GB883311A - Improvements in and relating to the production of alumina - Google Patents

Improvements in and relating to the production of alumina

Info

Publication number
GB883311A
GB883311A GB28409/59A GB2840959A GB883311A GB 883311 A GB883311 A GB 883311A GB 28409/59 A GB28409/59 A GB 28409/59A GB 2840959 A GB2840959 A GB 2840959A GB 883311 A GB883311 A GB 883311A
Authority
GB
United Kingdom
Prior art keywords
solution
stage
alumina
adjusted
precipitate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB28409/59A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Commonwealth Scientific and Industrial Research Organization CSIRO
Original Assignee
Commonwealth Scientific and Industrial Research Organization CSIRO
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Commonwealth Scientific and Industrial Research Organization CSIRO filed Critical Commonwealth Scientific and Industrial Research Organization CSIRO
Publication of GB883311A publication Critical patent/GB883311A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F7/00Compounds of aluminium
    • C01F7/02Aluminium oxide; Aluminium hydroxide; Aluminates
    • C01F7/20Preparation of aluminium oxide or hydroxide from aluminous ores using acids or salts
    • C01F7/26Preparation of aluminium oxide or hydroxide from aluminous ores using acids or salts with sulfuric acids or sulfates

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Paper (AREA)

Abstract

<PICT:0883311/III/1> Alumina is obtained from solutions produced by dissolving aluminium-containing materials, for example bauxite, in sulphuric acid by so adjusting the solution that the SO3 : Al2O3 weight ratio is less than 2,35 (which value corresponds to Al2(SO4)3), hydrolysing the adjusted solution at 180 DEG -300 DEG C. to precipitate a basic aluminium sulphate or hydrated alumina, and decomposing this precipitate to leave alumina. The hydrolysis is preferably carried out under pressure. The SO3 : Al2O3 weight ratio in the solution may be adjusted by dissolving aluminium metal in the solution, or by digesting the solution with a source of alumina, for example bauxite, preferably at 100 DEG C. to 140 DEG C., or by electrolysing the solution in a cell provided with a suitable membrane, for example a selective anion exchange membrane, paper, or parchment, thereby removing sulphate ions from the solution in the cathode compartment, or by adding to the solution, which may have been partially adjusted, some of the hydrolysis precipitate from a previous batch or a basic aluminium sulphate from any source. In examples, crushed bauxite is digested with sulphuric acid under pressure in digestion stage 1. If sufficient air or oxygen is provided, at least part of the sulphuric acid may be replaced by pyrite. The liquor from stage 1 is passed to modification stage 2, where the SO3 : AL2O3 ratio is adjusted by any of the methods previously indicated. Any iron in the solution may be reduced to the ferrous state by aluminium metal or other reducing agent. The adjusted liquor is passed to precipitation stage 3, where it is maintained at 180 DEG -300 DEG C. to permit hydrolysis to take place. The precipitate is recovered, and part is recycled to stage 3 and the remainder is calcined in stage 4 to give alumina product and sulphur dioxide, which is passed to digestion stage 1. The liquor from stage 3 is similarly recycled to stage 1.
GB28409/59A 1958-08-21 1959-08-19 Improvements in and relating to the production of alumina Expired GB883311A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AU883311X 1958-08-21

Publications (1)

Publication Number Publication Date
GB883311A true GB883311A (en) 1961-11-29

Family

ID=3763330

Family Applications (1)

Application Number Title Priority Date Filing Date
GB28409/59A Expired GB883311A (en) 1958-08-21 1959-08-19 Improvements in and relating to the production of alumina

Country Status (1)

Country Link
GB (1) GB883311A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4177242A (en) * 1977-02-28 1979-12-04 Aluminum Pechiney Method of obtaining pure alumina by acid attack on aluminous minerals containing other elements
US4244928A (en) * 1978-01-13 1981-01-13 Veb Mansfeld Kombinat William Pieck Process for the production of pure aluminum oxide
US6468483B2 (en) 2000-02-04 2002-10-22 Goldendale Aluminum Company Process for treating alumina-bearing ores to recover metal values therefrom

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4177242A (en) * 1977-02-28 1979-12-04 Aluminum Pechiney Method of obtaining pure alumina by acid attack on aluminous minerals containing other elements
US4244928A (en) * 1978-01-13 1981-01-13 Veb Mansfeld Kombinat William Pieck Process for the production of pure aluminum oxide
US6468483B2 (en) 2000-02-04 2002-10-22 Goldendale Aluminum Company Process for treating alumina-bearing ores to recover metal values therefrom

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