Mixing characteristics of wet granular matter in a bladed mixer

被引:134
作者
Radl, Stefan [1 ]
Kalvoda, Eva [1 ]
Glasser, Benjamin J. [2 ]
Khinast, Johannes G. [1 ,3 ]
机构
[1] Graz Univ Technol, Inst Proc & Particle Engn, A-8010 Graz, Austria
[2] Rutgers State Univ, Dept Chem & Biochem Engn, Piscataway, NJ 08854 USA
[3] Res Ctr Pharmaceut Engn GmbH, A-8010 Graz, Austria
关键词
Bladed mixer; Particle flow; Wet granular matter; DEM; Granulation; NUMERICAL-SIMULATION; CAPILLARY BRIDGES; SELF-DIFFUSION; PARTICLE FLOW; SEGREGATION; BEHAVIOR; MODEL;
D O I
10.1016/j.powtec.2010.02.022
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
We performed numerical simulations of dry and wet granular flow inside a four-bladed mixer using the discrete element method (DEM). A capillary force model was incorporated to mimic the complex effects of pendular liquid bridges on particle flow. The simulations are able to capture the main features of granular flow, which is substantiated by the comparison of our results with experimental data. It was found that mean and fluctuating velocity fields for wet and dry particles differ significantly from each other. Our results indicate a strong increase in heap formation for wet particles and hence velocity fluctuations in the vertical direction become more pronounced. We observe that mixing in bladed mixers is strongly heterogeneous for wet granular matter due to the formation of different flow regimes within the mixer. The analysis of mixing quality shows that the spatial distribution of mixing intensity is influenced by the moisture content. This can lead to locally and even globally higher mixing rates for wet particles compared to dry granular matter. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:171 / 189
页数:19
相关论文
共 42 条
[1]   Influence of particle shape on the packing and on the segregation of spherocylinders via Monte Carlo simulations [J].
Abreu, CRA ;
Tavares, FW ;
Castier, M .
POWDER TECHNOLOGY, 2003, 134 (1-2) :167-180
[2]   Design of granule structure: Computational methods and experimental realization [J].
Ansari, Mansoor A. ;
Stepanek, Frantisek .
AICHE JOURNAL, 2006, 52 (11) :3762-3774
[3]  
Bird R B., 2002, Transportphenomena
[4]   FUNDAMENTAL POWDER MIXING MECHANISMS [J].
BRIDGWATER, J .
POWDER TECHNOLOGY, 1976, 15 (02) :215-236
[5]   Cohesive effects in powder mixing in a tumbling blender [J].
Chaudhuri, Bodhisattwa ;
Mehrotra, Amit ;
Muzzio, Fernando J. ;
Tomassone, M. Silvina .
POWDER TECHNOLOGY, 2006, 165 (02) :105-114
[6]   Granular flow and segregation in a four-bladed mixer [J].
Conway, SL ;
Lekhal, A ;
Khinast, JG ;
Glasser, BJ .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (24) :7091-7107
[7]   DISCRETE NUMERICAL-MODEL FOR GRANULAR ASSEMBLIES [J].
CUNDALL, PA ;
STRACK, ODL .
GEOTECHNIQUE, 1979, 29 (01) :47-65
[8]   Measurement of the velocity field and frictional properties of wet masses in a high shear mixer [J].
Darelius, Anders ;
Lennartsson, Elin ;
Rasmuson, Anders ;
Bjorn, Ingela Niklasson ;
Folestad, Staffan .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (09) :2366-2374
[9]   Comparison of contact-force models for the simulation of collisions in DEM-based granular flow codes [J].
Di Renzo, A ;
Di Maio, FP .
CHEMICAL ENGINEERING SCIENCE, 2004, 59 (03) :525-541
[10]   An approach to simulate the motion of spherical and non-spherical fuel particles in combustion chambers [J].
Dziugys, A ;
Peters, B .
GRANULAR MATTER, 2001, 3 (04) :231-265