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Effect of electromagnetic forces on flow of slag at the surface of a consumable electrode in the electroslag process

机译:电磁力对电渣过程中可消耗电极表面的渣流的影响

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According to the results of experimental investigations, a specific contour of the flow of the slag melt is established in the slag pool in the quasi-stationary electroslag process. For example, when remelting a circular aluminium electrode in a quartz cylinder, positioned on a graphite base (slag is a transparent eutectic mixture KCl +LiCl), a circular flow directed downwards below the electrode and upwards along the solidification mould walls was observed. The possibility of this flow is also confirmed by theoretical analysis carried out in Ref. 2. This case corresponds to the condition rot f_e<0 (f_e is the density of the electromagnetic force). Cases of the opposite direction of the flow of the slag in the vicinity of the electrode are well known. For example, a circular flow of the slag melt was recorded in a current-conducting solidification mould made of a corrosion-resisting steel with a transparent wall. In this case, the flow of the electrolyte in the central part is directed from the metallic bath to the electrode. In Ref. 4, this discrepancy is explained by the fact that in the first case experiments were carried out with a solidification mould with no electrical conductivity, whereas an electrically conducting mould was used in the second case. The variation of the path of passage of current results in a change in the direction of flow of the slag. In these and other similar investigations, the problem of physical reasons for a specific direction of rotation of the slag has not been investigated. On the other hand, the distribution of the electromagnetic forces affect he field of velocities of the slag melt and, in particular, determines the conditions of formation of the field of velocities in the film of metal and the droplet flowing downwards. The hydrodynamic structure of the droplet affects the shape of the solidification front.
机译:根据实验研究的结果,在准静态电渣过程中,在渣池中建立了熔渣流的特定轮廓。例如,当将圆形铝电极在石英圆柱体上重熔时,石英圆柱体位于石墨基底上(炉渣是透明的低共熔混合物KCl + LiCl),观察到的是向下流向电极下方并沿凝固模具壁向上的环形流。参考文献中进行的理论分析也证实了这种流动的可能性。 2.这种情况对应于条件rot f_e <0(f_e是电磁力的密度)。在电极附近,炉渣的流动方向相反的情况是众所周知的。例如,在由具有透明壁的耐腐蚀钢制成的导电凝固模具中记录了熔渣的循环流动。在这种情况下,电解质在中央部分的流动从金属浴流向电极。在参考文献中在图4中,这种差异可以由以下事实解释:在第一种情况下,实验是使用没有导电性的凝固模具进行的,而在第二种情况下,则使用导电模具。电流通过路径的变化导致炉渣流动方向的变化。在这些和其他类似的研究中,尚未研究炉渣特定旋转方向的物理原因问题。另一方面,电磁力的分布影响炉渣熔体的速度场,并且特别地确定金属膜和向下流动的液滴中的速度场的形成条件。液滴的流体动力学结构会影响凝固前沿的形状。

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