期刊文献+

Gas-solid flow in a diffuser:Effect of inter-particle and particle-wall collisions

原文传递
导出
摘要 This article investigates the role of the specularity coefficient(φ,the extent of the energy dissipation due to particle-wall collisions),inter-particle restitution coefficient(e_(pp),the extent of the energy dissipation due to inter-particle collisions),and four combinations of these variables on the hydrodynamics,and the pressure recovery of the dilute gas-solid suspension in a diffuser.The investigation applies the two-fluid modeling approach along with the kinetic theory of the granular flow.The present investigation’s findings indicate that an increase inφor a reduction in e_(pp) reduces the pressure recovery by weakening the reverse momentum transfer phenomenon,which is recognized as the primary means for the pressure recovery.Besides,in a gas-solid flow system,a higherφor smaller e_(pp) enhances the particles’trapping in the recirculation zone.The recirculation zone’s strength and size increase asφincreases or e_(pp) reduces.Moreover,an increase in the wall-particle and inter-particle interactions strengthens the sidewise displacement of the particles.The effect of the wall-particle and inter-particle interactions are insignificant for extremely small solid loading.
机构地区 CFD Laboratory
出处 《Particuology》 SCIE EI CAS CSCD 2021年第4期187-200,共14页 颗粒学报(英文版)
  • 相关文献

参考文献6

二级参考文献47

  • 1周力行,张夏.SIMULATION OF SUDDEN-EXPANSION AND SWIRLING GAS-PARTICLE FLOWS USING A TWO-FLUID PARTICLE-WALL COLLISION MODEL WITH CONSIDERATION OF THE WALL ROUGHNESS[J].Acta Mechanica Sinica,2004,20(5):447-454. 被引量:3
  • 2Cammarata, L., Lettieri, P., Micale, G. D. M., & Colman, D. (2003). 2D and 3D CFD simu-lations of bubbling fluidized beds using Eulerian–Eulerian models. InternationalJournal of Chemical Reactor Engineering, 1, ArtA48.
  • 3Chen, X.-Z., Shi, D.-P., Gao, X., & Luo, Z.-H. (2011). A fundamental CFD study of thegas–solid flow field in fluidized bed polymerization reactors. Powder Technology,205, 276–288.
  • 4Fluent Inc. (2006). Fluent 6.3 user’s guide. Lebanon/New Hampshire, USA: Fluent Inc.
  • 5Gidaspow, D. (1994). Multiphase flow and fluidization: Continuum and kinetic theorydescriptions. Boston: Academic Press.
  • 6Huang, W., Gong, X., Guo, X., Dai, Z., Liu, H., Cao, Z., et al. (2009). Study of the pressuredrop of dense phase gas–solid flow through nozzle. Powder Technology, 189,82–86.
  • 7Klinzing, G. E., Rizk, F., Marcus, R. D., & Leung, L. S. (2010). Pneumatic conveying ofsolids: A theoretical and practical approach (3rd ed.). London: Springer.
  • 8Lain, S., & Sommerfeld, M. (2008). Euler/Legrange computations of pneumatic con-veying in a horizontal channel with different wall roughness. Powder Technology,184, 76–88.
  • 9Li, T. W., Grace, J. R., & Bi, X. T. (2010). Study of wall boundary condition in numericalsimulations of bubbling fluidised beds. Powder Technology, 203, 447–457.
  • 10Lun, C. K. K., Savage, S. B., Jeffery, D. J., & Chepurnity, N. (1984). Kinetic theories forgranular flow: Inelastic particles in Couette flow and slightly inelastic particlesin general flow field. Journal of Fluid Mechanics, 140, 223–256.

共引文献13

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部