Numerical simulations of high pressure carbon dioxide fluid fluidized beds

被引:6
|
作者
Cai, Wenjian [1 ]
Xia, Xietian [2 ]
Li, Xiang [2 ]
Chen, Xing [2 ]
Xu, Zenghui [2 ]
Lu, Huilin [1 ]
机构
[1] Harbin Inst Technol, Sch Energy Sci & Engn, Harbin 150001, Peoples R China
[2] China Construction Ecoenvironm Protect Technol Co, Suzhou 215100, Peoples R China
来源
PARTICUOLOGY | 2023年 / 78卷
基金
中国国家自然科学基金;
关键词
High pressure carbon dioxide; Fluidized bed; Transition; Aggregative fluidization; Particulate fluidization; Kinetic theory of granular flow; KINETIC-THEORY; EXTRACTION; DYNAMICS; CAROTENOIDS; FLOW; PARTICULATE; TRANSITION; PARTICLES; CRITERION; VELOCITY;
D O I
10.1016/j.partic.2022.09.009
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydrodynamics of carbon dioxide fluid-particle mixtures are predicted using a low density ratio-based kinetic theory of granular flow in high pressure carbon dioxide fluid fluidized beds. A coexistence of particle waves and particle aggregates exists along bed height. The threshold to identify the occurrence of particle aggregates is suggested based on standard deviation of solid volume fractions in aggregative fluidization. The existence time fractions and frequencies of particle aggregates are predicted along axial direction. The effect of carbon dioxide fluid temperature and pressure on volume fraction and velocity distributions are analyzed at different inlet carbon dioxide velocities and particle densities in high pressure carbon dioxide fluidized beds. Simulated results indicate that the carbon dioxide-particles fluidization transits from particulate to aggregative states with the increase of inlet carbon dioxide velocities. The computed fluid volume fractions and heterogeneity indexes are close to the measurements in a high pressure carbon dioxide fluidized bed.(c) 2022 Chinese Society of Particuology and Institute of Process Engineering, Chinese Academy of Sciences. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:1 / 15
页数:15
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