High capacity adsorbent for oxyanions and cations and method for making the same

Abstract

An alumina-based adsorbent and method of making exhibiting high affinity and capacity towards cations and oxyanions in a broad pH range and presence of large excess of competitive ions. Alumina based adsorbent is a mixed oxide of alumina existing in tetra-, penta-, and octahedral coordination at specific ratio, and oxides of polyvalent metals of elements titanium, zirconium, tin, cerium, lanthanum, iron, or combinations thereof. The alumina-based adsorbent may be used for selective removal of oxyanions of fluoride, phosphorus, arsenic, chromium, and/or selenium, and/or cations of lead, mercury, cadmium, copper, and/or zinc, from drinking water, industrial streams and wastes, in medicine and food industry.

Claims

1. An adsorbent for removal of fluoride ion and oxyanions of fluoride, phosphorus, arsenic, chromium, and/or selenium, said adsorbent comprising mixed oxide containing alumina in tetra-, penta-, and octahedral coordination, and a polyvalent metal oxide including titanium, zirconium, tin, iron, or any combination of thereof, wherein an amount of pentahedrally coordinated alumina is from about 10% to about 30% by weight, and an amount of tetrahedrally coordinated alumina is from about 5% to about 15% by weight.

2. The adsorbent of the claim 1 wherein content of said alumina in said mixed oxide is from about 20 wt % to about 80 wt %.

3. The adsorbent of the claim 1 wherein content of said alumina in said mixed oxide is from about 50 wt % to about 80 wt %.

4. The adsorbent of the claim 1 wherein said mixed oxide does not show phase segregation and remains amorphous up to 500° C.

5. The adsorbent of the claim 1 wherein said mixed oxide shows adsorption capacity decrease less than 40% after calcination.

6. The adsorbent of claim 1, wherein said adsorbent is capable of removing radioactive or non-radioactive versions of cesium, strontium, and/or barium.

7. The adsorbent of the claim 1 wherein said adsorbent is capable of removing naturally occurring alkali-metals and alkali-earth metals Groups 1 and 2.

8. The adsorbent of the claim 1 wherein said mixed oxide comprises said alumina formed from an aluminum sulfate component, said polyvalent metal oxide is formed from a mixed-metal acid component, and wherein said mixed oxide further comprises a basic component.

9. The adsorbent of claim 8 wherein said mixed mixed-metal acid component comprises a dissolved ore containing titanium, iron, manganese or combinations thereof.

10. The adsorbent of the claim 8 wherein said mixed metal acid component is comprised of an ore dissolved in hot sulfuric acid, to form a mixture of sulfates, such that once dissolved, remaining liquid is added to said aluminum sulfate component.

11. The adsorbent of claim 10 wherein said mixture of sulfates includes titanyl sulfate or iron sulfate.

12. The adsorbent of claim 11 wherein said titanyl sulfate is used to form said mixed metal oxide, said titanyl sulfate being combined with an aluminum sulfate salt and/or an iron salt.

13. The adsorbent of claim 1 wherein said mixed oxide is thermally stable, and has an adsorption capacity decrease of less than 40% after calcination.

14. An adsorbent for removal of cations of lead, mercury, cadmium, copper, and/or zinc, said adsorbent comprising mixed oxide containing alumina in tetra-, penta-, and octahedral coordination, and a polyvalent metal oxide including titanium, zirconium, tin, iron, or any combination of thereof, wherein an amount of pentahedrally coordinated alumina is from about 10% to about 30% by weight, and an amount of tetrahedrally coordinated alumina is from about 5% to about 15% by weight.

15. The adsorbent of the claim 14 wherein content of said alumina in said mixed oxide is from about 20 wt % to about 80 wt %.

16. The adsorbent of the claim 14 wherein content of said alumina in said mixed oxide is from about 50 wt % to about 80 wt %.

17. The adsorbent of the claim 14 wherein said mixed oxide does not show phase segregation and remains amorphous up to 500° C.

18. The adsorbent of the claim 14 wherein said mixed oxide shows adsorption capacity decrease less than 40% after calcination.

19. The adsorbent of the claim 14 wherein said mixed oxide comprises said alumina formed from an aluminum sulfate component, said polyvalent metal oxide is formed from a mixed-metal acid component, and wherein said mixed oxide further comprises a basic component.

20. The adsorbent of claim 19 wherein said mixed-metal acid component comprises a dissolved ore containing titanium, iron, manganese or combinations thereof.

