首页> 外文期刊>International journal of numerical methods for heat & fluid flow >Three-dimensional CFD simulation and experimental validation of particle segregation in CFB riser
【24h】

Three-dimensional CFD simulation and experimental validation of particle segregation in CFB riser

机译:CFB立管中颗粒偏析的三维CFD仿真及实验验证

获取原文
获取原文并翻译 | 示例
       

摘要

Purpose - The purpose of this paper is to perform the computational fluid dynamics (CFD) simulation with experimental validation to investigate the particle segregation effect in abrupt and smooth shapes circulating fluidized bed (CFB) risers. Design/methodology/approach - The experimental investigations were carried out in lab-scale CFB systems and the CFD simulations were performed by using commercial software BARRACUDA. Special attention was paid to investigate the gas-particle flow behavior at the top of the riser with three different superficial velocities, namely, 4, 6 and 7.7 m/s. Here, a CFD-based noble simulation approach called multiphase particle in cell (MP-PIC) was used to investigate the effect of traditional drag models (Wen-Yu, Ergun, Wen-Yu-Ergun and Richardson-Davidson-Harrison) on particle flow characteristics in CFB riser. Findings - Findings from the experimentations revealed that the increase in gas velocity leads to decrease the mixing index inside the riser. Moreover, the solid holdup found more in abrupt riser than smooth riser at the constant gas velocity. Despite the more experimental investigations, the findings with CFD simulations revealed that the MP-PIC approach, which was combined with different drag models could be more effective for the practical (industrial) design of CFB riser. Well agreement was found between the simulation and experimental outputs. The simulation work was compared with experimental data, which shows the good agreement (<4%). Originality/value - The experimental and simulation study performed in this research study constitutes an easy-to-use with different drag coefficient. The proposed MP-PIC model is more effective for large particles fluidized bed, which can be helpful for further research on industrial gas-particle fluidized bed reactors. This study is expected to give throughout the analysis of CFB hydrodynamics with further exploration of overall fluidization.
机译:目的 - 本文的目的是通过实验验证进行计算流体动力学(CFD)模拟,以研究循环流化床(CFB)立管的突然和平滑形状的粒子隔离效果。设计/方法/方法 - 实验研究在实验室规模中进行了CFB系统,通过使用商业软件Barracua进行CFD仿真。特别注意研究提升管顶部的气体颗粒流动,具有三种不同的表面速度,即4,6和7.7m / s。这里,使用CFFD的贵族贵族仿真方法(MP-PIC)中称为多相粒子(MP-PIC)来研究传统阻力模型(文宇,ergun,文玉牛和巫师 - 戴维森 - 哈里森)对粒子的影响CFB立管中的流动特性。结果 - 从实验中的发现表明,气体速度的增加导致提升管内的混合指数降低。此外,固体堆叠在恒定气体速度下比平滑提升器更突出的升压。尽管实验更具实验研究,但具有CFD模拟的发现表明,与不同阻力模型相结合的MP-PIC方法对于CFB提升机的实际(工业)设计更有效。在模拟和实验结果之间发现了良好的一致性。将仿真工作与实验数据进行比较,显示良好的一致性(<4%)。原创性/值 - 本研究中进行的实验性和仿真研究易于使用不同的阻力系数。所提出的MP-PIC模型对大型颗粒流化床更有效,这有助于进一步研究工业气体颗粒流化床反应堆。该研究预计在整个对CFB流体动力学的分析过程中,进一步探索了整体流化。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 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