Data science integrated with computational fluid dynamics for particle collision modeling in fluidized bed

被引:0
|
作者
Nimmanterdwong, Prathana [1 ]
Yurata, Tarabordin [2 ]
Chaiprasitpol, Nuttanun [2 ]
Pranomsri, Nawin [2 ]
Chalermsinsuwan, Benjapon [2 ,3 ]
机构
[1] Mahidol Univ, Fac Engn, Dept Chem Engn, 25-25 Puttamonthon 4 Rd, Nakhon Pathom 73170, Thailand
[2] Chulalongkorn Univ, Fac Sci, Dept Chem Technol, 254 Phyathai Rd, Bangkok 10330, Thailand
[3] Chulalongkorn Univ, Ctr Excellence Petrochem & Mat Technol, 254 Phyathai Rd, Bangkok 10330, Thailand
关键词
Coefficient of restitution; Data science; Machine learning; Neural network; CFD-DEM; RESTITUTION COEFFICIENT; SIMULATION;
D O I
10.1016/j.apt.2024.104419
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Fluidized beds are critical in numerous industrial applications, including chemical processing and energy production. Accurate modeling of solid particles and fluids within these beds is essential for process optimization and improved efficiency. In this study, we developed a machine learning model to predict the coefficient of restitution (COR) of solid particles in fluidized beds. Four variables-collision velocity, effective temperature, effective mass, and effective elastic modulus-were used in the model. Our dataset comprised 2446 data points from previous literature. We employed self-organizing map (SOM) and artificial neural network (ANN) approaches for data analysis. The initial ANN model, which did not incorporate data clustering, exhibited an impressive coefficient of determination (R-squared) of 0.989, indicating its high accuracy. To enhance the model further, we clustered the data into four groups using SOM and developed separate ANN models for each group. All four models achieved R-squared greater than 0.99, illustrating the effectiveness of data clustering. The resulting model can be integrated into simulation software, such as MFIX, to provide a more precise representation of fluidized bed behavior across various industrial settings. The findings emphasize the potential of machine learning models to enhance fluidized bed simulations, leading to increased efficiency and cost-effectiveness in industrial processes. Future studies should explore the inclusion of additional variables and extend the model's application to different industrial processes. Additionally, incorporating recommendations for optimizing fluidized bed behavior based on the model's predictions would provide valuable insights for process engineers. (c) 2024 The Society of Powder Technology Japan. Published by Elsevier B.V. and The Society of Powder Technology Japan. All rights reserved.
引用
收藏
页数:13
相关论文
共 50 条
  • [31] Coupled Computational Fluid Dynamics and Discrete Element Method Study of the Solid Dispersion Behavior in an Internally Circulating Fluidized Bed
    Yang, Shiliang
    Luo, Kun
    Qiu, Kunzan
    Fang, Mingming
    Fan, Jianren
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (16) : 6759 - 6772
  • [32] Computational fluid dynamics (CFD) study of a commercial-scale methanol-to-olefins (MTO) fluidized bed reactor
    Wan, Zhanghao
    Yang, Shiliang
    Hu, Jianhang
    Wang, Hua
    FUEL, 2022, 327
  • [33] Discrete particle modeling of granular temperature distribution in a bubbling fluidized bed
    He, Yurong
    Wang, Tianyu
    Deen, Niels
    Annaland, Martin van Sint
    Kuipers, Hans
    Wen, Dongsheng
    PARTICUOLOGY, 2012, 10 (04) : 428 - 437
  • [34] Fluid dynamics and thermal characteristics of a conical bubbling fluidized bed riser
    Das, Hirakh Jyoti
    Mahanta, Pinakeswar
    Saikia, Rituraj
    INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2022, 137
  • [35] Multi-fluid reactive modeling of fluidized bed pyrolysis process
    Sharma, Abhishek
    Wang, Shaobin
    Pareek, Vishnu
    Yang, Hong
    Zhang, Dongke
    CHEMICAL ENGINEERING SCIENCE, 2015, 123 : 311 - 321
  • [36] Two-fluid modeling of a wet spouted fluidized bed with wet restitution coefficient model
    Zhong, Hanbin
    Zhang, Yaning
    Xiong, Qingang
    Zhang, Juntao
    Zhu, Yuqin
    Liang, Shengrong
    Niu, Ben
    Zhang, Xinyu
    POWDER TECHNOLOGY, 2020, 364 : 363 - 372
  • [37] Three-dimensional computational fluid dynamics (CFD) study of the gas-particle circulation pattern within a fluidized bed granulator: By full factorial design of fluidization velocity and particle size
    Liu, Huolong
    Yoon, Seongkyu
    Li, Mingzhong
    DRYING TECHNOLOGY, 2017, 35 (09) : 1043 - 1058
  • [38] Computational fluid dynamics for dense gas-solid fluidized beds: a multi-scale modeling strategy
    van der Hoef, MA
    Annaland, MV
    Kuipers, JAM
    CHEMICAL ENGINEERING SCIENCE, 2004, 59 (22-23) : 5157 - 5165
  • [39] Multi-fluid Modeling Biomass Fast Pyrolysis in the Fluidized-Bed Reactor Including Particle Shrinkage Effects
    Zhong, Hanbin
    Zhang, Juntao
    Zhu, Yuqin
    Liang, Shengrong
    ENERGY & FUELS, 2016, 30 (08) : 6440 - 6447
  • [40] Computational study of particle temperature in a bubbling spout fluidized bed with hot gas injection
    Patil, A. V.
    Peters, E. A. J. F.
    Kuipers, J. A. M.
    POWDER TECHNOLOGY, 2015, 284 : 475 - 485