21. The adsorbent of the claim 19 wherein said mixed metal acid component is comprised of an ore dissolved in hot sulfuric acid, to form a mixture of sulfates, such that once dissolved, remaining liquid is added to said aluminum sulfate component.

22. The adsorbent of claim 21 wherein said mixture of sulfates includes titanyl sulfate or iron sulfate.

23. The adsorbent of claim 22 wherein said titanyl sulfate is used to form said mixed metal oxide, said titanyl sulfate being combined with an aluminum sulfate salt and/or an iron salt.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The features of the invention believed to be novel and the elements characteristic of the invention are set forth with particularity in the appended claims. The figures are for illustration purposes only and are not drawn to scale. The invention itself, however, both as to organization and method of operation, may best be understood by reference to the detailed description which follows taken in conjunction with the accompanying drawings in which:

(2) FIG. 1 graphs P/A separation factors calculated from adsorption capacities on As and P as a function of equilibrium pH on hydrous titanium oxide, hydrated ferric oxide, aluminum hydroxide, and the mixed oxide 33.4% TiO.sub.2-66.6% Al.sub.2O.sub.3 from Example 3; and

(3) Fluoride breakthrough curves are presented in FIG. 2 for the alumina based mixed oxide made in Example 3.

(4) FIG. 3 depicts isotherm data comparing the metal oxide adsorbent of the present invention (MOX-Invention) against TiO.sub.2 and disodium titanate, measuring capacity removal of Cr (mg/g) as a function of equilibrium concentration (ppm);

(5) FIG. 4 depicts isotherm data comparing the metal oxide adsorbent of the present invention (MOX-Invention) against disodium titanate, measuring capacity removal of Pb (mg/g) as a function of equilibrium concentration (ppm);

(6) FIG. 5 depicts a graph charting kinetic data for one embodiment of the metal oxide adsorbent of the present invention (MOX-Invention) versus disodium titanate for the removal of lead (Pb);

(7) FIG. 6 depicts a graph of Cd removal capacity for the metal oxide adsorbent developed pursuant to the present invention (MOX-Invention) versus titanium oxide (TiO.sub.2);

(8) FIG. 7 depicts a graph of copper (Cu) removal capacity for the metal oxide adsorbent developed pursuant to the present invention (MOX-Invention) and titanium oxide (TiO.sub.2); and

(9) FIG. 8 depicts a graph of zinc removal capacity for metal oxide developed pursuant to the metal oxide adsorbent of the present invention (MOX-Invention) versus titanium oxide (TiO.sub.2).

DESCRIPTION OF THE PREFERRED EMBODIMENT(S)

(10) In describing the preferred embodiment of the present invention, reference will be made herein to FIGS. 1-8 of the drawings in which like numerals refer to like features of the invention.

(11) The deficiencies of the prior art as discussed above can be alleviated or overcome by the adsorbent of the present invention. The present invention is directed to a high capacity mixed oxide adsorbent comprising alumina that exists in tetra-, penta-, and octahedral coordination, and a polyvalent metal oxide selected from the group of titanium, zirconium, tin, cerium, lanthanum, iron, or any combination thereof, that can be used for simultaneous selective removal of fluoride ion and oxyanions of phosphorus, arsenic(V) and arsenic(III) from different aqueous streams. The present invention is applicable to other oxyanions as well. Utilizing the composition of the present invention, oxyanions may be removed in varying degrees of efficiency. The mixed adsorbent of the present invention has been demonstrated to remove oxyanions such as chromium (trivalent or hexavalent, as chromate or dichromate), and selenium, such as selenite.

(12) Mixed oxide adsorbent is an amorphous material that contains from about 20 wt % up to about 80 wt % of alumina, or preferably from about 500% to about 80% of alumina, in which aluminum exists in octahedral, pentahedral, and tetrahedral coordination, wherein the amount of pentahedrally coordinated aluminum is from about 10% to about 30%, and tetrahedrally coordinated aluminum is from about 5% to about 15%.

(13) The unexpected result of the present invention is a strong synergism between all elements in the mixed oxide composition resulting in a significant increase of media adsorption capacity towards fluoride ion and oxyanions of phosphorus and arsenic in comparison with alumina hydroxide or activated alumina (on the order of twice to six times greater), as well as with other individual polyvalent metal oxides tested under similar conditions. Moreover, the applicability to oxyanions generally is realized.

