期刊文献+

流化床内气固两相绕流单沉浸管的流体动力计算 被引量:2

Hydrodynamics of Gas-Solid Flow Around a Single Immersed Pipe in Bubbling Fluidized Bed
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摘要 应用贴体坐标系,基于颗粒相采用颗粒动力学的气固两相双流体模型,数值模拟单沉浸管流化床内颗粒及气泡的行为,计算得到的瞬时颗粒浓度和速度揭示了气泡绕流沉浸管时出现的合并和破裂过程.瞬时颗粒浓度的功率谱密度表明,颗粒脉动的主频率为0.4~1.0Hz,大于床内无沉浸管颗粒的频率值.数值模拟得到的气泡频率与文献中实测值相吻合. A numerical study was conducted based on the gassolid twofluid model using bodyfitted coordination to analyze the behavior of particles and bubbles in fluidized beds with an immersed tube.The kinetic theory of granular flow was implemented in the model.The images of simulated instantaneous particle concentration and velocity give the whole processes of the amalgamation and breaks of bubbles.The main frequencies of instantaneous particle concentrations are in the range of 0.4-1.0 Hz which are larger than that in the bed without tube.Calculated particle velocity and bubble frequencies around a tube were in good agreement with previous experimental findings.
出处 《燃烧科学与技术》 EI CAS CSCD 2003年第5期475-481,共7页 Journal of Combustion Science and Technology
基金 国家自然科学基金资助项目(10072019).
关键词 流化床 贴体坐标系 沉浸管 fluidized bed body-fitted coordination immersed tube
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参考文献6

  • 1Lyczkowski R W, Folga S, Chang S Let aL State-of-the-art compution of dynamics and erosion in fluidized bed tube banks[ A]. Procevdings of the 10th International Conference on Feuidized Bed Combustion[ C ], San Francisco, 1989:465-478.
  • 2Ding J, Lyczkowski R W. Three-dimensional kinetic theory modeling of hydrodynamics and erosion in fluidized beds [ J ]. Power Technology,1992,73 : 127-138.
  • 3Li C ,Zakkay V. Hydrodynanfics and erosion modeling of fluidized bed combustions [ J ]. Journal of Fluids Engineering, 1994, 116:746-755.
  • 4Rong D, Mikami T, Horio M. Particle and bubble movements around tubes immersed in fluidized bed:a numerical study [ J ]. Chemical Engineering Science, 1999,54:5737-5754.
  • 5Wen C Y, Yu Y H. Mechanics of fluidization [ J ]. Chem Eng Prog Symp Ser,1996,62:100-113.
  • 6Olowson P A. Influence of pressure and fluidization velocity on the hydrodynamics of a fluidized bed containing horizontal tubes[ J]. Chemical Engineering Science,1994,49:2437-2446.

同被引文献15

  • 1赵永志,程易,金涌.提升管与下行床颗粒团聚行为的离散颗粒模拟[J].化工学报,2007,58(1):44-53. 被引量:25
  • 2Lyczkowski R W, Folga S, Chang S L,et al. State-of-theart computation of dynamics and erosion in fluidized bed tube banks [ A ]. Proceedings of the 10^th International Conference on Fluidized Bed Combustion [ C ]. San Francisco:ASME Press, 1989. 465-478.
  • 3Ding J, Lyczkowski R W. Three-dimensional kinetic theory modeling of hydrodynamics and erosion in fluidized beds [J]. Powder Technology, 1992, 73(2): 127-138.
  • 4Li C, Zakkay V. Hydrodynamics and erosion modeling of fluidized bed combustions [ J ]. Journal of Fluids Engineering, 1994, 116(4) : 746-755.
  • 5He Y, Lu H, Sun Q, et al. Hydrodynamics of gas-solid flow around immersed tubes in bubbling fluidized beds [ J ]. Powder Technology, 2004, 145 (2) : 88-105.
  • 6Cundall P A, Strack O D L. A discrete numerical model for granular assemblies [J]. Geotechnique, 1979, 29 ( 1 ) : 47-65.
  • 7Tsuji Y, Kawaguchi T, Tanaka T. Discrete particle simulation of two dimensional fluidized bed [ J ]. Powder Technology, 1993, 77(1): 79-87.
  • 8Rong D, Mikami T, Horio M. Particle and bubble movements around tubes immersed in fluidized beds-a numerical study [ J ]. Chemical Engineering Science, 1999, 54(23) : 5737-5754.
  • 9Rong D, Horio M. Behavior of particles and bubbles around immersed tubes in a fluidized bed at high temperature and pressure: A DEM simulation [J]. International Journal of Multiphase Flow, 2001, 27( 1 ) : 89-105.
  • 10赵永志,程易.沉浸管式流化床的颗粒尺度模拟[J].化学工程,2007,35(11):21-24. 被引量:4

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