Comparison of Bottom Blowing Element Based on the Characteristics of Gas Stream and Stirring Ability in 120t Converter

Yijie Hao, Ming Lv, Fuqing Hou, Shiwu Ruan, Zhaohui Zhang, Xiangdong Xing
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Abstract

The bottom blowing element is critical for ensuring the effectiveness of top and bottom blowing in converter steelmaking process. Investigating the influence of different bottom blowing elements on the stirring properties of molten bath contributes to the optimization of the bottom blowing system. The effects of structural variations in dispersive, circular seam and straight cylinder types of bottom blowing elements on molten bath fluid dynamics, turbulent kinetic energy and multiphase flow properties of gas-slag-metal were investigated through numerical simulations. In addition, physical simulations were used to measure the mixing time of molten bath, observe changes in the flow field, and validate and analyze the results of the numerical simulations. The results show that the dispersive type element has a wider dispersion range of the flow jets, while the straight cylinder type has the smallest dispersion range. When the bottom blowing intensity is below 0.05 Nm3/t·min, the dispersive type has the longest mixing time, while the circular seam type has the shortest mixing time. Conversely, at more than 0.08 Nm3/t·min, the dispersive type shows the shortest mixing time and the straight cylinder type shows the longest. The dispersive type significantly influences the bottom flow field and disperses tracers from the interior of molten bath. The circular seam type mainly affects the middle flow field and directs tracers along the central area. The straight cylinder type, on the other hand, has a significant influence on the surface flow field and directs tracers along the pool surface.

Abstract Image

基于 120t 转炉气流特性和搅拌能力的底部吹扫元件比较
底吹元件对于确保转炉炼钢过程中顶部和底部吹炼的有效性至关重要。研究不同底吹元件对熔池搅拌特性的影响有助于优化底吹系统。通过数值模拟研究了分散型、圆缝型和直筒型底吹元件的结构变化对熔池流体动力学、湍动能和气体-熔渣-金属多相流特性的影响。此外,还利用物理模拟测量了熔池的混合时间,观察了流场的变化,并对数值模拟的结果进行了验证和分析。结果表明,分散型元件的流动射流分散范围较大,而直筒式元件的分散范围最小。当底吹强度低于 0.05 Nm3/t-min 时,分散型元件的混合时间最长,而圆缝型元件的混合时间最短。相反,当吹气强度大于 0.08 Nm3/t-min 时,分散型的混合时间最短,而直筒式的混合时间最长。分散型对底部流场的影响很大,可分散熔池内部的示踪剂。环缝型主要影响中间流场,并引导示踪剂沿中心区域流动。而直筒式则对表面流场有很大影响,并将示踪剂沿熔池表面引导。
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