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Analysis of Plunging Pool Formation and Gas Absorption Phenomenon during Tapping

机译:攻丝过程中切入池形成及气体吸收现象分析

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摘要

Gas absorption phenomenon during tapping from converter to ladle was studied by water model experiments in water-air system. Changes of dissolved oxygen, DO in the vessels were observed by DO meter and volumetric coefficient for gas absorption rate, Ak _(O) was estimated. In addition, the amount of gas engulfment at plunging pool with the same water model was also observed and calculated with CFD method. Observed and Experimental results were in good agreement with each other when the criterion for liquid ratio was set as 0.5. Surface area of bubbles at plunging pool calculated by CFD was used to estimate mass transfer coefficient, k _(B). k _(B) in tapping and bottom bubbling experiments were discussed and linear relation between k _(B) and stirring power density was found. The Plunging pool was divided into 9 parts and velocity at bubble surface and area of bubbles in each part were calculated. It was found that the center and middle part of plunging pool was the main gas absorption region through this discussion. Bubble generation phenomenon at plunging pool in steel-air system was also calculated with the same mesh as water-air system and calculated results were compared with each other.
机译:通过水-空气系统中的水模型实验研究了转炉到钢包出钢期间的气体吸收现象。用溶解氧仪测量容器中溶解氧,溶解氧的变化,并利用气体吸收率的体积系数估算出Ak_(O)。此外,还观察了相同水模型下的跳水池中的气体吞噬量,并使用CFD方法计算。当液体比率的标准设定为0.5时,观察到的结果和实验结果彼此很好地吻合。通过CFD计算的浸入池处的气泡表面积用于估计传质系数k_(B)。讨论了拍打和底部冒泡实验中的k _(B),发现k _(B)与搅拌功率密度之间存在线性关系。将浸没池分成9个部分,并计算气泡表面的速度和每个部分的气泡面积。通过讨论发现,跳水池的中部是主要的气体吸收区域。在与水-空气系统相同的网格下,还计算了钢-空气系统浸水池中的气泡产生现象,并将计算结果进行了比较。

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