A study on the behaviour of bubbles of a 2D gas-solid fluidized bed using digital image analysis

被引:62
作者
Caicedo, GR [1 ]
Marqués, JJP [1 ]
Ruíz, MG [1 ]
Soler, JG [1 ]
机构
[1] Univ Alcala de Henares, Dept Chem Engn, Madrid 28871, Spain
关键词
bubbles; solid-gas systems; digital image analysis;
D O I
10.1016/S0255-2701(02)00039-9
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Bubble characteristics (shape factor, phi, and aspect ratio, beta) are very important in the design of fluidized beds since they have a strong influence on its hydrodynamics. Although several experimental techniques have been used to measure bubble parameters, in this work, experimental data were obtained using digital image analysis from two-dimensional (213) fluidized beds. Digital image analysis is susceptible to supplying a great quantity of information; it is none-intrusive, it is capable of securing several properties simultaneously and it is cost saving. The distribution of these two bubble characteristics (shape factor, phi, and aspect ratio, beta) as a function of the gas velocity is presented. Moreover, several experiments were performed where the influence of particle diameter, relative humidity, column width and bed height on the bubble characteristics was studied. The results show that the bubble parameters, phi and beta, follow a normal distribution which allows to perform a statistical treatment of the data obtained. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:9 / 14
页数:6
相关论文
共 11 条
[1]  
AGARWAL PK, 1985, CHEM ENG RES DES, V63, P323
[2]   GAS SAMPLING FROM FLUIDIZED-BEDS - A NOVEL PROBE SYSTEM [J].
ATKINSON, CM ;
CLARK, NN .
POWDER TECHNOLOGY, 1988, 54 (01) :59-70
[3]  
Chiba T., 1975, J CHEM ENG JPN, V8, P167
[4]   BUBBLE RISE VELOCITY IN 2-DIMENSIONAL FLUIDIZED-BEDS [J].
GERA, D ;
GAUTAM, M .
POWDER TECHNOLOGY, 1995, 84 (03) :283-285
[5]   BUBBLE PROPERTIES IN LARGE-PARTICLE FLUIDIZED-BEDS [J].
GLICKSMAN, LR ;
LORD, WK ;
SAKAGAMI, M .
CHEMICAL ENGINEERING SCIENCE, 1987, 42 (03) :479-491
[6]   Influence of horizontal tube banks on the behavior of bubbling fluidized beds 1. Bubble hydrodynamics [J].
Hull, AS ;
Chen, ZM ;
Fritz, JW ;
Agarwal, PK .
POWDER TECHNOLOGY, 1999, 103 (03) :230-242
[7]   CONVERSION OF PIERCED LENGTHS MEASURED AT A PROBE TO BUBBLE-SIZE MEASURES - AN ASSESSMENT OF THE GEOMETRICAL-PROBABILITY APPROACH AND BUBBLE SHAPE MODELS [J].
LIM, KS ;
AGARWAL, PK .
POWDER TECHNOLOGY, 1990, 63 (03) :205-219
[8]  
PRIETO JJ, 1997, THESIS ALCALA U SPAI
[9]  
ROWE PN, 1972, TRANS INST CHEM ENG, V50, P42
[10]   BUBBLE DYNAMICS AND ELUTRIATION STUDIES IN GAS-FLUIDIZED BEDS [J].
Saxena, S. C. ;
Mathur, A. ;
Sharma, G. K. .
CHEMICAL ENGINEERING COMMUNICATIONS, 1984, 29 (1-6) :35-61