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›› 2011, Vol. 11 ›› Issue (1): 40-43.

• 流动与传递 • 上一篇    下一篇

侧顶复吹条件下AOD转炉熔池内流体流动的数学模拟:模型对侧顶复吹过程的应用及结果

魏季和 贺元 史国敏   

  1. 上海大学材料科学与工程学院 上海大学材料科学与工程学院 宝钢集团上海第一钢铁有限公司
  • 收稿日期:2011-03-07 修回日期:1900-01-01 出版日期:2011-02-20 发布日期:2011-02-20
  • 通讯作者: 魏季和

Mathematical Modeling of Fluid Flow in an AOD Converter Bath under Conditions of Combined Side and Top Blowing: Application of the Model to Combined Side and Top Blowing Process and Results

WEI Ji-he HE Yuan SHI Guo-min   

  1. College of Materials Science and Engineering, Shanghai University College of Materials Science and Engineering, Shanghai University Baosteel Group Shanghai No.1 Iron & Steel Corp.
  • Received:2011-03-07 Revised:1900-01-01 Online:2011-02-20 Published:2011-02-20
  • Contact: WEI Ji-he

摘要: 由提出的侧顶复吹条件下AOD熔池内钢液流动三维数学模型的侧吹和顶吹分量对纯侧吹和纯顶吹下熔池内流体流动计算结果的叠加,处理和分析了复吹过程中120 t AOD转炉及线尺寸为其1/4的水模型熔池内流体的流动. 所得结果显示,该数学模型可用以模拟复吹AOD熔池内流体流动. 侧吹气流对复吹AOD熔池内流体流动起主导作用,整个熔池液体同样处于活泼的搅拌和循环运动中,无明显的死区. 与纯侧吹下的情况相比,顶吹气流并未改变熔池内气体搅拌和液体流动的基本特征,但会使液体局部流态显著变化. 侧枪数和枪位的变化同样未改变熔池内气体搅拌和液体流动及液相湍动能分布的基本特征和规律,但会使之发生局部改变. 采用6枪27°比采用7枪18°或22.5°和6枪22.5°可得更均匀的液体流场及湍动能分布.

关键词: 不锈钢, AOD转炉, 侧顶复吹过程, 流体流动, 数学模拟

Abstract: The fluid flows in the bath of a 120 t AOD converter and its water model with a 1/4 linear scale in the combined side and top blowing have been treated and analyzed from the superposition of the computed results of those during the simple side and top blowing processes respectively by the side and top blowing components of the mathematical model developed for the molten steel flow in an AOD bath under the conditions of combined blowing. The results demonstrate that the mathematical model can be used to simulate the fluid flow in an AOD bath with the combined blowing. The liquid flow in the bath with the combined blowing results from the gas side blowing streams under the influence of a gas top blowing jet, the gas side streams play a governing role for it, and the liquid is equally in vigorous stirring and circulatory motion during the combined blowing also without obvious dead zone in the whole bath. Compared with those in a simple side blowing, the impinging of a gas top blowing jet does not change the essential features of gas agitation and fluid flow in the bath, but can make the local flow pattern of the liquid vary evidently. The changes in the angle between each tuyere and the tuyere number have similarly not altered the basic characteristics and patterns of gas stirring and liquid flow and turbulent kinetic energy distribution in the bath. However, at a given tuyere number and gas side blowing rate or a given angular separation between each tuyere and gas side blowing rate, the variation of the number or the angle can change locally them. Using 6 tuyeres with 27° for blowing can reach more uniform flow field and turbulent energy distribution of the liquid in the AOD bath with the combined blowing than that taking 7 tuyeres with 18° or 22.5° and 6 tuyeres with 22.5°.

Key words: stainless steel, AOD refining, combined side and top blowing, fluid flow, mathematical modeling

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