(14) In one embodiment, aluminum hydroxides are able to adsorb arsenic(V) and have no affinity towards arsenic(III), and alumina-based mixed oxides of present invention are able to remove both arsenic(V) and arsenic(III) species with a significant capacity increase only for arsenic(V).

(15) There appears to be less synergistic affect towards other oxyanions like silicate, chromate, sulfate, and the like. However, testing has provided an unexpected result in the amount of removal of certain cations, that would otherwise not be considered candidates for the adsorbent of the present invention. In this regard, the removal of chromium (chromate), and selenium, and other less responsive oxyanions, although less efficient than the removal of fluoride ion and oxyanions of phosphorus and arsenic, is still significant enough to adopt the proposed mixed oxide adsorbent of the present invention for removal of these contaminants.

(16) As an illustrative example, Table I depicts a comparison of the removal of chromium by various compositions. As depicted, the removal of chromium as demonstrated by the mixed oxide composition of the present invention was at least as effective as the other compositions tested, and in most cases exceeded the removal amount.

(17) TABLE-US-00001 TABLE 1 Adsorbent Cr removed (mg)/dry media (g) disodium titanate 0 TiO.sub.2 (50 μm) 0.051 TiO.sub.2 (1.0 μm) 0.377 EnviroScrub 0.7814 MOX-Invention 1 0.589 MOX - Invention 2 0.837

(18) EnviroScrub is an aqueous amine mixture which irreversibly reacts with contaminants such as hydrogen sulfide and mercaptan. It is generally used to remove H.sub.2S from hydrocarbon liquids, natural gas, gas streams, waste-water streams, and scrubber systems. MOX—Invention 1 and MOX—Invention 2 represent two separate trial runs in the test.

(19) FIG. 3 depicts isotherm data comparing the metal oxide adsorbent of the present invention (MOX-Invention) against TiO.sub.2 and disodium titanate, measuring capacity removal of Cr (mg/g) as a function of equilibrium concentration (ppm). As depicted, the isotherm data indicates that the metal oxide adsorbent of the present invention is capable of a higher removal capacity at lower concentration levels, where the other adsorbents are unable to challenge.

(20) Table II depicts a comparison of the removal of selenium species (Se.sup.4+, Se.sup.6+) by various compositions. As depicted, the removal of selenium as demonstrated by the composition of the present invention was at least as effective as most other compositions tested, save ETS-4, and in most cases, at least one test composition of the present invention exceeded the removal amount of other tested compositions.

(21) TABLE-US-00002 TABLE II Adsorbent Se.sup.4+ (mg)/dry media (g) Se.sup.6+ (mg)/dry media (g) TiO.sub.2 (1.0 μm) 42.5 24.1 disodium titanate 18.3 0.0 EnviroScrub 47.1 5.7 ETS-4 7.8 62.1 ETS-10 4.1 27.9 MOX-Invention 1 56.2 9.5 MOX-Invention 2 57.0 35.5

(22) Comparisons were made to titanium oxide, AMP-025, EnviroScrub, and Englehard Corporation titanosilicate ETS-4 and ETS-10. The capacities depicted in Table II are based on selenium species, not on the full anion of selenite or selenite. Thus, the present invention is shown effectively capable of removing a plurality of oxyanions, inclusive of chromium and selenium.

(23) With respect to fluoride, the proposed mixed oxide has capacity on fluoride ion from about 40 mg F/g up to about 80 mg F/g at a pH range of approximately 7 to 6, respectively. Advantageously, the adsorbent's capacity on the fluoride ion does not decrease more than 30% in the presence of competitive ions that are approximately 10 to approximately 100 times in excess. The competitive ions typically include HCO.sub.3, Cl, NO.sub.3, SO.sub.4, or any such combination, and do not decrease more than 40% in the presence of equimolar amounts of phosphate, silicate ions, or their combination.

(24) Alumina based mixed oxide has higher affinity towards phosphate ion over arsenic ions with a separation factor for phosphorus/arsenic from approximately 1.2 to about 2 in equimolar solutions. Individual polyvalent metal oxides do not show preferences in uptake of these ions, and may preferably remove arsenic ions, like hydrous titanium oxide. The measured alumina based adsorbent capacity on the PO.sub.4 ion from hemo-dialysate solution at a pH level of about 5-6 is at least 160 mg PO.sub.4/g, and at least 100 mg PO.sub.4/g from a peritoneal dialysate solution at a pH level of about 7-8, which makes it an efficient phosphate scavenger in such applications as, for example, artificial kidney devices.

