赵立华, 马文俊, 王敏. 100t钢包吹氩精炼过程的物理模拟[J]. 工程科学学报, 2014, 36(S1): 140-144. DOI: 10.13374/j.issn1001-053x.2014.s1.026
引用本文: 赵立华, 马文俊, 王敏. 100t钢包吹氩精炼过程的物理模拟[J]. 工程科学学报, 2014, 36(S1): 140-144. DOI: 10.13374/j.issn1001-053x.2014.s1.026
ZHAO Li-hua, MA Wen-jun, WANG Min. Physical modeling of argon bottom blowing refining in a 100 t ladle[J]. Chinese Journal of Engineering, 2014, 36(S1): 140-144. DOI: 10.13374/j.issn1001-053x.2014.s1.026
Citation: ZHAO Li-hua, MA Wen-jun, WANG Min. Physical modeling of argon bottom blowing refining in a 100 t ladle[J]. Chinese Journal of Engineering, 2014, 36(S1): 140-144. DOI: 10.13374/j.issn1001-053x.2014.s1.026

100t钢包吹氩精炼过程的物理模拟

Physical modeling of argon bottom blowing refining in a 100 t ladle

  • 摘要: 针对某电炉厂在冶炼轴承钢过程中,钢包底吹精炼混匀效果和去夹杂效果不佳的问题进行了水模型研究.实验结果表明:钢包原型底吹位置由于两气柱间距离较近,在大气量下气柱产生偏移和叠加,造成钢液流场不稳定.根据实验结果建议:底吹位置应位于0.5R-0.5R-135°(R为钢包底部半径);该方案临界卷渣气量为0.24m3·h-1.

     

    Abstract: To improve the mixing effect and inclusion removing during the ladle bottom blowing refining process at an electric furnace factory,the water modeling experiment was conducted. Results show that the distance of two gas columns is too close,so stacking and shifting of the gas columns occur when the gas flow rate is large,which make the flow field of molten steel unstable. According to the results,it is proposed that the bottom blowing position should be located at 0.5R-0.5R-135°(R is the ladle bottom radius),and the critical gas flow rate for slag entrapment is 0.24 m3·h-1.

     

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