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
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