THE EFFECT OF INTERPARTICLE FORCES ON THE STABILITY OF GAS-FLUIDIZED BEDS .1. EXPERIMENTAL-EVIDENCE

被引:94
|
作者
RIETEMA, K [1 ]
PIEPERS, HW [1 ]
机构
[1] EINDHOVEN UNIV TECHNOL,DEPT CHEM ENGN,5600 MB EINDHOVEN,NETHERLANDS
关键词
D O I
10.1016/0009-2509(90)80015-7
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The stability theory for homogeneous fluidized beds presented earlier is reviewed. This theory is based on the concept of the elasticity of the bed structure as a consequence of interparticle forces. It is shown that this theory explains the effect of gas viscosity and gravity. It is further shown that the elasticity modulus is increased by gas adsorption to the solid surface at elevated pressure and, thus, explains the effect of gas pressure on bed expansion. The theory is compared with experimental results obtained with fluidization of fresh cracking catalyst and polypropylene by different gases and at gas pressures up to 15 bar. It is further shown that the elasticity modulus can be used to correlate bed expansion and bubble size during heterogeneous fluidization. The stability theory of Foscolo and Gibilaro is criticized and rejected on the basis of serious mistakes made in their theoretical derivation. © 1990.
引用
收藏
页码:1627 / 1639
页数:13
相关论文
共 50 条
  • [21] EFFECT OF BUBBLE COALESCENCE ON ENTRAINMENT IN GAS-FLUIDIZED BEDS
    FUNG, AS
    HAMDULLAHPUR, F
    POWDER TECHNOLOGY, 1993, 77 (03) : 251 - 265
  • [22] The effect of particle aggregation on the collapse of gas-fluidized beds.
    Castellanos, A
    Valverde, JM
    Quintanilla, MAS
    Mills, P
    POWDERS AND GRAINS 2001, 2001, : 569 - 572
  • [23] MASS-TRANSFER IN GAS-FLUIDIZED BEDS - MEASUREMENT OF ACTUAL DRIVING FORCES
    HSIUNG, TH
    THODOS, G
    CHEMICAL ENGINEERING SCIENCE, 1977, 32 (06) : 581 - 592
  • [24] Effect of inclination on gas-fluidized beds of fine cohesive powders
    Valverde, J. M.
    Castellanos, A.
    Quintanilla, M. A. S.
    Gilabert, F. A.
    POWDER TECHNOLOGY, 2008, 182 (03) : 398 - 405
  • [25] Experimental observations on the different mechanisms for solid ejection in gas-fluidized beds
    Almendros-Ibanez, J. A.
    Sanchez-Delgado, S.
    Sobrino, C.
    Santana, D.
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2009, 48 (03) : 734 - 744
  • [26] AN EXPERIMENTAL-STUDY OF THE EXPANSION CHARACTERISTICS OF GAS-FLUIDIZED BEDS OF FINE CATALYSTS
    FOSCOLO, PU
    DIFELICE, R
    GIBILARO, LG
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1987, 22 (02) : 69 - 78
  • [27] EFFECT OF BED HEIGHT ON PARTICLE ENTRAINMENT FROM GAS-FLUIDIZED BEDS
    BARON, T
    BRIENS, CL
    GALTIER, P
    BERGOUGNOU, MA
    POWDER TECHNOLOGY, 1990, 63 (02) : 149 - 156
  • [28] Linear stability analysis of gas-fluidized beds for the prediction of incipient bubbling conditions
    Busciglio, A.
    Micale, G.
    Vella, G.
    Rizzuti, L.
    CHEMICAL ENGINEERING JOURNAL, 2010, 157 (2-3) : 489 - 500
  • [29] Experimental quantification of interparticle forces in gas-solid fluidized beds operating at temperatures from ambient to 1500 °C
    Zhang, Qingjin
    Fu, Liangliang
    Xu, Guangwen
    Bai, Dingrong
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2024, 211 : 318 - 330