首页> 外文期刊>ISIJ international >Numerical Simulation of Multiphase Flow and Mixing Behavior in an Industrial Single Snorkel Refining Furnace Effect of Bubble Expansion and Snorkel Immersion Depth
【24h】

Numerical Simulation of Multiphase Flow and Mixing Behavior in an Industrial Single Snorkel Refining Furnace Effect of Bubble Expansion and Snorkel Immersion Depth

机译:工业单通气管精炼炉中气泡膨胀和通气管浸入深度的多相流动和混合行为的数值模拟

获取原文
       

摘要

A coupled mathematical model is used to simulate the multiphase flow in an industrial Single Snorkel Refining Furnace (SSRF). Based on the present model, the evolution characteristics of bubble size, density, and velocity are analysed during the long-distance rising process. The comparative studies indicate that the expansion of bubbles has an enormous impact on the circulation rate and free surface in the vacuum chamber. Furthermore, the effect of snorkel immersion depth (SID) on the circulation rate, mixing time, and fluid flow are investigated. The results indicate that the circulation rate decreases with the increase of SID, while the mixing time shows an uptrend with the increase of SID. Particularly, when the SID exceeds 0.4 m, the scope of dead zone around the snorkel dramatically increases, which further decreases the flow velocity of slag layer in the ladle.
机译:耦合数学模型用于模拟工业单通气管精炼炉(SSRF)中的多相流。在此模型的基础上,分析了长距离上升过程中气泡大小,密度和速度的演化特征。比较研究表明,气泡的膨胀对真空室中的循环速率和自由表面具有巨大影响。此外,研究了通气管浸入深度(SID)对循环速率,混合时间和流体流量的影响。结果表明,随着SID的增加,循环速度降低,而随着SID的增加,混合时间呈上升趋势。特别地,当SID超过0.4m时,通气管周围的死区的范围急剧增加,这进一步降低了钢水包中的渣层的流速。

著录项

相似文献

  • 外文文献
  • 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