Machine Learning and Data-Driven Modeling to Discover the Bed Expansion Ratio Correlation for Gas-Liquid-Solid Three-Phase Flows

被引:9
作者
Xie, Le [1 ]
Zhou, Guangming [1 ]
Wang, Dongdong [2 ]
Wang, Huaifa [3 ]
Jiang, Chongwen [1 ]
机构
[1] Cent South Univ, Coll Chem & Chem Engn, Changsha 410083, Hunan, Peoples R China
[2] Civil Aviat Univ China, Tianjin 300300, Peoples R China
[3] Taiyuan Univ Technol, Coll Min Engn, Taiyuan 030024, Shanxi, Peoples R China
基金
中国国家自然科学基金;
关键词
ELECTRICAL-RESISTANCE TOMOGRAPHY; BUBBLE-COLUMN REACTORS; FLUIDIZED-BED; PHASE HOLDUPS; REGIME IDENTIFICATION; MINIMUM FLUIDIZATION; NUMERICAL-SIMULATION; MULTIPHASE SYSTEMS; SCALE-UP; HYDRODYNAMICS;
D O I
10.1021/acs.iecr.2c03668
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
It is significant to study gas-liquid-solid three-phase flow characteristics for an in-depth understanding of the fluidization mechanism. For this purpose, this study measured 624-bed expansion ratio data under different operating conditions. Based on this data set, the XGBoost machine learning model was trained to investigate the effects of four major dimensionless numbers (ReL, Frg, Ar, and Eo) on the bed expansion ratio. The relative importance analysis was used for dimensionality reduction. Then, a bed expansion ratio correlation was proposed by multiple linear regression. Additionally, a data-driven model based on two-level optimization algorithm was employed to automatically discover bed expansion ratio correlation from measured exper-imental data. The data-driven modeling method had the advantages in directly finding the dominant dimensionless number groups and thus yielding a high precision correlation.
引用
收藏
页码:789 / 800
页数:12
相关论文
共 67 条
  • [31] Numerical simulation of gas-liquid-solid fluidization systems using a combined CFD-VOF-DPM method: bubble wake behavior
    Li, Y
    Zhang, JP
    Fan, LS
    [J]. CHEMICAL ENGINEERING SCIENCE, 1999, 54 (21) : 5101 - 5107
  • [32] Numerical studies of bubble formation dynamics in gas-liquid-solid fluidization at high pressures
    Li, Y
    Yang, GQ
    Zhang, JP
    Fan, LS
    [J]. POWDER TECHNOLOGY, 2001, 116 (2-3) : 246 - 260
  • [33] Particle fluctuations and dispersion in three-phase fluidized beds with viscous and low surface tension media
    Lim, Hyun Oh
    Seo, Myung Jae
    Kang, Yong
    Jun, Ki Won
    [J]. CHEMICAL ENGINEERING SCIENCE, 2011, 66 (14) : 3234 - 3242
  • [34] Application of the energy-minimization multi-scale method to gas-liquid-solid fluidized beds
    Liu, MY
    Li, JH
    Kwauk, MS
    [J]. CHEMICAL ENGINEERING SCIENCE, 2001, 56 (24) : 6805 - 6812
  • [35] Axial meso-scale modeling of gas-liquid-solid circulating fluidized beds
    Ma, Yongli
    Liu, Mingyan
    Zhou, Xiuhong
    Javed, Areej
    [J]. CHEMICAL ENGINEERING SCIENCE, 2019, 208
  • [36] Axial meso-scale modeling of gas-liquid-solid fluidized beds
    Ma, Yongli
    Liu, Mingyan
    Zhang, Yuan
    [J]. CHEMICAL ENGINEERING SCIENCE, 2019, 196 : 188 - 201
  • [37] An improved meso-scale flow model of gas-liquid-solid fluidized beds
    Ma, Yongli
    Liu, Mingyan
    Zhang, Yuan
    [J]. CHEMICAL ENGINEERING SCIENCE, 2018, 179 : 243 - 256
  • [38] Dimensional hydrodynamic similitude in three-phase fluidized beds
    Macchi, A
    Bia, HT
    Grace, JR
    McKnight, CA
    Hackman, L
    [J]. CHEMICAL ENGINEERING SCIENCE, 2001, 56 (21-22) : 6039 - 6045
  • [39] Flow regimes in slurry bubble column: Effect of column height and particle concentration
    Orvalho, Sandra
    Hashida, Masaaki
    Zednikova, Maria
    Stanovsky, Petr
    Ruzicka, Marek C.
    Sasaki, Shohei
    Tomiyama, Akio
    [J]. CHEMICAL ENGINEERING JOURNAL, 2018, 351 : 799 - 815
  • [40] Machine learning for full spatiotemporal acceleration of gas-particle flow simulations
    Ouyang, Bo
    Zhu, Li -Tao
    Luo, Zheng-Hong
    [J]. POWDER TECHNOLOGY, 2022, 408