Cluster characteristics of continuous size distributions and binary mixtures of Group B particles in dilute riser flow

被引:47
作者
Chew, Jia Wei [1 ]
Parker, Drew M. [1 ]
Cocco, Ray A. [2 ]
Hrenya, Christine M. [1 ]
机构
[1] Univ Colorado, Dept Chem & Biol Engn, Boulder, CO 80309 USA
[2] Particulate Solid Res Inc, Chicago, IL 60632 USA
基金
美国国家科学基金会;
关键词
Cluster; Fiber optic probe; Video images; Wavelet decomposition; CFB riser; FLUIDIZED-BED; SEGREGATION; VELOCITY; SOLIDS; IDENTIFICATION; CALIBRATION; DYNAMICS; BEHAVIOR; MINIMUM; POWDER;
D O I
10.1016/j.cej.2011.10.020
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Gas-solids circulating fluidized bed (CFB) experiments have been carried out, with a focus on understanding the impact of polydispersity on cluster characteristics in a dilute riser. Two categories of polydispersity were studied: continuous particle size distributions (PSDs) of varying distribution widths, and binary mixtures of varying compositions. Video images show that particle clusters exist even in these very dilute systems (solid loading m = 0.03-0.29). Local measurements were acquired using two independent instruments - a fiber optic probe and a high-speed video camera - with the cluster trends obtained from both are in qualitative agreement with each other. Cluster characteristics extracted from the measurements include appearance probability, duration and frequency. Results show that: (i) axial position is the strongest influence on radial profiles of cluster duration and frequency, but has negligible effect on cluster appearance probability, (ii) profile shapes are invariant with height, although magnitudes of cluster duration and frequency changes with height, and (iii) effects of both the widths of continuous PSDs and the compositions of binary mixtures are observed at the riser bottom for cluster duration and at the riser top for cluster frequency, though are insignificant for the appearance probability. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:348 / 358
页数:11
相关论文
共 64 条
[1]   CLUSTERS IDENTIFICATION AND CHARACTERIZATION IN A GAS-SOLID FLUIDIZED BED BY THE WAVELET ANALYSIS [J].
Afsahi, Forough-Azam ;
Sotudeh-Gharebagh, Rahmat ;
Mostoufi, Navid .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2009, 87 (03) :375-385
[2]   The role of meso-scale structures in rapid gas-solid flows [J].
Agrawal, K ;
Loezos, PN ;
Syamlal, M ;
Sundaresan, S .
JOURNAL OF FLUID MECHANICS, 2001, 445 :151-185
[3]   FLUID MECHANICAL DESCRIPTION OF FLUIDIZED BEDS - STABILITY OF STATE OF UNIFORM FLUIDIZATION [J].
ANDERSON, TB ;
JACKSON, R .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1968, 7 (01) :12-&
[4]  
Avidan A.A., 1997, Circulating fluidized beds, P466
[5]  
AVIDAN AA, 1990, REV CHEM ENG, V6, P1
[6]  
BAKSHI BR, 1995, CHEM ENG RES DES, V73, P608
[7]   A NEW THEORY OF THE INSTABILITY OF A UNIFORM FLUIDIZED-BED [J].
BATCHELOR, GK .
JOURNAL OF FLUID MECHANICS, 1988, 193 :75-110
[8]  
Brereton C., 1997, Circulating fluidized beds, V1st, P369
[9]   MICROSTRUCTURAL ASPECTS OF THE BEHAVIOR OF CIRCULATING FLUIDIZED-BEDS [J].
BRERETON, CMH ;
GRACE, JR .
CHEMICAL ENGINEERING SCIENCE, 1993, 48 (14) :2565-2572
[10]   Cluster characteristics of Geldart group B particles in a pilot-scale CFB riser. II. Polydisperse systems [J].
Chew, Jia Wei ;
Hays, Roy ;
Findlay, John G. ;
Knowlton, Ted M. ;
Karri, S. B. Reddy ;
Cocco, Ray A. ;
Hrenya, Christine M. .
CHEMICAL ENGINEERING SCIENCE, 2012, 68 (01) :82-93