共查询到18条相似文献,搜索用时 62 毫秒
1.
2.
控制中间包内钢液的合理流动对夹杂物的排除有重要影响,为此建立了模拟薄板坯连铸中间包钢液流动情况的模型。采用数学和物理模拟的研究方法,研究了不同尺寸和安装位置的控流装置对某钢厂薄板坯连铸中间包流动特性的影响。结果表明:中间包在无流动控制时,存在明显的短路流及较大死区;原使用控流装置其平均停留时间小,死区较大,实验效果并非最佳;通过实验提出的优化方案,使中间包内示踪刑开始响应时间为无控流装置下的2倍多,平均停留时间由264秒增加到301.4秒,死区由无控流装置的25.54%降低到15.39%,中间包的冶金性能有了明显改进。 相似文献
3.
4.
底吹氩中间包钢液流动特性的数值模拟研究 总被引:12,自引:3,他引:9
根据某厂实际中间包的操作工艺参数,采用欧拉两流体模型以及多孔介质模型,用数值模拟法研究了同时采用湍流控制器和气幕挡墙技术,中间包内气幕挡墙的位置及吹气量对中间包内钢液流动特性的影响。结果表明,采用气幕挡墙技术,吹气量及吹气位置对钢液流场及RTD曲线影响较大,吹气位置靠近人口或出口都不利于中间包钢液流动特性的改善,吹气量太大易引起表面卷渣现象,吹气量太小,不能形成有效的气幕挡墙。气幕挡墙距离人口1200~2000mm,且吹气量为0.90m^3/h时,可以有效延长钢液的停留时间,减小死区体积,有利于夹杂物的上浮去除。 相似文献
5.
板坯连铸单流中间包控流装置优化模拟研究 总被引:3,自引:0,他引:3
采用水力学模型试验,对太钢不锈钢板坯连铸单流中间包流场进行了模拟研究,并通过数值模拟进行验证,研究结果表明:该钢厂原型中间包流场存在严重问题,中间包内存在明显短路流现象,死区比例较大,钢液混匀效果差;通过正交优化试验得出最佳坝堰因素水平组合方案,使中间包流场得到改善;采用中间包气幕挡墙代替坝优化方案,使中间包流场得到进一步改善.根据水力学模型试验和数值模拟计算结果,结合钢厂实际情况,建议单流连铸中间包采用气幕挡墙代替坝的技术工艺,对于太钢不锈钢板坯中间包气幕挡墙最佳工艺参数:距离堰1 150 mm附近,底吹气量控制在120 L/min左右. 相似文献
6.
7.
薄板坯连铸中间包控流装置的数理模拟 总被引:1,自引:0,他引:1
采用水力学数理模拟的方法,研究了不同尺寸和安装位置的控流装置对马钢薄板坯连铸中间 包流动特性的影响。结果表明:中间包在无流动控制时,存在明显的短路流及较大死区;西马克公司提供的控 流装置其平均停留时间小,死区较大,实验效果并非最佳;改进后的优化方案使中间包内示踪剂开始响应时间 为无控流装置下的2倍多,平均停留时间由264.0s 增加到301.4 s,死区由无控流装置的25.54%降低到 15.39%,中间包的冶金性能有了明显改进。 相似文献
8.
9.
10.
11.
12.
13.
Liangcai Zhong Liying Li Bao Wang Maofang Jiang Lixing Zhu Li Zhang Rongrong Chen 《国际钢铁研究》2006,77(2):103-106
Fluid flow characteristics in a two‐strand slab tundish with Ar bubbling curtain were studied in water modelling experiments. It was found that the Ar bubbling curtain can greatly improve the flow characteristics in the tundish with a weir, a dam and a turbulence inhibitor. It dramatically increased the peak concentration time and plug volume and greatly decreased the dead volume, but hardly influenced the minimum residence time. Therefore, the fluid flow characteristics in a tundish with Ar bubbling curtain were favourable to the flotation and separation of inclusions from molten steel. The flow characteristics with low gas flow rate and short distance of the Ar bubbling curtain from the tundish outlet were better than those with high gas flow rate and large distance of the curtain from the outlet. 相似文献
14.
长水口插入深度对中间包钢液的流动状态有重要影响。以相似原理为基础,进行水模实验,测定了有无控流装置时中间包钢液的停留时间分布曲线(RTD);采用Fluent软件和数学模拟的方法,仿真计算获得了实际中间包内钢液的流动状态,分析比较了钢液流动的速度矢量图和流线图。从而确定了合理的长水口插入深度。研究结果表明,有、无控流装置时,建议长水口插入深度为110 mm左右。 相似文献
15.
Fluid Flow and Interfacial Phenomenon of Slag and Metal in Continuous Casting Tundish With Argon Blowing 总被引:1,自引:0,他引:1
The fluid flow and the interfacial phenomenon of slag and metal in tundish with gas blowing were studied with mathematical and physical modeling, and the effects of gas flowrate, the placement of porous beam for the generation of bubbles, and the combination of flow control devices on the flow and slag-metal interface were investigated. The results show that the position of gas bubbling has a significant effect on the flow in tundish, and the placement of porous beam and gas flowrate are the two main factors affecting the entrapment of slag in tundish. The closer the porous beam to the weir, the more reasonable is the flow, which is in favor of the control of slag entrapment in tundish. 相似文献
16.
17.