Method for recovering alumina from aluminium base nickel-contained waste slag
A technology of alumina and nickel waste slag, which is applied in the preparation of alkali metal aluminate/alumina/aluminum hydroxide, preparation of alumina/hydroxide, and removal of solid waste, which can solve problems such as environmental pollution and waste. Achieve benefits to the environment, short production cycle, significant economic and social benefits
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Embodiment 1
[0024] The method for reclaiming aluminum oxide from aluminum-based nickel-containing waste slag of the present invention is carried out according to the following steps successively:
[0025] (1) Batching sintering: the alumina-based nickel-containing catalyst waste residue is mixed with circulating liquid caustic soda, 30% NaOH solution and Na 2 CO 3 After batching, enter the ball mill for mixing and grinding, and the proportion control [Na 2 O] / {[Al 2 o 3 ]+[SiO 2 〕} The molar ratio is 1.05, the moisture content of the slurry is 42%, the fineness is <2mm, the temperature is 47±2°C, the slurry is calcined in a rotary kiln, the calcining temperature is 1200°C±60°C, and the time is 30 minutes.
[0026] (2) Dissolution of alkaline adjustment solution and solid-liquid separation: Stir and dissolve the clinker adjustment solution in a slurryer to form a crude sodium aluminate solution, the temperature of the dissolution adjustment solution is 75±5°C, Al 2 o 3 12g / l, Na 2 ...
Embodiment 2
[0029] The method for reclaiming aluminum oxide from aluminum-based nickel-containing waste slag of the present invention is carried out according to the following steps successively:
[0030] (1) Batching sintering: combine alumina-based nickel-containing catalyst waste residue with circulating liquid caustic soda, 35% NaOH solution and Na 2 CO 3 After batching, enter the ball mill for mixing and grinding, and the proportion control [Na 2 O] / {[Al 2 o 3 ]+[SiO 2 〕} The molar ratio is 1.15, the moisture content of the slurry is 48%, the fineness is less than 2mm, the temperature is 40±2°C, the slurry is calcined in a rotary kiln, the calcination temperature is 1150°C±50°C, and the time is 45 minutes.
[0031] (2) Dissolution of alkaline adjustment solution and solid-liquid separation: Stir and dissolve the clinker adjustment solution in a slurryer to form a crude sodium aluminate solution, the temperature of the dissolution adjustment solution is 76±6°C, Al 2 o 3 14g / l, ...
Embodiment 3
[0034] The method for reclaiming aluminum oxide from aluminum-based nickel-containing waste slag of the present invention is carried out according to the following steps successively:
[0035] (1) Batching sintering: combine alumina-based nickel-containing catalyst waste residue with circulating liquid caustic soda, 50% NaOH solution and Na 2 CO 3 After batching, enter the ball mill for mixing and grinding, and the proportion control [Na 2 O] / {[Al 2 o 3 ]+[SiO 2 〕} The molar ratio is 1.12, the moisture content of the slurry is 40%, the fineness is less than 2mm, and the temperature is 36±2°C. The slurry is calcined in a rotary kiln at a temperature of 1240°C±60°C for 30 minutes.
[0036] (2) Dissolution of alkaline adjusting solution and solid-liquid separation: Stir and dissolve the clinker using adjusting solution in a slurryer to form a crude sodium aluminate solution. The temperature of the adjusting solution is 80±5°C. 2 o 3 15g / l, Na 2O 132g / l, prepared with NaOH...
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