METHOD FOR PREPARING AN ADSORBENT MATERIAL COMPRISING A STEP OF BASIC MIXING, AND METHOD FOR EXTRACTING LITHIUM FROM SALINE SOLUTIONS USING SAID MATERIAL

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 method for the preparation of a crystallized and shaped solid material, preferably in extruded form, of formula LiX.sub.x.2Al(OH).sub.3,nH.sub.2O, wherein n is between 0.01 and 10, x is 1 when X is an anion selected from among chloride, hydroxide and nitrate anions, and x is 0.5 when X is an anion selected from among sulfate and carbonate anions, comprising a boehmite precipitation step a) under specific temperature and pH conditions, at least one basic mixing shaping step, wherein the method also comprises a final hydrothermal treatment step, all to increase the lithium adsorption capacity and the kinetics of adsorption of the materials obtained, compared with the materials of the prior art when it is used in a method for lithium extraction from saline solutions.

Claims

1. Method for preparing a crystallized solid material of formula LiX.sub.x.2Al(OH).sub.3, nH.sub.2O, wherein n is between 0.01 and 10, and x is equal to 1 when X is an anion selected from the group consisting of chloride, hydroxide and nitrate anions, and x is 0.5 when X is an anion selected from the group consisting of sulfate and carbonate anions, wherein the method comprises at least the following steps: a) precipitating boehmite, in an aqueous medium, of at least one basic precursor selected from the group consisting of among sodium aluminate, potassium aluminate, aqueous ammonia, sodium hydroxide and potassium hydroxide; and at least one acidic precursor selected selected from the group consisting of aluminum sulphate, aluminum chloride, aluminum nitrate, sulfuric acid, hydrochloric acid, and nitric acid, wherein at least one of one of the basic or acidic precursors comprises aluminum, to obtain a boehmite suspension, step a) operating at a temperature of between 5 and 35 C., and the amount of the basic precursor is chosen in order to obtain a pH of end of precipitation in the reaction medium of between 7.5 and 9.5, b) filtering and washing the boehmite precipitate obtained in step a), c) contacting the precipitate obtained in step b) with at least one lithium source, d) filtering the suspension obtained in step c) to obtain a paste, e) drying the paste obtained at the end of step d) at a temperature of between 20 and 80 C., f) shaping the basic extrusion-mixed dough in which the dried dough resulting from step e) is mixed in the presence of a basic amount of between 0.5 and 3% by weight relative to the dry matter, wherein the dry matter is the weight of the dough resulting from stage e), dried in an oven at 200 C. for 6 h, wherein the base is selected from the group consisting of inorganic bases and organic bases in solution, and in which the dough is then subjected to an extrusion step, g) hydrothermally treating the dried shaped material obtained at the end of step f), at a temperature of between 50 and 200.

2. Method according to claim 1, wherein the basic precursor is sodium hydroxide (NaOH).

3. Method according to claim 1, wherein the acidic precursor is aluminum trichloride (AlCl.sub.3).

4. Method according to claim 1, wherein step a) is carried out at a temperature between 10 and 25 C.

5. Method according to claim 1, wherein the amount of the basic precursor is selected in order to obtain a precipitation end pH of step a) in the reaction medium of between 7.7 and 8.8.

6. Method according to claim 1, wherein the source(s) of lithium is/are selected from the group consisting of lithium chloride (LiCl), lithium hydroxide (LiOH) nitrate Lithium (LiNO.sub.3), lithium sulphate (Li.sub.2SO.sub.4) and lithium carbonate (Li.sub.2CO.sub.3), alone or as a mixture.

7. Method according to claim 6, wherein the lithium source is lithium chloride (LiCl).

8. Method according to claim 1, wherein the f) shaping step is carried out in the presence of ammonia.

9. Method according to claim 8, wherein the dried paste is mixed in the presence of an amount of base of between 0.5 and 2.5% by weight relative to the dry matter, wherein the dry matter is the weight of the paste of step e), dried in an oven at 200 C. for 6 h in the shaping step f).

