The use of two different models to describe the axial mixing of solids in fluidised beds

被引:19
作者
Grasa, G [1 ]
Abanades, JC [1 ]
机构
[1] CSIC, Inst Carboquim, Dept Energy & Environm, Zaragoza 50015, Spain
关键词
solids mixing; fluidisation; mathematical; modelling; dispersion; powder technology;
D O I
10.1016/S0009-2509(02)00146-X
中图分类号
TQ [化学工业];
学科分类号
0817 [化学工程与技术];
摘要
Two widely used models to describe axial solid mixing in fluidised beds (the dispersion model and the countercurrent backmixing (CCBM) model) are evaluated against identical sets of experimental data. Experimental work has been obtained at different conditions (gas velocity, particle properties and two column diameters) using an image analysis technique. Previously published data by other authors are also compiled to enlarge the experimental database for model development and validation. It is shown that both models are capable to fit the majority of experiments well, in agreement with a well-known relation between the models in some extreme conditions. This relation is further explored by incorporating independent measurements of the tracer rise velocities during the mixing experiments. It is concluded that, although a simple correlation for the solid dispersion coefficients compiled in this work is useful, the CCBM model is a much more reliable idealisation in describing and scaling up axial solid mixing in fluidised beds. (C) 2002 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:2791 / 2798
页数:8
相关论文
共 34 条
[1]
ABANADES JC, 1999, 15 INT C FLUID BED C
[2]
Simulation of 2-D temperature distributions in fluidized bed reactors for highly exothermic reactions [J].
Artlich, S ;
Hartge, EU ;
Werther, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (03) :782-792
[3]
SOLIDS MIXING IN AN EXPANDED TOP FLUID BED [J].
AVIDAN, A ;
YERUSHALMI, J .
AICHE JOURNAL, 1985, 31 (05) :835-841
[4]
SOLIDS EXCHANGE BETWEEN THE BUBBLE WAKE AND THE EMULSION PHASE IN A 2-DIMENSIONAL GAS-FLUIDIZED BED [J].
BASESME, EA ;
LEVY, EK .
POWDER TECHNOLOGY, 1992, 72 (01) :45-50
[5]
DEGROOT JH, 1967, P INT S FLUID NETH A
[6]
Enwald H, 1996, INT J MULTIPHAS FLOW, V22, P21, DOI 10.1016/S0301-9322(96)90004-X
[7]
CORRELATION OF AXIAL MIXING OF SOLIDS IN FLUIDIZED-BEDS BY A DISPERSION COEFFICIENT [J].
ESIN, A ;
ALTUN, M .
POWDER TECHNOLOGY, 1984, 39 (02) :241-244
[8]
A calibration procedure to obtain solid concentrations from digital images of bulk powders [J].
Grasa, G ;
Abanades, JC .
POWDER TECHNOLOGY, 2001, 114 (1-3) :125-128
[9]
PARTICLE SEGREGATION IN FLUIDIZED BINARY-MIXTURES [J].
HOFFMANN, AC ;
JANSSEN, LPBM ;
PRINS, J .
CHEMICAL ENGINEERING SCIENCE, 1993, 48 (09) :1583-1592
[10]
Influence of horizontal tube banks on the behavior of bubbling fluidized beds 2. Mixing of solids [J].
Hull, AS ;
Chen, ZM ;
Agarwal, PK .
POWDER TECHNOLOGY, 2000, 111 (03) :192-199