DEFLUORIDATION OF WATER

• US 20090305883A1
• Filed: 06/09/2009
• Published: 12/10/2009
• Est. Priority Date: 06/09/2008
• Status: Abandoned Application

• Current Assignee: Alcoa Incorporated (Howmet Aerospace, Inc.)
• Original Assignee: Alcoa Incorporated (Howmet Aerospace, Inc.)
• Inventors: Labhsetwar, Nitin, Rayalu, Sadhana, Kamble, Sanjay, Ghosh, Rajat S.
• Application Number:
  US12/481,433
• Publication Number:
  US 20090305883A1
• Time in Patent Office: Days
• US Class Current: 502/400
• CPC Class Codes: B01J 20/02 comprising inorganic material
• CPC Class Codes: B01J 20/0266 Compounds of S
• CPC Class Codes: B01J 20/041 Oxides or hydroxides
• CPC Class Codes: B01J 20/06 comprising oxides or hydroxides of metals not provided for in group B01J20/04
• CPC Class Codes: B01J 20/08 comprising aluminium oxide or hydroxide; comprising bauxite
• CPC Class Codes: B01J 20/28059 being less than 100 m2/g
• CPC Class Codes: B01J 2220/42 Materials comprising a mixture of inorganic materials materials coated or impregnated on a carrier B01J20/32
• CPC Class Codes: B01J 2220/4881 Residues from shells, e.g. eggshells, mollusk shells
• CPC Class Codes: C02F 1/281 using inorganic sorbents
• CPC Class Codes: C02F 1/283 using coal, charred products, or inorganic mixtures containing them
• CPC Class Codes: C02F 1/286 using natural organic sorbents or derivatives thereof
• CPC Class Codes: C02F 1/288 using composite sorbents, e.g. coated, impregnated, multi-layered
• CPC Class Codes: C02F 2101/14 Fluorine or fluorine-containing compounds
• CPC Class Codes: C02F 2209/06 pH

Abstract

Bio-ceramic compositions for removing fluoride from water, and methods for making the same are disclosed. The bio-ceramic composition may comprise alumina, calcium oxide, sulfur, and/or carbon. The bio-ceramic composition may be produced from at least one natural media, such as chitin or eggshell membrane. The bio-ceramic composition may realize an initial fluoride adsorption capacity, in water, of at least about 5 mg/g.

Claims

1. A method comprising:

(a) preparing a liquid mixture comprises at least one natural media, alum and a calcium source;

(b) recovering a bio-ceramic adsorbent from the liquid mixture, wherein the bio-ceramic adsorbent comprises an initial fluoride adsorption capacity, in water, of at least about 5 mg/g.

2. The method of claim 1, wherein the natural media is eggshell membrane, wherein the calcium source is eggshell, and wherein the bio-ceramic adsorbent comprises about 45-65 wt. % alumina, about 10-20 wt. % calcium oxide, about 5-15 wt. % sulfur, and about 1-5 wt. % carbon.

3. The method of claim 1, wherein the recovering step comprises:

(i) agitating the liquid mixture;

(ii) drying the liquid mixture and recovering a mass;

(iii) calcining the mass; and

(iv) washing the mass.

4. The method of claim 3, wherein the recovering step comprises:

(v) grinding the mass.

5. The method of claim 1, wherein the bio-ceramic adsorbent at least comprises a first phase and a second phase, wherein the first phase is a crystalline alumina phase, and wherein the second phase is an amorphous alumina phase.

6. The method of claim 1, wherein the natural media is chitin, and wherein the bio-ceramic adsorbent comprises about 15-35 wt. % alumina, about 20-40 wt. % calcium oxide, about 5-20 wt. % sulfur, and about 1-5 wt. % carbon

7. A bio-ceramic adsorbent produced from at least one natural media, the adsorbent comprising 15-65 wt. % of a metal oxide, 10-40 wt. % calcium oxide, 5-20 wt. % sulfur, and 1-5 wt. % carbon, wherein the bio-ceramic adsorbent comprises an initial fluoride adsorption capacity, in water, of at least about 5 mg/g.

8. The bio-ceramic adsorbent of claim 7, wherein the adsorbent is produced from at least two natural media, wherein the first natural media is at least one of eggshell membrane, chitin, and wherein the second natural media is a natural calcium support material.

9. The bio-ceramic adsorbent of claim 8, wherein the natural calcium support material comprises is eggshell.

10. The bio-ceramic adsorbent of claim 9, wherein the metal oxide comprises an aluminum oxide.

11. The bio-ceramic adsorbent of claims 10, wherein the bio-ceramic adsorbent comprises a crystalline phase and an amorphous phase, and wherein the crystalline phase comprises at least some aluminum oxide.

12. The bio-ceramic adsorbent of claim 11, wherein the crystalline phase comprises at least one of α

-alumina, β

-alumina, and γ

-alumina.

13. The bio-ceramic adsorbent of claim 11, wherein the crystalline phase comprises both of α

-alumina and β

-alumina.

14. The bio-ceramic adsorbent of any of claim 7, wherein the bio-ceramic adsorbent is capable of removing fluoride from water, wherein the bio-ceramic adsorbent comprises an initial fluoride adsorption capacity of at least about 8 mg/g, wherein the initial fluoride concentration of the water is not greater than 100 mg/L.

15. The bio-ceramic adsorbent of claim 14, wherein the bio-ceramic adsorbent has a regenerated fluoride adsorption capacity that is at least 40% of the initial fluoride adsorption capacity.

16. The bio-ceramic adsorbent of claim 14, wherein the initial fluoride adsorption capacity is achievable in the presence of at least about 500 mg/L of sulfate anions.

17. The bio-ceramic adsorbent of any of claim 16, wherein the initial fluoride adsorption capacity is achievable when the water has a pH of from about pH 4 to about pH 9.

18. The bio-ceramic adsorbent of claim 17, wherein the bio-ceramic adsorbent comprises a specific surface area of not greater than about 30 m² per gram.

19. The bio-ceramic adsorbent of claim 18, wherein the bio-ceramic adsorbent has a bulk density of at least about 1.00 g/cm³.

20. An adsorbent produced from at least one natural media, the adsorbent comprising α

-alumina and β

-alumina, wherein the adsorbent is capable of removing fluoride from water, wherein the adsorbent comprises an initial fluoride adsorption capacity of at least about 5 mg/g, wherein the initial fluoride adsorption capacity is achievable in the presence of at least about 500 mg/L of sulfate anions, and wherein the initial fluoride adsorption capacity is achievable when the water has a pH of from about pH 4 to about pH 9.