Minimum fluidization velocity of particles with different size distributions at elevated pressures and temperatures

被引:37
作者
Shao, Yingjuan [1 ,2 ]
Li, Zhaozhi [1 ,2 ]
Zhong, Wenqi [1 ,2 ]
Bian, Zhoufeng [1 ,2 ]
Yu, Aibing [2 ,3 ]
机构
[1] Southeast Univ, Sch Energy & Environm, Key Lab Energy Thermal Convers & Control, Minist Educ, Nanjing 210096, Peoples R China
[2] Southeast Univ Monash Univ Joint Res Inst, Ctr Simulat & Modelling Particulate Syst, Suzhou, Peoples R China
[3] Monash Univ, Dept Chem Engn, ARC Res Hub Computat Particle Technol, Clayton, Vic 3800, Australia
基金
中国国家自然科学基金;
关键词
Minimum fluidization velocity; Pressurized fluidized bed; Particle size distribution; Pressure; Temperature; SPOUT-FLUID BED; INTERPARTICLE FORCES; COAL COMBUSTION; OPERATING TEMPERATURE; FLOW; GASIFICATION; SIMULATION; BEHAVIORS; EXPANSION; VOIDAGE;
D O I
10.1016/j.ces.2020.115555
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper presents a detailed investigation into the effect of pressure, temperature and particle size distribution (PSD) on the minimum fluidization velocity (U-mf). A series of measurement of U-mf were carried out under the pressure from 0.1 MPa to 0.5 MPa and the temperature from 300 degrees C to 850 degrees C on a lab-scale pressurized fluidized bed reactor for three narrow PSD and three wide PSD (binary, uniform, and Gaussian-type) silica sand particles. The results showed that the U-mf for narrow and wide PSDs both decreased with increasing temperature and decreased slightly with rising pressure. Besides, the Gaussian-type mixtures had almost the same U-mf as the reference narrow PSD particle, while the U-mf of binary and uniform PSD mixtures was larger than these two. Based on the experimental data, a new simple relationship for predicting U-mf of the different PSD particles at elevated pressures and temperatures was developed. (C) 2020 Elsevier Ltd. All rights reserved.
引用
收藏
页数:12
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