(25) Another advantage of the present invention is that mixed oxide is a thermally stable adsorbent and has an adsorption capacity decrease of less than 40% (after calcination at 450° C. for 2 hours).

(26) Some of the hydroxides (aluminum hydroxide, ferric hydroxide, zirconium hydroxide, and the like) are amphoteric and appear to behave as cation exchangers or anion exchangers depending upon the pH level. This unexpected result has been confirmed by the data taken with respect to the composition of the present invention. In particular, testing has shown the improved capacity of the composition of the present invention over standard oxides, such as TiO.sub.2 for contaminants such as Pb, Hg, Cu, Cd, and Zn, among others.

(27) Table III depicts a comparison of the removal of mercury (Hg) by various adsorbent compositions. As depicted, the removal of Hg as demonstrated by the adsorbent composition of the present invention was at least as effective as most other adsorbent compositions tested.

(28) TABLE-US-00003 TABLE III Adsorbent Hg removed (mg)/dry media (g) TiO.sub.2 (1.0 μm) >0.326 TiO.sub.2 (50 μm) 0.326 TiO.sub.2 0.326 (different source) Zeolite 0.166 titanosilicate 0.439 MOX-Invention 1 0.403

(29) The adsorbent composition of MOX—Invention Test 1 indicates an appreciable removal amount of mercury with respect to the other compositions compared, fared better than the others, and removal capacity was similar with that of the titanosilicate composition.

(30) Similar comparative tests were performed for lead (Pb) removal. Table IV depicts the removal amount results of various compositions with respect to Pb. In this comparison, the adsorbent composition of Invention Test 1 was shown to be the most effective in removing lead.

(31) TABLE-US-00004 TABLE IV Adsorbent Pb removed (mg)/dry media (g) MOX-Invention 1 500 TiO.sub.2 (50 μm) 163 titanoaluminosilicate 171 TiO.sub.2 (1 μm) 227 disodium titanate 239 ETS-4 247 ATS 1 280 ATS 2 303 ETS-10 350

(32) In the comparisons of Table IV, ATS was one of the compositions compared. ATS is a high capacity ceramic ion-exchanger with strong kinetics due to its formation, and is selective predominantly for lead removal even in the presence of competing ions like calcium and magnesium.

(33) FIG. 4 depicts isotherm data comparing the metal oxide adsorbent of the present invention (MOX-Invention) against disodium titanate, measuring capacity removal of Pb (mg/g) as a function of equilibrium concentration (ppm). As depicted, the isotherm data indicates how quickly the media of the present invention removes Pb. The metal oxide adsorbent composition of the present invention has faster kinetics and a slightly higher overall capacity for removal.

(34) As demonstrated above, the synthesis of a mixed metal oxide (MOX) and its subsequent use to remove oxyanions is achieved by the mixed metal oxide adsorbent composition of the present invention.

(35) Additionally, cations such as Pb.sup.2+, Hg.sup.2+, Cu.sup.2+, may also be removed by the composition of the present invention. The media of the present invention has demonstrated a capacity of at least 385 mg/g for lead removal. This is significantly higher than the Pb capacity of TiO.sub.2 alone, which suggests a reason for this unexpected result, that recombination of the metal oxides allow for sorption (adsorption or ion-exchange) of cations simultaneously with anion removal.

(36) Activated carbons are generally not successful in removing cations without additional additives. For example, Graver Technologies' Metsorb STP® can be added to an activated carbon component to remove Pb to a much higher capacity than activated carbon alone. Activated carbon can remove Hg.sup.2+, but usually only after treatment with a secondary material, such as a thiol or sulfuric acid. The adsorbent of the present invention does not require this.

(37) In general, ion-exchange properties, either cation or anion, of adsorbent composite materials depend on the type of impregnated oxide chosen, and as a rule capacity increases up to a certain point with an increase of inorganic oxide content; however, the correlation between the amount of dopant oxide and capacity is not universal, as in many cases capacity is a function of a specific metal oxide phase/structure formed in the pores, and it can vary significantly for similar loadings of the same polyvalent metal oxide. The synthetic method used to form such inorganic adsorbent and composite materials is unique. The compositions identified herein are essentially synthesized from a non-pure basis to provide a mixed oxide (or hydroxide) to remove both cations and anions simultaneously. As an example, an embodiment of the present invention that forms cation/anion sorption media comprises: a mixed metal oxide including alumina, titania, and other metals, for example, Fe, Mn, Mg, and such other metals prevalent in ores.

