CA1170645A - Crystalline lithium aluminates - Google Patents

Abstract

ABSTRACT
Porous substrates containing seeds of hydrous crystalline alumina are contacted with an aqueous solu-tion of alkaline aluminate, thereby causing additional crystalline hydrous alumina to grow on the seeds within the pores of the substrate. Preferable substrates are macroporous ion-exchange resins.
29,261-F

Description

~ ~ 7 ~ 5 CRYSTALLINE LITHIUM ALUMINATES

It is known, e.g., from U.S. Patents 4,116,858 (Lee and Bauman, September 26, 1978) and 4,154,311 (Lee and Bauman, June 26, 1979) that an ion-exchange resin may be saturated with aqueous AlCl3 solution and that reaction with NH40H converts the AlCl3 in situ to Al(OH)3. This so-formed amorphous Al(OH)3 is then reacted with LiX, where X is halide, at elevated temperature to form crys-talline LiX-2Al(OH)3 which is useful in selectively recov-ering Li+ values from aqueous solutions, e.g., Li-contain-ing brines.

It is also known, e.g., from U.S. Patents 4,116,856 (Lee and Bauman, September 26, 1978) and 4,221,767 (Lee and Bauman, September 9, 1980) that improvments in the above discussed formation o crys-talline LiX-2Al(OH)3 are found by reacting amorphous Al(OH)3 or crystalline hydrous alumina (e.g., nordstran-dite, bayerite, gibbsite or mixtures of these) with LioH
; to form LiOH-2Al(OH)3 which is then reacted with LiX to form the crystalline LiX-2Al(OH)3, where X is halide.

L~J
29,261-F -1-.

I ~ 7~S4~

Various forms of alumina, Al2O3, are known, some of which occur as natural minerals, some of which are hydrated and some of which are crystalline. The Handbook of Chemistry shows the following:

Crystalline Name Form M.P.C
aluminum oxide, Al2O3 hex. col. 2050 ~~Al2O3, corundum trig;col.cr,n 2015 y-Al2O3, r-alumina wh.micro.cr.,n tr.to alpha Al2O3 3H2O, gibbsite, monocl.,wh.cr. tr.to (hydrargillite) A12O3 H20 (Boehmite) Al2O3 3H2O, bayerite wh.micro.cr. tr.to Al23 H20 (Boehmite) aluminum oxide, amor.wh.pwd. -xH2O,tr.to A123 XH2 y-Al2o3 Nordstrandite is a crystalline hydrous alumina, as are gibbsite and bayerite.

The present process differs from the above previous lithium aluminate preparations in that AlCl3 is used only once, to provide amorphous Al(OH)3 in a substrate such as a macroporous ion-exchange resin.
Further loading of ~l into the substrate pores is accom-plished by crystallizing the alumina in the pores and growing the crystals in an alkaline aluminate solution.

The present invention is a process for growing crystalline hydrous alumina within the pores of a porous ~:

29,261-F -2-, , ~ ~ 7 ~

substrate, characterized by providing a seed of crystal-line hydrous alumina in said pores by the ln situ precipi-tation of a water-soluble aluminum compound, thereby form-ing amorphous hydrous alumina; converting the so-formed amorphous hydrous alumina to crystalline hydrous alumina by heating; and adding to the seed-bearing substrate an aqueous solution of an alkaline aluminate, thereby providing alumi-num oxide values which grow additional quantities of crys-talline hydrous alumina on the crystalline hydrous alumina seeds.

The so-formed crystalline hydrous alumina may then be converted to LiX-2Al(OH)3 nH20 by reaction with a lithium salt, where X is an anion or negative valence salt radical. Depending on the type of crystalline hydrous alumina formed, the crystalline unit cells may be of the

2-layer or 3-layer variety.

