Mathematical model of flow characteristic in multi-strand continuous casting tundishes

In this paper, the subject of mathematical model is a series of math expressions, which is used to calculate different regions＇ volume fraction and analyze flow characterization in multi-strand tundish. But research about mathematical model for multi-strand tundish is few, and so far, there has been no acknowledged math model for multi- strand tundish to describe its flow characteristic. If Sahai＇s model, which is originally proposed for the case of single-strand tundish （proposed in reference, and this model is widely used in the world）, is applied to describe flow feature in multi-strand tundish, the calculation results would be unreasonable. Based on the data of watermodel experiment results, the sum of each strand＇s dead region＇s volume fraction is bigger than 100%, and this obviously doesn＇T agree with reality; and the value of dead region＇s volume fraction is calculated to be minus according to mathematical simulation results data in another case. What＇s more, Sahai＇s model does not propose the standard of plotting the RTD-curve, and this makes scholars around the world can＇t achieve consensus of views about plotting RTD-curve. And the model doesn＇t consider the bypass flow and can＇t calculate its volume fraction, but bypass flow is critical to tundish metallurgy. And through Sahai＇s model, the calculation result of plug flow region＇s volume fraction is also not reasonable, because the model doesn＇t well describe the essence of plug flow. So these suggest that it is not reliable to apply Sahai＇s single-strand tundish model to multi-strand tundish case. Then a new model is attempted to propose in this paper for your discussion. In the new model, the standard of plotting RTD curve is definitely proposed, and relative calculation method is also proposed; and the feature of dead region is carefully studied and the model proposes a new method to calculate its volume fraction, and the calculation formula about its volume fraction can be adjustable according the actual demand; what＇s more, the new model considers the bypass flow and proposes a method to calculate its volume fraction for the first time, and then volume fraction of plug flow region, backmix flow region, dead region and bypass flow can be calculated and obtained at the same time; and this new model can better capture the deviation of reality flow pattern from ideal plug flow pattern, and reflects the feature of plug flow.

错位桨对污泥固液两相流混合的数值模拟

为了提高搅拌器的搅动范围、减小流动死区,基于混合理论和等螺距的设计原理,提出了一种错位叶片的结构形式.采用Fluent软件对错位桨搅拌器(6SBP)和普通6BP搅拌器在污泥液体中的流场变化进行了三维数值模拟,模拟分析比较了6SBP桨和6BP桨式两种搅拌器的流场形态、速度分布和功耗的特点,并通过实验进行了验证.结果表明,模拟结果和实验结果较吻合,错位桨搅拌流场不对称,能够减小流动死区,增大搅动范围.在N=3r/s的工作状态下,6SBP桨的轴向速度和径向速度分布要大于6BP桨,而功耗约为6BP桨的77%.

100t钢包吹氩工艺优化数值模拟研究

通过数值模拟,研究了100 t钢包在LF精炼过程中底吹氩气流量对钢包内钢液流动特性、"渣眼"面积及活跃区比例的影响。结果表明,在一定范围内,增大吹氩量有利于增大"渣眼"面积,强化钢水运动,缩小"死区"体积比例,有利于脱硫反应的进行。但当吹氩量超过临界值时,"死区"体积比例缩小幅度降低。100 t钢包最佳吹氩量为300 L/min。

多流中间包流动特征的数学模型

提出了针对多流中间包流动特征的数学模型,给出了绘制停留时间分布(RTD)曲线的标准及其相关计算的规范;明确了"死区"的特性,并计算了其体积分数;模型中考虑到了短路流,指出计算短路流的方法.模型可以更好地刻画活塞流的流动特性.

斜向流换热器壳程流场均匀化研究

传统弓形折流板换热器壳程流体横向流动时存在流动阻力和传热死区大等缺点。为克服上述不足,研究开发了一种新型高效节能的斜向流管壳式换热器,采用导向型折流栅替代传统弓形折流板,倾斜流道内流体斜向冲刷换热管束。考察和对比了斜向流换热器和弓形折流板换热器壳程主流区的流体流速分布和变化规律,证实了导向型折流栅具有显著的控涡均化壳程流场和提高壳程流体整体流速的作用,有助于减小壳程压降,增大有效换热面积,为管壳式换热器结构改良提供了参考依据。

桥台冲刷机理和计算方法

本文根据流体力学和河流动力学的基本原理，对桥周围的水流结构及其形成原因和冲刷深度计算方法进行了分析和讨论。通过模型试验对桥台冲刷的跟踪测量，按照冲刷发展的不同阶段分析了桥台周围局部冲刷坑的形成过程，以及上游滞水区随水深和桥台路堤长度的变化趋势。根据试验，用量纲分析原理和逐步回归分析的方法，提出桥台冲刷深度与主要影响因素的关系式。