七流连铸中间包流场的数值模拟

采用FLUENT软件对中天钢铁集团公司七流连铸中间包内型流场进行数值模拟,研究速度矢量、湍动能和流体迹线分布规律,分析中间包内有无C型挡墙加入的流场特征.模拟结果表明,加入C型挡墙使中间包的湍动能主要集中在入口区域,利于延长包内各流的平均停留时间,减小死区体积分数,包内各流流动更加均匀,有利于钢液温度和成份的均匀.     

八流中间包内型优化水模实验

根据相似原理,利用水模拟钢液流动来研究中间包内流场的流动状况,通过调节中间包内挡墙位置及其开孔大小来改善和优化中间包内的流场。对比计算机采集的RTD数据及用墨汁作为示踪剂的照片寻求出最优化方案。得出经过改进的中间包各流平均停留时间增加50-90s,死区体积由25％～30％降低到14％～19％,活塞流的体积比从8％～13％增加到26％-27％,优化了中间包内的流场。     

漩流中间包流场的数值模拟

采用CFD软件Fluent对漩流中间包内的流场进行了数值模拟,分析了漩流中间包内的流场特征,以及漩流室的加入,中间包内的流动形态.模拟结果表明,由于漩流室的加入使湍动能耗散主要集中在漩流室内部,有利于夹杂物的聚合长大;漩流室的加入可改善钢液的流动状态,利于夹杂物的上浮。由于入口位置的非对称布置,造成了漩流中间包内的流场在入口区呈明显的非对称分布,这些结果为进一步优化漩流中间包内漩流室的位置和中间包挡墙参数提供了理论依据.     

首钢中间包优化设计(Ⅰ)

应用湍流流动数学模型研究了首钢中间包内钢液的流动与混合 ,该模型包括求解三维湍流的N -S方程和k -ε双方程模型 对首钢第二炼钢厂现有中间包的流场和钢液的停留时间做了模拟与分析 ,并预报了在不同位置加设不同高度的坝后 ,中间包内钢液的流动状态及停留时间 结果表明 ,如果坝的设置不当 ,中间包内钢液的流动状态则会更差     

六机六流中间包流场优化水模研究

根据相似原理,利用水模拟钢液流动,研究中间包内流场的流动情况。在不同方案的内腔设计下,分别进行水模型试验,通过计算机采集相关数据,对比由计算机采集数据绘制成的RTD曲线及用墨汁作为示踪剂的流场照片,寻求出最优化方案。经过改进的中间包各流平均停留时间较长,不同流量的平均停留时间分别为459,380,374s;死区体积最小,死区平均体积分数为15．1％,中间包内流场得到了优化。     

首钢中间包优化设计(Ⅱ)

应用湍流流动的数学模型研究了首钢中间包内钢液的流动与混合,该模型包括求解三维湍流的N－S方程和K－ε双方程模型。对首钢第二炼钢厂现有中间包的流场和停留时间作了模拟与分析,并预报了在不同位置加设不同高度的堰坝后中间包内钢液的流动状态及停留时间。结果表明：如果二重堰的设置不当,中间包内钢液的流动状态则会更差。     

小方坯连铸机中间包内钢液流动水模试验研究

在小方坯连铸机四流梯形中间包内,使用不同形状的冲钢砖对钢液流动状态的影响,进行了水模试验研究。试验发现,注流的旋转散乱与中间包内钢液的流场有密切关系。通过水模的多次试验找到了较合理的冲钢砖结构,使钢液的流场更趋合理,消除了注流的旋转散乱状态。     

板坯连铸机中间包流场研究

应用湍流流动的数学模型研究板坯连铸机中间包内钢液的流动,该模型包括求解三维湍流的Navirt-Stekes方程和K-ε两方程的湍流模型。对宝钢板坯连铸机中间包的流场作了模拟与分析,结果证明宝钢连铸机中间包的流场方式是合理的。     

板坯连铸中间包内气液两相流数值模拟

模拟研究了中间包上使用狭缝式透气砖条件下,连铸中间包内气体体积分布和流场.结果表明,狭缝宽度和气体流量对气幕挡墙的形成影响显著;气体流量约为10 m3/h时,中间包内钢液的流动特性较好.     

二流连铸中间包内型优化水模试验

以相似原理为基础,用水模拟钢液研究中间包内的钢水流动特征,通过测定模型中间包内停留时间分布曲线(RTD),计算其平均停留时间及死区、活塞区和混合区的体积。试验表明,经过改进的中间包,其最短停留时间由20s增加到54s,平均停留时间由249s增加到305s,死区体积则由30．34％降低到14．74％,优化了中间包内的流场。     

连铸中间包内流场与温度场的数值模拟

针对国内某钢厂中间包,利用CFD软件FLUENT研究该中间包内传输现象,计算挡墙对中间包流场和温度分布的影响,结果表明设置合适的中间包挡墙,能明显改善中间包内的流场和温度场.     