A~ used herein, the expressions "2-layer" and "3-layer" refer to the number of layers bounded on both sides by the aluminate layers into which the subject Li compounds are intercalated. The following graphic illus-trations will aid in describing the 2-layer and 3-layer systems:

2-layer 3-layer _ Li salt ~ Li salt C
o nAl(OHj~ C nAl(OH~
Ll salt o Ll salt ~ , ~ i _ =~

29,261-F -3-~ ~7~5 It will be realized that the crystals of lithium aluminates are normally present as aggregates or stacks of a plurality of unit cells rather than each unit cell standing as a separate physical entity.

2-Layer LiX 2Al(OH)3 nH20 is formed from gibbsite and a lithium salt (LiX) other than LioH~ The lithium salt concentration must be high (at least about 12-15 percent of LiCl, for example) and the temperature must be high, preferably close to the boiling point of the LiX solution. LioH tends to solubiliz.e the gibbsite and when it reprecipitates it forms 3-layer unit cells.

3-Layer LiX-2Al(OH)3-nH2O is formed from hydrous alumina and LioH whi~h forms crystalline LiOH 2Al(OH)3 nH2O, which can then be neutralized with an acid to form crystal-line LiX 2Al(OH)3 nH2O, where X is the anion of the acidor of the lithium salt.

The porous substrate into which the crystal-line hydrous alumina is loaded may be an inert material, such as an inorganic or organic material. For certain uses and reasons, the substrate is preferably a macro-porous resin such as an ion-exchange resin as taught in U.S. Patents 4,116,858 and 4,116,856, both previously identified. Examples of the macroporous resins that can be employed are the strong acid and weak base types of macroporous resins.

once the substrate is loaded to satisfaction with the crystalline hydrous alumina, the composite is then ready for reaction with LiX, where X is a monova-lent anion, such as OH , Cl , Br , I , RCOO or OCl , or 29,261-F -4-i ~ 796~ ~

may be divalent or trivalent, such as SO4 , PO4 or R(C00)2 The alkaline aluminate solution, e.g., NaAlO2-xNaOH, may be prepared, e.g., by dissolving com-mercial grade sodium aluminate, NaAlO2, in water or maybe prepared, e.g., by reacting Al(OH)3 with concentrated NaOH. Commercially available solutions of sodium alumi-nate can be used. When reacting crystalline Al(OH)3 with concentrated NaOH it is preferred that the NaOH be of 50 percent concentration or higher, at a temperature at which the NaOH is a li~uid. After the NaAlO2xNaOH is prepared, it is diluted during its use in the present invention. When preparing the aluminate solution, it is also preferred that there be about 1.0 to 1.5 mole of NaOH per mole of Al(OH)3, since too much caustic tends to solubilize the crystalline hydrous alumina seed which is provided in the porous substrate to serve as precipi-tation sites for additional growth of crystalline hydrous alumina. The alkaline material may be KOH, but it is more costly.

In preparing a porous substrate having "seeds"
of crystalline Al(OH)3 within the small pores, it is not generally possible or practical to insert appreciable amounts of non-soluble crystals into the pores. There-fore, the seeds are best implanted by providing aluminumsolution in the pores and then precipitating hydrous alu-mina ln situ within the pores. To accomplish this one may use a soluble Al salt, e.g., AlC13, and then alkalize the A1 to insoluble Al(OH)3. This freshly formed Al(OH)3, being amorphous, is then treated in one of various ways to cause the Al(OH)3 to crystallize.

29,261-F -5-6 4 ~

When the substrate is a weak base anion--exchange resin in its basic form, the preferred proce-dure for incorporating Al(OH)3 seeds therein is to add an a~ueous solution of AlC13 to where the amount of Cl is about e~uivalent to the base capacity. After about 1 hour at room temperature (or somewhat shorter times if the mixture is warmed to not more than about 60C), most, if not all, of the Al values have been converted to Al(OH)3. This is followed by washing out excess AlCl3, titrating to the resin-OH capacity with NaOH and washing again to substantially remove remaining chlorides.

