炼钢 ›› 2019, Vol. 35 ›› Issue (4): 12-18.

• 转炉及电炉冶炼 • 上一篇    下一篇

底枪支数和布置对复吹转炉熔池混匀的影响

周泉林 ,杨晓江1,张 全1,孙建月2,3,杜文斌2,3,季伟烨2,3,钟良才2,3   

  1. (1. 河钢乐亭钢铁有限公司,河北 唐山063016; 2. 东北大学 冶金学院,辽宁 沈阳 110004; 3. 东北大学 多金属共生矿生态化冶金教育部重点实验室,辽宁 沈阳 110004)
  • 接受日期:1900-01-01 出版日期:2019-08-05

Influence of number and arrangement of bottom tuyeres on bath mixing in a combination blown converter

  • Accepted:1900-01-01 Online:2019-08-05

摘要: 在200 t复吹转炉的1:12缩小模型进行了物理模拟试验,研究了4~12支底枪不同的布置方案对复吹转炉熔池混匀的影响。复吹条件下,在所研究的气体流量范围,4支底枪不同布置方案的混匀时间变化范围较大,混匀时间在20~49 s;6支底枪不同布置方案的混匀时间在18~42 s;而8~12支底枪不同布置方案的混匀时间在14~38 s;4,6,8,10,12支底枪的混匀时间小于27 s的底枪布置方案占对应试验总布置方案的比例分别为14 %、13 %、33 %、44 %、67 %,有较多的8~12支底枪布置方案的混匀时间小于27 s,在转炉冶炼的一个炉役内可供吹炼选择的底枪布置方案较多。当底枪支数由4支增加到8支,不同底吹方案的混匀时间平均值下降较为明显,当底枪支数由8支增加到12支,对于0.57 m3/h的底吹气体流量,混匀时间平均值有所降低,而底吹气量为2.29 m3/h时,混匀时间平均值变化不大。

关键词: 复吹转炉, 底枪支数, 底枪布置, 熔池混匀时间, 物理模拟

Abstract: Influence of different arrangement of 4–12 bottom tuyeres of a 200 t top and bottom combination blown converter on its bath mixing was investigated in an 1:12 model with physical modeling experiment. Under the condition of combined blowing and the gas flowrates used in this work, the variation range of bath mixing time with different arrangements of 4 bottom tuyeres is large, being 20–49 s, the bath mixing time with different arrangements of 6 bottom tuyeres is 18–42 s, while that with different arrangements of 8–12 bottom tuyeres is 14–38 s. The ratios of bottom tuyere cases with mixing time smaller than 27 s to the corresponding total cases studied were 14 %, 13 %, 33 %, 39 % and 67 %, respectively. This means that 8–12 bottom tuyeres have more bottom tuyere arrangement cases with mixing time smaller than 27 s and these cases can be chosen for combined blowing during a converter campaign. The average values of bath mixing time of different cases at a certain number of bottom tuyeres decrease apparently when the bottom tuyeres increase from 4 to 8. As the bottom tuyeres increase from 8 to 12, the average values decrease a little for the bottom gas flowrtae of 0.57 m3/h, while the average values hardly vary for the bottom gas flowrtae of 2.29 m3/h.

Key words: combination blown converter, number of bottom tuyeres, arrangement of bottom tuyeres, bath mixing time, physical modeling