首页> 外文期刊>ISIJ international >Modeling of Fluid Flow and Residence Time Distribution in a Four-strand Tundish for Enhancing Inclusion Removal
【24h】

Modeling of Fluid Flow and Residence Time Distribution in a Four-strand Tundish for Enhancing Inclusion Removal

机译:增强夹杂物去除能力的四股中间包内流体流动和停留时间分布的建模

获取原文
获取原文并翻译 | 示例
           

摘要

The introduction of the appropriate size and precise location of flow control devices such as dam, turbulence inhibitor, etc., helps to modify the flow pattern and minimizing short circuiting and dead zone. Beside this, these also create the surface directed flow and maximize the residence time available for the flotation of inclusions and assimilation of the reaction products from the molten steel into the slag phase. These can be products of deoxidation, reoxidation, precipitation, emulsification and/or entrainment of refractory components into the melt and thus encompass both indigenous and exogenous inclusions. To this end, both the numerical and physical simulations were carried out mainly for three cases: a) in absence of flow control devices (i.e., bare tundish), b) in the presence of a dam, and c) with the application of turbulence inhibiting device (TID) and dam combination in the existing tundish configuration. The commercial CFD (computational fluid dynamics) package FLUENT® was used to predict the flow field prevalent in the water model tundish at steady state, whereas in the experimental program, both Particle Image Velocimetry (PIV) techniques for flow measurements and tracer dispersion experiments for concentration measurements were applied in the present study. Among all types of configurations applied in the present study, a combination of TID with holes+a dam work reasonably found to be an optimum configuration of the four-strand tundish regarding inclusion floatation. A superior strand similarity is also achieved in this configuration. Also the predicted time averaged horizontal and vertical components agreed within±10% with the experimentally derived ones.
机译:引入合适尺寸和精确位置的流量控制装置(如水坝,湍流抑制器等)有助于修改流量模式,并最大程度地减少短路和死区。除此之外,它们还产生表面导向的流动,并使停留时间最大化,从而可用于夹杂物的浮选和反应产物从钢水到炉渣相的同化。这些可以是耐火成分进入熔体的脱氧,再氧化,沉淀,乳化和/或夹带的产物,因此涵盖了原生和外生夹杂物。为此,主要在以下三种情况下进行了数值和物理模拟:a)没有流量控制装置(即,中间包裸露),b)有大坝,以及c)湍流作用现有中间包配置中的抑制装置(TID)和水坝组合。商业CFD(计算流体动力学)软件包FLUENT®用于预测稳态时水模型中间包中普遍存在的流场,而在实验程序中,用于流量测量的粒子图像测速(PIV)技术和用于示踪剂扩散实验在本研究中应用浓度测量。在本研究中应用的所有类型的构造中,TID与孔+坝的组合合理地被认为是关于夹杂物漂浮的四链中间包的最佳构造。在这种构造中也实现了优异的链相似性。而且,预计的时间平均水平和垂直分量与实验得出的分量在±10%之内。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号