Experimental investigations on a cyclone separator performance at an extremely low particle concentration

被引:52
作者
Ji, Zhongli [1 ]
Xiong, Zhiyi [1 ]
Wu, Xiaolin [1 ]
Chen, Honghai [1 ]
Wu, Hongxiao [2 ]
机构
[1] China Univ Petr, Dept Mech & Elect Engn, Beijing, Peoples R China
[2] BCB Filtrat Technol CO LTD, Beijing, Peoples R China
关键词
Cyclone separator; Collection efficiency; Grade efficiency; Low particle concentration; Particle agglomeration; GAS; DESIGN;
D O I
10.1016/j.powtec.2008.10.015
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In order to evaluate the influence of extremely low particle concentration oil separation performance of cyclone separator, the overall collection efficiencies and grade efficiencies of a cyclone separator with particle concentrations of 5-2000 mg/m(3) and inlet velocities of 6-30 m/s have been investigated under ambient temperature and atmospheric pressure conditions. Aerosol spectrometer based oil measuring particle number is used to measure the particle concentrations and particle size distributions of the inlet and outlet of the cyclone separator. The overall efficiency is equal to the ratio of the particle concentration difference between the inlet and outlet of the cyclone separator to the inlet particle concentration. The grade efficiency is obtained by comparing the particle size distributions of the inlet and Outlet of the cyclone separator. The effects of particle concentration on separation performance are predicted by Smolik empirical model. Particle agglomeration, which has been found in the inlet and Outlet of the cyclone separator, has a very important influence on the collection efficiencies and grade efficiencies of the cyclone separator at the particle concentration of 5-2000 mg/m(3). The cut sizes for different inlet gas velocity with extremely low particle concentration can be quantitatively Calculated by Barth model, Mothes and Loffer model and Muschelknautz model, respectively. Experimental results show that the overall collection efficiencies and grade efficiencies increased with the increasing particle concentrations and inlet velocities, and most of the particles with the diameter bigger than 10 mu m can be removed by cyclone separator. (C) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:254 / 259
页数:6
相关论文
共 19 条
  • [1] ALEMEYER S, 2004, CHEM ENG PROCESS, V43, P511
  • [2] Barth W., 1956, Brenn. Warme Kraft, V8, P9, DOI DOI 10.1016/J.CEJ.2008.10.022
  • [3] Modern design of aerocyclones
    Bohnet, M
    Morweiser, M
    [J]. ADVANCED POWDER TECHNOLOGY, 1997, 8 (02) : 137 - 161
  • [4] Modeling the gas and particle flow inside cyclone separators
    Cortes, Cristobal
    Gil, Antonia
    [J]. PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2007, 33 (05) : 409 - 452
  • [5] Simulation of mass-loading effects in gas-solid cyclone separators
    Derksen, J. J.
    Sundaresan, S.
    van den Akker, H. E. A.
    [J]. POWDER TECHNOLOGY, 2006, 163 (1-2) : 59 - 68
  • [6] A study of the effect of high inlet solids loading on a cyclone separator pressure drop and collection efficiency
    Fassani, FL
    Goldstein, L
    [J]. POWDER TECHNOLOGY, 2000, 107 (1-2) : 60 - 65
  • [7] EFFECTS OF GEOMETRY AND SOLID LOADING ON THE PERFORMANCE OF GAS CYCLONES
    HOFFMANN, AC
    VANSANTEN, A
    ALLEN, RWK
    CLIFT, R
    [J]. POWDER TECHNOLOGY, 1992, 70 (01) : 83 - 91
  • [8] HOFFMANN AC, 1991, FILTR SEPARAT, V28, P188
  • [9] Leith D., 1972, AICHE S SERIES, V68, P196
  • [10] Numerical modelling of the fluid and particle penetration through small sampling cyclones
    Ma, L
    Ingham, DB
    Wen, X
    [J]. JOURNAL OF AEROSOL SCIENCE, 2000, 31 (09) : 1097 - 1119