Application of Computational Fluid Dynamics to analysis of metallurgical process for continuous casting tundishes

A series of simulations by mathematical and physical modeling on fluid flow, mass and heat transfer in continuous casting tundishes have been carried out. It was found by computational fluid dynamics (CFD) simulation that in most cases tundish flow must be treated as a non-isothermal reactor due to the existence of temperature difference between the transport ladle and the tundish. The critical conditions when the non-isothermal flow in the tundish can not be neglected have been found by CFD simulation and water modeling. A direct measurement in a 40 t tundish has confirmed the simulation results.     

Fluid Flow in Tundish Due to Different Type Arrangement of Weir and Dam

Tundish is an important metallurgical reactor in the continuous casting process,In order to control the fluid flow in tundish and thus take full advantage of the residence time available for the removal of inclusions from molten steel,the effect of weir and dam on the fluid flow has been studied in a water model based on the characteristic number Froude and Reynold number similarity criteria.The residence time distribution curves of the flow were measured by SG800,The optimum arrangement of dam and weir and the nonstationary flow in tundish were discussed.The results show that the comnbination of weir and dam is benefit for the flow pattern in tundish,weir can prevent the upper recirculating flow.dam can cut off the bottom flow and turn to upwards,it is advantageous to separate the nometallic inclusions.Furthermore,it is importnat to exceed the critical depth of bath during exchange ladles,not only for the inclusion floatation but also for avoiding tundish slag drainage earlier.     

Fluid flow in large-capacity horizontal continuous casting tundishes

The configuration of the tundish for a two-strand horizontal continuous caster was designed and optimized through water modeling. Three designs of the tundish were studied: the original tundish without any flow control devices, the tundish with a turbulence inhibitor at the bottom, and the tundish with an inlet launder and an inclined dam. The residence time, the location and size of the dead zone, and the fluid field pattern were investigated. At the same time, the asymmetry flow field and wavy inlet jet in the horizontal tundish were observed and the reasons for them were discussed. The results indicate that the tundish with an inlet launder and an inclined dam is the best of the three designs.     

五流连铸机中间包结构研究

应用湍流流动的数学模型研究五流连铸机中间包内钢液的运动,对某厂五连铸机中间包的流场作了模拟和分析,结果表明,该中间包存在一些问题,指出了改进的方向。     

Optimization of flow control devices in a single-strand slab continuous casting tundish

The optimization of flow control devices in a single-slab continuous casting tundish was carried out by physical modeling, and the optimized scheme was presented. With the optimal tundish configuration, the minimum residence time of liquid steel was increased by 1.4 times, the peak concentration time was increased by 97%, and the dead volume fraction was decreased by 72%. A mathematical model for molten steel in the tundish was established by using the fluid dynamics package Fluent. The velocity field, conc...     

底吹气中间包内流动与夹杂物控制

以宝钢集团梅山钢厂1台连铸中间包为原型,采用水模型的方法对底吹气中间包内的流动和夹杂物控制进行研究.结果表明,采用自行设计的装置进行底吹气,能够在中间包内形成均匀、稳定而又细小的气泡;底吹气能够在中间包内形成微气泡形式的"气幕挡墙","气幕挡墙"的形成能有效地破坏中间包内"层流"结构的流动形式,避免形成短路流动,提高平均停留时间,缩小死区体积分率;在吹气位置的选择上,采用中部位置(B2)进行吹气,效果较好;采用底吹气的方式可以实现对中间包内流动的控制,且不需要大的气体流量;底吹气有利于中间包内夹杂物的去除.     

Modeling study on fluid flow and inclusion motion in 6-strand bloom caster tundishes

The behavior of fluid flow and particle motion in a 6-strand bloom caster tundish was investigated by a water model and numerical simulation. Compared with a device without flow control, the tundish with flow control has an important effect on the fluid flow pattern and inclusion removal. It is revealed that by non-isothermal process, which is real production condition, the fluid flow in tundish shows a strong buoyancy pattern, which drives particles to move upwards. The particle removal was quantitatively studied by mathematical and physical simulations.     

两流非对称中间包内控流装置优化的水模型研究

通过水模型实验和数值模拟,研究了两流非对称中间包采用不同控流装置时流体流动的特性.结果表明：圆形湍流控制器与单挡墙组成的控流装置中间包两出口流体流动差异较大;非对称长方形湍流控制器和多孔挡墙组成控流装置的中间包,两流之间的平均停留时间差异是圆形湍流控制器和单挡墙组成控流装置中间包的2/3,且近长水口侧出口的平均停留时间延长7.5%.