Numerical investigation for the suitable choice of bubble diameter correlation for EMMS/bubbling drag model

被引:4
作者
Ahmad, Nouman [1 ,2 ]
Deng, Jianqiang [1 ,2 ]
Adnan, Muhammad [2 ]
机构
[1] Shaanxi Key Lab Energy Chem Proc Intensificat, Xian 710049, Peoples R China
[2] Xi An Jiao Tong Univ, Sch Chem Engn & Technol, Xian 710049, Peoples R China
来源
CHINESE JOURNAL OF CHEMICAL ENGINEERING | 2022年 / 47卷
基金
中国国家自然科学基金;
关键词
Mesoscale; Bubbles; Energy minimization multiscale (EMMS); Heterogeneity index; Bubbling fluidized bed; SOLID FLUIDIZED-BED; CFD SIMULATION; MULTISCALE CFD; EMMS MODEL; FLOW; PARTICLES; GELDART; RISER; SIZE; VALIDATION;
D O I
10.1016/j.cjche.2021.10.006
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Mesoscale bubbles exist inherently in bubbling fluidized beds and hence should be considered in the constitutive modeling of the drag force. The energy minimization multiscale bubbling (EMMS/bubbling) drag model takes the effects of mesoscale structures (i.e., bubbles) into the modeling of drag coefficient and thus improves the coarse-grid simulation of bubbling and turbulent fluidized beds. However, its dependence on the bubble diameter correlation has not been thoroughly investigated. The hydrodynamic disparity between homogeneous and heterogeneous fluidization is accounted for by the heterogeneity index, Hd, which can be affected by choice of bubble diameter correlation. How this choice of bubble diameter correlation influences the model prediction calls for further fundamental research. This article incorporated seven different bubble diameter correlations into EMMS/bubbling drag model and studied their effects on Hd. The performance of these correlations has been compared with the correlation used previously by EMMS/bubbling drag model. We found that some of the correlations predicted lower Hd by order of a magnitude than the correlation used by the original EMMS/bubbling drag. Based on such analysis, we proposed a modification in the EMMS drag model for bubbling and turbulent fluidized beds. A computational fluid dynamics (CFD) simulation using two-fluid model with the modified EMMS/bubbling drag model was performed for two bubbling and one turbulent fluidized beds. Voidage distribution, time averaged solid concentration and axial solid concentration profiles were studied and compared with the previous version of the EMMS/bubbling drag model and experimental data. We found that the right choice of bubble diameter correlations can significantly improve the results for CFD simulations. (C) 2021 The Chemical Industry and Engineering Society of China, and Chemical Industry Press Co., Ltd. All rights reserved.
引用
收藏
页码:254 / 270
页数:17
相关论文
共 50 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] Mixing and segregation in a bidisperse gas-solid fluidised bed: a numerical and experimental study
    Bokkers, GA
    Annaland, MVS
    Kuipers, JAM
    [J]. POWDER TECHNOLOGY, 2004, 140 (03) : 176 - 186
  • [3] QUANTITATIVE ESTIMATION OF BUBBLE-SIZE IN PFBC
    CAI, P
    SCHIAVETTI, M
    DEMICHELE, G
    GRAZZINI, GC
    MICCIO, M
    [J]. POWDER TECHNOLOGY, 1994, 80 (02) : 99 - 109
  • [4] DARTON RC, 1977, T I CHEM ENG-LOND, V55, P274
  • [5] Traveling column for comparison of invasive and non-invasive fluidization voidage measurement techniques
    Dubrawski, K.
    Tebianian, S.
    Bi, H. T.
    Chaouki, J.
    Ellis, N.
    Gerspacher, R.
    Jafari, R.
    Kantzas, A.
    Lim, C.
    Patience, G. S.
    Pugsley, T.
    Qi, M. Z.
    Zhu, J. X.
    Grace, J. R.
    [J]. POWDER TECHNOLOGY, 2013, 235 : 203 - 220
  • [6] Development and validation of an enhanced filtered drag model for simulating gas-solid fluidization of Geldart A particles in all flow regimes
    Gao, Xi
    Li, Tingwen
    Sarkar, Avik
    Lu, Liqiang
    Rogers, William A.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2018, 184 : 33 - 51
  • [7] Gauthier TA, 2009, INT J CHEM REACT ENG, V7
  • [8] Physical mapping of fluidization regimes - the EMMS approach
    Ge, W
    Li, JH
    [J]. CHEMICAL ENGINEERING SCIENCE, 2002, 57 (18) : 3993 - 4004
  • [9] EFFECT OF PARTICLE-SIZE AND SIZE DISTRIBUTION ON BEHAVIOR OF GAS-FLUIDIZED BEDS
    GELDART, D
    [J]. POWDER TECHNOLOGY, 1972, 6 (04) : 201 - &
  • [10] Gidaspow D., 1994, MULTIPHASE FLOW FLUI