炼钢

• 转炉及电炉冶炼 •    下一篇

转炉底吹工艺水模试验与工业应用

颜慧成1, 丁剑1, 王现周1, 史进强1, 何顺生2, 唐笑宇2   

  1. (河钢集团邯钢公司1.技术中心,2.邯宝炼钢厂,河北邯郸056015)
  • 接受日期:1900-01-01 出版日期:2020-04-05

Water modeling study and industrial application of bottom blowing technology in 260t converter

  • Accepted:1900-01-01 Online:2020-04-05

摘要: 通过建立260t转炉1:10水力学试验模型,研究了底吹气流量、底吹砖数量、分布位置等参数对混匀时间的影响,分析了不同底吹条件下熔池流场的典型特征。结果表明:提高底吹砖总气量能显著减少混匀时间;总气量12L/min条件下,在熔池底部0.6R时, 12块砖混匀时间最长;选择采用8块底吹砖后,底吹砖寿命达到了5000炉左右,能稳定控制[%C]•[%O]≤0.0024,炉役平均碳氧积0.0020;熔池流场呈现明显环流趋势,底吹气量过大时熔池出现振荡现象。

关键词: 转炉底吹, 水模拟, 混匀时间, 碳氧积, 工业应用

Abstract: A 1:10 water model for a 260 t converter has been established and the effect of bottom-blowing gas flow rate, the quantity and position of bottom nozzles on bath mixing time has been investigated. The typical feature of flow field in the bath has been observed under differentbottom blowing condition. The results show that mixing time of converter bath reduces with the increase of bottom blowing gas flow rate. When total flow rate is 12 L/min, mixing time is longest with twelve bottomblowing nozzles at 0.6R position. When eight nozzlesis used, the life of nozzles reaches 5000 heats,[%C]•[%O] is smaller than 0.0024, and the mean value is 0.0020 in the converter campaign.Flow field in bath shows a circulation from the center to the wallof converter. Vibration of bath appears when bottom blowing gas flow rate exceeds the critical value.