SIZE DISTRIBUTION OF PARTICLES ENTRAINED FROM FLUIDIZED-BEDS - ELECTROSTATIC EFFECTS

被引:36
|
作者
BRIENS, CL
BERGOUGNOU, MA
INCULET, II
BARON, T
HAZLETT, JD
机构
[1] NATL RES COUNCIL CANADA,INST ENVIRONM CHEM,OTTAWA K1A 0R9,ONTARIO,CANADA
[2] ATOCHEM,USINE MONT,F-64300 ORTHEZ,FRANCE
关键词
D O I
10.1016/0032-5910(92)85054-Y
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Experimental results obtained with solids ranging from 69-mu-m cracking catalyst to 400-mu-m polyethylene showed that the smallest particles were not the most easily elutriated from fluidized beds of mixed size particles. This is in contradiction with the assumption made by existing models for the prediction of the flux and size distribution of particles elutriated from a fluidized bed. The smallest particles cannot be removed by elutriation from a mixture of particles of various sizes. The smallest particles may be agglomerated with larger particles. Reducing or eliminating particle electrostatic charges by injecting counteracting charges or increasing the gas humidity did not greatly affect the size distribution of the elutriated particles. Electrostatic forces were, thus, not responsible for particle agglomeration. Electrostatic effects, on the other hand, greatly reduced the flux of elutriated particles by creating an extra electrostatic pressure drop in the fluidized bed freeboard. They also changed the fluidization quality of the bed of polyethylene particles.
引用
收藏
页码:57 / 62
页数:6
相关论文
共 50 条
  • [1] SIZE DISTRIBUTION OF THE PARTICLES ENTRAINED FROM FLUIDIZED-BEDS - GAS HUMIDITY EFFECTS
    BARON, T
    BRIENS, CL
    HAZLETT, JD
    BERGOUGNOU, MA
    GALTIER, P
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1992, 70 (04): : 631 - 635
  • [2] ELECTROSTATIC SEPARATION OF FINE PARTICLES IN VIBRATED FLUIDIZED-BEDS
    KIEWIET, CW
    BERGOUGNOU, MA
    BROWN, JD
    INCULET, II
    IEEE TRANSACTIONS ON INDUSTRY APPLICATIONS, 1978, 14 (06) : 526 - 530
  • [3] DISTRIBUTION OF SOLID PARTICLES IN LIQUID FLUIDIZED-BEDS
    PATWARDHAN, VS
    TIEN, C
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1984, 62 (01): : 46 - 54
  • [4] BUBBLE-SIZE DISTRIBUTION IN FLUIDIZED-BEDS
    JODRA, LG
    ROMERO, JMA
    ANALES DE QUIMICA SERIE A-QUIMICA FISICA Y QUIMICA TECNICA, 1981, 77 (01): : 144 - 154
  • [5] DISTRIBUTION OF BUBBLE SIZE IN GAS FLUIDIZED-BEDS
    ROWE, PN
    YACONO, C
    TRANSACTIONS OF THE INSTITUTION OF CHEMICAL ENGINEERS, 1975, 53 (01): : 59 - 60
  • [6] ELECTROSTATIC CHARGING IN GAS FLUIDIZED-BEDS
    BOLAND, D
    GELDART, D
    POWDER TECHNOLOGY, 1972, 5 (05) : 289 - &
  • [7] FORECASTING OF BUBBLE-SIZE DISTRIBUTION IN FLUIDIZED-BEDS
    MOLERUS, O
    WERTHER, J
    CHEMISCHE TECHNIK, 1982, 34 (10): : 511 - 516
  • [8] STUDIES OF SEGREGATION MIXING IN FLUIDIZED-BEDS OF DIFFERENT SIZE PARTICLES
    NIENOW, AW
    NAIMER, NS
    CHIBA, T
    CHEMICAL ENGINEERING COMMUNICATIONS, 1987, 62 (1-6) : 53 - 66
  • [9] LATERAL MIXING OF PARTICLES IN FLUIDIZED-BEDS
    SUBBARAO, D
    MOGHADDAM, E
    BANNARD, JE
    CHEMICAL ENGINEERING SCIENCE, 1985, 40 (10) : 1988 - 1990
  • [10] A MODEL FOR PARTICLE-SIZE DISTRIBUTION AND ELUTRIATION IN FLUIDIZED-BEDS
    MILIOLI, FE
    FOSTER, PJ
    POWDER TECHNOLOGY, 1995, 83 (03) : 265 - 280