期刊文献+

颗粒旋转对鼓泡流化床内气固两相流动特性影响的数值模拟 被引量:7

Numerical simulation of gas and particles flow behavior considering effect of particle rotations in bubbling fluidized beds
下载PDF
导出
摘要 运用考虑颗粒自旋转流动对颗粒碰撞能量交换和耗散影响的颗粒动理学方法,建立鼓泡流化床气固两相Euler-Euler双流体模型,数值模拟流化床内气体颗粒两相流动特性。分析表明,颗粒平动温度与旋转温度之比是法向和切向颗粒弹性恢复系数和摩擦系数的函数。与不考虑颗粒旋转效应计算结果相比,考虑颗粒旋转效应后床内较容易形成气泡,颗粒自旋转运动将导致床内非均匀结构更明显。并且床层平均空隙率和床层膨胀高度增加,床中心区域颗粒轴向速度提高,床内颗粒平动温度下降。考虑颗粒旋转效应后预测的颗粒轴向速度和颗粒脉动速度与文献实验结果基本吻合。考虑颗粒旋转效应后获得的气泡直径更接近于前人经验关联式。 The flow behavior of bubble and particles in a gas-solid bubbling fluidized bed was simulated by using a two-fluid model incorporating the effect of particle rotations based on the kinetic theory for rapid granular flow of slightly frictional spheres. A simplified model was implemented without changing the current kinetic theory framework by introducing an effective coefficient of restitution to account for additional energy dissipation due to frictional collisions. Simulations were performed to study the bubble dynamics in a bubbling gas-fluidized bed without and with the consideration of particle rotations. With particle rotation, bubbles were easily formed in the bed, the particle concentrations decreased, and the bed expansion increased. Simulated results indicated that the axial velocities of particles increased, and the translational granular temperature of particles decreased in comparison with the case without particle rotation in the center regime of bed. It was found that the present model with particle rotations better
出处 《化工学报》 EI CAS CSCD 北大核心 2007年第11期2738-2746,共9页 CIESC Journal
基金 国家自然科学基金项目(20606006 20490200)~~
关键词 颗粒旋转 颗粒动理学 鼓泡流化床 particle rotation kinetic theory of granular flow bubbling fluidized bed
  • 相关文献

参考文献17

  • 1由长福,祁海鹰,徐旭常.Basset力研究进展与应用分析[J].应用力学学报,2002,19(2):31-33. 被引量:34
  • 2袁竹林,马明,徐益谦.离散数值模拟颗粒自转对流化床内颗粒流态的影响[J].燃烧科学与技术,2001,7(3):238-241. 被引量:11
  • 3骆仲泱,吴学成,王勤辉,高琼,方梦祥,岑可法.循环流化床中颗粒旋转特性[J].化工学报,2005,56(10):1869-1874. 被引量:15
  • 4Gidaspow D. Multiphase Flow and Fluidization: Continuum and Kinetic Theory Descriptions. Boston: Academic Press, 1994. 被引量:1
  • 5Lun C K. Kinetic theory for granular flow of dense, slightly inelastic, slightly rough, spheres. Journal of Fluid Mechanics, 1991, 233:539-559. 被引量:1
  • 6Jenkins J T. Boundary conditions for rapid granular flow flat, frictional walls. Journal of Applied Mechanics, 1992, 59:120-127. 被引量:1
  • 7Lun C K K, Savage S B, Jeffrey D J, Chepurniy N. Kinetic theories for granular flow: inelastic particles in Couette flow and slightly inelastic particles in a general flow field. J. Fluid Mech. , 1984, 140:223-231. 被引量:1
  • 8Sela N, Goldhirsch I. Hydrodynamic equations for rapid flows of smooth inelastic spheres, to Burnett order. J. Fluid Mech., 1998, 361:41-52. 被引量:1
  • 9Bagnold R A. Experiments on a gravity free dispersion of large solid spheres in a Newtonian fluid under shear.Proceedings of the Royal Society of London, 1954, A225:49-63. 被引量:1
  • 10Huilin L, Gidaspow D, Bouillard J, Wentie L Hydrodynamic simulation of gas-solid flow in a riser using kinetic theory of granular flow. Chemical Engineering Journal, 2003, 95:1-13. 被引量:1

二级参考文献17

  • 1Yuan Zhulin,J Developments Chemical Engineering Mineral Processing,2000年,8卷,3/4期,207页 被引量:1
  • 2Horio M, Kuroki H. Three-dimensional flow visualization for dilute dispersed solids in bubbling and fluidized beds. Chem. Eng. Sci.,1994,49(15):2413-2421 被引量:1
  • 3Kuroki H, Horio M. The flow structure of a three-dimensional circulation fluidized bed observed by the laser sheet technique. In:Avidan A A,ed.Circulation Fluidized Bed Technology Ⅳ.Proc. 4th Int. Conf. Circulating Fluidized Beds. Oxford: Pergamon Press,1993.77-84 被引量:1
  • 4Werther J. Measurement techniques in fluidized beds. Powder Technology,1999,102(1):15-36 被引量:1
  • 5Gera D, Gautam M, Tsuji Y, Kawaguchi T, Tanaka T. Computer simulation of bubbles in large-particle fluidized beds. Powder Technology,1998,98(1):38-47 被引量:1
  • 6CenKefa(岑可法) FanJianren(樊建人).Theory and Calculation of Engineering Gas-Solid Multiphase Flow(工程气固多相流动的理论及计算)[M].Hangzhou:Zhejiang University Press,1990.. 被引量:1
  • 7Hussainov M, Kartushinsky A, Mulgi A, Rudi U. Gas-solid flow with the slip velocity of particles in a horizontal channel. J. Aerosol Sci.,1996,27(1):41-59 被引量:1
  • 8Satoru Matsuda,Hiroyuki Hatano,Takeuchi H,Pyatenko A T,Tsuchiya K.Motion of individual solid particles in a circulating fluidized bed riser. In: Kwauk M, Li J, eds. Proc. 5th Int. Conf. on Circulating Fluidized Beds. Beijing: Science Press, 1996. 176-181 被引量:1
  • 9CenKefa(岑可法) FanJianren(樊建人).The analysis of the forces acting on coal particles and the trajectories in gas flows[J].浙江大学学报,1987,21(6):1-11. 被引量:1
  • 10Goldschmidt M J V, Beetstra R, Kuipers J A M. Hydrodynamic modelling of dense gas-fluidised beds: comparison and validation of 3D discrete particle and continuum models.Powder Technology,2004,142(1):23-47 被引量:1

共引文献50

同被引文献83

引证文献7

二级引证文献25

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