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On the AlF/sub 3/ and temperature control of an aluminum electrolysis cell

机译:AlF / sub 3 /与铝电解槽的温度控制

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摘要

We propose a control strategy for excess AlF/sub 3/ and bath temperature of a prebake aluminum electrolysis cell based on analyses of measured data and studies of a simple dynamic model. Model validation indicates that there are dynamics that the model does not capture, and hence, we use real data of excess AlF/sub 3/ and bath temperature to estimate AlF/sub 3/ and energy disturbances, respectively. The estimation results show that the energy disturbance is the dominating disturbance. Hence, the proposed control strategy is based on an almost constant AlF/sub 3/ input close to average consumption and energy manipulations to compensate for the disturbances. This requires the possibility for the resistance reference to be reduced without decreasing the current efficiency. Compared to present control strategies, this introduces an additional degree of freedom in the controller. The proposed control strategy may imply a significant economic potential through increased and stabilized current efficiency, reduced and stabilized energy consumption, reduced consumption of expensive additives, and prolongation of cell life.
机译:我们基于对测量数据的分析和对简单动态模型的研究,提出了一种预铝电解槽的过量AlF / sub 3 /和浴温的控制策略。模型验证表明存在模型无法捕获的动力学,因此,我们使用过量AlF / sub 3 /和熔池温度的真实数据分别估计AlF / sub 3 /和能量扰动。估计结果表明,能量扰动是主要扰动。因此,所提出的控制策略基于接近平均消耗和能量操纵以补偿干扰的几乎恒定的AlF / sub 3 /输入。这要求在不降低电流效率的情况下减小电阻参考的可能性。与当前的控制策略相比,这在控制器中引入了额外的自由度。通过提高和稳定电流效率,减少和稳定能源消耗,减少昂贵添加剂的消耗以及延长电池寿命,提出的控制策略可能暗示着巨大的经济潜力。

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