Method for producing aluminum-Me intermediate alloy by one-step electrolysis method
A technology of master alloy and electrolytic method, which is applied in the field of production of aluminum master alloy, can solve problems such as difficulties, difficulty in reducing products, secondary pollution, etc., and achieve the effects of improving resource utilization, reducing production costs, and reducing emissions
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Embodiment 1
[0012] Embodiment 1: produce Al-10%Si alloy, the raw material ratio that adds in existing aluminum electrolyzer is:
[0013] Cheap metal oxides that can be reduced by aluminum A: bauxite (weight ratio content of ingredients: Al 2 o 3 80%, SiO 2 15%, Fe 2 o 3 5%);
[0014] Metal oxide B: SiO 2 (the weight ratio content of composition: SiO 2 95%, Fe 2 o 3 5%);
[0015] When opening the tank, the cheap metal oxide A that can be reduced by aluminum is 80% and the metal oxide B is 20% by weight; Metal oxide A 95%, metal oxide B 5% feed, stable production of Al-Si10%-Fe1% alloy, and the power consumption per ton of product is 16000 degrees / ton;
[0016] The present embodiment adopts self-baking anode experimental electrolyzer production, and electrolysis technical parameter is as follows:
[0017] Tank working voltage: 4.2V, electrolysis temperature: 950°C,
[0018] Pole distance: 4.0cm, Molecular ratio: 2.6,
[0019] Additives (weight ratio): calcium fluoride 3%, magne...
Embodiment 2
[0025] Embodiment 2: produce Al-10Mn-Fe alloy, the raw material ratio that adds in the electrolyzer is:
[0026] Cheap metal oxides that can be reduced by aluminum A: pyrolusite (weight ratio content of ingredients: MnO 2 75%, FeO 20%, SiO 2 5%);
[0027] Metal oxide B: electrolytic alumina;
[0028] When opening the tank, only cheap metal oxide A that can be reduced by aluminum is added. After the Mn reaches 10% in the pre-tank inspection, 10% of cheap metal oxide A that can be reduced by aluminum and 90% metal oxide B are fed in a weight ratio. Stable production of Al-Mn10%-Fe2% alloy; power consumption per ton of product is 15000 kWh / ton.
[0029] The present embodiment adopts self-baking anode experimental electrolyzer production, and electrolysis technical parameter is as follows:
[0030] Tank working voltage: 4.2V, electrolysis temperature: 980°C,
[0031] Pole distance: 4.0cm, Molecular ratio: 2.6,
[0032] Additives (weight ratio): calcium fluoride 3%, magnesium...
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