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Discussion About Model of Residual Time Distribution for Tundish

机译:关于中间包剩余时间分配模型的讨论

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Tundish metallurgy is critical in continuous casting process, and it has much to do with the clean steel technology. And the most effective and convenient way to evaluate the tundish designing or tundish metallurgy is to calculate different regions' volume fraction in the tundish, such as plug flow region, backmix flow region, bypass flow region and dead region. Till now this can only be solved through some calculation models based on the analysis of residual time distribution (RTD) curve, and RTD is referred from chemical reaction engineering. But RTD is far away from metallurgy field because complicated mathematical calculation and analysis are covered. Few metallurgists do further research about its applicability and correctness since modified mixed model and combined model are proposed and widely used in tundish metallurgy. In this paper, the short-coming of these two calculation models are pointed out and explained. Then it finds to irrationally define the dead region's volume fraction equals to 1-θav, the reason is that this equation doesn't definitely describe the definition of dead region, which is defined the region where tracers spend more than twice mean residual time, so this equation does not characterize the property of dead region. In some case, minus value of the dead region's volume fraction are obtained if this equation is adopted;and it is also not reasonable to define plug flow's volume fraction equals to 1/2(θmin + θmax) or θmin, because θmin is also influenced by backmix flow. Even when θmin and θmax have the same value, the plug flow volume fraction is different according to variance σ2. Then in this paper, these two models are further proved based on mathematical simulation, it suggests to calculate the different regions' volume fraction in tundish inadequately through the present models available, and to trustless use the results to guide the tundish designing and tundish metallurgy process. At last it suggests that another new calculation model should be attempted to calculate the different regions' volume fraction in the tundish.
机译:中间包冶金在连铸过程中至关重要,它与清洁钢技术有很大关系。评估中间包设计或中间包冶金的最有效,最方便的方法是计算中间包中不同区域的体积分数,例如塞流区,回混流区,旁通流区和死区。到目前为止,这只能通过基于剩余时间分布(RTD)曲线分析的一些计算模型来解决,而RTD则来自化学反应工程。但是RTD距离冶金领域很远,因为它涵盖了复杂的数学计算和分析。自从提出了改进的混合模型和组合模型并在中间包冶金中广泛使用以来,很少有冶金学家对它的适用性和正确性进行进一步的研究。本文指出并解释了这两种计算模型的缺点。然后发现非理性地定义了死区的体积分数等于1-θav,原因是该方程式并未明确描述死区的定义,死区的定义是示踪剂花费了两倍多的平均剩余时间,因此该方程式没有描述死区的特性。在某些情况下,如果采用此方程式,则会获得死区体积分数的负值;并且定义塞流的体积分数等于1/2(θmin+θmax)或θmin也是不合理的,因为θmin也会受到影响通过返混流。即使当θmin和θmax具有相同值时,柱塞流体积分数也根据方差σ2而不同。然后本文在数学模拟的基础上进一步证明了这两个模型,建议通过现有模型不足地计算出中间包中不同区域的体积分数,并以不可信的结果指导中间包设计和中间包冶金工艺。最后,建议尝试使用另一个新的计算模型来计算中间包中不同区域的体积分数。

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