10. Crystalline solid material of formula LiX.sub.x.2Al(OH).sub.3, nH.sub.2O, wherein n is between 0.01 and 10, x is equal to 1 when X is an anion selected from the group consisting of chloride, hydroxide and nitrate anions, and x is equal to 0.5 when X is an anion selected from the group consisting of sulfate and carbonate anions, in extruded form obtainable by a method as defined in claim 1.

11. Method for extracting lithium from saline solutions, wherein the lithium is extracted from saline solutions by a solid material of formula LiX.sub.x.2Al(OH).sub.3, nH.sub.2O, wherein n is between 0.01 and 10, x is equal to 1 when X is an anion selected from the group consisting of chloride, hydroxide and nitrate anions, and x is equal to 0.5 when X is an anion selected from the group consisting of sulfate and carbonate anions, prepared according to the method as defined according to claim 1, or as defined in claim 10.

12. Extraction method according to claim 11, wherein the lithium extraction method comprises at least the following steps: activating the crystallized solid material of formula LiX.sub.x.2Al(OH).sub.3, nH.sub.2O, wherein n, x and X have the above definition, charging the adsorption-activated material carried out by passing the saline solution on the activated material, optionally washing the saline solution impregnating the material by passing a washing solution on the material, optionally repeated, desorbing lithium by passing water or an aqueous solution of lithium salt on the material to obtain an eluate comprising at least lithium.

13. Extraction method according to claim 12, wherein activating the crystallized solid material 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 method according to claim 11, wherein activating the crystallized solid material is carried out at a temperature between 0 C. and 90 C., and with a residence time of the solution of lithium chloride or water in the column between 0.03 and 10 h.

15. Extraction method according to claim 12, wherein charging the adsorption-activated material is carried out at a temperature between 0 C. and 90 C., and with a residence time of the salt solution in the column between 0.03 and 10 h.

16. Extraction method according to claim 12, wherein the washing solution for washing the saline solution impregnating the material is water or an aqueous solution of sodium chloride (NaCl), optionally comprising lithium chloride (LiCl).

17. Extraction method according to claim 12, wherein the washing the saline solution impregnating the material is carried out at a temperature between 0 C. and 90 C., and with a residence time of the washing solution in the column between 0.03 and 10 h.

18. Extraction method according to claim 12, wherein desorbing lithium 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 method according to claim 12, wherein desorbing lithium is carried out at a temperature between 0 C. and 90 C., and with a residence time of the desorption solution in the column between 0.03 and 10 h.

20. Lithium extraction device, wherein said device comprises a unit comprising at least one column, wherein the column comprises at least one lining comprising the crystallized solid material prepared by the method as defined according to claim 1.

Description

DESCRIPTION OF THE FIGURES

[0180] FIG. 1 shows the X-ray diffraction pattern of the solid material of formula LiX.sub.x.2Al(OH).sub.3,nH.sub.2O, wherein X=Cl, x=1 and n is between 0.01 and 10, and that is obtained in the form of extrudates in Example 2 according to the invention.

[0181] FIG. 2 shows the X-ray diffraction pattern of the solid material of formula LiX.sub.x.2Al(OH).sub.3,nH.sub.2O, wherein X=Cl, x=1 and n is between 0.01 and 10, and that is obtained in the form of extrudates in Example 6 and does not conform to the invention.

[0182] FIG. 3 shows the saturation curves obtained for each of the extrudates obtained in Examples 1, 2, 3, 5 and 6.

[0183] The invention is illustrated by the following examples which in no way present a limiting character.

EXAMPLES

Example 1: (Non-Compliant)

[0184] A solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O is prepared, wherein n is between 0.01 and 1, according to a synthesis method not in accordance with the invention, wherein the synthesis step Al(OH).sub.3 is carried out at pH=10.5

[0185] 1/Synthesis Al(OH).sub.3

[0186] 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.sub.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.

[0187] The XRD of the precipitate shows that the precipitate obtained in Example 1 is indeed a boehmite precipitate. The boehmite precipitate obtained in Example 1 is crystallized.

