Simulation of Very Low Frequency Pulsed Fluidized Bed

被引:0
作者
Abedi, N. [1 ]
Esfahany, M. Nasr [2 ]
机构
[1] Isfahan Univ Technol, Pardis Coll, Chem Engn Grp, Esfahan 8415683111, Iran
[2] Isfahan Univ Technol, Dept Chem Engn, Esfahan 8415683111, Iran
基金
美国国家科学基金会;
关键词
Combined airflow; CFD simulation; Fluidization quality; Pulsed fluidized bed; Pulse frequency; HEAT-TRANSFER; FLOW; CFD; HYDRODYNAMICS; PARTICLES; DEM; EQUATIONS; DYNAMICS;
D O I
10.47176/jafm.17.10.2548
中图分类号
O414.1 [热力学];
学科分类号
摘要
Achieving high fluidization quality and bed stability is a paramount challenge in pulsed fluidized beds. 2D hydrodynamics models were studied using the Eulerian-Eulerian method with KTGF. This study investigates the impact of rectangular pulsation superimposed on steady airflow, while maintaining a constant temporal average gas velocity, on fluidization quality. Numerical results indicated that superimposing pulsations on steady airflow and increasing the steady airflow velocity to three times the minimum fluidization velocity resulted in a decrease in the bed expansion ratio. This decrease was most notable particularly at a pulsation frequency of 0.05Hz, with a reducing of approximately by about 21%. By decreasing the velocity ratio from 9.52 to 6.52, the pressure drop increased by 27% and 4.5% at 0.05 Hz and 10 Hz, respectively. Additionally, the fluidization index increased by 32% and 2% under these conditions. The optimal range of pulsed airflow velocity fell between 2.76 and 1.17 times the steady airflow velocity and was most effective at 0.05 - 0.1 Hz.
引用
收藏
页码:2141 / 2153
页数:13
相关论文
共 45 条
[1]   Investigating effect of pulsed flow on hydrodynamics of gas-solid fluidized bed using two-fluid model simulation and experiment [J].
Bizhaem, Hamed Khosravi ;
Tabrizi, Hassan Basirat .
POWDER TECHNOLOGY, 2017, 311 :328-340
[2]   Experimental study on hydrodynamic characteristics of gas-solid pulsed fluidized bed [J].
Bizhaem, Hamed Khosravi ;
Tabrizi, Hassan Basirat .
POWDER TECHNOLOGY, 2013, 237 :14-23
[3]   Structuring chaotic fluidized beds [J].
Coppens, MO ;
van Ommen, JR .
CHEMICAL ENGINEERING JOURNAL, 2003, 96 (1-3) :117-124
[4]   Numerical investigation of pulsed fluidized bed using CFD-DEM: Insights on the dynamics [J].
de Oliveira, D. G. ;
Wu, C. L. ;
Nandakumar, K. .
POWDER TECHNOLOGY, 2020, 363 :745-756
[5]   Modeling and Simulation of an Oxygen-Blown Bubbling Fluidized Bed Gasifier using the Computational Particle-Fluid Dynamics (CPFD) Approach [J].
Di Nardo, A. ;
Calchetti, G. ;
Stendardo, S. .
JOURNAL OF APPLIED FLUID MECHANICS, 2018, 11 (04) :825-834
[6]   A BUBBLING FLUIDIZATION MODEL USING KINETIC-THEORY OF GRANULAR FLOW [J].
DING, J ;
GIDASPOW, D .
AICHE JOURNAL, 1990, 36 (04) :523-538
[7]   Experimental and numerical study of the characteristics of the forced oscillation in a pulsation fluidized bed (PFB) for coal separation [J].
Dong, Liang ;
Zhu, Fenglong ;
Li, Yanjiao ;
Zhao, Yuemin ;
Duan, Chenlong ;
Ren, Yongxin ;
Wang, Guanghui ;
He, Jingfeng ;
Zhang, Yong .
CHEMICAL ENGINEERING SCIENCE, 2021, 234 (234)
[8]   Kinetic characteristics of the particles in a dense-phase pulsed fluidized bed for dry beneficiation [J].
Dong, Liang ;
Zhang, Bo ;
Zhang, Yong ;
Zhao, Yuemin ;
Zhou, Enhui ;
Lv, Peng ;
Duan, Chenlong .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2017, 95 (06) :1133-1140
[9]   Effect of active pulsing air flow on gas-vibro fluidized bed for fine coal separation [J].
Dong, Liang ;
Zhang, Yong ;
Zhao, Yuemin ;
Peng, Liping ;
Zhou, Enhui ;
Cai, Luhui ;
Zhang, Bo ;
Duan, Chenlong .
ADVANCED POWDER TECHNOLOGY, 2016, 27 (05) :2257-2264
[10]   Elutriation and agglomerate size distribution in a silica nanoparticle vibro-fluidized bed [J].
Feng, Zhen ;
Liu, Daoyin ;
Zhang, Wangle ;
Feng, Hao ;
van Ommen, J. Ruud .
CHEMICAL ENGINEERING JOURNAL, 2022, 434