Investigation of drying process of non-spherical particle in a pulsed fluidized bed

被引:0
作者
Jin, Hanyu [1 ]
Wang, Shuai [1 ,2 ]
He, Yurong [1 ]
机构
[1] Harbin Inst Technol, Sch Energy Sci & Engn, Harbin 150001, Peoples R China
[2] Harbin Inst Technol, Zhengzhou Res Inst, Zhengzhou 450000, Peoples R China
来源
PARTICUOLOGY | 2025年 / 98卷
关键词
Drying; Non-spherical particle; Gas pulsation; Fluidized bed; HEAT-TRANSFER; MODEL;
D O I
10.1016/j.partic.2025.01.013
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Gas pulsation is an efficient enhancing way for fluidized bed drying process. In this work, the influence of gas pulsation on mass and heat transfer performance in a fluidized bed with non-spherical wet particles is numerically investigated via the computational fluid dynamics-discrete element method (CFD-DEM) approach, where the liquid transfer between particles and the heat transfer by liquid bridge are considered. The aspect ratio effect of non-spherical particle on drying process is revealed. It is found that the increase of aspect ratio can weaken the overall drying quality. The influence of gas pulsation on the drying of non-spherical particle is analyzed. The results reveal that adjusting a suitable gas pulsation mode can efficiently regulate the drying process of non-spherical wet particles with greater aspect ratios. (c) 2025 Chinese Society of Particuology and Institute of Process Engineering, Chinese Academy of Sciences. Published by Elsevier B.V. All rights are reserved, including those for text and data mining, AI training, and similar technologies.
引用
收藏
页码:134 / 141
页数:8
相关论文
共 23 条
  • [1] Bouamrane O.L., Mekhaneg B., Panigrahi S.S., Hemis M., Singh C.B., Fluidization-bed drying and microwave radiation effects on drying rate, fatty acid, protein, and germination of flaxseed, Journal of Food Process Engineering, 47, (2024)
  • [2] Chen K., Bachmann P., Buck A., Jacob M., Tsotsas E., Experimental study and modeling of particle drying in a continuously-operated horizontal fluidized bed, Particuology, 34, pp. 134-146, (2017)
  • [3] Cheng G.J., Yu A.B., Zulli P., Evaluation of effective thermal conductivity from the structure of a packed bed, Chemical Engineering Science, 54, 19, pp. 4199-4209, (1999)
  • [4] de Munck M.J.A., Peters E.A.J.F., Kuipers J.A.M., Experimental study on vibrating fluidized bed solids drying, Chemical Engineering Journal, 472, (2023)
  • [5] de Munck M.J.A., Marrevee D.P.F., Peters E.A.J.F., Kuipers J.A.M., Experimental study on binary solids drying in a vibro-fluidized bed, Powder Technology, 435, (2024)
  • [6] de Munck M.J.A., Peters E.A.J.F., Kuipers J.A.M., CFD-DEM modeling and validation of solids drying in a gas-fluidized bed, Chemical Engineering Science, 291, (2024)
  • [7] Di Felice R., The voidage function for fluid-particle interaction systems, International Journal of Multiphase Flow, 20, pp. 153-159, (1994)
  • [8] Farivar F., Zhang H., Tian Z.F., Gupte A., CFD-DEM simulation of fluidization of multisphere-modelled cylindrical particles, Powder Technology, 360, pp. 1017-1027, (2020)
  • [9] Gao X., Yu J., Lu L., Li C., Rogers W.A., Development and validation of SuperDEM-CFD coupled model for simulating non-spherical particles hydrodynamics in fluidized beds, Chemical Engineering Journal, 420, (2021)
  • [10] Gidaspow D., Multiphase flow and fluidization: Continuum and kinetic theory description, (1994)