When the substrate is any other porous struc-ture (other exchange resins, polymers or inorganic inert materials), it is recommended that the seeds be implanted lS within the pores by using soluble Al (such as AlCl3) which is precipitated ln situ using NH40H to form Al(OH)3 in the pores. Excess AlCl3, or Al(OH)3 formed outside the pores, is easily washed away.

once the seed of Al(OH)3 is implanted in the pores of the substrate it may be conveniently crystallized as nordstrandite, bayerite or gibbsite, e.g., as follows:

1. To obtain nordstrandite use a soluble amine, e.g., ethylenediamine (about 20 percent concentration) at about 50C overnight, then wash out the amine.

2. To obtain bayerite use NH3 (about 1-30 percent in H20) at reflux temperature for 1-16 hours or more, then wash out excess NH40H.

29,261-F -6-~ ~ 7~645 .

3. To obtain gibbsite use aqueous NaOH in an amount of about 0.1-0.5 mole of NaOH per mole of Al(OH)3, boil for about 0.5 hour or more, and wash with H2O. Sodi-um aluminate may be used instead of the NaOH.

Any of the above-described seeds of crystal-line Al(OH)3 may be used as growth sites for producing additional crystalline Al(OH)3 by treatment with alka-line aluminate solution. If this additional treatment is done at less than about 50C, the newly-precipitated crystalline Al(OH)3 is principally nordstrandite and/or bayerite; if done at greater than about 50C it is prin-cipally gibbsite. There is a tendency for the seed crys-tal to promote formation of additional Al(OH)3 having the same crystal structure as the seed.

The NaAlO2 xNaOH, once formed, and having a NaOH/Al(OH)3 ratio generally in the range of about l.O--1.5, is then preferably used as a diluted aqueous solu-tion of about 5-30 percent concentration by weight as the precursor for the additional Al(OH)3 growth on the seed. The NaAlO2 xNaOH solution is mixed with the seed--containing porous substrate. As the aluminum oxide in the sodium aluminate becomes crystallized to Al(OH)3, the pH increases. Addition of more amorphous aluminum hydroxide lowers the pH by reforming additional sodium aluminate and solubilizes the amorphous alumina which then crystallizes out of the sodium aluminate and pro-duces further growth of the seeded crystalline Al(OH)3 which is, again, indicated by a rise in the pH. The step of adding NaAlO2 xNaOH, or of adding amorphous alu-mina to reform NaAlO2 xNaOH, may be repeated one or more 29,261-F -7-~ 3 ~'~6~ `

times until the relative speed of pH change is slowed, indicating that the pores are substantially filled with crystalline Al(OH)3 and any additional formation of crys-talline Al(OH)3 is likely to take place outside the pores.
If additional pre-formed NaAlO2 xNaOH is added as a source of additional crystalline Al(OH)3, it should be preceded by an amount of acid (preferably HCl) to neutralize the caustic already present from a previous addition of sodium aluminate. This prevents the caustic from building to a concentration which would resolubilize the desired crys-talline Al(OH)3.

Another technique for causing additional pre-cipitation of hydrous alumina onto the seed, is to add the alkaline aluminate in an amount sufficient to supply all, or even an excess, of the aluminate values expected to be precipitated. Then by slow or incremental addition of an acid, e.g., HCl, the alkaline metal is converted to alkali metal salt (e.g., NaCl), thus decreasing the ratio of alkali metal hydroxide in the alkaline aluminate, thereby causing precipitation of the aluminate and caus-ing the seed to add to this additional aluminate.

It can be seen, then, that by reacting amor-phous aluminum hydroxide to form sodium aluminate, the amorphous aluminum hydroxide is solubilized. The solu-bilized amorphous aluminum hydroxide, in the presenceof the crystalline Al(OH)3 seed, precipitates out as crystalline Al(OH)3 and the seed increases in size.

The reaction of LiX (i.e., a lithium salt or lithium compound) with the crystalline hydrous alumina is performed using an aqueous solution of the LiX and 29,261-F -8-~ ~ . 364 ~ `

employing, preferably, an elevated temperature. It is best if the LiX is a concentrated solution and the tem-perature is at or near the boiling point. Weak solutions of LiX and/or lower temperatures of reaction are less effective in obtaining a high degree of the desired inter-calation in a reasonable length of time.