[0188] 2/Addition of Lithium Chloride LiCl

[0189] A solution containing 78.5 g of lithium chloride LiCl supplied by Prolabo and 1326 ml of water which is added to the cake is prepared. This reaction medium is stirred and heated to 80 C. for 2 h.

[0190] Filtration and drying in an oven at 80 C. for 8 h follow the first 2 steps.

[0191] 3/Mixing Extrusion

[0192] The shaping step is performed by mixing and extrusion. For the mixing step, 35.5 g of paste obtained above is introduced into a Brabender-type mixer (80 ml tank volume) with 1.39 g of ammonia solution at 20.18% by weight, which corresponds to 1% by weight of base (NH.sub.4OH) relative to the dry matter, wherein the dry matter is the weight of the paste resulting from the preceding drying step, dried in an oven at 200 C. for 6 hours. The ammoniacal solution is mixed with 16 g of demineralized water and is added in 2 minutes by 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.

[0193] The paste so obtained is shaped using a piston extruder (MTS) equipped with a cylindrical die 1 mm in diameter.

[0194] 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. 20 g of distilled water are put in the bottom of the autoclave. The extrudates are not in contact with the liquid at the bottom of the autoclave.

[0195] The hydrothermal treatment is carried out at a temperature of 100 C. for 6 h under an atmosphere saturated with water.

[0196] Extrudates of the solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O, wherein n=0.25, with good cohesion and good appearance are obtained. An LiCl.2Al(OH).sub.3,nH.sub.2O phase is detected on the X-ray diffraction pattern of the extrudates of the solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O, wherein n=0.25 as obtained in Example 1 (FIG. 1).

[0197] The extrudates obtained are also characterized by the following measurements:

[0198] Elemental analysis shows a good Li/Al/Cl stoichiometry corresponding to the composition of an LiCl.2Al(OH).sub.3,nH.sub.2O structure

[0199] Al=21.2% mass; Li=4.2% mass; Cl,=19% mass.

[0200] The extrudates obtained have a specific surface area: S.sub.BET=4 m.sup.2/g.

[0201] The extrudates obtained according to Example 1 have 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 of less than 17% in the cohesion test) or water (percentage of destruction less than 24% in the cohesion test).

Example 2 (According to the Invention)

[0202] A solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O is prepared, wherein n is between 0.01 and 1, according to a synthesis method according to the invention, in which the shaping step is implemented by direct extrusion, without a binder.

[0203] 1/Boehmite Precipitation AlOOH

[0204] 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.sub.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 duration 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.

[0205] 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.

[0206] 2/Addition of Lithium Chloride LiCl

[0207] A solution containing 78.5 g of lithium chloride LiCl supplied by Prolabo and 1326 ml of water which is added to the cake is prepared. This reaction medium is stirred and heated to 80 C. for 2 h.

[0208] Filtration and drying in an oven at 80 C. for 8 hours follow the first 2 steps.

[0209] 3/Mixing Extrusion

[0210] The shaping step is performed by mixing and extrusion. For the mixing step, 35.5 g of the paste obtained above is introduced into a Brabender-type mixer (80 ml tank volume) with 1.39 g of ammonia solution at 20.18% by weight, which corresponds to 1% by weight of base (NH.sub.4OH) relative to the dry matter, wherein the dry matter is the mass of the paste resulting from the preceding drying step, dried in an oven at 200 C. for 6 hours. The ammoniacal solution is mixed with 16 g of demineralized water and is added in 2 minutes by 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.

[0211] The paste so obtained is shaped using a piston extruder (MTS) equipped with a cylindrical die 1 mm in diameter.

[0212] 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. 20 g of distilled water are put in the bottom of the autoclave. The extrudates are not in contact with the liquid at the bottom of the autoclave.

[0213] The hydrothermal treatment is carried out at a temperature of 100 C. for 6 h under an atmosphere saturated with water.

[0214] Extrudates of the solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O, wherein n=0.25, with good cohesion and good appearance are obtained. An LiCl.2Al(OH).sub.3,nH.sub.2O phase is detected on the X-ray diffraction pattern of the extrudates of the solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O, wherein n=0.25 as obtained in Example 2 (FIG. 1).

