Particles residence time distribution in a gas-solid cyclone reactor using a CFD-DDPM tracer method

被引:29
作者
Li, Anjun [1 ]
Zhu, Liyun [1 ]
Wang, Kun [1 ]
Wang, Guotao [1 ]
Wang, Zhenbo [1 ]
机构
[1] China Univ Petr East China, State Key Lab Heavy Oil, Qingdao 266580, Shandong, Peoples R China
基金
中国国家自然科学基金;
关键词
RTD; CFD simulation; Cyclone reactor; Eulerian-Lagrangian model; FLUIDIZED-BED; FLOW; SIMULATION; HYDRODYNAMICS; PYROLYSIS; MODEL; RISER;
D O I
10.1016/j.powtec.2019.11.038
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The simulation of particles residence time distribution (RTD) in a gas-solid cyclone reactor (GSCR) based on the CFD-DDPM tracer method was conducted. The comparison between the computed results and the experimental data shows that this model is applicable to predict the gas-solid hydrodynamics with better accuracy. Simulated results depict that the predicted particles RTD will be more accurate if a lower sampling duration is applied. Reynolds number, particulate loading and Stokes number have significant effects on the shape of RTD curves. The appearance time of the first peak in the diffusion chamber is not affected by Reynolds number, but the peak height diminishes with the increase of Reynolds number. A particle with a higher Stokes number descends faster and has a shorter residence time. As particulate loading increases, the appearance time of the first peak shifts left along the X-axis. The agglomeration and separation chamber MRT are sensitive to the change of Reynolds number, particulate loading and Stokes number. (C) 2020 Published by Elsevier B.V.
引用
收藏
页码:205 / 217
页数:13
相关论文
共 35 条
[1]  
[Anonymous], POWDER TECHNOL
[2]  
[Anonymous], SEP SCI TECHNOL
[3]   CFD simulation of cyclone separators to reduce air pollution [J].
Bogodage, Sakura Ganegama ;
Leung, Andrew Y. T. .
POWDER TECHNOLOGY, 2015, 286 :488-506
[4]   Characterization of liquid phase mixing in turbulent bed contactor through RTD studies [J].
Bruce, AER ;
Sai, PST ;
Krishnaiah, K .
CHEMICAL ENGINEERING JOURNAL, 2004, 104 (1-3) :19-26
[5]   A new methodology for measurement of sludge residence time distribution in a paddle dryer using X-ray fluorescence analysis [J].
Charlou, Christophe ;
Milhe, Mathieu ;
Sauceau, Martial ;
Arlabosse, Patricia .
WATER RESEARCH, 2015, 69 :1-8
[6]   CFD optimization of feedstock injection angle in a FCC riser [J].
Chen, Sheng ;
Fan, Yiping ;
Yan, Zihan ;
Wang, Wei ;
Liu, Xinhua ;
Lu, Chunxi .
CHEMICAL ENGINEERING SCIENCE, 2016, 153 :58-74
[7]   Performance evaluation of a complete Lagrangian KTGF approach for dilute granular flow modelling [J].
Cloete, Schalk ;
Johansen, Stein Tore ;
Amini, Shahriar .
POWDER TECHNOLOGY, 2012, 226 :43-52
[8]   Numerical Study of Gas-Solid Flow in a Radial-Inlet Structure Cyclone Separator [J].
Cui, Jie ;
Chen, Xueli ;
Gong, Xin ;
Yu, Guangsuo .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (11) :5450-5460
[9]   A BUBBLING FLUIDIZATION MODEL USING KINETIC-THEORY OF GRANULAR FLOW [J].
DING, J ;
GIDASPOW, D .
AICHE JOURNAL, 1990, 36 (04) :523-538
[10]   Investigations on the residence time distribution of a three-chamber feed frame with special focus on its geometric and parametric setups [J].
Duelle, M. ;
Oezcoban, H. ;
Leopold, C. S. .
POWDER TECHNOLOGY, 2018, 331 :276-285