The term "intercalation" is used to indicate that the reaction of the LiX with the crystalline hydrous alumina hydroxide creates LiX 2Al(OH)3 nH2O crystals wherein the LiX moiety lies between layers of the hydrous alumina hydroxide and causes an expansion of the hydrous alumina crystal lattice. The LiX can be substantially leached out, but so long as a significant percentage of it remains, e.g., about 50 percent of the possible amount, the crystal lattice remains expanded and the amount of intercalated LiX can be replenished until the lattice is again loaded with LiX.

The advantages of the present method and of using NaAlO2 xNaOH as the source of hydrous alumina to build crystalline Al(OH)3 in the substrate are:

1. crystalline Al(OH)3 (such as gibbsite, bayerite, nordstrandite and mixtures of these) can, by being combined with NaOH, be used and the substrate sub-stantially loaded with the crystalline material, using fewer steps than are shown in U.S. Patents 4,116,856 and 4,116,858 (both previously identified);
c 2. because it is not necessary to dry the substrate ~such as an ion-exchange resin) after the first 29,261-F -9_ i ~ 7~S

loading step, osmotic shock is substantially decreased and substrate breakage or decrepitation is substantially avoided;

i 3. because the composite is neutralized only once, aluminum loss due to neutralization problems is minimized;

4. one may selectively prepare 2-layer lith-ium aluminates or 3-layer lithium aluminates; and

5. having the hydrous alumina present in the porous substrate as crystalline Al(OH)3 rather than amor-phous Al(OH)3 is beneficial in providing optimum loading of LiX, thereby forming crystalline Li~-2Al(OH)3 nH20 in a more consistent and expeditious manner.

Example 1 (a) Lithium Aluminate from Gibbsite A macroporous strong acid ion-exchange resin (525 ml) containing 10 percent divinylbenzene is stirred into an equal volume of 29 percent aqueous AlCl3 solution.
The resin is filtered so that the excess AlCl3 solution is removed from the resin. The resin is dried to free--flowing resin with dry N2 and then stirred into 600 ml of aqueous 30 percent NH3 solution. The mixture is washed. The resin is contacted with an ex`cess of brine to convert RSO3NH4 to RSO3Na and then filtered to remove all of the solution from the beads. The resin is then added to 456 g of H2O and 230 g of NaAlO2 ~NaOH solution 29,261-F -10-4~

(from gibbsite and 50 percent NaOH). The mixture is stirred and heated to 75C-80C for one hour. The tem-perature is reduced to 70C and five 25-g additions of amorphous Al~OH)3 are added at 10-minute intervals.
After the last addition, the heat and stirrer are turned off and the resin mixture is allowed to set overnight.
The final aluminum content of the washed resin is approx-imately 3.92 mmoles of Al/ml of resin. X-ray diffraction analysis shows very crystalline gibbsite is present in the resin.

(b) Conversion to 2-Layer Lithium Aluminate The resin is refluxed in 30 percent aqueous LiCl solution for at least 4 hours. The resin now con-tains 2-layer LiCl 2Al(OH)3 nH2O.

(c) Preparation of 3-Layer LiCl 2Al(OH)3 nH O in a porous substrate via gibbsite 2 The same resin employed in (a) (110 ml) and containing gibbsite, prepared as described above, is heated with 110 ml of an aqueous solution containing 8.31 g of LiCl and 3.52 g of LioH-H2o. The resulting slurry is stirred at a temperature of 75C. lN NaOH
(75 ml) are added and the resin is heated for another ~ hour. The resin is placed in a 95C oven for 12 hours.
; X-ray analyses of samples taken periodically show a decrease in the amount of gibbsite with a corresponding increase in the amount of LiCl-2Al(OH)3 nH2O.

29,261-F -11-~ ~ J 36~5 The resin is then washed and neutralized with HCl in a solution containing NH4Cl and LiCl. Neutraliza-tion to a pH of 5.6 (at room temperature) requires about 220 milliequivalents of HCl. The LiCl LioH gibbsite reac-tion will also take place at 25C.

