摘要
进行了300t脱磷转炉水模型实验,研究了8支底吹元件下不同底吹布置方式、底吹流量大小、顶吹参数、废钢加入比及不同废钢单重对熔池混合效果的影响。研究得出,当底吹元件集中对称布置在炉底0.42D圆周上,底吹供气强度达到2.94m^3/h,氧枪的枪位控制在58~88mm之间时,熔池的混匀效果较好。通过熔池废钢加入的研究得出,当废钢比增加到lo%时,熔池混匀时间值变化非常显著,不同单重废钢对熔池的混匀规律影响相似,在顶吹流量为30000m^3/h时,对于1.5t废钢单重,达到悬浮重量须满足底吹流量不小于4010m^3/h,研究结果可为实际操作工艺参数的优化提供参考依据。
Taking water-model experiments of a 300 t dephosphorization converter, when under eight bottom blo- wing element, different bottom blowing arrangement, the size of the bottom blowing flow rate and top blowing pa- rameters on the influence of the molten pool mixing effect was studied. From the research, when the bottom blo- wing elements concentrated and symmetrically arranged in the furnace bottom of 0.42D on the circumference of a circle, the bottom blowing flow rate is 2.94m^3/h, the lance height is 58 -- 88mm, the blending effect of the mol- ten pool is best. When the scrap ratio reaches to 10%, the mixing time increases greatly, and different single scrap has similar influence on mixing time. For a 1.5 t scrap, the bottom blowing flow rate must reach to 4 010 m^3/h, the scrap can meet the suspension energy, when the top blowing flow rate is 30 000 m^3/h. The research re- sults can provide reference for optimization of practical operation parameters.
出处
《钢铁研究学报》
CAS
CSCD
北大核心
2015年第12期42-47,共6页
Journal of Iron and Steel Research
关键词
脱磷转炉
物理模拟
底吹布置
混匀时间
熔池废钢
dephosphorization converteri physical simulations bottom tuyere configuration mixing times scrap