Abstract Coarse grains of aluminum hydroxide having high resistance to disintegration to powder in a calcination step are continuously produced from a supersaturated sodium aluminate solution of the Bayer process through (1) a first precipitation step of adding recycle seed aluminum hydroxide to a supersaturated sodium aluminate solution having a molar ratio of Na2O as caustic soda to Al2O3 in solution of less than 1.8 supplied to a precipitation tank of substantially complete mixing type in a ratio of 30-150 kg of the recycle seed to 1 m3 of the solution, thereby partially decomposing the seed-added solution until the molar ratio of the solution reaches 2.0-2.4 while keeping the solution at 65 DEG -80 DEG C.; (2) a second precipitation step of supplying the resulting sodium aluminate solution in a slurry state from the first precipitation step to at most three precipitation tanks of growth type arranged in series and decomposing the solution in the slurry state until the molar ratio reaches at least 2.6 while keeping the solution in the slurry state at a precipitated solid aluminum hydroxide concentration of 400-1,500 g/l and at a slurry temperature of 45 DEG -65 DEG C. in the precipitation tanks of growth type, and (3) a third step of supplying the decomposed solution in a slurry state from the second precipitation step to a classifier, thereby classifying the precipitated aluminum hydroxide grains into coarse grains of aluminum hydroxide as product and fine grains of aluminum hydroxide, and recycling the fine grains of aluminum hydroxide as seed.
A process for producing coarse grains of aluminum hydroxide by continuously precipitating coarse grains of aluminum hydroxide from a supersaturated sodium aluminate solution of the Bayer process, which comprises: (1) a first precipitation step of adding recycle seed aluminum hydroxide to a supersaturated sodium aluminate solution having a molar ratio of Na 2 O as caustic soda to Al 2 O 3 in solution of less than 1.8 supplied to a precipitation tank of substantially complete mixing type in a ratio of 30-150 kg of the recycle seed to 1 m 3 of the solution, thereby partially decomposing the seed-added solution until the molar ratio of the solution reaches 2.0-2.4 while keeping the solution at 65°-80° C.; (2) a second precipitation step of supplying the resulting sodium aluminate solution in a slurry state from the first precipitation step to at most three precipitation tanks of growth type arranged in series and decomposing the solution in the slurry state until the molar ratio reaches at least 2.6 while keeping the solution in the slurry state at a precipitated solid aluminum hydroxide concentration of 400-1,500 g/l and at a slurry temperature of 45°-65° C. in the precipitation tanks of growth type; and (3) a third step of supplying the decomposed solution in a slurry state from the second precipitation step to a classifier, thereby classifying the precipitated aluminum hydroxide grains into coarse grains of aluminum hydroxide as product and fine grains of aluminum hydroxide, and recycling the fine grains of aluminum hydroxide as seed.
Claim 2
Dependent Claim
252 words
A process for producing coarse grains of aluminum hydroxide by continuously precipitating coarse grains of aluminum hydroxide from a supersaturated sodium aluminate solution of the Bayer process, which comprises: (1) a first precipitation step of adding recycle seed aluminum hydroxide to a supersaturated sodium aluminate solution having a molar ratio of Na 2 O as caustic soda to Al 2 O 3 in solution of less than 1.8 supplied to a precipitation tank of substantially complete mixing type in a ratio of 30-150 kg of the recycle seed to 1 m 3 of the solution, thereby partially decomposing the seed-added solution until the molar ratio of the solution reaches 2.0-2.4 while keeping the solution at 65°-80° C.; (2) a second precipitation step of supplying the resulting sodium aluminate solution in a slurry state from the first precipitation step to at most three precipitation tanks of growth type arranged in series and decomposing the solution in the slurry state until the molar ratio reaches at least 2.6 while keeping the solution in the slurry state at a precipitated solid aluminum hydroxide concentration of 400-1,500 g/l and at a slurry temperature of 45°-65° C. in the precipitation tanks of growth type; and (3) a third step of supplying the decomposed solution in a slurry state from the second precipitation step to a classifier, thereby classifying the precipitated aluminum hydroxide grains into coarse grains of aluminum hydroxide as product and fine grains of aluminum hydroxide, and recycling the fine grains of aluminum hydroxide as seed.
Claim 3
Dependent Claim
157 words
The process according to claim 1, wherein in the first precipitation step the supersaturated sodium aluminate solution to the first precipitation step is divided into two streams of sodium aluminate solution, one of the streams is admixed with a portion of the recycle seed aluminum hydroxide and partially decomposed until the molar ratio becomes more than 1.8 but less than the set molar ratio for the first precipitation step, thereby precipitating aluminum hydroxide, and then the partially decomposed sodium aluminate solution in a slurry state is admixed with the other stream of sodium aluminate solution, which has been cooled to a temperature low enough to lower the temperature of the partially decomposed stream of sodium aluminate solution in a slurry state at least by 3° C., and the remaining portion of recycle seed aluminum hydroxide, thereby precipitating aluminum hydroxide until the molar ratio of the admixed slurry reaches the set molar ratio of the first precipitation step.
Claim 4
Dependent Claim
20 words
The process according to claim 1, wherein the recycle seed having an average particle size of 50-90 μm is used.