing step is put in an oven at 80 ° C. for 10 hours. the solid obtained is not ground.

A solid in the form of large pebbles is obtained. These are impossible to mix with a Brabender type laboratory tool. No powder could be obtained and therefore no extrudates were obtained.

EXAMPLE 5 (Comparative oven drying at T = 200 ° C. with grinding then basic extrusion mixing):

A solid material of formula LiCl 2 Al (OH) 3, nH 2 O, with n being between 0.01 and 1, is prepared according to a synthesis method according to the invention, in which the forming step is carried out. work by direct extrusion, without binder.

1 / boehmite precipitation AIOOH

In a beaker cooled by an ice bath, a solution containing 326 ml of deionized water and 135.6 g of aluminum chloride hexahydrate (AlCl 3) is prepared. Then, with magnetic stirring, 67.5 g of sodium hydroxide (NaOH) are added for 30 minutes to adjust the pH. The pH reached at the end of the synthesis is 8. The temperature is maintained at 20 ° C. throughout the course of the precipitation step. The suspension obtained is filtered and then washed with water. The cake is suspended in a 3 L beaker with 320 mL of water.

A sample of the precipitate obtained is taken from the reaction medium. The XRD of the precipitate shows that the precipitate obtained in Example 5 is indeed a boehmite precipitate. The boehmite precipitate obtained in Example 5 is poorly crystallized. 2 / Addition of lithium chloride LiCl.

A solution containing 78.5 g of lithium chloride LiCl provided by Prolabo and 1326 ml of water which is added to the plumped cake is prepared. This reaction medium is stirred and heated at 80 ° C for 2 h.

Filtration follows the first 2 steps. 3 / Drying in an oven and grinding

The cake resulting from the filtration / washing step is put in an oven at 200 ° C. for 10 hours. the solid obtained is then milled with the ultracentrifugal mill (Retsch ZM1) cooled with liquid nitrogen.

The median diameter, that is to say the D50 of the particles of said powder is about 40 pm. The loss on ignition of the powder measured after drying at 200 ° C. for 6 hours is 15%. The basic extrusion kneading step is then carried out on the powder obtained as indicated in Example 2.

The desired material is not obtained. Indeed, the solid material thus prepared is not characterized by the formula LiCl 2 Al (OH) 3, nH 2 O according to a synthesis method according to the invention. In X-ray diffraction, a mixture of LiCl phase and Al (OH) 3 is obtained.

Example 6: (Comparative kneading basic extrusion in the presence of 4% by weight of NHa):

A solid material of formula LiCl 2 Al (OH) 3, nH 2 O, with n being between 0.01 and 1, is prepared according to a synthesis method according to the invention, in which the forming step is carried out. work by direct extrusion, without binder.

1 / Boehmite Precipitation AIOOH

In a beaker cooled by an ice bath, a solution containing 326 ml of deionized water and 135.6 g of aluminum chloride hexahydrate (AlCl 3) is prepared. Then, with magnetic stirring, 67.5 g of sodium hydroxide (NaOH) are added for 30 minutes to adjust the pH. The pH reached at the end of the synthesis is 8. The temperature is maintained at 20 ° C. throughout the course of the precipitation step. The suspension obtained is filtered and then washed with water. The cake is suspended in a 3 L beaker with 320 mL of water.

A sample of the precipitate obtained is taken from the reaction medium. The XRD of the precipitate shows that the precipitate obtained is indeed a precipitate of boehmite. The boehmite precipitate obtained in Example 6 is poorly crystalline. 2 / Addition of lithium chloride LiCl.

A solution containing 78.5 g of lithium chloride LiCl provided by Prolabo and 1326 ml of water which is added to the plumped cake is prepared. This reaction medium is stirred and heated at 80 ° C for 2 h.

Filtration and drying in an oven at 80 ° C for 10 hours follow the first 2 steps. 3 / Mixing Extrusion The shaping step is performed by mixing and extrusion. For the kneading step, 35.5 g of powder obtained above, is introduced into a Brabender type mixer (80ml volume tank) with 5.56 g of ammonia solution at 20.18% by weight, which corresponds to 4% base weight (NH4OH) relative to the dry matter, the dry matter being the mass of said powder from the preceding drying, dried in an oven at 200 ° C for 6h. The ammonia solution is mixed with 12 g of demineralised water and is added in 2 minutes under a mixing at 50 rpm. A supplement of water of about 2.7 g is added in order to obtain a cohesive, homogeneous and extrudable paste. The mixing is continued at the same speed for 30 minutes after the end of the addition of ammonia and water.

The paste obtained is shaped using a piston extruder (MTS) equipped with a cylindrical die 1 mm in diameter.

The extrudates obtained are then subjected to a hydrothermal treatment step in an autoclave comprising water. 10 g of extrudates are placed in a basket placed in a 500 ml autoclave. In the bottom of the autoclave are put 20 g of distilled water. The extrudates are not in contact with the liquid at the bottom of the autoclave.