(d) The same resin employed in (a) and (c) above (225 ml) and containing gibbsite (3.7 mmoles of Al/ml of resin) is placed in a stainless steel beaker with 275 ml of H2O and 35 g of LioH-H2o and the mixture heated to 80C. X-ray analysis shows that all of the gibbsite is converted to 3-layer LiOH-2Al(OH)3-nH20 in about 30 min-utes. The resin is neutrali~ed with HCl. This reaction also occurs at room temperature but at a much slower rate.

Example 2 (a) Preparation of 3-Layer LiCl-2Al(OH)3-nH2O in a Porous Substrate via Bayerite A macroporous weak base ion-exchange resin ;20 (500 ml) in the chloride form is poured into an equal vol-ume of saturated aqueous AlCl3 solution. The slurry is ; stirred without heating for 40 minutes. The resin is fil-tered by suction until all of the excess AlC13 solution is removed from the resin and the resin is stirred into 500 ml of 30 percent NH3 in H20 at room temperature. An exotherm from 25C to 30C is observed. The resin is stirred for a total of 20 minutes. The ammonia solution is poured off of the resin and the resin is allowed to set for 16 hours at room temperature. X-ray analysis of 29, 261-F -12-) 6 ~ ~

the resin shows that bayerite has formed in the resin.
There is still a large amount of amorphous Al(OH)3 pres-ent. Aluminum analysis indicates that the resin contains 0.7 mmoIe of Al/ml of resin at this point.

The resin is washed thoroughly so that the filtrate is clear. Even a small amount of crystalline Al(OH)3 in the solution phase cannot be tolerated.

The resin and 230 ml of deionized water are stirred and heated to 45C and 173 g of freshly prepared NaAlO2 xNaOH is added to the slurry. This mixture is reacted for 1 hour. From x-ray data it can be seen that the amorphous Al(OH)3 content of the resin is decreased.

Four 216-g additions of amorphous Al(OH~3 are added at 15-minute intervals. After the last addi-tion, the resin is allowed to stand for 16 hours. X-ray analysis of the product shows only well crystallized bayerite.

(b) The resin described above (210 ml) is neutra-lized with 240 milliequivalents of HCl. The resin is then heated at 110C-115C in 250 ml of 30 percent LiCl solution for 1.5 to 3 hours. Very crystalline 3-layer LiCl 2Al(OH)3 nH2O is the product. No further neutrali-zation is necessary.

~ayerite in porous resin can also be converted to 3-layer lithium aluminate by reaction with LioH or a mixture of LiCl and LioH.

29,261-F -13-3 ~ ,'()6~S

Example 3 - Growth of Nordstrandite in a Porous Sub-strate The same resin employed in Example 2 (500 ml) is poured into an equal volume of aqueous 25 percent AlC13 solution and the mixture is stirred for 30-40 min-utes. The resin is then filtered to remove the excess AlC13 and stirred into 30 percent NH40H solution. The resin is stirred for 30 minutes and washed thoroughly with H20. The resin is successively treated with NH40H
and H20 until substantially all of the Cl is removed.
The resin is washed with deionized water to remove all traces of NH40H.

The resin is then placed in a polyethylene bottle with an egual volume of 12 percent ethylenedia-mine and heated at 50C for 16 hours. X-ray shows the presence of nordstrandite.

The resin is then contacted with an e~ual vol-ume of deionized water and 230 g of fresh NaA102-~NaOH for one hour. Five 25-g additions of amorphous Al(OH)3 are then added at 15-minute intervals. The resulting product is nordstrandite in the pores of the resin.

Exam~le 4 - The Modified Method for High Loading of Crystalline Hydrous Alumina To 3000 ml of the same resin employed in Exam-ples 2 and 3 except that it was in the OH' form, was addedwater to a total of 3750 ml was stirred as 147 g of anhy-drous AlC13 were added. Stirring was continued for one 29,261-F -14-7 ~ 6 ~ 5 hour as the pH slowly rose to 5. The slurry was ~ell washed with deionized water until the effluent was almost colorless. The washed resin was reslurried with 40 ml of 30 percent NH3 and 155 ml of 50 percent NaOH to a pH of 10.5. The resin was then washed on a filter.

