现代微型装置单流中间包熔体对流运动的数学建模,同时提供精炼效果

A. Verzilov, A. Smirnov, S. Semiryagin, A. Semenko, U. A. Smirnov, U. U. Kulish, Scientific, Manufacturing Enterprise Dneproenergostal
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引用次数: 0

摘要

数学建模解决了现代冶金微型装置中单流中间包熔体对流运动的建模问题。为了从精炼效果的角度对金属接收器设计进行比较评价,在建立的中间包对流流动模型中加入了模拟非金属夹杂物运动的元素。非金属夹杂物的数量、大小和密度作为初始数据。中间包液浴中非金属夹杂物的引入通过保护管直接进入金属的传入部分。非金属夹杂物的数量为120个单位。非金属夹杂物的主要尺寸:25 μm - 30单位、50 μm - 30单位、100 μm - 30单位、150 μm - 30单位。结果表明,采用侧壁斜向中间包最近窄壁且无板的金属接收器可获得最大的精炼效果。这种设计特点和安装方法为非金属夹杂物的出现提供了一种合理的循环流动轨迹。尽管如此,在作者看来,最佳的设计是在中间包最近的窄壁方向设计斜面侧壁的金属接收器,中间包有板。它有去除夹杂物效率的第二个指标,在87.5%的水平,但使用它时中间包内的流动性质更理想。这是由于从接收器金属流出的气流部分被其结构突出物-板所熄灭,这对中间包最近的窄壁衬里的影响较小。此外,通过将接收器金属板的高度降低到20 - 30毫米的范围,可以将非金属夹杂物的去除效率提高90%以上。在同时使用金属接收器和阈值时,为液体浴顶部的金属流的普遍运动创造了有利条件。这为覆盖渣中非金属夹杂物的出现和同化提供了有利条件。研究发现,阈值的优选位置是玻璃点胶机轴线与钢包从玻璃点胶机侧面落下的射流轴线之间距离的约1/3处。通过阈值和金属接收器的相互布置,中间包中夹杂物的去除效率为97.5%。这个数字是所有研究选项的最大值。
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Mathematical Modeling of the Motion of Convective Flows of the Melt in a Single- Flow Tundish of a Modern Micro-Plant While Providing a Refining Effect
Mathematical modeling solved the problem of modeling the motion of convective flows of the melt in single-flow tundish used in modern metallurgical micro-plants.For comparative evaluation of metal receiver designs from the point of view of the refining effect, an element simulating the motion of non-metallic inclusions was added to the developed model of convective flow in the tundish. The number, size, and density of non-metallic inclusions were set as the initial data. The introduction of non-metallic inclusions in the liquid bath of the tundish was carried out through a protective tube directly into the incoming portions of the metal. The number of non-metallic inclusions was 120 units. The main dimensions of non-metallic inclusions: 25 μm – 30 units, 50 μm – 30 units, 100 μm – 30 units, 150 μm – 30 units. It is established that the maximum refining effect is achieved when using a metal receiver with beveled side walls towards the nearest narrow wall of the tundish and which has no board. Such design features and method of installation provide a rational for the emergence of non-metallic inclusions trajectory of circulating flows. Despite this, the optimal in the opinion of the authors is the design of the metal receiver with beveled side walls in the direction of the nearest narrow wall of the tundish which has a board. It has a second indicator of the efficiency of removal of inclusions at the level of 87.5 %, but the nature of the flow in the tundish when using it is more optimal. This is due to the fact that the flows coming out of the metal of the receiver are partially extinguished by its structural protrusion - the board, which provides less impact on the lining of the nearest narrow wall of the tundish. Also, by reducing the height of the metal board of the receiver to the range of 20 - 30 mm, it is possible to increase the efficiency of removal of non-metallic inclusions by more than 90%. At simultaneous use of the metal receiver and a threshold favorable conditions for the prevailing movement of streams of metal in the top part of a liquid bath are created. Due to this, favorable conditions are provided for the emergence and assimilation of non-metallic inclusions by cover slag. It is found that the preferred location of the threshold is a distance of approximately 1/3 of the distance between the axis of the glass-dispenser and the axis of the jet falling from the steel ladle from the side of the glass-dispenser. With this mutual arrangement of the threshold and the metal receiver, the efficiency of removal of inclusions from the tundish is 97.5 %. This figure is the maximum for all studied options.
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