(38) This sorption exchange material preferably includes metal oxide of aluminum oxides and titanium oxides, and doping polyvalent metal oxide including zirconium, tin, cerium, lanthanum, iron, or manganese, or any combination thereof, where the mixed oxide or the doping polyvalent metal oxide or both are configured to selectively adsorb organic molecules, fluoride ion, oxyanions of phosphorous and arsenic, or heavy metals such as Pb, Hg, Cd, and the like. In yet another unexpected result, an adsorbent composition of the present invention has been shown to be capable of removing naturally occurring cations from the alkali-metal, alkali-earth metals (Groups 1-2), including radioactive and non-radioactive versions of Cs, Sr, Ba, Ra, and the like, under conditions where they are dissolved ions in water.

(39) In one embodiment, the mixed metal oxide is preferably formed from an aluminum sulfate component, a mixed-metal acid component, and a basic component. The mixed metal acid component is comprised of a dissolved ore, such as ilmenite, rutile, or titanium slag. The ore is dissolved in hot sulfuric acid to make a mixture of sulfates (titanyl sulfate, iron sulfate, etc.). After the dissolution of the ore, the remaining liquid (and solids) are added to aluminum sulfate (or another aluminum salt).

(40) FIG. 5 depicts a graph charting kinetic data for one embodiment of the metal oxide adsorbent of the present invention (MOX-Invention) versus disodium titanate for the removal of lead (Pb). As depicted, the adsorbent of the present invention removes significantly more lead over a shorter period of time than the disodium titanate, showing a considerable difference in the first 200 minutes.

(41) With respect to the removal of oxyanions other than the aforementioned arsenic and phosphorus, FIG. 6 depicts a graph of Cd removal capacity for the metal oxide adsorbent developed pursuant to the present invention (MOX-Invention) versus titanium oxide (TiO.sub.2). This data indicates that while the metal oxide adsorbent composition of the present invention (MOX-Invention) does not have as high of a capacity, it does adsorb a measurable amount more cadmium in solution when compared to the TiO.sub.2 adsorbent.

(42) Similarly, FIG. 7 depicts a graph of copper (Cu) removal capacity for the metal oxide adsorbent developed pursuant to the present invention (MOX-Invention) and titanium oxide (TiO.sub.2). Data shows that while the metal oxide adsorbent composition of the present invention (MOX-Invention) does not have as high of a removal capacity, it does adsorb a measurable amount more copper in solution as a function of the concentration of copper than that compared to the TiO.sub.2 material.

(43) FIG. 8 depicts a graph of zinc removal capacity for metal oxide developed pursuant to the metal oxide adsorbent of the present invention (MOX-Invention) versus titanium oxide (TiO.sub.2). Data shows that while the metal oxide adsorbent composition of the present invention (MOX-Invention) does not have as high of a capacity at lower concentrations, it does adsorb a measurable amount more zinc in solution than that compared to the TiO.sub.2 material at higher concentrations of zinc.

(44) In another embodiment of the present invention, a method of making the aforementioned alumina-based mixed oxides is taught. The method requires a reaction between a solution or a slurry containing an aluminum compound, a polyvalent metal compound, and a base solution in the pH range of approximately 4 to about 10, ageing freshly formed precipitate in mother-liquor (a residual liquid resulting from the crystallization and remaining after the substances that readily or regularly crystallize have been removed) at the pH level of precipitation, washing the precipitate with water, and subsequently drying precipitate.

(45) Specific to the method of forming the aluminum compound, a water soluble compound is chosen, preferably including aluminum sulfate, aluminum chloride, aluminum nitrate, and combinations thereof, or aluminum oxide pseudo-sol. The polyvalent metal compound preferably comprises water soluble nitrates, chlorides, sulfates of titanium, zirconium, tin, cerium, lanthanum, iron, or combinations thereof, or sol of titanium, zirconium, tin, cerium, lanthanum, iron, or combinations thereof. Additionally, polyvalent metal compound may comprise nano sized titanium, zirconium, tin, cerium, lanthanum, iron oxides, or combinations thereof.

