Numerical simulation on characteristics of hydrodynamics, interphase and wall to bed heat transfer in a pseudo 2D spouted bed using supercritical CO2 as fluidizing agent

被引:0
|
作者
Jiang, Kun [1 ]
Jin, Hui [1 ]
机构
[1] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, Xian 710049, Peoples R China
来源
PARTICUOLOGY | 2025年 / 96卷
基金
国家重点研发计划;
关键词
Spouted bed; Two fluid model; Kinetic theory of granular flow; Supercritical CO 2; Hydrodynamics; Heat transfer; CFD-DEM MODEL; KINETIC-THEORY; PHARMACEUTICAL POWDERS; MINIMUM FLUIDIZATION; GRANULAR FLOW; MASS-TRANSFER; VELOCITY; PARTICLES; PERFORMANCE; COMBUSTION;
D O I
10.1016/j.partic.2024.10.019
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
By employing the Eulerian-Eulerian Two Fluid Model, the effect of different particle size, supercritical CO2 (scCO2) velocity at slit jet (Ujet) and initial bed height on the macroscopic characteristics (i.e., fountain morphology, profiles of particle velocity, momentum transfer characteristics among particles, transient temperature evolutions of particles, interphase heat transfer coefficient and wall to bed heat transfer characteristics) in the pseudo 2D rectangular spouted bed using scCO2 as fluidizing agent is numerically studied in detail herein. Considering there are currently no relevant visualized experiments reported using scCO2 as a fluidized agent due to the extreme operating pressure of CO2 (25 MPa in this paper) under supercritical conditions, present numerical model was validated with experimental data by using air as the fluidizing agent, confirming simulated instantaneous volume fraction distribution of air and transient temperature evolutions of particles basically consistent with the experiments. Numerical results reveal some of the internal relations among hydrodynamics characteristics in bed, momentum transfer characteristics among particles and relevant heat transfer behaviours. Results show larger Ujet and smaller particle size will accelerate the particles' translational motion in spout, spout core and fountain core zone. Larger particle concentration will promote inter-particle collisions while suppress the kinetic motion of particles in above zones. Decrease the particle size will enhance interphase convective heat transfer coefficient, while increasing Ujet results insignificant impacts. Finally, we also observe the transition zone between annular and periphery zone has a certain enhancing effect on the wall to bed heat transfer coefficient. (c) 2024 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:106 / 125
页数:20
相关论文
共 50 条
  • [21] Computational and Experimental Study of Heat Transfer and Hydrodynamics in a 2D Gas-Solid Fluidized Bed Reactor
    Hamzehei, Mahdi
    Rahimzadeh, Hassan
    Ahmadi, Goodarz
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (11) : 5110 - 5121
  • [22] Numerical simulation of sandy bed erosion by 2D vertical jet
    HUAI WenXin
    Science China(Technological Sciences), 2011, (12) : 3265 - 3274
  • [23] Numerical simulation of sandy bed erosion by 2D vertical jet
    Huai WenXin
    Wang ZengWu
    Qian ZhongDong
    Han YaQiong
    SCIENCE CHINA-TECHNOLOGICAL SCIENCES, 2011, 54 (12) : 3265 - 3274
  • [24] Numerical simulation of sandy bed erosion by 2D vertical jet
    WenXin Huai
    ZengWu Wang
    ZhongDong Qian
    YaQiong Han
    Science China Technological Sciences, 2011, 54 : 3265 - 3274
  • [25] Heat transfer characteristics of supercritical CO2 in square microchannels
    Xu, Wanting
    Xu, Bo
    Wang, Xin
    Chen, Zhenqian
    Huagong Xuebao/CIESC Journal, 2022, 73 (04): : 1534 - 1545
  • [26] Numerical Analysis of Heat Transfer Characteristics to Supercritical CO2 in a Vertical Mini-Channel: Transition and Pseudo-Boiling
    Baoqiang Yuan
    Wei Wang
    Gongming Xin
    Wenjing Du
    Journal of Thermal Science, 2024, 33 : 101 - 113
  • [27] Numerical Analysis of Heat Transfer Characteristics to Supercritical CO2 in a Vertical Mini-Channel:Transition and Pseudo-Boiling
    YUAN Baoqiang
    WANG Wei
    XIN Gongming
    DU Wenjing
    JournalofThermalScience, 2024, 33 (01) : 101 - 113
  • [28] Numerical Analysis of Heat Transfer Characteristics to Supercritical CO2 in a Vertical Mini-Channel: Transition and Pseudo-Boiling
    Yuan, Baoqiang
    Wang, Wei
    Xin, Gongming
    Du, Wenjing
    JOURNAL OF THERMAL SCIENCE, 2024, 33 (01) : 101 - 113
  • [29] Numerical Simulation of Heat Transfer Characteristics for Supercritical CO2-Propane Mixture in Tubes
    Yu, Bo-Wen
    Li, Hao-Ran
    Hong, Wen-Peng
    Niu, Xiao-Juan
    Kung Cheng Je Wu Li Hsueh Pao/Journal of Engineering Thermophysics, 2022, 43 (02): : 465 - 471
  • [30] Optimization of the UO2 kernel coating process by 2D simulation of spouted bed dynamics in the coater
    Liu, Malin
    Liu, Bing
    Shao, Youlin
    NUCLEAR ENGINEERING AND DESIGN, 2012, 251 : 124 - 130