Method for processing bauxites

• US 3,944,648 A
• Filed: 07/03/1974
• Issued: 03/16/1976
• Est. Priority Date: 07/07/1973
• Status: Expired due to Term

• Current Assignee: Almasfuzitoi Timfoldgyar, Femipari Kutato Intezet, Vallalat; Aluterv Aluminiumipari Tervezo
• Original Assignee: Almasfuzitoi Timfoldgyar, Femipari Kutato Intezet, Vallalat; Aluterv Aluminiumipari Tervezo
• Inventors: Lengyel, Laszlo, Siklosi, Peter, Feher, Ivan, Ferenczi, Tibor, Solymar, Karoly, Toth, Pal, Matyasi, Jozsef, Voros, Istvan, Zambo, Janos, Wentzely, Kalman, Sigmond, Gyorgy, Pinter, Tihamer, Lazar, Ferenc, Bujdoso, Erno, Ozvald, Zoltan, Orban nee Kelemen, Marika
• Primary Examiner(s): Carter, Herbert T.
• Application Number:
  US05/485,570
• Time in Patent Office: 622 Days
• Field of Search: 423/121, 423/128, 423/131, 423/129
• US Class Current: 423/121
• CPC Class Codes: C01F 7/0633 characterised by the use of additives

Abstract

A method for processing bauxites according to the Bayer technology, with an increased yield in Al₂ O₃ and with decreased caustic soda losses, starting particularly from goethite bauxites of boehmite and/or diaspore type and carrying out the digestion at 180°C to 300°C using an aluminate liquor containing Na₂ O_caustic in a concentration of 80 to 300 g./l. The digestion is carried out in the presence of a calcium compound in an amount corresponding to 2 to 6 % of CaO calculated for the dry weight of bauxite and of a sulfate salt in an amount corresponding to 1.0 to 7.0 g./l. of sulfate ion concentration, whereby the goethite content of the bauxite is converted into hematite. The process provides advantageous conditions for the complete dissolution of the boehmite and diaspore content of bauxite in the vicinity of the equilibrium molar ratio, and enables to recover efficiently the caustic soda losses in the Bayer process itself, requiring no supplementary operation.

Claims

1. A method for processing goethite-containing bauxite to aluminum hydrate according to the Bayer technology, in which bauxite is digested in sodium hydroxide and the resulting material clarified to remove red mud, with an increased yield of aluminum hydrate and with decreased losses of sodium hydroxide, comprising conducting said digestion at 200°

to 250°

C. in an aluminate liquor containing Na₂ O_caustic in a concentration of 80 to 300 g./l., and a calcium compound selected from the group consisting of calcium carbonate, calcium oxide, calcium hydroxide and calcium sulfate in an amount corresponding to 2 to 6% by weight of CaO calculated on the dry weight of the bauxite and a sulfate salt selected from the group consisting of sodium sulfate and calcium sulfate in an amount corresponding to 1.0 to 7.0 g./l. of sulfate ion concentration, whereby the goethite content of the bauxite is converted into hematite.

2. A method as claimed in claim 1, in which said sulfate salt is calcium sulfate and the amount of said calcium compound is decreased by the CaO content of said calcium sulfate.

3. A method as claimed in claim 1, in which calcium carbonate is added in the form of a calcite-containing bauxite.

4. A method for processing goethite-containing bauxite to aluminum hydrate according to the Bayer technology, in which bauxite is digested in sodium hydroxide and the resulting material clarified to remove red mud, with an increased yield of aluminum hydrate and with decreased losses of sodium hydroxide, comprising conducting said digestion at 200°

to 250°

C. in an aluminate liquor containing Na₂ O_caustic in a concentration of 80 to 300 g./l., and calcined lime in an amount corresponding to 2 to 6% by weight of CaO calculated on the dry weight of the bauxite and sodium sulfate in an amount corresponding to 1.0 7.0 g./l. of sulfate ion concentration, whereby the goethite content of the bauxite is converted into hematite.

5. A method as claimed in claim 4, in which said aluminate liquor contains sodium chloride in a concentration of 1 to 20 g./l.

6. A process as claimed in claim 4, in which said temperature is about 235°

to 245°

C.

7. A process as claimed in claim 4, in which said digestion is performed in an autoclave.