(46) Another feature of the method of the present invention is that precipitation may be carried out at a constant pH level, which is kept in the range of 4-10 under batch or continuous flow conditions by using base chosen from alkali hydroxides, ammonium hydroxide, alkali carbonates, ammonium carbonate, and combinations thereof.

(47) The precipitation may be carried at a pH level changing from acidic to about 4-10 under batch conditions by the addition of a base reagent chosen from alkali hydroxides, ammonium hydroxide, alkali carbonates, ammonium carbonate, or combinations thereof.

(48) On the final stage, freshly formed alumina based mixed oxide precipitate is aged in mother-liquor at the pH level of precipitation at ambient or elevated temperature for 1-3 hours and then dried.

(49) The present invention is described more specifically by reference to the following exemplary embodiments, which are not intended to limit the invention described in the appended claims.

Example I

(50) In a first exemplary embodiment, preparation of a metal containing solution of the present invention involves mixing 130.6 g of Al.sub.2(SO.sub.4)3*18H.sub.2O, 133 g of a 15.0 wt % titanyl sulfate solution (on TiO.sub.2) and 400 g of deionized water. Metal containing solution and 25 wt % solution of NaOH are added simultaneously into a 2 L glass beaker filled with 800 mL of water with the use of a peristaltic pump at a predetermined flow rate which allows for a constant pH level of 5 in the reaction mixture, the pH level being constant throughout the precipitation process. Next, the precipitate of alumina titania mixed oxide is aged in mother-liquor at ambient temperature for 1 hour, and then the aged precipitate is separated from mother-liquor by filtration and washed with deionized water. The wet cake is then dried at 100° C. in air for approximately 18 hours. The dry adsorbent contains 50% Al.sub.2O.sub.3 and 50% TiO.sub.2.

Example II

(51) In a second exemplary embodiment, preparation of the metal containing solution comprises mixing 130.6 g of Al.sub.2(SO.sub.4)3*18H.sub.2O, 133 g of a 15.0 wt % titanyl sulfate solution (on TiO.sub.2), and 400 g of deionized water. The metal containing solution and 25 wt % solution of NaOH are then added simultaneously into a 2 L glass beaker filled with 800 mL of water with the use of peristaltic pump at a predetermined flow rate that maintains a constant pH level at about 9 in the reaction mixture throughout precipitation process. Next, the precipitate of alumina titania mixed oxide is aged in mother-liquor at ambient temperature for 1 hour and then the aged precipitate is separated from mother-liquor by filtration and washed with deionized water. The wet cake is dried at 100° C. in air for 18 hours. The resultant dry adsorbent contains 50% Al.sub.2O.sub.3 and 50% TiO.sub.2.

Example III

(52) In a third exemplary embodiment, preparation of a metal containing solution comprises mixing 94.5 g of AlCl.sub.3*6H.sub.2O, 66.5 g of a 15.0 wt % titanyl sulfate solution (on TiO.sub.2), and 400 g of deionized water. N.sub.aOH at 25 wt % solution is slowly added to a beaker with the metal containing solution until the pH level reaches 7. Next, the precipitate of alumina titania mixed oxide is aged in mother-liquor at ambient temperature for 3 hours and then the aged precipitate is separated from mother-liquor by filtration and washed with deionized water. The wet cake was dried at 100° C. in air for 18 hours. The dry adsorbent contains approximately 66.6% Al.sub.2O.sub.3 and 33.4% TiO.sub.2.

Example 4

(53) In a fourth exemplary embodiment, preparation of a metal containing solution comprises mixing 147 g of Al(NO.sub.3)3*9H.sub.2O, 10 g of anatase TiO.sub.2, and 400 g of deionized water. NaOH at 25 wt % solution is slowly added to a beaker with metal containing solution until a pH level of approximately 7 is reached. Next, the precipitate of alumina titania mixed oxide is aged in mother-liquor at ambient temperature for 3 hours, and then the aged precipitate is separated from mother-liquor by filtration, and washed with deionized water. The wet cake is then dried at 100° C. in air for 18 hours. The dry adsorbent contains approximately 66.6% Al.sub.2O.sub.3 and 33.4% TiO.sub.2.

