Effects of the inlet duct length on the flow field and performance of a cyclone separator with a contracted inlet duct

被引:51
作者
Yao, Yuge [1 ]
Huang, Wenshi [1 ]
Wu, Yuxin [1 ]
Zhang, Yang [1 ]
Zhang, Man [1 ]
Yang, Hairui [1 ]
Lyu, Junfu [1 ]
机构
[1] Tsinghua Univ, Dept Energy & Power Engn, Key Lab Thermal Sci & Power Engn, Minist Educ, Beijing 100084, Peoples R China
关键词
Cyclone separator; Inlet duct length; Contracted inlet duct; Pressure drop; Separation efficiency; PRESSURE-DROP; COLLECTION EFFICIENCY; NUMERICAL-SIMULATION; GAS-FLOW; VELOCITY; PREDICTION; PARTICLES; MODEL; ANGLE; SHAPE;
D O I
10.1016/j.powtec.2021.07.044
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The inlet duct length may affect the gas flow field and performance of a cyclone separator with a contracted inlet duct. In this study, a numerical simulation using the Eulerian-Lagrangian approach with a one-way coupling method was conducted to evaluate the gas flow field and separation efficiency of the cyclone separators with contracted inlet ducts of different lengths. The simulation results indicated that increasing the inlet duct length led to higher gas tangential velocity in the cyclone body. The effect of the inlet duct length on gas axial velocity was inferior to that on gas tangential velocity. A longer inlet duct reduced both the pressure drop and the separation efficiency. The reductions of the expansion loss at the inlet of the cylinder and friction loss inside the cyclone body contributed the most reduction of the pressure drop as the inlet duct length increased. Generally, when the inlet duct was 1.5 times longer than the cylinder diameter, the effect of inlet duct length on the gas flow field and performance of a cyclone separator became slight. (c) 2021 Elsevier B.V. All rights reserved.
引用
收藏
页码:12 / 22
页数:11
相关论文
共 43 条
[21]  
Huard M., 2010, INT J CHEM REACT ENG, V8, P1, DOI [10.2202/1542-6580.2069, DOI 10.2202/1542-6580.2069]
[22]   Numerical simulation of a dense flow cyclone using the kinetic theory of granular flow in a dense discrete phase model [J].
Hwang, In Sik ;
Jeong, Hyo Jae ;
Hwang, Jungho .
POWDER TECHNOLOGY, 2019, 356 :129-138
[23]   Numerical investigation of the effect of number and shape of inlet of cyclone and particle size on particle separation [J].
Khazaee, Iman .
HEAT AND MASS TRANSFER, 2017, 53 (06) :2009-2016
[24]   CFD investigation of maldistribution in a full-loop circulating fluidized bed with double parallel cyclones [J].
Li, Shuyue ;
Shen, Yansong .
POWDER TECHNOLOGY, 2021, 381 :665-684
[25]   High-efficiency industrial cyclone separator: A CFD study [J].
Misiulia, Dzmitry ;
Antonyuk, Sergiy ;
Andersson, Anders Gustav ;
Lundstrom, Tord Staffan .
POWDER TECHNOLOGY, 2020, 364 :943-953
[26]   INVESTIGATION OF PARTICLE TRAJECTORIES IN 2-PHASE FLOW SYSTEMS [J].
MORSI, SA ;
ALEXANDER, AJ .
JOURNAL OF FLUID MECHANICS, 1972, 55 (SEP26) :193-+
[27]   Influence of the dipleg shape on the performance of gas cyclones [J].
Parvaz, Farzad ;
Hosseini, Seyyed Hossein ;
Elsayed, Khairy ;
Ahmadi, Goodarz .
SEPARATION AND PURIFICATION TECHNOLOGY, 2020, 233
[28]   Numerical investigation of effects of inner cone on flow field, performance and erosion rate of cyclone separators [J].
Parvaz, Farzad ;
Hosseini, Seyyed Hossein ;
Elsayed, Khairy ;
Ahmadi, Goodarz .
SEPARATION AND PURIFICATION TECHNOLOGY, 2018, 201 :223-237
[29]   Effects of the inlet section angle on the separation performance of a cyclone [J].
Qian, Fuping ;
Wu, Yanpeng .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2009, 87 (12A) :1567-1572
[30]   Numerical simulation of flow field in three types of standard cyclone separators [J].
Safikhani, H. ;
Akhavan-Behabadi, M. A. ;
Shams, M. ;
Rahimyan, M. H. .
ADVANCED POWDER TECHNOLOGY, 2010, 21 (04) :435-442