[0215] The extrudates obtained are also characterized by the following measurements:

[0216] Elemental analysis shows a good Li/Al/Cl stoichiometry corresponding to the composition of an LiCl.2Al(OH).sub.3,nH.sub.2O structure

[0217] Al=21.2% mass; Li=4.2% mass; Cl,=19% mass.

[0218] The extrudates obtained have a specific surface area: S.sub.BET=3 m.sup.2/g.

[0219] The extrudates obtained according to Example 2 have good visual cohesion, have no, or only few, cracks and exhibit both very good cohesion and very good mechanical strength when they are in contact with a brine (percentage destruction of less than 15% in the cohesion test) or water (percentage of destruction less than 20% in the cohesion test).

Example 3 (Comparative: Direct Extrusion without Basic Mixing)

[0220] A solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O is prepared, wherein n is between 0.01 and 1, according to a synthesis method according to the invention, in which the shaping step is implemented by direct extrusion, without basic mixing.

[0221] 1/Boehmite Precipitation AlOOH

[0222] 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.sub.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 duration 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.

[0223] A sample of the precipitate obtained is taken from the reaction medium. The XRD of the precipitate shows that the precipitate obtained in Example 3 is indeed a boehmite precipitate. The boehmite precipitate obtained in Example 3 is not very crystalline.

[0224] 2/Addition of Lithium Chloride LiCl

[0225] A solution containing 78.5 g of lithium chloride LiCl supplied by Prolabo and 1326 ml of water which is added to the cake is prepared. This reaction medium is stirred and heated to 80 C. for 2 h.

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

[0226] The solid material thus prepared is characterized by the formula LiCl.2Al(OH).sub.3,nH.sub.2O, wherein n=0.25 according to a synthetic method according to the invention. The shaping step of the paste obtained is carried out directly after the drying step, without a prior mixing step and in the absence of a binder.

[0227] The paste obtained is shaped using a piston extruder (MTS) equipped with a cylindrical die 1 mm in diameter.

[0228] The extrudates obtained at the end of the shaping step are then dried in an oven at 40 C. for 12 hours.

[0229] The extrudates so 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. 20 g of distilled water are put in the bottom of the autoclave. The extrudates are not in contact with the liquid at the bottom of the autoclave.

[0230] The hydrothermal treatment is carried out at a temperature of 100 C. for 6 h under an atmosphere saturated with water.

[0231] Extrudates of the solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O, wherein n=0.25, with good cohesion and good appearance are obtained. An LiCl.2Al(OH).sub.3,nH.sub.2O phase is detected on the X-ray diffraction pattern of the extrudates of the solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O, wherein n=0.25 (not supplied).

[0232] The extrudates obtained are also characterized by the following measurements:

[0233] Elemental analysis shows a good Li/Al/Cl stoichiometry corresponding to the composition of an LiCl.2Al(OH).sub.3,nH.sub.2O structure.

[0234] Al=20.00% mass; Li=4.03% mass; Cl=20.5% mass, C=5.87% mass.

[0235] The extrudates obtained have a specific surface area: S.sub.BET=3 m.sup.2/g.

[0236] The extrudates obtained according to Example 3 visually exhibit good cohesion, and show no or few cracks. However, when they are subjected to the strength test described above, they have a cohesion and a mechanical strength that are worse than the material obtained in Example 2 according to the invention when they are brought into contact with brine (percentage of destruction of about 35% in the cohesion test) or water (percentage of destruction of about 45% in the cohesion test).

Example 4 (Comparative Acidic and then Basic Mixing)

[0237] A solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O is prepared, wherein n is between 0.01 and 1, according to a synthesis method according to the invention, in which the shaping step is implemented by direct extrusion, without a binder.

[0238] 1/Boehmite Precipitation AlOOH

[0239] 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.sub.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 duration 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.

[0240] 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 is not very crystalline.

[0241] 2/Addition of Lithium Chloride LiCl

[0242] A solution containing 78.5 g of lithium chloride LiCl supplied by Prolabo and 1326 ml of water which is added to the cake is prepared. This reaction medium is stirred and heated to 80 C. for 2 h.

