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150t復吹轉爐熔池傳質及合適的底吹氣量

Mass Transfer and Optimal Bottom Blown Gas Amount in 150 t Top-Bottom Converter Bath

  • 摘要: 通過水模型實驗研究了復吹轉爐中頂吹、底吹及熔池產生的CO氣流對熔池的攪拌作用。按正交實驗設計法,由實驗得出吹煉中期和后期影響熔池內傳質的主要因素及合適的頂吹和底吹氣量。在高速脫碳期,頂吹和底吹氣流的攪拌作用與CO氣流的相比可忽略不計;在脫碳后期,底吹氣流對熔池的攪拌起主要作用。在吹煉后期,底吹氣量為5Nm3/h時可達到最佳的攪拌效果。根據水模型實驗結果,回歸整理出混勻時間和容量傳質系數的準數方程。

     

    Abstract: By hydrodynamic model experiments, the effect of topblown gas, bottom blown gas and CO gas on bath stirring in 150 t top-bottom converter were studicdt According to method of orthogonal experiment design, the essetial factors and optimal amount of top and bottom gas were found. At high carbon range, compared with the stirring by CO, the stirring by top and bottom blown gas could be neglected; at low carbon range, the stirring by bottom blown gas was the main factor. The optimal gas amound was about 5 Nm3/h. The equations of mixture time and rate constant of mass transfer were established.

     

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