Alumina hydrate production from Bayer liquor by seeding

Claim 1

In the Bayer process of producing alumina hydrate from bauxite wherein bauxite is digested with a caustic liquor at elevated temperatures and pressures to extract alumina values from the bauxite in the form of a pregnant caustic aluminate liquor and wherein alumina hydrate is recovered from the pregnant liquor by seeded precipitation, the improvement for obtaining a strong, coarse alumina hydrate product in increased yield which comprises: (A) establishing three separate but interconnected precipitation stages for effecting agglomeration, growth and seed generation, carrying out each stage in a series of vessels; (B) charging a portion of the pregnant liquor to the agglomeration stage, the liquor having an A/C ratio from about 0.575 to about 0.700 and a caustic concentration, expressed in grams/liter Na 2 CO 3 , from about 165 to about 300 g/l, adding alumina hydrate seed to the liquor in an amount from about 70 to about 140 g/l of liquor, maintaining the seeded liquor within the temperature range from about 74° to about 85° C. for a time period from about 8 to about 24 hours to precipitate alumina hydrate in a slurry form, removing the slurry and subjecting it to size classification to recover an overflow slurry fraction containing fine alumina hydrate particles and an underflow slurry fraction containing coarse alumina hydrate particles; (C) charging another portion of the pregnant liquor to the growth stage, adding to the liquor the coarse alumina hydrate from step (B) and alumina hydrate seed thus forming a slurry, the combined hydrate amount added to the liquor being kept within the range of about 120-300 grams/liter of pregnant liquor, maintaining the slurry within the temperature range from about 74° to about 85° C. for a time period from about 8 to about 24 hours to allow precipitation of alumina hydrate and cementation of the seed and coarse alumina hydrate with newly precipitated alumina hydrate, removing the slurry and subjecting it to size classification to generate an overflow slurry fraction containing fine alumina hydrate particles and an underflow slurry fraction containing strong, coarse alumina hydrate product; (D) charging to the seed generation stage at least one of the overflow slurry fractions generated in steps (B) or (C), adding seed and maintaining the slurry from about 6 to about 24 hours within the temperature range from about 57° to about 66° C., removing the slurry and subjecting it to size classification to obtain an underflow slurry fraction containing coarse alumina hydrate particles and an overflow slurry fraction containing fine alumina hydrate particles, charging the underflow slurry fraction to step (C) to form strong, coarse alumina hydrate product and charging the overflow slurry fraction to at least one of the steps (B) or (C) as seed.