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Production of aluminum raffinate using a three-layer oven for electrolytic refinement, comprises flowing direct current from an anode in the direction of a cathode, and depositing the aluminum raffinate in the aluminum raffinate layer
Production of aluminum raffinate using a three-layer oven for electrolytic refinement, comprises flowing direct current from an anode in the direction of a cathode, and depositing the aluminum raffinate in the aluminum raffinate layer
The production of an aluminum raffinate using a three-layer oven for electrolytic refinement (3), which comprises a cathode (1) and an anode (2), comprises flowing a direct current (I) from the anode in the direction of the cathode during the supplying of an aluminum raw material to an anodic parent alloy melting layer, and depositing the aluminum raffinate in an aluminum raffinate layer (B1). The electrolytic refinement forms the aluminum raffinate, a refining electrolysis bath layer (B2) and the melting layer between the cathode and the anode. The production of an aluminum raffinate using a three-layer oven for electrolytic refinement (3), which comprises a cathode (1) and an anode (2), comprises flowing a direct current (I) from the anode in the direction of the cathode during the supplying of an aluminum raw material to an anodic parent alloy melting layer, and depositing the aluminum raffinate in an aluminum raffinate layer (B1). The electrolytic refinement forms the aluminum raffinate, a refining electrolysis bath layer (B2) and the melting layer between the cathode and the anode. The cathode comprises a graphite material having an iron content of 0.15 wt.% or less and a pore area ratio of 20% or less. The direct current flows with a density of 3-4 A/cm 2per unit area of the cathode. The layers are present in molten state at a temperature of 750-800 [deg]C.
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机译:使用用于电解精制的三层烘箱(3)来生产萃余酸铝,其包括阴极(1)和阳极(2),包括使来自阳极的直流电(I)沿阴极方向流动在将铝原料供给至阳极母合金熔融层的过程中,将萃余液铝沉积在萃余液铝层(B1)中。电解精制形成萃余铝,精制电解浴层(B2)和阴极与阳极之间的熔融层。使用用于电解精制的三层烘箱(3)来生产萃余酸铝,其包括阴极(1)和阳极(2),包括使来自阳极的直流电(I)沿阴极方向流动在将铝原料供给至阳极母合金熔融层的过程中,将萃余液铝沉积在萃余液铝层(B1)中。电解精制形成萃余液铝,精制电解浴层(B2)和阴极与阳极之间的熔融层。阴极包括铁含量为0.15重量%以下且孔面积比为20%以下的石墨材料。直流电流以每单位阴极面积3-4 A / cm 2>的密度流动。这些层以熔融状态在750-800℃的温度下存在。
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