The hydrothermal treatment is carried out at a temperature of 100 ° C. for 6 h under a saturated water atmosphere.

Extrusions of the solid material of formula UCI.2AI (OH) 3, nH20 with n = 0.25 having good cohesion and a good appearance are obtained. A LiCI.2AI (OH) 3, nH 2 O phase is detected on the X-ray diffraction pattern of the extrudates of the solid material of formula LiCl 2 Al (OH) 3, nH 2 O with n = 0.25 obtained in Example 4 ( Figure 3). An additional line that probably corresponds to salammoniac phase (NH4) CI is also detected.

The extrudates obtained are also characterized by the following measurements: Elemental analysis shows a good Li / Al / Cl stoichiometry corresponding to the composition of a LiCI.2Al (OH) 3, nH 2 O structure

Al = 21.2% mass; Li = 4.2% mass; Cl, = 19% mass.

The extrudates obtained have a specific surface area: SBet = 3 m 2 / g.

The extrudates obtained according to Example 6 visually exhibit good cohesion, have no or only few cracks and exhibit both very good cohesion and very good mechanical strength when they are brought into contact with a brine (percentage destruction less than 15% in the cohesion test) or water (percentage of destruction less than 20% in the cohesion test). The addition of 4% basis weight leads to a solid whose DRX spectrum is different from that obtained for the example according to the invention. Furthermore, the solid when it is introduced into the process described below has adsorption performance lower than those obtained for the example according to the invention.

Example 7: adsorption capacity and adsorption kinetics test.

The kinetics of lithium adsorption by the extrudates and their adsorption capacity is tested by the production of a drilling curve also known as a leakage curve or column saturation curve. A saturation curve is carried out for each of the extrudates obtained in Examples 1 to 6: 15 g of wet solid are placed in a column of 10 column volumes of a 0.02 mol / l lithium chloride (LiCl) saline solution. Crosses the column in closed circuit until reaching a stable concentration of lithium in solution

A natural solution containing about 0.06 mol / L of lithium crosses the column by upward passage, at a rate of 6 BV / h, that is to say six times the volume occupied by the extruded bed in one hour.

The lithium concentration is measured at the outlet of the column as a function of the volume of solution passed. The quantity of lithium adsorbed is calculated by integration on the volume of the difference between the concentration of the feed solution and the concentration measured at the outlet of the column. The capacity is then calculated by dividing this amount of lithium adsorbed by the dry mass of solid introduced into the column.

FIG. 4 illustrates the saturation curves obtained for each of the extrudates obtained in the examples according to the invention 2 and 3 and not in accordance with the invention 1 and 6.

The extrudates obtained according to Example 2 and 3 in accordance with the invention are compared with those obtained in Example 1 and 6 obtained according to a preparation method not in accordance with the invention. No tests could be performed for Examples 4 and 5 in view of the solids obtained. The extrudates of Example 2 and 3 obtained according to the invention show, in addition to improved mechanical strength, a greater lithium adsorption capacity. Their lithium adsorption capacities are respectively 6.6 and 6.4 mg (Li) / g (dry solid), compared to 5.3 mg (Li) / g (dry solid) for the solids obtained according to US Pat. Example 1 and 4.8 mg (Li) / g (dry solid) for the solids obtained according to Example 6, according to preparation methods not in accordance with the invention.

Claims (20)

