Solids mixing in gas-liquid-solid fluidized beds: Experiments and modelling

被引:28
|
作者
Cassanello, M
Larachi, F
Guy, C
Chaouki, J
机构
[1] ECOLE POLYTECH, DEPT CHEM ENGN, MONTREAL, PQ H3C 3A7, CANADA
[2] UNIV BUENOS AIRES, FAC CIENCIAS EXACTAS & NAT, DEPT IND, PINMATE, RA-1428 BUENOS AIRES, DF, ARGENTINA
[3] UNIV LAVAL, DEPT CHEM ENGN, ST FOY, PQ G1K 7P4, CANADA
基金
加拿大自然科学与工程研究理事会;
关键词
D O I
10.1016/0009-2509(96)00058-9
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Mixing in monosized particles and binary mixtures of solids in three-phase fluidized beds is investigated by means of a non-invasive Radioactive Particle Tracking technique (RPT). Pulses of particles at different column heights are constructed from the trajectory of a single radioactive tracer whose motion is tracked for several hours. For each pulse released, number distributions of particles in the axial direction are thus obtained for each instant of time from injections at different axial positions in the reactor. Using this information, axial mixing times for the solids are measured for the experimental conditions studied. A one-dimensional two-zone model based on the three-phase counter-current backmixing model used for gas-solid fluidization (Gwyn et al., 1970) is proposed and solved for these conditions to calculate solids axial number distributions and mixing times. Agreement between experimental and predicted results is satisfactory.
引用
收藏
页码:2011 / 2020
页数:10
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