Process for preparing cryolite from fly ash
AssigneeIowa State University Research Foundation, Inc.
InventorsMustafa Boybay, Turgut Demirel
Life of this patent
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Abstract
Cryolite (Na.sub.3 AlF.sub.6) as a source of aluminum is prepared from coal fly ash by reacting the aluminum oxide (Al.sub.2 O.sub.3) in fly ash with phosphoric acid to form aluminum phosphate, which is then converted to sodium aluminate by reaction with sodium hydroxide, and the sodium aluminate is converted to cryolite by reaction with hydrofluoric acid (HF), or equivalent reagent providing H.sup.+ and F.sup.- ions. Aluminum is thereby obtained from fly ash in a preferred form (as cryolite) for use in producing metallic aluminum.
Claims10
The process of preparing cryolite (Na.sub.3 AlF.sub.6) from a coal fly ash containing aluminum oxide as one of the principal constitutents, comprising:
- (a) reacting aqueous phosphoric acid (H.sub.3 PO.sub.4) with said fly ash to convert a substantial portion of the aluminum of said fly ash to aluminum phosphate (AlPO.sub.4), thereby obtaining a first reaction mixture containing a substantial amount of AlPO.sub.4 ;
- (b) adding aqueous sodium hydroxide (NaOH) to said first reaction mixture and reacting said NaOH therewith to form a second reaction mixture, the amount of NaOH added being sufficient to convert said AlPO.sub.4 to sodium aluminate (Na.sub.3 AlO.sub.3);
- (c) separating the undissolved solids from said second reaction mixture to obtain a solution containing said Na.sub.3 AlO.sub.3 ;
- (d) adding hydrogen ions (H.sup.+) and fluoride ions (F.sup.-) to said Na.sub.3 AlO.sub.3 contaning solution to form cryolite as a precipitate, said addition being continued to a final pH below 9.0;
- and
- (e) separating the precipitated cryolite from the residual solution.
The process of preparing cryolite (Na.sub.3 AlF.sub.6) from coal fly ash containing Al.sub.2 O.sub.3, Fe.sub.2 O.sub.3, CaO, and SiO.sub.2 as principal constituents, comprising:
- (a) reacting aqueous phosphoric acid (H.sub.3 PO.sub.4) with said fly ash, at least 12% by weight of said fly ash being Al.sub.2 O.sub.3 and the amount of said CaO being less than 6% by weight, said H.sub.3 PO.sub.4 containing not over 30% water by weight and being employed in a molar ratio of 0.6 to 2.0 moles of H.sub.3 PO.sub.4 per Fly Ash Acidification Mole (FAA Mole), said FAA Mole being computed as 2 times the total moles of Al.sub.2 O.sub.3 and Fe.sub.2 O.sub.3 in the amount of fly ash used plus 0.67 times the moles of CaO therein, thereby converting the Al.sub.2 O.sub.3 to aluminum phosphate (AlPO.sub.4);
- (b) adding aqueous sodium hydroxide (NaOH) to convert said AlPO.sub.4 to sodium aluminate (Na.sub.3 AlO.sub.3), the resulting reaction mixture containing solids and having a pH of above 12.0;
- (c) separating the solids from said reaction mixture to obtain a solution containing said Na.sub.3 AlO.sub.3 at a pH above 12.0;
- (d) adding hydrogen ions (H.sup.+) and fluoride ions (F.sup.-) to said Na.sub.3 AlO.sub.3 containing solution to reduce the pH to below 8.5 with the formation of cryolite;
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- (e) separating the precipitated cryolite from the residual solution.
Dependencies are inferred from the claim text.