Analysis of particle motion in a paddle mixer using Discrete Element Method (DEM)

被引:76
作者
Hassanpour, Ali [1 ]
Tan, Hongsing [2 ]
Bayly, Andrew [2 ]
Gopalkrishnan, Prasad [3 ]
Ng, Boonho [2 ]
Ghadiri, Mojtaba [1 ]
机构
[1] Univ Leeds, Inst Particle Sci & Engn, Leeds, W Yorkshire, England
[2] P&G Tech Ctr Ltd, Newcastle Upon Tyne, Tyne & Wear, England
[3] P&G Co, ITC, Cincinnati, OH USA
关键词
Paddle mixer; Particle velocity field; Positron Emission Particle Tracking (PEPT); Discrete Element Method (DEM); SIMULATION; FLOW;
D O I
10.1016/j.powtec.2010.07.025
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The use of Discrete Element Method (DEM) modelling is rapidly expanding as a modelling tool to analyse particulate processes and to address technological needs in various aspects of pharmaceutical, food and detergent processing industries. Examples include estimation of parameters that are difficult to measure or quantify experimentally (e.g. internal flow fields and mixing patterns) and facilitating the scale-up of particulate processes from laboratory to pilot plant. This article compares DEM simulations of particle flow in a paddle mixer to experimental measurements using Positron Emission Particle Tracking (PEPT). Good qualitative agreement is shown between DEM and PEPT in terms of flow patterns inside the mixer. Quantitative comparison of PEPT measurements and DEM analyses shows reasonable agreement in terms of velocity distribution. In general, the DEM is shown to be capable of predicting the dynamics of the particulate flow inside the mixer. (c) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:189 / 194
页数:6
相关论文
共 11 条
[1]   FUNDAMENTAL POWDER MIXING MECHANISMS [J].
BRIDGWATER, J .
POWDER TECHNOLOGY, 1976, 15 (02) :215-236
[2]   DISCRETE NUMERICAL-MODEL FOR GRANULAR ASSEMBLIES [J].
CUNDALL, PA ;
STRACK, ODL .
GEOTECHNIQUE, 1979, 29 (01) :47-65
[3]   Effect of granulation scale-up on the strength of granules [J].
Hassanpour, A. ;
Kwan, C. C. ;
Ng, B. H. ;
Rahmanian, N. ;
Ding, Y. L. ;
Antony, S. J. ;
Jia, X. D. ;
Ghadiri, M. .
POWDER TECHNOLOGY, 2009, 189 (02) :304-312
[4]   Motion in a particle bed agitated by a single blade [J].
Laurent, BFC ;
Bridgewater, J ;
Parker, DJ .
AICHE JOURNAL, 2000, 46 (09) :1723-1734
[5]   PARTICLE FLOW PATTERNS IN A MECHANICALLY STIRRED 2-DIMENSIONAL CYLINDRICAL [J].
MALHOTRA, K ;
MUJUMDAR, AS ;
OKAZAKI, M .
POWDER TECHNOLOGY, 1990, 60 (02) :179-189
[6]   Solids motion in a conical frustum-shaped high shear mixer granulator [J].
Ng, B. H. ;
Kwan, C. C. ;
Ding, Y. L. ;
Ghadiri, M. ;
Fan, X. F. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (03) :756-765
[7]   Positron emission particle tracking using the new Birmingham positron camera [J].
Parker, DJ ;
Forster, RN ;
Fowles, P ;
Takhar, PS .
NUCLEAR INSTRUMENTS & METHODS IN PHYSICS RESEARCH SECTION A-ACCELERATORS SPECTROMETERS DETECTORS AND ASSOCIATED EQUIPMENT, 2002, 477 (1-3) :540-545
[8]   Characterization of continuous convective powder mixing processes [J].
Portillo, Patricia M. ;
Ierapetritou, Marianthi G. ;
Muzzio, Fernando J. .
POWDER TECHNOLOGY, 2008, 182 (03) :368-378
[9]   Simulation of a continuous granular mixer: Effect of operating conditions on flow and mixing [J].
Sarkar, Avik ;
Wassgren, Carl R. .
CHEMICAL ENGINEERING SCIENCE, 2009, 64 (11) :2672-2682
[10]   Numerical analysis of agitation torque and particle motion in a high shear mixer [J].
Sato, Yoshinobu ;
Nakamura, Hideya ;
Watano, Satoru .
POWDER TECHNOLOGY, 2008, 186 (02) :130-136