Leaching method for valuable elements in quadratic aluminum dust
A valuable element, secondary aluminum technology, applied in the field of comprehensive utilization of waste aluminum ash, can solve the problems of simple recovery method, cannot be recycled, not recycled, etc., achieves high leaching rate, realizes recycling, and reduces pollution.
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Embodiment 1
[0017] A method for leaching valuable elements in secondary aluminum ash, comprising the following steps:
[0018] (100) adding secondary aluminum ash to NaOH solution, and adding 12 g of secondary aluminum ash to every 100 ml of NaOH solution to form a mixture; wherein, the concentration of the NaOH solution is 1.5 mol / L;
[0019] (200) adding the above-mentioned mixture into a ball mill, and milling for 3-3.5 hours; wherein, the temperature during the ball milling is 80° C., the milling time is preferably 3 hours, and the ball milling speed of the ball mill is 125 r / min;
[0020] (300) Suction filtration, drying the filter residue in a vacuum drying oven to obtain reusable aluminum ash powder, the drying temperature is 110°C.
[0021] The valuable elements are Na, K, Cl and Si, and the leaching rates of the valuable elements Na, K, Cl and Si are: 83.6%, 78.3%, 97.4%, and 55.7%, respectively.
Embodiment 2
[0023] A method for leaching valuable elements in secondary aluminum ash, comprising the following steps:
[0024] (100) Add secondary aluminum ash to NaOH solution, and add 12.5 g of secondary aluminum ash to every 100 ml of NaOH solution to form a mixture; wherein, the concentration of the NaOH solution is 1.5 mol / L;
[0025] (200) adding the above-mentioned mixture into a ball mill, and milling for 3-3.5 hours; wherein, the temperature during the ball milling is 75° C., the milling time is preferably 3 hours, and the ball milling speed of the ball mill is 150 r / min;
[0026] (300) Suction filtration, drying the filter residue in a vacuum drying oven to obtain reusable aluminum ash powder, the drying temperature is 105°C.
[0027] The valuable elements are Na, K, Cl and Si, and the leaching rates of the valuable elements Na, K, Cl and Si are: 85.4%, 79.6%, 93.9%, and 55.7%, respectively.
Embodiment 3
[0029] A method for leaching valuable elements in secondary aluminum ash, comprising the following steps:
[0030] (100) Add secondary aluminum ash to NaOH solution, and add 11.5 g of secondary aluminum ash to every 100 ml of NaOH solution to form a mixture; wherein, the concentration of the NaOH solution is 1.5 mol / L;
[0031] (200) adding the above-mentioned mixture into a ball mill, and milling for 3-3.5 hours; wherein, the temperature during the ball milling is 77°C, the milling time is preferably 3 hours, and the ball milling speed of the ball mill is 135r / min;
[0032] (300) Suction filtration, drying the filter residue in a vacuum drying oven to obtain reusable aluminum ash powder, the drying temperature is 115°C.
[0033] The valuable elements are Na, K, Cl and Si, and the leaching rates of the valuable elements Na, K, Cl and Si are: 86.7%, 79.2%, 96.5%, and 55.7%, respectively.
[0034] The invention discloses a method for leaching valuable elements in secondary alum...
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