[0243] Filtration and drying in an oven at 80 C. for 8 hours follow the first 2 steps.

[0244] The shaping of the dried paste obtained is carried out with a total acid content, expressed relative to the dried paste of 1% by weight, and a degree of neutralization of 20%. The mixing is carried out on a Brabender mixer. The dried paste is introduced into the mixer. The acidified water is added with nitric acid in 4 minutes, with mixing at 50 rpm. The acid mixing is continued for 10 minutes. A neutralization step is carried out by adding an ammoniacal solution and mixing for 3 minutes. The mixing is continued at the same speed for 30 minutes after the end of the addition of ammonia.

[0245] No cohesive paste could be obtained.

[0246] The wet solid obtained is shaped using a piston extruder (MTS) equipped with a cylindrical die 1 mm in diameter. No intact extrudates could be obtained.

[0247] The rushes obtained are very friable and have no hold in brine.

Example 5 (Comparative Mixing with Water then Extrusion)

[0248] A solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O is prepared, wherein n is between 0.01 and 1, according to a synthesis method according to the invention, in which the shaping step is implemented by direct extrusion, without a binder.

[0249] 1/Boehmite Precipitation AlOOH

[0250] 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.sub.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 duration 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.

[0251] A sample of the precipitate obtained is taken from the reaction medium. The XRD (FIG. 1) of the precipitate shows that the precipitate obtained in example 5 is indeed a boehmite precipitate. The boehmite precipitate obtained in Example 5 is not very crystallized.

[0252] 2/Addition of Lithium Chloride LiCl

[0253] A solution containing 78.5 g of lithium chloride LiCl supplied by Prolabo and 1326 ml of water which is added to the cake is prepared. This reaction medium is stirred and heated to 80 C. for 2 h.

[0254] Filtration and drying in an oven at 80 C. for 8 hours follow the first 2 steps.

[0255] 3/Mixing Extrusion

[0256] The shaping step is performed by mixing and extrusion. For the mixing step, 35.5 g of dough obtained above is introduced into a Brabender-type mixer (tank volume 80 ml). No basic additions are made. An addition of approximately 19 g of demineralized water is carried out in 2 minutes under mixing at 50 rpm. The mixing is continued at the same speed for 30 minutes after the end of the addition of water.

[0257] The paste obtained is shaped using a piston extruder (MTS) equipped with a cylindrical die 1 mm in diameter.

[0258] The extrudates obtained are also characterized by the following measurements:

[0259] Elemental analysis shows a good Li/Al/Cl stoichiometry corresponding to the composition of an LiCl.2Al(OH).sub.3,nH.sub.2O structure

[0260] Al=20.00% mass; Li=4.03% mass; Cl=20.5% mass, C=5.87% mass.

[0261] The extrudates obtained have a specific surface area: S.sub.BET=3 m.sup.2/g.

[0262] The extrudates obtained according to Example 5 visually exhibit good cohesion, have no, or only few, cracks but exhibit poorer cohesion and mechanical strength when they are brought into contact with a brine (percentage of destruction of about 35% in the cohesion test) or water (destruction percentage of about 45% in the cohesion test).

Example 6: (Comparative Mixing in the Presence of 4% Ammonia)

[0263] A solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O is prepared, wherein n is between 0.01 and 1, according to a synthesis method according to the invention, in which the shaping step is implemented by direct extrusion, without a binder.

[0264] 1/Boehmite Precipitation AlOOH

[0265] 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.sub.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 duration 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.

[0266] A sample of the precipitate obtained is taken from the reaction medium. The XRD of the precipitate shows that the precipitate obtained in Example 6 is indeed a boehmite precipitate. The boehmite precipitate obtained in Example 6 is not very crystalline.

[0267] 2/Addition of Lithium Chloride LiCl

[0268] A solution containing 78.5 g of lithium chloride LiCl supplied by Prolabo and 1326 ml of water which is added to the cake is prepared. This reaction medium is stirred and heated to 80 C. for 2 h.

[0269] Filtration and drying in an oven at 80 C. for 8 hours follow the first 2 steps.

