Numerical study of mixing and segregation in a biomass fluidized bed

被引:40
作者
Bai, Wei [1 ]
Keller, Norman K. G. [2 ]
Heindel, Theodore J. [1 ,2 ]
Fox, Rodney O. [1 ]
机构
[1] Iowa State Univ, Dept Chem & Biol Engn, Ames, IA 50011 USA
[2] Iowa State Univ, Dept Mech Engn, Ames, IA 50011 USA
关键词
Fluidized bed modeling; Biomass particle; Mixing; Segregation; RAY COMPUTED-TOMOGRAPHY; SIDE-AIR INJECTION; GAS HOLDUP; SIMULATIONS; PARTICLES; MIXTURES; REACTOR; SPHERES; FLOWS; SAND;
D O I
10.1016/j.powtec.2012.12.018
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Due to its renewable characteristics, biomass is potentially important to energy conversion processes. Fluidized beds are involved in many processes related to energy conversion of biomass. Hence, detailed insight on the hydrodynamics of biomass fluidized beds is crucial for successful energy conversion as well as to better design and scale-up of fluidized bed reactors. The present work focuses on modeling the mixing and segregation behavior of biomass mixtures in a fluidized bed. Different effects, such as mixture composition, particle size, and superficial gas velocity, on the mixing and segregation are simulated and the results are compared to measurements obtained using X-ray computed tomography. Furthermore, side injection of biomass particles into a fluidized bed is also studied and compared with visual observations. A comparison between the numerical simulations and measurements shows good agreement. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:355 / 366
页数:12
相关论文
共 32 条
  • [1] The role of meso-scale structures in rapid gas-solid flows
    Agrawal, K
    Loezos, PN
    Syamlal, M
    Sundaresan, S
    [J]. JOURNAL OF FLUID MECHANICS, 2001, 445 : 151 - 185
  • [2] Drag force of intermediate Reynolds number flow past mono- and bidisperse arrays of spheres
    Beetstra, R.
    van der Hoef, M. A.
    Kuipers, J. A. M.
    [J]. AICHE JOURNAL, 2007, 53 (02) : 489 - 501
  • [3] Benyahia S., 2009, SUMMARY MFIX EQUATIO
  • [4] Fluidization of biomass particles: A review of experimental multiphase flow aspects
    Cui, Heping
    Grace, John R.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2007, 62 (1-2) : 45 - 55
  • [5] CFD Modeling and X-Ray Imaging of Biomass in a Fluidized Bed
    Deza, Mirka
    Franka, Nathan P.
    Heindel, Theodore J.
    Battaglia, Francine
    [J]. JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 2009, 131 (11): : 1113031 - 11130311
  • [6] Local time-average gas holdup comparisons in cold flow fluidized beds with side-air injection
    Drake, Joshua B.
    Heindel, Theodore J.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2012, 68 (01) : 157 - 165
  • [7] The repeatability and uniformity of 3D fluidized beds
    Drake, Joshua B.
    Heindel, Theodore J.
    [J]. POWDER TECHNOLOGY, 2011, 213 (1-3) : 148 - 154
  • [8] Bed height and material density effects on fluidized bed hydrodynamics
    Escudero, David
    Heindel, Theodore J.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2011, 66 (16) : 3648 - 3655
  • [9] EMPIRICAL-METHOD OF ESTIMATING THE VOID FRACTION IN MIXTURES OF UNIFORM PARTICLES OF DIFFERENT SIZE
    FEDORS, RF
    LANDEL, RF
    [J]. POWDER TECHNOLOGY, 1979, 23 (02) : 225 - 231
  • [10] X-ray computed tomography of a gas-sparged stirred-tank reactor
    Ford, Jason J.
    Heindel, Theodore J.
    Jensen, Terrence C.
    Drake, Joshua B.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2008, 63 (08) : 2075 - 2085