Example 5

(54) In a fifth exemplary embodiment, the preparation of a metal containing solution comprises mixing 100 g of 20% aluminum hydroxide pseudo-solution, 10 g of rutile TiO.sub.2 and 300 g of deionized water. A 25 wt % solution of NaOH is added slowly to a beaker with the metal containing solution until the pH level reaches approximately 7. Next, the precipitate of alumina titania mixed oxide is aged in mother-liquor at ambient temperature for 3 hours, and then the aged precipitate is separated from mother-liquor by filtration, and washed with deionized water. The wet cake is dried at 100° C. in air for 18 hours. The dry adsorbent contains 66.6% Al.sub.2O.sub.3 and 33.4% TiO.sub.2.

Example 6

(55) In a sixth exemplary embodiment, the preparation of a metal containing solution comprises mixing 130.6 g of Al.sub.2(SO.sub.4)3*18H.sub.2O, 100 g of a 20 wt % ZrOCl.sub.2 solution (on ZrO.sub.2), and 400 g of deionized water. The metal containing solution and 25 wt % solution of NaOH are added simultaneously into a 2 L glass beaker filled with 800 mL of water with the use of peristaltic pump at a predetermined flow rate to maintain a constant pH level of 7 in the reaction mixture throughout precipitation process. Next, the precipitate of alumina zirconia mixed oxide is aged in mother-liquor at ambient temperature for 1 hour, and then the aged precipitate is separated from mother-liquor by filtration, and washed with deionized water. The wet cake is dried at 100° C. in air for 18 hours. The dry adsorbent contains 50% Al.sub.2O.sub.3 and 50% ZrO.sub.2.

Example 7

(56) In a seventh exemplary embodiment, a preparation of metal containing solution comprises mixing 130.6 g of Al.sub.2(SO.sub.4)3*18H.sub.2O, 100 g of a 20 wt % La(NO.sub.3)3 (on La.sub.2O.sub.3) solution, and 400 g of deionized water. The metal containing solution and 25 wt % solution of NaOH are added simultaneously into a 2 L glass beaker filled with 800 mL of water with the use of peristaltic pump at a predetermined flow rate to maintain a constant pH level of 7 in the reaction mixture throughout precipitation process. Next, the precipitate of alumina lanthanum mixed oxide is aged in mother-liquor at ambient temperature for 1 hour, and then the aged precipitate is separated from mother-liquor by filtration, and washed with deionized water. The wet cake is dried at 100° C. in air for 18 hours. The dry adsorbent contains 50% Al.sub.2O.sub.3 and 50% La.sub.2O.sub.3.

Example 8

(57) In an eighth exemplary embodiment, the preparation of a metal containing solution comprises mixing 130.6 g of Al.sub.2(SO.sub.4)3*18H.sub.2O, 67.5 g of FeCl.sub.3*6H.sub.2O, and 400 g of deionized water. The metal containing solution and 25 wt % solution of NaOH is added simultaneously into a 2 L glass beaker filled with 800 mL of water with the use of peristaltic pump at a predetermined flow rate maintaining a constant pH level of approximately 7 in the reaction mixture throughout precipitation process. Next, the precipitate of alumina iron mixed oxide is aged in mother-liquor at ambient temperature for 1 hour, and then the aged precipitate is separated from mother-liquor by filtration, and washed with deionized water. The wet cake is dried at 100° C. in air for 18 hours. The dry adsorbent contains 50% Al.sub.2O.sub.3 and 50% Fe.sub.2O.sub.3.

Example 9

(58) The Al-27 MAS NMR spectra of freshly prepared alumina hydroxide and alumina based mixed oxides have been recorded on a Bruker Avance III 400 MHz spectrometer.

(59) TABLE-US-00005 Sample Octahedral Al % Pentahedral Al % Tetrahedral Al % Al(OH).sub.3 100 0 0 50% Al.sub.2O.sub.3- 80 15 5 50% TiO.sub.2 Example 2 50% Al.sub.2O.sub.3- 60 25 15 50% ZrO.sub.2 Example 6 50% Al.sub.2O.sub.3- 80 15 5 50% Fe.sub.2O.sub.3 Example 8 67% Al.sub.2O.sub.3- 70 70 10 33% TiO.sub.2 Example 3

Example 10

(60) Adsorption experiments have been carried out under batch conditions with a contact time 18 hours. The following test solutions were used in the adsorption experiments:

(61) a) Fluoride ion—10 ppm F+2 mM NaHCO.sub.3+2 mM Na.sub.2SO.sub.4, pH=6;

(62) b) Phosphate ion—0.83 ppm P+2 mM NaHCO.sub.3, pH=8; and

(63) c) Arsenate ion—2 ppm As+2 mM NaHCO.sub.3, pH=8.

