Solids circulation and axial dispersion of cohesionless particles in a V-mixer

被引:41
作者
Kuo, HP [1 ]
Knight, PC
Parker, DJ
Seville, JPK
机构
[1] Chang Gung Univ, Dept Chem & Mat Engn, Tao Yuan 333, Taiwan
[2] Univ Birmingham, Dept Chem Engn, Ctr Formulat Engn, Birmingham B15 2TT, W Midlands, England
[3] Univ Birmingham, Sch Phys & Space Res, Positron Imaging Ctr, Birmingham B15 2TT, W Midlands, England
关键词
V-mixer; particle mixing; Positron Emission Particle Tracking; flow reversal;
D O I
10.1016/j.powtec.2004.12.003
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The motion of mono-sized 3 mm glass beads in a V-mixer was studied using the Positron Emission Particle Tracking (PEPT) technique. A similarity is found between the motion in V-mixers and in rotating drums. In both cases, there is a surface flow regime and a solid body motion regime. Within each arm of the mixer, there is a regular circulation in rotating Lagrangian coordinates, the direction of which changes as the volumetric fill increases. The flow reversal occurs at intermediate fills and is system dependent. It was attributed to the surface flow regime and the freeboard in the arm of the V-mixer. The circulation intensity in the arm was quantified and was found to increase quadratically with increasing rotational speed. It was attributed to the kinetic energies of particles within each arm. The circulation intensity decreases when the fill level increases from 10% fill to 46% fill and a minimum value exists at intermediate fills. The axial dispersion coefficient of the particles in the V-mixer increases linearly as the rotational speed increases from 15 rpm to 60 rpm. (c) 2005 Elsevier B.V. All rights reserved.
引用
收藏
页码:133 / 140
页数:8
相关论文
共 23 条
[1]   Using flow perturbations to enhance mixing of dry powders in V-blenders [J].
Brone, D ;
Wightman, C ;
Connor, K ;
Alexander, A ;
Muzzio, FJ ;
Robinson, P .
POWDER TECHNOLOGY, 1997, 91 (03) :165-172
[2]   Quantitative characterization of mixing of dry powders in V-blenders [J].
Brone, D ;
Alexander, A ;
Muzzio, FJ .
AICHE JOURNAL, 1998, 44 (02) :271-278
[3]   THE MIXING OF SOLIDS IN TUMBLING MIXERS .1. [J].
CARLEYMACAULY, KW ;
DONALD, MB .
CHEMICAL ENGINEERING SCIENCE, 1962, 17 (07) :493-&
[4]   A STUDY OF THE PERFORMANCE OF A MODIFIED V-SHAPED SOLIDS MIXER USING SEGREGATING MATERIALS [J].
CHANG, RK ;
CHANG, SI ;
ROBINSON, JR .
INTERNATIONAL JOURNAL OF PHARMACEUTICS, 1992, 80 (2-3) :171-178
[5]   A COMPARISON OF FREE-FLOWING, SEGREGATING AND NON-FREE-FLOWING, COHESIVE MIXING SYSTEMS IN ASSESSING THE PERFORMANCE OF A MODIFIED V-SHAPED SOLIDS MIXER [J].
CHANG, RK ;
BADAWY, S ;
HUSSAIN, MA ;
BUEHLER, JD .
DRUG DEVELOPMENT AND INDUSTRIAL PHARMACY, 1995, 21 (03) :361-368
[6]   MIXING OF PHARMACEUTICAL SOLIDS .1. EFFECT OF PARTICLE-SIZE ON MIXING IN CYLINDRICAL SHEAR AND V-SHAPED TUMBLING MIXERS [J].
CHOWHAN, ZT ;
LINN, EE .
POWDER TECHNOLOGY, 1979, 24 (02) :237-244
[7]  
DEVILLIERS MM, 1997, INT J PHARM, V15, P1
[8]   Scaling relationships for rotating drums [J].
Ding, YL ;
Forster, RN ;
Seville, JPK ;
Parker, DJ .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (12) :3737-3750
[9]   Solids motion in rolling mode rotating drums operated at low to medium rotational speeds [J].
Ding, YL ;
Seville, JPK ;
Forster, R ;
Parker, DJ .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (05) :1769-1780
[10]  
FORSTER RN, 2001, KONA POWDER PARTICLE, V18, P139