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Numerical simulation on electrolyte flow field in 156 kA drained aluminum reduction cells

机译:156 kA排水铝还原池中电解质流场的数值模拟。

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Based on the commercial CFD software CFX-4.3, two-phase flow of electrolyte in 156 kA drained aluminum reduction cells with a new structure was numerically simulated by multi-fluid model and k-ε turbulence model. The results show that the electrolyte flow in the drained cells is more even than in the conventional cells. Corresponding to center point feeding, the electrolyte flow in the drained cells is more advantageous to the release of anode gas, the dissolution and diffusion of alumina, and the gradient reduction of the electrolyte density and temperature. The average velocity of the electrolyte is 8.3 cm/s, and the maximum velocity is 59.5 cm/s. The average and maximum velocities of the gas are 23.2 cm/s and 61.1 cm/s, respectively. The cathode drained slope and anode cathode distance have certain effects on the electrolyte flow.
机译:基于商用CFD软件CFX-4.3,利用多流体模型和k-ε湍流模型对具有新结构的156 kA排水型铝还原池中电解质的两相流动进行了数值模拟。结果表明,与常规电池相比,排干电池中的电解液流动更均匀。对应于中心点进料,排干的电池中的电解质流更有利于阳极气体的释放,氧化铝的溶解和扩散以及电解质密度和温度的梯度降低。电解液的平均速度为8.3 cm / s,最大速度为59.5 cm / s。气体的平均速度和最大速度分别为23.2 cm / s和61.1 cm / s。阴极的排出斜率和阳极的阴极距离对电解液的流量有一定的影响。

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