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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
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在相似理论的基础上,通过水力学模拟对两流板坯连铸中间包3种不同气幕挡墙形式下的包内流场进行研究。实验结果表明:在同一吹气量(28L/h)时,气幕挡墙置于中间包端部(方案一),在气幕的两侧形成两个方向相反的回流区域,延长了钢液的平均停留时间,采用该方案时中间包内死区比例为18.5%;气幕挡墙置于中间包墙坝之间(方案二),也形成了两个较大的回流区,增加了钢液间的混合和夹杂物的去除,中间包内死区最小为17.4%,为三种方案之最优;气幕挡墙置于中间包挡墙之前(方案三),气幕挡墙并未形成有效的气幕,中间包内部流体未得到充分混匀,出现27.5%的较大的死区。 相似文献
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气幕挡墙技术是改善钢液洁净度的重要方法,吹入的气泡不仅可以改善中间包流场,还可以黏附去除夹杂物,大大提高夹杂物的去除率。采用Euler-Lagrange-Lagrange方法来研究钢液、气泡和夹杂物三相交互作用行为,该模型考虑了钢液与气泡、钢液与夹杂物、气泡与夹杂物之间的相互作用。在正常连铸条件下,研究了气泡黏附与吹气量对不同粒径夹杂物去除的影响。模拟结果表明,考虑气泡黏附的夹杂物去除率比不考虑黏附去除提高了19.12%~28.94%,气泡黏附夹杂物是去除夹杂物的重要方式之一,在气幕挡墙的研究中不可忽略。在本研究的吹气范围内,夹杂物的上浮去除率和黏附去除率都随着吹气量的增加而增大。与传统的挡墙挡坝中间包相比,使用气幕挡墙取代传统挡坝更有利于夹杂物的去除。 相似文献
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This paper focuses on the numerical modelling of slag entrainment in liquid metal. Due to the complexity of the multi‐phase flow situation and the inherently unsteady nature of the process, feasible simulations are restricted to rather coarse grids. Nevertheless, important flow structures like secondary suction vortices cannot be captured by an insufficiently resolved grid. As a consequence three numerical approaches are proposed in order to focus on local slag entrainment events within a global flow simulation. Firstly, in the course of Volume of Fluid (VOF) simulations the evolving metal‐slag interface is sharpened by a solution dependent adaptive grid refinement. Secondly, possible suction vortices are tested by super‐imposed Chimera grids. In this approach a finely resolved O‐shaped grid is placed around the trajectory of a representative Lagrangian fluid particle that is started from a local depression at the metal‐slag interface. Thirdly, a simplified concept of Lagrangian slag droplets is utilized in order to detect irregularly occurring flow situations that are prone to slag entrainment. These modelling approaches are applied to metallurgical processes like tundish pouring or continuous casting. With help of these slag entrainment modelling approaches a global metallurgical flow simulation can be augmented by the effect of local entrainment events. 相似文献
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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
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中间包上水口环形吹氩可以在塞棒周围形成清洗钢液的环形气幕,同时部分氩气泡随钢液进入上水口内,可以减少非金属夹杂物在水口内壁的黏附,起到防止水口堵塞的作用。然而,不合理的吹氩量会导致中间包内液面渣层受过强的气液羽流冲击而形成渣眼,使得钢液裸露并发生二次氧化,严重影响铸坯质量。采用标准 k ε 湍流模型研究中间包内流体流动,采用DPM模型和VOF模型耦合方法,研究上水口环形吹氩条件下渣眼的形成及演化规律。结果表明,上水口环形吹氩在塞棒周围形成较强的上升流,塞棒上部邻近区域存在多个涡流区;在钢液涡流的影响下,中间包液渣下层远离塞棒区域,上层向塞棒区域迁移;随着吹氩量的增大,平均湍动能增大,塞棒附近钢液速度逐渐增大,钢渣界面钢液速度先增大后减小,渣眼边缘钢液速度先增大后减小然后再增大,速度与垂直方向夹角逐渐减小;增大吹氩量,中间包熔池液面形成以塞棒为中心的渣眼,渣眼面积逐渐增大。试验条件下不产生渣眼的临界吹氩量为4.2 L/min,对应的钢渣界面最大速度为0.247 m/s,与垂直方向夹角为70°。 相似文献
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Inertial and buoyancy driven water flows under gas bubbling and thermal stratification conditions in a tundish model 总被引:5,自引:0,他引:5
A. Vargas-Zamora J. Palafox-Ramos R. D. Morales M. Díaz-Cruz J. de J. Barreto-Sandoval 《Metallurgical and Materials Transactions B》2004,35(2):247-257
Steel flow dominated by inertial and buoyancy flows under gas bubbling and thermal stratification conditions, in a one-strand
tundish, was studied using a 2/5 scale water model. The use of a turbulence inhibitor yields plug flow volume fractions well