1. Process for the preparation of a crystallized solid material of formula LiXx.2AI (OH) 3, nH20 with n being between 0.01 and 10, x being equal to 1 when X is an anion chosen from chloride, hydroxide anions and nitrate, and x being equal to 0.5 when X is an anion selected from sulfate and carbonate anions, said process comprising at least the following steps: a) a step of precipitation of boehmite, in aqueous medium, from at least one basic precursor selected from sodium aluminate, potassium aluminate, ammonia, sodium hydroxide and potassium hydroxide and at least one acidic precursor selected from aluminum sulphate, aluminum chloride, aluminum nitrate, sulfuric acid, hydrochloric acid, and nitric acid, wherein at least one of the basic precursors or acid comprises aluminum, to obtain a suspension of boehmite, said step a) operating at a temperature between 5 and 35 ° C, and the quantifies basic precursor being chosen so as to obtain a pH of end of precipitation in the reaction medium of between 7.5 and 9.5, b) a step of filtration and washing of the boehmite precipitate obtained in step a) c) a step of contacting the precipitate obtained in step b) with at least one lithium source, d) a filtration step of the suspension obtained in step c) to obtain a paste, e) a step of drying the paste obtained at the end of step d), said drying step being carried out by atomization or in an oven or oven at a temperature of between 20 and 80 ° C. for a period of preferably between between 1h and 20h, said drying step being followed by a step of grinding the dried powder in the case where the drying step is carried out in an oven or oven, f) a step of setting a step of setting in the form of said basic extrusion kneaded powder in the form of said dried powder resulting from step e) is kneaded in the presence of a base amount of between 0.5 and 3% by weight relative to the dry matter, the dry matter being the mass of said powder obtained from step e), dried in an oven at 200 ° C for 6 hours, said base is selected from inorganic bases and organic bases in solution, and wherein said powder is then subjected to an extrusion step, g) a treatment step hydrothermal the dried shaped material obtained at the end of step g), at a temperature between 50 and 200 ° C and for a period of preferably between 30 min and 12 hours. The process of claim 1 wherein the basic precursor is sodium hydroxide (NaOH). 3. Method according to one of claims 1 or 2 wherein the acidic precursor is aluminum trichloride (AICI3). 4. Method according to one of claims 1 to 3 wherein said step a) of precipitation of boehmite is carried out at a temperature between 10 and 25 ° C. 5. Method according to one of claims 1 to 4 wherein the amount of the basic precursor is chosen so as to obtain a precipitation end pH of said step a) in the reaction medium of between 7.7 and 8.8. 6. Method according to one of claims 1 to 5 wherein the lithium source is lithium chloride (LiCl). 7. Method according to one of claims 1 to 6 wherein in the case where the drying step is carried out in an oven, said drying step is carried out at a temperature between 30 and 100 ° C for a duration of preferably between between 1am and 10am, 8. Method according to one of claims 1 to 7 wherein said f) shaping step is carried out in the presence of ammonia. 9. The method of claim 8 wherein said dried powder is kneaded in the presence of a base amount of between 0.5 and 2.5% by weight relative to the dry matter, the dry matter being the mass of said pulp resulting of step e), dried in an oven at 200 ° C for 6h in said f) shaping step. 10. Crystalline solid material of formula LiXx.2AI (OH) 3, nH20 with n being between 0.01 and 10, x being equal to 1 when X is an anion chosen from chloride, hydroxide and nitrate anions, and x being equal to 0.5 when X is an anion chosen from sulfate and carbonate anions, shaped, preferably in extruded form, obtainable by a process as defined in any one of claims 1 to 9. 11. A method for extracting lithium from saline solutions, said method implementing said solid material of formula LiXx.2AI (OH) 3, nH20 with n being between 0.01 and 10, x being equal to 1 when X is an anion chosen from chloride, hydroxide and nitrate anions, and x being equal to 0.5 when X is an anion chosen from sulphate and carbonate anions, prepared according to the process as defined according to one of claims 1 to 9, or as defined in claim 10 for the extraction of lithium from saline solutions. 12. Extraction process according to claim 11, wherein said lithium extraction process comprises at least the following steps: a step of activating said crystallized solid material of formula LiXx.2AI (OH) 3, nH20 with n, x and X having the above definition, - a step of loading said activated adsorption material made by passing said saline solution on said activated material, - optionally at least one step of washing the saline solution impregnating said material by passing a washing solution on said material; - a lithium desorption step carried out by passing water or an aqueous solution of lithium salt on said material to obtain an eluate comprising at least lithium. 13. Extraction process according to claim 12 wherein said activation step is carried out by the upward or downward passage of water or a solution of lithium chloride (LiCl) having a concentration of between 0.001 mol / L and 0.1 mol / L. 14. Extraction process according to claim 12 or 13 wherein said activation step is carried out at a temperature between 0 ° C and 90 ° C, and with a residence time of said solution of lithium chloride or of water in the column between 0.03 and 10 h. 15. Extraction method according to one of claims 12 to 14 wherein said loading step is carried out at a temperature between 0 ° C and 90 ° C, and with a residence time of said salt solution in the column included between 0.03 and 10 h. 16. Extraction method according to one of claims 12 to 15 wherein said washing solution used in the washing step is water or an aqueous solution of sodium chloride (NaCl), optionally comprising sodium chloride. lithium (LiCl). 17. Extraction process according to one of claims 12 to 16 wherein said washing step is carried out at a temperature between 0 ° C and 90 ° C, and with a residence time of said washing solution in the column between 0.03 and 10 h. 18. Extraction process according to one of claims 12 to 17 wherein said desorption step is carried out by upward or downward passage of a desorption solution selected from water and a solution of lithium chloride (LiCl). containing from 0.001 mol / L to 2 mol / L of LiCl. 19. Extraction process according to one of claims 12 to 18 wherein said desorption step is carried out at a temperature between 0 ° C and 90 ° C, and with a residence time of said desorption solution in the column between 0.03 and 10 h. 20. A lithium extraction device characterized in that it comprises a unit comprising at least one column, said column comprising at least one packing comprising the crystallized solid material prepared according to the process as defined in one of claims 1 to 9, or as defined in claim 10.