共查询到17条相似文献,搜索用时 156 毫秒
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钢包浇铸末期旋涡卷渣严重影响钢水洁净度和金属收得率。利用钢包渣示踪法研究了上海梅山钢铁股份有限公司250 t钢包浇铸过程卷渣行为。通过在中间包注流区采集钢样,基于含Ba夹杂物成分、尺寸和形貌研究卷渣形成的夹杂物特性,并通过夹杂物中平均Ba含量变化来判断旋涡卷渣发生的程度。结果表明:卷渣形成的夹杂物普遍尺寸较大、形貌呈球形,在钢包余钢量不低于15~18 t的时候便开始出现旋涡卷渣。为了抑制旋涡卷渣,针对梅钢250 t钢包的实际工况,提出了一种新的出水口结构,并利用物理模拟试验对比了常规出水口和新出水口的旋涡特性,采用新的出水口可以显著降低钢包的起旋高度和贯通高度。 相似文献
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钢包的水口偏心率会显著影响浇注末期汇流旋涡的形成和发展过程。基于钢包特征设置合理的水口偏心率,有利于控制旋涡形态、抑制旋涡的危害。但是偏心率的变化如何改变流场,对浇注过程产生哪些影响,目前的研究并不充分。通过数值模拟方法,研究了水口偏心率对钢包流场和旋涡的影响规律,同时定义了“影响度”指标,定量分析了偏心率对浇注过程中表征流场和旋涡特性的14个物理量(如水口流量、旋涡角速度、湍动能、水口含气率等)的影响程度。结果表明,水口偏心率和各物理量之间存在非线性关系;不同物理量变化的临界点不同,普遍为0.5~0.7,旋涡的稳定性和容器壁面是影响临界点的主要因素。 相似文献
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针对高拉速下薄板坯连铸结晶器内的液面卷渣问题,建立了1∶1水力学模型,采用水/真空泵油模拟钢/保护渣介质,研究了连铸拉速、水口插入深度、保护渣黏度对漏斗形结晶器内液渣层变化及卷渣行为的影响。结果表明,随着拉速提高,结晶器内液面波高升高,液面高度自窄边向水口方向逐渐降低,液渣层厚度相应由薄变厚,导致结晶器窄边附近钢液裸露;结晶器内窄边至水口之间1/2处波高变化较大、液面流速最大、易发生剪切卷渣。在试验条件下,采用增加水口插入深度、降低最高拉速、适当提高保护渣黏度等方法,使液面速度小于0.486 m/s的临界流速、液面波动指数F数小于5.45,可防止结晶器内产生剪切卷渣。然而,这些手段不能避免结晶器内水口附近的旋涡卷渣,这是因为薄板坯连铸钢通量大以及漏斗形结晶器和鸭嘴形水口容易形成负压旋涡造成的。 相似文献
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针对浇注钢包环出钢口四孔透气塞吹氩控制下渣工艺,建立了某钢厂130 t钢包三维DPM-VOF耦合数学模型以计算浇注钢包下渣过程,并通过冷态实验验证了该模型的有效性。利用该模型研究了不同偏心率对下渣行为的影响,揭示了该工艺控制下渣的行为规律,并分析了吹氩流量对控制下渣的影响。结果表明,随着偏心率的增大,不同浇注高度下的最大切向速度减小,汇流漩涡临界高度降低。环出钢口四孔透气塞吹入氩气后,气泡流股的汇聚有效地减弱了水口上方钢液的周向旋转速度,大幅降低了汇流漩涡下渣临界高度。4个气泡流股的气液两相流会抑制流向水口钢液的径向流动速度,由排流沉坑引起的下渣也得到明显抑制。随着吹氩流量的增加,下渣临界高度呈降低趋势。就本研究而言,控制下渣的最佳吹氩流量为30 L/min。 相似文献
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At the late stage of continuous casting (CC) ladle teeming,sink vortex can suck the liquid slag into tundish,and cause negative influences on the cleanliness of molten steel.To address this issue,a two-phase fluid mechanical modeling method for ladle teeming was proposed.Firstly,a dynamic model for vortex suction process was built,and the profiles of vortex flow field were acquired.Then,based on the level set method (LSM),a two-phase 3D interface coupling model for slag entrapment was built.Finally,in combination with high-order essentially non-oscillatory (ENO) and total variation diminishing (TVD) methods,a LSM-based numerical solution method was proposed to obtain the 3D coupling evolution regularities in vortex suction process.Numerical results show that the vortex with higher kinetic energy can form an expanded sandglass-shape region with larger slag fraction and lower rotating velocity;there is a pressure oscillation phenomenon at the vortex penetration state,which is caused by the energy shock of two-phase vortex penetration coupling. 相似文献
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钢包在非稳态浇注过程中易形成旋涡,导致钢渣及空气的大量卷入,严重危害了钢的质量.为了更好的研究旋涡,采用ANSYS CFX软件,分别采用k-ε和RNG k-ε 2种湍流模型对钢包非稳态浇注过程中自由表面旋涡进行数值模拟,得到自由表面从表面旋转到旋涡贯通水口的演化过程,将两者的计算结果与相关文献以及Burgers涡模型进行相互对比,得到:两者计算的旋涡演化过程、旋涡产生临界高度无差别;两者的速度场与相关文献均一致,但RNG k-ε模型更真实的表现了旋涡的剪切流动;将两者的切向速度分布与Burgers涡对比,得到RNG k-ε湍流模型与理论模型更加吻合.综上:用RNG k-ε湍流模型计算自由表面旋涡更加正确合理. 相似文献
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The fluid flow in tundish is a non-isothermal process and the temperature variation of stream from teeming ladle dominates the fluid flow and thermal distribution in tundish. A numerical model was established to investigate the effect of inlet cooling rate on fluid flow and temperature distribution in tundish based on a FTSC (Flexible Thin Slab Casting) tundish. The inlet cooling rate varies from 0.5 to 0.25 ℃/min. Under the present calculation conditions, the following conclusions were made. When the stream temperature from teeming ladle drops seriously (for inlet cooling rate of 0.5 ℃/min), there is a “backward flow” at the coming end of casting. The horizontal flow along the free surface turns to flow along the bottom of tundish. The bottom flow shortens the fluid flow route in tundish and deteriorates the removal effect of nonmetallic inclusions from molten steel. Nevertheless, when the inlet cooling rate decreases to 0.25 ℃/min, the horizontal flow is sustained during the whole casting period. The present research provides theoretical directions for temperature control in teeming ladle and continuous casting tundish during production of advanced steels. 相似文献