above 40 pct for a casting rate of 3.12 tons/min under isothermal conditions. Small flow rates of gas injection (246 cm3/min), through a gas curtain, improved the fluid flow by enhancing the plug flow volume fraction. Higher flow rates originated
an increase of back-mixing flow, thus forming recirculating flows in both sides of this curtain. Step inputs of hot water
drove streams of this fluid toward the bath surface due to buoyancy forces. A rise in gas flow rate led to a thermal homogenization
in two separated cells of flow located at each side of the gas curtain. Step inputs of cold water drove streams of fluid along
the tundish bottom. Use of the gas curtain homogenized the lower part of the tundish as well as the upper part of the bath
at the left side of the curtain. However, temperature at the top corner of the tundish, in the outlet box, remained very different
than the rest of the temperatures inside this tundish. High gas flow rates (912 cm3/min) were required to homogenize the bath after times as long as twice the mean residence time of the fluid. Particle image
velocimetry (PIV) measurements corroborated the formation of recirculating flows at both sides of the gas curtain. 相似文献
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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
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Laboratory experiments were carried out to study the phenomena related to open‐eye formation in ladle treatment. Ga‐In‐Sn alloy with a melting temperature of 283 K was used to simulate the liquid steel, while MgCI2‐Glycerol(87%) solution as well as HCl solution were used to simulate the ladle slag. No open‐eye was formed at lower gas flow rates, but, occurred when gas flow reached a critical rate. This critical gas flow rate was found to depend significantly on the height of the top liquid. No noticeable amount of top liquid was observed in any of the samples taken from the metal bulk during gas stirring. To confirm this aspect, samples of slag‐metal interface were taken around the open‐eye in an industrial gas stirred steel ladle. No entrapped slag droplet was found in the solidified steel within the region between the interface and 2 cm from the interface. The accordance of the laboratory and industrial results suggests that the entrainment of slag into the steel bulk around the open‐eye cannot be considered as the major contribution to inclusion formation. 相似文献
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《钢铁冶炼》2013,40(6):436-440
AbstractFluid flow characteristics in a two strand slab continuous casting tundish with different configurations of argon gas bubbling curtain (GBC) were investigated in physical modelling experiments. It was found from this research that the GBC with a small flow rate acted as a gas dam and could greatly improve the flow characteristics in the tundish. It increased dramatically the peak concentration time and plug flow volume, decreased greatly the dead volume, created surface directed flow and eliminated short circuiting. Therefore, the fluid flow characteristics in a tundish with GBC were favourable to the floatation and separation of inclusions from molten steel. The flow characteristics with low gas flow rate and short distance of the bubbling curtain from the tundish outlet were better than those with high gas flow rate and large distance of the curtain to the outlet. The optimal configuration for the improvement in fluid flow characteristics was turbulence inhibitor (TI)–weir–dam–GBC (TI–W–D–GBC), followed by TI–channel weir (CW)–GBC, TI–W–GBC and TI–GBC. 相似文献
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