A local cluster-structure-dependent drag model for Eulerian simulation of gas-solid flow in CFB risers

被引:17
作者
Du, Shaohua [1 ]
Liu, Lijun [1 ]
机构
[1] Xi An Jiao Tong Univ, Minist Educ, Sch Energy & Power Engn, Key Lab Thermofluid Sci & Engn, Xian 710049, Shaanxi, Peoples R China
基金
中国国家自然科学基金;
关键词
Gas-solid flow; Drag model; Hydrodynamics; Numerical simulation; Meso-scale structure; LATTICE BOLTZMANN SIMULATIONS; FLUIDIZED-BEDS; EMMS MODEL; NUMBER; HYDRODYNAMICS; ARRAYS;
D O I
10.1016/j.cej.2019.03.009
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Numerical simulating of gas-solid fluidization is crucial to the development of circulating fluidized beds. Accurate simulation entails a structure-dependent drag model based on the sub-grid scale. In this work, a local cluster-structure-dependent drag model is proposed based on the scale resolution of local grid cells, which are resolved into three subsystems to take the effect of heterogeneous flow structure into consideration. The accurate drag correlation based on direct numerical simulation, instead of the Wen & Yu drag correlation, is coupled with the novel drag model to calculate the drag coefficient when the flow structure turns to be homogeneous. In addition, the effect of local solid concentration gradient on the interphase drag force at low voidage is also considered. Then the novel drag model is solved by a genetic algorithm and the obtained drag coefficient is incorporated into the two-fluid model to simulate the gas-solid flow in circulating fluidized bed risers with Geldart A and B particles to validate its accuracy. The results show that the proposed drag model is feasible to capture the heterogeneous flow structure and provide more accurate prediction of solid fluxes and solid concentrations than Gidaspow drag model. In addition, taking the effect of solid concentration gradient into consideration improves the accuracy of prediction, especially in the simulation of CFB risers with Geldart B particles.
引用
收藏
页码:687 / 699
页数:13
相关论文
共 37 条
  • [1] Characterization of gas fluidization regimes using pressure fluctuations
    Bai, D
    Shibuya, E
    Nakagawa, N
    Kato, K
    [J]. POWDER TECHNOLOGY, 1996, 87 (02) : 105 - 111
  • [2] Analysis of Model Parameters Affecting the Pressure Profile in a Circulating Fluidized Bed
    Benyahia, Sofiane
    [J]. AICHE JOURNAL, 2012, 58 (02) : 427 - 439
  • [3] Improvement of EMMS drag model for heterogeneous gas-solid flows based on cluster modeling
    Chen, Cheng
    Dai, Qunte
    Qi, Haiying
    [J]. CHEMICAL ENGINEERING SCIENCE, 2016, 141 : 8 - 16
  • [4] A fundamental CFD study of the gas-solid flow field in fluidized bed polymerization reactors
    Chen, Xi-Zhong
    Shi, De-Pan
    Gao, Xi
    Luo, Zheng-Hong
    [J]. POWDER TECHNOLOGY, 2011, 205 (1-3) : 276 - 288
  • [5] A multiscale mass transfer model for gas-solid riser flows: Part 1 - Sub-grid model and simple tests
    Dong, Weigang
    Wang, Wei
    Li, Jinghai
    [J]. CHEMICAL ENGINEERING SCIENCE, 2008, 63 (10) : 2798 - 2810
  • [6] ERGUN S, 1952, CHEM ENG PROG, V48, P89
  • [7] Development of fluidized bed reactors for silicon production
    Filtvedt, W. O.
    Javidi, M.
    Holt, A.
    Melaaen, M. C.
    Marstein, E.
    Tathgar, H.
    Ramachandran, P. A.
    [J]. SOLAR ENERGY MATERIALS AND SOLAR CELLS, 2010, 94 (12) : 1980 - 1995
  • [8] CFD simulation of a fluidized bed using the EMMS approach for the gas-solid drag force
    Ghadirian, Emad
    Arastoopour, Hamid
    [J]. POWDER TECHNOLOGY, 2016, 288 : 35 - 44
  • [9] Gidaspow D., 1994, Multiphase Flow and Fluidization: Continuum and Kinetic Theory Descriptions, DOI DOI 10.1016/B978-0-08-051226-6.50015-7
  • [10] Quantifying cluster dynamics to improve EMMS drag law and radial heterogeneity description in coupling with gas-solid two-fluid method
    Hu, Shanwei
    Liu, Xinhua
    Zhang, Nan
    Li, Jinghai
    Ge, Wei
    Wang, Wei
    [J]. CHEMICAL ENGINEERING JOURNAL, 2017, 307 : 326 - 338