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A water model of a typical 150t ladle was designed and constructed to determine the flow characteristics. A kind of organic emulsion was selected to model nonmetallic inclusion particles with the purpose of studying the inclusion removal effect under gas blowing in a teeming ladle. The presented modeling method for inclusion particles in the teeming process is different from those under steady condition. The numerical simulation was performed by using commercial software with the Eulerian‐Eulerian multiphase model applied to a model gas blown through a ladle. The numerical component of this study was conducted aiming at exploring the transient flow characteristics in teeming ladle corresponding to the physical experimental condition. Under the present conditions the authors came to the conclusion that soft gas blowing (2.7~4.0 × 10?6 m3/s) was favourable to float inclusion particles into the slag layer. It is suggested to end the gas blowing when the drainage percentage reaches 50%. 相似文献
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采用相似比为1∶10的水模型研究了钢包底吹氩系统中吹气孔直径对钢液流动的影响,通过测量钢包中心面的速度场,得到流体流动随吹气孔直径的变化规律。研究结果表明,吹气孔直径在1~3 mm范围内,随吹气孔直径增加,气柱、液面和包壁附近的流体速度减小,整个钢包内速度场分布更均匀。随吹气孔直径增加,涡心坐标从(0.12,0.12)向(0.12,0.10)和(0.12,0.09)变化,涡心向上移动,横向移动不明显。随着吹气孔直径的增加,底部产生的气泡直径变大,混匀时间有所减小。 相似文献
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Mathematical simulation of fluid dynamics during steel draining operations from a ladle 总被引:2,自引:0,他引:2
O. Davila L. Garcia-Demedices R. D. Morales 《Metallurgical and Materials Transactions B》2006,37(1):71-87
Fluid flow dynamics during ladle drainage operations of steel under isothermal and nonisothermal conditions has been studied
using the turbulence shear stress transport k-ε model (SST k-ω) and the multiphase volume of fluid (VOF) model. At high bath levels, the angular velocity of the melt, close to the ladle
nozzle, is small rotating anticlockwise and intense vertical-recirculating flows are developed in most of the liquid volume
due to descending steel streams along the ladle vertical wall. These streams ascend further downstream driven by buoyancy
forces. At low bath levels, the melt, which is close to the nozzle, rotates clockwise with higher velocities whose magnitudes
are higher for shorter ladle standstill times. These velocities are responsible for the formation and development of a vortex
on the bath free surface, which entrains slag into the nozzle by shear-stress mechanisms at the metal-slag interface. The
critical bath level or bath height for this phenomenon is 0.35 m (in this particular ladle design) for a ladle standstill
time of 15 minutes and decreases with longer ladle standstill times. At these steps, the vertical-recirculating flows are
substituted by complex horizontal-rotating flows in most of the liquid volume. Under isothermal conditions, the critical bath
level for vortex formation on the melt free surface is 0.20 m, which agrees very well with that determined with a 1/3 scale
water model of 0.073 m. It is concluded that buoyancy forces, originated by thermal gradients, as the ladle cools, are responsible
for increasing the critical bath level for vortex formation. Understanding vortex mechanisms will be useful to design simple
and efficient devices to break down the vortex flow during steel draining even at very low metal residues in the ladle. 相似文献