基于物理模拟的180 t钢包底吹氩工艺优化研究

    Study on Process Optimization of 180 t Ladle Bottom Blowing Argon Based on Physical Simulation

    • 摘要: 针对某钢厂采用钢包双孔底吹氩模式过程中存在钢水二次氧化、搅拌能耗散大的问题,建立了该厂钢包1∶4水模型,模拟研究了单双透气砖布置方式、底吹气体流量对钢液混匀时间的影响。基于最优底吹透气砖布置方式,研究了实际工况下非对称双孔底吹气流量对混匀时间的影响;同时,利用优质真空泵油模拟钢包顶渣,对不同气体流量下钢液的裸露面积进行了比较。结果表明:双孔底吹氩模式时,底吹位置0.6 R、吹气流量为500 L/min、底吹角度为130°时混匀时间较小,混匀时间为59.8 s;单孔底吹氩模式时,底吹位置0.6 R、吹气流量为500 L/min时混匀时间较小,混匀时间70.15 s;对比单双孔吹氩模式,相同吹气流量下,双孔底吹都优于单孔底吹;非对称流量即差流量吹氩模式下,钢包混匀精炼效果明显弱于等量吹氩模式;考虑到钢液的二次氧化,在实际精炼过程中,最大底吹气流量应控制底吹气流量在500 L/min左右。

       

      Abstract: Aiming at the problems of secondary oxidation of molten steel and large dissipation of stirring energy in the process of using double-hole bottom argon blowing mode in a steel plant, a 1 ∶ 4 water model of ladle in this plant was established. The effects of single and double permeable brick arrangement and bottom blowing gas flow rate on the mixing time of molten steel were simulated. Based on the optimal arrangement of bottom blowing permeable bricks, the influence of asymmetric double-hole bottom blowing flow rate on the mixing time under actual working conditions was studied. At the same time, high-quality vacuum pump oil was used to simulate ladle top slag, and the exposed area of molten steel under different gas flow rates was compared. The results show that in the double hole bottom blowing argon mode, when the bottom blowing position is 0.6 R, the blowing flow rate is 500 L/min, and the bottom blowing angle is 130°, the mixing time is small,and the mixing time is 59.8 s. In the single hole bottom blowing argon mode, when the bottom blowing position is 0.6 R and the blowing flow rate is 500 L/min, the mixing time is small, the mixing time is 70.15 s. Compared with the single and double hole argon blowing mode, under the same blowing flow rate, the double hole bottom blowing is better than the single hole bottom blowing. The refining effect of ladle mixing in the asymmetric flow argon blowing mode is obviously weaker than that in the equal argon blowing mode. Considering the secondary oxidation of molten steel, in the actual refining process, the maximum bottom blowing flow rate should be controlled at about 500 L/min.

       

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