A sample of 197 ml of the resin so prepared was slurried in H2O with 5.22 g of NaAlO2 nNaOH (NaAlO2 xNaOH
is a solution of sodium aluminate made by dissolving 1960 g of gibbsite in 2100 ml of 50 percent NaOH at 100C). The final volume of resin was 192 ml.

The resin was transferred to a one-liter beaker and 299 g of NaAlO2 xNaOH was added plus water to a total volume of 540 ml. By means of a pump, 36 percent HCl was metered into the stirred slurry at a rate of 1 ml/minute. The temperature rose to a maximum of 40C and it was maintained at 30C-40C during the course of the HCl addition. The pH decreased from 14 to 12.8. The pump was controlled by the pH, and near the end of the HCl addition, was essentially in an on-off mode as the pH fluctuated. After 164 ml of 35 percent HCl had been added the slurry was well washed to yield 230 ml of resin which contained 4.63 mmoles of Al/cc of resin. The Al was present as bayerite as determined by x-ray.

Example 5 The same resin employed in Examples 2 and 3 (200 ml) was treated at room temperature with a large excess of aqueous 25.5 percent AlCl3. The resin is sucked dry on a filter funnel and dumped into 200 ml of 29,261-F -15-~ 5 30 percent aqueous ammonia and stirred for 15 minutes.
The resin is rinsed briefly with water and allowed to stand overnight at room temperature. It was titrated to stable 10.1 pH with 74 ml of N/1 NaOH. The resin was then washed until chloride free to give a settled volume of 166 ml and was added to water to a total vol-ume of 260 ml. A sodium aluminate solution (4.4 g) (1960 g of gibbsite dissolved in 2100 ml of 50 percent NaOH at 100C) was added. After one hour of stirring at room temperature an additional 70 g of sodium alumi-nate solution was added. After an additional 45 minutes of stirring at 30C-35C, the pH had risen to 13.6. Dur-ing the next hour four equal additions of amorphous Al(OH)3 (100 g ~ 1 mole Al) of 9 g each were made. The pH held at 13.5-13.6. The supernatant solution was fil-tered and returned to the resin pot with a pH increase to 13.9. Two more 9-g additions of amorphous Al(OH)3 were made during the next hour and then two more 9-g additions in the next 45 minutes. The washed resin, with a settled volume of 203 ml, showed an aluminum content of 4.5 mmoles/ml.

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Claims (8)

1. A process for growing crystalline hydrous alumina within the pores of a porous substrate, character-ized by providing a seed of crystalline hydrous alumina in said pores by the in situ precipitation of a water-soluble aluminum compound, thereby forming amorphous hydrous alu-mina; converting the so-formed amorphous hydrous alumina to crystalline hydrous alumina by heating; and adding to the seed-bearing substrate an aqueous solution of an alka-line aluminate, thereby providing aluminum oxide values which grow additional quantities of crystalline hydrous alumina on the crystalline hydrous alumina seeds.

2. The process of Claim 1 wherein the alka-line aluminate comprises NaAlO2-xNaOH where x is a numeri-cal value of 0.1 to 0.5.

3. The process of Claim 1 wherein the production of the additional quantities of crystalline hydrous alumina is promoted by addition of an acid which forms a soluble salt with the alkali.

4. The process of Claim 3 wherein the acid is HCl.

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5. The process of Claim 1 wherein the por-ous substrate is selected from the group consisting of inorganic, organic, polymeric and resinous materials.

6. The process of Claim 1 wherein the por-ous substrate is a macroporous ion-exchange resin.

7. The process of Claim 1 and including the additional step of reacting the so-formed crystal-line hydrous alumina with LiOH to form crystalline LiOH?2Al(OH)3?nH2O.

8. The process of Claim 1 and including the additional step of reacting the so-formed crystal-line hydrous alumina with lithium salt, LiX, to form crystalline LiX?2Al(OH)3?nH20 where X is the anion of the lithium salt.

29,261-F -18-