Method for recycling crystalline alkali in unrefined solution full confluence production by sintering process
A technology of sintering method and crystallization alkali, applied in the direction of alumina/aluminum hydroxide, etc., can solve the problems of increased energy consumption and increased labor intensity
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Embodiment 1
[0011] The liquid-solid ratio of primary washing liquid and crystallization alkali completely dissolved is 10:1m 3 / t, once washing liquid dissolves the crystallization alkali temperature 50 ℃, decrystallization alkali time, 10min solution composition Na 2 o C 25.50g / l;
Embodiment 2
[0013] The liquid-solid ratio of primary washing liquid and crystallization alkali completely dissolved is 10:1m 3 / t, the temperature of the crystallization alkali dissolved in the primary wash solution is 70°C, the time of the crystallization alkali solution, and the solution component Na is 10min 2 o C 32.6g / l;
Embodiment 3
[0015] The liquid-solid ratio of primary washing liquid and crystallization alkali completely dissolved is 2:1m 3 / t, once washing liquid dissolves the crystallization alkali temperature 50 ℃, decrystallization alkali time, 10min solution composition Na 2 o C 106.1g / l;
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