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US3944648A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for processing bauxites

Assignee: Individual
•
Filing: 1974-07-03
•
Granted: 1976-03-16
•
Expires: 1994-07-03
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Abstract

Abstract A method for processing bauxites according to the Bayer technology, with an increased yield in Al 2 O 3 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 Na 2 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.

Inventors

  • 👤 Karoly Solymar
  • 👤 Janos Zambo
  • 👤 Marika Orban nee Kelemen
  • 👤 Erno Bujdoso
  • 👤 Ivan Feher
  • 👤 Zoltan Ozvald
  • 👤 Istvan Voros
  • 👤 Tibor Ferenczi
  • 👤 Pal Toth
  • 👤 Ferenc Lazar
  • 👤 Tihamer Pinter
  • 👤 Gyorgy Sigmond
  • 👤 Peter Siklosi
  • 👤 Kalman Wentzely
  • 👤 Laszlo Lengyel
  • 👤 Jozsef Matyasi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 22:28
CPC Classifications
C; C01; C01F; C01F7/00; C01F7/02; C01F7/04; C01F7/06; C01F7/062; C01F7/0633

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 148 words
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 Na 2 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.
Claim 2
Independent Claim 148 words
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 Na 2 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.
Claim 3
Dependent Claim 32 words
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.
Claim 4
Dependent Claim 20 words
A method as claimed in claim 1, in which calcium carbonate is added in the form of a calcite-containing bauxite.
Claim 5
Independent Claim 119 words
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 Na 2 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.
Claim 6
Independent Claim 119 words
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 Na 2 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.
Claim 7
Dependent Claim 23 words
A method as claimed in claim 4, in which said aluminate liquor contains sodium chloride in a concentration of 1 to 20 g./l.
Claim 8
Dependent Claim 16 words
A process as claimed in claim 4, in which said temperature is about 235° to 245°C.
Claim 9
Dependent Claim 16 words
A process as claimed in claim 4, in which said digestion is performed in an autoclave.

References Cited (Backward Citations)

US663167A Cited
US1422004A Cited
US2181669A Cited
US2519362A Cited
US2926069A Cited
US3210155A Cited
US3737514A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-03-16 1979-09-15 1980-03-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-03-16 1983-09-15 1984-03-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-03-16 1987-09-15 1988-03-16 $7700.00 Window Closed / Lapsed

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