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首页> 外文期刊>Light Metals >CFD MODELLING OF ALUMINA MIXING IN ALUMINIUM REDUCTION CELLS
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CFD MODELLING OF ALUMINA MIXING IN ALUMINIUM REDUCTION CELLS

机译:铝还原电池中铝混合的CFD模拟

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摘要

Aluminium reduction cells have been continuously improved tornreduce energy consumption and increase metal production rates.rnOne method of reducing energy consumption is to operate the cellrnat low anode-cathode distances (ACDs). Line currents have beenrnincreased to increase production rates, which often requires largerrnanodes to maintain an acceptable current density. These changesrnmay have a significant impact on aspects of cell performance suchrnas bath flow and alumina mixing.rnIn previous work, a computational fluid dynamics (CFD) model ofrnbath hydrodynamics in an aluminium reduction cell has beenrndeveloped and validated using water model data. In the presentrnwork, the CFD model has been extended to study the effect ofrnACD and side channel width on bath flow and alumina mixing inrna typical full-scale industrial cell.
机译:铝还原电池一直在不断改进,以减少能耗并提高金属生产率。一种降低能耗的方法是在低阳极-阴极距离(ACD)下运行电池。线电流已增加,以提高生产率,这通常需要较大的阳极才能保持可接受的电流密度。这些变化可能会对电池性能产生重大影响,例如浴液流动和氧化铝混合。在以前的工作中,已经开发了铝还原电池中浴液动力学的计算流体动力学(CFD)模型,并使用水模型数据进行了验证。在目前的工作中,CFD模型已经扩展到研究rnACD和侧通道宽度对典型的全尺寸工业电解池中的熔池流量和氧化铝混合的影响。

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