(64) Commercial adsorbents, such as those from GFO (Bayer), MetSorb (Graver Technologies) and activated alumina AA400, have been used for a comparison study.

(65) TABLE-US-00006 TABLE V Ion Exchange Capacities (IEC) of test ions on alumina based mixed oxides Sorbent IEC-F, mg/g IEC-PO4, mg/g IEC-AsO4, mg/g Example 1 75 55 65 Example 2 70 55 70 Example 3 70 50 60 Example 4 65 50 60 Example 5 65 50 60 Example 6 75 55 70 Example 7 80 60 65 Example 8 65 50 65 GFO, Granular 10 12 20 Ferric Oxide MetSorb TiO2 12 10.5 17 Activated 15 7 7 Alumina AA400

Example 11

(66) Adsorption experiments have been carried out under batch conditions with a contact time 18 hours. The following equimolar test solutions were used in adsorption experiments:

(67) a) Phosphate ion—0.83 ppm P+2 mM NaHCO.sub.3, pH=8; and

(68) b) Arsenate ion—2 ppm As+2 mM NaHCO.sub.3, pH=8

(69) Adsorption capacities on As and P as a function of equilibrium pH on hydrous titanium oxide, hydrated ferric oxide, aluminum hydroxide, and mixed oxide 33.4% TiO.sub.2-66.6% Al.sub.2O.sub.3 from Example 3 have been determined and P/As separation factors have been calculated from experimental data according to formula:
SF=IEC−P/IEC−As (at fixed pH),
and presented in FIG. 1. As seen Fe.sub.2O.sub.3 and Al.sub.2O.sub.3 do not show selectivity to AsO.sub.4 or PO.sub.4 in the pH range 6-10, whereas anatase TiO.sub.2 exhibits affinity towards AsO.sub.4 at a pH level of greater than or equal to 7. Alumina based mixed TiO.sub.2—Al.sub.2O.sub.3 shows distinct affinity towards phosphate ion over arsenate ion in the tested pH range. The separation factor P/As for this media increases with an increase of equilibrium pH reaching a value of 1.5 at a pH=8, and 1.9 at a pH=9.7.

Example 12

(70) The alumina based mixed oxide made in Example 3 (66.6% Al.sub.2O.sub.3-33.4% TiO.sub.2, particle size 45-75 μm) and activated alumina 400G (particle size 45-75 μm) were tested for fluoride ion removal from tap water spiked with 6.2 ppm F and pH=7.5 under column conditions. In both cases two grams of adsorbent were placed in a glass column with inner diameter 8 mm and test solution was passed through an adsorbent bed with flow rate 80 BV/hr. Fluoride breakthrough curves are presented in FIG. 2. As seen, alumina-based adsorbent from Example 3 (purifies˜3,300 BV) outperform the benchmark activated alumina 400G (purifies˜500 BV) before breakthrough (1.5 ppm F) more than 6 times.

Example 13

(71) The effect of competitive ions on fluoride ion sorption on mixed oxide of Example I is shown in the Table VI. Initial concentration of fluoride ion in all test solutions was 10 ppm and contact time was 18 hours.

(72) TABLE-US-00007 TABLE VI Effect of competitive ions on fluoride ion sorption on alumina-titania mixed oxide Competitive ion Ion Excess, times IEC-F, mg/g — — 75 HCO.sub.3 5 65 Cl 50 70 SO.sub.4 25 65 SiO.sub.3 4 45 PO.sub.4 1 45

Example 14

(73) Effect of thermal treatment on AsO.sub.4 ion sorption on mixed oxide of Example I is shown in the Table VII. The arsenic test solution contained 2 ppm As(V), pH=8. The fluoride test solution contained 10 ppm F in tap water, pH=7.5. The contact time was 18 hours.

(74) TABLE-US-00008 TABLE VII Effect of thermal treatment on AsO4 and F ion uptake by alumina-titania adsorbent IEC 100° C., IEC 250° C., IEC 350° C., IEC 450° C., Ion mg/g mg/g mg/g mg/g AsO.sub.4 75 65 60 50 F 25 21 19 18

(75) While the present invention has been particularly described, in conjunction with a specific preferred embodiment, it is evident that many alternatives, modifications and variations will be apparent to those skilled in the art in light of the foregoing description. It is therefore contemplated that the appended claims will embrace any such alternatives, modifications and variations as falling within the true scope and spirit of the present invention.