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五流中间包内钢液流动行为

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以某钢厂五流中间包为研究对象,建立了1∶2。5的中间包物理模型。通过水模拟物理实验探究了长水口插入深度、钢液位高度及堵一流对中间包内钢液行为的影响。同时,对堵流和不堵流情况下夹杂物的上浮情况进行了分析。结果表明,增加长水口插入深度可延长流体停留时间,减小死区体积。当插入深度超过94 mm后,各流停留时间变化波动较小,第二流和第三流的死区体积稳定。此外,随着钢液位增加,第一流和第三流的死区体积变化较大,出口平均死区体积均先增大后减小。当钢液位高度为314 mm或333 mm时,停留时间较长,死区体积较小。未堵流时,出口平均死区体积分数为17。6%;堵第二流时,出口平均死区体积分数增至23。15%,但夹杂物去除率提高,尤其是20 μm的夹杂物去除率提高了12。4%。综合考虑,建议实际生产中钢液位高度为中间包高度的80%~85%,实际长水口插入深度约为234 mm。另外,若出现钢水供应不足、出坯困难等现象而必须进行堵一流操作时,为保持中间包内钢液原有流动特性,建议堵第二流。
Flow behavior of liquid steel in five-strand tundish
Taking the five-strand tundish of a steel mill as the research object,the physical model of tundish of 1∶2.5 is established.The effects of different insertion depth of nozzle,liquid steel level height,and blocking one strand on the behavior of liquid steel in tundish were investigated by through water simulation physical experiments.At the same time,a reasonable analysis of inclusions in the case of blocking and non-blocking is carried out.The results show that increasing the insertion depth of nozzle can increase the retention time of internal fluid and reduce the dead zone volume.When the insertion depth of nozzle exceeds 94 mm,the fluctuation of the residence time of each flow is small,and the dead zone volume of the second and third flow is stable.In addition,with the increase of steel liquid level,the dead zone volume of the first and third strand changes greatly,and the average dead zone volume of the outlet both increases first and then decreases.When the liquid steel level height is 314 mm or 333 mm,the residence time is longer and the dead zone volume is smaller.When the outlet is not blocked,the average dead zone volume at the outlet is 17.6%;when the second strand is blocked,the average dead zone volume increases to 23.15%,but the removal rate of inclusions is increased,especially for 20 μm inclusions,the removal rate is increased by 12.4%.For comprehensive consideration,it is suggested that the liquid steel level height in actual production should be 80%-85%of the height of the tundish,and the actual insertion depth of nozzle should be about 234 mm.In addition,if there is insufficient supply of liquid steel,difficulties in billet production and other phenomena and it is necessary to block one-strand operation,it is recommended to block the second strand in order to maintain the original flow characteristics of the liquid steel in the tundish.

tundishinsertion depthliquid steel level heightinclusiondead zone volume

龚伟、吴正义、武豪、江雪婷、邓爱军

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中冶南方连铸技术工程有限责任公司,武汉 420073

安徽工业大学冶金工程学院,马鞍山 243032

中间包 插入深度 钢液位高度 夹杂物 死区体积

2024

江西冶金
江西省冶金集团公司 江西省金属学会

江西冶金

影响因子:0.117
ISSN:1006-2777
年,卷(期):2024.44(6)