Improvements in or relating to process for the production of coarse grained alumina hydrate from aluminate liquors

摘要

PICT:0696465/III/1 Coarse grained hydrated alumina is produced by precipitation from a fresh portion of super-saturated aluminate solution in the presence of the coarse fraction of a previously precipitated and classified hydrate, whilst agitating the mixture, and the fine particles precipitated are separated from the enlarged coarser particles formed by growth of the seed particles. In one procedure, alumina is precipitated in the presence of relatively fine seed particles and the slurry passed to two cone classifiers. The fine hydrate slurry is used as seed for a fresh initial precipitation, and the coarse hydrate underflow passed in part to washing, filtering and drying apparatus, and in part, as seed, to a tank supplied with fresh aluminate liquor. When the precipitation has reached a point at which aluminacaustic weight ratio is about 0.4, the air lift agitation is discontinued, and natural classification is allowed to begin. About half of the slurry, containing the largest crystals, are pumped to a quiescent settling tank, and the balance passed to the first of the two cone classifiers above referred to, to which is also passed the finer hydrate slurry from the quiescent settling tank. The coarse particle fraction from the latter, containing not less than 70 per cent by weight of particles of plus 200 mesh size, passes to an elutriator, and thence to filtering, and drying or calcining zones. In Fig. 2, fresh aluminate liquor is pumped from tank 65 to a series of precipitating tanks 50, 50a-c. Precipitation occurs in tank 50 in the presence of fine seed from storage tank 55. After stratification, the coarser particle fraction is pumped to a settling tank 51, and the coarser particle fraction therefrom to the second precipitating tank 50a, and so on through the series of tanks. The fine particle fractions from all the settling tanks 51, 51a-c pass to thickener 61, and thence to storage tank 55, the spent liquor passing to the alumina-digester 64. The final coarsest particle slurry from tank 51c passes to wet screening 67 or hydraulic classification 68, and thence to filter 71, and drier 73 or calciner 74. The coarse particle slurry is discharged from tank 51c by injection of water, or the filtrate 78 from filter 71.