[0270] 3/Mixing Extrusion

[0271] The shaping step is performed by mixing and extrusion. For the mixing step, 35.5 g of dough obtained above is introduced into a Brabender-type mixer (tank volume 80 ml) with 5.56 g of ammonia solution at 20.18% by weight, which corresponds to 4% by weight of base (NH.sub.3) relative to the dry matter, wherein the dry matter is the weight of the dough resulting from the preceding drying, dried in an oven at 200 C. for 6 h. The ammoniacal solution is mixed with approximately 12 g of demineralised water and is added in 2 minutes under stirring 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.

[0272] The paste obtained is shaped using a piston extruder (MTS) equipped with a cylindrical die 1 mm in diameter.

[0273] 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. 20 g of distilled water are put in the bottom of the autoclave. The extrudates are not in contact with the liquid at the bottom of the autoclave.

[0274] The hydrothermal treatment is carried out at a temperature of 100 C. for 6 h under an atmosphere saturated with water.

[0275] Extrudates of the solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O, wherein n=0.25, with good cohesion and good appearance are obtained.

[0276] An LiCl.2Al(OH).sub.3,nH.sub.2O phase is detected on the X-ray diffraction pattern of the extruded solid material of formula LiCl.2Al(OH).sub.3,nH.sub.2O. An additional line that probably corresponds to the (NH.sub.4)CI phase is also detected.

[0277] The extrudates obtained are also characterized by the following measurements:

[0278] Elemental analysis shows a good Li/Al/Cl stoichiometry corresponding to the composition of an LiCl.2Al(OH).sub.3,nH.sub.2O structure

[0279] Al=21.2% mass; Li=4.2% mass; Cl,=19% mass.

[0280] The extrudates obtained have a specific surface area: S.sub.BET=3 m.sup.2/g.

[0281] 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 of less than 15% in the cohesion test) or water (percentage of destruction less than 20% in the cohesion test).

[0282] The addition of 4 wt % of base leads to a solid whose XRD spectrum (FIG. 2) is different from that obtained for the example according to the invention. Furthermore, the solid when it is introduced into the method described below has adsorption performance that is lower than that obtained for the example according to the invention.

Example 7 Adsorption Capacity and Adsorption Kinetics Test

[0283] The kinetics of lithium adsorption by the extrudates and their adsorption capacity is tested by performing a drilling curve also called leakage curve or column saturation curve. A saturation curve is produced for each of the extrudates obtained in Examples 1 to 6: [0284] 15 g of moist solid are placed in a column [0285] 10 column volumes of 0.02 mol/L lithium chloride (LiCl) saline solution crosses the closed circuit column until a stable lithium solution concentration is reached [0286] A natural solution containing approximately 0.06 mol/L of lithium crosses the column at a rate of 6 BV/h, i.e. six times the volume occupied by the bed of the extrudates in one hour. [0287] The lithium concentration is measured at the outlet of the column as a function of the volume of solution passed. [0288] The quantity of lithium adsorbed is calculated by integration on the volume of the difference between the concentration of the supply 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.

[0289] FIG. 3 illustrates the saturation curves obtained for each of the extrudates obtained in Examples 1, 2, 3, 5 and 6.

[0290] The extrudates obtained according to Example 2 according to the invention are compared with those obtained in Example 1, 3, 5 and 6 that are obtained according to preparation methods not in accordance with the invention. No test could be performed for Example 4 in view of the solids obtained. The extrudates of Example 2 obtained according to the invention show in addition to improved mechanical strength, a significant lithium adsorption capacity. Their lithium adsorption capacity is 6.4 mg (Li)/g (dry solid), is compared to 4.8 mg (Li)/g (dry solid) for the solids obtained according to Example 6, according to a method of preparation not in accordance with the invention. The extrudates obtained according to Examples 3 and 5, according to methods not in accordance with the invention, show a capacity equivalent to the extrudates obtained according to Example 2 according to the invention. The non-compliant extrudates obtained according to Example 1 show a degraded capacity of 5.3 mg (Li)/g (dry solid).